Datasets
-
Activity coefficient (12)
-
Mole fraction (42)
-
η - Viscosity, Pa*s (28)
-
σcond - Electrical conductivity, S/m (2)
-
Excess molar enthalpy (molar enthalpy (12)
-
Pvap - Vapor or sublimation pressure, kPa (10)
-
n0 - Refractive index (Na D-line) (14)
-
ρg - Mass density, kg/m3 (2)
-
ρl - Mass density, kg/m3 (54)
-
csound,fluid - Speed of Sound, m/s (10)
-
γ - Surface tension liquid-gas, N/m (6)
-
Tboil - Boiling temperature at pressure P, K (38)
-
λ - Thermal conductivity, W/m/K (4)
-
Binary diffusion coefficient, m2/s (2)
-
Vapor Liquid Equilibrium at Constant Pressure (3)
-
Vapor or sublimation pressure, kPa (8)
Activity coefficient of Ethanol (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
Temperature, K - Liquid |
Activity coefficient of Ethanol (1) - Liquid |
273.35 |
2.54 |
283.15 |
3.13 |
Activity coefficient of Ethanol (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
Temperature, K - Liquid |
Activity coefficient of Ethanol (1) - Liquid |
303.15 |
4.14 |
308.15 |
4.43 |
313.15 |
4.66 |
318.15 |
4.85 |
323.15 |
5.03 |
328.15 |
5.2 |
333.15 |
5.3 |
Activity coefficient of Ethanol (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
Temperature, K - Liquid |
Activity coefficient of Ethanol (1) - Liquid |
358.15 |
5.9 |
363.15 |
6.0 |
368.15 |
6.1 |
372.15 |
6.2 |
Activity coefficient of Ethanol (1)
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Mole fraction = 0 (Liquid)
Temperature, K - Liquid |
Activity coefficient of Ethanol (1) - Liquid |
323.15 |
5.17 |
333.15 |
4.77 |
343.15 |
4.37 |
353.15 |
4.11 |
Activity coefficient of Ethanol (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Ethanol (1) - Liquid |
Activity coefficient of Ethanol (1) - Liquid |
298.15 |
101.33 |
0.0000 |
3.77 |
Activity coefficient of Ethanol (1)
[ref]
Operational conditions:
- Pressure, kPa = 101.325 (Liquid)
- Mole fraction = 0 (Liquid)
Temperature, K - Liquid |
Activity coefficient of Ethanol (1) - Liquid |
303.25 |
5.03 |
313.25 |
5.33 |
323.25 |
5.54 |
333.25 |
5.76 |
343.25 |
5.96 |
Activity coefficient of Ethanol (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
Temperature, K - Liquid |
Activity coefficient of Ethanol (1) - Liquid |
273.35 |
2.54 |
283.15 |
3.13 |
Activity coefficient of Ethanol (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
Temperature, K - Liquid |
Activity coefficient of Ethanol (1) - Liquid |
303.15 |
4.14 |
308.15 |
4.43 |
313.15 |
4.66 |
318.15 |
4.85 |
323.15 |
5.03 |
328.15 |
5.2 |
333.15 |
5.3 |
Activity coefficient of Ethanol (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
Temperature, K - Liquid |
Activity coefficient of Ethanol (1) - Liquid |
358.15 |
5.9 |
363.15 |
6.0 |
368.15 |
6.1 |
372.15 |
6.2 |
Activity coefficient of Ethanol (1)
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Mole fraction = 0 (Liquid)
Temperature, K - Liquid |
Activity coefficient of Ethanol (1) - Liquid |
323.15 |
5.17 |
333.15 |
4.77 |
343.15 |
4.37 |
353.15 |
4.11 |
Activity coefficient of Ethanol (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Ethanol (1) - Liquid |
Activity coefficient of Ethanol (1) - Liquid |
298.15 |
101.33 |
0.0000 |
3.77 |
Activity coefficient of Ethanol (1)
[ref]
Operational conditions:
- Pressure, kPa = 101.325 (Liquid)
- Mole fraction = 0 (Liquid)
Temperature, K - Liquid |
Activity coefficient of Ethanol (1) - Liquid |
303.25 |
5.03 |
313.25 |
5.33 |
323.25 |
5.54 |
333.25 |
5.76 |
343.25 |
5.96 |
Mole fraction of Ethanol (1)
[ref]
Fixed |
Measured |
Mole fraction of Ethanol (1) - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Ethanol (1) - Gas |
0.0630 |
32.86 |
0.3560 |
0.0760 |
19.71 |
0.4070 |
0.1040 |
32.86 |
0.4630 |
0.1170 |
13.15 |
0.4610 |
0.1410 |
19.71 |
0.5100 |
0.1500 |
32.86 |
0.4940 |
0.2410 |
13.15 |
0.5670 |
0.2480 |
32.86 |
0.5560 |
0.2600 |
19.71 |
0.5920 |
0.3830 |
13.15 |
0.6320 |
0.3900 |
19.71 |
0.6320 |
0.4540 |
32.86 |
0.6620 |
0.4920 |
13.15 |
0.6680 |
0.4990 |
19.71 |
0.6790 |
0.5810 |
32.86 |
0.6960 |
0.5900 |
13.15 |
0.7140 |
0.5990 |
19.71 |
0.7060 |
0.6560 |
13.15 |
0.7370 |
0.6570 |
32.86 |
0.7320 |
0.6880 |
19.71 |
0.7600 |
0.7600 |
32.86 |
0.7920 |
0.7710 |
13.15 |
0.8120 |
0.7990 |
19.71 |
0.8260 |
0.8050 |
19.71 |
0.8280 |
0.8390 |
32.86 |
0.8500 |
0.8400 |
13.15 |
0.8550 |
0.8410 |
19.71 |
0.8540 |
0.8540 |
32.86 |
0.8680 |
0.8640 |
13.15 |
0.8740 |
0.8830 |
19.71 |
0.8880 |
0.8970 |
13.15 |
0.9040 |
0.9080 |
13.15 |
0.9100 |
0.9110 |
13.15 |
0.9140 |
0.9130 |
19.71 |
0.9150 |
0.9130 |
32.86 |
0.9130 |
0.9310 |
19.71 |
0.9320 |
0.9310 |
32.86 |
0.9310 |
0.9320 |
32.86 |
0.9340 |
0.9340 |
13.15 |
0.9340 |
0.9450 |
19.71 |
0.9450 |
0.9470 |
13.15 |
0.9470 |
0.9600 |
19.71 |
0.9570 |
0.9640 |
19.71 |
0.9640 |
0.9650 |
32.86 |
0.9630 |
0.9710 |
13.15 |
0.9690 |
Mole fraction of Ethanol (1)
[ref]
Fixed |
Measured |
Mole fraction of Ethanol (1) - Liquid |
Temperature, K - Liquid |
Mole fraction of Ethanol (1) - Gas |
0.0000 |
353.15 |
0.0000 |
0.0511 |
353.15 |
0.3845 |
0.0986 |
353.15 |
0.4937 |
0.1999 |
353.15 |
0.5535 |
0.2986 |
353.15 |
0.6025 |
0.3978 |
353.15 |
0.6304 |
0.4984 |
353.15 |
0.6776 |
0.5982 |
353.15 |
0.7217 |
0.6975 |
353.15 |
0.7643 |
0.8045 |
353.15 |
0.8231 |
0.9119 |
353.15 |
0.9033 |
1.0000 |
353.15 |
1.0000 |
0.0000 |
363.15 |
0.0000 |
0.0501 |
363.15 |
0.2856 |
0.0988 |
363.15 |
0.4168 |
0.1990 |
363.15 |
0.5324 |
0.2996 |
363.15 |
0.5880 |
0.3989 |
363.15 |
0.6379 |
0.5050 |
363.15 |
0.6838 |
0.6005 |
363.15 |
0.7219 |
0.6994 |
363.15 |
0.7680 |
0.8193 |
363.15 |
0.8330 |
0.8984 |
363.15 |
0.8913 |
1.0000 |
363.15 |
1.0000 |
Mole fraction of Ethanol (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Gas |
Mole fraction of Ethanol (1) - Liquid |
423.20 |
808.20 |
0.1803 |
423.20 |
826.70 |
0.2290 |
423.20 |
823.30 |
0.2292 |
423.20 |
828.80 |
0.2296 |
423.20 |
836.30 |
0.2505 |
423.20 |
861.00 |
0.3141 |
423.20 |
862.40 |
0.3150 |
423.20 |
873.70 |
0.3399 |
423.20 |
886.70 |
0.3702 |
423.20 |
886.40 |
0.3712 |
423.20 |
890.10 |
0.3941 |
423.20 |
918.30 |
0.4564 |
423.20 |
919.00 |
0.4598 |
423.20 |
923.10 |
0.4910 |
423.20 |
923.80 |
0.4913 |
423.20 |
967.40 |
0.9983 |
363.30 |
125.70 |
0.1601 |
363.30 |
137.50 |
0.2791 |
363.30 |
143.30 |
0.3696 |
363.30 |
144.40 |
0.3963 |
363.30 |
144.00 |
0.3993 |
363.30 |
144.40 |
0.4223 |
363.30 |
146.00 |
0.4261 |
363.30 |
147.80 |
0.4722 |
363.30 |
155.40 |
0.6363 |
363.30 |
156.10 |
0.7085 |
363.30 |
158.90 |
0.7923 |
363.30 |
157.60 |
0.9973 |
381.40 |
156.10 |
0.0172 |
381.40 |
183.00 |
0.0430 |
381.40 |
192.70 |
0.0563 |
381.40 |
234.80 |
0.1592 |
381.40 |
252.00 |
0.2643 |
381.40 |
256.10 |
0.2894 |
381.40 |
265.80 |
0.3585 |
381.40 |
265.80 |
0.3618 |
381.40 |
269.90 |
0.4173 |
381.40 |
271.10 |
0.4215 |
381.40 |
270.40 |
0.4256 |
381.40 |
271.50 |
0.4271 |
381.40 |
271.60 |
0.4367 |
381.40 |
273.50 |
0.4371 |
381.40 |
274.00 |
0.4404 |
381.40 |
275.00 |
0.4535 |
381.40 |
275.20 |
0.4587 |
381.40 |
276.10 |
0.4771 |
381.40 |
279.90 |
0.4974 |
381.40 |
280.60 |
0.5015 |
381.40 |
282.70 |
0.5333 |
381.40 |
283.00 |
0.5389 |
381.40 |
287.80 |
0.6382 |
381.40 |
290.60 |
0.7099 |
381.40 |
295.40 |
0.7938 |
381.40 |
288.40 |
0.9967 |
403.50 |
361.50 |
0.0431 |
403.50 |
453.10 |
0.1450 |
403.50 |
501.90 |
0.2971 |
403.50 |
521.80 |
0.3778 |
403.50 |
532.20 |
0.4679 |
403.50 |
563.10 |
0.6380 |
403.50 |
566.50 |
0.7067 |
403.50 |
576.10 |
0.7953 |
403.50 |
536.00 |
0.9991 |
423.70 |
532.80 |
0.0137 |
423.70 |
582.50 |
0.0256 |
423.70 |
622.90 |
0.0415 |
423.70 |
629.70 |
0.0427 |
423.70 |
760.80 |
0.1204 |
423.70 |
845.90 |
0.2507 |
423.70 |
855.00 |
0.2825 |
423.70 |
898.70 |
0.3926 |
423.70 |
948.80 |
0.5669 |
423.70 |
964.60 |
0.6417 |
423.70 |
972.10 |
0.7094 |
423.70 |
987.90 |
0.7947 |
423.70 |
986.30 |
0.9980 |
Mole fraction of Ethanol (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Gas |
Mole fraction of Ethanol (1) - Gas |
423.20 |
808.20 |
0.4490 |
423.20 |
826.70 |
0.4867 |
423.20 |
823.30 |
0.4704 |
423.20 |
828.80 |
0.4919 |
423.20 |
836.30 |
0.4799 |
423.20 |
861.00 |
0.5252 |
423.20 |
862.40 |
0.5250 |
423.20 |
873.70 |
0.5301 |
423.20 |
886.70 |
0.5453 |
423.20 |
886.40 |
0.5457 |
423.20 |
890.10 |
0.5572 |
423.20 |
918.30 |
0.5952 |
423.20 |
919.00 |
0.5947 |
423.20 |
923.10 |
0.6068 |
423.20 |
923.80 |
0.6063 |
423.20 |
967.40 |
0.9993 |
363.30 |
125.70 |
0.4717 |
363.30 |
137.50 |
0.5328 |
363.30 |
143.30 |
0.5810 |
363.30 |
144.40 |
0.5787 |
363.30 |
144.00 |
0.5784 |
363.30 |
144.40 |
0.5971 |
363.30 |
146.00 |
0.6157 |
363.30 |
147.80 |
0.6061 |
363.30 |
155.40 |
0.7076 |
363.30 |
156.10 |
0.7468 |
363.30 |
158.90 |
0.8101 |
363.30 |
157.60 |
0.9971 |
381.40 |
156.10 |
0.1495 |
381.40 |
183.00 |
0.2713 |
381.40 |
192.70 |
0.3314 |
381.40 |
234.80 |
0.4736 |
381.40 |
252.00 |
0.5375 |
381.40 |
256.10 |
0.5610 |
381.40 |
265.80 |
0.5664 |
381.40 |
265.80 |
0.5687 |
381.40 |
269.90 |
0.5925 |
381.40 |
271.10 |
0.5886 |
381.40 |
270.40 |
0.5979 |
381.40 |
271.50 |
0.5979 |
381.40 |
271.60 |
0.5977 |
381.40 |
273.50 |
0.6017 |
381.40 |
274.00 |
0.6092 |
381.40 |
275.00 |
0.6144 |
381.40 |
275.20 |
0.6198 |
381.40 |
276.10 |
0.6119 |
381.40 |
279.90 |
0.6294 |
381.40 |
280.60 |
0.6312 |
381.40 |
282.70 |
0.6526 |
381.40 |
283.00 |
0.6491 |
381.40 |
287.80 |
0.7024 |
381.40 |
290.60 |
0.7371 |
381.40 |
295.40 |
0.8089 |
381.40 |
288.40 |
0.9977 |
403.50 |
361.50 |
0.2594 |
403.50 |
453.10 |
0.4336 |
403.50 |
501.90 |
0.5298 |
403.50 |
521.80 |
0.5628 |
403.50 |
532.20 |
0.6041 |
403.50 |
563.10 |
0.7010 |
403.50 |
566.50 |
0.7404 |
403.50 |
576.10 |
0.8059 |
403.50 |
536.00 |
0.9994 |
423.70 |
532.80 |
0.1100 |
423.70 |
582.50 |
0.2017 |
423.70 |
622.90 |
0.2390 |
423.70 |
629.70 |
0.2587 |
423.70 |
760.80 |
0.4009 |
423.70 |
845.90 |
0.4881 |
423.70 |
855.00 |
0.4975 |
423.70 |
898.70 |
0.5603 |
423.70 |
948.80 |
0.6430 |
423.70 |
964.60 |
0.6960 |
423.70 |
972.10 |
0.7390 |
423.70 |
987.90 |
0.8071 |
423.70 |
986.30 |
0.9981 |
Mole fraction of Ethanol (1)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Mole fraction of Ethanol (1) - Gas |
0.6830 |
0.7420 |
0.7380 |
0.7750 |
0.7820 |
0.8010 |
0.8370 |
0.8430 |
0.8810 |
0.8810 |
0.9430 |
0.9370 |
0.9600 |
0.9540 |
Mole fraction of Ethanol (1)
[ref]
Operational condition: Pressure, kPa =
101.32 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Mole fraction of Ethanol (1) - Gas |
0.0000 |
0.0000 |
0.0180 |
0.1650 |
0.0280 |
0.2210 |
0.0510 |
0.3210 |
0.0810 |
0.4030 |
0.1250 |
0.4740 |
0.1690 |
0.5130 |
0.2280 |
0.5510 |
0.3350 |
0.6090 |
0.4740 |
0.6460 |
0.5560 |
0.6830 |
0.6640 |
0.7320 |
0.7560 |
0.7920 |
0.8930 |
0.8920 |
0.9220 |
0.9110 |
0.9610 |
0.9540 |
1.0000 |
1.0000 |
Mole fraction of Ethanol (1)
[ref]
Operational condition: Temperature, K =
393.15 (Gas)
Mole fraction of Ethanol (1) - Liquid |
Mole fraction of Ethanol (1) - Gas |
0.0000 |
0.0000 |
0.0120 |
0.1190 |
0.0160 |
0.1480 |
0.0350 |
0.2430 |
0.0460 |
0.2920 |
0.0600 |
0.3250 |
0.0750 |
0.3730 |
0.1010 |
0.4070 |
0.2030 |
0.4840 |
0.3090 |
0.5460 |
0.4040 |
0.5870 |
0.5520 |
0.6560 |
0.6360 |
0.7070 |
0.7680 |
0.7820 |
0.8940 |
0.8860 |
1.0000 |
1.0000 |
Mole fraction of Ethanol (1)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Mole fraction of Ethanol (1) - Gas |
0.0000 |
0.0000 |
0.0150 |
0.1390 |
0.0350 |
0.2610 |
0.1000 |
0.4360 |
0.1830 |
0.5250 |
0.2920 |
0.5850 |
0.3940 |
0.6110 |
0.5010 |
0.6480 |
0.5430 |
0.6690 |
0.6310 |
0.7140 |
0.7490 |
0.7810 |
0.7940 |
0.8140 |
0.8480 |
0.8550 |
0.8990 |
0.8980 |
0.9490 |
0.9460 |
1.0000 |
1.0000 |
Azeotropic composition: mole fraction of Ethanol (1)
[ref]
Pressure, kPa - Liquid |
Azeotropic composition: mole fraction of Ethanol (1) - Liquid |
101.30 |
0.8910 |
Mole fraction of Ethanol (1)
[ref]
Fixed |
Measured |
Mole fraction of Ethanol (1) - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Ethanol (1) - Gas |
0.0000 |
93.79 |
0.0000 |
0.0043 |
94.19 |
0.0632 |
0.0117 |
94.06 |
0.1429 |
0.0131 |
93.79 |
0.1677 |
0.0178 |
93.93 |
0.2142 |
0.0261 |
93.93 |
0.2679 |
0.0351 |
93.93 |
0.3089 |
0.0727 |
93.79 |
0.4371 |
0.1199 |
93.73 |
0.4988 |
0.1708 |
93.73 |
0.5371 |
0.2770 |
94.26 |
0.5832 |
0.3791 |
93.99 |
0.6282 |
0.4694 |
94.13 |
0.6462 |
0.5521 |
93.66 |
0.6851 |
0.6404 |
93.93 |
0.7148 |
0.6639 |
93.99 |
0.7355 |
0.7097 |
93.93 |
0.7595 |
0.7586 |
93.59 |
0.8025 |
0.7876 |
93.99 |
0.8191 |
0.7982 |
93.66 |
0.8242 |
0.8386 |
93.86 |
0.8476 |
0.8814 |
93.73 |
0.8790 |
0.9267 |
93.79 |
0.9263 |
1.0000 |
93.33 |
1.0000 |
Mole fraction of Ethanol (1)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Mole fraction of Ethanol (1) - Gas |
0.9815 |
0.9788 |
0.9026 |
0.9087 |
0.7987 |
0.8250 |
0.7314 |
0.7780 |
0.6862 |
0.7559 |
0.6193 |
0.7146 |
0.5344 |
0.6774 |
0.4157 |
0.6287 |
0.2669 |
0.5642 |
0.1920 |
0.5379 |
0.1385 |
0.4967 |
0.0850 |
0.4328 |
0.0453 |
0.2951 |
0.0246 |
0.1487 |
0.0148 |
0.0353 |
Mole fraction of Ethanol (1)
[ref]
Operational condition: Temperature, K =
323.15 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Mole fraction of Ethanol (1) - Gas |
0.0429 |
0.2982 |
0.0654 |
0.3821 |
0.1545 |
0.5132 |
0.1825 |
0.5462 |
0.2421 |
0.5679 |
0.4081 |
0.6176 |
0.4356 |
0.6278 |
0.5049 |
0.6664 |
0.6400 |
0.7303 |
0.6527 |
0.7322 |
0.8056 |
0.8265 |
0.9006 |
0.8996 |
Henry's Law constant (mole fraction scale), kPa of Ethanol (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol (1) - Liquid |
Henry's Law constant (mole fraction scale), kPa of Ethanol (1) - Liquid |
298.15 |
0.0000 |
29.7 |
Mole fraction of Ethanol (1)
[ref]
Operational condition: Temperature, K =
313.15 (Gas)
Mole fraction of Ethanol (1) - Liquid |
Mole fraction of Ethanol (1) - Gas |
0.0000 |
0.0000 |
0.0050 |
0.0360 |
0.0070 |
0.0690 |
0.0100 |
0.0960 |
0.0140 |
0.1330 |
0.0200 |
0.1810 |
0.0260 |
0.2210 |
0.0350 |
0.2690 |
0.0500 |
0.3320 |
0.0750 |
0.4070 |
0.0850 |
0.4210 |
0.1080 |
0.4780 |
0.1110 |
0.4740 |
0.1360 |
0.5190 |
0.1580 |
0.5410 |
0.2010 |
0.5730 |
0.2560 |
0.5980 |
0.3190 |
0.6120 |
0.4180 |
0.6550 |
0.4480 |
0.6600 |
0.5180 |
0.6970 |
0.5830 |
0.7300 |
0.6820 |
0.7670 |
0.7480 |
0.8050 |
0.8280 |
0.8410 |
0.8920 |
0.8930 |
0.9430 |
0.9600 |
1.0000 |
1.0000 |
Mole fraction of Ethanol (1)
[ref]
Operational condition: Pressure, kPa =
101.32 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Mole fraction of Ethanol (1) - Gas |
0.0000 |
0.0000 |
0.0790 |
0.4070 |
0.1430 |
0.4930 |
0.1950 |
0.5300 |
0.2920 |
0.5700 |
0.3780 |
0.6020 |
0.4500 |
0.6260 |
0.4950 |
0.6570 |
0.5810 |
0.6910 |
0.6480 |
0.7210 |
0.6960 |
0.7420 |
0.7940 |
0.8070 |
0.8400 |
0.8440 |
0.8900 |
0.8930 |
1.0000 |
1.0000 |
Mole fraction of Ethanol (1)
[ref]
Operational condition: Pressure, kPa =
50.66 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Mole fraction of Ethanol (1) - Gas |
0.0082 |
0.1538 |
0.0229 |
0.2400 |
0.0298 |
0.2144 |
0.0541 |
0.3024 |
0.0621 |
0.3741 |
0.1842 |
0.5151 |
0.2529 |
0.5540 |
0.2970 |
0.5828 |
0.3594 |
0.6030 |
0.3739 |
0.6061 |
0.4730 |
0.6445 |
0.5949 |
0.6925 |
0.7017 |
0.7555 |
0.8214 |
0.8279 |
0.9313 |
0.9351 |
0.9435 |
0.9445 |
Mole fraction of Ethanol (1)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Mole fraction of Ethanol (1) - Gas |
0.0180 |
0.1800 |
0.0790 |
0.4180 |
0.0900 |
0.4410 |
0.1470 |
0.5100 |
0.2440 |
0.5670 |
0.3110 |
0.5890 |
0.3530 |
0.6040 |
0.4250 |
0.6270 |
0.4880 |
0.6520 |
0.5700 |
0.6880 |
0.6160 |
0.7130 |
0.6700 |
0.7360 |
0.7110 |
0.7600 |
0.8020 |
0.8190 |
0.8350 |
0.8440 |
0.8690 |
0.8730 |
0.9010 |
0.9000 |
0.9140 |
0.9120 |
0.9220 |
0.9200 |
0.9400 |
0.9370 |
0.9720 |
0.9690 |
Mole fraction of Ethanol (1)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Mole fraction of Ethanol (1) - Gas |
0.0000 |
0.0000 |
0.1190 |
0.5180 |
0.1540 |
0.5390 |
0.2180 |
0.5980 |
0.2690 |
0.5960 |
0.3220 |
0.6240 |
0.3570 |
0.6500 |
0.3930 |
0.6420 |
0.4250 |
0.6550 |
0.4400 |
0.6610 |
0.5570 |
0.6830 |
0.6500 |
0.7410 |
0.7590 |
0.7900 |
0.8650 |
0.8670 |
1.0000 |
1.0000 |
Mole fraction of Ethanol (1)
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Mole fraction of Ethanol (1) - Gas |
Mole fraction of Ethanol (1) - Liquid |
0.8160 |
0.7985 |
0.8552 |
0.8491 |
0.8983 |
0.9006 |
0.9175 |
0.9204 |
0.9368 |
0.9401 |
0.9563 |
0.9598 |
0.9780 |
0.9801 |
0.9894 |
0.9905 |
0.9981 |
0.9984 |
Henry's Law constant (mole fraction scale), kPa of Ethanol (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
Temperature, K - Liquid |
Henry's Law constant (mole fraction scale), kPa of Ethanol (1) - Liquid |
278.20 |
6.5 |
283.20 |
10.0 |
288.20 |
13.0 |
293.20 |
20.0 |
298.20 |
26.0 |
Mole fraction of Ethanol (1)
[ref]
Operational condition: Pressure, kPa =
100 (Gas)
Mole fraction of Ethanol (1) - Liquid |
Mole fraction of Ethanol (1) - Gas |
0.0000 |
0.0000 |
0.0017 |
0.0347 |
0.0054 |
0.0796 |
0.0137 |
0.1486 |
0.0215 |
0.2340 |
0.0381 |
0.3254 |
0.0668 |
0.4023 |
0.1033 |
0.4677 |
0.1516 |
0.5155 |
0.2144 |
0.5533 |
0.2660 |
0.5727 |
0.3142 |
0.5943 |
0.3544 |
0.6076 |
0.4030 |
0.6241 |
0.4488 |
0.6390 |
Mole fraction of Ethanol (1)
[ref]
Fixed |
Measured |
Mole fraction of Ethanol (1) - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Ethanol (1) - Gas |
0.0630 |
32.86 |
0.3560 |
0.0760 |
19.71 |
0.4070 |
0.1040 |
32.86 |
0.4630 |
0.1170 |
13.15 |
0.4610 |
0.1410 |
19.71 |
0.5100 |
0.1500 |
32.86 |
0.4940 |
0.2410 |
13.15 |
0.5670 |
0.2480 |
32.86 |
0.5560 |
0.2600 |
19.71 |
0.5920 |
0.3830 |
13.15 |
0.6320 |
0.3900 |
19.71 |
0.6320 |
0.4540 |
32.86 |
0.6620 |
0.4920 |
13.15 |
0.6680 |
0.4990 |
19.71 |
0.6790 |
0.5810 |
32.86 |
0.6960 |
0.5900 |
13.15 |
0.7140 |
0.5990 |
19.71 |
0.7060 |
0.6560 |
13.15 |
0.7370 |
0.6570 |
32.86 |
0.7320 |
0.6880 |
19.71 |
0.7600 |
0.7600 |
32.86 |
0.7920 |
0.7710 |
13.15 |
0.8120 |
0.7990 |
19.71 |
0.8260 |
0.8050 |
19.71 |
0.8280 |
0.8390 |
32.86 |
0.8500 |
0.8400 |
13.15 |
0.8550 |
0.8410 |
19.71 |
0.8540 |
0.8540 |
32.86 |
0.8680 |
0.8640 |
13.15 |
0.8740 |
0.8830 |
19.71 |
0.8880 |
0.8970 |
13.15 |
0.9040 |
0.9080 |
13.15 |
0.9100 |
0.9110 |
13.15 |
0.9140 |
0.9130 |
19.71 |
0.9150 |
0.9130 |
32.86 |
0.9130 |
0.9310 |
19.71 |
0.9320 |
0.9310 |
32.86 |
0.9310 |
0.9320 |
32.86 |
0.9340 |
0.9340 |
13.15 |
0.9340 |
0.9450 |
19.71 |
0.9450 |
0.9470 |
13.15 |
0.9470 |
0.9600 |
19.71 |
0.9570 |
0.9640 |
19.71 |
0.9640 |
0.9650 |
32.86 |
0.9630 |
0.9710 |
13.15 |
0.9690 |
Mole fraction of Ethanol (1)
[ref]
Fixed |
Measured |
Mole fraction of Ethanol (1) - Liquid |
Temperature, K - Liquid |
Mole fraction of Ethanol (1) - Gas |
0.0000 |
353.15 |
0.0000 |
0.0511 |
353.15 |
0.3845 |
0.0986 |
353.15 |
0.4937 |
0.1999 |
353.15 |
0.5535 |
0.2986 |
353.15 |
0.6025 |
0.3978 |
353.15 |
0.6304 |
0.4984 |
353.15 |
0.6776 |
0.5982 |
353.15 |
0.7217 |
0.6975 |
353.15 |
0.7643 |
0.8045 |
353.15 |
0.8231 |
0.9119 |
353.15 |
0.9033 |
1.0000 |
353.15 |
1.0000 |
0.0000 |
363.15 |
0.0000 |
0.0501 |
363.15 |
0.2856 |
0.0988 |
363.15 |
0.4168 |
0.1990 |
363.15 |
0.5324 |
0.2996 |
363.15 |
0.5880 |
0.3989 |
363.15 |
0.6379 |
0.5050 |
363.15 |
0.6838 |
0.6005 |
363.15 |
0.7219 |
0.6994 |
363.15 |
0.7680 |
0.8193 |
363.15 |
0.8330 |
0.8984 |
363.15 |
0.8913 |
1.0000 |
363.15 |
1.0000 |
Mole fraction of Ethanol (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Gas |
Mole fraction of Ethanol (1) - Liquid |
423.20 |
808.20 |
0.1803 |
423.20 |
826.70 |
0.2290 |
423.20 |
823.30 |
0.2292 |
423.20 |
828.80 |
0.2296 |
423.20 |
836.30 |
0.2505 |
423.20 |
861.00 |
0.3141 |
423.20 |
862.40 |
0.3150 |
423.20 |
873.70 |
0.3399 |
423.20 |
886.70 |
0.3702 |
423.20 |
886.40 |
0.3712 |
423.20 |
890.10 |
0.3941 |
423.20 |
918.30 |
0.4564 |
423.20 |
919.00 |
0.4598 |
423.20 |
923.10 |
0.4910 |
423.20 |
923.80 |
0.4913 |
423.20 |
967.40 |
0.9983 |
363.30 |
125.70 |
0.1601 |
363.30 |
137.50 |
0.2791 |
363.30 |
143.30 |
0.3696 |
363.30 |
144.40 |
0.3963 |
363.30 |
144.00 |
0.3993 |
363.30 |
144.40 |
0.4223 |
363.30 |
146.00 |
0.4261 |
363.30 |
147.80 |
0.4722 |
363.30 |
155.40 |
0.6363 |
363.30 |
156.10 |
0.7085 |
363.30 |
158.90 |
0.7923 |
363.30 |
157.60 |
0.9973 |
381.40 |
156.10 |
0.0172 |
381.40 |
183.00 |
0.0430 |
381.40 |
192.70 |
0.0563 |
381.40 |
234.80 |
0.1592 |
381.40 |
252.00 |
0.2643 |
381.40 |
256.10 |
0.2894 |
381.40 |
265.80 |
0.3585 |
381.40 |
265.80 |
0.3618 |
381.40 |
269.90 |
0.4173 |
381.40 |
271.10 |
0.4215 |
381.40 |
270.40 |
0.4256 |
381.40 |
271.50 |
0.4271 |
381.40 |
271.60 |
0.4367 |
381.40 |
273.50 |
0.4371 |
381.40 |
274.00 |
0.4404 |
381.40 |
275.00 |
0.4535 |
381.40 |
275.20 |
0.4587 |
381.40 |
276.10 |
0.4771 |
381.40 |
279.90 |
0.4974 |
381.40 |
280.60 |
0.5015 |
381.40 |
282.70 |
0.5333 |
381.40 |
283.00 |
0.5389 |
381.40 |
287.80 |
0.6382 |
381.40 |
290.60 |
0.7099 |
381.40 |
295.40 |
0.7938 |
381.40 |
288.40 |
0.9967 |
403.50 |
361.50 |
0.0431 |
403.50 |
453.10 |
0.1450 |
403.50 |
501.90 |
0.2971 |
403.50 |
521.80 |
0.3778 |
403.50 |
532.20 |
0.4679 |
403.50 |
563.10 |
0.6380 |
403.50 |
566.50 |
0.7067 |
403.50 |
576.10 |
0.7953 |
403.50 |
536.00 |
0.9991 |
423.70 |
532.80 |
0.0137 |
423.70 |
582.50 |
0.0256 |
423.70 |
622.90 |
0.0415 |
423.70 |
629.70 |
0.0427 |
423.70 |
760.80 |
0.1204 |
423.70 |
845.90 |
0.2507 |
423.70 |
855.00 |
0.2825 |
423.70 |
898.70 |
0.3926 |
423.70 |
948.80 |
0.5669 |
423.70 |
964.60 |
0.6417 |
423.70 |
972.10 |
0.7094 |
423.70 |
987.90 |
0.7947 |
423.70 |
986.30 |
0.9980 |
Mole fraction of Ethanol (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Gas |
Mole fraction of Ethanol (1) - Gas |
423.20 |
808.20 |
0.4490 |
423.20 |
826.70 |
0.4867 |
423.20 |
823.30 |
0.4704 |
423.20 |
828.80 |
0.4919 |
423.20 |
836.30 |
0.4799 |
423.20 |
861.00 |
0.5252 |
423.20 |
862.40 |
0.5250 |
423.20 |
873.70 |
0.5301 |
423.20 |
886.70 |
0.5453 |
423.20 |
886.40 |
0.5457 |
423.20 |
890.10 |
0.5572 |
423.20 |
918.30 |
0.5952 |
423.20 |
919.00 |
0.5947 |
423.20 |
923.10 |
0.6068 |
423.20 |
923.80 |
0.6063 |
423.20 |
967.40 |
0.9993 |
363.30 |
125.70 |
0.4717 |
363.30 |
137.50 |
0.5328 |
363.30 |
143.30 |
0.5810 |
363.30 |
144.40 |
0.5787 |
363.30 |
144.00 |
0.5784 |
363.30 |
144.40 |
0.5971 |
363.30 |
146.00 |
0.6157 |
363.30 |
147.80 |
0.6061 |
363.30 |
155.40 |
0.7076 |
363.30 |
156.10 |
0.7468 |
363.30 |
158.90 |
0.8101 |
363.30 |
157.60 |
0.9971 |
381.40 |
156.10 |
0.1495 |
381.40 |
183.00 |
0.2713 |
381.40 |
192.70 |
0.3314 |
381.40 |
234.80 |
0.4736 |
381.40 |
252.00 |
0.5375 |
381.40 |
256.10 |
0.5610 |
381.40 |
265.80 |
0.5664 |
381.40 |
265.80 |
0.5687 |
381.40 |
269.90 |
0.5925 |
381.40 |
271.10 |
0.5886 |
381.40 |
270.40 |
0.5979 |
381.40 |
271.50 |
0.5979 |
381.40 |
271.60 |
0.5977 |
381.40 |
273.50 |
0.6017 |
381.40 |
274.00 |
0.6092 |
381.40 |
275.00 |
0.6144 |
381.40 |
275.20 |
0.6198 |
381.40 |
276.10 |
0.6119 |
381.40 |
279.90 |
0.6294 |
381.40 |
280.60 |
0.6312 |
381.40 |
282.70 |
0.6526 |
381.40 |
283.00 |
0.6491 |
381.40 |
287.80 |
0.7024 |
381.40 |
290.60 |
0.7371 |
381.40 |
295.40 |
0.8089 |
381.40 |
288.40 |
0.9977 |
403.50 |
361.50 |
0.2594 |
403.50 |
453.10 |
0.4336 |
403.50 |
501.90 |
0.5298 |
403.50 |
521.80 |
0.5628 |
403.50 |
532.20 |
0.6041 |
403.50 |
563.10 |
0.7010 |
403.50 |
566.50 |
0.7404 |
403.50 |
576.10 |
0.8059 |
403.50 |
536.00 |
0.9994 |
423.70 |
532.80 |
0.1100 |
423.70 |
582.50 |
0.2017 |
423.70 |
622.90 |
0.2390 |
423.70 |
629.70 |
0.2587 |
423.70 |
760.80 |
0.4009 |
423.70 |
845.90 |
0.4881 |
423.70 |
855.00 |
0.4975 |
423.70 |
898.70 |
0.5603 |
423.70 |
948.80 |
0.6430 |
423.70 |
964.60 |
0.6960 |
423.70 |
972.10 |
0.7390 |
423.70 |
987.90 |
0.8071 |
423.70 |
986.30 |
0.9981 |
Mole fraction of Ethanol (1)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Mole fraction of Ethanol (1) - Gas |
0.6830 |
0.7420 |
0.7380 |
0.7750 |
0.7820 |
0.8010 |
0.8370 |
0.8430 |
0.8810 |
0.8810 |
0.9430 |
0.9370 |
0.9600 |
0.9540 |
Mole fraction of Ethanol (1)
[ref]
Operational condition: Pressure, kPa =
101.32 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Mole fraction of Ethanol (1) - Gas |
0.0000 |
0.0000 |
0.0180 |
0.1650 |
0.0280 |
0.2210 |
0.0510 |
0.3210 |
0.0810 |
0.4030 |
0.1250 |
0.4740 |
0.1690 |
0.5130 |
0.2280 |
0.5510 |
0.3350 |
0.6090 |
0.4740 |
0.6460 |
0.5560 |
0.6830 |
0.6640 |
0.7320 |
0.7560 |
0.7920 |
0.8930 |
0.8920 |
0.9220 |
0.9110 |
0.9610 |
0.9540 |
1.0000 |
1.0000 |
Mole fraction of Ethanol (1)
[ref]
Operational condition: Temperature, K =
393.15 (Gas)
Mole fraction of Ethanol (1) - Liquid |
Mole fraction of Ethanol (1) - Gas |
0.0000 |
0.0000 |
0.0120 |
0.1190 |
0.0160 |
0.1480 |
0.0350 |
0.2430 |
0.0460 |
0.2920 |
0.0600 |
0.3250 |
0.0750 |
0.3730 |
0.1010 |
0.4070 |
0.2030 |
0.4840 |
0.3090 |
0.5460 |
0.4040 |
0.5870 |
0.5520 |
0.6560 |
0.6360 |
0.7070 |
0.7680 |
0.7820 |
0.8940 |
0.8860 |
1.0000 |
1.0000 |
Mole fraction of Ethanol (1)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Mole fraction of Ethanol (1) - Gas |
0.0000 |
0.0000 |
0.0150 |
0.1390 |
0.0350 |
0.2610 |
0.1000 |
0.4360 |
0.1830 |
0.5250 |
0.2920 |
0.5850 |
0.3940 |
0.6110 |
0.5010 |
0.6480 |
0.5430 |
0.6690 |
0.6310 |
0.7140 |
0.7490 |
0.7810 |
0.7940 |
0.8140 |
0.8480 |
0.8550 |
0.8990 |
0.8980 |
0.9490 |
0.9460 |
1.0000 |
1.0000 |
Azeotropic composition: mole fraction of Ethanol (1)
[ref]
Pressure, kPa - Liquid |
Azeotropic composition: mole fraction of Ethanol (1) - Liquid |
101.30 |
0.8910 |
Mole fraction of Ethanol (1)
[ref]
Fixed |
Measured |
Mole fraction of Ethanol (1) - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Ethanol (1) - Gas |
0.0000 |
93.79 |
0.0000 |
0.0043 |
94.19 |
0.0632 |
0.0117 |
94.06 |
0.1429 |
0.0131 |
93.79 |
0.1677 |
0.0178 |
93.93 |
0.2142 |
0.0261 |
93.93 |
0.2679 |
0.0351 |
93.93 |
0.3089 |
0.0727 |
93.79 |
0.4371 |
0.1199 |
93.73 |
0.4988 |
0.1708 |
93.73 |
0.5371 |
0.2770 |
94.26 |
0.5832 |
0.3791 |
93.99 |
0.6282 |
0.4694 |
94.13 |
0.6462 |
0.5521 |
93.66 |
0.6851 |
0.6404 |
93.93 |
0.7148 |
0.6639 |
93.99 |
0.7355 |
0.7097 |
93.93 |
0.7595 |
0.7586 |
93.59 |
0.8025 |
0.7876 |
93.99 |
0.8191 |
0.7982 |
93.66 |
0.8242 |
0.8386 |
93.86 |
0.8476 |
0.8814 |
93.73 |
0.8790 |
0.9267 |
93.79 |
0.9263 |
1.0000 |
93.33 |
1.0000 |
Mole fraction of Ethanol (1)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Mole fraction of Ethanol (1) - Gas |
0.9815 |
0.9788 |
0.9026 |
0.9087 |
0.7987 |
0.8250 |
0.7314 |
0.7780 |
0.6862 |
0.7559 |
0.6193 |
0.7146 |
0.5344 |
0.6774 |
0.4157 |
0.6287 |
0.2669 |
0.5642 |
0.1920 |
0.5379 |
0.1385 |
0.4967 |
0.0850 |
0.4328 |
0.0453 |
0.2951 |
0.0246 |
0.1487 |
0.0148 |
0.0353 |
Mole fraction of Ethanol (1)
[ref]
Operational condition: Temperature, K =
323.15 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Mole fraction of Ethanol (1) - Gas |
0.0429 |
0.2982 |
0.0654 |
0.3821 |
0.1545 |
0.5132 |
0.1825 |
0.5462 |
0.2421 |
0.5679 |
0.4081 |
0.6176 |
0.4356 |
0.6278 |
0.5049 |
0.6664 |
0.6400 |
0.7303 |
0.6527 |
0.7322 |
0.8056 |
0.8265 |
0.9006 |
0.8996 |
Henry's Law constant (mole fraction scale), kPa of Ethanol (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol (1) - Liquid |
Henry's Law constant (mole fraction scale), kPa of Ethanol (1) - Liquid |
298.15 |
0.0000 |
29.7 |
Mole fraction of Ethanol (1)
[ref]
Operational condition: Temperature, K =
313.15 (Gas)
Mole fraction of Ethanol (1) - Liquid |
Mole fraction of Ethanol (1) - Gas |
0.0000 |
0.0000 |
0.0050 |
0.0360 |
0.0070 |
0.0690 |
0.0100 |
0.0960 |
0.0140 |
0.1330 |
0.0200 |
0.1810 |
0.0260 |
0.2210 |
0.0350 |
0.2690 |
0.0500 |
0.3320 |
0.0750 |
0.4070 |
0.0850 |
0.4210 |
0.1080 |
0.4780 |
0.1110 |
0.4740 |
0.1360 |
0.5190 |
0.1580 |
0.5410 |
0.2010 |
0.5730 |
0.2560 |
0.5980 |
0.3190 |
0.6120 |
0.4180 |
0.6550 |
0.4480 |
0.6600 |
0.5180 |
0.6970 |
0.5830 |
0.7300 |
0.6820 |
0.7670 |
0.7480 |
0.8050 |
0.8280 |
0.8410 |
0.8920 |
0.8930 |
0.9430 |
0.9600 |
1.0000 |
1.0000 |
Mole fraction of Ethanol (1)
[ref]
Operational condition: Pressure, kPa =
101.32 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Mole fraction of Ethanol (1) - Gas |
0.0000 |
0.0000 |
0.0790 |
0.4070 |
0.1430 |
0.4930 |
0.1950 |
0.5300 |
0.2920 |
0.5700 |
0.3780 |
0.6020 |
0.4500 |
0.6260 |
0.4950 |
0.6570 |
0.5810 |
0.6910 |
0.6480 |
0.7210 |
0.6960 |
0.7420 |
0.7940 |
0.8070 |
0.8400 |
0.8440 |
0.8900 |
0.8930 |
1.0000 |
1.0000 |
Mole fraction of Ethanol (1)
[ref]
Operational condition: Pressure, kPa =
50.66 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Mole fraction of Ethanol (1) - Gas |
0.0082 |
0.1538 |
0.0229 |
0.2400 |
0.0298 |
0.2144 |
0.0541 |
0.3024 |
0.0621 |
0.3741 |
0.1842 |
0.5151 |
0.2529 |
0.5540 |
0.2970 |
0.5828 |
0.3594 |
0.6030 |
0.3739 |
0.6061 |
0.4730 |
0.6445 |
0.5949 |
0.6925 |
0.7017 |
0.7555 |
0.8214 |
0.8279 |
0.9313 |
0.9351 |
0.9435 |
0.9445 |
Mole fraction of Ethanol (1)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Mole fraction of Ethanol (1) - Gas |
0.0180 |
0.1800 |
0.0790 |
0.4180 |
0.0900 |
0.4410 |
0.1470 |
0.5100 |
0.2440 |
0.5670 |
0.3110 |
0.5890 |
0.3530 |
0.6040 |
0.4250 |
0.6270 |
0.4880 |
0.6520 |
0.5700 |
0.6880 |
0.6160 |
0.7130 |
0.6700 |
0.7360 |
0.7110 |
0.7600 |
0.8020 |
0.8190 |
0.8350 |
0.8440 |
0.8690 |
0.8730 |
0.9010 |
0.9000 |
0.9140 |
0.9120 |
0.9220 |
0.9200 |
0.9400 |
0.9370 |
0.9720 |
0.9690 |
Mole fraction of Ethanol (1)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Mole fraction of Ethanol (1) - Gas |
0.0000 |
0.0000 |
0.1190 |
0.5180 |
0.1540 |
0.5390 |
0.2180 |
0.5980 |
0.2690 |
0.5960 |
0.3220 |
0.6240 |
0.3570 |
0.6500 |
0.3930 |
0.6420 |
0.4250 |
0.6550 |
0.4400 |
0.6610 |
0.5570 |
0.6830 |
0.6500 |
0.7410 |
0.7590 |
0.7900 |
0.8650 |
0.8670 |
1.0000 |
1.0000 |
Mole fraction of Ethanol (1)
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Mole fraction of Ethanol (1) - Gas |
Mole fraction of Ethanol (1) - Liquid |
0.8160 |
0.7985 |
0.8552 |
0.8491 |
0.8983 |
0.9006 |
0.9175 |
0.9204 |
0.9368 |
0.9401 |
0.9563 |
0.9598 |
0.9780 |
0.9801 |
0.9894 |
0.9905 |
0.9981 |
0.9984 |
Henry's Law constant (mole fraction scale), kPa of Ethanol (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
Temperature, K - Liquid |
Henry's Law constant (mole fraction scale), kPa of Ethanol (1) - Liquid |
278.20 |
6.5 |
283.20 |
10.0 |
288.20 |
13.0 |
293.20 |
20.0 |
298.20 |
26.0 |
Mole fraction of Ethanol (1)
[ref]
Operational condition: Pressure, kPa =
100 (Gas)
Mole fraction of Ethanol (1) - Liquid |
Mole fraction of Ethanol (1) - Gas |
0.0000 |
0.0000 |
0.0017 |
0.0347 |
0.0054 |
0.0796 |
0.0137 |
0.1486 |
0.0215 |
0.2340 |
0.0381 |
0.3254 |
0.0668 |
0.4023 |
0.1033 |
0.4677 |
0.1516 |
0.5155 |
0.2144 |
0.5533 |
0.2660 |
0.5727 |
0.3142 |
0.5943 |
0.3544 |
0.6076 |
0.4030 |
0.6241 |
0.4488 |
0.6390 |
Viscosity, Pa*s
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Ethanol (1) - Liquid |
Viscosity, Pa*s - Liquid |
350.70 |
10000.00 |
0.1000 |
0.0005 |
350.70 |
10000.00 |
0.2000 |
0.0006 |
350.70 |
10000.00 |
0.3000 |
0.0006 |
350.70 |
10000.00 |
0.4000 |
0.0006 |
350.70 |
10000.00 |
0.6000 |
0.0006 |
350.70 |
10000.00 |
0.8000 |
0.0005 |
350.70 |
10000.00 |
1.0000 |
0.0005 |
350.70 |
20000.00 |
0.1000 |
0.0005 |
350.70 |
20000.00 |
0.2000 |
0.0006 |
350.70 |
20000.00 |
0.3000 |
0.0007 |
350.70 |
20000.00 |
0.4000 |
0.0007 |
350.70 |
20000.00 |
0.6000 |
0.0006 |
350.70 |
20000.00 |
0.8000 |
0.0006 |
350.70 |
20000.00 |
1.0000 |
0.0005 |
350.70 |
30000.00 |
0.1000 |
0.0006 |
350.70 |
30000.00 |
0.2000 |
0.0007 |
350.70 |
30000.00 |
0.3000 |
0.0007 |
350.70 |
30000.00 |
0.4000 |
0.0007 |
350.70 |
30000.00 |
0.6000 |
0.0007 |
350.70 |
30000.00 |
0.8000 |
0.0006 |
350.70 |
30000.00 |
1.0000 |
0.0006 |
350.70 |
40000.00 |
0.1000 |
0.0006 |
350.70 |
40000.00 |
0.2000 |
0.0007 |
350.70 |
40000.00 |
0.3000 |
0.0007 |
350.70 |
40000.00 |
0.4000 |
0.0007 |
350.70 |
40000.00 |
0.6000 |
0.0007 |
350.70 |
40000.00 |
0.8000 |
0.0006 |
350.70 |
40000.00 |
1.0000 |
0.0006 |
373.20 |
10000.00 |
0.1000 |
0.0004 |
373.20 |
10000.00 |
0.2000 |
0.0004 |
373.20 |
10000.00 |
0.3000 |
0.0005 |
373.20 |
10000.00 |
0.4000 |
0.0005 |
373.20 |
10000.00 |
0.6000 |
0.0004 |
373.20 |
10000.00 |
0.8000 |
0.0004 |
373.20 |
10000.00 |
1.0000 |
0.0004 |
373.20 |
20000.00 |
0.1000 |
0.0004 |
373.20 |
20000.00 |
0.2000 |
0.0004 |
373.20 |
20000.00 |
0.3000 |
0.0005 |
373.20 |
20000.00 |
0.4000 |
0.0005 |
373.20 |
20000.00 |
0.6000 |
0.0005 |
373.20 |
20000.00 |
0.8000 |
0.0004 |
373.20 |
20000.00 |
1.0000 |
0.0004 |
373.20 |
30000.00 |
0.1000 |
0.0004 |
373.20 |
30000.00 |
0.2000 |
0.0005 |
373.20 |
30000.00 |
0.3000 |
0.0005 |
373.20 |
30000.00 |
0.4000 |
0.0005 |
373.20 |
30000.00 |
0.6000 |
0.0005 |
373.20 |
30000.00 |
0.8000 |
0.0004 |
373.20 |
30000.00 |
1.0000 |
0.0004 |
373.20 |
40000.00 |
0.1000 |
0.0004 |
373.20 |
40000.00 |
0.2000 |
0.0005 |
373.20 |
40000.00 |
0.3000 |
0.0005 |
373.20 |
40000.00 |
0.4000 |
0.0005 |
373.20 |
40000.00 |
0.6000 |
0.0005 |
373.20 |
40000.00 |
0.8000 |
0.0005 |
373.20 |
40000.00 |
1.0000 |
0.0004 |
476.20 |
10000.00 |
0.1000 |
0.0001 |
476.20 |
10000.00 |
0.2000 |
0.0002 |
476.20 |
10000.00 |
0.3000 |
0.0001 |
476.20 |
10000.00 |
0.4000 |
0.0001 |
476.20 |
10000.00 |
0.6000 |
0.0001 |
476.20 |
10000.00 |
0.8000 |
0.0001 |
476.20 |
10000.00 |
1.0000 |
0.0001 |
476.20 |
20000.00 |
0.1000 |
0.0002 |
476.20 |
20000.00 |
0.2000 |
0.0002 |
476.20 |
20000.00 |
0.3000 |
0.0002 |
476.20 |
20000.00 |
0.4000 |
0.0001 |
476.20 |
20000.00 |
0.6000 |
0.0001 |
476.20 |
20000.00 |
0.8000 |
0.0001 |
476.20 |
20000.00 |
1.0000 |
0.0001 |
476.20 |
30000.00 |
0.1000 |
0.0002 |
476.20 |
30000.00 |
0.2000 |
0.0002 |
476.20 |
30000.00 |
0.3000 |
0.0002 |
476.20 |
30000.00 |
0.4000 |
0.0002 |
476.20 |
30000.00 |
0.6000 |
0.0001 |
476.20 |
30000.00 |
0.8000 |
0.0001 |
476.20 |
30000.00 |
1.0000 |
0.0001 |
476.20 |
40000.00 |
0.1000 |
0.0002 |
476.20 |
40000.00 |
0.2000 |
0.0002 |
476.20 |
40000.00 |
0.3000 |
0.0002 |
476.20 |
40000.00 |
0.4000 |
0.0002 |
476.20 |
40000.00 |
0.6000 |
0.0002 |
476.20 |
40000.00 |
0.8000 |
0.0002 |
476.20 |
40000.00 |
1.0000 |
0.0002 |
Viscosity, Pa*s
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Ethanol (1) - Liquid |
Viscosity, Pa*s - Liquid |
523.20 |
20000.00 |
0.0000 |
0.0001 |
523.20 |
20000.00 |
0.1000 |
0.0001 |
523.20 |
20000.00 |
0.2000 |
0.0001 |
523.20 |
20000.00 |
0.3000 |
0.0001 |
523.20 |
20000.00 |
0.4000 |
0.0001 |
523.20 |
20000.00 |
0.6000 |
0.0001 |
523.20 |
20000.00 |
0.8000 |
0.0001 |
523.20 |
20000.00 |
1.0000 |
0.0001 |
523.20 |
30000.00 |
0.0000 |
0.0001 |
523.20 |
30000.00 |
0.1000 |
0.0001 |
523.20 |
30000.00 |
0.2000 |
0.0001 |
523.20 |
30000.00 |
0.3000 |
0.0001 |
523.20 |
30000.00 |
0.4000 |
0.0001 |
523.20 |
30000.00 |
0.6000 |
0.0001 |
523.20 |
30000.00 |
0.8000 |
0.0001 |
523.20 |
30000.00 |
1.0000 |
0.0001 |
523.20 |
40000.00 |
0.0000 |
0.0001 |
523.20 |
40000.00 |
0.1000 |
0.0001 |
523.20 |
40000.00 |
0.2000 |
0.0001 |
523.20 |
40000.00 |
0.3000 |
0.0001 |
523.20 |
40000.00 |
0.4000 |
0.0001 |
523.20 |
40000.00 |
0.6000 |
0.0001 |
523.20 |
40000.00 |
0.8000 |
0.0001 |
523.20 |
40000.00 |
1.0000 |
0.0001 |
573.20 |
20000.00 |
0.0000 |
0.0001 |
573.20 |
20000.00 |
0.1000 |
0.0001 |
573.20 |
20000.00 |
0.2000 |
0.0001 |
573.20 |
20000.00 |
0.3000 |
0.0001 |
573.20 |
20000.00 |
0.4000 |
0.0001 |
573.20 |
20000.00 |
0.6000 |
0.0001 |
573.20 |
20000.00 |
0.8000 |
0.0001 |
573.20 |
20000.00 |
1.0000 |
0.0001 |
573.20 |
30000.00 |
0.0000 |
0.0001 |
573.20 |
30000.00 |
0.1000 |
0.0001 |
573.20 |
30000.00 |
0.2000 |
0.0001 |
573.20 |
30000.00 |
0.3000 |
0.0001 |
573.20 |
30000.00 |
0.4000 |
0.0001 |
573.20 |
30000.00 |
0.6000 |
0.0001 |
573.20 |
30000.00 |
0.8000 |
0.0001 |
573.20 |
30000.00 |
1.0000 |
0.0001 |
573.20 |
40000.00 |
0.0000 |
0.0001 |
573.20 |
40000.00 |
0.1000 |
0.0001 |
573.20 |
40000.00 |
0.2000 |
0.0001 |
573.20 |
40000.00 |
0.3000 |
0.0001 |
573.20 |
40000.00 |
0.4000 |
0.0001 |
573.20 |
40000.00 |
0.6000 |
0.0001 |
573.20 |
40000.00 |
0.8000 |
0.0001 |
573.20 |
40000.00 |
1.0000 |
0.0001 |
618.20 |
20000.00 |
0.0000 |
0.0001 |
618.20 |
20000.00 |
0.1000 |
0.0001 |
618.20 |
20000.00 |
0.2000 |
0.0000 |
618.20 |
20000.00 |
0.3000 |
0.0000 |
618.20 |
20000.00 |
0.4000 |
0.0000 |
618.20 |
20000.00 |
0.6000 |
0.0000 |
618.20 |
20000.00 |
0.8000 |
0.0000 |
618.20 |
20000.00 |
1.0000 |
0.0000 |
618.20 |
30000.00 |
0.0000 |
0.0001 |
618.20 |
30000.00 |
0.1000 |
0.0001 |
618.20 |
30000.00 |
0.2000 |
0.0001 |
618.20 |
30000.00 |
0.3000 |
0.0001 |
618.20 |
30000.00 |
0.4000 |
0.0001 |
618.20 |
30000.00 |
0.6000 |
0.0001 |
618.20 |
30000.00 |
0.8000 |
0.0001 |
618.20 |
30000.00 |
1.0000 |
0.0001 |
618.20 |
40000.00 |
0.0000 |
0.0001 |
618.20 |
40000.00 |
0.1000 |
0.0001 |
618.20 |
40000.00 |
0.2000 |
0.0001 |
618.20 |
40000.00 |
0.3000 |
0.0001 |
618.20 |
40000.00 |
0.4000 |
0.0001 |
618.20 |
40000.00 |
0.6000 |
0.0001 |
618.20 |
40000.00 |
0.8000 |
0.0001 |
618.20 |
40000.00 |
1.0000 |
0.0001 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Water (2) - Liquid |
Viscosity, Pa*s - Liquid |
293.15 |
0.0000 |
0.0012 |
293.15 |
0.0501 |
0.0013 |
293.15 |
0.0986 |
0.0014 |
293.15 |
0.1961 |
0.0015 |
293.15 |
0.2961 |
0.0017 |
293.15 |
0.3991 |
0.0020 |
293.15 |
0.4971 |
0.0022 |
293.15 |
0.5989 |
0.0025 |
293.15 |
0.6991 |
0.0027 |
293.15 |
0.8001 |
0.0027 |
293.15 |
0.8996 |
0.0022 |
293.15 |
0.9499 |
0.0016 |
293.15 |
1.0000 |
0.0010 |
298.15 |
0.0000 |
0.0011 |
298.15 |
0.0501 |
0.0012 |
298.15 |
0.0986 |
0.0012 |
298.15 |
0.1961 |
0.0014 |
298.15 |
0.2961 |
0.0015 |
298.15 |
0.3991 |
0.0017 |
298.15 |
0.5989 |
0.0021 |
298.15 |
0.6991 |
0.0023 |
298.15 |
0.8001 |
0.0023 |
298.15 |
0.8996 |
0.0019 |
298.15 |
0.9499 |
0.0014 |
298.15 |
1.0000 |
0.0009 |
303.15 |
0.0000 |
0.0010 |
303.15 |
0.0501 |
0.0010 |
303.15 |
0.0986 |
0.0011 |
303.15 |
0.1961 |
0.0012 |
303.15 |
0.2961 |
0.0014 |
303.15 |
0.3991 |
0.0015 |
303.15 |
0.5989 |
0.0018 |
303.15 |
0.6991 |
0.0019 |
303.15 |
0.8001 |
0.0019 |
303.15 |
0.8996 |
0.0016 |
303.15 |
0.9499 |
0.0012 |
303.15 |
1.0000 |
0.0008 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
92.3 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol (1) - Liquid |
Viscosity, Pa*s - Liquid |
293.15 |
0.0201 |
0.0012 |
293.15 |
0.0408 |
0.0015 |
293.15 |
0.0497 |
0.0016 |
293.15 |
0.0600 |
0.0018 |
293.15 |
0.0796 |
0.0020 |
293.15 |
0.1004 |
0.0023 |
293.15 |
0.1499 |
0.0027 |
293.15 |
0.1984 |
0.0029 |
293.15 |
0.2499 |
0.0029 |
293.15 |
0.3016 |
0.0028 |
293.15 |
0.3499 |
0.0027 |
293.15 |
0.3990 |
0.0026 |
293.15 |
0.4495 |
0.0024 |
293.15 |
0.4989 |
0.0023 |
293.15 |
0.5495 |
0.0022 |
293.15 |
0.6067 |
0.0020 |
293.15 |
0.6503 |
0.0019 |
293.15 |
0.6956 |
0.0018 |
293.15 |
0.7500 |
0.0017 |
293.15 |
0.7843 |
0.0016 |
293.15 |
0.8475 |
0.0015 |
293.15 |
0.8864 |
0.0014 |
293.15 |
0.9290 |
0.0013 |
298.15 |
0.0201 |
0.0011 |
298.15 |
0.0408 |
0.0013 |
298.15 |
0.0497 |
0.0014 |
298.15 |
0.0600 |
0.0016 |
298.15 |
0.0796 |
0.0017 |
298.15 |
0.1004 |
0.0019 |
298.15 |
0.1499 |
0.0022 |
298.15 |
0.1984 |
0.0024 |
298.15 |
0.2499 |
0.0024 |
298.15 |
0.3016 |
0.0023 |
298.15 |
0.3499 |
0.0023 |
298.15 |
0.3990 |
0.0022 |
298.15 |
0.4495 |
0.0021 |
298.15 |
0.4989 |
0.0020 |
298.15 |
0.5495 |
0.0019 |
298.15 |
0.6067 |
0.0017 |
298.15 |
0.6503 |
0.0017 |
298.15 |
0.6956 |
0.0016 |
298.15 |
0.7500 |
0.0015 |
298.15 |
0.7843 |
0.0014 |
298.15 |
0.8475 |
0.0013 |
298.15 |
0.8864 |
0.0013 |
298.15 |
0.9290 |
0.0012 |
303.15 |
0.0201 |
0.0010 |
303.15 |
0.0408 |
0.0012 |
303.15 |
0.0497 |
0.0012 |
303.15 |
0.0600 |
0.0013 |
303.15 |
0.0796 |
0.0015 |
303.15 |
0.1004 |
0.0017 |
303.15 |
0.1499 |
0.0019 |
303.15 |
0.1984 |
0.0020 |
303.15 |
0.2499 |
0.0020 |
303.15 |
0.3016 |
0.0020 |
303.15 |
0.3499 |
0.0019 |
303.15 |
0.3990 |
0.0019 |
303.15 |
0.4495 |
0.0018 |
303.15 |
0.4989 |
0.0017 |
303.15 |
0.5495 |
0.0016 |
303.15 |
0.6067 |
0.0015 |
303.15 |
0.6503 |
0.0015 |
303.15 |
0.6956 |
0.0014 |
303.15 |
0.7500 |
0.0013 |
303.15 |
0.7843 |
0.0013 |
303.15 |
0.8475 |
0.0012 |
303.15 |
0.8864 |
0.0011 |
303.15 |
0.9290 |
0.0011 |
308.15 |
0.0201 |
0.0009 |
308.15 |
0.0408 |
0.0010 |
308.15 |
0.0497 |
0.0011 |
308.15 |
0.0600 |
0.0012 |
308.15 |
0.0796 |
0.0013 |
308.15 |
0.1004 |
0.0014 |
308.15 |
0.1499 |
0.0016 |
308.15 |
0.1984 |
0.0017 |
308.15 |
0.2499 |
0.0017 |
308.15 |
0.3016 |
0.0017 |
308.15 |
0.3499 |
0.0017 |
308.15 |
0.3990 |
0.0016 |
308.15 |
0.4495 |
0.0015 |
308.15 |
0.4989 |
0.0015 |
308.15 |
0.5495 |
0.0014 |
308.15 |
0.6067 |
0.0013 |
308.15 |
0.6503 |
0.0013 |
308.15 |
0.6956 |
0.0012 |
308.15 |
0.7500 |
0.0012 |
308.15 |
0.7843 |
0.0011 |
308.15 |
0.8475 |
0.0011 |
308.15 |
0.8864 |
0.0010 |
308.15 |
0.9290 |
0.0010 |
293.15 |
0.0000 |
0.0011 |
298.15 |
0.0000 |
0.0009 |
303.15 |
0.0000 |
0.0008 |
308.15 |
0.0000 |
0.0008 |
293.15 |
1.0000 |
0.0012 |
298.15 |
1.0000 |
0.0011 |
303.15 |
1.0000 |
0.0010 |
308.15 |
1.0000 |
0.0009 |
Viscosity, Pa*s
[ref]
Operational conditions:
- Pressure, kPa = 100 (Liquid)
- Molality, mol/kg = 16 (Liquid)
Temperature, K - Liquid |
Viscosity, Pa*s - Liquid |
298.15 |
0.0024 |
303.15 |
0.0020 |
Viscosity, Pa*s
[ref]
Operational conditions:
- Temperature, K = 298.2 (Liquid)
- Pressure, kPa = 100 (Liquid)
Mass fraction of Water (2) - Liquid |
Viscosity, Pa*s - Liquid |
0.5080 |
0.0022 |
0.4260 |
0.0022 |
0.3110 |
0.0018 |
0.2470 |
0.0018 |
0.2350 |
0.0017 |
0.2060 |
0.0017 |
Viscosity, Pa*s
[ref]
Operational conditions:
- Temperature, K = 298.2 (Liquid)
- Pressure, kPa = 100 (Liquid)
Mass fraction of Water (2) - Liquid |
Viscosity, Pa*s - Liquid |
0.0610 |
0.0013 |
0.1240 |
0.0015 |
0.1720 |
0.0016 |
0.2330 |
0.0018 |
0.2760 |
0.0019 |
0.3400 |
0.0019 |
0.4100 |
0.0022 |
0.5000 |
0.0023 |
0.6200 |
0.0023 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Volume fraction of Ethanol (1) - Liquid |
Viscosity, Pa*s - Liquid |
303.15 |
0.1000 |
0.0007 |
303.15 |
0.2000 |
0.0010 |
303.15 |
0.3000 |
0.0012 |
303.15 |
0.4000 |
0.0013 |
303.15 |
0.5000 |
0.0014 |
308.15 |
0.1000 |
0.0006 |
308.15 |
0.2000 |
0.0009 |
308.15 |
0.3000 |
0.0009 |
308.15 |
0.4000 |
0.0011 |
308.15 |
0.5000 |
0.0012 |
313.15 |
0.1000 |
0.0006 |
313.15 |
0.2000 |
0.0007 |
313.15 |
0.3000 |
0.0009 |
313.15 |
0.4000 |
0.0009 |
313.15 |
0.5000 |
0.0011 |
318.15 |
0.1000 |
0.0006 |
318.15 |
0.2000 |
0.0006 |
318.15 |
0.3000 |
0.0008 |
318.15 |
0.4000 |
0.0009 |
318.15 |
0.5000 |
0.0009 |
318.15 |
0.3000 |
0.0008 |
323.15 |
0.1000 |
0.0005 |
323.15 |
0.2000 |
0.0006 |
323.15 |
0.3000 |
0.0007 |
323.15 |
0.4000 |
0.0007 |
323.15 |
0.5000 |
0.0008 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Molality, mol/kg of Ethanol (1) - Liquid |
Viscosity, Pa*s - Liquid |
293.15 |
14.0 |
0.0029 |
298.15 |
14.0 |
0.0024 |
303.15 |
14.0 |
0.0020 |
308.15 |
14.0 |
0.0017 |
313.15 |
14.0 |
0.0014 |
293.15 |
16.0 |
0.0029 |
298.15 |
16.0 |
0.0024 |
303.15 |
16.0 |
0.0020 |
308.15 |
16.0 |
0.0017 |
313.15 |
16.0 |
0.0015 |
293.15 |
18.0 |
0.0029 |
298.15 |
18.0 |
0.0024 |
303.15 |
18.0 |
0.0020 |
308.15 |
18.0 |
0.0017 |
313.15 |
18.0 |
0.0015 |
293.15 |
20.0 |
0.0029 |
298.15 |
20.0 |
0.0024 |
303.15 |
20.0 |
0.0020 |
308.15 |
20.0 |
0.0017 |
313.15 |
20.0 |
0.0015 |
293.15 |
22.0 |
0.0029 |
298.15 |
22.0 |
0.0024 |
303.15 |
22.0 |
0.0020 |
308.15 |
22.0 |
0.0017 |
313.15 |
22.0 |
0.0015 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Water (2) - Liquid |
Viscosity, Pa*s - Liquid |
298.15 |
0.2009 |
0.0014 |
298.15 |
0.3001 |
0.0016 |
298.15 |
0.4016 |
0.0018 |
298.15 |
0.5001 |
0.0019 |
298.15 |
0.6000 |
0.0022 |
298.15 |
0.7000 |
0.0023 |
298.15 |
0.8000 |
0.0024 |
298.15 |
0.9000 |
0.0019 |
318.15 |
0.1000 |
0.0008 |
318.15 |
0.2000 |
0.0010 |
318.15 |
0.3001 |
0.0010 |
318.15 |
0.4036 |
0.0011 |
318.15 |
0.5002 |
0.0012 |
318.15 |
0.6000 |
0.0012 |
318.15 |
0.7000 |
0.0013 |
318.15 |
0.8007 |
0.0013 |
318.15 |
0.9000 |
0.0010 |
Viscosity, Pa*s
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Mole fraction of Water (2) - Liquid |
Viscosity, Pa*s - Liquid |
0.0480 |
0.0012 |
0.1116 |
0.0013 |
0.1599 |
0.0013 |
0.1761 |
0.0014 |
0.2668 |
0.0015 |
0.3010 |
0.0016 |
0.3994 |
0.0017 |
0.4970 |
0.0019 |
0.6122 |
0.0022 |
0.7116 |
0.0024 |
0.7774 |
0.0024 |
0.8145 |
0.0024 |
0.8529 |
0.0022 |
0.8967 |
0.0019 |
0.9481 |
0.0014 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Mole fraction of Water (2) - Liquid |
Temperature, K - Liquid |
Viscosity, Pa*s - Liquid |
0.1000 |
268.10 |
0.0023 |
0.1000 |
273.10 |
0.0021 |
0.1000 |
278.10 |
0.0018 |
0.1000 |
283.10 |
0.0016 |
0.1000 |
288.15 |
0.0015 |
0.1000 |
293.15 |
0.0014 |
0.1000 |
298.15 |
0.0012 |
0.1000 |
303.15 |
0.0012 |
0.1000 |
308.15 |
0.0011 |
0.1000 |
313.15 |
0.0009 |
0.1000 |
318.15 |
0.0009 |
0.1000 |
323.15 |
0.0008 |
0.2000 |
268.10 |
0.0028 |
0.2000 |
273.10 |
0.0025 |
0.2000 |
278.10 |
0.0022 |
0.2000 |
283.10 |
0.0020 |
0.2000 |
288.15 |
0.0017 |
0.2000 |
293.15 |
0.0015 |
0.2000 |
298.15 |
0.0014 |
0.2000 |
303.15 |
0.0012 |
0.2000 |
308.15 |
0.0011 |
0.2000 |
313.15 |
0.0010 |
0.2000 |
318.15 |
0.0009 |
0.2000 |
323.15 |
0.0008 |
0.3000 |
268.10 |
0.0033 |
0.3000 |
273.10 |
0.0029 |
0.3000 |
278.10 |
0.0026 |
0.3000 |
283.10 |
0.0023 |
0.3000 |
288.15 |
0.0020 |
0.3000 |
293.15 |
0.0017 |
0.3000 |
298.15 |
0.0015 |
0.3000 |
303.15 |
0.0014 |
0.3000 |
308.15 |
0.0012 |
0.3000 |
313.15 |
0.0011 |
0.3000 |
318.15 |
0.0010 |
0.3000 |
323.15 |
0.0009 |
0.4000 |
268.10 |
0.0040 |
0.4000 |
273.10 |
0.0035 |
0.4000 |
278.10 |
0.0030 |
0.4000 |
283.10 |
0.0026 |
0.4000 |
288.15 |
0.0022 |
0.4000 |
293.15 |
0.0019 |
0.4000 |
298.15 |
0.0017 |
0.4000 |
303.15 |
0.0014 |
0.4000 |
308.15 |
0.0013 |
0.4000 |
313.15 |
0.0011 |
0.4000 |
318.15 |
0.0010 |
0.4000 |
323.15 |
0.0009 |
0.5000 |
268.10 |
0.0048 |
0.5000 |
273.10 |
0.0041 |
0.5000 |
278.10 |
0.0035 |
0.5000 |
283.10 |
0.0030 |
0.5000 |
288.15 |
0.0025 |
0.5000 |
293.15 |
0.0022 |
0.5000 |
298.15 |
0.0018 |
0.5000 |
303.15 |
0.0016 |
0.5000 |
308.15 |
0.0014 |
0.5000 |
313.15 |
0.0013 |
0.5000 |
318.15 |
0.0011 |
0.5000 |
323.15 |
0.0010 |
0.6000 |
268.10 |
0.0059 |
0.6000 |
273.10 |
0.0050 |
0.6000 |
278.10 |
0.0042 |
0.6000 |
283.10 |
0.0035 |
0.6000 |
288.15 |
0.0029 |
0.6000 |
293.15 |
0.0025 |
0.6000 |
298.15 |
0.0021 |
0.6000 |
303.15 |
0.0018 |
0.6000 |
308.15 |
0.0016 |
0.6000 |
313.15 |
0.0014 |
0.6000 |
318.15 |
0.0013 |
0.6000 |
323.15 |
0.0011 |
0.7000 |
268.10 |
0.0072 |
0.7000 |
273.10 |
0.0059 |
0.7000 |
278.10 |
0.0049 |
0.7000 |
283.10 |
0.0041 |
0.7000 |
288.15 |
0.0034 |
0.7000 |
293.15 |
0.0028 |
0.7000 |
298.15 |
0.0024 |
0.7000 |
303.15 |
0.0020 |
0.7000 |
308.15 |
0.0018 |
0.7000 |
313.15 |
0.0016 |
0.7000 |
318.15 |
0.0014 |
0.7000 |
323.15 |
0.0012 |
0.8000 |
268.10 |
0.0075 |
0.8000 |
273.10 |
0.0062 |
0.8000 |
278.10 |
0.0050 |
0.8000 |
283.10 |
0.0041 |
0.8000 |
288.15 |
0.0034 |
0.8000 |
293.15 |
0.0028 |
0.8000 |
298.15 |
0.0024 |
0.8000 |
303.15 |
0.0021 |
0.8000 |
308.15 |
0.0018 |
0.8000 |
313.15 |
0.0016 |
0.8000 |
318.15 |
0.0014 |
0.8000 |
323.15 |
0.0012 |
0.9000 |
268.10 |
0.0060 |
0.9000 |
273.10 |
0.0050 |
0.9000 |
278.10 |
0.0041 |
0.9000 |
283.10 |
0.0033 |
0.9000 |
288.15 |
0.0027 |
0.9000 |
293.15 |
0.0023 |
0.9000 |
298.15 |
0.0019 |
0.9000 |
303.15 |
0.0017 |
0.9000 |
308.15 |
0.0014 |
0.9000 |
313.15 |
0.0013 |
0.9000 |
318.15 |
0.0011 |
0.9000 |
323.15 |
0.0010 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mass fraction of Water (2) - Liquid |
Viscosity, Pa*s - Liquid |
303.15 |
0.1500 |
0.0014 |
303.15 |
0.2000 |
0.0015 |
303.15 |
0.2500 |
0.0016 |
308.15 |
0.1500 |
0.0012 |
308.15 |
0.2000 |
0.0013 |
308.15 |
0.2500 |
0.0014 |
313.15 |
0.1500 |
0.0011 |
313.15 |
0.2000 |
0.0012 |
313.15 |
0.2500 |
0.0012 |
318.15 |
0.1500 |
0.0010 |
318.15 |
0.2000 |
0.0010 |
318.15 |
0.2500 |
0.0011 |
323.15 |
0.1500 |
0.0009 |
323.15 |
0.2000 |
0.0009 |
323.15 |
0.2500 |
0.0010 |
328.15 |
0.1500 |
0.0008 |
328.15 |
0.2000 |
0.0008 |
328.15 |
0.2500 |
0.0009 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mass fraction of Ethanol (1) - Liquid |
Viscosity, Pa*s - Liquid |
293.15 |
0.1000 |
0.0015 |
293.15 |
0.2000 |
0.0022 |
293.15 |
0.3000 |
0.0027 |
293.15 |
0.4000 |
0.0029 |
293.15 |
0.5000 |
0.0029 |
303.15 |
0.1000 |
0.0012 |
303.15 |
0.2000 |
0.0016 |
303.15 |
0.3000 |
0.0019 |
303.15 |
0.4000 |
0.0020 |
303.15 |
0.5000 |
0.0020 |
313.15 |
0.1000 |
0.0009 |
313.15 |
0.2000 |
0.0012 |
313.15 |
0.3000 |
0.0014 |
313.15 |
0.4000 |
0.0015 |
313.15 |
0.5000 |
0.0015 |
Viscosity, Pa*s
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Ethanol (1) - Liquid |
Viscosity, Pa*s - Liquid |
350.70 |
10000.00 |
0.1000 |
0.0005 |
350.70 |
10000.00 |
0.2000 |
0.0006 |
350.70 |
10000.00 |
0.3000 |
0.0006 |
350.70 |
10000.00 |
0.4000 |
0.0006 |
350.70 |
10000.00 |
0.6000 |
0.0006 |
350.70 |
10000.00 |
0.8000 |
0.0005 |
350.70 |
10000.00 |
1.0000 |
0.0005 |
350.70 |
20000.00 |
0.1000 |
0.0005 |
350.70 |
20000.00 |
0.2000 |
0.0006 |
350.70 |
20000.00 |
0.3000 |
0.0007 |
350.70 |
20000.00 |
0.4000 |
0.0007 |
350.70 |
20000.00 |
0.6000 |
0.0006 |
350.70 |
20000.00 |
0.8000 |
0.0006 |
350.70 |
20000.00 |
1.0000 |
0.0005 |
350.70 |
30000.00 |
0.1000 |
0.0006 |
350.70 |
30000.00 |
0.2000 |
0.0007 |
350.70 |
30000.00 |
0.3000 |
0.0007 |
350.70 |
30000.00 |
0.4000 |
0.0007 |
350.70 |
30000.00 |
0.6000 |
0.0007 |
350.70 |
30000.00 |
0.8000 |
0.0006 |
350.70 |
30000.00 |
1.0000 |
0.0006 |
350.70 |
40000.00 |
0.1000 |
0.0006 |
350.70 |
40000.00 |
0.2000 |
0.0007 |
350.70 |
40000.00 |
0.3000 |
0.0007 |
350.70 |
40000.00 |
0.4000 |
0.0007 |
350.70 |
40000.00 |
0.6000 |
0.0007 |
350.70 |
40000.00 |
0.8000 |
0.0006 |
350.70 |
40000.00 |
1.0000 |
0.0006 |
373.20 |
10000.00 |
0.1000 |
0.0004 |
373.20 |
10000.00 |
0.2000 |
0.0004 |
373.20 |
10000.00 |
0.3000 |
0.0005 |
373.20 |
10000.00 |
0.4000 |
0.0005 |
373.20 |
10000.00 |
0.6000 |
0.0004 |
373.20 |
10000.00 |
0.8000 |
0.0004 |
373.20 |
10000.00 |
1.0000 |
0.0004 |
373.20 |
20000.00 |
0.1000 |
0.0004 |
373.20 |
20000.00 |
0.2000 |
0.0004 |
373.20 |
20000.00 |
0.3000 |
0.0005 |
373.20 |
20000.00 |
0.4000 |
0.0005 |
373.20 |
20000.00 |
0.6000 |
0.0005 |
373.20 |
20000.00 |
0.8000 |
0.0004 |
373.20 |
20000.00 |
1.0000 |
0.0004 |
373.20 |
30000.00 |
0.1000 |
0.0004 |
373.20 |
30000.00 |
0.2000 |
0.0005 |
373.20 |
30000.00 |
0.3000 |
0.0005 |
373.20 |
30000.00 |
0.4000 |
0.0005 |
373.20 |
30000.00 |
0.6000 |
0.0005 |
373.20 |
30000.00 |
0.8000 |
0.0004 |
373.20 |
30000.00 |
1.0000 |
0.0004 |
373.20 |
40000.00 |
0.1000 |
0.0004 |
373.20 |
40000.00 |
0.2000 |
0.0005 |
373.20 |
40000.00 |
0.3000 |
0.0005 |
373.20 |
40000.00 |
0.4000 |
0.0005 |
373.20 |
40000.00 |
0.6000 |
0.0005 |
373.20 |
40000.00 |
0.8000 |
0.0005 |
373.20 |
40000.00 |
1.0000 |
0.0004 |
476.20 |
10000.00 |
0.1000 |
0.0001 |
476.20 |
10000.00 |
0.2000 |
0.0002 |
476.20 |
10000.00 |
0.3000 |
0.0001 |
476.20 |
10000.00 |
0.4000 |
0.0001 |
476.20 |
10000.00 |
0.6000 |
0.0001 |
476.20 |
10000.00 |
0.8000 |
0.0001 |
476.20 |
10000.00 |
1.0000 |
0.0001 |
476.20 |
20000.00 |
0.1000 |
0.0002 |
476.20 |
20000.00 |
0.2000 |
0.0002 |
476.20 |
20000.00 |
0.3000 |
0.0002 |
476.20 |
20000.00 |
0.4000 |
0.0001 |
476.20 |
20000.00 |
0.6000 |
0.0001 |
476.20 |
20000.00 |
0.8000 |
0.0001 |
476.20 |
20000.00 |
1.0000 |
0.0001 |
476.20 |
30000.00 |
0.1000 |
0.0002 |
476.20 |
30000.00 |
0.2000 |
0.0002 |
476.20 |
30000.00 |
0.3000 |
0.0002 |
476.20 |
30000.00 |
0.4000 |
0.0002 |
476.20 |
30000.00 |
0.6000 |
0.0001 |
476.20 |
30000.00 |
0.8000 |
0.0001 |
476.20 |
30000.00 |
1.0000 |
0.0001 |
476.20 |
40000.00 |
0.1000 |
0.0002 |
476.20 |
40000.00 |
0.2000 |
0.0002 |
476.20 |
40000.00 |
0.3000 |
0.0002 |
476.20 |
40000.00 |
0.4000 |
0.0002 |
476.20 |
40000.00 |
0.6000 |
0.0002 |
476.20 |
40000.00 |
0.8000 |
0.0002 |
476.20 |
40000.00 |
1.0000 |
0.0002 |
Viscosity, Pa*s
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Ethanol (1) - Liquid |
Viscosity, Pa*s - Liquid |
523.20 |
20000.00 |
0.0000 |
0.0001 |
523.20 |
20000.00 |
0.1000 |
0.0001 |
523.20 |
20000.00 |
0.2000 |
0.0001 |
523.20 |
20000.00 |
0.3000 |
0.0001 |
523.20 |
20000.00 |
0.4000 |
0.0001 |
523.20 |
20000.00 |
0.6000 |
0.0001 |
523.20 |
20000.00 |
0.8000 |
0.0001 |
523.20 |
20000.00 |
1.0000 |
0.0001 |
523.20 |
30000.00 |
0.0000 |
0.0001 |
523.20 |
30000.00 |
0.1000 |
0.0001 |
523.20 |
30000.00 |
0.2000 |
0.0001 |
523.20 |
30000.00 |
0.3000 |
0.0001 |
523.20 |
30000.00 |
0.4000 |
0.0001 |
523.20 |
30000.00 |
0.6000 |
0.0001 |
523.20 |
30000.00 |
0.8000 |
0.0001 |
523.20 |
30000.00 |
1.0000 |
0.0001 |
523.20 |
40000.00 |
0.0000 |
0.0001 |
523.20 |
40000.00 |
0.1000 |
0.0001 |
523.20 |
40000.00 |
0.2000 |
0.0001 |
523.20 |
40000.00 |
0.3000 |
0.0001 |
523.20 |
40000.00 |
0.4000 |
0.0001 |
523.20 |
40000.00 |
0.6000 |
0.0001 |
523.20 |
40000.00 |
0.8000 |
0.0001 |
523.20 |
40000.00 |
1.0000 |
0.0001 |
573.20 |
20000.00 |
0.0000 |
0.0001 |
573.20 |
20000.00 |
0.1000 |
0.0001 |
573.20 |
20000.00 |
0.2000 |
0.0001 |
573.20 |
20000.00 |
0.3000 |
0.0001 |
573.20 |
20000.00 |
0.4000 |
0.0001 |
573.20 |
20000.00 |
0.6000 |
0.0001 |
573.20 |
20000.00 |
0.8000 |
0.0001 |
573.20 |
20000.00 |
1.0000 |
0.0001 |
573.20 |
30000.00 |
0.0000 |
0.0001 |
573.20 |
30000.00 |
0.1000 |
0.0001 |
573.20 |
30000.00 |
0.2000 |
0.0001 |
573.20 |
30000.00 |
0.3000 |
0.0001 |
573.20 |
30000.00 |
0.4000 |
0.0001 |
573.20 |
30000.00 |
0.6000 |
0.0001 |
573.20 |
30000.00 |
0.8000 |
0.0001 |
573.20 |
30000.00 |
1.0000 |
0.0001 |
573.20 |
40000.00 |
0.0000 |
0.0001 |
573.20 |
40000.00 |
0.1000 |
0.0001 |
573.20 |
40000.00 |
0.2000 |
0.0001 |
573.20 |
40000.00 |
0.3000 |
0.0001 |
573.20 |
40000.00 |
0.4000 |
0.0001 |
573.20 |
40000.00 |
0.6000 |
0.0001 |
573.20 |
40000.00 |
0.8000 |
0.0001 |
573.20 |
40000.00 |
1.0000 |
0.0001 |
618.20 |
20000.00 |
0.0000 |
0.0001 |
618.20 |
20000.00 |
0.1000 |
0.0001 |
618.20 |
20000.00 |
0.2000 |
0.0000 |
618.20 |
20000.00 |
0.3000 |
0.0000 |
618.20 |
20000.00 |
0.4000 |
0.0000 |
618.20 |
20000.00 |
0.6000 |
0.0000 |
618.20 |
20000.00 |
0.8000 |
0.0000 |
618.20 |
20000.00 |
1.0000 |
0.0000 |
618.20 |
30000.00 |
0.0000 |
0.0001 |
618.20 |
30000.00 |
0.1000 |
0.0001 |
618.20 |
30000.00 |
0.2000 |
0.0001 |
618.20 |
30000.00 |
0.3000 |
0.0001 |
618.20 |
30000.00 |
0.4000 |
0.0001 |
618.20 |
30000.00 |
0.6000 |
0.0001 |
618.20 |
30000.00 |
0.8000 |
0.0001 |
618.20 |
30000.00 |
1.0000 |
0.0001 |
618.20 |
40000.00 |
0.0000 |
0.0001 |
618.20 |
40000.00 |
0.1000 |
0.0001 |
618.20 |
40000.00 |
0.2000 |
0.0001 |
618.20 |
40000.00 |
0.3000 |
0.0001 |
618.20 |
40000.00 |
0.4000 |
0.0001 |
618.20 |
40000.00 |
0.6000 |
0.0001 |
618.20 |
40000.00 |
0.8000 |
0.0001 |
618.20 |
40000.00 |
1.0000 |
0.0001 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Water (2) - Liquid |
Viscosity, Pa*s - Liquid |
293.15 |
0.0000 |
0.0012 |
293.15 |
0.0501 |
0.0013 |
293.15 |
0.0986 |
0.0014 |
293.15 |
0.1961 |
0.0015 |
293.15 |
0.2961 |
0.0017 |
293.15 |
0.3991 |
0.0020 |
293.15 |
0.4971 |
0.0022 |
293.15 |
0.5989 |
0.0025 |
293.15 |
0.6991 |
0.0027 |
293.15 |
0.8001 |
0.0027 |
293.15 |
0.8996 |
0.0022 |
293.15 |
0.9499 |
0.0016 |
293.15 |
1.0000 |
0.0010 |
298.15 |
0.0000 |
0.0011 |
298.15 |
0.0501 |
0.0012 |
298.15 |
0.0986 |
0.0012 |
298.15 |
0.1961 |
0.0014 |
298.15 |
0.2961 |
0.0015 |
298.15 |
0.3991 |
0.0017 |
298.15 |
0.5989 |
0.0021 |
298.15 |
0.6991 |
0.0023 |
298.15 |
0.8001 |
0.0023 |
298.15 |
0.8996 |
0.0019 |
298.15 |
0.9499 |
0.0014 |
298.15 |
1.0000 |
0.0009 |
303.15 |
0.0000 |
0.0010 |
303.15 |
0.0501 |
0.0010 |
303.15 |
0.0986 |
0.0011 |
303.15 |
0.1961 |
0.0012 |
303.15 |
0.2961 |
0.0014 |
303.15 |
0.3991 |
0.0015 |
303.15 |
0.5989 |
0.0018 |
303.15 |
0.6991 |
0.0019 |
303.15 |
0.8001 |
0.0019 |
303.15 |
0.8996 |
0.0016 |
303.15 |
0.9499 |
0.0012 |
303.15 |
1.0000 |
0.0008 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
92.3 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol (1) - Liquid |
Viscosity, Pa*s - Liquid |
293.15 |
0.0201 |
0.0012 |
293.15 |
0.0408 |
0.0015 |
293.15 |
0.0497 |
0.0016 |
293.15 |
0.0600 |
0.0018 |
293.15 |
0.0796 |
0.0020 |
293.15 |
0.1004 |
0.0023 |
293.15 |
0.1499 |
0.0027 |
293.15 |
0.1984 |
0.0029 |
293.15 |
0.2499 |
0.0029 |
293.15 |
0.3016 |
0.0028 |
293.15 |
0.3499 |
0.0027 |
293.15 |
0.3990 |
0.0026 |
293.15 |
0.4495 |
0.0024 |
293.15 |
0.4989 |
0.0023 |
293.15 |
0.5495 |
0.0022 |
293.15 |
0.6067 |
0.0020 |
293.15 |
0.6503 |
0.0019 |
293.15 |
0.6956 |
0.0018 |
293.15 |
0.7500 |
0.0017 |
293.15 |
0.7843 |
0.0016 |
293.15 |
0.8475 |
0.0015 |
293.15 |
0.8864 |
0.0014 |
293.15 |
0.9290 |
0.0013 |
298.15 |
0.0201 |
0.0011 |
298.15 |
0.0408 |
0.0013 |
298.15 |
0.0497 |
0.0014 |
298.15 |
0.0600 |
0.0016 |
298.15 |
0.0796 |
0.0017 |
298.15 |
0.1004 |
0.0019 |
298.15 |
0.1499 |
0.0022 |
298.15 |
0.1984 |
0.0024 |
298.15 |
0.2499 |
0.0024 |
298.15 |
0.3016 |
0.0023 |
298.15 |
0.3499 |
0.0023 |
298.15 |
0.3990 |
0.0022 |
298.15 |
0.4495 |
0.0021 |
298.15 |
0.4989 |
0.0020 |
298.15 |
0.5495 |
0.0019 |
298.15 |
0.6067 |
0.0017 |
298.15 |
0.6503 |
0.0017 |
298.15 |
0.6956 |
0.0016 |
298.15 |
0.7500 |
0.0015 |
298.15 |
0.7843 |
0.0014 |
298.15 |
0.8475 |
0.0013 |
298.15 |
0.8864 |
0.0013 |
298.15 |
0.9290 |
0.0012 |
303.15 |
0.0201 |
0.0010 |
303.15 |
0.0408 |
0.0012 |
303.15 |
0.0497 |
0.0012 |
303.15 |
0.0600 |
0.0013 |
303.15 |
0.0796 |
0.0015 |
303.15 |
0.1004 |
0.0017 |
303.15 |
0.1499 |
0.0019 |
303.15 |
0.1984 |
0.0020 |
303.15 |
0.2499 |
0.0020 |
303.15 |
0.3016 |
0.0020 |
303.15 |
0.3499 |
0.0019 |
303.15 |
0.3990 |
0.0019 |
303.15 |
0.4495 |
0.0018 |
303.15 |
0.4989 |
0.0017 |
303.15 |
0.5495 |
0.0016 |
303.15 |
0.6067 |
0.0015 |
303.15 |
0.6503 |
0.0015 |
303.15 |
0.6956 |
0.0014 |
303.15 |
0.7500 |
0.0013 |
303.15 |
0.7843 |
0.0013 |
303.15 |
0.8475 |
0.0012 |
303.15 |
0.8864 |
0.0011 |
303.15 |
0.9290 |
0.0011 |
308.15 |
0.0201 |
0.0009 |
308.15 |
0.0408 |
0.0010 |
308.15 |
0.0497 |
0.0011 |
308.15 |
0.0600 |
0.0012 |
308.15 |
0.0796 |
0.0013 |
308.15 |
0.1004 |
0.0014 |
308.15 |
0.1499 |
0.0016 |
308.15 |
0.1984 |
0.0017 |
308.15 |
0.2499 |
0.0017 |
308.15 |
0.3016 |
0.0017 |
308.15 |
0.3499 |
0.0017 |
308.15 |
0.3990 |
0.0016 |
308.15 |
0.4495 |
0.0015 |
308.15 |
0.4989 |
0.0015 |
308.15 |
0.5495 |
0.0014 |
308.15 |
0.6067 |
0.0013 |
308.15 |
0.6503 |
0.0013 |
308.15 |
0.6956 |
0.0012 |
308.15 |
0.7500 |
0.0012 |
308.15 |
0.7843 |
0.0011 |
308.15 |
0.8475 |
0.0011 |
308.15 |
0.8864 |
0.0010 |
308.15 |
0.9290 |
0.0010 |
293.15 |
0.0000 |
0.0011 |
298.15 |
0.0000 |
0.0009 |
303.15 |
0.0000 |
0.0008 |
308.15 |
0.0000 |
0.0008 |
293.15 |
1.0000 |
0.0012 |
298.15 |
1.0000 |
0.0011 |
303.15 |
1.0000 |
0.0010 |
308.15 |
1.0000 |
0.0009 |
Viscosity, Pa*s
[ref]
Operational conditions:
- Pressure, kPa = 100 (Liquid)
- Molality, mol/kg = 16 (Liquid)
Temperature, K - Liquid |
Viscosity, Pa*s - Liquid |
298.15 |
0.0024 |
303.15 |
0.0020 |
Viscosity, Pa*s
[ref]
Operational conditions:
- Temperature, K = 298.2 (Liquid)
- Pressure, kPa = 100 (Liquid)
Mass fraction of Water (2) - Liquid |
Viscosity, Pa*s - Liquid |
0.5080 |
0.0022 |
0.4260 |
0.0022 |
0.3110 |
0.0018 |
0.2470 |
0.0018 |
0.2350 |
0.0017 |
0.2060 |
0.0017 |
Viscosity, Pa*s
[ref]
Operational conditions:
- Temperature, K = 298.2 (Liquid)
- Pressure, kPa = 100 (Liquid)
Mass fraction of Water (2) - Liquid |
Viscosity, Pa*s - Liquid |
0.0610 |
0.0013 |
0.1240 |
0.0015 |
0.1720 |
0.0016 |
0.2330 |
0.0018 |
0.2760 |
0.0019 |
0.3400 |
0.0019 |
0.4100 |
0.0022 |
0.5000 |
0.0023 |
0.6200 |
0.0023 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Volume fraction of Ethanol (1) - Liquid |
Viscosity, Pa*s - Liquid |
303.15 |
0.1000 |
0.0007 |
303.15 |
0.2000 |
0.0010 |
303.15 |
0.3000 |
0.0012 |
303.15 |
0.4000 |
0.0013 |
303.15 |
0.5000 |
0.0014 |
308.15 |
0.1000 |
0.0006 |
308.15 |
0.2000 |
0.0009 |
308.15 |
0.3000 |
0.0009 |
308.15 |
0.4000 |
0.0011 |
308.15 |
0.5000 |
0.0012 |
313.15 |
0.1000 |
0.0006 |
313.15 |
0.2000 |
0.0007 |
313.15 |
0.3000 |
0.0009 |
313.15 |
0.4000 |
0.0009 |
313.15 |
0.5000 |
0.0011 |
318.15 |
0.1000 |
0.0006 |
318.15 |
0.2000 |
0.0006 |
318.15 |
0.3000 |
0.0008 |
318.15 |
0.4000 |
0.0009 |
318.15 |
0.5000 |
0.0009 |
318.15 |
0.3000 |
0.0008 |
323.15 |
0.1000 |
0.0005 |
323.15 |
0.2000 |
0.0006 |
323.15 |
0.3000 |
0.0007 |
323.15 |
0.4000 |
0.0007 |
323.15 |
0.5000 |
0.0008 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Molality, mol/kg of Ethanol (1) - Liquid |
Viscosity, Pa*s - Liquid |
293.15 |
14.0 |
0.0029 |
298.15 |
14.0 |
0.0024 |
303.15 |
14.0 |
0.0020 |
308.15 |
14.0 |
0.0017 |
313.15 |
14.0 |
0.0014 |
293.15 |
16.0 |
0.0029 |
298.15 |
16.0 |
0.0024 |
303.15 |
16.0 |
0.0020 |
308.15 |
16.0 |
0.0017 |
313.15 |
16.0 |
0.0015 |
293.15 |
18.0 |
0.0029 |
298.15 |
18.0 |
0.0024 |
303.15 |
18.0 |
0.0020 |
308.15 |
18.0 |
0.0017 |
313.15 |
18.0 |
0.0015 |
293.15 |
20.0 |
0.0029 |
298.15 |
20.0 |
0.0024 |
303.15 |
20.0 |
0.0020 |
308.15 |
20.0 |
0.0017 |
313.15 |
20.0 |
0.0015 |
293.15 |
22.0 |
0.0029 |
298.15 |
22.0 |
0.0024 |
303.15 |
22.0 |
0.0020 |
308.15 |
22.0 |
0.0017 |
313.15 |
22.0 |
0.0015 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Water (2) - Liquid |
Viscosity, Pa*s - Liquid |
298.15 |
0.2009 |
0.0014 |
298.15 |
0.3001 |
0.0016 |
298.15 |
0.4016 |
0.0018 |
298.15 |
0.5001 |
0.0019 |
298.15 |
0.6000 |
0.0022 |
298.15 |
0.7000 |
0.0023 |
298.15 |
0.8000 |
0.0024 |
298.15 |
0.9000 |
0.0019 |
318.15 |
0.1000 |
0.0008 |
318.15 |
0.2000 |
0.0010 |
318.15 |
0.3001 |
0.0010 |
318.15 |
0.4036 |
0.0011 |
318.15 |
0.5002 |
0.0012 |
318.15 |
0.6000 |
0.0012 |
318.15 |
0.7000 |
0.0013 |
318.15 |
0.8007 |
0.0013 |
318.15 |
0.9000 |
0.0010 |
Viscosity, Pa*s
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Mole fraction of Water (2) - Liquid |
Viscosity, Pa*s - Liquid |
0.0480 |
0.0012 |
0.1116 |
0.0013 |
0.1599 |
0.0013 |
0.1761 |
0.0014 |
0.2668 |
0.0015 |
0.3010 |
0.0016 |
0.3994 |
0.0017 |
0.4970 |
0.0019 |
0.6122 |
0.0022 |
0.7116 |
0.0024 |
0.7774 |
0.0024 |
0.8145 |
0.0024 |
0.8529 |
0.0022 |
0.8967 |
0.0019 |
0.9481 |
0.0014 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Mole fraction of Water (2) - Liquid |
Temperature, K - Liquid |
Viscosity, Pa*s - Liquid |
0.1000 |
268.10 |
0.0023 |
0.1000 |
273.10 |
0.0021 |
0.1000 |
278.10 |
0.0018 |
0.1000 |
283.10 |
0.0016 |
0.1000 |
288.15 |
0.0015 |
0.1000 |
293.15 |
0.0014 |
0.1000 |
298.15 |
0.0012 |
0.1000 |
303.15 |
0.0012 |
0.1000 |
308.15 |
0.0011 |
0.1000 |
313.15 |
0.0009 |
0.1000 |
318.15 |
0.0009 |
0.1000 |
323.15 |
0.0008 |
0.2000 |
268.10 |
0.0028 |
0.2000 |
273.10 |
0.0025 |
0.2000 |
278.10 |
0.0022 |
0.2000 |
283.10 |
0.0020 |
0.2000 |
288.15 |
0.0017 |
0.2000 |
293.15 |
0.0015 |
0.2000 |
298.15 |
0.0014 |
0.2000 |
303.15 |
0.0012 |
0.2000 |
308.15 |
0.0011 |
0.2000 |
313.15 |
0.0010 |
0.2000 |
318.15 |
0.0009 |
0.2000 |
323.15 |
0.0008 |
0.3000 |
268.10 |
0.0033 |
0.3000 |
273.10 |
0.0029 |
0.3000 |
278.10 |
0.0026 |
0.3000 |
283.10 |
0.0023 |
0.3000 |
288.15 |
0.0020 |
0.3000 |
293.15 |
0.0017 |
0.3000 |
298.15 |
0.0015 |
0.3000 |
303.15 |
0.0014 |
0.3000 |
308.15 |
0.0012 |
0.3000 |
313.15 |
0.0011 |
0.3000 |
318.15 |
0.0010 |
0.3000 |
323.15 |
0.0009 |
0.4000 |
268.10 |
0.0040 |
0.4000 |
273.10 |
0.0035 |
0.4000 |
278.10 |
0.0030 |
0.4000 |
283.10 |
0.0026 |
0.4000 |
288.15 |
0.0022 |
0.4000 |
293.15 |
0.0019 |
0.4000 |
298.15 |
0.0017 |
0.4000 |
303.15 |
0.0014 |
0.4000 |
308.15 |
0.0013 |
0.4000 |
313.15 |
0.0011 |
0.4000 |
318.15 |
0.0010 |
0.4000 |
323.15 |
0.0009 |
0.5000 |
268.10 |
0.0048 |
0.5000 |
273.10 |
0.0041 |
0.5000 |
278.10 |
0.0035 |
0.5000 |
283.10 |
0.0030 |
0.5000 |
288.15 |
0.0025 |
0.5000 |
293.15 |
0.0022 |
0.5000 |
298.15 |
0.0018 |
0.5000 |
303.15 |
0.0016 |
0.5000 |
308.15 |
0.0014 |
0.5000 |
313.15 |
0.0013 |
0.5000 |
318.15 |
0.0011 |
0.5000 |
323.15 |
0.0010 |
0.6000 |
268.10 |
0.0059 |
0.6000 |
273.10 |
0.0050 |
0.6000 |
278.10 |
0.0042 |
0.6000 |
283.10 |
0.0035 |
0.6000 |
288.15 |
0.0029 |
0.6000 |
293.15 |
0.0025 |
0.6000 |
298.15 |
0.0021 |
0.6000 |
303.15 |
0.0018 |
0.6000 |
308.15 |
0.0016 |
0.6000 |
313.15 |
0.0014 |
0.6000 |
318.15 |
0.0013 |
0.6000 |
323.15 |
0.0011 |
0.7000 |
268.10 |
0.0072 |
0.7000 |
273.10 |
0.0059 |
0.7000 |
278.10 |
0.0049 |
0.7000 |
283.10 |
0.0041 |
0.7000 |
288.15 |
0.0034 |
0.7000 |
293.15 |
0.0028 |
0.7000 |
298.15 |
0.0024 |
0.7000 |
303.15 |
0.0020 |
0.7000 |
308.15 |
0.0018 |
0.7000 |
313.15 |
0.0016 |
0.7000 |
318.15 |
0.0014 |
0.7000 |
323.15 |
0.0012 |
0.8000 |
268.10 |
0.0075 |
0.8000 |
273.10 |
0.0062 |
0.8000 |
278.10 |
0.0050 |
0.8000 |
283.10 |
0.0041 |
0.8000 |
288.15 |
0.0034 |
0.8000 |
293.15 |
0.0028 |
0.8000 |
298.15 |
0.0024 |
0.8000 |
303.15 |
0.0021 |
0.8000 |
308.15 |
0.0018 |
0.8000 |
313.15 |
0.0016 |
0.8000 |
318.15 |
0.0014 |
0.8000 |
323.15 |
0.0012 |
0.9000 |
268.10 |
0.0060 |
0.9000 |
273.10 |
0.0050 |
0.9000 |
278.10 |
0.0041 |
0.9000 |
283.10 |
0.0033 |
0.9000 |
288.15 |
0.0027 |
0.9000 |
293.15 |
0.0023 |
0.9000 |
298.15 |
0.0019 |
0.9000 |
303.15 |
0.0017 |
0.9000 |
308.15 |
0.0014 |
0.9000 |
313.15 |
0.0013 |
0.9000 |
318.15 |
0.0011 |
0.9000 |
323.15 |
0.0010 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mass fraction of Water (2) - Liquid |
Viscosity, Pa*s - Liquid |
303.15 |
0.1500 |
0.0014 |
303.15 |
0.2000 |
0.0015 |
303.15 |
0.2500 |
0.0016 |
308.15 |
0.1500 |
0.0012 |
308.15 |
0.2000 |
0.0013 |
308.15 |
0.2500 |
0.0014 |
313.15 |
0.1500 |
0.0011 |
313.15 |
0.2000 |
0.0012 |
313.15 |
0.2500 |
0.0012 |
318.15 |
0.1500 |
0.0010 |
318.15 |
0.2000 |
0.0010 |
318.15 |
0.2500 |
0.0011 |
323.15 |
0.1500 |
0.0009 |
323.15 |
0.2000 |
0.0009 |
323.15 |
0.2500 |
0.0010 |
328.15 |
0.1500 |
0.0008 |
328.15 |
0.2000 |
0.0008 |
328.15 |
0.2500 |
0.0009 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mass fraction of Ethanol (1) - Liquid |
Viscosity, Pa*s - Liquid |
293.15 |
0.1000 |
0.0015 |
293.15 |
0.2000 |
0.0022 |
293.15 |
0.3000 |
0.0027 |
293.15 |
0.4000 |
0.0029 |
293.15 |
0.5000 |
0.0029 |
303.15 |
0.1000 |
0.0012 |
303.15 |
0.2000 |
0.0016 |
303.15 |
0.3000 |
0.0019 |
303.15 |
0.4000 |
0.0020 |
303.15 |
0.5000 |
0.0020 |
313.15 |
0.1000 |
0.0009 |
313.15 |
0.2000 |
0.0012 |
313.15 |
0.3000 |
0.0014 |
313.15 |
0.4000 |
0.0015 |
313.15 |
0.5000 |
0.0015 |
Electrical conductivity, S/m
[ref]
Operational conditions:
- Temperature, K = 298 (Liquid)
- Pressure, kPa = 100 (Liquid)
- Frequency, MHz = 0.001 (Liquid)
Molality, mol/kg of Ethanol (1) - Liquid |
Electrical conductivity, S/m - Liquid |
0.9000 |
0.0002 |
1.46 |
0.0003 |
2.69 |
0.0003 |
4.09 |
0.0003 |
7.59 |
0.0003 |
9.51 |
0.0003 |
Electrical conductivity, S/m
[ref]
Operational conditions:
- Temperature, K = 298 (Liquid)
- Pressure, kPa = 100 (Liquid)
- Frequency, MHz = 0.001 (Liquid)
Molality, mol/kg of Ethanol (1) - Liquid |
Electrical conductivity, S/m - Liquid |
0.9000 |
0.0002 |
1.46 |
0.0003 |
2.69 |
0.0003 |
4.09 |
0.0003 |
7.59 |
0.0003 |
9.51 |
0.0003 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.0001 |
-0.0010 |
0.0002 |
-0.0021 |
0.0003 |
-0.0031 |
0.0004 |
-0.0042 |
0.0005 |
-0.0052 |
0.0006 |
-0.0062 |
0.0007 |
-0.0072 |
0.0008 |
-0.0083 |
0.0009 |
-0.0093 |
0.0010 |
-0.0103 |
0.0011 |
-0.0113 |
0.0012 |
-0.0123 |
0.0013 |
-0.0133 |
0.0014 |
-0.0144 |
0.0016 |
-0.0154 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Mole fraction of Water (2) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.0010 |
-0.0021 |
0.0021 |
-0.0042 |
0.0031 |
-0.0063 |
0.0041 |
-0.0083 |
0.0051 |
-0.0104 |
0.0062 |
-0.0124 |
0.0072 |
-0.0144 |
0.0082 |
-0.0163 |
0.0092 |
-0.0183 |
0.0102 |
-0.0202 |
0.0113 |
-0.0221 |
0.0123 |
-0.0240 |
0.0133 |
-0.0259 |
0.0143 |
-0.0278 |
0.0153 |
-0.0296 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Ethanol (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
333.15 |
1824.00 |
0.0079 |
-0.0399 |
333.15 |
1824.00 |
0.0160 |
-0.0795 |
333.15 |
1824.00 |
0.0333 |
-0.1550 |
333.15 |
1824.00 |
0.0519 |
-0.2170 |
333.15 |
1824.00 |
0.0719 |
-0.2660 |
333.15 |
1824.00 |
0.0936 |
-0.2970 |
333.15 |
1824.00 |
0.1172 |
-0.3080 |
333.15 |
1824.00 |
0.1430 |
-0.3060 |
333.15 |
1824.00 |
0.1712 |
-0.2880 |
333.15 |
1824.00 |
0.2023 |
-0.2590 |
333.15 |
1824.00 |
0.2366 |
-0.2310 |
333.15 |
1824.00 |
0.2747 |
-0.1900 |
333.15 |
1824.00 |
0.3173 |
-0.1470 |
333.15 |
1824.00 |
0.3653 |
-0.1010 |
333.15 |
1824.00 |
0.4196 |
-0.0523 |
333.15 |
1824.00 |
0.4818 |
-0.0073 |
333.15 |
1824.00 |
0.5535 |
0.0274 |
333.15 |
1824.00 |
0.6372 |
0.0418 |
333.15 |
1824.00 |
0.7361 |
0.0312 |
333.15 |
1824.00 |
0.8548 |
0.0006 |
333.15 |
1824.00 |
0.9236 |
-0.0155 |
333.15 |
1824.00 |
0.9608 |
-0.0121 |
363.15 |
1203.00 |
0.0079 |
-0.0112 |
363.15 |
1203.00 |
0.0160 |
-0.0235 |
363.15 |
1203.00 |
0.0333 |
-0.0465 |
363.15 |
1203.00 |
0.0518 |
-0.0592 |
363.15 |
1203.00 |
0.0719 |
-0.0586 |
363.15 |
1203.00 |
0.0936 |
-0.0453 |
363.15 |
1203.00 |
0.1172 |
-0.0202 |
363.15 |
1203.00 |
0.1430 |
0.0157 |
363.15 |
1203.00 |
0.1712 |
0.0549 |
363.15 |
1203.00 |
0.2022 |
0.0991 |
363.15 |
1203.00 |
0.2365 |
0.1440 |
363.15 |
1203.00 |
0.2746 |
0.1910 |
363.15 |
1203.00 |
0.3173 |
0.2410 |
363.15 |
1203.00 |
0.3652 |
0.2880 |
363.15 |
1203.00 |
0.4196 |
0.3320 |
363.15 |
1203.00 |
0.4817 |
0.3590 |
363.15 |
1203.00 |
0.5534 |
0.3660 |
363.15 |
1203.00 |
0.6371 |
0.3400 |
363.15 |
1203.00 |
0.7360 |
0.2680 |
363.15 |
1203.00 |
0.8548 |
0.1470 |
363.15 |
1203.00 |
0.9236 |
0.0752 |
383.15 |
1500.00 |
0.0333 |
0.0120 |
383.15 |
1500.00 |
0.0719 |
0.0617 |
383.15 |
1500.00 |
0.1172 |
0.1420 |
383.15 |
1500.00 |
0.1712 |
0.2460 |
383.15 |
1500.00 |
0.2365 |
0.3590 |
383.15 |
1500.00 |
0.3173 |
0.4690 |
383.15 |
1500.00 |
0.4196 |
0.5540 |
383.15 |
1500.00 |
0.5534 |
0.5790 |
383.15 |
1500.00 |
0.6371 |
0.5440 |
383.15 |
1500.00 |
0.7360 |
0.4450 |
383.15 |
1500.00 |
0.7926 |
0.3710 |
383.15 |
1500.00 |
0.8548 |
0.2700 |
383.15 |
1500.00 |
0.9236 |
0.1460 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
298.15 |
0.0582 |
-0.4920 |
298.15 |
0.1198 |
-0.7470 |
298.15 |
0.1500 |
-0.7700 |
298.15 |
0.1837 |
-0.7670 |
298.15 |
0.2500 |
-0.7020 |
298.15 |
0.2981 |
-0.6490 |
298.15 |
0.4127 |
-0.5010 |
298.15 |
0.5000 |
-0.3910 |
298.15 |
0.6070 |
-0.3230 |
298.15 |
0.7010 |
-0.2710 |
298.15 |
0.8120 |
-0.2060 |
298.15 |
0.9000 |
-0.1480 |
323.15 |
0.0330 |
-0.1920 |
323.15 |
0.0720 |
-0.3490 |
323.15 |
0.1070 |
-0.4090 |
323.15 |
0.1480 |
-0.4140 |
323.15 |
0.2280 |
-0.3570 |
323.15 |
0.2960 |
-0.3040 |
323.15 |
0.3550 |
-0.2400 |
323.15 |
0.4430 |
-0.1500 |
323.15 |
0.4950 |
-0.1080 |
323.15 |
0.5530 |
-0.0740 |
323.15 |
0.6370 |
-0.0550 |
323.15 |
0.7360 |
-0.0450 |
323.15 |
0.8550 |
-0.0500 |
323.15 |
0.9090 |
-0.0450 |
323.15 |
0.9680 |
-0.0180 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Water (2) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
423.20 |
5000.00 |
0.1473 |
0.3929 |
423.20 |
5000.00 |
0.2673 |
0.6656 |
423.20 |
5000.00 |
0.4508 |
0.9010 |
423.20 |
5000.00 |
0.5845 |
0.9103 |
423.20 |
5000.00 |
0.6864 |
0.8180 |
423.20 |
5000.00 |
0.7665 |
0.6846 |
423.20 |
5000.00 |
0.8312 |
0.5352 |
423.20 |
5000.00 |
0.8845 |
0.3836 |
423.20 |
5000.00 |
0.9292 |
0.2381 |
423.20 |
5000.00 |
0.9673 |
0.1066 |
423.20 |
15000.00 |
0.1466 |
0.3842 |
423.20 |
15000.00 |
0.2662 |
0.6529 |
423.20 |
15000.00 |
0.4493 |
0.8982 |
423.20 |
15000.00 |
0.5831 |
0.9113 |
423.20 |
15000.00 |
0.6851 |
0.8253 |
423.20 |
15000.00 |
0.7655 |
0.6946 |
423.20 |
15000.00 |
0.8304 |
0.5455 |
423.20 |
15000.00 |
0.8839 |
0.3922 |
423.20 |
15000.00 |
0.9289 |
0.2442 |
423.20 |
15000.00 |
0.9671 |
0.1102 |
523.20 |
15000.00 |
0.1466 |
0.7867 |
523.20 |
15000.00 |
0.2662 |
1.2739 |
523.20 |
15000.00 |
0.4493 |
1.6766 |
523.20 |
15000.00 |
0.5831 |
1.715 |
523.20 |
15000.00 |
0.6851 |
1.5605 |
523.20 |
15000.00 |
0.7655 |
1.3464 |
523.20 |
15000.00 |
0.8304 |
1.09 |
523.20 |
15000.00 |
0.8839 |
0.8281 |
523.20 |
15000.00 |
0.9289 |
0.5485 |
523.20 |
15000.00 |
0.9671 |
0.2651 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Fixed |
Measured |
Mole fraction of Ethanol (1) - Liquid |
Pressure, kPa - Liquid |
Temperature, K - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.1020 |
100.00 |
298.15 |
-0.7066 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.0001 |
-0.0010 |
0.0002 |
-0.0021 |
0.0003 |
-0.0031 |
0.0004 |
-0.0042 |
0.0005 |
-0.0052 |
0.0006 |
-0.0062 |
0.0007 |
-0.0072 |
0.0008 |
-0.0083 |
0.0009 |
-0.0093 |
0.0010 |
-0.0103 |
0.0011 |
-0.0113 |
0.0012 |
-0.0123 |
0.0013 |
-0.0133 |
0.0014 |
-0.0144 |
0.0016 |
-0.0154 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Mole fraction of Water (2) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.0010 |
-0.0021 |
0.0021 |
-0.0042 |
0.0031 |
-0.0063 |
0.0041 |
-0.0083 |
0.0051 |
-0.0104 |
0.0062 |
-0.0124 |
0.0072 |
-0.0144 |
0.0082 |
-0.0163 |
0.0092 |
-0.0183 |
0.0102 |
-0.0202 |
0.0113 |
-0.0221 |
0.0123 |
-0.0240 |
0.0133 |
-0.0259 |
0.0143 |
-0.0278 |
0.0153 |
-0.0296 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Ethanol (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
333.15 |
1824.00 |
0.0079 |
-0.0399 |
333.15 |
1824.00 |
0.0160 |
-0.0795 |
333.15 |
1824.00 |
0.0333 |
-0.1550 |
333.15 |
1824.00 |
0.0519 |
-0.2170 |
333.15 |
1824.00 |
0.0719 |
-0.2660 |
333.15 |
1824.00 |
0.0936 |
-0.2970 |
333.15 |
1824.00 |
0.1172 |
-0.3080 |
333.15 |
1824.00 |
0.1430 |
-0.3060 |
333.15 |
1824.00 |
0.1712 |
-0.2880 |
333.15 |
1824.00 |
0.2023 |
-0.2590 |
333.15 |
1824.00 |
0.2366 |
-0.2310 |
333.15 |
1824.00 |
0.2747 |
-0.1900 |
333.15 |
1824.00 |
0.3173 |
-0.1470 |
333.15 |
1824.00 |
0.3653 |
-0.1010 |
333.15 |
1824.00 |
0.4196 |
-0.0523 |
333.15 |
1824.00 |
0.4818 |
-0.0073 |
333.15 |
1824.00 |
0.5535 |
0.0274 |
333.15 |
1824.00 |
0.6372 |
0.0418 |
333.15 |
1824.00 |
0.7361 |
0.0312 |
333.15 |
1824.00 |
0.8548 |
0.0006 |
333.15 |
1824.00 |
0.9236 |
-0.0155 |
333.15 |
1824.00 |
0.9608 |
-0.0121 |
363.15 |
1203.00 |
0.0079 |
-0.0112 |
363.15 |
1203.00 |
0.0160 |
-0.0235 |
363.15 |
1203.00 |
0.0333 |
-0.0465 |
363.15 |
1203.00 |
0.0518 |
-0.0592 |
363.15 |
1203.00 |
0.0719 |
-0.0586 |
363.15 |
1203.00 |
0.0936 |
-0.0453 |
363.15 |
1203.00 |
0.1172 |
-0.0202 |
363.15 |
1203.00 |
0.1430 |
0.0157 |
363.15 |
1203.00 |
0.1712 |
0.0549 |
363.15 |
1203.00 |
0.2022 |
0.0991 |
363.15 |
1203.00 |
0.2365 |
0.1440 |
363.15 |
1203.00 |
0.2746 |
0.1910 |
363.15 |
1203.00 |
0.3173 |
0.2410 |
363.15 |
1203.00 |
0.3652 |
0.2880 |
363.15 |
1203.00 |
0.4196 |
0.3320 |
363.15 |
1203.00 |
0.4817 |
0.3590 |
363.15 |
1203.00 |
0.5534 |
0.3660 |
363.15 |
1203.00 |
0.6371 |
0.3400 |
363.15 |
1203.00 |
0.7360 |
0.2680 |
363.15 |
1203.00 |
0.8548 |
0.1470 |
363.15 |
1203.00 |
0.9236 |
0.0752 |
383.15 |
1500.00 |
0.0333 |
0.0120 |
383.15 |
1500.00 |
0.0719 |
0.0617 |
383.15 |
1500.00 |
0.1172 |
0.1420 |
383.15 |
1500.00 |
0.1712 |
0.2460 |
383.15 |
1500.00 |
0.2365 |
0.3590 |
383.15 |
1500.00 |
0.3173 |
0.4690 |
383.15 |
1500.00 |
0.4196 |
0.5540 |
383.15 |
1500.00 |
0.5534 |
0.5790 |
383.15 |
1500.00 |
0.6371 |
0.5440 |
383.15 |
1500.00 |
0.7360 |
0.4450 |
383.15 |
1500.00 |
0.7926 |
0.3710 |
383.15 |
1500.00 |
0.8548 |
0.2700 |
383.15 |
1500.00 |
0.9236 |
0.1460 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
298.15 |
0.0582 |
-0.4920 |
298.15 |
0.1198 |
-0.7470 |
298.15 |
0.1500 |
-0.7700 |
298.15 |
0.1837 |
-0.7670 |
298.15 |
0.2500 |
-0.7020 |
298.15 |
0.2981 |
-0.6490 |
298.15 |
0.4127 |
-0.5010 |
298.15 |
0.5000 |
-0.3910 |
298.15 |
0.6070 |
-0.3230 |
298.15 |
0.7010 |
-0.2710 |
298.15 |
0.8120 |
-0.2060 |
298.15 |
0.9000 |
-0.1480 |
323.15 |
0.0330 |
-0.1920 |
323.15 |
0.0720 |
-0.3490 |
323.15 |
0.1070 |
-0.4090 |
323.15 |
0.1480 |
-0.4140 |
323.15 |
0.2280 |
-0.3570 |
323.15 |
0.2960 |
-0.3040 |
323.15 |
0.3550 |
-0.2400 |
323.15 |
0.4430 |
-0.1500 |
323.15 |
0.4950 |
-0.1080 |
323.15 |
0.5530 |
-0.0740 |
323.15 |
0.6370 |
-0.0550 |
323.15 |
0.7360 |
-0.0450 |
323.15 |
0.8550 |
-0.0500 |
323.15 |
0.9090 |
-0.0450 |
323.15 |
0.9680 |
-0.0180 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Water (2) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
423.20 |
5000.00 |
0.1473 |
0.3929 |
423.20 |
5000.00 |
0.2673 |
0.6656 |
423.20 |
5000.00 |
0.4508 |
0.9010 |
423.20 |
5000.00 |
0.5845 |
0.9103 |
423.20 |
5000.00 |
0.6864 |
0.8180 |
423.20 |
5000.00 |
0.7665 |
0.6846 |
423.20 |
5000.00 |
0.8312 |
0.5352 |
423.20 |
5000.00 |
0.8845 |
0.3836 |
423.20 |
5000.00 |
0.9292 |
0.2381 |
423.20 |
5000.00 |
0.9673 |
0.1066 |
423.20 |
15000.00 |
0.1466 |
0.3842 |
423.20 |
15000.00 |
0.2662 |
0.6529 |
423.20 |
15000.00 |
0.4493 |
0.8982 |
423.20 |
15000.00 |
0.5831 |
0.9113 |
423.20 |
15000.00 |
0.6851 |
0.8253 |
423.20 |
15000.00 |
0.7655 |
0.6946 |
423.20 |
15000.00 |
0.8304 |
0.5455 |
423.20 |
15000.00 |
0.8839 |
0.3922 |
423.20 |
15000.00 |
0.9289 |
0.2442 |
423.20 |
15000.00 |
0.9671 |
0.1102 |
523.20 |
15000.00 |
0.1466 |
0.7867 |
523.20 |
15000.00 |
0.2662 |
1.2739 |
523.20 |
15000.00 |
0.4493 |
1.6766 |
523.20 |
15000.00 |
0.5831 |
1.715 |
523.20 |
15000.00 |
0.6851 |
1.5605 |
523.20 |
15000.00 |
0.7655 |
1.3464 |
523.20 |
15000.00 |
0.8304 |
1.09 |
523.20 |
15000.00 |
0.8839 |
0.8281 |
523.20 |
15000.00 |
0.9289 |
0.5485 |
523.20 |
15000.00 |
0.9671 |
0.2651 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Fixed |
Measured |
Mole fraction of Ethanol (1) - Liquid |
Pressure, kPa - Liquid |
Temperature, K - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.1020 |
100.00 |
298.15 |
-0.7066 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
288.00 |
0.0000 |
1.71 |
288.00 |
0.1000 |
2.55 |
288.00 |
0.2500 |
3.01 |
288.00 |
0.5000 |
3.99 |
288.00 |
0.7500 |
4.05 |
288.00 |
0.9000 |
4.19 |
288.00 |
1.0000 |
4.71 |
298.00 |
0.0000 |
3.16 |
298.00 |
0.1000 |
4.84 |
298.00 |
0.2500 |
6.08 |
298.00 |
0.5000 |
7.27 |
298.00 |
0.7500 |
7.72 |
298.00 |
0.9000 |
7.79 |
298.00 |
1.0000 |
7.92 |
308.00 |
0.0000 |
5.63 |
308.00 |
0.1000 |
9.39 |
308.00 |
0.2500 |
11.24 |
308.00 |
0.5000 |
12.56 |
308.00 |
0.7500 |
13.35 |
308.00 |
0.9000 |
13.60 |
308.00 |
1.0000 |
13.73 |
323.00 |
0.0000 |
12.68 |
323.00 |
0.1000 |
21.58 |
323.00 |
0.2500 |
25.84 |
323.00 |
0.5000 |
28.48 |
323.00 |
0.7500 |
28.84 |
323.00 |
0.9000 |
28.97 |
323.00 |
1.0000 |
29.22 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Ethanol (1) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0000 |
353.15 |
47.33 |
0.0511 |
353.15 |
69.98 |
0.0986 |
353.15 |
79.91 |
0.1999 |
353.15 |
92.66 |
0.2986 |
353.15 |
95.08 |
0.3978 |
353.15 |
99.86 |
0.4984 |
353.15 |
102.45 |
0.5982 |
353.15 |
105.84 |
0.6975 |
353.15 |
109.37 |
0.8045 |
353.15 |
111.10 |
0.9119 |
353.15 |
110.53 |
1.0000 |
353.15 |
108.14 |
0.0000 |
363.15 |
70.07 |
0.0501 |
363.15 |
93.06 |
0.0988 |
363.15 |
105.87 |
0.1990 |
363.15 |
124.98 |
0.2996 |
363.15 |
136.95 |
0.3989 |
363.15 |
143.00 |
0.5050 |
363.15 |
148.48 |
0.6005 |
363.15 |
153.26 |
0.6994 |
363.15 |
156.58 |
0.8193 |
363.15 |
159.34 |
0.8984 |
363.15 |
159.27 |
1.0000 |
363.15 |
156.04 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
473.20 |
0.1070 |
2180.00 |
473.20 |
0.1070 |
2150.00 |
473.20 |
0.1070 |
2180.00 |
473.10 |
0.2020 |
2400.00 |
473.10 |
0.2020 |
2380.00 |
473.20 |
0.2020 |
2390.00 |
473.30 |
0.2990 |
2590.00 |
473.30 |
0.2990 |
2590.00 |
473.30 |
0.2990 |
2570.00 |
473.00 |
0.4980 |
2760.00 |
473.00 |
0.4980 |
2760.00 |
473.00 |
0.4980 |
2760.00 |
473.00 |
0.7920 |
2970.00 |
473.00 |
0.7920 |
2980.00 |
473.00 |
0.7920 |
2980.00 |
528.40 |
0.1070 |
5590.00 |
528.40 |
0.1070 |
5590.00 |
528.30 |
0.1070 |
5630.00 |
523.20 |
0.2020 |
5820.00 |
523.20 |
0.2020 |
5740.00 |
523.20 |
0.2020 |
5680.00 |
523.30 |
0.2990 |
6110.00 |
523.40 |
0.2990 |
6090.00 |
523.40 |
0.2990 |
6070.00 |
523.10 |
0.4980 |
6750.00 |
523.10 |
0.4980 |
6670.00 |
523.00 |
0.4980 |
6690.00 |
548.20 |
0.1070 |
7550.00 |
548.20 |
0.1070 |
7580.00 |
548.30 |
0.1070 |
7610.00 |
548.30 |
0.2020 |
8360.00 |
548.30 |
0.2020 |
8330.00 |
548.20 |
0.2020 |
8330.00 |
548.40 |
0.2990 |
8960.00 |
548.40 |
0.2990 |
8960.00 |
548.40 |
0.2990 |
8950.00 |
573.30 |
0.1070 |
10970.00 |
573.20 |
0.1070 |
10750.00 |
573.20 |
0.1070 |
10840.00 |
573.20 |
0.2020 |
11860.00 |
573.20 |
0.2020 |
11860.00 |
573.20 |
0.2020 |
12020.00 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Mole fraction =
0.5 (Liquid)
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
456.86 |
2130.00 |
458.15 |
2100.00 |
473.15 |
2820.00 |
483.15 |
3460.00 |
483.56 |
3450.00 |
493.15 |
4120.00 |
498.15 |
4500.00 |
498.15 |
4500.00 |
503.15 |
4830.00 |
503.15 |
4850.00 |
508.15 |
5310.00 |
510.15 |
5450.00 |
510.68 |
5450.00 |
513.15 |
5750.00 |
521.15 |
6560.00 |
521.15 |
6560.00 |
523.15 |
6710.00 |
533.15 |
7700.00 |
533.15 |
7650.00 |
533.15 |
7650.00 |
537.45 |
8280.00 |
543.15 |
9020.00 |
543.15 |
9120.00 |
546.05 |
9650.00 |
546.15 |
9520.00 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Temperature, K =
313.15 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0000 |
7.41 |
0.0050 |
7.83 |
0.0070 |
8.08 |
0.0100 |
8.27 |
0.0140 |
8.55 |
0.0200 |
8.97 |
0.0260 |
9.32 |
0.0350 |
9.85 |
0.0500 |
10.64 |
0.0750 |
11.72 |
0.0850 |
12.17 |
0.1080 |
13.01 |
0.1110 |
13.12 |
0.1360 |
13.77 |
0.1580 |
14.25 |
0.2010 |
14.93 |
0.2560 |
15.51 |
0.3190 |
15.79 |
0.4180 |
16.37 |
0.4480 |
16.57 |
0.5180 |
16.96 |
0.5830 |
17.21 |
0.6820 |
17.51 |
0.7480 |
17.71 |
0.8280 |
17.81 |
0.8920 |
17.95 |
0.9430 |
18.00 |
1.0000 |
18.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
288.00 |
0.0000 |
1.71 |
288.00 |
0.1000 |
2.55 |
288.00 |
0.2500 |
3.01 |
288.00 |
0.5000 |
3.99 |
288.00 |
0.7500 |
4.05 |
288.00 |
0.9000 |
4.19 |
288.00 |
1.0000 |
4.71 |
298.00 |
0.0000 |
3.16 |
298.00 |
0.1000 |
4.84 |
298.00 |
0.2500 |
6.08 |
298.00 |
0.5000 |
7.27 |
298.00 |
0.7500 |
7.72 |
298.00 |
0.9000 |
7.79 |
298.00 |
1.0000 |
7.92 |
308.00 |
0.0000 |
5.63 |
308.00 |
0.1000 |
9.39 |
308.00 |
0.2500 |
11.24 |
308.00 |
0.5000 |
12.56 |
308.00 |
0.7500 |
13.35 |
308.00 |
0.9000 |
13.60 |
308.00 |
1.0000 |
13.73 |
323.00 |
0.0000 |
12.68 |
323.00 |
0.1000 |
21.58 |
323.00 |
0.2500 |
25.84 |
323.00 |
0.5000 |
28.48 |
323.00 |
0.7500 |
28.84 |
323.00 |
0.9000 |
28.97 |
323.00 |
1.0000 |
29.22 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Ethanol (1) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0000 |
353.15 |
47.33 |
0.0511 |
353.15 |
69.98 |
0.0986 |
353.15 |
79.91 |
0.1999 |
353.15 |
92.66 |
0.2986 |
353.15 |
95.08 |
0.3978 |
353.15 |
99.86 |
0.4984 |
353.15 |
102.45 |
0.5982 |
353.15 |
105.84 |
0.6975 |
353.15 |
109.37 |
0.8045 |
353.15 |
111.10 |
0.9119 |
353.15 |
110.53 |
1.0000 |
353.15 |
108.14 |
0.0000 |
363.15 |
70.07 |
0.0501 |
363.15 |
93.06 |
0.0988 |
363.15 |
105.87 |
0.1990 |
363.15 |
124.98 |
0.2996 |
363.15 |
136.95 |
0.3989 |
363.15 |
143.00 |
0.5050 |
363.15 |
148.48 |
0.6005 |
363.15 |
153.26 |
0.6994 |
363.15 |
156.58 |
0.8193 |
363.15 |
159.34 |
0.8984 |
363.15 |
159.27 |
1.0000 |
363.15 |
156.04 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
473.20 |
0.1070 |
2180.00 |
473.20 |
0.1070 |
2150.00 |
473.20 |
0.1070 |
2180.00 |
473.10 |
0.2020 |
2400.00 |
473.10 |
0.2020 |
2380.00 |
473.20 |
0.2020 |
2390.00 |
473.30 |
0.2990 |
2590.00 |
473.30 |
0.2990 |
2590.00 |
473.30 |
0.2990 |
2570.00 |
473.00 |
0.4980 |
2760.00 |
473.00 |
0.4980 |
2760.00 |
473.00 |
0.4980 |
2760.00 |
473.00 |
0.7920 |
2970.00 |
473.00 |
0.7920 |
2980.00 |
473.00 |
0.7920 |
2980.00 |
528.40 |
0.1070 |
5590.00 |
528.40 |
0.1070 |
5590.00 |
528.30 |
0.1070 |
5630.00 |
523.20 |
0.2020 |
5820.00 |
523.20 |
0.2020 |
5740.00 |
523.20 |
0.2020 |
5680.00 |
523.30 |
0.2990 |
6110.00 |
523.40 |
0.2990 |
6090.00 |
523.40 |
0.2990 |
6070.00 |
523.10 |
0.4980 |
6750.00 |
523.10 |
0.4980 |
6670.00 |
523.00 |
0.4980 |
6690.00 |
548.20 |
0.1070 |
7550.00 |
548.20 |
0.1070 |
7580.00 |
548.30 |
0.1070 |
7610.00 |
548.30 |
0.2020 |
8360.00 |
548.30 |
0.2020 |
8330.00 |
548.20 |
0.2020 |
8330.00 |
548.40 |
0.2990 |
8960.00 |
548.40 |
0.2990 |
8960.00 |
548.40 |
0.2990 |
8950.00 |
573.30 |
0.1070 |
10970.00 |
573.20 |
0.1070 |
10750.00 |
573.20 |
0.1070 |
10840.00 |
573.20 |
0.2020 |
11860.00 |
573.20 |
0.2020 |
11860.00 |
573.20 |
0.2020 |
12020.00 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Mole fraction =
0.5 (Liquid)
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
456.86 |
2130.00 |
458.15 |
2100.00 |
473.15 |
2820.00 |
483.15 |
3460.00 |
483.56 |
3450.00 |
493.15 |
4120.00 |
498.15 |
4500.00 |
498.15 |
4500.00 |
503.15 |
4830.00 |
503.15 |
4850.00 |
508.15 |
5310.00 |
510.15 |
5450.00 |
510.68 |
5450.00 |
513.15 |
5750.00 |
521.15 |
6560.00 |
521.15 |
6560.00 |
523.15 |
6710.00 |
533.15 |
7700.00 |
533.15 |
7650.00 |
533.15 |
7650.00 |
537.45 |
8280.00 |
543.15 |
9020.00 |
543.15 |
9120.00 |
546.05 |
9650.00 |
546.15 |
9520.00 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Temperature, K =
313.15 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0000 |
7.41 |
0.0050 |
7.83 |
0.0070 |
8.08 |
0.0100 |
8.27 |
0.0140 |
8.55 |
0.0200 |
8.97 |
0.0260 |
9.32 |
0.0350 |
9.85 |
0.0500 |
10.64 |
0.0750 |
11.72 |
0.0850 |
12.17 |
0.1080 |
13.01 |
0.1110 |
13.12 |
0.1360 |
13.77 |
0.1580 |
14.25 |
0.2010 |
14.93 |
0.2560 |
15.51 |
0.3190 |
15.79 |
0.4180 |
16.37 |
0.4480 |
16.57 |
0.5180 |
16.96 |
0.5830 |
17.21 |
0.6820 |
17.51 |
0.7480 |
17.71 |
0.8280 |
17.81 |
0.8920 |
17.95 |
0.9430 |
18.00 |
1.0000 |
18.00 |
Refractive index (Na D-line)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Molality, mol/kg of Ethanol (1) - Liquid |
Refractive index (Na D-line) - Liquid |
298.15 |
100.00 |
16.0 |
1.3569 |
Refractive index (Na D-line)
[ref]
Operational conditions:
- Temperature, K = 298 (Liquid)
- Pressure, kPa = 100 (Liquid)
Molality, mol/kg of Ethanol (1) - Liquid |
Refractive index (Na D-line) - Liquid |
0.9000 |
1.3362 |
1.46 |
1.3375 |
2.69 |
1.34 |
4.09 |
1.3431 |
7.59 |
1.3497 |
9.51 |
1.3521 |
Refractive index (Na D-line)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mass fraction of Ethanol (1) - Liquid |
Refractive index (Na D-line) - Liquid |
298.15 |
0.1084 |
1.3396 |
298.15 |
0.1219 |
1.3405 |
298.15 |
0.2859 |
1.3512 |
298.15 |
0.2907 |
1.3516 |
298.15 |
0.3737 |
1.3554 |
298.15 |
0.3750 |
1.3555 |
298.15 |
0.4432 |
1.3579 |
298.15 |
0.4445 |
1.3577 |
298.15 |
0.4998 |
1.3579 |
298.15 |
0.5049 |
1.3596 |
298.15 |
0.6193 |
1.3618 |
298.15 |
0.6275 |
1.3618 |
313.15 |
0.1672 |
1.3406 |
313.15 |
0.2858 |
1.347 |
313.15 |
0.2894 |
1.3463 |
313.15 |
0.3525 |
1.3493 |
313.15 |
0.3757 |
1.3508 |
313.15 |
0.4420 |
1.3529 |
313.15 |
0.4445 |
1.3529 |
313.15 |
0.4982 |
1.3543 |
313.15 |
0.5018 |
1.3542 |
313.15 |
0.6180 |
1.3562 |
313.15 |
0.6271 |
1.3562 |
313.15 |
0.7114 |
1.3569 |
Refractive index (Na D-line)
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
Molality, mol/kg of Ethanol (1) - Liquid |
Refractive index (Na D-line) - Liquid |
14.0 |
1.355 |
16.0 |
1.3564 |
18.0 |
1.3575 |
20.0 |
1.3583 |
22.0 |
1.3585 |
Refractive index (Na D-line)
[ref]
Operational conditions:
- Temperature, K = 338.15 (Liquid)
- Pressure, kPa = 98 (Liquid)
Mass fraction of Ethanol (1) - Liquid |
Refractive index (Na D-line) - Liquid |
0.2000 |
1.3363 |
0.4000 |
1.3415 |
0.6000 |
1.3569 |
0.9000 |
1.3587 |
Refractive index (Na D-line)
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Mole fraction of Water (2) - Liquid |
Refractive index (Na D-line) - Liquid |
0.0480 |
1.3601 |
0.1116 |
1.361 |
0.1599 |
1.3615 |
0.1761 |
1.3617 |
0.2668 |
1.3625 |
0.3010 |
1.3627 |
0.3994 |
1.363 |
0.4970 |
1.3628 |
0.6122 |
1.3618 |
0.7116 |
1.3597 |
0.7774 |
1.3573 |
0.8145 |
1.3554 |
0.8529 |
1.3524 |
0.8967 |
1.3478 |
0.9481 |
1.3406 |
Refractive index (Na D-line)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mass fraction of Ethanol (1) - Liquid |
Refractive index (Na D-line) - Liquid |
288.15 |
0.0000 |
1.3334 |
288.15 |
0.0247 |
1.3349 |
288.15 |
0.0538 |
1.3369 |
288.15 |
0.0781 |
1.3385 |
288.15 |
0.1014 |
1.3403 |
288.15 |
0.1249 |
1.3421 |
288.15 |
0.1528 |
1.3444 |
288.15 |
0.1778 |
1.3463 |
288.15 |
0.2036 |
1.3483 |
288.15 |
0.2250 |
1.3498 |
288.15 |
0.2470 |
1.3514 |
288.15 |
0.2699 |
1.3528 |
288.15 |
0.2955 |
1.3543 |
288.15 |
0.3241 |
1.3559 |
288.15 |
0.3468 |
1.3572 |
288.15 |
0.3723 |
1.3584 |
288.15 |
0.3959 |
1.3597 |
288.15 |
0.4255 |
1.3607 |
288.15 |
0.4462 |
1.3616 |
288.15 |
0.4735 |
1.3623 |
288.15 |
0.4969 |
1.3632 |
288.15 |
0.5239 |
1.3638 |
288.15 |
0.5458 |
1.3643 |
288.15 |
0.5709 |
1.3648 |
288.15 |
0.5972 |
1.3655 |
288.15 |
0.6203 |
1.3658 |
288.15 |
0.6467 |
1.366 |
288.15 |
0.6694 |
1.3664 |
288.15 |
0.6959 |
1.3666 |
288.15 |
0.7187 |
1.3666 |
288.15 |
0.7494 |
1.367 |
288.15 |
0.7672 |
1.367 |
288.15 |
0.7993 |
1.3669 |
288.15 |
0.8187 |
1.3671 |
288.15 |
0.8451 |
1.3668 |
288.15 |
0.8670 |
1.3668 |
288.15 |
0.9028 |
1.3664 |
288.15 |
0.9235 |
1.366 |
288.15 |
0.9481 |
1.3653 |
288.15 |
0.9752 |
1.3645 |
288.15 |
1.0000 |
1.3634 |
298.15 |
0.0000 |
1.3325 |
298.15 |
0.0247 |
1.334 |
298.15 |
0.0538 |
1.3359 |
298.15 |
0.0781 |
1.3377 |
298.15 |
0.1014 |
1.3392 |
298.15 |
0.1249 |
1.341 |
298.15 |
0.1528 |
1.3429 |
298.15 |
0.1778 |
1.3447 |
298.15 |
0.2036 |
1.3465 |
298.15 |
0.2250 |
1.3478 |
298.15 |
0.2470 |
1.3493 |
298.15 |
0.2699 |
1.3506 |
298.15 |
0.2955 |
1.3521 |
298.15 |
0.3241 |
1.3536 |
298.15 |
0.3468 |
1.3546 |
298.15 |
0.3723 |
1.3557 |
298.15 |
0.3959 |
1.3566 |
298.15 |
0.4255 |
1.3577 |
298.15 |
0.4462 |
1.3583 |
298.15 |
0.4735 |
1.3592 |
298.15 |
0.4969 |
1.3597 |
298.15 |
0.5239 |
1.3604 |
298.15 |
0.5458 |
1.3608 |
298.15 |
0.5709 |
1.3613 |
298.15 |
0.5972 |
1.3619 |
298.15 |
0.6203 |
1.362 |
298.15 |
0.6467 |
1.3624 |
298.15 |
0.6694 |
1.3626 |
298.15 |
0.6959 |
1.3629 |
298.15 |
0.7187 |
1.3631 |
298.15 |
0.7494 |
1.3631 |
298.15 |
0.7672 |
1.3632 |
298.15 |
0.7993 |
1.3632 |
298.15 |
0.8187 |
1.3632 |
298.15 |
0.8451 |
1.3629 |
298.15 |
0.8670 |
1.3628 |
298.15 |
0.9028 |
1.3623 |
298.15 |
0.9235 |
1.362 |
298.15 |
0.9481 |
1.3612 |
298.15 |
0.9752 |
1.3604 |
298.15 |
1.0000 |
1.3592 |
308.15 |
0.0000 |
1.3313 |
308.15 |
0.0247 |
1.3328 |
308.15 |
0.0538 |
1.3345 |
308.15 |
0.0781 |
1.3362 |
308.15 |
0.1014 |
1.3377 |
308.15 |
0.1249 |
1.3392 |
308.15 |
0.1528 |
1.341 |
308.15 |
0.1778 |
1.3427 |
308.15 |
0.2036 |
1.3443 |
308.15 |
0.2250 |
1.3455 |
308.15 |
0.2470 |
1.3468 |
308.15 |
0.2699 |
1.3479 |
308.15 |
0.2955 |
1.3492 |
308.15 |
0.3241 |
1.3505 |
308.15 |
0.3468 |
1.3516 |
308.15 |
0.3723 |
1.3525 |
308.15 |
0.3959 |
1.3534 |
308.15 |
0.4255 |
1.3545 |
308.15 |
0.4462 |
1.355 |
308.15 |
0.4735 |
1.3557 |
308.15 |
0.4969 |
1.3562 |
308.15 |
0.5239 |
1.3567 |
308.15 |
0.5458 |
1.3573 |
308.15 |
0.5709 |
1.3577 |
308.15 |
0.5972 |
1.358 |
308.15 |
0.6203 |
1.3582 |
308.15 |
0.6467 |
1.3584 |
308.15 |
0.6694 |
1.3587 |
308.15 |
0.6959 |
1.3587 |
308.15 |
0.7187 |
1.3589 |
308.15 |
0.7494 |
1.359 |
308.15 |
0.7672 |
1.359 |
308.15 |
0.7993 |
1.3588 |
308.15 |
0.8187 |
1.3589 |
308.15 |
0.8451 |
1.3586 |
308.15 |
0.8670 |
1.3584 |
308.15 |
0.9028 |
1.3578 |
308.15 |
0.9235 |
1.3574 |
308.15 |
0.9481 |
1.3568 |
308.15 |
0.9752 |
1.3559 |
308.15 |
1.0000 |
1.3548 |
318.15 |
0.0000 |
1.3298 |
318.15 |
0.0247 |
1.3312 |
318.15 |
0.0538 |
1.333 |
318.15 |
0.0781 |
1.3345 |
318.15 |
0.1014 |
1.3358 |
318.15 |
0.1249 |
1.3374 |
318.15 |
0.1528 |
1.339 |
318.15 |
0.1778 |
1.3405 |
318.15 |
0.2036 |
1.3418 |
318.15 |
0.2250 |
1.3431 |
318.15 |
0.2470 |
1.3442 |
318.15 |
0.2699 |
1.3452 |
318.15 |
0.2955 |
1.3464 |
318.15 |
0.3241 |
1.3477 |
318.15 |
0.3468 |
1.3485 |
318.15 |
0.3723 |
1.3493 |
318.15 |
0.3959 |
1.35 |
318.15 |
0.4255 |
1.351 |
318.15 |
0.4462 |
1.3515 |
318.15 |
0.4735 |
1.3521 |
318.15 |
0.4969 |
1.3525 |
318.15 |
0.5239 |
1.353 |
318.15 |
0.5458 |
1.3533 |
318.15 |
0.5709 |
1.3537 |
318.15 |
0.5972 |
1.3538 |
318.15 |
0.6203 |
1.3542 |
318.15 |
0.6467 |
1.3543 |
318.15 |
0.6694 |
1.3545 |
318.15 |
0.6959 |
1.3545 |
318.15 |
0.7187 |
1.3547 |
318.15 |
0.7494 |
1.3547 |
318.15 |
0.7672 |
1.3547 |
318.15 |
0.7993 |
1.3548 |
318.15 |
0.8187 |
1.3548 |
318.15 |
0.8451 |
1.3546 |
318.15 |
0.8670 |
1.3542 |
318.15 |
0.9028 |
1.3537 |
318.15 |
0.9235 |
1.3533 |
318.15 |
0.9481 |
1.3525 |
318.15 |
0.9752 |
1.3517 |
318.15 |
1.0000 |
1.3507 |
Refractive index (Na D-line)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Molality, mol/kg of Ethanol (1) - Liquid |
Refractive index (Na D-line) - Liquid |
298.15 |
100.00 |
16.0 |
1.3569 |
Refractive index (Na D-line)
[ref]
Operational conditions:
- Temperature, K = 298 (Liquid)
- Pressure, kPa = 100 (Liquid)
Molality, mol/kg of Ethanol (1) - Liquid |
Refractive index (Na D-line) - Liquid |
0.9000 |
1.3362 |
1.46 |
1.3375 |
2.69 |
1.34 |
4.09 |
1.3431 |
7.59 |
1.3497 |
9.51 |
1.3521 |
Refractive index (Na D-line)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mass fraction of Ethanol (1) - Liquid |
Refractive index (Na D-line) - Liquid |
298.15 |
0.1084 |
1.3396 |
298.15 |
0.1219 |
1.3405 |
298.15 |
0.2859 |
1.3512 |
298.15 |
0.2907 |
1.3516 |
298.15 |
0.3737 |
1.3554 |
298.15 |
0.3750 |
1.3555 |
298.15 |
0.4432 |
1.3579 |
298.15 |
0.4445 |
1.3577 |
298.15 |
0.4998 |
1.3579 |
298.15 |
0.5049 |
1.3596 |
298.15 |
0.6193 |
1.3618 |
298.15 |
0.6275 |
1.3618 |
313.15 |
0.1672 |
1.3406 |
313.15 |
0.2858 |
1.347 |
313.15 |
0.2894 |
1.3463 |
313.15 |
0.3525 |
1.3493 |
313.15 |
0.3757 |
1.3508 |
313.15 |
0.4420 |
1.3529 |
313.15 |
0.4445 |
1.3529 |
313.15 |
0.4982 |
1.3543 |
313.15 |
0.5018 |
1.3542 |
313.15 |
0.6180 |
1.3562 |
313.15 |
0.6271 |
1.3562 |
313.15 |
0.7114 |
1.3569 |
Refractive index (Na D-line)
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
Molality, mol/kg of Ethanol (1) - Liquid |
Refractive index (Na D-line) - Liquid |
14.0 |
1.355 |
16.0 |
1.3564 |
18.0 |
1.3575 |
20.0 |
1.3583 |
22.0 |
1.3585 |
Refractive index (Na D-line)
[ref]
Operational conditions:
- Temperature, K = 338.15 (Liquid)
- Pressure, kPa = 98 (Liquid)
Mass fraction of Ethanol (1) - Liquid |
Refractive index (Na D-line) - Liquid |
0.2000 |
1.3363 |
0.4000 |
1.3415 |
0.6000 |
1.3569 |
0.9000 |
1.3587 |
Refractive index (Na D-line)
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Mole fraction of Water (2) - Liquid |
Refractive index (Na D-line) - Liquid |
0.0480 |
1.3601 |
0.1116 |
1.361 |
0.1599 |
1.3615 |
0.1761 |
1.3617 |
0.2668 |
1.3625 |
0.3010 |
1.3627 |
0.3994 |
1.363 |
0.4970 |
1.3628 |
0.6122 |
1.3618 |
0.7116 |
1.3597 |
0.7774 |
1.3573 |
0.8145 |
1.3554 |
0.8529 |
1.3524 |
0.8967 |
1.3478 |
0.9481 |
1.3406 |
Refractive index (Na D-line)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mass fraction of Ethanol (1) - Liquid |
Refractive index (Na D-line) - Liquid |
288.15 |
0.0000 |
1.3334 |
288.15 |
0.0247 |
1.3349 |
288.15 |
0.0538 |
1.3369 |
288.15 |
0.0781 |
1.3385 |
288.15 |
0.1014 |
1.3403 |
288.15 |
0.1249 |
1.3421 |
288.15 |
0.1528 |
1.3444 |
288.15 |
0.1778 |
1.3463 |
288.15 |
0.2036 |
1.3483 |
288.15 |
0.2250 |
1.3498 |
288.15 |
0.2470 |
1.3514 |
288.15 |
0.2699 |
1.3528 |
288.15 |
0.2955 |
1.3543 |
288.15 |
0.3241 |
1.3559 |
288.15 |
0.3468 |
1.3572 |
288.15 |
0.3723 |
1.3584 |
288.15 |
0.3959 |
1.3597 |
288.15 |
0.4255 |
1.3607 |
288.15 |
0.4462 |
1.3616 |
288.15 |
0.4735 |
1.3623 |
288.15 |
0.4969 |
1.3632 |
288.15 |
0.5239 |
1.3638 |
288.15 |
0.5458 |
1.3643 |
288.15 |
0.5709 |
1.3648 |
288.15 |
0.5972 |
1.3655 |
288.15 |
0.6203 |
1.3658 |
288.15 |
0.6467 |
1.366 |
288.15 |
0.6694 |
1.3664 |
288.15 |
0.6959 |
1.3666 |
288.15 |
0.7187 |
1.3666 |
288.15 |
0.7494 |
1.367 |
288.15 |
0.7672 |
1.367 |
288.15 |
0.7993 |
1.3669 |
288.15 |
0.8187 |
1.3671 |
288.15 |
0.8451 |
1.3668 |
288.15 |
0.8670 |
1.3668 |
288.15 |
0.9028 |
1.3664 |
288.15 |
0.9235 |
1.366 |
288.15 |
0.9481 |
1.3653 |
288.15 |
0.9752 |
1.3645 |
288.15 |
1.0000 |
1.3634 |
298.15 |
0.0000 |
1.3325 |
298.15 |
0.0247 |
1.334 |
298.15 |
0.0538 |
1.3359 |
298.15 |
0.0781 |
1.3377 |
298.15 |
0.1014 |
1.3392 |
298.15 |
0.1249 |
1.341 |
298.15 |
0.1528 |
1.3429 |
298.15 |
0.1778 |
1.3447 |
298.15 |
0.2036 |
1.3465 |
298.15 |
0.2250 |
1.3478 |
298.15 |
0.2470 |
1.3493 |
298.15 |
0.2699 |
1.3506 |
298.15 |
0.2955 |
1.3521 |
298.15 |
0.3241 |
1.3536 |
298.15 |
0.3468 |
1.3546 |
298.15 |
0.3723 |
1.3557 |
298.15 |
0.3959 |
1.3566 |
298.15 |
0.4255 |
1.3577 |
298.15 |
0.4462 |
1.3583 |
298.15 |
0.4735 |
1.3592 |
298.15 |
0.4969 |
1.3597 |
298.15 |
0.5239 |
1.3604 |
298.15 |
0.5458 |
1.3608 |
298.15 |
0.5709 |
1.3613 |
298.15 |
0.5972 |
1.3619 |
298.15 |
0.6203 |
1.362 |
298.15 |
0.6467 |
1.3624 |
298.15 |
0.6694 |
1.3626 |
298.15 |
0.6959 |
1.3629 |
298.15 |
0.7187 |
1.3631 |
298.15 |
0.7494 |
1.3631 |
298.15 |
0.7672 |
1.3632 |
298.15 |
0.7993 |
1.3632 |
298.15 |
0.8187 |
1.3632 |
298.15 |
0.8451 |
1.3629 |
298.15 |
0.8670 |
1.3628 |
298.15 |
0.9028 |
1.3623 |
298.15 |
0.9235 |
1.362 |
298.15 |
0.9481 |
1.3612 |
298.15 |
0.9752 |
1.3604 |
298.15 |
1.0000 |
1.3592 |
308.15 |
0.0000 |
1.3313 |
308.15 |
0.0247 |
1.3328 |
308.15 |
0.0538 |
1.3345 |
308.15 |
0.0781 |
1.3362 |
308.15 |
0.1014 |
1.3377 |
308.15 |
0.1249 |
1.3392 |
308.15 |
0.1528 |
1.341 |
308.15 |
0.1778 |
1.3427 |
308.15 |
0.2036 |
1.3443 |
308.15 |
0.2250 |
1.3455 |
308.15 |
0.2470 |
1.3468 |
308.15 |
0.2699 |
1.3479 |
308.15 |
0.2955 |
1.3492 |
308.15 |
0.3241 |
1.3505 |
308.15 |
0.3468 |
1.3516 |
308.15 |
0.3723 |
1.3525 |
308.15 |
0.3959 |
1.3534 |
308.15 |
0.4255 |
1.3545 |
308.15 |
0.4462 |
1.355 |
308.15 |
0.4735 |
1.3557 |
308.15 |
0.4969 |
1.3562 |
308.15 |
0.5239 |
1.3567 |
308.15 |
0.5458 |
1.3573 |
308.15 |
0.5709 |
1.3577 |
308.15 |
0.5972 |
1.358 |
308.15 |
0.6203 |
1.3582 |
308.15 |
0.6467 |
1.3584 |
308.15 |
0.6694 |
1.3587 |
308.15 |
0.6959 |
1.3587 |
308.15 |
0.7187 |
1.3589 |
308.15 |
0.7494 |
1.359 |
308.15 |
0.7672 |
1.359 |
308.15 |
0.7993 |
1.3588 |
308.15 |
0.8187 |
1.3589 |
308.15 |
0.8451 |
1.3586 |
308.15 |
0.8670 |
1.3584 |
308.15 |
0.9028 |
1.3578 |
308.15 |
0.9235 |
1.3574 |
308.15 |
0.9481 |
1.3568 |
308.15 |
0.9752 |
1.3559 |
308.15 |
1.0000 |
1.3548 |
318.15 |
0.0000 |
1.3298 |
318.15 |
0.0247 |
1.3312 |
318.15 |
0.0538 |
1.333 |
318.15 |
0.0781 |
1.3345 |
318.15 |
0.1014 |
1.3358 |
318.15 |
0.1249 |
1.3374 |
318.15 |
0.1528 |
1.339 |
318.15 |
0.1778 |
1.3405 |
318.15 |
0.2036 |
1.3418 |
318.15 |
0.2250 |
1.3431 |
318.15 |
0.2470 |
1.3442 |
318.15 |
0.2699 |
1.3452 |
318.15 |
0.2955 |
1.3464 |
318.15 |
0.3241 |
1.3477 |
318.15 |
0.3468 |
1.3485 |
318.15 |
0.3723 |
1.3493 |
318.15 |
0.3959 |
1.35 |
318.15 |
0.4255 |
1.351 |
318.15 |
0.4462 |
1.3515 |
318.15 |
0.4735 |
1.3521 |
318.15 |
0.4969 |
1.3525 |
318.15 |
0.5239 |
1.353 |
318.15 |
0.5458 |
1.3533 |
318.15 |
0.5709 |
1.3537 |
318.15 |
0.5972 |
1.3538 |
318.15 |
0.6203 |
1.3542 |
318.15 |
0.6467 |
1.3543 |
318.15 |
0.6694 |
1.3545 |
318.15 |
0.6959 |
1.3545 |
318.15 |
0.7187 |
1.3547 |
318.15 |
0.7494 |
1.3547 |
318.15 |
0.7672 |
1.3547 |
318.15 |
0.7993 |
1.3548 |
318.15 |
0.8187 |
1.3548 |
318.15 |
0.8451 |
1.3546 |
318.15 |
0.8670 |
1.3542 |
318.15 |
0.9028 |
1.3537 |
318.15 |
0.9235 |
1.3533 |
318.15 |
0.9481 |
1.3525 |
318.15 |
0.9752 |
1.3517 |
318.15 |
1.0000 |
1.3507 |
Mass density, kg/m3
[ref]
Operational condition: Mole fraction =
0.5 (Gas)
Temperature, K - Gas |
Mass density, kg/m3 - Gas |
513.15 |
69.41 |
523.15 |
84.56 |
533.15 |
117.12 |
543.15 |
147.5 |
Mass density, kg/m3
[ref]
Operational condition: Mole fraction =
0.5 (Gas)
Temperature, K - Gas |
Mass density, kg/m3 - Gas |
513.15 |
69.41 |
523.15 |
84.56 |
533.15 |
117.12 |
543.15 |
147.5 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Ethanol (1) - Liquid |
Mass density, kg/m3 - Liquid |
298.15 |
100.00 |
0.0030 |
995.3 |
298.15 |
100.00 |
0.0042 |
994.5 |
298.15 |
100.00 |
0.0082 |
993.0 |
298.15 |
100.00 |
0.0119 |
991.5 |
298.15 |
100.00 |
0.0158 |
989.8 |
298.15 |
100.00 |
0.0184 |
988.4 |
298.15 |
100.00 |
0.0219 |
987.6 |
298.15 |
100.00 |
0.0255 |
986.0 |
298.15 |
100.00 |
0.0279 |
984.7 |
298.15 |
100.00 |
0.0315 |
984.0 |
298.15 |
100.00 |
0.0366 |
981.6 |
298.15 |
100.00 |
0.0392 |
980.7 |
298.15 |
100.00 |
0.0439 |
979.2 |
298.15 |
100.00 |
0.0483 |
977.5 |
298.15 |
100.00 |
0.0516 |
977.1 |
298.15 |
100.00 |
0.0559 |
975.8 |
298.15 |
100.00 |
0.0600 |
974.5 |
298.15 |
100.00 |
0.0652 |
972.9 |
298.15 |
100.00 |
0.0679 |
972.2 |
298.15 |
100.00 |
0.0722 |
971.0 |
298.15 |
100.00 |
0.0801 |
968.6 |
298.15 |
100.00 |
0.0840 |
967.9 |
298.15 |
100.00 |
0.0879 |
966.7 |
298.15 |
100.00 |
0.0926 |
965.6 |
298.15 |
100.00 |
0.0958 |
964.6 |
298.15 |
100.00 |
0.1006 |
963.2 |
298.15 |
100.00 |
0.1111 |
960.2 |
298.15 |
100.00 |
0.1225 |
956.8 |
298.15 |
100.00 |
0.1296 |
954.9 |
298.15 |
100.00 |
0.1402 |
951.8 |
298.15 |
100.00 |
0.1510 |
948.4 |
298.15 |
100.00 |
0.1601 |
945.6 |
298.15 |
100.00 |
0.1703 |
942.5 |
298.15 |
100.00 |
0.1800 |
939.8 |
298.15 |
100.00 |
0.1903 |
936.5 |
298.15 |
100.00 |
0.1996 |
933.5 |
298.15 |
100.00 |
0.2269 |
925.4 |
298.15 |
100.00 |
0.2502 |
918.5 |
298.15 |
100.00 |
0.2745 |
911.7 |
298.15 |
100.00 |
0.3009 |
904.5 |
298.15 |
100.00 |
0.3500 |
891.9 |
298.15 |
100.00 |
0.4034 |
879.4 |
298.15 |
100.00 |
0.4501 |
868.8 |
298.15 |
100.00 |
0.4980 |
859.3 |
298.15 |
100.00 |
0.5501 |
849.5 |
298.15 |
100.00 |
0.5998 |
840.9 |
298.15 |
100.00 |
0.6489 |
832.7 |
298.15 |
100.00 |
0.6967 |
825.2 |
298.15 |
100.00 |
0.7475 |
818.2 |
298.15 |
100.00 |
0.7996 |
810.9 |
298.15 |
100.00 |
0.8484 |
804.4 |
298.15 |
100.00 |
0.8993 |
798.0 |
298.15 |
100.00 |
0.9503 |
791.7 |
298.15 |
100.00 |
1.0000 |
785.7 |
298.15 |
10000.00 |
0.0030 |
999.8 |
298.15 |
10000.00 |
0.0042 |
998.9 |
298.15 |
10000.00 |
0.0082 |
997.3 |
298.15 |
10000.00 |
0.0119 |
995.8 |
298.15 |
10000.00 |
0.0158 |
994.0 |
298.15 |
10000.00 |
0.0184 |
992.6 |
298.15 |
10000.00 |
0.0219 |
991.7 |
298.15 |
10000.00 |
0.0255 |
990.2 |
298.15 |
10000.00 |
0.0279 |
988.7 |
298.15 |
10000.00 |
0.0315 |
988.0 |
298.15 |
10000.00 |
0.0366 |
985.7 |
298.15 |
10000.00 |
0.0392 |
984.7 |
298.15 |
10000.00 |
0.0439 |
983.3 |
298.15 |
10000.00 |
0.0483 |
981.6 |
298.15 |
10000.00 |
0.0516 |
981.0 |
298.15 |
10000.00 |
0.0559 |
979.8 |
298.15 |
10000.00 |
0.0600 |
978.5 |
298.15 |
10000.00 |
0.0652 |
976.9 |
298.15 |
10000.00 |
0.0679 |
976.1 |
298.15 |
10000.00 |
0.0722 |
974.9 |
298.15 |
10000.00 |
0.0801 |
972.4 |
298.15 |
10000.00 |
0.0840 |
971.8 |
298.15 |
10000.00 |
0.0879 |
970.6 |
298.15 |
10000.00 |
0.0926 |
969.3 |
298.15 |
10000.00 |
0.0958 |
968.5 |
298.15 |
10000.00 |
0.1006 |
967.1 |
298.15 |
10000.00 |
0.1111 |
964.1 |
298.15 |
10000.00 |
0.1225 |
960.7 |
298.15 |
10000.00 |
0.1296 |
958.8 |
298.15 |
10000.00 |
0.1402 |
955.8 |
298.15 |
10000.00 |
0.1510 |
952.5 |
298.15 |
10000.00 |
0.1601 |
949.8 |
298.15 |
10000.00 |
0.1703 |
946.7 |
298.15 |
10000.00 |
0.1800 |
943.9 |
298.15 |
10000.00 |
0.1903 |
940.9 |
298.15 |
10000.00 |
0.1996 |
938.0 |
298.15 |
10000.00 |
0.2269 |
930.0 |
298.15 |
10000.00 |
0.2502 |
923.3 |
298.15 |
10000.00 |
0.2745 |
916.6 |
298.15 |
10000.00 |
0.3009 |
909.6 |
298.15 |
10000.00 |
0.3500 |
897.1 |
298.15 |
10000.00 |
0.4034 |
884.9 |
298.15 |
10000.00 |
0.4501 |
874.7 |
298.15 |
10000.00 |
0.4980 |
865.4 |
298.15 |
10000.00 |
0.5501 |
855.8 |
298.15 |
10000.00 |
0.5998 |
847.4 |
298.15 |
10000.00 |
0.6489 |
839.5 |
298.15 |
10000.00 |
0.6967 |
832.3 |
298.15 |
10000.00 |
0.7475 |
825.4 |
298.15 |
10000.00 |
0.7996 |
818.3 |
298.15 |
10000.00 |
0.8484 |
812.1 |
298.15 |
10000.00 |
0.8993 |
805.8 |
298.15 |
10000.00 |
0.9503 |
799.9 |
298.15 |
10000.00 |
1.0000 |
794.0 |
298.15 |
20000.00 |
0.0030 |
1004.2 |
298.15 |
20000.00 |
0.0042 |
1003.2 |
298.15 |
20000.00 |
0.0082 |
1001.7 |
298.15 |
20000.00 |
0.0119 |
1000.1 |
298.15 |
20000.00 |
0.0158 |
998.2 |
298.15 |
20000.00 |
0.0184 |
996.8 |
298.15 |
20000.00 |
0.0219 |
995.9 |
298.15 |
20000.00 |
0.0255 |
994.4 |
298.15 |
20000.00 |
0.0279 |
992.9 |
298.15 |
20000.00 |
0.0315 |
992.1 |
298.15 |
20000.00 |
0.0366 |
989.8 |
298.15 |
20000.00 |
0.0392 |
988.6 |
298.15 |
20000.00 |
0.0439 |
987.3 |
298.15 |
20000.00 |
0.0483 |
985.6 |
298.15 |
20000.00 |
0.0516 |
985.1 |
298.15 |
20000.00 |
0.0559 |
983.8 |
298.15 |
20000.00 |
0.0600 |
982.4 |
298.15 |
20000.00 |
0.0652 |
980.8 |
298.15 |
20000.00 |
0.0679 |
980.0 |
298.15 |
20000.00 |
0.0722 |
978.7 |
298.15 |
20000.00 |
0.0801 |
976.2 |
298.15 |
20000.00 |
0.0840 |
975.7 |
298.15 |
20000.00 |
0.0879 |
974.4 |
298.15 |
20000.00 |
0.0926 |
973.2 |
298.15 |
20000.00 |
0.0958 |
972.4 |
298.15 |
20000.00 |
0.1006 |
971.0 |
298.15 |
20000.00 |
0.1111 |
968.0 |
298.15 |
20000.00 |
0.1225 |
964.7 |
298.15 |
20000.00 |
0.1296 |
962.8 |
298.15 |
20000.00 |
0.1402 |
961.3 |
298.15 |
20000.00 |
0.1510 |
956.6 |
298.15 |
20000.00 |
0.1601 |
953.9 |
298.15 |
20000.00 |
0.1703 |
950.9 |
298.15 |
20000.00 |
0.1800 |
948.1 |
298.15 |
20000.00 |
0.1903 |
945.2 |
298.15 |
20000.00 |
0.1996 |
942.3 |
298.15 |
20000.00 |
0.2269 |
934.5 |
298.15 |
20000.00 |
0.2502 |
928.0 |
298.15 |
20000.00 |
0.2745 |
921.3 |
298.15 |
20000.00 |
0.3009 |
914.5 |
298.15 |
20000.00 |
0.3500 |
902.3 |
298.15 |
20000.00 |
0.4034 |
890.4 |
298.15 |
20000.00 |
0.4501 |
880.4 |
298.15 |
20000.00 |
0.4980 |
871.3 |
298.15 |
20000.00 |
0.5501 |
861.9 |
298.15 |
20000.00 |
0.5998 |
853.7 |
298.15 |
20000.00 |
0.6489 |
846.0 |
298.15 |
20000.00 |
0.6967 |
839.0 |
298.15 |
20000.00 |
0.7475 |
832.3 |
298.15 |
20000.00 |
0.7996 |
825.4 |
298.15 |
20000.00 |
0.8484 |
819.3 |
298.15 |
20000.00 |
0.8993 |
813.3 |
298.15 |
20000.00 |
0.9503 |
807.5 |
298.15 |
20000.00 |
1.0000 |
801.9 |
298.15 |
30000.00 |
0.0030 |
1008.5 |
298.15 |
30000.00 |
0.0042 |
1007.4 |
298.15 |
30000.00 |
0.0082 |
1005.9 |
298.15 |
30000.00 |
0.0119 |
1004.3 |
298.15 |
30000.00 |
0.0158 |
1002.4 |
298.15 |
30000.00 |
0.0184 |
1000.9 |
298.15 |
30000.00 |
0.0219 |
1000.1 |
298.15 |
30000.00 |
0.0255 |
998.4 |
298.15 |
30000.00 |
0.0279 |
996.9 |
298.15 |
30000.00 |
0.0315 |
996.1 |
298.15 |
30000.00 |
0.0366 |
993.8 |
298.15 |
30000.00 |
0.0392 |
992.6 |
298.15 |
30000.00 |
0.0439 |
991.2 |
298.15 |
30000.00 |
0.0483 |
989.5 |
298.15 |
30000.00 |
0.0516 |
988.9 |
298.15 |
30000.00 |
0.0559 |
987.7 |
298.15 |
30000.00 |
0.0600 |
986.3 |
298.15 |
30000.00 |
0.0652 |
984.7 |
298.15 |
30000.00 |
0.0679 |
983.9 |
298.15 |
30000.00 |
0.0722 |
982.6 |
298.15 |
30000.00 |
0.0801 |
980.0 |
298.15 |
30000.00 |
0.0840 |
979.5 |
298.15 |
30000.00 |
0.0879 |
978.2 |
298.15 |
30000.00 |
0.0926 |
976.9 |
298.15 |
30000.00 |
0.0958 |
976.1 |
298.15 |
30000.00 |
0.1006 |
974.8 |
298.15 |
30000.00 |
0.1111 |
971.7 |
298.15 |
30000.00 |
0.1225 |
968.5 |
298.15 |
30000.00 |
0.1296 |
966.7 |
298.15 |
30000.00 |
0.1402 |
963.7 |
298.15 |
30000.00 |
0.1510 |
960.5 |
298.15 |
30000.00 |
0.1601 |
957.9 |
298.15 |
30000.00 |
0.1703 |
955.0 |
298.15 |
30000.00 |
0.1800 |
952.2 |
298.15 |
30000.00 |
0.1903 |
949.3 |
298.15 |
30000.00 |
0.1996 |
946.5 |
298.15 |
30000.00 |
0.2269 |
938.7 |
298.15 |
30000.00 |
0.2502 |
932.4 |
298.15 |
30000.00 |
0.2745 |
925.9 |
298.15 |
30000.00 |
0.3009 |
919.2 |
298.15 |
30000.00 |
0.3500 |
907.2 |
298.15 |
30000.00 |
0.4034 |
895.5 |
298.15 |
30000.00 |
0.4501 |
885.7 |
298.15 |
30000.00 |
0.4980 |
876.8 |
298.15 |
30000.00 |
0.5501 |
867.6 |
298.15 |
30000.00 |
0.5998 |
859.5 |
298.15 |
30000.00 |
0.6489 |
852.0 |
298.15 |
30000.00 |
0.6967 |
845.1 |
298.15 |
30000.00 |
0.7475 |
838.5 |
298.15 |
30000.00 |
0.7996 |
831.9 |
298.15 |
30000.00 |
0.8484 |
825.9 |
298.15 |
30000.00 |
0.8993 |
820.0 |
298.15 |
30000.00 |
0.9503 |
814.5 |
298.15 |
30000.00 |
1.0000 |
808.9 |
298.15 |
40000.00 |
0.0030 |
1012.7 |
298.15 |
40000.00 |
0.0042 |
1011.5 |
298.15 |
40000.00 |
0.0082 |
1010.0 |
298.15 |
40000.00 |
0.0119 |
1008.3 |
298.15 |
40000.00 |
0.0158 |
1006.4 |
298.15 |
40000.00 |
0.0184 |
1005.0 |
298.15 |
40000.00 |
0.0219 |
1004.1 |
298.15 |
40000.00 |
0.0255 |
1002.4 |
298.15 |
40000.00 |
0.0279 |
1000.8 |
298.15 |
40000.00 |
0.0315 |
1000.0 |
298.15 |
40000.00 |
0.0366 |
997.6 |
298.15 |
40000.00 |
0.0392 |
996.4 |
298.15 |
40000.00 |
0.0439 |
995.1 |
298.15 |
40000.00 |
0.0483 |
993.3 |
298.15 |
40000.00 |
0.0516 |
992.7 |
298.15 |
40000.00 |
0.0559 |
991.5 |
298.15 |
40000.00 |
0.0600 |
990.1 |
298.15 |
40000.00 |
0.0652 |
988.4 |
298.15 |
40000.00 |
0.0679 |
987.6 |
298.15 |
40000.00 |
0.0722 |
986.3 |
298.15 |
40000.00 |
0.0801 |
983.7 |
298.15 |
40000.00 |
0.0840 |
983.2 |
298.15 |
40000.00 |
0.0879 |
981.9 |
298.15 |
40000.00 |
0.0926 |
980.6 |
298.15 |
40000.00 |
0.0958 |
979.8 |
298.15 |
40000.00 |
0.1006 |
978.5 |
298.15 |
40000.00 |
0.1111 |
975.4 |
298.15 |
40000.00 |
0.1225 |
972.2 |
298.15 |
40000.00 |
0.1296 |
970.4 |
298.15 |
40000.00 |
0.1402 |
967.3 |
298.15 |
40000.00 |
0.1510 |
964.3 |
298.15 |
40000.00 |
0.1601 |
961.7 |
298.15 |
40000.00 |
0.1703 |
958.9 |
298.15 |
40000.00 |
0.1800 |
956.2 |
298.15 |
40000.00 |
0.1903 |
953.3 |
298.15 |
40000.00 |
0.1996 |
950.5 |
298.15 |
40000.00 |
0.2269 |
942.9 |
298.15 |
40000.00 |
0.2502 |
936.7 |
298.15 |
40000.00 |
0.2745 |
930.3 |
298.15 |
40000.00 |
0.3009 |
923.7 |
298.15 |
40000.00 |
0.3500 |
911.9 |
298.15 |
40000.00 |
0.4034 |
900.4 |
298.15 |
40000.00 |
0.4501 |
890.8 |
298.15 |
40000.00 |
0.4980 |
882.0 |
298.15 |
40000.00 |
0.5501 |
873.0 |
298.15 |
40000.00 |
0.5998 |
865.1 |
298.15 |
40000.00 |
0.6489 |
857.7 |
298.15 |
40000.00 |
0.6967 |
851.0 |
298.15 |
40000.00 |
0.7475 |
844.5 |
298.15 |
40000.00 |
0.7996 |
838.1 |
298.15 |
40000.00 |
0.8484 |
832.3 |
298.15 |
40000.00 |
0.8993 |
826.5 |
298.15 |
40000.00 |
0.9503 |
821.0 |
298.15 |
40000.00 |
1.0000 |
815.7 |
323.15 |
100.00 |
0.0030 |
986.5 |
323.15 |
100.00 |
0.0042 |
985.4 |
323.15 |
100.00 |
0.0082 |
984.0 |
323.15 |
100.00 |
0.0119 |
982.7 |
323.15 |
100.00 |
0.0158 |
980.5 |
323.15 |
100.00 |
0.0184 |
979.2 |
323.15 |
100.00 |
0.0219 |
978.0 |
323.15 |
100.00 |
0.0255 |
976.5 |
323.15 |
100.00 |
0.0279 |
974.8 |
323.15 |
100.00 |
0.0315 |
973.9 |
323.15 |
100.00 |
0.0366 |
971.4 |
323.15 |
100.00 |
0.0392 |
970.2 |
323.15 |
100.00 |
0.0439 |
968.6 |
323.15 |
100.00 |
0.0483 |
966.6 |
323.15 |
100.00 |
0.0516 |
965.9 |
323.15 |
100.00 |
0.0559 |
964.5 |
323.15 |
100.00 |
0.0600 |
962.9 |
323.15 |
100.00 |
0.0652 |
960.9 |
323.15 |
100.00 |
0.0679 |
960.2 |
323.15 |
100.00 |
0.0722 |
958.3 |
323.15 |
100.00 |
0.0801 |
955.1 |
323.15 |
100.00 |
0.0840 |
954.7 |
323.15 |
100.00 |
0.0879 |
952.9 |
323.15 |
100.00 |
0.0926 |
951.4 |
323.15 |
100.00 |
0.0958 |
950.1 |
323.15 |
100.00 |
0.1006 |
948.5 |
323.15 |
100.00 |
0.1111 |
944.7 |
323.15 |
100.00 |
0.1225 |
940.6 |
323.15 |
100.00 |
0.1296 |
938.2 |
323.15 |
100.00 |
0.1402 |
934.5 |
323.15 |
100.00 |
0.1510 |
930.7 |
323.15 |
100.00 |
0.1601 |
927.5 |
323.15 |
100.00 |
0.1703 |
924.0 |
323.15 |
100.00 |
0.1800 |
920.6 |
323.15 |
100.00 |
0.1903 |
917.3 |
323.15 |
100.00 |
0.1996 |
914.1 |
323.15 |
100.00 |
0.2269 |
905.2 |
323.15 |
100.00 |
0.2502 |
898.1 |
323.15 |
100.00 |
0.2745 |
890.8 |
323.15 |
100.00 |
0.3009 |
883.5 |
323.15 |
100.00 |
0.3500 |
870.2 |
323.15 |
100.00 |
0.4034 |
857.3 |
323.15 |
100.00 |
0.4501 |
846.7 |
323.15 |
100.00 |
0.4980 |
837.0 |
323.15 |
100.00 |
0.5501 |
826.9 |
323.15 |
100.00 |
0.5998 |
818.4 |
323.15 |
100.00 |
0.6489 |
810.1 |
323.15 |
100.00 |
0.6967 |
802.8 |
323.15 |
100.00 |
0.7475 |
795.4 |
323.15 |
100.00 |
0.7996 |
788.4 |
323.15 |
100.00 |
0.8484 |
781.9 |
323.15 |
100.00 |
0.8993 |
775.6 |
323.15 |
100.00 |
0.9503 |
769.5 |
323.15 |
100.00 |
1.0000 |
763.7 |
323.15 |
10000.00 |
0.0030 |
990.8 |
323.15 |
10000.00 |
0.0042 |
989.6 |
323.15 |
10000.00 |
0.0082 |
988.2 |
323.15 |
10000.00 |
0.0119 |
986.9 |
323.15 |
10000.00 |
0.0158 |
984.7 |
323.15 |
10000.00 |
0.0184 |
983.3 |
323.15 |
10000.00 |
0.0219 |
982.2 |
323.15 |
10000.00 |
0.0255 |
980.6 |
323.15 |
10000.00 |
0.0279 |
979.0 |
323.15 |
10000.00 |
0.0315 |
978.1 |
323.15 |
10000.00 |
0.0366 |
975.6 |
323.15 |
10000.00 |
0.0392 |
974.3 |
323.15 |
10000.00 |
0.0439 |
972.8 |
323.15 |
10000.00 |
0.0483 |
970.7 |
323.15 |
10000.00 |
0.0516 |
970.0 |
323.15 |
10000.00 |
0.0559 |
968.6 |
323.15 |
10000.00 |
0.0600 |
967.1 |
323.15 |
10000.00 |
0.0652 |
965.0 |
323.15 |
10000.00 |
0.0679 |
964.3 |
323.15 |
10000.00 |
0.0722 |
962.5 |
323.15 |
10000.00 |
0.0801 |
959.3 |
323.15 |
10000.00 |
0.0840 |
958.9 |
323.15 |
10000.00 |
0.0879 |
957.1 |
323.15 |
10000.00 |
0.0926 |
955.5 |
323.15 |
10000.00 |
0.0958 |
954.4 |
323.15 |
10000.00 |
0.1006 |
952.8 |
323.15 |
10000.00 |
0.1111 |
949.0 |
323.15 |
10000.00 |
0.1225 |
945.1 |
323.15 |
10000.00 |
0.1296 |
942.6 |
323.15 |
10000.00 |
0.1402 |
939.0 |
323.15 |
10000.00 |
0.1510 |
935.2 |
323.15 |
10000.00 |
0.1601 |
932.2 |
323.15 |
10000.00 |
0.1703 |
928.8 |
323.15 |
10000.00 |
0.1800 |
925.5 |
323.15 |
10000.00 |
0.1903 |
922.1 |
323.15 |
10000.00 |
0.1996 |
919.0 |
323.15 |
10000.00 |
0.2269 |
910.3 |
323.15 |
10000.00 |
0.2502 |
903.4 |
323.15 |
10000.00 |
0.2745 |
896.3 |
323.15 |
10000.00 |
0.3009 |
889.2 |
323.15 |
10000.00 |
0.3500 |
876.2 |
323.15 |
10000.00 |
0.4034 |
863.7 |
323.15 |
10000.00 |
0.4501 |
853.3 |
323.15 |
10000.00 |
0.4980 |
843.9 |
323.15 |
10000.00 |
0.5501 |
834.3 |
323.15 |
10000.00 |
0.5998 |
826.3 |
323.15 |
10000.00 |
0.6489 |
817.9 |
323.15 |
10000.00 |
0.6967 |
810.9 |
323.15 |
10000.00 |
0.7475 |
803.8 |
323.15 |
10000.00 |
0.7996 |
796.9 |
323.15 |
10000.00 |
0.8484 |
790.8 |
323.15 |
10000.00 |
0.8993 |
784.7 |
323.15 |
10000.00 |
0.9503 |
779.0 |
323.15 |
10000.00 |
1.0000 |
773.4 |
323.15 |
20000.00 |
0.0030 |
994.9 |
323.15 |
20000.00 |
0.0042 |
993.9 |
323.15 |
20000.00 |
0.0082 |
992.4 |
323.15 |
20000.00 |
0.0119 |
991.1 |
323.15 |
20000.00 |
0.0158 |
988.9 |
323.15 |
20000.00 |
0.0184 |
987.5 |
323.15 |
20000.00 |
0.0219 |
986.3 |
323.15 |
20000.00 |
0.0255 |
984.7 |
323.15 |
20000.00 |
0.0279 |
983.1 |
323.15 |
20000.00 |
0.0315 |
982.2 |
323.15 |
20000.00 |
0.0366 |
979.6 |
323.15 |
20000.00 |
0.0392 |
978.4 |
323.15 |
20000.00 |
0.0439 |
976.8 |
323.15 |
20000.00 |
0.0483 |
974.8 |
323.15 |
20000.00 |
0.0516 |
974.0 |
323.15 |
20000.00 |
0.0559 |
972.7 |
323.15 |
20000.00 |
0.0600 |
971.2 |
323.15 |
20000.00 |
0.0652 |
969.1 |
323.15 |
20000.00 |
0.0679 |
968.3 |
323.15 |
20000.00 |
0.0722 |
966.6 |
323.15 |
20000.00 |
0.0801 |
963.4 |
323.15 |
20000.00 |
0.0840 |
963.0 |
323.15 |
20000.00 |
0.0879 |
961.2 |
323.15 |
20000.00 |
0.0926 |
959.6 |
323.15 |
20000.00 |
0.0958 |
958.5 |
323.15 |
20000.00 |
0.1006 |
956.9 |
323.15 |
20000.00 |
0.1111 |
953.2 |
323.15 |
20000.00 |
0.1225 |
949.2 |
323.15 |
20000.00 |
0.1296 |
946.9 |
323.15 |
20000.00 |
0.1402 |
943.3 |
323.15 |
20000.00 |
0.1510 |
939.7 |
323.15 |
20000.00 |
0.1601 |
936.7 |
323.15 |
20000.00 |
0.1703 |
933.3 |
323.15 |
20000.00 |
0.1800 |
930.1 |
323.15 |
20000.00 |
0.1903 |
926.8 |
323.15 |
20000.00 |
0.1996 |
923.8 |
323.15 |
20000.00 |
0.2269 |
915.3 |
323.15 |
20000.00 |
0.2502 |
908.5 |
323.15 |
20000.00 |
0.2745 |
901.6 |
323.15 |
20000.00 |
0.3009 |
894.7 |
323.15 |
20000.00 |
0.3500 |
882.1 |
323.15 |
20000.00 |
0.4034 |
869.8 |
323.15 |
20000.00 |
0.4501 |
859.7 |
323.15 |
20000.00 |
0.4980 |
850.6 |
323.15 |
20000.00 |
0.5501 |
841.2 |
323.15 |
20000.00 |
0.5998 |
833.5 |
323.15 |
20000.00 |
0.6489 |
825.3 |
323.15 |
20000.00 |
0.6967 |
818.4 |
323.15 |
20000.00 |
0.7475 |
811.7 |
323.15 |
20000.00 |
0.7996 |
804.9 |
323.15 |
20000.00 |
0.8484 |
799.1 |
323.15 |
20000.00 |
0.8993 |
793.2 |
323.15 |
20000.00 |
0.9503 |
787.7 |
323.15 |
20000.00 |
1.0000 |
782.3 |
323.15 |
30000.00 |
0.0030 |
999.0 |
323.15 |
30000.00 |
0.0042 |
998.0 |
323.15 |
30000.00 |
0.0082 |
996.5 |
323.15 |
30000.00 |
0.0119 |
995.2 |
323.15 |
30000.00 |
0.0158 |
993.0 |
323.15 |
30000.00 |
0.0184 |
991.5 |
323.15 |
30000.00 |
0.0219 |
990.4 |
323.15 |
30000.00 |
0.0255 |
988.7 |
323.15 |
30000.00 |
0.0279 |
987.1 |
323.15 |
30000.00 |
0.0315 |
986.3 |
323.15 |
30000.00 |
0.0366 |
983.6 |
323.15 |
30000.00 |
0.0392 |
982.4 |
323.15 |
30000.00 |
0.0439 |
980.8 |
323.15 |
30000.00 |
0.0483 |
978.8 |
323.15 |
30000.00 |
0.0516 |
978.0 |
323.15 |
30000.00 |
0.0559 |
976.6 |
323.15 |
30000.00 |
0.0600 |
975.1 |
323.15 |
30000.00 |
0.0652 |
973.1 |
323.15 |
30000.00 |
0.0679 |
972.3 |
323.15 |
30000.00 |
0.0722 |
970.5 |
323.15 |
30000.00 |
0.0801 |
967.4 |
323.15 |
30000.00 |
0.0840 |
967.0 |
323.15 |
30000.00 |
0.0879 |
965.3 |
323.15 |
30000.00 |
0.0926 |
963.7 |
323.15 |
30000.00 |
0.0958 |
962.6 |
323.15 |
30000.00 |
0.1006 |
961.0 |
323.15 |
30000.00 |
0.1111 |
957.3 |
323.15 |
30000.00 |
0.1225 |
953.4 |
323.15 |
30000.00 |
0.1296 |
951.1 |
323.15 |
30000.00 |
0.1402 |
947.6 |
323.15 |
30000.00 |
0.1510 |
944.0 |
323.15 |
30000.00 |
0.1601 |
941.1 |
323.15 |
30000.00 |
0.1703 |
937.7 |
323.15 |
30000.00 |
0.1800 |
934.6 |
323.15 |
30000.00 |
0.1903 |
931.4 |
323.15 |
30000.00 |
0.1996 |
928.4 |
323.15 |
30000.00 |
0.2269 |
920.1 |
323.15 |
30000.00 |
0.2502 |
913.5 |
323.15 |
30000.00 |
0.2745 |
906.7 |
323.15 |
30000.00 |
0.3009 |
899.8 |
323.15 |
30000.00 |
0.3500 |
887.5 |
323.15 |
30000.00 |
0.4034 |
875.5 |
323.15 |
30000.00 |
0.4501 |
865.7 |
323.15 |
30000.00 |
0.4980 |
856.8 |
323.15 |
30000.00 |
0.5501 |
847.6 |
323.15 |
30000.00 |
0.5998 |
839.6 |
323.15 |
30000.00 |
0.6489 |
832.1 |
323.15 |
30000.00 |
0.6967 |
825.4 |
323.15 |
30000.00 |
0.7475 |
818.8 |
323.15 |
30000.00 |
0.7996 |
812.3 |
323.15 |
30000.00 |
0.8484 |
806.6 |
323.15 |
30000.00 |
0.8993 |
800.9 |
323.15 |
30000.00 |
0.9503 |
795.6 |
323.15 |
30000.00 |
1.0000 |
790.3 |
323.15 |
40000.00 |
0.0030 |
1003.1 |
323.15 |
40000.00 |
0.0042 |
1002.0 |
323.15 |
40000.00 |
0.0082 |
1000.5 |
323.15 |
40000.00 |
0.0119 |
999.2 |
323.15 |
40000.00 |
0.0158 |
996.9 |
323.15 |
40000.00 |
0.0184 |
995.5 |
323.15 |
40000.00 |
0.0219 |
994.4 |
323.15 |
40000.00 |
0.0255 |
992.7 |
323.15 |
40000.00 |
0.0279 |
991.1 |
323.15 |
40000.00 |
0.0315 |
990.2 |
323.15 |
40000.00 |
0.0366 |
987.6 |
323.15 |
40000.00 |
0.0392 |
986.3 |
323.15 |
40000.00 |
0.0439 |
984.7 |
323.15 |
40000.00 |
0.0483 |
982.7 |
323.15 |
40000.00 |
0.0516 |
982.0 |
323.15 |
40000.00 |
0.0559 |
980.5 |
323.15 |
40000.00 |
0.0600 |
979.1 |
323.15 |
40000.00 |
0.0652 |
977.0 |
323.15 |
40000.00 |
0.0679 |
976.3 |
323.15 |
40000.00 |
0.0722 |
974.4 |
323.15 |
40000.00 |
0.0801 |
971.4 |
323.15 |
40000.00 |
0.0840 |
970.9 |
323.15 |
40000.00 |
0.0879 |
969.2 |
323.15 |
40000.00 |
0.0926 |
967.6 |
323.15 |
40000.00 |
0.0958 |
966.5 |
323.15 |
40000.00 |
0.1006 |
964.9 |
323.15 |
40000.00 |
0.1111 |
961.3 |
323.15 |
40000.00 |
0.1225 |
957.4 |
323.15 |
40000.00 |
0.1296 |
955.2 |
323.15 |
40000.00 |
0.1402 |
951.7 |
323.15 |
40000.00 |
0.1510 |
948.2 |
323.15 |
40000.00 |
0.1601 |
945.3 |
323.15 |
40000.00 |
0.1703 |
942.0 |
323.15 |
40000.00 |
0.1800 |
938.9 |
323.15 |
40000.00 |
0.1903 |
935.8 |
323.15 |
40000.00 |
0.1996 |
932.9 |
323.15 |
40000.00 |
0.2269 |
924.7 |
323.15 |
40000.00 |
0.2502 |
918.2 |
323.15 |
40000.00 |
0.2745 |
911.5 |
323.15 |
40000.00 |
0.3009 |
904.8 |
323.15 |
40000.00 |
0.3500 |
892.7 |
323.15 |
40000.00 |
0.4034 |
881.0 |
323.15 |
40000.00 |
0.4501 |
871.3 |
323.15 |
40000.00 |
0.4980 |
862.6 |
323.15 |
40000.00 |
0.5501 |
853.6 |
323.15 |
40000.00 |
0.5998 |
845.8 |
323.15 |
40000.00 |
0.6489 |
838.5 |
323.15 |
40000.00 |
0.6967 |
831.9 |
323.15 |
40000.00 |
0.7475 |
825.5 |
323.15 |
40000.00 |
0.7996 |
819.1 |
323.15 |
40000.00 |
0.8484 |
813.6 |
323.15 |
40000.00 |
0.8993 |
808.0 |
323.15 |
40000.00 |
0.9503 |
802.8 |
323.15 |
40000.00 |
1.0000 |
797.7 |
348.15 |
100.00 |
0.0030 |
973.1 |
348.15 |
100.00 |
0.0042 |
971.9 |
348.15 |
100.00 |
0.0082 |
970.7 |
348.15 |
100.00 |
0.0119 |
969.1 |
348.15 |
100.00 |
0.0158 |
966.6 |
348.15 |
100.00 |
0.0184 |
965.4 |
348.15 |
100.00 |
0.0219 |
963.9 |
348.15 |
100.00 |
0.0255 |
962.0 |
348.15 |
100.00 |
0.0279 |
960.4 |
348.15 |
100.00 |
0.0315 |
959.4 |
348.15 |
100.00 |
0.0366 |
956.7 |
348.15 |
100.00 |
0.0392 |
955.3 |
348.15 |
100.00 |
0.0439 |
953.5 |
348.15 |
100.00 |
0.0483 |
951.2 |
348.15 |
100.00 |
0.0516 |
950.2 |
348.15 |
100.00 |
0.0559 |
948.8 |
348.15 |
100.00 |
0.0600 |
946.9 |
348.15 |
100.00 |
0.0652 |
944.8 |
348.15 |
100.00 |
0.0679 |
943.7 |
348.15 |
100.00 |
0.0722 |
941.5 |
348.15 |
100.00 |
0.0801 |
938.1 |
348.15 |
100.00 |
0.0840 |
937.5 |
348.15 |
100.00 |
0.0879 |
935.3 |
348.15 |
100.00 |
0.0926 |
933.6 |
348.15 |
100.00 |
0.0958 |
932.2 |
348.15 |
100.00 |
0.1006 |
930.2 |
348.15 |
100.00 |
0.1111 |
925.9 |
348.15 |
100.00 |
0.1225 |
921.5 |
348.15 |
100.00 |
0.1296 |
918.7 |
348.15 |
100.00 |
0.1402 |
914.6 |
348.15 |
100.00 |
0.1510 |
910.4 |
348.15 |
100.00 |
0.1601 |
906.9 |
348.15 |
100.00 |
0.1703 |
903.1 |
348.15 |
100.00 |
0.1800 |
899.5 |
348.15 |
100.00 |
0.1903 |
895.8 |
348.15 |
100.00 |
0.1996 |
892.6 |
348.15 |
100.00 |
0.2269 |
883.1 |
348.15 |
100.00 |
0.2502 |
875.6 |
348.15 |
100.00 |
0.2745 |
868.0 |
348.15 |
100.00 |
0.3009 |
860.4 |
348.15 |
100.00 |
0.3500 |
846.7 |
348.15 |
100.00 |
0.4034 |
833.4 |
348.15 |
100.00 |
0.4501 |
822.7 |
348.15 |
100.00 |
0.4980 |
812.7 |
348.15 |
100.00 |
0.5501 |
802.6 |
348.15 |
100.00 |
0.5998 |
793.8 |
348.15 |
100.00 |
0.6489 |
785.6 |
348.15 |
100.00 |
0.6967 |
778.2 |
348.15 |
100.00 |
0.7475 |
770.9 |
348.15 |
100.00 |
0.7996 |
763.9 |
348.15 |
100.00 |
0.8484 |
757.6 |
348.15 |
100.00 |
0.8993 |
751.5 |
348.15 |
100.00 |
0.9503 |
745.7 |
348.15 |
100.00 |
1.0000 |
739.4 |
348.15 |
10000.00 |
0.0030 |
977.5 |
348.15 |
10000.00 |
0.0042 |
976.3 |
348.15 |
10000.00 |
0.0082 |
975.0 |
348.15 |
10000.00 |
0.0119 |
973.4 |
348.15 |
10000.00 |
0.0158 |
971.0 |
348.15 |
10000.00 |
0.0184 |
969.6 |
348.15 |
10000.00 |
0.0219 |
968.2 |
348.15 |
10000.00 |
0.0255 |
966.4 |
348.15 |
10000.00 |
0.0279 |
964.8 |
348.15 |
10000.00 |
0.0315 |
963.8 |
348.15 |
10000.00 |
0.0366 |
961.0 |
348.15 |
10000.00 |
0.0392 |
959.6 |
348.15 |
10000.00 |
0.0439 |
957.8 |
348.15 |
10000.00 |
0.0483 |
955.6 |
348.15 |
10000.00 |
0.0516 |
954.6 |
348.15 |
10000.00 |
0.0559 |
953.2 |
348.15 |
10000.00 |
0.0600 |
951.3 |
348.15 |
10000.00 |
0.0652 |
949.1 |
348.15 |
10000.00 |
0.0679 |
948.2 |
348.15 |
10000.00 |
0.0722 |
946.1 |
348.15 |
10000.00 |
0.0801 |
942.6 |
348.15 |
10000.00 |
0.0840 |
941.9 |
348.15 |
10000.00 |
0.0879 |
939.9 |
348.15 |
10000.00 |
0.0926 |
938.1 |
348.15 |
10000.00 |
0.0958 |
936.8 |
348.15 |
10000.00 |
0.1006 |
934.9 |
348.15 |
10000.00 |
0.1111 |
930.7 |
348.15 |
10000.00 |
0.1225 |
926.3 |
348.15 |
10000.00 |
0.1296 |
923.6 |
348.15 |
10000.00 |
0.1402 |
919.5 |
348.15 |
10000.00 |
0.1510 |
915.4 |
348.15 |
10000.00 |
0.1601 |
912.1 |
348.15 |
10000.00 |
0.1703 |
908.4 |
348.15 |
10000.00 |
0.1800 |
904.8 |
348.15 |
10000.00 |
0.1903 |
901.3 |
348.15 |
10000.00 |
0.1996 |
898.1 |
348.15 |
10000.00 |
0.2269 |
888.9 |
348.15 |
10000.00 |
0.2502 |
881.6 |
348.15 |
10000.00 |
0.2745 |
874.2 |
348.15 |
10000.00 |
0.3009 |
866.8 |
348.15 |
10000.00 |
0.3500 |
853.6 |
348.15 |
10000.00 |
0.4034 |
840.7 |
348.15 |
10000.00 |
0.4501 |
830.3 |
348.15 |
10000.00 |
0.4980 |
820.7 |
348.15 |
10000.00 |
0.5501 |
811.0 |
348.15 |
10000.00 |
0.5998 |
802.5 |
348.15 |
10000.00 |
0.6489 |
794.6 |
348.15 |
10000.00 |
0.6967 |
787.6 |
348.15 |
10000.00 |
0.7475 |
780.7 |
348.15 |
10000.00 |
0.7996 |
774.0 |
348.15 |
10000.00 |
0.8484 |
768.0 |
348.15 |
10000.00 |
0.8993 |
762.1 |
348.15 |
10000.00 |
0.9503 |
756.7 |
348.15 |
10000.00 |
1.0000 |
751.2 |
348.15 |
20000.00 |
0.0030 |
981.9 |
348.15 |
20000.00 |
0.0042 |
980.6 |
348.15 |
20000.00 |
0.0082 |
979.4 |
348.15 |
20000.00 |
0.0119 |
977.7 |
348.15 |
20000.00 |
0.0158 |
975.3 |
348.15 |
20000.00 |
0.0184 |
973.9 |
348.15 |
20000.00 |
0.0219 |
972.6 |
348.15 |
20000.00 |
0.0255 |
970.7 |
348.15 |
20000.00 |
0.0279 |
969.1 |
348.15 |
20000.00 |
0.0315 |
968.0 |
348.15 |
20000.00 |
0.0366 |
965.3 |
348.15 |
20000.00 |
0.0392 |
963.8 |
348.15 |
20000.00 |
0.0439 |
962.1 |
348.15 |
20000.00 |
0.0483 |
959.9 |
348.15 |
20000.00 |
0.0516 |
958.9 |
348.15 |
20000.00 |
0.0559 |
957.5 |
348.15 |
20000.00 |
0.0600 |
955.8 |
348.15 |
20000.00 |
0.0652 |
953.5 |
348.15 |
20000.00 |
0.0679 |
952.5 |
348.15 |
20000.00 |
0.0722 |
950.4 |
348.15 |
20000.00 |
0.0801 |
947.0 |
348.15 |
20000.00 |
0.0840 |
946.3 |
348.15 |
20000.00 |
0.0879 |
944.4 |
348.15 |
20000.00 |
0.0926 |
942.6 |
348.15 |
20000.00 |
0.0958 |
941.3 |
348.15 |
20000.00 |
0.1006 |
939.4 |
348.15 |
20000.00 |
0.1111 |
935.3 |
348.15 |
20000.00 |
0.1225 |
931.1 |
348.15 |
20000.00 |
0.1296 |
928.3 |
348.15 |
20000.00 |
0.1402 |
924.4 |
348.15 |
20000.00 |
0.1510 |
920.3 |
348.15 |
20000.00 |
0.1601 |
917.1 |
348.15 |
20000.00 |
0.1703 |
913.5 |
348.15 |
20000.00 |
0.1800 |
910.0 |
348.15 |
20000.00 |
0.1903 |
906.5 |
348.15 |
20000.00 |
0.1996 |
903.4 |
348.15 |
20000.00 |
0.2269 |
894.4 |
348.15 |
20000.00 |
0.2502 |
887.3 |
348.15 |
20000.00 |
0.2745 |
880.2 |
348.15 |
20000.00 |
0.3009 |
872.9 |
348.15 |
20000.00 |
0.3500 |
860.0 |
348.15 |
20000.00 |
0.4034 |
847.5 |
348.15 |
20000.00 |
0.4501 |
837.4 |
348.15 |
20000.00 |
0.4980 |
828.1 |
348.15 |
20000.00 |
0.5501 |
818.7 |
348.15 |
20000.00 |
0.5998 |
810.5 |
348.15 |
20000.00 |
0.6489 |
802.9 |
348.15 |
20000.00 |
0.6967 |
796.1 |
348.15 |
20000.00 |
0.7475 |
789.4 |
348.15 |
20000.00 |
0.7996 |
783.0 |
348.15 |
20000.00 |
0.8484 |
777.3 |
348.15 |
20000.00 |
0.8993 |
771.6 |
348.15 |
20000.00 |
0.9503 |
766.4 |
348.15 |
20000.00 |
1.0000 |
761.2 |
348.15 |
30000.00 |
0.0030 |
986.1 |
348.15 |
30000.00 |
0.0042 |
984.8 |
348.15 |
30000.00 |
0.0082 |
983.6 |
348.15 |
30000.00 |
0.0119 |
981.9 |
348.15 |
30000.00 |
0.0158 |
979.4 |
348.15 |
30000.00 |
0.0184 |
978.1 |
348.15 |
30000.00 |
0.0219 |
976.7 |
348.15 |
30000.00 |
0.0255 |
975.0 |
348.15 |
30000.00 |
0.0279 |
973.3 |
348.15 |
30000.00 |
0.0315 |
972.3 |
348.15 |
30000.00 |
0.0366 |
969.5 |
348.15 |
30000.00 |
0.0392 |
968.1 |
348.15 |
30000.00 |
0.0439 |
966.3 |
348.15 |
30000.00 |
0.0483 |
964.1 |
348.15 |
30000.00 |
0.0516 |
963.2 |
348.15 |
30000.00 |
0.0559 |
961.7 |
348.15 |
30000.00 |
0.0600 |
960.0 |
348.15 |
30000.00 |
0.0652 |
957.8 |
348.15 |
30000.00 |
0.0679 |
956.8 |
348.15 |
30000.00 |
0.0722 |
954.7 |
348.15 |
30000.00 |
0.0801 |
951.3 |
348.15 |
30000.00 |
0.0840 |
950.7 |
348.15 |
30000.00 |
0.0879 |
948.8 |
348.15 |
30000.00 |
0.0926 |
947.0 |
348.15 |
30000.00 |
0.0958 |
945.7 |
348.15 |
30000.00 |
0.1006 |
943.9 |
348.15 |
30000.00 |
0.1111 |
939.8 |
348.15 |
30000.00 |
0.1225 |
935.6 |
348.15 |
30000.00 |
0.1296 |
932.9 |
348.15 |
30000.00 |
0.1402 |
929.1 |
348.15 |
30000.00 |
0.1510 |
925.1 |
348.15 |
30000.00 |
0.1601 |
922.0 |
348.15 |
30000.00 |
0.1703 |
918.4 |
348.15 |
30000.00 |
0.1800 |
915.0 |
348.15 |
30000.00 |
0.1903 |
911.6 |
348.15 |
30000.00 |
0.1996 |
908.5 |
348.15 |
30000.00 |
0.2269 |
899.7 |
348.15 |
30000.00 |
0.2502 |
892.8 |
348.15 |
30000.00 |
0.2745 |
885.8 |
348.15 |
30000.00 |
0.3009 |
878.6 |
348.15 |
30000.00 |
0.3500 |
866.2 |
348.15 |
30000.00 |
0.4034 |
854.0 |
348.15 |
30000.00 |
0.4501 |
844.2 |
348.15 |
30000.00 |
0.4980 |
835.1 |
348.15 |
30000.00 |
0.5501 |
825.9 |
348.15 |
30000.00 |
0.5998 |
818.0 |
348.15 |
30000.00 |
0.6489 |
810.6 |
348.15 |
30000.00 |
0.6967 |
804.0 |
348.15 |
30000.00 |
0.7475 |
797.6 |
348.15 |
30000.00 |
0.7996 |
791.3 |
348.15 |
30000.00 |
0.8484 |
785.8 |
348.15 |
30000.00 |
0.8993 |
780.3 |
348.15 |
30000.00 |
0.9503 |
775.2 |
348.15 |
30000.00 |
1.0000 |
770.3 |
348.15 |
40000.00 |
0.0030 |
990.1 |
348.15 |
40000.00 |
0.0042 |
988.8 |
348.15 |
40000.00 |
0.0082 |
987.6 |
348.15 |
40000.00 |
0.0119 |
986.0 |
348.15 |
40000.00 |
0.0158 |
983.5 |
348.15 |
40000.00 |
0.0184 |
982.1 |
348.15 |
40000.00 |
0.0219 |
980.8 |
348.15 |
40000.00 |
0.0255 |
979.0 |
348.15 |
40000.00 |
0.0279 |
977.3 |
348.15 |
40000.00 |
0.0315 |
976.3 |
348.15 |
40000.00 |
0.0366 |
973.6 |
348.15 |
40000.00 |
0.0392 |
972.1 |
348.15 |
40000.00 |
0.0439 |
970.4 |
348.15 |
40000.00 |
0.0483 |
968.2 |
348.15 |
40000.00 |
0.0516 |
967.3 |
348.15 |
40000.00 |
0.0559 |
965.9 |
348.15 |
40000.00 |
0.0600 |
964.1 |
348.15 |
40000.00 |
0.0652 |
961.9 |
348.15 |
40000.00 |
0.0679 |
960.9 |
348.15 |
40000.00 |
0.0722 |
958.9 |
348.15 |
40000.00 |
0.0801 |
955.6 |
348.15 |
40000.00 |
0.0840 |
954.9 |
348.15 |
40000.00 |
0.0879 |
953.0 |
348.15 |
40000.00 |
0.0926 |
951.3 |
348.15 |
40000.00 |
0.0958 |
950.0 |
348.15 |
40000.00 |
0.1006 |
948.1 |
348.15 |
40000.00 |
0.1111 |
944.2 |
348.15 |
40000.00 |
0.1225 |
940.0 |
348.15 |
40000.00 |
0.1296 |
937.4 |
348.15 |
40000.00 |
0.1402 |
933.7 |
348.15 |
40000.00 |
0.1510 |
929.7 |
348.15 |
40000.00 |
0.1601 |
926.6 |
348.15 |
40000.00 |
0.1703 |
923.1 |
348.15 |
40000.00 |
0.1800 |
919.8 |
348.15 |
40000.00 |
0.1903 |
916.4 |
348.15 |
40000.00 |
0.1996 |
913.4 |
348.15 |
40000.00 |
0.2269 |
904.8 |
348.15 |
40000.00 |
0.2502 |
898.1 |
348.15 |
40000.00 |
0.2745 |
891.1 |
348.15 |
40000.00 |
0.3009 |
884.2 |
348.15 |
40000.00 |
0.3500 |
872.0 |
348.15 |
40000.00 |
0.4034 |
860.0 |
348.15 |
40000.00 |
0.4501 |
850.5 |
348.15 |
40000.00 |
0.4980 |
841.6 |
348.15 |
40000.00 |
0.5501 |
832.7 |
348.15 |
40000.00 |
0.5998 |
824.9 |
348.15 |
40000.00 |
0.6489 |
817.8 |
348.15 |
40000.00 |
0.6967 |
811.3 |
348.15 |
40000.00 |
0.7475 |
805.1 |
348.15 |
40000.00 |
0.7996 |
799.0 |
348.15 |
40000.00 |
0.8484 |
793.6 |
348.15 |
40000.00 |
0.8993 |
788.3 |
348.15 |
40000.00 |
0.9503 |
783.4 |
348.15 |
40000.00 |
1.0000 |
778.6 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Pressure, kPa - Liquid |
Temperature, K - Liquid |
Mole fraction of Ethanol (1) - Liquid |
Mass density, kg/m3 - Liquid |
39170.00 |
297.05 |
0.0163 |
1006.1 |
30810.00 |
297.05 |
0.0163 |
1003.2 |
21070.00 |
297.05 |
0.0163 |
997.5 |
11280.00 |
297.05 |
0.0163 |
993.5 |
2490.00 |
297.05 |
0.0163 |
990.8 |
38480.00 |
323.15 |
0.0163 |
995.2 |
30890.00 |
323.15 |
0.0163 |
992.3 |
21080.00 |
323.15 |
0.0163 |
988.4 |
11390.00 |
323.15 |
0.0163 |
984.4 |
2570.00 |
323.15 |
0.0163 |
980.6 |
39910.00 |
348.15 |
0.0163 |
982.3 |
29500.00 |
348.15 |
0.0163 |
978.3 |
20750.00 |
348.15 |
0.0163 |
974.7 |
10980.00 |
348.15 |
0.0163 |
970.6 |
3220.00 |
348.15 |
0.0163 |
967.1 |
35700.00 |
373.15 |
0.0163 |
964.6 |
30600.00 |
373.15 |
0.0163 |
962.5 |
21160.00 |
373.15 |
0.0163 |
958.3 |
11320.00 |
373.15 |
0.0163 |
953.8 |
3370.00 |
373.15 |
0.0163 |
950.2 |
39890.00 |
398.15 |
0.0163 |
948.0 |
30790.00 |
398.15 |
0.0163 |
943.7 |
21360.00 |
398.15 |
0.0163 |
939.3 |
11630.00 |
398.15 |
0.0163 |
934.4 |
3710.00 |
398.15 |
0.0163 |
930.3 |
39560.00 |
423.15 |
0.0163 |
927.2 |
30570.00 |
423.15 |
0.0163 |
922.4 |
20970.00 |
423.15 |
0.0163 |
917.0 |
10170.00 |
423.15 |
0.0163 |
911.0 |
2680.00 |
423.15 |
0.0163 |
906.7 |
38340.00 |
448.15 |
0.0163 |
903.5 |
31050.00 |
448.15 |
0.0163 |
899.4 |
21530.00 |
448.15 |
0.0163 |
893.7 |
11920.00 |
448.15 |
0.0163 |
887.5 |
3960.00 |
448.15 |
0.0163 |
882.3 |
39230.00 |
292.95 |
0.0730 |
988.0 |
30930.00 |
292.95 |
0.0730 |
985.0 |
21120.00 |
292.95 |
0.0730 |
981.2 |
11320.00 |
292.95 |
0.0730 |
977.6 |
2450.00 |
292.95 |
0.0730 |
974.2 |
38600.00 |
323.15 |
0.0730 |
973.6 |
30360.00 |
323.15 |
0.0730 |
970.6 |
20790.00 |
323.15 |
0.0730 |
966.7 |
10940.00 |
323.15 |
0.0730 |
962.8 |
2610.00 |
323.15 |
0.0730 |
959.3 |
39600.00 |
348.15 |
0.0730 |
958.9 |
30400.00 |
348.15 |
0.0730 |
955.0 |
20870.00 |
348.15 |
0.0730 |
950.8 |
11060.00 |
348.15 |
0.0730 |
946.6 |
3330.00 |
348.15 |
0.0730 |
943.0 |
37230.00 |
373.15 |
0.0730 |
939.9 |
30670.00 |
373.15 |
0.0730 |
937.0 |
21080.00 |
373.15 |
0.0730 |
932.5 |
11320.00 |
373.15 |
0.0730 |
927.7 |
3510.00 |
373.15 |
0.0730 |
923.9 |
39500.00 |
398.15 |
0.0730 |
920.7 |
30790.00 |
398.15 |
0.0730 |
916.3 |
21160.00 |
398.15 |
0.0730 |
911.4 |
11510.00 |
398.15 |
0.0730 |
906.2 |
3710.00 |
398.15 |
0.0730 |
901.9 |
40110.00 |
423.15 |
0.0730 |
898.6 |
30490.00 |
423.15 |
0.0730 |
893.0 |
20110.00 |
423.15 |
0.0730 |
887.1 |
10710.00 |
423.15 |
0.0730 |
881.1 |
2760.00 |
423.15 |
0.0730 |
875.9 |
37210.00 |
448.15 |
0.0730 |
873.0 |
31170.00 |
448.15 |
0.0730 |
869.2 |
21690.00 |
448.15 |
0.0730 |
862.7 |
12160.00 |
448.15 |
0.0730 |
855.6 |
4000.00 |
448.15 |
0.0730 |
849.3 |
40030.00 |
298.15 |
0.0946 |
979.8 |
29980.00 |
298.15 |
0.0946 |
976.1 |
20060.00 |
298.15 |
0.0946 |
972.4 |
10120.00 |
298.15 |
0.0946 |
968.6 |
2560.00 |
298.15 |
0.0946 |
965.8 |
39810.00 |
323.15 |
0.0946 |
966.2 |
32400.00 |
323.15 |
0.0946 |
963.3 |
20710.00 |
323.15 |
0.0946 |
958.8 |
11140.00 |
323.15 |
0.0946 |
954.9 |
2730.00 |
323.15 |
0.0946 |
951.3 |
37790.00 |
348.15 |
0.0946 |
948.7 |
29730.00 |
348.15 |
0.0946 |
945.4 |
20870.00 |
348.15 |
0.0946 |
941.6 |
11390.00 |
348.15 |
0.0946 |
937.4 |
2730.00 |
348.15 |
0.0946 |
933.7 |
39410.00 |
373.15 |
0.0946 |
927.3 |
30850.00 |
373.15 |
0.0946 |
922.3 |
21200.00 |
373.15 |
0.0946 |
917.7 |
11390.00 |
373.15 |
0.0946 |
912.8 |
3330.00 |
373.15 |
0.0946 |
908.6 |
39610.00 |
398.15 |
0.0946 |
905.3 |
30850.00 |
398.15 |
0.0946 |
901.1 |
21200.00 |
398.15 |
0.0946 |
896.0 |
11430.00 |
398.15 |
0.0946 |
890.4 |
3510.00 |
398.15 |
0.0946 |
885.8 |
39860.00 |
423.15 |
0.0946 |
882.2 |
30100.00 |
423.15 |
0.0946 |
875.5 |
20200.00 |
423.15 |
0.0946 |
869.5 |
10050.00 |
423.15 |
0.0946 |
863.9 |
2750.00 |
423.15 |
0.0946 |
860.1 |
40140.00 |
448.15 |
0.0946 |
858.6 |
30990.00 |
448.15 |
0.0946 |
852.6 |
21690.00 |
448.15 |
0.0946 |
845.8 |
11550.00 |
448.15 |
0.0946 |
837.9 |
3860.00 |
448.15 |
0.0946 |
831.7 |
39150.00 |
298.35 |
0.0343 |
998.6 |
31040.00 |
298.35 |
0.0343 |
995.7 |
21300.00 |
298.35 |
0.0343 |
991.9 |
11280.00 |
298.35 |
0.0343 |
987.9 |
2590.00 |
298.35 |
0.0343 |
984.1 |
39010.00 |
323.65 |
0.0343 |
988.2 |
30930.00 |
323.65 |
0.0343 |
985.2 |
21200.00 |
323.65 |
0.0343 |
981.4 |
11320.00 |
323.65 |
0.0343 |
977.4 |
2610.00 |
323.65 |
0.0343 |
973.6 |
39860.00 |
348.15 |
0.0343 |
974.7 |
30850.00 |
348.15 |
0.0343 |
971.3 |
21160.00 |
348.15 |
0.0343 |
967.5 |
11590.00 |
348.15 |
0.0343 |
963.5 |
3260.00 |
348.15 |
0.0343 |
959.9 |
39000.00 |
373.15 |
0.0343 |
957.9 |
30520.00 |
373.15 |
0.0343 |
954.5 |
21120.00 |
373.15 |
0.0343 |
950.3 |
11470.00 |
373.15 |
0.0343 |
945.9 |
3390.00 |
373.15 |
0.0343 |
942.1 |
37300.00 |
398.15 |
0.0343 |
938.3 |
30930.00 |
398.15 |
0.0343 |
935.2 |
21530.00 |
398.15 |
0.0343 |
930.7 |
11730.00 |
398.15 |
0.0343 |
925.8 |
3550.00 |
398.15 |
0.0343 |
921.6 |
39680.00 |
423.15 |
0.0343 |
918.2 |
30640.00 |
423.15 |
0.0343 |
913.4 |
21070.00 |
423.15 |
0.0343 |
908.1 |
10240.00 |
423.15 |
0.0343 |
901.8 |
2680.00 |
423.15 |
0.0343 |
897.3 |
40060.00 |
448.15 |
0.0343 |
894.8 |
31010.00 |
448.15 |
0.0343 |
889.8 |
22180.00 |
448.15 |
0.0343 |
884.2 |
11960.00 |
448.15 |
0.0343 |
877.7 |
4080.00 |
448.15 |
0.0343 |
872.1 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Ethanol (1) - Liquid |
Mass density, kg/m3 - Liquid |
350.70 |
10000.00 |
0.1000 |
933.68 |
350.70 |
10000.00 |
0.2000 |
895.78 |
350.70 |
10000.00 |
0.3000 |
863.89 |
350.70 |
10000.00 |
0.4000 |
838.33 |
350.70 |
10000.00 |
0.6000 |
798.55 |
350.70 |
10000.00 |
0.8000 |
768.37 |
350.70 |
10000.00 |
1.0000 |
745.63 |
350.70 |
20000.00 |
0.1000 |
936.77 |
350.70 |
20000.00 |
0.2000 |
900.9 |
350.70 |
20000.00 |
0.3000 |
870.14 |
350.70 |
20000.00 |
0.4000 |
845.24 |
350.70 |
20000.00 |
0.6000 |
807.87 |
350.70 |
20000.00 |
0.8000 |
778.79 |
350.70 |
20000.00 |
1.0000 |
757.47 |
350.70 |
30000.00 |
0.1000 |
941.46 |
350.70 |
30000.00 |
0.2000 |
905.65 |
350.70 |
30000.00 |
0.3000 |
876.58 |
350.70 |
30000.00 |
0.4000 |
852.53 |
350.70 |
30000.00 |
0.6000 |
815.61 |
350.70 |
30000.00 |
0.8000 |
787.77 |
350.70 |
30000.00 |
1.0000 |
766.87 |
350.70 |
40000.00 |
0.1000 |
945.15 |
350.70 |
40000.00 |
0.2000 |
911.39 |
350.70 |
40000.00 |
0.3000 |
881.9 |
350.70 |
40000.00 |
0.4000 |
859.05 |
350.70 |
40000.00 |
0.6000 |
822.93 |
350.70 |
40000.00 |
0.8000 |
795.87 |
350.70 |
40000.00 |
1.0000 |
775.75 |
373.20 |
10000.00 |
0.1000 |
913.36 |
373.20 |
10000.00 |
0.2000 |
874.72 |
373.20 |
10000.00 |
0.3000 |
842.36 |
373.20 |
10000.00 |
0.4000 |
815.79 |
373.20 |
10000.00 |
0.6000 |
776.56 |
373.20 |
10000.00 |
0.8000 |
747.1 |
373.20 |
10000.00 |
1.0000 |
726.87 |
373.20 |
20000.00 |
0.1000 |
918.8 |
373.20 |
20000.00 |
0.2000 |
880.64 |
373.20 |
20000.00 |
0.3000 |
849.56 |
373.20 |
20000.00 |
0.4000 |
823.45 |
373.20 |
20000.00 |
0.6000 |
785.48 |
373.20 |
20000.00 |
0.8000 |
757.25 |
373.20 |
20000.00 |
1.0000 |
738.25 |
373.20 |
30000.00 |
0.1000 |
924.46 |
373.20 |
30000.00 |
0.2000 |
886.74 |
373.20 |
30000.00 |
0.3000 |
856.1 |
373.20 |
30000.00 |
0.4000 |
830.81 |
373.20 |
30000.00 |
0.6000 |
794.06 |
373.20 |
30000.00 |
0.8000 |
767.44 |
373.20 |
30000.00 |
1.0000 |
750.02 |
373.20 |
40000.00 |
0.1000 |
928.74 |
373.20 |
40000.00 |
0.2000 |
892.24 |
373.20 |
40000.00 |
0.3000 |
862.39 |
373.20 |
40000.00 |
0.4000 |
837.9 |
373.20 |
40000.00 |
0.6000 |
801.93 |
373.20 |
40000.00 |
0.8000 |
776.49 |
373.20 |
40000.00 |
1.0000 |
757.87 |
476.20 |
10000.00 |
0.1000 |
802.54 |
476.20 |
10000.00 |
0.2000 |
752.52 |
476.20 |
10000.00 |
0.3000 |
713.85 |
476.20 |
10000.00 |
0.4000 |
682.37 |
476.20 |
10000.00 |
0.6000 |
636.05 |
476.20 |
10000.00 |
0.8000 |
605.36 |
476.20 |
10000.00 |
1.0000 |
582.85 |
476.20 |
20000.00 |
0.1000 |
810.76 |
476.20 |
20000.00 |
0.2000 |
764.89 |
476.20 |
20000.00 |
0.3000 |
728.6 |
476.20 |
20000.00 |
0.4000 |
700.31 |
476.20 |
20000.00 |
0.6000 |
658.71 |
476.20 |
20000.00 |
0.8000 |
633.16 |
476.20 |
20000.00 |
1.0000 |
613.37 |
476.20 |
30000.00 |
0.1000 |
819.25 |
476.20 |
30000.00 |
0.2000 |
776.24 |
476.20 |
30000.00 |
0.3000 |
743.62 |
476.20 |
30000.00 |
0.4000 |
717.25 |
476.20 |
30000.00 |
0.6000 |
679.71 |
476.20 |
30000.00 |
0.8000 |
656.43 |
476.20 |
30000.00 |
1.0000 |
638.82 |
476.20 |
40000.00 |
0.1000 |
827.58 |
476.20 |
40000.00 |
0.2000 |
786.01 |
476.20 |
40000.00 |
0.3000 |
754.08 |
476.20 |
40000.00 |
0.4000 |
730.44 |
476.20 |
40000.00 |
0.6000 |
694.35 |
476.20 |
40000.00 |
0.8000 |
671.76 |
476.20 |
40000.00 |
1.0000 |
656.07 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Ethanol (1) - Liquid |
Mass density, kg/m3 - Liquid |
523.20 |
20000.00 |
0.0000 |
816.1 |
523.20 |
20000.00 |
0.1000 |
745.9 |
523.20 |
20000.00 |
0.2000 |
694.1 |
523.20 |
20000.00 |
0.3000 |
653.2 |
523.20 |
20000.00 |
0.4000 |
622.3 |
523.20 |
20000.00 |
0.6000 |
578.5 |
523.20 |
20000.00 |
0.8000 |
550.5 |
523.20 |
20000.00 |
1.0000 |
533.1 |
523.20 |
30000.00 |
0.0000 |
825.5 |
523.20 |
30000.00 |
0.1000 |
761.6 |
523.20 |
30000.00 |
0.2000 |
713.6 |
523.20 |
30000.00 |
0.3000 |
676.9 |
523.20 |
30000.00 |
0.4000 |
650.7 |
523.20 |
30000.00 |
0.6000 |
612.4 |
523.20 |
30000.00 |
0.8000 |
588.9 |
523.20 |
30000.00 |
1.0000 |
573.6 |
523.20 |
40000.00 |
0.0000 |
834.3 |
523.20 |
40000.00 |
0.1000 |
773.2 |
523.20 |
40000.00 |
0.2000 |
728.3 |
523.20 |
40000.00 |
0.3000 |
694.7 |
523.20 |
40000.00 |
0.4000 |
671.6 |
523.20 |
40000.00 |
0.6000 |
636.3 |
523.20 |
40000.00 |
0.8000 |
615.2 |
523.20 |
40000.00 |
1.0000 |
601.3 |
573.20 |
20000.00 |
0.0000 |
734.8 |
573.20 |
20000.00 |
0.1000 |
649.3 |
573.20 |
20000.00 |
0.2000 |
585.4 |
573.20 |
20000.00 |
0.3000 |
534.9 |
573.20 |
20000.00 |
0.4000 |
494.9 |
573.20 |
20000.00 |
0.6000 |
446.2 |
573.20 |
20000.00 |
0.8000 |
426.2 |
573.20 |
20000.00 |
1.0000 |
421.1 |
573.20 |
30000.00 |
0.0000 |
750.7 |
573.20 |
30000.00 |
0.1000 |
674.8 |
573.20 |
30000.00 |
0.2000 |
621.4 |
573.20 |
30000.00 |
0.3000 |
582.5 |
573.20 |
30000.00 |
0.4000 |
553.5 |
573.20 |
30000.00 |
0.6000 |
517.6 |
573.20 |
30000.00 |
0.8000 |
499.0 |
573.20 |
30000.00 |
1.0000 |
491.5 |
573.20 |
40000.00 |
0.0000 |
764.3 |
573.20 |
40000.00 |
0.1000 |
694.9 |
573.20 |
40000.00 |
0.2000 |
647.6 |
573.20 |
40000.00 |
0.3000 |
614.0 |
573.20 |
40000.00 |
0.4000 |
587.9 |
573.20 |
40000.00 |
0.6000 |
557.4 |
573.20 |
40000.00 |
0.8000 |
540.4 |
573.20 |
40000.00 |
1.0000 |
531.0 |
618.20 |
20000.00 |
0.0000 |
619.7 |
618.20 |
20000.00 |
0.1000 |
445.3 |
618.20 |
20000.00 |
0.2000 |
281.3 |
618.20 |
20000.00 |
0.3000 |
250.4 |
618.20 |
20000.00 |
0.4000 |
253.1 |
618.20 |
20000.00 |
0.6000 |
270.6 |
618.20 |
20000.00 |
0.8000 |
295.0 |
618.20 |
20000.00 |
1.0000 |
314.6 |
618.20 |
30000.00 |
0.0000 |
656.9 |
618.20 |
30000.00 |
0.1000 |
566.3 |
618.20 |
30000.00 |
0.2000 |
501.5 |
618.20 |
30000.00 |
0.3000 |
460.9 |
618.20 |
30000.00 |
0.4000 |
437.4 |
618.20 |
30000.00 |
0.6000 |
420.1 |
618.20 |
30000.00 |
0.8000 |
418.9 |
618.20 |
30000.00 |
1.0000 |
423.8 |
618.20 |
40000.00 |
0.0000 |
682.3 |
618.20 |
40000.00 |
0.1000 |
610.3 |
618.20 |
40000.00 |
0.2000 |
561.0 |
618.20 |
40000.00 |
0.3000 |
529.3 |
618.20 |
40000.00 |
0.4000 |
509.1 |
618.20 |
40000.00 |
0.6000 |
488.2 |
618.20 |
40000.00 |
0.8000 |
481.7 |
618.20 |
40000.00 |
1.0000 |
481.2 |
Mass density, kg/m3
[ref]
Operational condition: Mole fraction =
0.5 (Liquid)
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
456.86 |
664.33 |
458.15 |
664.26 |
483.15 |
617.97 |
483.56 |
618.12 |
498.15 |
584.08 |
498.15 |
583.65 |
503.15 |
570.54 |
503.15 |
570.54 |
508.15 |
557.48 |
510.15 |
549.73 |
510.68 |
550.06 |
521.15 |
523.14 |
521.15 |
523.14 |
533.15 |
464.96 |
537.45 |
465.05 |
543.15 |
425.01 |
543.50 |
423.96 |
546.05 |
425.77 |
546.15 |
298.56 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Temperature, K - Fluid (supercritical or subcritical phases) |
Pressure, kPa - Fluid (supercritical or subcritical phases) |
Mole fraction of Ethanol (1) - Fluid (supercritical or subcritical phases) |
Mass density, kg/m3 - Fluid (supercritical or subcritical phases) |
524.15 |
7270.00 |
0.8000 |
383.33 |
525.15 |
7460.00 |
0.8000 |
383.31 |
526.15 |
7550.00 |
0.8000 |
367.95 |
528.15 |
7710.00 |
0.8000 |
312.86 |
528.15 |
7870.00 |
0.8000 |
367.91 |
528.15 |
8040.00 |
0.8000 |
383.24 |
528.15 |
8410.00 |
0.8000 |
406.33 |
531.15 |
8420.00 |
0.8000 |
367.86 |
533.15 |
4750.00 |
0.8000 |
53.24 |
533.15 |
7070.00 |
0.5000 |
84.52 |
533.15 |
7100.00 |
0.8000 |
115.14 |
533.15 |
8140.00 |
0.8000 |
188.77 |
533.15 |
8270.00 |
0.8000 |
244.11 |
533.15 |
8350.00 |
0.8000 |
284.34 |
533.15 |
8420.00 |
0.8000 |
312.77 |
533.15 |
8440.00 |
0.8000 |
307.44 |
533.15 |
8750.00 |
0.8000 |
367.82 |
533.15 |
8990.00 |
0.8000 |
383.14 |
533.15 |
9460.00 |
0.8000 |
406.22 |
533.15 |
10480.00 |
0.8000 |
440.21 |
533.15 |
10860.00 |
0.8000 |
446.58 |
533.15 |
17410.00 |
0.8000 |
516.16 |
533.15 |
8270.00 |
0.8000 |
260.96 |
533.15 |
10480.00 |
0.8000 |
440.21 |
533.15 |
10860.00 |
0.8000 |
446.58 |
538.15 |
9170.00 |
0.8000 |
312.69 |
538.15 |
27310.00 |
0.8000 |
553.51 |
538.15 |
27310.00 |
0.8000 |
553.51 |
543.15 |
4920.00 |
0.8000 |
53.21 |
543.15 |
7570.00 |
0.5000 |
84.48 |
543.15 |
7610.00 |
0.8000 |
115.08 |
543.15 |
9020.00 |
0.8000 |
188.68 |
543.15 |
9530.00 |
0.8000 |
260.83 |
543.15 |
9680.00 |
0.8000 |
284.19 |
543.15 |
9920.00 |
0.8000 |
312.61 |
543.15 |
10630.00 |
0.8000 |
367.62 |
543.15 |
10940.00 |
0.8000 |
382.93 |
543.15 |
11670.00 |
0.8000 |
406.0 |
548.15 |
7850.00 |
0.8000 |
115.06 |
548.15 |
9420.00 |
0.8000 |
188.63 |
548.15 |
9680.00 |
0.5000 |
294.01 |
548.15 |
9720.00 |
0.5000 |
327.56 |
548.15 |
9980.00 |
0.8000 |
243.92 |
548.15 |
10390.00 |
0.5000 |
421.66 |
548.15 |
10630.00 |
0.8000 |
307.19 |
548.15 |
10680.00 |
0.8000 |
312.53 |
548.15 |
11790.00 |
0.5000 |
464.07 |
548.15 |
11950.00 |
0.8000 |
382.83 |
548.15 |
14420.00 |
0.8000 |
439.83 |
548.15 |
14800.00 |
0.8000 |
446.2 |
548.15 |
17240.00 |
0.5000 |
522.28 |
548.15 |
26570.00 |
0.5000 |
568.89 |
548.15 |
30490.00 |
0.5000 |
581.74 |
548.15 |
14420.00 |
0.8000 |
439.83 |
548.15 |
14800.00 |
0.8000 |
446.2 |
553.15 |
5080.00 |
0.8000 |
53.19 |
553.15 |
6130.00 |
0.5000 |
55.97 |
553.15 |
7190.00 |
0.5000 |
69.28 |
553.15 |
7970.00 |
0.5000 |
84.44 |
553.15 |
9210.00 |
0.5000 |
117.47 |
553.15 |
10090.00 |
0.5000 |
171.33 |
553.15 |
10330.00 |
0.5000 |
234.67 |
553.15 |
10520.00 |
0.5000 |
327.48 |
553.15 |
10600.00 |
0.5000 |
293.93 |
553.15 |
10890.00 |
0.5000 |
385.77 |
553.15 |
11430.00 |
0.8000 |
312.45 |
553.15 |
11790.00 |
0.5000 |
424.77 |
553.15 |
11850.00 |
0.5000 |
419.86 |
553.15 |
12540.00 |
0.8000 |
367.42 |
553.15 |
13460.00 |
0.5000 |
463.93 |
553.15 |
19450.00 |
0.5000 |
522.11 |
553.15 |
25160.00 |
0.8000 |
515.53 |
553.15 |
25720.00 |
0.5000 |
555.9 |
553.15 |
47100.00 |
0.5000 |
614.98 |
558.15 |
8310.00 |
0.8000 |
115.0 |
558.15 |
10340.00 |
0.8000 |
188.54 |
558.15 |
11380.00 |
0.8000 |
260.63 |
558.15 |
11700.00 |
0.8000 |
283.97 |
558.15 |
13990.00 |
0.8000 |
382.62 |
558.15 |
15170.00 |
0.8000 |
405.66 |
563.15 |
6360.00 |
0.5000 |
55.95 |
563.15 |
7510.00 |
0.5000 |
69.25 |
563.15 |
8400.00 |
0.5000 |
84.4 |
563.15 |
8830.00 |
0.2000 |
67.68 |
563.15 |
9900.00 |
0.5000 |
117.41 |
563.15 |
11080.00 |
0.5000 |
171.24 |
563.15 |
12360.00 |
0.5000 |
327.3 |
563.15 |
12940.00 |
0.8000 |
312.28 |
563.15 |
12970.00 |
0.8000 |
312.28 |
563.15 |
13290.00 |
0.5000 |
385.56 |
563.15 |
14460.00 |
0.8000 |
367.22 |
563.15 |
16510.00 |
0.5000 |
463.66 |
563.15 |
23620.00 |
0.5000 |
521.79 |
568.15 |
9040.00 |
0.2000 |
67.66 |
573.15 |
5420.00 |
0.8000 |
53.14 |
573.15 |
6590.00 |
0.5000 |
55.92 |
573.15 |
7820.00 |
0.5000 |
69.21 |
573.15 |
8780.00 |
0.5000 |
84.36 |
573.15 |
8990.00 |
0.8000 |
114.92 |
573.15 |
10460.00 |
0.5000 |
117.35 |
573.15 |
11580.00 |
0.8000 |
188.4 |
573.15 |
12050.00 |
0.5000 |
171.15 |
573.15 |
12840.00 |
0.8000 |
243.61 |
573.15 |
13010.00 |
0.5000 |
234.43 |
573.15 |
13190.00 |
0.8000 |
260.43 |
573.15 |
13610.00 |
0.5000 |
293.62 |
573.15 |
13720.00 |
0.8000 |
283.75 |
573.15 |
14410.00 |
0.8000 |
306.79 |
573.15 |
14490.00 |
0.8000 |
312.12 |
573.15 |
15660.00 |
0.5000 |
385.34 |
573.15 |
16440.00 |
0.8000 |
367.02 |
573.15 |
16820.00 |
0.5000 |
419.39 |
573.15 |
17060.00 |
0.5000 |
421.07 |
573.15 |
17150.00 |
0.8000 |
382.31 |
573.15 |
17210.00 |
0.5000 |
424.29 |
573.15 |
18650.00 |
0.8000 |
405.32 |
573.15 |
20120.00 |
0.5000 |
463.38 |
573.15 |
21340.00 |
0.8000 |
439.21 |
573.15 |
22500.00 |
0.8000 |
451.39 |
573.15 |
28040.00 |
0.5000 |
521.47 |
573.15 |
39960.00 |
0.5000 |
567.95 |
573.15 |
44900.00 |
0.5000 |
580.76 |
573.15 |
21340.00 |
0.8000 |
439.21 |
573.15 |
22500.00 |
0.8000 |
451.39 |
577.15 |
45760.00 |
0.8000 |
552.13 |
577.15 |
45760.00 |
0.8000 |
552.13 |
578.15 |
23390.00 |
0.8000 |
445.43 |
578.15 |
35170.00 |
0.8000 |
514.74 |
578.15 |
38000.00 |
0.5000 |
555.01 |
578.15 |
23390.00 |
0.8000 |
445.43 |
593.15 |
50760.00 |
0.5000 |
567.2 |
598.15 |
5820.00 |
0.8000 |
53.08 |
598.15 |
7080.00 |
0.5000 |
55.85 |
598.15 |
8560.00 |
0.5000 |
69.13 |
598.15 |
9720.00 |
0.5000 |
84.26 |
598.15 |
10060.00 |
0.8000 |
114.78 |
598.15 |
11840.00 |
0.5000 |
117.21 |
598.15 |
12030.00 |
0.2000 |
90.05 |
598.15 |
13600.00 |
0.8000 |
188.16 |
598.15 |
14290.00 |
0.2000 |
138.08 |
598.15 |
15290.00 |
0.2000 |
221.72 |
598.15 |
15460.00 |
0.2000 |
286.74 |
598.15 |
15540.00 |
0.2000 |
308.36 |
598.15 |
15600.00 |
0.8000 |
243.3 |
598.15 |
15640.00 |
0.2000 |
325.01 |
598.15 |
16230.00 |
0.8000 |
260.09 |
598.15 |
16810.00 |
0.2000 |
420.24 |
598.15 |
17080.00 |
0.8000 |
283.38 |
598.15 |
18140.00 |
0.8000 |
306.39 |
598.15 |
18350.00 |
0.8000 |
311.71 |
598.15 |
19160.00 |
0.5000 |
326.69 |
598.15 |
21410.00 |
0.8000 |
366.53 |
598.15 |
21610.00 |
0.5000 |
384.81 |
598.15 |
21850.00 |
0.5000 |
418.8 |
598.15 |
22460.00 |
0.8000 |
381.79 |
598.15 |
24130.00 |
0.5000 |
420.47 |
598.15 |
24210.00 |
0.5000 |
423.68 |
598.15 |
24610.00 |
0.8000 |
404.76 |
598.15 |
27590.00 |
0.2000 |
547.13 |
598.15 |
28350.00 |
0.8000 |
438.59 |
598.15 |
28670.00 |
0.5000 |
462.7 |
598.15 |
38940.00 |
0.5000 |
520.65 |
598.15 |
48240.00 |
0.2000 |
617.36 |
598.15 |
48500.00 |
0.5000 |
554.28 |
598.15 |
28350.00 |
0.8000 |
438.59 |
603.15 |
10470.00 |
0.2000 |
67.54 |
603.15 |
12120.00 |
0.5000 |
117.18 |
603.15 |
14860.00 |
0.5000 |
170.89 |
603.15 |
16860.00 |
0.2000 |
350.86 |
603.15 |
16940.00 |
0.5000 |
234.07 |
603.15 |
18730.00 |
0.5000 |
293.15 |
613.15 |
23290.00 |
0.2000 |
452.8 |
623.15 |
6210.00 |
0.8000 |
53.01 |
623.15 |
7610.00 |
0.5000 |
55.79 |
623.15 |
9230.00 |
0.5000 |
69.05 |
623.15 |
10590.00 |
0.5000 |
84.15 |
623.15 |
11070.00 |
0.8000 |
114.64 |
623.15 |
13180.00 |
0.5000 |
117.07 |
623.15 |
13400.00 |
0.2000 |
89.94 |
623.15 |
15510.00 |
0.8000 |
187.93 |
623.15 |
16770.00 |
0.2000 |
137.9 |
623.15 |
18300.00 |
0.8000 |
242.99 |
623.15 |
19450.00 |
0.2000 |
221.42 |
623.15 |
20470.00 |
0.8000 |
283.01 |
623.15 |
20590.00 |
0.2000 |
286.35 |
623.15 |
21000.00 |
0.2000 |
307.94 |
623.15 |
21380.00 |
0.2000 |
324.56 |
623.15 |
21860.00 |
0.8000 |
305.99 |
623.15 |
21920.00 |
0.2000 |
350.47 |
623.15 |
22240.00 |
0.8000 |
311.3 |
623.15 |
24920.00 |
0.2000 |
420.24 |
623.15 |
26360.00 |
0.8000 |
366.04 |
623.15 |
27820.00 |
0.8000 |
381.27 |
623.15 |
27940.00 |
0.5000 |
384.27 |
623.15 |
30710.00 |
0.8000 |
404.2 |
623.15 |
31220.00 |
0.5000 |
418.2 |
623.15 |
31480.00 |
0.5000 |
419.87 |
623.15 |
31720.00 |
0.5000 |
423.08 |
623.15 |
36430.00 |
0.8000 |
444.29 |
623.15 |
37340.00 |
0.5000 |
462.02 |
623.15 |
41330.00 |
0.2000 |
546.22 |
623.15 |
50360.00 |
0.5000 |
519.83 |
623.15 |
36430.00 |
0.8000 |
444.29 |
628.15 |
19790.00 |
0.8000 |
259.69 |
628.15 |
36970.00 |
0.8000 |
437.84 |
628.15 |
36970.00 |
0.8000 |
437.84 |
633.15 |
11600.00 |
0.2000 |
67.45 |
633.15 |
13740.00 |
0.5000 |
117.01 |
633.15 |
17410.00 |
0.5000 |
170.64 |
633.15 |
23850.00 |
0.5000 |
292.69 |
633.15 |
26000.00 |
0.5000 |
326.07 |
638.15 |
21420.00 |
0.5000 |
233.65 |
643.15 |
35160.00 |
0.2000 |
451.97 |
648.15 |
6600.00 |
0.8000 |
52.95 |
648.15 |
8080.00 |
0.5000 |
55.72 |
648.15 |
9890.00 |
0.5000 |
68.96 |
648.15 |
11430.00 |
0.5000 |
84.05 |
648.15 |
12050.00 |
0.8000 |
114.5 |
648.15 |
14470.00 |
0.5000 |
116.92 |
648.15 |
14680.00 |
0.2000 |
89.83 |
648.15 |
17440.00 |
0.8000 |
187.69 |
648.15 |
19110.00 |
0.2000 |
137.73 |
648.15 |
23400.00 |
0.2000 |
221.13 |
648.15 |
25670.00 |
0.8000 |
305.59 |
648.15 |
25860.00 |
0.2000 |
285.96 |
648.15 |
26120.00 |
0.8000 |
310.89 |
648.15 |
26740.00 |
0.2000 |
307.52 |
648.15 |
28730.00 |
0.2000 |
349.97 |
648.15 |
31420.00 |
0.8000 |
365.54 |
648.15 |
33230.00 |
0.8000 |
380.75 |
648.15 |
33660.00 |
0.2000 |
420.24 |
648.15 |
34330.00 |
0.5000 |
383.73 |
648.15 |
36760.00 |
0.8000 |
403.64 |
648.15 |
39020.00 |
0.5000 |
419.27 |
653.15 |
19550.00 |
0.2000 |
137.7 |
653.15 |
21530.00 |
0.8000 |
242.62 |
653.15 |
22750.00 |
0.8000 |
259.36 |
653.15 |
24460.00 |
0.8000 |
282.58 |
653.15 |
26990.00 |
0.8000 |
310.81 |
653.15 |
28660.00 |
0.2000 |
324.03 |
653.15 |
34300.00 |
0.8000 |
380.65 |
653.15 |
35620.00 |
0.5000 |
383.63 |
653.15 |
40110.00 |
0.5000 |
417.48 |
653.15 |
40890.00 |
0.5000 |
422.34 |
653.15 |
44100.00 |
0.8000 |
437.21 |
653.15 |
48080.00 |
0.5000 |
461.19 |
653.15 |
44100.00 |
0.8000 |
437.21 |
673.15 |
6990.00 |
0.8000 |
52.89 |
673.15 |
8570.00 |
0.5000 |
55.65 |
673.15 |
10540.00 |
0.5000 |
68.88 |
673.15 |
12250.00 |
0.5000 |
83.95 |
673.15 |
12980.00 |
0.2000 |
67.32 |
673.15 |
13010.00 |
0.8000 |
114.36 |
673.15 |
15740.00 |
0.5000 |
116.78 |
673.15 |
15940.00 |
0.2000 |
89.72 |
673.15 |
19310.00 |
0.8000 |
187.46 |
673.15 |
20680.00 |
0.5000 |
170.3 |
673.15 |
21310.00 |
0.2000 |
137.56 |
673.15 |
23620.00 |
0.8000 |
242.38 |
673.15 |
25130.00 |
0.8000 |
259.1 |
673.15 |
25740.00 |
0.5000 |
233.23 |
673.15 |
27230.00 |
0.8000 |
282.28 |
673.15 |
27430.00 |
0.2000 |
220.84 |
673.15 |
29500.00 |
0.8000 |
305.19 |
673.15 |
30040.00 |
0.8000 |
310.49 |
673.15 |
30620.00 |
0.5000 |
292.07 |
673.15 |
31230.00 |
0.2000 |
285.57 |
673.15 |
32510.00 |
0.2000 |
307.09 |
673.15 |
33730.00 |
0.2000 |
323.66 |
673.15 |
34050.00 |
0.5000 |
325.37 |
673.15 |
35510.00 |
0.2000 |
349.48 |
673.15 |
36420.00 |
0.8000 |
365.05 |
673.15 |
38700.00 |
0.8000 |
380.23 |
673.15 |
40850.00 |
0.5000 |
383.2 |
673.15 |
42660.00 |
0.2000 |
420.24 |
673.15 |
42950.00 |
0.8000 |
403.08 |
673.15 |
46620.00 |
0.5000 |
418.66 |
673.15 |
47140.00 |
0.2000 |
451.15 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Water (2) - Liquid |
Mass density, kg/m3 - Liquid |
293.15 |
0.0000 |
789.75 |
293.15 |
0.0501 |
795.99 |
293.15 |
0.0986 |
802.09 |
293.15 |
0.1961 |
814.88 |
293.15 |
0.2961 |
829.05 |
293.15 |
0.3991 |
845.25 |
293.15 |
0.4971 |
862.82 |
293.15 |
0.5989 |
884.07 |
293.15 |
0.6991 |
908.69 |
293.15 |
0.8001 |
937.33 |
293.15 |
0.8996 |
965.71 |
293.15 |
0.9499 |
979.28 |
293.15 |
1.0000 |
998.2 |
298.15 |
0.0000 |
785.46 |
298.15 |
0.0501 |
791.68 |
298.15 |
0.0986 |
797.77 |
298.15 |
0.1961 |
810.54 |
298.15 |
0.2961 |
824.7 |
298.15 |
0.3991 |
840.94 |
298.15 |
0.5989 |
879.89 |
298.15 |
0.6991 |
904.65 |
298.15 |
0.8001 |
933.65 |
298.15 |
0.8996 |
963.24 |
298.15 |
0.9499 |
977.72 |
298.15 |
1.0000 |
997.05 |
303.15 |
0.0000 |
781.15 |
303.15 |
0.0501 |
787.35 |
303.15 |
0.0986 |
793.41 |
303.15 |
0.1961 |
806.14 |
303.15 |
0.2961 |
820.29 |
303.15 |
0.3991 |
836.55 |
303.15 |
0.5989 |
875.63 |
303.15 |
0.6991 |
900.55 |
303.15 |
0.8001 |
929.9 |
303.15 |
0.8996 |
960.61 |
303.15 |
0.9499 |
975.93 |
303.15 |
1.0000 |
995.65 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Water (2) - Liquid |
Mass density, kg/m3 - Liquid |
278.15 |
0.0010 |
802.2 |
278.15 |
0.0021 |
802.34 |
278.15 |
0.0041 |
802.59 |
278.15 |
0.0067 |
802.91 |
278.15 |
0.0093 |
803.22 |
278.15 |
0.0119 |
803.54 |
278.15 |
0.0144 |
803.85 |
278.15 |
0.0179 |
804.29 |
278.15 |
0.0211 |
804.68 |
278.15 |
0.0251 |
805.17 |
278.15 |
0.0292 |
805.69 |
278.15 |
0.0312 |
805.94 |
278.15 |
0.0336 |
806.24 |
278.15 |
0.0366 |
806.61 |
288.15 |
0.0010 |
793.72 |
288.15 |
0.0021 |
793.86 |
288.15 |
0.0041 |
794.1 |
288.15 |
0.0067 |
794.42 |
288.15 |
0.0093 |
794.73 |
288.15 |
0.0119 |
795.06 |
288.15 |
0.0144 |
795.37 |
288.15 |
0.0179 |
795.8 |
288.15 |
0.0211 |
796.2 |
288.15 |
0.0251 |
796.68 |
288.15 |
0.0292 |
797.2 |
288.15 |
0.0312 |
797.46 |
288.15 |
0.0336 |
797.75 |
288.15 |
0.0366 |
798.13 |
298.15 |
0.0010 |
785.15 |
298.15 |
0.0021 |
785.29 |
298.15 |
0.0041 |
785.53 |
298.15 |
0.0067 |
785.85 |
298.15 |
0.0093 |
786.16 |
298.15 |
0.0119 |
786.48 |
298.15 |
0.0144 |
786.79 |
298.15 |
0.0179 |
787.22 |
298.15 |
0.0211 |
787.61 |
298.15 |
0.0251 |
788.1 |
298.15 |
0.0292 |
788.61 |
298.15 |
0.0312 |
788.87 |
298.15 |
0.0336 |
789.16 |
298.15 |
0.0366 |
789.54 |
308.15 |
0.0010 |
776.47 |
308.15 |
0.0021 |
776.61 |
308.15 |
0.0041 |
776.85 |
308.15 |
0.0067 |
777.16 |
308.15 |
0.0093 |
777.47 |
308.15 |
0.0119 |
777.79 |
308.15 |
0.0144 |
778.09 |
308.15 |
0.0179 |
778.52 |
308.15 |
0.0211 |
778.92 |
308.15 |
0.0251 |
779.4 |
308.15 |
0.0292 |
779.91 |
308.15 |
0.0312 |
780.16 |
308.15 |
0.0336 |
780.45 |
308.15 |
0.0366 |
780.83 |
318.15 |
0.0010 |
767.66 |
318.15 |
0.0021 |
767.79 |
318.15 |
0.0041 |
768.03 |
318.15 |
0.0067 |
768.34 |
318.15 |
0.0093 |
768.65 |
318.15 |
0.0119 |
768.96 |
318.15 |
0.0144 |
769.26 |
318.15 |
0.0179 |
769.69 |
318.15 |
0.0211 |
770.08 |
318.15 |
0.0251 |
770.56 |
318.15 |
0.0292 |
771.06 |
318.15 |
0.0312 |
771.31 |
318.15 |
0.0336 |
771.6 |
318.15 |
0.0366 |
771.97 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
84.5 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Molality, mol/kg of Ethanol (1) - Liquid |
Mass density, kg/m3 - Liquid |
288.15 |
0.0216 |
998.9 |
288.15 |
0.0435 |
998.707 |
288.15 |
0.0649 |
998.526 |
288.15 |
0.0865 |
998.318 |
288.15 |
0.1087 |
998.132 |
288.15 |
0.1306 |
997.942 |
288.15 |
0.1749 |
997.562 |
288.15 |
0.2188 |
997.195 |
293.15 |
0.0216 |
998.003 |
293.15 |
0.0435 |
997.81 |
293.15 |
0.0649 |
997.632 |
293.15 |
0.0865 |
997.424 |
293.15 |
0.1087 |
997.24 |
293.15 |
0.1306 |
997.051 |
293.15 |
0.1749 |
996.671 |
293.15 |
0.2188 |
996.303 |
298.15 |
0.0216 |
996.845 |
298.15 |
0.0435 |
996.654 |
298.15 |
0.0649 |
996.474 |
298.15 |
0.0865 |
996.265 |
298.15 |
0.1087 |
996.081 |
298.15 |
0.1306 |
995.892 |
298.15 |
0.1749 |
995.508 |
298.15 |
0.2188 |
995.144 |
303.15 |
0.0216 |
995.446 |
303.15 |
0.0435 |
995.257 |
303.15 |
0.0649 |
995.076 |
303.15 |
0.0865 |
994.87 |
303.15 |
0.1087 |
994.683 |
303.15 |
0.1306 |
994.494 |
303.15 |
0.1749 |
994.111 |
303.15 |
0.2188 |
993.747 |
308.15 |
0.0216 |
993.829 |
308.15 |
0.0435 |
993.639 |
308.15 |
0.0649 |
993.46 |
308.15 |
0.0865 |
993.243 |
308.15 |
0.1087 |
993.05 |
308.15 |
0.1306 |
992.873 |
308.15 |
0.1749 |
992.498 |
308.15 |
0.2188 |
992.123 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
92.3 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol (1) - Liquid |
Mass density, kg/m3 - Liquid |
293.15 |
0.0024 |
997.039 |
293.15 |
0.0202 |
989.382 |
293.15 |
0.0295 |
985.977 |
293.15 |
0.0366 |
983.574 |
293.15 |
0.0513 |
978.913 |
293.15 |
0.0600 |
976.452 |
293.15 |
0.0707 |
973.538 |
293.15 |
0.0801 |
971.049 |
293.15 |
0.0904 |
968.313 |
293.15 |
0.0997 |
965.87 |
293.15 |
0.1294 |
957.918 |
293.15 |
0.1497 |
952.184 |
293.15 |
0.2008 |
937.088 |
293.15 |
0.2503 |
922.612 |
293.15 |
0.2998 |
908.897 |
293.15 |
0.3507 |
895.841 |
293.15 |
0.3992 |
884.433 |
293.15 |
0.4514 |
873.258 |
293.15 |
0.5002 |
863.248 |
293.15 |
0.5494 |
854.117 |
293.15 |
0.6018 |
845.002 |
293.15 |
0.6503 |
837.196 |
293.15 |
0.7006 |
829.434 |
293.15 |
0.7355 |
824.262 |
293.15 |
0.7965 |
815.831 |
293.15 |
0.8433 |
809.567 |
293.15 |
0.8920 |
803.132 |
293.15 |
0.9093 |
800.938 |
293.15 |
0.9207 |
799.51 |
293.15 |
0.9307 |
798.225 |
293.15 |
0.9398 |
797.133 |
293.15 |
0.9483 |
796.043 |
293.15 |
0.9603 |
794.596 |
293.15 |
0.9702 |
793.374 |
293.15 |
0.9801 |
792.038 |
293.15 |
0.9895 |
791.076 |
298.15 |
0.0024 |
995.871 |
298.15 |
0.0202 |
988.159 |
298.15 |
0.0295 |
984.669 |
298.15 |
0.0366 |
982.196 |
298.15 |
0.0513 |
977.287 |
298.15 |
0.0600 |
974.729 |
298.15 |
0.0707 |
971.631 |
298.15 |
0.0801 |
968.969 |
298.15 |
0.0904 |
966.039 |
298.15 |
0.0997 |
963.419 |
298.15 |
0.1294 |
954.963 |
298.15 |
0.1497 |
948.951 |
298.15 |
0.2008 |
933.41 |
298.15 |
0.2503 |
918.708 |
298.15 |
0.2998 |
904.858 |
298.15 |
0.3507 |
891.711 |
298.15 |
0.3992 |
880.239 |
298.15 |
0.4514 |
869.012 |
298.15 |
0.5002 |
858.963 |
298.15 |
0.5494 |
849.801 |
298.15 |
0.6018 |
840.665 |
298.15 |
0.6503 |
832.839 |
298.15 |
0.7006 |
825.07 |
298.15 |
0.7355 |
819.907 |
298.15 |
0.7965 |
811.475 |
298.15 |
0.8433 |
805.219 |
298.15 |
0.8920 |
798.808 |
298.15 |
0.9093 |
796.615 |
298.15 |
0.9207 |
795.193 |
298.15 |
0.9307 |
793.91 |
298.15 |
0.9398 |
792.821 |
298.15 |
0.9483 |
791.735 |
298.15 |
0.9603 |
790.291 |
298.15 |
0.9702 |
789.073 |
298.15 |
0.9801 |
787.741 |
298.15 |
0.9895 |
786.779 |
303.15 |
0.0024 |
994.464 |
303.15 |
0.0202 |
986.01 |
303.15 |
0.0295 |
983.11 |
303.15 |
0.0366 |
980.577 |
303.15 |
0.0513 |
975.532 |
303.15 |
0.0600 |
972.787 |
303.15 |
0.0707 |
969.513 |
303.15 |
0.0801 |
966.689 |
303.15 |
0.0904 |
963.577 |
303.15 |
0.0997 |
960.797 |
303.15 |
0.1294 |
951.878 |
303.15 |
0.1497 |
945.612 |
303.15 |
0.2008 |
929.658 |
303.15 |
0.2503 |
914.742 |
303.15 |
0.2998 |
900.761 |
303.15 |
0.3507 |
887.521 |
303.15 |
0.3992 |
875.988 |
303.15 |
0.4514 |
864.712 |
303.15 |
0.5002 |
854.622 |
303.15 |
0.5494 |
845.433 |
303.15 |
0.6018 |
836.274 |
303.15 |
0.6503 |
828.435 |
303.15 |
0.7006 |
820.66 |
303.15 |
0.7355 |
815.498 |
303.15 |
0.7965 |
807.074 |
303.15 |
0.8433 |
800.833 |
303.15 |
0.8920 |
794.442 |
303.15 |
0.9093 |
792.256 |
303.15 |
0.9207 |
790.841 |
303.15 |
0.9307 |
789.562 |
303.15 |
0.9398 |
788.477 |
303.15 |
0.9483 |
787.394 |
303.15 |
0.9603 |
785.958 |
303.15 |
0.9702 |
784.743 |
303.15 |
0.9801 |
783.417 |
303.15 |
0.9895 |
782.456 |
308.15 |
0.0024 |
992.863 |
308.15 |
0.0202 |
984.706 |
308.15 |
0.0295 |
981.361 |
308.15 |
0.0366 |
978.735 |
308.15 |
0.0513 |
973.534 |
308.15 |
0.0600 |
970.651 |
308.15 |
0.0707 |
967.196 |
308.15 |
0.0801 |
964.224 |
308.15 |
0.0904 |
960.944 |
308.15 |
0.0997 |
958.013 |
308.15 |
0.1294 |
948.682 |
308.15 |
0.1497 |
942.174 |
308.15 |
0.2008 |
925.836 |
308.15 |
0.2503 |
910.712 |
308.15 |
0.2998 |
896.603 |
308.15 |
0.3507 |
883.273 |
308.15 |
0.3992 |
871.678 |
308.15 |
0.4514 |
860.353 |
308.15 |
0.5002 |
850.223 |
308.15 |
0.5494 |
841.009 |
308.15 |
0.6018 |
831.83 |
308.15 |
0.6503 |
823.98 |
308.15 |
0.7006 |
816.2 |
308.15 |
0.7355 |
811.052 |
308.15 |
0.7965 |
802.628 |
308.15 |
0.8433 |
796.401 |
308.15 |
0.8920 |
790.037 |
308.15 |
0.9093 |
787.861 |
308.15 |
0.9207 |
786.448 |
308.15 |
0.9307 |
785.175 |
308.15 |
0.9398 |
784.096 |
308.15 |
0.9483 |
783.019 |
308.15 |
0.9603 |
781.59 |
308.15 |
0.9702 |
780.379 |
308.15 |
0.9801 |
779.061 |
308.15 |
0.9895 |
778.103 |
293.15 |
0.0000 |
998.429 |
298.15 |
0.0000 |
997.267 |
303.15 |
0.0000 |
995.867 |
308.15 |
0.0000 |
994.252 |
293.15 |
1.0000 |
789.547 |
298.15 |
1.0000 |
785.26 |
303.15 |
1.0000 |
780.941 |
308.15 |
1.0000 |
776.592 |
293.15 |
0.0201 |
989.54 |
293.15 |
0.0408 |
982.27 |
293.15 |
0.0497 |
979.54 |
293.15 |
0.0600 |
976.51 |
293.15 |
0.0796 |
971.24 |
293.15 |
0.1004 |
963.75 |
293.15 |
0.1499 |
951.92 |
293.15 |
0.1984 |
935.19 |
293.15 |
0.2499 |
922.7 |
293.15 |
0.3016 |
908.77 |
293.15 |
0.3499 |
896.37 |
293.15 |
0.3990 |
884.54 |
293.15 |
0.4495 |
873.57 |
293.15 |
0.4989 |
864.28 |
293.15 |
0.5495 |
854.95 |
293.15 |
0.6067 |
844.7 |
293.15 |
0.6503 |
837.27 |
293.15 |
0.6956 |
830.42 |
293.15 |
0.7500 |
822.4 |
293.15 |
0.7843 |
817.86 |
293.15 |
0.8475 |
809.97 |
293.15 |
0.8864 |
804.22 |
293.15 |
0.9290 |
798.49 |
298.15 |
0.0201 |
988.31 |
298.15 |
0.0408 |
980.85 |
298.15 |
0.0497 |
977.99 |
298.15 |
0.0600 |
974.31 |
298.15 |
0.0796 |
969.17 |
298.15 |
0.1004 |
961.4 |
298.15 |
0.1499 |
948.9 |
298.15 |
0.1984 |
931.84 |
298.15 |
0.2499 |
918.95 |
298.15 |
0.3016 |
904.86 |
298.15 |
0.3499 |
892.28 |
298.15 |
0.3990 |
880.34 |
298.15 |
0.4495 |
869.34 |
298.15 |
0.4989 |
860.04 |
298.15 |
0.5495 |
850.72 |
298.15 |
0.6067 |
840.19 |
298.15 |
0.6503 |
832.95 |
298.15 |
0.6956 |
826.05 |
298.15 |
0.7500 |
818.03 |
298.15 |
0.7843 |
813.49 |
298.15 |
0.8475 |
805.63 |
298.15 |
0.8864 |
799.93 |
298.15 |
0.9290 |
794.19 |
303.15 |
0.0201 |
986.86 |
303.15 |
0.0408 |
978.54 |
303.15 |
0.0497 |
976.06 |
303.15 |
0.0600 |
971.89 |
303.15 |
0.0796 |
966.81 |
303.15 |
0.1004 |
958.69 |
303.15 |
0.1499 |
945.56 |
303.15 |
0.1984 |
928.77 |
303.15 |
0.2499 |
915.3 |
303.15 |
0.3016 |
900.76 |
303.15 |
0.3499 |
888.09 |
303.15 |
0.3990 |
876.09 |
303.15 |
0.4495 |
865.03 |
303.15 |
0.4989 |
855.7 |
303.15 |
0.5495 |
846.35 |
303.15 |
0.6067 |
835.6 |
303.15 |
0.6503 |
828.55 |
303.15 |
0.6956 |
821.65 |
303.15 |
0.7500 |
813.63 |
303.15 |
0.7843 |
809.09 |
303.15 |
0.8475 |
801.24 |
303.15 |
0.8864 |
795.58 |
303.15 |
0.9290 |
789.85 |
308.15 |
0.0201 |
985.15 |
308.15 |
0.0408 |
976.58 |
308.15 |
0.0497 |
973.32 |
308.15 |
0.0600 |
969.36 |
308.15 |
0.0796 |
964.08 |
308.15 |
0.1004 |
955.87 |
308.15 |
0.1499 |
942.15 |
308.15 |
0.1984 |
925.04 |
308.15 |
0.2499 |
911.28 |
308.15 |
0.3016 |
896.6 |
308.15 |
0.3499 |
883.84 |
308.15 |
0.3990 |
871.78 |
308.15 |
0.4495 |
860.66 |
308.15 |
0.4989 |
851.3 |
308.15 |
0.5495 |
841.93 |
308.15 |
0.6067 |
831.06 |
308.15 |
0.6503 |
824.09 |
308.15 |
0.6956 |
817.19 |
308.15 |
0.7500 |
809.16 |
308.15 |
0.7843 |
804.63 |
308.15 |
0.8475 |
796.81 |
308.15 |
0.8864 |
791.17 |
308.15 |
0.9290 |
785.46 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 100 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Mass density, kg/m3 - Liquid |
1.0000 |
785.5 |
0.7084 |
825.2 |
0.4238 |
876.2 |
0.3870 |
883.5 |
0.2437 |
920.1 |
0.1461 |
950.1 |
0.1270 |
952.3 |
0.0641 |
970.7 |
0.0000 |
997.1 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
85 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mass fraction of Ethanol (1) - Liquid |
Mass density, kg/m3 - Liquid |
298.15 |
0.0400 |
990.13 |
303.15 |
0.0400 |
988.79 |
308.15 |
0.0400 |
987.24 |
313.15 |
0.0400 |
985.42 |
298.15 |
0.0800 |
983.9 |
303.15 |
0.0800 |
982.43 |
308.15 |
0.0800 |
980.77 |
313.15 |
0.0800 |
978.85 |
298.15 |
0.1600 |
972.57 |
303.15 |
0.1600 |
970.69 |
308.15 |
0.1600 |
968.6 |
313.15 |
0.1600 |
966.4 |
Mass density, kg/m3
[ref]
Operational conditions:
- Pressure, kPa = 100 (Liquid)
- Molality, mol/kg = 16 (Liquid)
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
298.15 |
925.8 |
303.15 |
923.139 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 298.2 (Liquid)
- Pressure, kPa = 100 (Liquid)
Mass fraction of Water (2) - Liquid |
Mass density, kg/m3 - Liquid |
0.5080 |
911.41 |
0.4260 |
890.1 |
0.3110 |
865.5 |
0.2470 |
850.5 |
0.2350 |
847.41 |
0.2060 |
841.91 |
Mass density, kg/m3
[ref]
Operational conditions:
- Pressure, kPa = 100 (Liquid)
- Temperature, K = 308.15 (Liquid)
Mass ratio of solute to solvent of Ethanol (1) - Liquid |
Mass density, kg/m3 - Liquid |
0.0500 |
990.6 |
0.1000 |
982.8 |
0.1500 |
971.7 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 298.2 (Liquid)
- Pressure, kPa = 100 (Liquid)
Mass fraction of Water (2) - Liquid |
Mass density, kg/m3 - Liquid |
0.0610 |
802.5 |
0.1240 |
819.5 |
0.1720 |
833.4 |
0.2330 |
848.2 |
0.2760 |
857.9 |
0.3400 |
861.8 |
0.4100 |
887.3 |
0.5000 |
908.8 |
0.6200 |
935.2 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mass fraction of Ethanol (1) - Liquid |
Mass density, kg/m3 - Liquid |
298.15 |
0.1084 |
979.29 |
298.15 |
0.1219 |
977.47 |
298.15 |
0.2859 |
953.33 |
298.15 |
0.2907 |
952.58 |
298.15 |
0.3737 |
937.25 |
298.15 |
0.3750 |
936.69 |
298.15 |
0.4432 |
922.6 |
298.15 |
0.4445 |
922.55 |
298.15 |
0.4998 |
910.43 |
298.15 |
0.5049 |
908.96 |
298.15 |
0.6193 |
882.85 |
298.15 |
0.6275 |
880.81 |
313.15 |
0.1672 |
964.04 |
313.15 |
0.2858 |
943.6 |
313.15 |
0.2894 |
942.82 |
313.15 |
0.3525 |
930.27 |
313.15 |
0.3757 |
925.3 |
313.15 |
0.4420 |
911.19 |
313.15 |
0.4445 |
910.92 |
313.15 |
0.4982 |
898.47 |
313.15 |
0.5018 |
897.76 |
313.15 |
0.6180 |
870.51 |
313.15 |
0.6271 |
868.41 |
313.15 |
0.7114 |
848.29 |
Mass density, kg/m3
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
Molality, mol/kg of Water (2) - Liquid |
Mass density, kg/m3 - Liquid |
0.0000 |
785.207 |
0.2140 |
786.407 |
0.2705 |
786.72 |
0.3199 |
786.998 |
0.3659 |
787.262 |
0.4543 |
787.753 |
0.5541 |
788.3 |
0.6437 |
788.782 |
0.7430 |
789.321 |
0.8349 |
789.775 |
0.9264 |
790.279 |
1.0189 |
790.734 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol (1) - Liquid |
Mass density, kg/m3 - Liquid |
283.15 |
0.0000 |
999.7 |
283.15 |
0.0106 |
994.82 |
283.15 |
0.0206 |
990.75 |
283.15 |
0.0301 |
987.45 |
283.15 |
0.0400 |
984.42 |
283.15 |
0.0513 |
981.3 |
283.15 |
0.0630 |
978.39 |
283.15 |
0.0737 |
975.9 |
283.15 |
0.0903 |
972.21 |
283.15 |
0.0988 |
970.36 |
283.15 |
0.1118 |
967.43 |
283.15 |
0.1274 |
963.79 |
283.15 |
0.1412 |
960.35 |
283.15 |
0.1546 |
956.87 |
283.15 |
0.1712 |
952.38 |
283.15 |
0.1883 |
947.66 |
283.15 |
0.2027 |
943.56 |
283.15 |
0.2245 |
937.39 |
283.15 |
0.2413 |
932.58 |
283.15 |
0.2602 |
927.36 |
283.15 |
0.2810 |
921.7 |
283.15 |
0.3008 |
916.48 |
283.15 |
0.3214 |
911.12 |
283.15 |
0.3422 |
905.93 |
283.15 |
0.3708 |
899.06 |
283.15 |
0.3898 |
894.64 |
283.15 |
0.4225 |
887.34 |
283.15 |
0.4419 |
883.22 |
283.15 |
0.4775 |
875.94 |
283.15 |
0.4998 |
871.65 |
283.15 |
0.5446 |
863.32 |
283.15 |
0.5631 |
860.06 |
283.15 |
0.6134 |
851.45 |
283.15 |
0.6385 |
847.44 |
283.15 |
0.6889 |
839.59 |
283.15 |
0.7182 |
835.36 |
283.15 |
0.7797 |
826.69 |
283.15 |
0.8252 |
820.4 |
283.15 |
0.8740 |
813.94 |
283.15 |
0.9388 |
805.69 |
283.15 |
1.0000 |
797.93 |
288.15 |
0.0000 |
999.1 |
288.15 |
0.0106 |
994.16 |
288.15 |
0.0206 |
990.1 |
288.15 |
0.0301 |
986.69 |
288.15 |
0.0400 |
983.51 |
288.15 |
0.0513 |
980.2 |
288.15 |
0.0630 |
977.08 |
288.15 |
0.0737 |
974.36 |
288.15 |
0.0903 |
970.32 |
288.15 |
0.0988 |
968.26 |
288.15 |
0.1118 |
965.05 |
288.15 |
0.1274 |
961.09 |
288.15 |
0.1412 |
957.42 |
288.15 |
0.1546 |
953.75 |
288.15 |
0.1712 |
949.03 |
288.15 |
0.1883 |
944.18 |
288.15 |
0.2027 |
939.92 |
288.15 |
0.2245 |
933.59 |
288.15 |
0.2413 |
928.78 |
288.15 |
0.2602 |
923.46 |
288.15 |
0.2810 |
917.78 |
288.15 |
0.3008 |
912.42 |
288.15 |
0.3214 |
907.08 |
288.15 |
0.3422 |
901.83 |
288.15 |
0.3708 |
894.93 |
288.15 |
0.3898 |
890.41 |
288.15 |
0.4225 |
883.12 |
288.15 |
0.4419 |
879.04 |
288.15 |
0.4775 |
871.68 |
288.15 |
0.4998 |
867.4 |
288.15 |
0.5446 |
859.02 |
288.15 |
0.5631 |
855.68 |
288.15 |
0.6134 |
847.1 |
288.15 |
0.6385 |
843.05 |
288.15 |
0.6889 |
835.22 |
288.15 |
0.7182 |
830.94 |
288.15 |
0.7797 |
822.24 |
288.15 |
0.8252 |
815.98 |
288.15 |
0.8740 |
809.54 |
288.15 |
0.9388 |
801.31 |
288.15 |
1.0000 |
793.64 |
293.15 |
0.0000 |
998.2 |
293.15 |
0.0106 |
993.29 |
293.15 |
0.0206 |
989.19 |
293.15 |
0.0301 |
985.7 |
293.15 |
0.0400 |
982.4 |
293.15 |
0.0513 |
978.92 |
293.15 |
0.0630 |
975.59 |
293.15 |
0.0737 |
972.67 |
293.15 |
0.0903 |
968.29 |
293.15 |
0.0988 |
966.06 |
293.15 |
0.1118 |
962.58 |
293.15 |
0.1274 |
958.36 |
293.15 |
0.1412 |
954.46 |
293.15 |
0.1546 |
950.63 |
293.15 |
0.1712 |
945.74 |
293.15 |
0.1883 |
940.71 |
293.15 |
0.2027 |
936.37 |
293.15 |
0.2245 |
929.93 |
293.15 |
0.2413 |
925.03 |
293.15 |
0.2602 |
919.65 |
293.15 |
0.2810 |
913.9 |
293.15 |
0.3008 |
908.52 |
293.15 |
0.3214 |
903.14 |
293.15 |
0.3422 |
897.88 |
293.15 |
0.3708 |
890.89 |
293.15 |
0.3898 |
886.45 |
293.15 |
0.4225 |
879.04 |
293.15 |
0.4419 |
874.93 |
293.15 |
0.4775 |
867.54 |
293.15 |
0.4998 |
863.22 |
293.15 |
0.5446 |
854.84 |
293.15 |
0.5631 |
851.52 |
293.15 |
0.6134 |
842.88 |
293.15 |
0.6385 |
838.78 |
293.15 |
0.6889 |
830.97 |
293.15 |
0.7182 |
826.69 |
293.15 |
0.7797 |
818.01 |
293.15 |
0.8252 |
811.73 |
293.15 |
0.8740 |
805.3 |
293.15 |
0.9388 |
797.05 |
293.15 |
1.0000 |
789.33 |
298.15 |
0.0000 |
997.04 |
298.15 |
0.0106 |
992.13 |
298.15 |
0.0206 |
987.96 |
298.15 |
0.0301 |
984.4 |
298.15 |
0.0400 |
981.01 |
298.15 |
0.0513 |
977.36 |
298.15 |
0.0630 |
973.84 |
298.15 |
0.0737 |
970.72 |
298.15 |
0.0903 |
966.02 |
298.15 |
0.0988 |
963.64 |
298.15 |
0.1118 |
959.93 |
298.15 |
0.1274 |
955.44 |
298.15 |
0.1412 |
951.35 |
298.15 |
0.1546 |
947.34 |
298.15 |
0.1712 |
942.26 |
298.15 |
0.1883 |
937.13 |
298.15 |
0.2027 |
932.69 |
298.15 |
0.2245 |
926.16 |
298.15 |
0.2413 |
921.17 |
298.15 |
0.2602 |
915.75 |
298.15 |
0.2810 |
909.9 |
298.15 |
0.3008 |
904.53 |
298.15 |
0.3214 |
899.05 |
298.15 |
0.3422 |
893.76 |
298.15 |
0.3708 |
886.75 |
298.15 |
0.3898 |
882.24 |
298.15 |
0.4225 |
874.82 |
298.15 |
0.4419 |
870.68 |
298.15 |
0.4775 |
863.28 |
298.15 |
0.4998 |
858.98 |
298.15 |
0.5446 |
850.55 |
298.15 |
0.5631 |
847.23 |
298.15 |
0.6134 |
838.56 |
298.15 |
0.6385 |
834.45 |
298.15 |
0.6889 |
826.63 |
298.15 |
0.7182 |
822.35 |
298.15 |
0.7797 |
813.64 |
298.15 |
0.8252 |
807.39 |
298.15 |
0.8740 |
800.98 |
298.15 |
0.9388 |
792.82 |
298.15 |
1.0000 |
785.22 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Molality, mol/kg of Ethanol (1) - Liquid |
Mass density, kg/m3 - Liquid |
293.15 |
14.0 |
936.706 |
293.15 |
16.0 |
930.583 |
293.15 |
18.0 |
924.182 |
298.15 |
14.0 |
933.024 |
298.15 |
16.0 |
926.799 |
298.15 |
18.0 |
920.298 |
303.15 |
14.0 |
929.265 |
303.15 |
16.0 |
922.942 |
303.15 |
18.0 |
916.351 |
308.15 |
14.0 |
925.437 |
308.15 |
16.0 |
919.015 |
308.15 |
18.0 |
912.337 |
313.15 |
14.0 |
921.529 |
313.15 |
16.0 |
915.018 |
313.15 |
18.0 |
908.255 |
293.15 |
20.0 |
918.792 |
293.15 |
22.0 |
913.462 |
298.15 |
20.0 |
914.849 |
298.15 |
22.0 |
909.466 |
303.15 |
20.0 |
910.842 |
303.15 |
22.0 |
905.406 |
308.15 |
20.0 |
906.77 |
308.15 |
22.0 |
901.281 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Water (2) - Liquid |
Mass density, kg/m3 - Liquid |
298.15 |
0.0998 |
797.6 |
298.15 |
0.2018 |
810.78 |
298.15 |
0.3085 |
826.73 |
298.15 |
0.4145 |
843.26 |
298.15 |
0.5001 |
858.65 |
298.15 |
0.6205 |
885.56 |
298.15 |
0.7005 |
904.69 |
298.15 |
0.7992 |
933.6 |
298.15 |
0.9051 |
965.51 |
318.15 |
0.1000 |
780.53 |
318.15 |
0.2010 |
793.6 |
318.15 |
0.3001 |
807.71 |
318.15 |
0.4004 |
823.81 |
318.15 |
0.5003 |
840.31 |
318.15 |
0.5998 |
863.31 |
318.15 |
0.7001 |
888.76 |
318.15 |
0.8001 |
919.19 |
318.15 |
0.9000 |
952.47 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Water (2) - Liquid |
Mass density, kg/m3 - Liquid |
283.15 |
0.0805 |
808.05 |
283.15 |
0.1584 |
818.14 |
283.15 |
0.2376 |
828.89 |
283.15 |
0.3322 |
842.93 |
283.15 |
0.4026 |
854.12 |
283.15 |
0.4910 |
869.86 |
283.15 |
0.5806 |
888.19 |
283.15 |
0.6480 |
903.57 |
283.15 |
0.7185 |
921.65 |
283.15 |
0.8009 |
944.6 |
283.15 |
0.8813 |
965.96 |
283.15 |
0.9605 |
984.04 |
288.15 |
0.0805 |
803.79 |
288.15 |
0.1584 |
813.87 |
288.15 |
0.2376 |
824.61 |
288.15 |
0.3322 |
838.67 |
288.15 |
0.4026 |
849.89 |
288.15 |
0.4910 |
865.67 |
288.15 |
0.5806 |
884.08 |
288.15 |
0.6480 |
899.55 |
288.15 |
0.7185 |
917.78 |
288.15 |
0.8009 |
941.07 |
288.15 |
0.8813 |
963.49 |
288.15 |
0.9605 |
983.11 |
293.15 |
0.0805 |
799.51 |
293.15 |
0.1584 |
809.57 |
293.15 |
0.2376 |
820.29 |
293.15 |
0.3322 |
834.37 |
293.15 |
0.4026 |
845.61 |
293.15 |
0.4910 |
861.44 |
293.15 |
0.5806 |
879.93 |
293.15 |
0.6480 |
895.48 |
293.15 |
0.7185 |
913.84 |
293.15 |
0.8009 |
937.48 |
293.15 |
0.8813 |
960.85 |
293.15 |
0.9605 |
981.89 |
298.15 |
0.0805 |
795.19 |
298.15 |
0.1584 |
805.23 |
298.15 |
0.2376 |
815.93 |
298.15 |
0.3322 |
830.01 |
298.15 |
0.4026 |
841.27 |
298.15 |
0.4910 |
857.16 |
298.15 |
0.5806 |
875.71 |
298.15 |
0.6480 |
891.35 |
298.15 |
0.7185 |
909.85 |
298.15 |
0.8009 |
933.81 |
298.15 |
0.8813 |
958.06 |
298.15 |
0.9605 |
980.42 |
303.15 |
0.0805 |
790.85 |
303.15 |
0.1584 |
800.84 |
303.15 |
0.2376 |
811.53 |
303.15 |
0.3322 |
825.61 |
303.15 |
0.4026 |
836.89 |
303.15 |
0.4910 |
852.81 |
303.15 |
0.5806 |
871.44 |
303.15 |
0.6480 |
887.16 |
303.15 |
0.7185 |
905.8 |
303.15 |
0.8009 |
930.07 |
303.15 |
0.8813 |
955.13 |
303.15 |
0.9605 |
978.75 |
308.15 |
0.0805 |
786.45 |
308.15 |
0.1584 |
796.41 |
308.15 |
0.2376 |
807.07 |
308.15 |
0.3322 |
821.15 |
308.15 |
0.4026 |
832.45 |
308.15 |
0.4910 |
848.4 |
308.15 |
0.5806 |
867.11 |
308.15 |
0.6480 |
882.91 |
308.15 |
0.7185 |
901.68 |
308.15 |
0.8009 |
926.25 |
308.15 |
0.8813 |
952.05 |
308.15 |
0.9605 |
976.91 |
313.15 |
0.0805 |
782.01 |
313.15 |
0.1584 |
791.93 |
313.15 |
0.2376 |
802.5 |
313.15 |
0.3322 |
816.63 |
313.15 |
0.4026 |
827.94 |
313.15 |
0.4910 |
843.95 |
313.15 |
0.5806 |
862.72 |
313.15 |
0.6480 |
878.59 |
313.15 |
0.7185 |
897.49 |
313.15 |
0.8009 |
922.34 |
313.15 |
0.8813 |
948.82 |
313.15 |
0.9605 |
974.89 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Mole fraction of Water (2) - Liquid |
Mass density, kg/m3 - Liquid |
0.0480 |
791.06 |
0.1116 |
799.08 |
0.1599 |
805.32 |
0.1761 |
807.44 |
0.2668 |
820.06 |
0.3010 |
825.06 |
0.3994 |
840.69 |
0.4970 |
858.26 |
0.6122 |
882.42 |
0.7116 |
907.85 |
0.7774 |
926.61 |
0.8145 |
937.62 |
0.8529 |
949.42 |
0.8967 |
960.95 |
0.9481 |
976.77 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Mole fraction of Water (2) - Liquid |
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
0.1000 |
268.10 |
824.9 |
0.1000 |
273.10 |
820.3 |
0.1000 |
278.10 |
815.9 |
0.1000 |
283.10 |
811.4 |
0.1000 |
288.15 |
806.9 |
0.1000 |
293.15 |
802.1 |
0.1000 |
298.15 |
797.7 |
0.1000 |
303.15 |
793.0 |
0.1000 |
308.15 |
788.2 |
0.1000 |
313.15 |
783.6 |
0.1000 |
318.15 |
779.0 |
0.1000 |
323.15 |
774.3 |
0.2000 |
268.10 |
838.2 |
0.2000 |
273.10 |
833.7 |
0.2000 |
278.10 |
829.0 |
0.2000 |
283.10 |
824.7 |
0.2000 |
288.15 |
820.1 |
0.2000 |
293.15 |
815.6 |
0.2000 |
298.15 |
811.0 |
0.2000 |
303.15 |
806.0 |
0.2000 |
308.15 |
801.4 |
0.2000 |
313.15 |
796.8 |
0.2000 |
318.15 |
792.2 |
0.2000 |
323.15 |
787.5 |
0.3000 |
268.10 |
852.2 |
0.3000 |
273.10 |
847.7 |
0.3000 |
278.10 |
842.9 |
0.3000 |
283.10 |
838.5 |
0.3000 |
288.15 |
833.9 |
0.3000 |
293.15 |
829.4 |
0.3000 |
298.15 |
825.1 |
0.3000 |
303.15 |
820.6 |
0.3000 |
308.15 |
816.0 |
0.3000 |
313.15 |
811.1 |
0.3000 |
318.15 |
806.6 |
0.3000 |
323.15 |
801.9 |
0.4000 |
268.10 |
867.7 |
0.4000 |
273.10 |
863.4 |
0.4000 |
278.10 |
858.8 |
0.4000 |
283.10 |
854.1 |
0.4000 |
288.15 |
849.5 |
0.4000 |
293.15 |
845.0 |
0.4000 |
298.15 |
840.6 |
0.4000 |
303.15 |
836.1 |
0.4000 |
308.15 |
831.4 |
0.4000 |
313.15 |
826.9 |
0.4000 |
318.15 |
822.4 |
0.4000 |
323.15 |
817.7 |
0.5000 |
268.10 |
886.6 |
0.5000 |
273.10 |
882.1 |
0.5000 |
278.10 |
877.7 |
0.5000 |
283.10 |
872.8 |
0.5000 |
288.15 |
868.5 |
0.5000 |
293.15 |
863.8 |
0.5000 |
298.15 |
859.2 |
0.5000 |
303.15 |
854.8 |
0.5000 |
308.15 |
850.1 |
0.5000 |
313.15 |
845.2 |
0.5000 |
318.15 |
840.5 |
0.5000 |
323.15 |
835.8 |
0.6000 |
268.10 |
908.1 |
0.6000 |
273.10 |
903.5 |
0.6000 |
278.10 |
899.3 |
0.6000 |
283.10 |
894.6 |
0.6000 |
288.15 |
889.6 |
0.6000 |
293.15 |
885.1 |
0.6000 |
298.15 |
880.6 |
0.6000 |
303.15 |
876.1 |
0.6000 |
308.15 |
871.4 |
0.6000 |
313.15 |
866.8 |
0.6000 |
318.15 |
862.1 |
0.6000 |
323.15 |
857.3 |
0.7000 |
268.10 |
931.6 |
0.7000 |
273.10 |
927.1 |
0.7000 |
278.10 |
922.7 |
0.7000 |
283.10 |
918.7 |
0.7000 |
288.15 |
914.5 |
0.7000 |
293.15 |
909.9 |
0.7000 |
298.15 |
905.3 |
0.7000 |
303.15 |
901.0 |
0.7000 |
308.15 |
896.5 |
0.7000 |
313.15 |
892.0 |
0.7000 |
318.15 |
887.4 |
0.7000 |
323.15 |
883.0 |
0.8000 |
268.10 |
951.0 |
0.8000 |
273.10 |
948.0 |
0.8000 |
278.10 |
945.0 |
0.8000 |
283.10 |
941.4 |
0.8000 |
288.15 |
938.0 |
0.8000 |
293.15 |
934.6 |
0.8000 |
298.15 |
931.3 |
0.8000 |
303.15 |
927.6 |
0.8000 |
308.15 |
923.8 |
0.8000 |
313.15 |
919.5 |
0.8000 |
318.15 |
915.5 |
0.8000 |
323.15 |
911.2 |
0.9000 |
268.10 |
977.3 |
0.9000 |
273.10 |
975.6 |
0.9000 |
278.10 |
973.2 |
0.9000 |
283.10 |
970.8 |
0.9000 |
288.15 |
967.3 |
0.9000 |
293.15 |
963.7 |
0.9000 |
298.15 |
960.3 |
0.9000 |
303.15 |
956.2 |
0.9000 |
308.15 |
952.7 |
0.9000 |
313.15 |
949.0 |
0.9000 |
318.15 |
945.5 |
0.9000 |
323.15 |
942.0 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mass fraction of Water (2) - Liquid |
Mass density, kg/m3 - Liquid |
303.15 |
0.1500 |
822.7 |
303.15 |
0.2000 |
836.0 |
303.15 |
0.2500 |
848.8 |
308.15 |
0.1500 |
818.4 |
308.15 |
0.2000 |
831.8 |
308.15 |
0.2500 |
843.0 |
313.15 |
0.1500 |
813.1 |
313.15 |
0.2000 |
827.1 |
313.15 |
0.2500 |
838.2 |
318.15 |
0.1500 |
807.1 |
318.15 |
0.2000 |
821.0 |
318.15 |
0.2500 |
833.6 |
323.15 |
0.1500 |
801.4 |
323.15 |
0.2000 |
814.6 |
323.15 |
0.2500 |
827.5 |
328.15 |
0.1500 |
796.9 |
328.15 |
0.2000 |
809.1 |
328.15 |
0.2500 |
822.5 |
Mass density, kg/m3
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Volume fraction = 0.5 (Liquid)
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
288.15 |
930.86 |
293.15 |
927.08 |
298.15 |
923.22 |
303.15 |
919.31 |
308.15 |
915.32 |
313.15 |
911.27 |
318.15 |
908.03 |
318.15 |
907.3 |
323.15 |
904.32 |
323.15 |
903.71 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mass fraction of Ethanol (1) - Liquid |
Mass density, kg/m3 - Liquid |
293.15 |
0.1000 |
981.8 |
293.15 |
0.2000 |
968.2 |
293.15 |
0.3000 |
953.6 |
293.15 |
0.4000 |
935.5 |
293.15 |
0.5000 |
913.9 |
303.15 |
0.1000 |
979.0 |
303.15 |
0.2000 |
964.1 |
303.15 |
0.3000 |
947.4 |
303.15 |
0.4000 |
927.2 |
303.15 |
0.5000 |
905.6 |
313.15 |
0.1000 |
974.6 |
313.15 |
0.2000 |
958.7 |
313.15 |
0.3000 |
940.3 |
313.15 |
0.4000 |
919.8 |
313.15 |
0.5000 |
897.6 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Ethanol (1) - Liquid |
Mass density, kg/m3 - Liquid |
298.15 |
100.00 |
0.0030 |
995.3 |
298.15 |
100.00 |
0.0042 |
994.5 |
298.15 |
100.00 |
0.0082 |
993.0 |
298.15 |
100.00 |
0.0119 |
991.5 |
298.15 |
100.00 |
0.0158 |
989.8 |
298.15 |
100.00 |
0.0184 |
988.4 |
298.15 |
100.00 |
0.0219 |
987.6 |
298.15 |
100.00 |
0.0255 |
986.0 |
298.15 |
100.00 |
0.0279 |
984.7 |
298.15 |
100.00 |
0.0315 |
984.0 |
298.15 |
100.00 |
0.0366 |
981.6 |
298.15 |
100.00 |
0.0392 |
980.7 |
298.15 |
100.00 |
0.0439 |
979.2 |
298.15 |
100.00 |
0.0483 |
977.5 |
298.15 |
100.00 |
0.0516 |
977.1 |
298.15 |
100.00 |
0.0559 |
975.8 |
298.15 |
100.00 |
0.0600 |
974.5 |
298.15 |
100.00 |
0.0652 |
972.9 |
298.15 |
100.00 |
0.0679 |
972.2 |
298.15 |
100.00 |
0.0722 |
971.0 |
298.15 |
100.00 |
0.0801 |
968.6 |
298.15 |
100.00 |
0.0840 |
967.9 |
298.15 |
100.00 |
0.0879 |
966.7 |
298.15 |
100.00 |
0.0926 |
965.6 |
298.15 |
100.00 |
0.0958 |
964.6 |
298.15 |
100.00 |
0.1006 |
963.2 |
298.15 |
100.00 |
0.1111 |
960.2 |
298.15 |
100.00 |
0.1225 |
956.8 |
298.15 |
100.00 |
0.1296 |
954.9 |
298.15 |
100.00 |
0.1402 |
951.8 |
298.15 |
100.00 |
0.1510 |
948.4 |
298.15 |
100.00 |
0.1601 |
945.6 |
298.15 |
100.00 |
0.1703 |
942.5 |
298.15 |
100.00 |
0.1800 |
939.8 |
298.15 |
100.00 |
0.1903 |
936.5 |
298.15 |
100.00 |
0.1996 |
933.5 |
298.15 |
100.00 |
0.2269 |
925.4 |
298.15 |
100.00 |
0.2502 |
918.5 |
298.15 |
100.00 |
0.2745 |
911.7 |
298.15 |
100.00 |
0.3009 |
904.5 |
298.15 |
100.00 |
0.3500 |
891.9 |
298.15 |
100.00 |
0.4034 |
879.4 |
298.15 |
100.00 |
0.4501 |
868.8 |
298.15 |
100.00 |
0.4980 |
859.3 |
298.15 |
100.00 |
0.5501 |
849.5 |
298.15 |
100.00 |
0.5998 |
840.9 |
298.15 |
100.00 |
0.6489 |
832.7 |
298.15 |
100.00 |
0.6967 |
825.2 |
298.15 |
100.00 |
0.7475 |
818.2 |
298.15 |
100.00 |
0.7996 |
810.9 |
298.15 |
100.00 |
0.8484 |
804.4 |
298.15 |
100.00 |
0.8993 |
798.0 |
298.15 |
100.00 |
0.9503 |
791.7 |
298.15 |
100.00 |
1.0000 |
785.7 |
298.15 |
10000.00 |
0.0030 |
999.8 |
298.15 |
10000.00 |
0.0042 |
998.9 |
298.15 |
10000.00 |
0.0082 |
997.3 |
298.15 |
10000.00 |
0.0119 |
995.8 |
298.15 |
10000.00 |
0.0158 |
994.0 |
298.15 |
10000.00 |
0.0184 |
992.6 |
298.15 |
10000.00 |
0.0219 |
991.7 |
298.15 |
10000.00 |
0.0255 |
990.2 |
298.15 |
10000.00 |
0.0279 |
988.7 |
298.15 |
10000.00 |
0.0315 |
988.0 |
298.15 |
10000.00 |
0.0366 |
985.7 |
298.15 |
10000.00 |
0.0392 |
984.7 |
298.15 |
10000.00 |
0.0439 |
983.3 |
298.15 |
10000.00 |
0.0483 |
981.6 |
298.15 |
10000.00 |
0.0516 |
981.0 |
298.15 |
10000.00 |
0.0559 |
979.8 |
298.15 |
10000.00 |
0.0600 |
978.5 |
298.15 |
10000.00 |
0.0652 |
976.9 |
298.15 |
10000.00 |
0.0679 |
976.1 |
298.15 |
10000.00 |
0.0722 |
974.9 |
298.15 |
10000.00 |
0.0801 |
972.4 |
298.15 |
10000.00 |
0.0840 |
971.8 |
298.15 |
10000.00 |
0.0879 |
970.6 |
298.15 |
10000.00 |
0.0926 |
969.3 |
298.15 |
10000.00 |
0.0958 |
968.5 |
298.15 |
10000.00 |
0.1006 |
967.1 |
298.15 |
10000.00 |
0.1111 |
964.1 |
298.15 |
10000.00 |
0.1225 |
960.7 |
298.15 |
10000.00 |
0.1296 |
958.8 |
298.15 |
10000.00 |
0.1402 |
955.8 |
298.15 |
10000.00 |
0.1510 |
952.5 |
298.15 |
10000.00 |
0.1601 |
949.8 |
298.15 |
10000.00 |
0.1703 |
946.7 |
298.15 |
10000.00 |
0.1800 |
943.9 |
298.15 |
10000.00 |
0.1903 |
940.9 |
298.15 |
10000.00 |
0.1996 |
938.0 |
298.15 |
10000.00 |
0.2269 |
930.0 |
298.15 |
10000.00 |
0.2502 |
923.3 |
298.15 |
10000.00 |
0.2745 |
916.6 |
298.15 |
10000.00 |
0.3009 |
909.6 |
298.15 |
10000.00 |
0.3500 |
897.1 |
298.15 |
10000.00 |
0.4034 |
884.9 |
298.15 |
10000.00 |
0.4501 |
874.7 |
298.15 |
10000.00 |
0.4980 |
865.4 |
298.15 |
10000.00 |
0.5501 |
855.8 |
298.15 |
10000.00 |
0.5998 |
847.4 |
298.15 |
10000.00 |
0.6489 |
839.5 |
298.15 |
10000.00 |
0.6967 |
832.3 |
298.15 |
10000.00 |
0.7475 |
825.4 |
298.15 |
10000.00 |
0.7996 |
818.3 |
298.15 |
10000.00 |
0.8484 |
812.1 |
298.15 |
10000.00 |
0.8993 |
805.8 |
298.15 |
10000.00 |
0.9503 |
799.9 |
298.15 |
10000.00 |
1.0000 |
794.0 |
298.15 |
20000.00 |
0.0030 |
1004.2 |
298.15 |
20000.00 |
0.0042 |
1003.2 |
298.15 |
20000.00 |
0.0082 |
1001.7 |
298.15 |
20000.00 |
0.0119 |
1000.1 |
298.15 |
20000.00 |
0.0158 |
998.2 |
298.15 |
20000.00 |
0.0184 |
996.8 |
298.15 |
20000.00 |
0.0219 |
995.9 |
298.15 |
20000.00 |
0.0255 |
994.4 |
298.15 |
20000.00 |
0.0279 |
992.9 |
298.15 |
20000.00 |
0.0315 |
992.1 |
298.15 |
20000.00 |
0.0366 |
989.8 |
298.15 |
20000.00 |
0.0392 |
988.6 |
298.15 |
20000.00 |
0.0439 |
987.3 |
298.15 |
20000.00 |
0.0483 |
985.6 |
298.15 |
20000.00 |
0.0516 |
985.1 |
298.15 |
20000.00 |
0.0559 |
983.8 |
298.15 |
20000.00 |
0.0600 |
982.4 |
298.15 |
20000.00 |
0.0652 |
980.8 |
298.15 |
20000.00 |
0.0679 |
980.0 |
298.15 |
20000.00 |
0.0722 |
978.7 |
298.15 |
20000.00 |
0.0801 |
976.2 |
298.15 |
20000.00 |
0.0840 |
975.7 |
298.15 |
20000.00 |
0.0879 |
974.4 |
298.15 |
20000.00 |
0.0926 |
973.2 |
298.15 |
20000.00 |
0.0958 |
972.4 |
298.15 |
20000.00 |
0.1006 |
971.0 |
298.15 |
20000.00 |
0.1111 |
968.0 |
298.15 |
20000.00 |
0.1225 |
964.7 |
298.15 |
20000.00 |
0.1296 |
962.8 |
298.15 |
20000.00 |
0.1402 |
961.3 |
298.15 |
20000.00 |
0.1510 |
956.6 |
298.15 |
20000.00 |
0.1601 |
953.9 |
298.15 |
20000.00 |
0.1703 |
950.9 |
298.15 |
20000.00 |
0.1800 |
948.1 |
298.15 |
20000.00 |
0.1903 |
945.2 |
298.15 |
20000.00 |
0.1996 |
942.3 |
298.15 |
20000.00 |
0.2269 |
934.5 |
298.15 |
20000.00 |
0.2502 |
928.0 |
298.15 |
20000.00 |
0.2745 |
921.3 |
298.15 |
20000.00 |
0.3009 |
914.5 |
298.15 |
20000.00 |
0.3500 |
902.3 |
298.15 |
20000.00 |
0.4034 |
890.4 |
298.15 |
20000.00 |
0.4501 |
880.4 |
298.15 |
20000.00 |
0.4980 |
871.3 |
298.15 |
20000.00 |
0.5501 |
861.9 |
298.15 |
20000.00 |
0.5998 |
853.7 |
298.15 |
20000.00 |
0.6489 |
846.0 |
298.15 |
20000.00 |
0.6967 |
839.0 |
298.15 |
20000.00 |
0.7475 |
832.3 |
298.15 |
20000.00 |
0.7996 |
825.4 |
298.15 |
20000.00 |
0.8484 |
819.3 |
298.15 |
20000.00 |
0.8993 |
813.3 |
298.15 |
20000.00 |
0.9503 |
807.5 |
298.15 |
20000.00 |
1.0000 |
801.9 |
298.15 |
30000.00 |
0.0030 |
1008.5 |
298.15 |
30000.00 |
0.0042 |
1007.4 |
298.15 |
30000.00 |
0.0082 |
1005.9 |
298.15 |
30000.00 |
0.0119 |
1004.3 |
298.15 |
30000.00 |
0.0158 |
1002.4 |
298.15 |
30000.00 |
0.0184 |
1000.9 |
298.15 |
30000.00 |
0.0219 |
1000.1 |
298.15 |
30000.00 |
0.0255 |
998.4 |
298.15 |
30000.00 |
0.0279 |
996.9 |
298.15 |
30000.00 |
0.0315 |
996.1 |
298.15 |
30000.00 |
0.0366 |
993.8 |
298.15 |
30000.00 |
0.0392 |
992.6 |
298.15 |
30000.00 |
0.0439 |
991.2 |
298.15 |
30000.00 |
0.0483 |
989.5 |
298.15 |
30000.00 |
0.0516 |
988.9 |
298.15 |
30000.00 |
0.0559 |
987.7 |
298.15 |
30000.00 |
0.0600 |
986.3 |
298.15 |
30000.00 |
0.0652 |
984.7 |
298.15 |
30000.00 |
0.0679 |
983.9 |
298.15 |
30000.00 |
0.0722 |
982.6 |
298.15 |
30000.00 |
0.0801 |
980.0 |
298.15 |
30000.00 |
0.0840 |
979.5 |
298.15 |
30000.00 |
0.0879 |
978.2 |
298.15 |
30000.00 |
0.0926 |
976.9 |
298.15 |
30000.00 |
0.0958 |
976.1 |
298.15 |
30000.00 |
0.1006 |
974.8 |
298.15 |
30000.00 |
0.1111 |
971.7 |
298.15 |
30000.00 |
0.1225 |
968.5 |
298.15 |
30000.00 |
0.1296 |
966.7 |
298.15 |
30000.00 |
0.1402 |
963.7 |
298.15 |
30000.00 |
0.1510 |
960.5 |
298.15 |
30000.00 |
0.1601 |
957.9 |
298.15 |
30000.00 |
0.1703 |
955.0 |
298.15 |
30000.00 |
0.1800 |
952.2 |
298.15 |
30000.00 |
0.1903 |
949.3 |
298.15 |
30000.00 |
0.1996 |
946.5 |
298.15 |
30000.00 |
0.2269 |
938.7 |
298.15 |
30000.00 |
0.2502 |
932.4 |
298.15 |
30000.00 |
0.2745 |
925.9 |
298.15 |
30000.00 |
0.3009 |
919.2 |
298.15 |
30000.00 |
0.3500 |
907.2 |
298.15 |
30000.00 |
0.4034 |
895.5 |
298.15 |
30000.00 |
0.4501 |
885.7 |
298.15 |
30000.00 |
0.4980 |
876.8 |
298.15 |
30000.00 |
0.5501 |
867.6 |
298.15 |
30000.00 |
0.5998 |
859.5 |
298.15 |
30000.00 |
0.6489 |
852.0 |
298.15 |
30000.00 |
0.6967 |
845.1 |
298.15 |
30000.00 |
0.7475 |
838.5 |
298.15 |
30000.00 |
0.7996 |
831.9 |
298.15 |
30000.00 |
0.8484 |
825.9 |
298.15 |
30000.00 |
0.8993 |
820.0 |
298.15 |
30000.00 |
0.9503 |
814.5 |
298.15 |
30000.00 |
1.0000 |
808.9 |
298.15 |
40000.00 |
0.0030 |
1012.7 |
298.15 |
40000.00 |
0.0042 |
1011.5 |
298.15 |
40000.00 |
0.0082 |
1010.0 |
298.15 |
40000.00 |
0.0119 |
1008.3 |
298.15 |
40000.00 |
0.0158 |
1006.4 |
298.15 |
40000.00 |
0.0184 |
1005.0 |
298.15 |
40000.00 |
0.0219 |
1004.1 |
298.15 |
40000.00 |
0.0255 |
1002.4 |
298.15 |
40000.00 |
0.0279 |
1000.8 |
298.15 |
40000.00 |
0.0315 |
1000.0 |
298.15 |
40000.00 |
0.0366 |
997.6 |
298.15 |
40000.00 |
0.0392 |
996.4 |
298.15 |
40000.00 |
0.0439 |
995.1 |
298.15 |
40000.00 |
0.0483 |
993.3 |
298.15 |
40000.00 |
0.0516 |
992.7 |
298.15 |
40000.00 |
0.0559 |
991.5 |
298.15 |
40000.00 |
0.0600 |
990.1 |
298.15 |
40000.00 |
0.0652 |
988.4 |
298.15 |
40000.00 |
0.0679 |
987.6 |
298.15 |
40000.00 |
0.0722 |
986.3 |
298.15 |
40000.00 |
0.0801 |
983.7 |
298.15 |
40000.00 |
0.0840 |
983.2 |
298.15 |
40000.00 |
0.0879 |
981.9 |
298.15 |
40000.00 |
0.0926 |
980.6 |
298.15 |
40000.00 |
0.0958 |
979.8 |
298.15 |
40000.00 |
0.1006 |
978.5 |
298.15 |
40000.00 |
0.1111 |
975.4 |
298.15 |
40000.00 |
0.1225 |
972.2 |
298.15 |
40000.00 |
0.1296 |
970.4 |
298.15 |
40000.00 |
0.1402 |
967.3 |
298.15 |
40000.00 |
0.1510 |
964.3 |
298.15 |
40000.00 |
0.1601 |
961.7 |
298.15 |
40000.00 |
0.1703 |
958.9 |
298.15 |
40000.00 |
0.1800 |
956.2 |
298.15 |
40000.00 |
0.1903 |
953.3 |
298.15 |
40000.00 |
0.1996 |
950.5 |
298.15 |
40000.00 |
0.2269 |
942.9 |
298.15 |
40000.00 |
0.2502 |
936.7 |
298.15 |
40000.00 |
0.2745 |
930.3 |
298.15 |
40000.00 |
0.3009 |
923.7 |
298.15 |
40000.00 |
0.3500 |
911.9 |
298.15 |
40000.00 |
0.4034 |
900.4 |
298.15 |
40000.00 |
0.4501 |
890.8 |
298.15 |
40000.00 |
0.4980 |
882.0 |
298.15 |
40000.00 |
0.5501 |
873.0 |
298.15 |
40000.00 |
0.5998 |
865.1 |
298.15 |
40000.00 |
0.6489 |
857.7 |
298.15 |
40000.00 |
0.6967 |
851.0 |
298.15 |
40000.00 |
0.7475 |
844.5 |
298.15 |
40000.00 |
0.7996 |
838.1 |
298.15 |
40000.00 |
0.8484 |
832.3 |
298.15 |
40000.00 |
0.8993 |
826.5 |
298.15 |
40000.00 |
0.9503 |
821.0 |
298.15 |
40000.00 |
1.0000 |
815.7 |
323.15 |
100.00 |
0.0030 |
986.5 |
323.15 |
100.00 |
0.0042 |
985.4 |
323.15 |
100.00 |
0.0082 |
984.0 |
323.15 |
100.00 |
0.0119 |
982.7 |
323.15 |
100.00 |
0.0158 |
980.5 |
323.15 |
100.00 |
0.0184 |
979.2 |
323.15 |
100.00 |
0.0219 |
978.0 |
323.15 |
100.00 |
0.0255 |
976.5 |
323.15 |
100.00 |
0.0279 |
974.8 |
323.15 |
100.00 |
0.0315 |
973.9 |
323.15 |
100.00 |
0.0366 |
971.4 |
323.15 |
100.00 |
0.0392 |
970.2 |
323.15 |
100.00 |
0.0439 |
968.6 |
323.15 |
100.00 |
0.0483 |
966.6 |
323.15 |
100.00 |
0.0516 |
965.9 |
323.15 |
100.00 |
0.0559 |
964.5 |
323.15 |
100.00 |
0.0600 |
962.9 |
323.15 |
100.00 |
0.0652 |
960.9 |
323.15 |
100.00 |
0.0679 |
960.2 |
323.15 |
100.00 |
0.0722 |
958.3 |
323.15 |
100.00 |
0.0801 |
955.1 |
323.15 |
100.00 |
0.0840 |
954.7 |
323.15 |
100.00 |
0.0879 |
952.9 |
323.15 |
100.00 |
0.0926 |
951.4 |
323.15 |
100.00 |
0.0958 |
950.1 |
323.15 |
100.00 |
0.1006 |
948.5 |
323.15 |
100.00 |
0.1111 |
944.7 |
323.15 |
100.00 |
0.1225 |
940.6 |
323.15 |
100.00 |
0.1296 |
938.2 |
323.15 |
100.00 |
0.1402 |
934.5 |
323.15 |
100.00 |
0.1510 |
930.7 |
323.15 |
100.00 |
0.1601 |
927.5 |
323.15 |
100.00 |
0.1703 |
924.0 |
323.15 |
100.00 |
0.1800 |
920.6 |
323.15 |
100.00 |
0.1903 |
917.3 |
323.15 |
100.00 |
0.1996 |
914.1 |
323.15 |
100.00 |
0.2269 |
905.2 |
323.15 |
100.00 |
0.2502 |
898.1 |
323.15 |
100.00 |
0.2745 |
890.8 |
323.15 |
100.00 |
0.3009 |
883.5 |
323.15 |
100.00 |
0.3500 |
870.2 |
323.15 |
100.00 |
0.4034 |
857.3 |
323.15 |
100.00 |
0.4501 |
846.7 |
323.15 |
100.00 |
0.4980 |
837.0 |
323.15 |
100.00 |
0.5501 |
826.9 |
323.15 |
100.00 |
0.5998 |
818.4 |
323.15 |
100.00 |
0.6489 |
810.1 |
323.15 |
100.00 |
0.6967 |
802.8 |
323.15 |
100.00 |
0.7475 |
795.4 |
323.15 |
100.00 |
0.7996 |
788.4 |
323.15 |
100.00 |
0.8484 |
781.9 |
323.15 |
100.00 |
0.8993 |
775.6 |
323.15 |
100.00 |
0.9503 |
769.5 |
323.15 |
100.00 |
1.0000 |
763.7 |
323.15 |
10000.00 |
0.0030 |
990.8 |
323.15 |
10000.00 |
0.0042 |
989.6 |
323.15 |
10000.00 |
0.0082 |
988.2 |
323.15 |
10000.00 |
0.0119 |
986.9 |
323.15 |
10000.00 |
0.0158 |
984.7 |
323.15 |
10000.00 |
0.0184 |
983.3 |
323.15 |
10000.00 |
0.0219 |
982.2 |
323.15 |
10000.00 |
0.0255 |
980.6 |
323.15 |
10000.00 |
0.0279 |
979.0 |
323.15 |
10000.00 |
0.0315 |
978.1 |
323.15 |
10000.00 |
0.0366 |
975.6 |
323.15 |
10000.00 |
0.0392 |
974.3 |
323.15 |
10000.00 |
0.0439 |
972.8 |
323.15 |
10000.00 |
0.0483 |
970.7 |
323.15 |
10000.00 |
0.0516 |
970.0 |
323.15 |
10000.00 |
0.0559 |
968.6 |
323.15 |
10000.00 |
0.0600 |
967.1 |
323.15 |
10000.00 |
0.0652 |
965.0 |
323.15 |
10000.00 |
0.0679 |
964.3 |
323.15 |
10000.00 |
0.0722 |
962.5 |
323.15 |
10000.00 |
0.0801 |
959.3 |
323.15 |
10000.00 |
0.0840 |
958.9 |
323.15 |
10000.00 |
0.0879 |
957.1 |
323.15 |
10000.00 |
0.0926 |
955.5 |
323.15 |
10000.00 |
0.0958 |
954.4 |
323.15 |
10000.00 |
0.1006 |
952.8 |
323.15 |
10000.00 |
0.1111 |
949.0 |
323.15 |
10000.00 |
0.1225 |
945.1 |
323.15 |
10000.00 |
0.1296 |
942.6 |
323.15 |
10000.00 |
0.1402 |
939.0 |
323.15 |
10000.00 |
0.1510 |
935.2 |
323.15 |
10000.00 |
0.1601 |
932.2 |
323.15 |
10000.00 |
0.1703 |
928.8 |
323.15 |
10000.00 |
0.1800 |
925.5 |
323.15 |
10000.00 |
0.1903 |
922.1 |
323.15 |
10000.00 |
0.1996 |
919.0 |
323.15 |
10000.00 |
0.2269 |
910.3 |
323.15 |
10000.00 |
0.2502 |
903.4 |
323.15 |
10000.00 |
0.2745 |
896.3 |
323.15 |
10000.00 |
0.3009 |
889.2 |
323.15 |
10000.00 |
0.3500 |
876.2 |
323.15 |
10000.00 |
0.4034 |
863.7 |
323.15 |
10000.00 |
0.4501 |
853.3 |
323.15 |
10000.00 |
0.4980 |
843.9 |
323.15 |
10000.00 |
0.5501 |
834.3 |
323.15 |
10000.00 |
0.5998 |
826.3 |
323.15 |
10000.00 |
0.6489 |
817.9 |
323.15 |
10000.00 |
0.6967 |
810.9 |
323.15 |
10000.00 |
0.7475 |
803.8 |
323.15 |
10000.00 |
0.7996 |
796.9 |
323.15 |
10000.00 |
0.8484 |
790.8 |
323.15 |
10000.00 |
0.8993 |
784.7 |
323.15 |
10000.00 |
0.9503 |
779.0 |
323.15 |
10000.00 |
1.0000 |
773.4 |
323.15 |
20000.00 |
0.0030 |
994.9 |
323.15 |
20000.00 |
0.0042 |
993.9 |
323.15 |
20000.00 |
0.0082 |
992.4 |
323.15 |
20000.00 |
0.0119 |
991.1 |
323.15 |
20000.00 |
0.0158 |
988.9 |
323.15 |
20000.00 |
0.0184 |
987.5 |
323.15 |
20000.00 |
0.0219 |
986.3 |
323.15 |
20000.00 |
0.0255 |
984.7 |
323.15 |
20000.00 |
0.0279 |
983.1 |
323.15 |
20000.00 |
0.0315 |
982.2 |
323.15 |
20000.00 |
0.0366 |
979.6 |
323.15 |
20000.00 |
0.0392 |
978.4 |
323.15 |
20000.00 |
0.0439 |
976.8 |
323.15 |
20000.00 |
0.0483 |
974.8 |
323.15 |
20000.00 |
0.0516 |
974.0 |
323.15 |
20000.00 |
0.0559 |
972.7 |
323.15 |
20000.00 |
0.0600 |
971.2 |
323.15 |
20000.00 |
0.0652 |
969.1 |
323.15 |
20000.00 |
0.0679 |
968.3 |
323.15 |
20000.00 |
0.0722 |
966.6 |
323.15 |
20000.00 |
0.0801 |
963.4 |
323.15 |
20000.00 |
0.0840 |
963.0 |
323.15 |
20000.00 |
0.0879 |
961.2 |
323.15 |
20000.00 |
0.0926 |
959.6 |
323.15 |
20000.00 |
0.0958 |
958.5 |
323.15 |
20000.00 |
0.1006 |
956.9 |
323.15 |
20000.00 |
0.1111 |
953.2 |
323.15 |
20000.00 |
0.1225 |
949.2 |
323.15 |
20000.00 |
0.1296 |
946.9 |
323.15 |
20000.00 |
0.1402 |
943.3 |
323.15 |
20000.00 |
0.1510 |
939.7 |
323.15 |
20000.00 |
0.1601 |
936.7 |
323.15 |
20000.00 |
0.1703 |
933.3 |
323.15 |
20000.00 |
0.1800 |
930.1 |
323.15 |
20000.00 |
0.1903 |
926.8 |
323.15 |
20000.00 |
0.1996 |
923.8 |
323.15 |
20000.00 |
0.2269 |
915.3 |
323.15 |
20000.00 |
0.2502 |
908.5 |
323.15 |
20000.00 |
0.2745 |
901.6 |
323.15 |
20000.00 |
0.3009 |
894.7 |
323.15 |
20000.00 |
0.3500 |
882.1 |
323.15 |
20000.00 |
0.4034 |
869.8 |
323.15 |
20000.00 |
0.4501 |
859.7 |
323.15 |
20000.00 |
0.4980 |
850.6 |
323.15 |
20000.00 |
0.5501 |
841.2 |
323.15 |
20000.00 |
0.5998 |
833.5 |
323.15 |
20000.00 |
0.6489 |
825.3 |
323.15 |
20000.00 |
0.6967 |
818.4 |
323.15 |
20000.00 |
0.7475 |
811.7 |
323.15 |
20000.00 |
0.7996 |
804.9 |
323.15 |
20000.00 |
0.8484 |
799.1 |
323.15 |
20000.00 |
0.8993 |
793.2 |
323.15 |
20000.00 |
0.9503 |
787.7 |
323.15 |
20000.00 |
1.0000 |
782.3 |
323.15 |
30000.00 |
0.0030 |
999.0 |
323.15 |
30000.00 |
0.0042 |
998.0 |
323.15 |
30000.00 |
0.0082 |
996.5 |
323.15 |
30000.00 |
0.0119 |
995.2 |
323.15 |
30000.00 |
0.0158 |
993.0 |
323.15 |
30000.00 |
0.0184 |
991.5 |
323.15 |
30000.00 |
0.0219 |
990.4 |
323.15 |
30000.00 |
0.0255 |
988.7 |
323.15 |
30000.00 |
0.0279 |
987.1 |
323.15 |
30000.00 |
0.0315 |
986.3 |
323.15 |
30000.00 |
0.0366 |
983.6 |
323.15 |
30000.00 |
0.0392 |
982.4 |
323.15 |
30000.00 |
0.0439 |
980.8 |
323.15 |
30000.00 |
0.0483 |
978.8 |
323.15 |
30000.00 |
0.0516 |
978.0 |
323.15 |
30000.00 |
0.0559 |
976.6 |
323.15 |
30000.00 |
0.0600 |
975.1 |
323.15 |
30000.00 |
0.0652 |
973.1 |
323.15 |
30000.00 |
0.0679 |
972.3 |
323.15 |
30000.00 |
0.0722 |
970.5 |
323.15 |
30000.00 |
0.0801 |
967.4 |
323.15 |
30000.00 |
0.0840 |
967.0 |
323.15 |
30000.00 |
0.0879 |
965.3 |
323.15 |
30000.00 |
0.0926 |
963.7 |
323.15 |
30000.00 |
0.0958 |
962.6 |
323.15 |
30000.00 |
0.1006 |
961.0 |
323.15 |
30000.00 |
0.1111 |
957.3 |
323.15 |
30000.00 |
0.1225 |
953.4 |
323.15 |
30000.00 |
0.1296 |
951.1 |
323.15 |
30000.00 |
0.1402 |
947.6 |
323.15 |
30000.00 |
0.1510 |
944.0 |
323.15 |
30000.00 |
0.1601 |
941.1 |
323.15 |
30000.00 |
0.1703 |
937.7 |
323.15 |
30000.00 |
0.1800 |
934.6 |
323.15 |
30000.00 |
0.1903 |
931.4 |
323.15 |
30000.00 |
0.1996 |
928.4 |
323.15 |
30000.00 |
0.2269 |
920.1 |
323.15 |
30000.00 |
0.2502 |
913.5 |
323.15 |
30000.00 |
0.2745 |
906.7 |
323.15 |
30000.00 |
0.3009 |
899.8 |
323.15 |
30000.00 |
0.3500 |
887.5 |
323.15 |
30000.00 |
0.4034 |
875.5 |
323.15 |
30000.00 |
0.4501 |
865.7 |
323.15 |
30000.00 |
0.4980 |
856.8 |
323.15 |
30000.00 |
0.5501 |
847.6 |
323.15 |
30000.00 |
0.5998 |
839.6 |
323.15 |
30000.00 |
0.6489 |
832.1 |
323.15 |
30000.00 |
0.6967 |
825.4 |
323.15 |
30000.00 |
0.7475 |
818.8 |
323.15 |
30000.00 |
0.7996 |
812.3 |
323.15 |
30000.00 |
0.8484 |
806.6 |
323.15 |
30000.00 |
0.8993 |
800.9 |
323.15 |
30000.00 |
0.9503 |
795.6 |
323.15 |
30000.00 |
1.0000 |
790.3 |
323.15 |
40000.00 |
0.0030 |
1003.1 |
323.15 |
40000.00 |
0.0042 |
1002.0 |
323.15 |
40000.00 |
0.0082 |
1000.5 |
323.15 |
40000.00 |
0.0119 |
999.2 |
323.15 |
40000.00 |
0.0158 |
996.9 |
323.15 |
40000.00 |
0.0184 |
995.5 |
323.15 |
40000.00 |
0.0219 |
994.4 |
323.15 |
40000.00 |
0.0255 |
992.7 |
323.15 |
40000.00 |
0.0279 |
991.1 |
323.15 |
40000.00 |
0.0315 |
990.2 |
323.15 |
40000.00 |
0.0366 |
987.6 |
323.15 |
40000.00 |
0.0392 |
986.3 |
323.15 |
40000.00 |
0.0439 |
984.7 |
323.15 |
40000.00 |
0.0483 |
982.7 |
323.15 |
40000.00 |
0.0516 |
982.0 |
323.15 |
40000.00 |
0.0559 |
980.5 |
323.15 |
40000.00 |
0.0600 |
979.1 |
323.15 |
40000.00 |
0.0652 |
977.0 |
323.15 |
40000.00 |
0.0679 |
976.3 |
323.15 |
40000.00 |
0.0722 |
974.4 |
323.15 |
40000.00 |
0.0801 |
971.4 |
323.15 |
40000.00 |
0.0840 |
970.9 |
323.15 |
40000.00 |
0.0879 |
969.2 |
323.15 |
40000.00 |
0.0926 |
967.6 |
323.15 |
40000.00 |
0.0958 |
966.5 |
323.15 |
40000.00 |
0.1006 |
964.9 |
323.15 |
40000.00 |
0.1111 |
961.3 |
323.15 |
40000.00 |
0.1225 |
957.4 |
323.15 |
40000.00 |
0.1296 |
955.2 |
323.15 |
40000.00 |
0.1402 |
951.7 |
323.15 |
40000.00 |
0.1510 |
948.2 |
323.15 |
40000.00 |
0.1601 |
945.3 |
323.15 |
40000.00 |
0.1703 |
942.0 |
323.15 |
40000.00 |
0.1800 |
938.9 |
323.15 |
40000.00 |
0.1903 |
935.8 |
323.15 |
40000.00 |
0.1996 |
932.9 |
323.15 |
40000.00 |
0.2269 |
924.7 |
323.15 |
40000.00 |
0.2502 |
918.2 |
323.15 |
40000.00 |
0.2745 |
911.5 |
323.15 |
40000.00 |
0.3009 |
904.8 |
323.15 |
40000.00 |
0.3500 |
892.7 |
323.15 |
40000.00 |
0.4034 |
881.0 |
323.15 |
40000.00 |
0.4501 |
871.3 |
323.15 |
40000.00 |
0.4980 |
862.6 |
323.15 |
40000.00 |
0.5501 |
853.6 |
323.15 |
40000.00 |
0.5998 |
845.8 |
323.15 |
40000.00 |
0.6489 |
838.5 |
323.15 |
40000.00 |
0.6967 |
831.9 |
323.15 |
40000.00 |
0.7475 |
825.5 |
323.15 |
40000.00 |
0.7996 |
819.1 |
323.15 |
40000.00 |
0.8484 |
813.6 |
323.15 |
40000.00 |
0.8993 |
808.0 |
323.15 |
40000.00 |
0.9503 |
802.8 |
323.15 |
40000.00 |
1.0000 |
797.7 |
348.15 |
100.00 |
0.0030 |
973.1 |
348.15 |
100.00 |
0.0042 |
971.9 |
348.15 |
100.00 |
0.0082 |
970.7 |
348.15 |
100.00 |
0.0119 |
969.1 |
348.15 |
100.00 |
0.0158 |
966.6 |
348.15 |
100.00 |
0.0184 |
965.4 |
348.15 |
100.00 |
0.0219 |
963.9 |
348.15 |
100.00 |
0.0255 |
962.0 |
348.15 |
100.00 |
0.0279 |
960.4 |
348.15 |
100.00 |
0.0315 |
959.4 |
348.15 |
100.00 |
0.0366 |
956.7 |
348.15 |
100.00 |
0.0392 |
955.3 |
348.15 |
100.00 |
0.0439 |
953.5 |
348.15 |
100.00 |
0.0483 |
951.2 |
348.15 |
100.00 |
0.0516 |
950.2 |
348.15 |
100.00 |
0.0559 |
948.8 |
348.15 |
100.00 |
0.0600 |
946.9 |
348.15 |
100.00 |
0.0652 |
944.8 |
348.15 |
100.00 |
0.0679 |
943.7 |
348.15 |
100.00 |
0.0722 |
941.5 |
348.15 |
100.00 |
0.0801 |
938.1 |
348.15 |
100.00 |
0.0840 |
937.5 |
348.15 |
100.00 |
0.0879 |
935.3 |
348.15 |
100.00 |
0.0926 |
933.6 |
348.15 |
100.00 |
0.0958 |
932.2 |
348.15 |
100.00 |
0.1006 |
930.2 |
348.15 |
100.00 |
0.1111 |
925.9 |
348.15 |
100.00 |
0.1225 |
921.5 |
348.15 |
100.00 |
0.1296 |
918.7 |
348.15 |
100.00 |
0.1402 |
914.6 |
348.15 |
100.00 |
0.1510 |
910.4 |
348.15 |
100.00 |
0.1601 |
906.9 |
348.15 |
100.00 |
0.1703 |
903.1 |
348.15 |
100.00 |
0.1800 |
899.5 |
348.15 |
100.00 |
0.1903 |
895.8 |
348.15 |
100.00 |
0.1996 |
892.6 |
348.15 |
100.00 |
0.2269 |
883.1 |
348.15 |
100.00 |
0.2502 |
875.6 |
348.15 |
100.00 |
0.2745 |
868.0 |
348.15 |
100.00 |
0.3009 |
860.4 |
348.15 |
100.00 |
0.3500 |
846.7 |
348.15 |
100.00 |
0.4034 |
833.4 |
348.15 |
100.00 |
0.4501 |
822.7 |
348.15 |
100.00 |
0.4980 |
812.7 |
348.15 |
100.00 |
0.5501 |
802.6 |
348.15 |
100.00 |
0.5998 |
793.8 |
348.15 |
100.00 |
0.6489 |
785.6 |
348.15 |
100.00 |
0.6967 |
778.2 |
348.15 |
100.00 |
0.7475 |
770.9 |
348.15 |
100.00 |
0.7996 |
763.9 |
348.15 |
100.00 |
0.8484 |
757.6 |
348.15 |
100.00 |
0.8993 |
751.5 |
348.15 |
100.00 |
0.9503 |
745.7 |
348.15 |
100.00 |
1.0000 |
739.4 |
348.15 |
10000.00 |
0.0030 |
977.5 |
348.15 |
10000.00 |
0.0042 |
976.3 |
348.15 |
10000.00 |
0.0082 |
975.0 |
348.15 |
10000.00 |
0.0119 |
973.4 |
348.15 |
10000.00 |
0.0158 |
971.0 |
348.15 |
10000.00 |
0.0184 |
969.6 |
348.15 |
10000.00 |
0.0219 |
968.2 |
348.15 |
10000.00 |
0.0255 |
966.4 |
348.15 |
10000.00 |
0.0279 |
964.8 |
348.15 |
10000.00 |
0.0315 |
963.8 |
348.15 |
10000.00 |
0.0366 |
961.0 |
348.15 |
10000.00 |
0.0392 |
959.6 |
348.15 |
10000.00 |
0.0439 |
957.8 |
348.15 |
10000.00 |
0.0483 |
955.6 |
348.15 |
10000.00 |
0.0516 |
954.6 |
348.15 |
10000.00 |
0.0559 |
953.2 |
348.15 |
10000.00 |
0.0600 |
951.3 |
348.15 |
10000.00 |
0.0652 |
949.1 |
348.15 |
10000.00 |
0.0679 |
948.2 |
348.15 |
10000.00 |
0.0722 |
946.1 |
348.15 |
10000.00 |
0.0801 |
942.6 |
348.15 |
10000.00 |
0.0840 |
941.9 |
348.15 |
10000.00 |
0.0879 |
939.9 |
348.15 |
10000.00 |
0.0926 |
938.1 |
348.15 |
10000.00 |
0.0958 |
936.8 |
348.15 |
10000.00 |
0.1006 |
934.9 |
348.15 |
10000.00 |
0.1111 |
930.7 |
348.15 |
10000.00 |
0.1225 |
926.3 |
348.15 |
10000.00 |
0.1296 |
923.6 |
348.15 |
10000.00 |
0.1402 |
919.5 |
348.15 |
10000.00 |
0.1510 |
915.4 |
348.15 |
10000.00 |
0.1601 |
912.1 |
348.15 |
10000.00 |
0.1703 |
908.4 |
348.15 |
10000.00 |
0.1800 |
904.8 |
348.15 |
10000.00 |
0.1903 |
901.3 |
348.15 |
10000.00 |
0.1996 |
898.1 |
348.15 |
10000.00 |
0.2269 |
888.9 |
348.15 |
10000.00 |
0.2502 |
881.6 |
348.15 |
10000.00 |
0.2745 |
874.2 |
348.15 |
10000.00 |
0.3009 |
866.8 |
348.15 |
10000.00 |
0.3500 |
853.6 |
348.15 |
10000.00 |
0.4034 |
840.7 |
348.15 |
10000.00 |
0.4501 |
830.3 |
348.15 |
10000.00 |
0.4980 |
820.7 |
348.15 |
10000.00 |
0.5501 |
811.0 |
348.15 |
10000.00 |
0.5998 |
802.5 |
348.15 |
10000.00 |
0.6489 |
794.6 |
348.15 |
10000.00 |
0.6967 |
787.6 |
348.15 |
10000.00 |
0.7475 |
780.7 |
348.15 |
10000.00 |
0.7996 |
774.0 |
348.15 |
10000.00 |
0.8484 |
768.0 |
348.15 |
10000.00 |
0.8993 |
762.1 |
348.15 |
10000.00 |
0.9503 |
756.7 |
348.15 |
10000.00 |
1.0000 |
751.2 |
348.15 |
20000.00 |
0.0030 |
981.9 |
348.15 |
20000.00 |
0.0042 |
980.6 |
348.15 |
20000.00 |
0.0082 |
979.4 |
348.15 |
20000.00 |
0.0119 |
977.7 |
348.15 |
20000.00 |
0.0158 |
975.3 |
348.15 |
20000.00 |
0.0184 |
973.9 |
348.15 |
20000.00 |
0.0219 |
972.6 |
348.15 |
20000.00 |
0.0255 |
970.7 |
348.15 |
20000.00 |
0.0279 |
969.1 |
348.15 |
20000.00 |
0.0315 |
968.0 |
348.15 |
20000.00 |
0.0366 |
965.3 |
348.15 |
20000.00 |
0.0392 |
963.8 |
348.15 |
20000.00 |
0.0439 |
962.1 |
348.15 |
20000.00 |
0.0483 |
959.9 |
348.15 |
20000.00 |
0.0516 |
958.9 |
348.15 |
20000.00 |
0.0559 |
957.5 |
348.15 |
20000.00 |
0.0600 |
955.8 |
348.15 |
20000.00 |
0.0652 |
953.5 |
348.15 |
20000.00 |
0.0679 |
952.5 |
348.15 |
20000.00 |
0.0722 |
950.4 |
348.15 |
20000.00 |
0.0801 |
947.0 |
348.15 |
20000.00 |
0.0840 |
946.3 |
348.15 |
20000.00 |
0.0879 |
944.4 |
348.15 |
20000.00 |
0.0926 |
942.6 |
348.15 |
20000.00 |
0.0958 |
941.3 |
348.15 |
20000.00 |
0.1006 |
939.4 |
348.15 |
20000.00 |
0.1111 |
935.3 |
348.15 |
20000.00 |
0.1225 |
931.1 |
348.15 |
20000.00 |
0.1296 |
928.3 |
348.15 |
20000.00 |
0.1402 |
924.4 |
348.15 |
20000.00 |
0.1510 |
920.3 |
348.15 |
20000.00 |
0.1601 |
917.1 |
348.15 |
20000.00 |
0.1703 |
913.5 |
348.15 |
20000.00 |
0.1800 |
910.0 |
348.15 |
20000.00 |
0.1903 |
906.5 |
348.15 |
20000.00 |
0.1996 |
903.4 |
348.15 |
20000.00 |
0.2269 |
894.4 |
348.15 |
20000.00 |
0.2502 |
887.3 |
348.15 |
20000.00 |
0.2745 |
880.2 |
348.15 |
20000.00 |
0.3009 |
872.9 |
348.15 |
20000.00 |
0.3500 |
860.0 |
348.15 |
20000.00 |
0.4034 |
847.5 |
348.15 |
20000.00 |
0.4501 |
837.4 |
348.15 |
20000.00 |
0.4980 |
828.1 |
348.15 |
20000.00 |
0.5501 |
818.7 |
348.15 |
20000.00 |
0.5998 |
810.5 |
348.15 |
20000.00 |
0.6489 |
802.9 |
348.15 |
20000.00 |
0.6967 |
796.1 |
348.15 |
20000.00 |
0.7475 |
789.4 |
348.15 |
20000.00 |
0.7996 |
783.0 |
348.15 |
20000.00 |
0.8484 |
777.3 |
348.15 |
20000.00 |
0.8993 |
771.6 |
348.15 |
20000.00 |
0.9503 |
766.4 |
348.15 |
20000.00 |
1.0000 |
761.2 |
348.15 |
30000.00 |
0.0030 |
986.1 |
348.15 |
30000.00 |
0.0042 |
984.8 |
348.15 |
30000.00 |
0.0082 |
983.6 |
348.15 |
30000.00 |
0.0119 |
981.9 |
348.15 |
30000.00 |
0.0158 |
979.4 |
348.15 |
30000.00 |
0.0184 |
978.1 |
348.15 |
30000.00 |
0.0219 |
976.7 |
348.15 |
30000.00 |
0.0255 |
975.0 |
348.15 |
30000.00 |
0.0279 |
973.3 |
348.15 |
30000.00 |
0.0315 |
972.3 |
348.15 |
30000.00 |
0.0366 |
969.5 |
348.15 |
30000.00 |
0.0392 |
968.1 |
348.15 |
30000.00 |
0.0439 |
966.3 |
348.15 |
30000.00 |
0.0483 |
964.1 |
348.15 |
30000.00 |
0.0516 |
963.2 |
348.15 |
30000.00 |
0.0559 |
961.7 |
348.15 |
30000.00 |
0.0600 |
960.0 |
348.15 |
30000.00 |
0.0652 |
957.8 |
348.15 |
30000.00 |
0.0679 |
956.8 |
348.15 |
30000.00 |
0.0722 |
954.7 |
348.15 |
30000.00 |
0.0801 |
951.3 |
348.15 |
30000.00 |
0.0840 |
950.7 |
348.15 |
30000.00 |
0.0879 |
948.8 |
348.15 |
30000.00 |
0.0926 |
947.0 |
348.15 |
30000.00 |
0.0958 |
945.7 |
348.15 |
30000.00 |
0.1006 |
943.9 |
348.15 |
30000.00 |
0.1111 |
939.8 |
348.15 |
30000.00 |
0.1225 |
935.6 |
348.15 |
30000.00 |
0.1296 |
932.9 |
348.15 |
30000.00 |
0.1402 |
929.1 |
348.15 |
30000.00 |
0.1510 |
925.1 |
348.15 |
30000.00 |
0.1601 |
922.0 |
348.15 |
30000.00 |
0.1703 |
918.4 |
348.15 |
30000.00 |
0.1800 |
915.0 |
348.15 |
30000.00 |
0.1903 |
911.6 |
348.15 |
30000.00 |
0.1996 |
908.5 |
348.15 |
30000.00 |
0.2269 |
899.7 |
348.15 |
30000.00 |
0.2502 |
892.8 |
348.15 |
30000.00 |
0.2745 |
885.8 |
348.15 |
30000.00 |
0.3009 |
878.6 |
348.15 |
30000.00 |
0.3500 |
866.2 |
348.15 |
30000.00 |
0.4034 |
854.0 |
348.15 |
30000.00 |
0.4501 |
844.2 |
348.15 |
30000.00 |
0.4980 |
835.1 |
348.15 |
30000.00 |
0.5501 |
825.9 |
348.15 |
30000.00 |
0.5998 |
818.0 |
348.15 |
30000.00 |
0.6489 |
810.6 |
348.15 |
30000.00 |
0.6967 |
804.0 |
348.15 |
30000.00 |
0.7475 |
797.6 |
348.15 |
30000.00 |
0.7996 |
791.3 |
348.15 |
30000.00 |
0.8484 |
785.8 |
348.15 |
30000.00 |
0.8993 |
780.3 |
348.15 |
30000.00 |
0.9503 |
775.2 |
348.15 |
30000.00 |
1.0000 |
770.3 |
348.15 |
40000.00 |
0.0030 |
990.1 |
348.15 |
40000.00 |
0.0042 |
988.8 |
348.15 |
40000.00 |
0.0082 |
987.6 |
348.15 |
40000.00 |
0.0119 |
986.0 |
348.15 |
40000.00 |
0.0158 |
983.5 |
348.15 |
40000.00 |
0.0184 |
982.1 |
348.15 |
40000.00 |
0.0219 |
980.8 |
348.15 |
40000.00 |
0.0255 |
979.0 |
348.15 |
40000.00 |
0.0279 |
977.3 |
348.15 |
40000.00 |
0.0315 |
976.3 |
348.15 |
40000.00 |
0.0366 |
973.6 |
348.15 |
40000.00 |
0.0392 |
972.1 |
348.15 |
40000.00 |
0.0439 |
970.4 |
348.15 |
40000.00 |
0.0483 |
968.2 |
348.15 |
40000.00 |
0.0516 |
967.3 |
348.15 |
40000.00 |
0.0559 |
965.9 |
348.15 |
40000.00 |
0.0600 |
964.1 |
348.15 |
40000.00 |
0.0652 |
961.9 |
348.15 |
40000.00 |
0.0679 |
960.9 |
348.15 |
40000.00 |
0.0722 |
958.9 |
348.15 |
40000.00 |
0.0801 |
955.6 |
348.15 |
40000.00 |
0.0840 |
954.9 |
348.15 |
40000.00 |
0.0879 |
953.0 |
348.15 |
40000.00 |
0.0926 |
951.3 |
348.15 |
40000.00 |
0.0958 |
950.0 |
348.15 |
40000.00 |
0.1006 |
948.1 |
348.15 |
40000.00 |
0.1111 |
944.2 |
348.15 |
40000.00 |
0.1225 |
940.0 |
348.15 |
40000.00 |
0.1296 |
937.4 |
348.15 |
40000.00 |
0.1402 |
933.7 |
348.15 |
40000.00 |
0.1510 |
929.7 |
348.15 |
40000.00 |
0.1601 |
926.6 |
348.15 |
40000.00 |
0.1703 |
923.1 |
348.15 |
40000.00 |
0.1800 |
919.8 |
348.15 |
40000.00 |
0.1903 |
916.4 |
348.15 |
40000.00 |
0.1996 |
913.4 |
348.15 |
40000.00 |
0.2269 |
904.8 |
348.15 |
40000.00 |
0.2502 |
898.1 |
348.15 |
40000.00 |
0.2745 |
891.1 |
348.15 |
40000.00 |
0.3009 |
884.2 |
348.15 |
40000.00 |
0.3500 |
872.0 |
348.15 |
40000.00 |
0.4034 |
860.0 |
348.15 |
40000.00 |
0.4501 |
850.5 |
348.15 |
40000.00 |
0.4980 |
841.6 |
348.15 |
40000.00 |
0.5501 |
832.7 |
348.15 |
40000.00 |
0.5998 |
824.9 |
348.15 |
40000.00 |
0.6489 |
817.8 |
348.15 |
40000.00 |
0.6967 |
811.3 |
348.15 |
40000.00 |
0.7475 |
805.1 |
348.15 |
40000.00 |
0.7996 |
799.0 |
348.15 |
40000.00 |
0.8484 |
793.6 |
348.15 |
40000.00 |
0.8993 |
788.3 |
348.15 |
40000.00 |
0.9503 |
783.4 |
348.15 |
40000.00 |
1.0000 |
778.6 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Pressure, kPa - Liquid |
Temperature, K - Liquid |
Mole fraction of Ethanol (1) - Liquid |
Mass density, kg/m3 - Liquid |
39170.00 |
297.05 |
0.0163 |
1006.1 |
30810.00 |
297.05 |
0.0163 |
1003.2 |
21070.00 |
297.05 |
0.0163 |
997.5 |
11280.00 |
297.05 |
0.0163 |
993.5 |
2490.00 |
297.05 |
0.0163 |
990.8 |
38480.00 |
323.15 |
0.0163 |
995.2 |
30890.00 |
323.15 |
0.0163 |
992.3 |
21080.00 |
323.15 |
0.0163 |
988.4 |
11390.00 |
323.15 |
0.0163 |
984.4 |
2570.00 |
323.15 |
0.0163 |
980.6 |
39910.00 |
348.15 |
0.0163 |
982.3 |
29500.00 |
348.15 |
0.0163 |
978.3 |
20750.00 |
348.15 |
0.0163 |
974.7 |
10980.00 |
348.15 |
0.0163 |
970.6 |
3220.00 |
348.15 |
0.0163 |
967.1 |
35700.00 |
373.15 |
0.0163 |
964.6 |
30600.00 |
373.15 |
0.0163 |
962.5 |
21160.00 |
373.15 |
0.0163 |
958.3 |
11320.00 |
373.15 |
0.0163 |
953.8 |
3370.00 |
373.15 |
0.0163 |
950.2 |
39890.00 |
398.15 |
0.0163 |
948.0 |
30790.00 |
398.15 |
0.0163 |
943.7 |
21360.00 |
398.15 |
0.0163 |
939.3 |
11630.00 |
398.15 |
0.0163 |
934.4 |
3710.00 |
398.15 |
0.0163 |
930.3 |
39560.00 |
423.15 |
0.0163 |
927.2 |
30570.00 |
423.15 |
0.0163 |
922.4 |
20970.00 |
423.15 |
0.0163 |
917.0 |
10170.00 |
423.15 |
0.0163 |
911.0 |
2680.00 |
423.15 |
0.0163 |
906.7 |
38340.00 |
448.15 |
0.0163 |
903.5 |
31050.00 |
448.15 |
0.0163 |
899.4 |
21530.00 |
448.15 |
0.0163 |
893.7 |
11920.00 |
448.15 |
0.0163 |
887.5 |
3960.00 |
448.15 |
0.0163 |
882.3 |
39230.00 |
292.95 |
0.0730 |
988.0 |
30930.00 |
292.95 |
0.0730 |
985.0 |
21120.00 |
292.95 |
0.0730 |
981.2 |
11320.00 |
292.95 |
0.0730 |
977.6 |
2450.00 |
292.95 |
0.0730 |
974.2 |
38600.00 |
323.15 |
0.0730 |
973.6 |
30360.00 |
323.15 |
0.0730 |
970.6 |
20790.00 |
323.15 |
0.0730 |
966.7 |
10940.00 |
323.15 |
0.0730 |
962.8 |
2610.00 |
323.15 |
0.0730 |
959.3 |
39600.00 |
348.15 |
0.0730 |
958.9 |
30400.00 |
348.15 |
0.0730 |
955.0 |
20870.00 |
348.15 |
0.0730 |
950.8 |
11060.00 |
348.15 |
0.0730 |
946.6 |
3330.00 |
348.15 |
0.0730 |
943.0 |
37230.00 |
373.15 |
0.0730 |
939.9 |
30670.00 |
373.15 |
0.0730 |
937.0 |
21080.00 |
373.15 |
0.0730 |
932.5 |
11320.00 |
373.15 |
0.0730 |
927.7 |
3510.00 |
373.15 |
0.0730 |
923.9 |
39500.00 |
398.15 |
0.0730 |
920.7 |
30790.00 |
398.15 |
0.0730 |
916.3 |
21160.00 |
398.15 |
0.0730 |
911.4 |
11510.00 |
398.15 |
0.0730 |
906.2 |
3710.00 |
398.15 |
0.0730 |
901.9 |
40110.00 |
423.15 |
0.0730 |
898.6 |
30490.00 |
423.15 |
0.0730 |
893.0 |
20110.00 |
423.15 |
0.0730 |
887.1 |
10710.00 |
423.15 |
0.0730 |
881.1 |
2760.00 |
423.15 |
0.0730 |
875.9 |
37210.00 |
448.15 |
0.0730 |
873.0 |
31170.00 |
448.15 |
0.0730 |
869.2 |
21690.00 |
448.15 |
0.0730 |
862.7 |
12160.00 |
448.15 |
0.0730 |
855.6 |
4000.00 |
448.15 |
0.0730 |
849.3 |
40030.00 |
298.15 |
0.0946 |
979.8 |
29980.00 |
298.15 |
0.0946 |
976.1 |
20060.00 |
298.15 |
0.0946 |
972.4 |
10120.00 |
298.15 |
0.0946 |
968.6 |
2560.00 |
298.15 |
0.0946 |
965.8 |
39810.00 |
323.15 |
0.0946 |
966.2 |
32400.00 |
323.15 |
0.0946 |
963.3 |
20710.00 |
323.15 |
0.0946 |
958.8 |
11140.00 |
323.15 |
0.0946 |
954.9 |
2730.00 |
323.15 |
0.0946 |
951.3 |
37790.00 |
348.15 |
0.0946 |
948.7 |
29730.00 |
348.15 |
0.0946 |
945.4 |
20870.00 |
348.15 |
0.0946 |
941.6 |
11390.00 |
348.15 |
0.0946 |
937.4 |
2730.00 |
348.15 |
0.0946 |
933.7 |
39410.00 |
373.15 |
0.0946 |
927.3 |
30850.00 |
373.15 |
0.0946 |
922.3 |
21200.00 |
373.15 |
0.0946 |
917.7 |
11390.00 |
373.15 |
0.0946 |
912.8 |
3330.00 |
373.15 |
0.0946 |
908.6 |
39610.00 |
398.15 |
0.0946 |
905.3 |
30850.00 |
398.15 |
0.0946 |
901.1 |
21200.00 |
398.15 |
0.0946 |
896.0 |
11430.00 |
398.15 |
0.0946 |
890.4 |
3510.00 |
398.15 |
0.0946 |
885.8 |
39860.00 |
423.15 |
0.0946 |
882.2 |
30100.00 |
423.15 |
0.0946 |
875.5 |
20200.00 |
423.15 |
0.0946 |
869.5 |
10050.00 |
423.15 |
0.0946 |
863.9 |
2750.00 |
423.15 |
0.0946 |
860.1 |
40140.00 |
448.15 |
0.0946 |
858.6 |
30990.00 |
448.15 |
0.0946 |
852.6 |
21690.00 |
448.15 |
0.0946 |
845.8 |
11550.00 |
448.15 |
0.0946 |
837.9 |
3860.00 |
448.15 |
0.0946 |
831.7 |
39150.00 |
298.35 |
0.0343 |
998.6 |
31040.00 |
298.35 |
0.0343 |
995.7 |
21300.00 |
298.35 |
0.0343 |
991.9 |
11280.00 |
298.35 |
0.0343 |
987.9 |
2590.00 |
298.35 |
0.0343 |
984.1 |
39010.00 |
323.65 |
0.0343 |
988.2 |
30930.00 |
323.65 |
0.0343 |
985.2 |
21200.00 |
323.65 |
0.0343 |
981.4 |
11320.00 |
323.65 |
0.0343 |
977.4 |
2610.00 |
323.65 |
0.0343 |
973.6 |
39860.00 |
348.15 |
0.0343 |
974.7 |
30850.00 |
348.15 |
0.0343 |
971.3 |
21160.00 |
348.15 |
0.0343 |
967.5 |
11590.00 |
348.15 |
0.0343 |
963.5 |
3260.00 |
348.15 |
0.0343 |
959.9 |
39000.00 |
373.15 |
0.0343 |
957.9 |
30520.00 |
373.15 |
0.0343 |
954.5 |
21120.00 |
373.15 |
0.0343 |
950.3 |
11470.00 |
373.15 |
0.0343 |
945.9 |
3390.00 |
373.15 |
0.0343 |
942.1 |
37300.00 |
398.15 |
0.0343 |
938.3 |
30930.00 |
398.15 |
0.0343 |
935.2 |
21530.00 |
398.15 |
0.0343 |
930.7 |
11730.00 |
398.15 |
0.0343 |
925.8 |
3550.00 |
398.15 |
0.0343 |
921.6 |
39680.00 |
423.15 |
0.0343 |
918.2 |
30640.00 |
423.15 |
0.0343 |
913.4 |
21070.00 |
423.15 |
0.0343 |
908.1 |
10240.00 |
423.15 |
0.0343 |
901.8 |
2680.00 |
423.15 |
0.0343 |
897.3 |
40060.00 |
448.15 |
0.0343 |
894.8 |
31010.00 |
448.15 |
0.0343 |
889.8 |
22180.00 |
448.15 |
0.0343 |
884.2 |
11960.00 |
448.15 |
0.0343 |
877.7 |
4080.00 |
448.15 |
0.0343 |
872.1 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Ethanol (1) - Liquid |
Mass density, kg/m3 - Liquid |
350.70 |
10000.00 |
0.1000 |
933.68 |
350.70 |
10000.00 |
0.2000 |
895.78 |
350.70 |
10000.00 |
0.3000 |
863.89 |
350.70 |
10000.00 |
0.4000 |
838.33 |
350.70 |
10000.00 |
0.6000 |
798.55 |
350.70 |
10000.00 |
0.8000 |
768.37 |
350.70 |
10000.00 |
1.0000 |
745.63 |
350.70 |
20000.00 |
0.1000 |
936.77 |
350.70 |
20000.00 |
0.2000 |
900.9 |
350.70 |
20000.00 |
0.3000 |
870.14 |
350.70 |
20000.00 |
0.4000 |
845.24 |
350.70 |
20000.00 |
0.6000 |
807.87 |
350.70 |
20000.00 |
0.8000 |
778.79 |
350.70 |
20000.00 |
1.0000 |
757.47 |
350.70 |
30000.00 |
0.1000 |
941.46 |
350.70 |
30000.00 |
0.2000 |
905.65 |
350.70 |
30000.00 |
0.3000 |
876.58 |
350.70 |
30000.00 |
0.4000 |
852.53 |
350.70 |
30000.00 |
0.6000 |
815.61 |
350.70 |
30000.00 |
0.8000 |
787.77 |
350.70 |
30000.00 |
1.0000 |
766.87 |
350.70 |
40000.00 |
0.1000 |
945.15 |
350.70 |
40000.00 |
0.2000 |
911.39 |
350.70 |
40000.00 |
0.3000 |
881.9 |
350.70 |
40000.00 |
0.4000 |
859.05 |
350.70 |
40000.00 |
0.6000 |
822.93 |
350.70 |
40000.00 |
0.8000 |
795.87 |
350.70 |
40000.00 |
1.0000 |
775.75 |
373.20 |
10000.00 |
0.1000 |
913.36 |
373.20 |
10000.00 |
0.2000 |
874.72 |
373.20 |
10000.00 |
0.3000 |
842.36 |
373.20 |
10000.00 |
0.4000 |
815.79 |
373.20 |
10000.00 |
0.6000 |
776.56 |
373.20 |
10000.00 |
0.8000 |
747.1 |
373.20 |
10000.00 |
1.0000 |
726.87 |
373.20 |
20000.00 |
0.1000 |
918.8 |
373.20 |
20000.00 |
0.2000 |
880.64 |
373.20 |
20000.00 |
0.3000 |
849.56 |
373.20 |
20000.00 |
0.4000 |
823.45 |
373.20 |
20000.00 |
0.6000 |
785.48 |
373.20 |
20000.00 |
0.8000 |
757.25 |
373.20 |
20000.00 |
1.0000 |
738.25 |
373.20 |
30000.00 |
0.1000 |
924.46 |
373.20 |
30000.00 |
0.2000 |
886.74 |
373.20 |
30000.00 |
0.3000 |
856.1 |
373.20 |
30000.00 |
0.4000 |
830.81 |
373.20 |
30000.00 |
0.6000 |
794.06 |
373.20 |
30000.00 |
0.8000 |
767.44 |
373.20 |
30000.00 |
1.0000 |
750.02 |
373.20 |
40000.00 |
0.1000 |
928.74 |
373.20 |
40000.00 |
0.2000 |
892.24 |
373.20 |
40000.00 |
0.3000 |
862.39 |
373.20 |
40000.00 |
0.4000 |
837.9 |
373.20 |
40000.00 |
0.6000 |
801.93 |
373.20 |
40000.00 |
0.8000 |
776.49 |
373.20 |
40000.00 |
1.0000 |
757.87 |
476.20 |
10000.00 |
0.1000 |
802.54 |
476.20 |
10000.00 |
0.2000 |
752.52 |
476.20 |
10000.00 |
0.3000 |
713.85 |
476.20 |
10000.00 |
0.4000 |
682.37 |
476.20 |
10000.00 |
0.6000 |
636.05 |
476.20 |
10000.00 |
0.8000 |
605.36 |
476.20 |
10000.00 |
1.0000 |
582.85 |
476.20 |
20000.00 |
0.1000 |
810.76 |
476.20 |
20000.00 |
0.2000 |
764.89 |
476.20 |
20000.00 |
0.3000 |
728.6 |
476.20 |
20000.00 |
0.4000 |
700.31 |
476.20 |
20000.00 |
0.6000 |
658.71 |
476.20 |
20000.00 |
0.8000 |
633.16 |
476.20 |
20000.00 |
1.0000 |
613.37 |
476.20 |
30000.00 |
0.1000 |
819.25 |
476.20 |
30000.00 |
0.2000 |
776.24 |
476.20 |
30000.00 |
0.3000 |
743.62 |
476.20 |
30000.00 |
0.4000 |
717.25 |
476.20 |
30000.00 |
0.6000 |
679.71 |
476.20 |
30000.00 |
0.8000 |
656.43 |
476.20 |
30000.00 |
1.0000 |
638.82 |
476.20 |
40000.00 |
0.1000 |
827.58 |
476.20 |
40000.00 |
0.2000 |
786.01 |
476.20 |
40000.00 |
0.3000 |
754.08 |
476.20 |
40000.00 |
0.4000 |
730.44 |
476.20 |
40000.00 |
0.6000 |
694.35 |
476.20 |
40000.00 |
0.8000 |
671.76 |
476.20 |
40000.00 |
1.0000 |
656.07 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Ethanol (1) - Liquid |
Mass density, kg/m3 - Liquid |
523.20 |
20000.00 |
0.0000 |
816.1 |
523.20 |
20000.00 |
0.1000 |
745.9 |
523.20 |
20000.00 |
0.2000 |
694.1 |
523.20 |
20000.00 |
0.3000 |
653.2 |
523.20 |
20000.00 |
0.4000 |
622.3 |
523.20 |
20000.00 |
0.6000 |
578.5 |
523.20 |
20000.00 |
0.8000 |
550.5 |
523.20 |
20000.00 |
1.0000 |
533.1 |
523.20 |
30000.00 |
0.0000 |
825.5 |
523.20 |
30000.00 |
0.1000 |
761.6 |
523.20 |
30000.00 |
0.2000 |
713.6 |
523.20 |
30000.00 |
0.3000 |
676.9 |
523.20 |
30000.00 |
0.4000 |
650.7 |
523.20 |
30000.00 |
0.6000 |
612.4 |
523.20 |
30000.00 |
0.8000 |
588.9 |
523.20 |
30000.00 |
1.0000 |
573.6 |
523.20 |
40000.00 |
0.0000 |
834.3 |
523.20 |
40000.00 |
0.1000 |
773.2 |
523.20 |
40000.00 |
0.2000 |
728.3 |
523.20 |
40000.00 |
0.3000 |
694.7 |
523.20 |
40000.00 |
0.4000 |
671.6 |
523.20 |
40000.00 |
0.6000 |
636.3 |
523.20 |
40000.00 |
0.8000 |
615.2 |
523.20 |
40000.00 |
1.0000 |
601.3 |
573.20 |
20000.00 |
0.0000 |
734.8 |
573.20 |
20000.00 |
0.1000 |
649.3 |
573.20 |
20000.00 |
0.2000 |
585.4 |
573.20 |
20000.00 |
0.3000 |
534.9 |
573.20 |
20000.00 |
0.4000 |
494.9 |
573.20 |
20000.00 |
0.6000 |
446.2 |
573.20 |
20000.00 |
0.8000 |
426.2 |
573.20 |
20000.00 |
1.0000 |
421.1 |
573.20 |
30000.00 |
0.0000 |
750.7 |
573.20 |
30000.00 |
0.1000 |
674.8 |
573.20 |
30000.00 |
0.2000 |
621.4 |
573.20 |
30000.00 |
0.3000 |
582.5 |
573.20 |
30000.00 |
0.4000 |
553.5 |
573.20 |
30000.00 |
0.6000 |
517.6 |
573.20 |
30000.00 |
0.8000 |
499.0 |
573.20 |
30000.00 |
1.0000 |
491.5 |
573.20 |
40000.00 |
0.0000 |
764.3 |
573.20 |
40000.00 |
0.1000 |
694.9 |
573.20 |
40000.00 |
0.2000 |
647.6 |
573.20 |
40000.00 |
0.3000 |
614.0 |
573.20 |
40000.00 |
0.4000 |
587.9 |
573.20 |
40000.00 |
0.6000 |
557.4 |
573.20 |
40000.00 |
0.8000 |
540.4 |
573.20 |
40000.00 |
1.0000 |
531.0 |
618.20 |
20000.00 |
0.0000 |
619.7 |
618.20 |
20000.00 |
0.1000 |
445.3 |
618.20 |
20000.00 |
0.2000 |
281.3 |
618.20 |
20000.00 |
0.3000 |
250.4 |
618.20 |
20000.00 |
0.4000 |
253.1 |
618.20 |
20000.00 |
0.6000 |
270.6 |
618.20 |
20000.00 |
0.8000 |
295.0 |
618.20 |
20000.00 |
1.0000 |
314.6 |
618.20 |
30000.00 |
0.0000 |
656.9 |
618.20 |
30000.00 |
0.1000 |
566.3 |
618.20 |
30000.00 |
0.2000 |
501.5 |
618.20 |
30000.00 |
0.3000 |
460.9 |
618.20 |
30000.00 |
0.4000 |
437.4 |
618.20 |
30000.00 |
0.6000 |
420.1 |
618.20 |
30000.00 |
0.8000 |
418.9 |
618.20 |
30000.00 |
1.0000 |
423.8 |
618.20 |
40000.00 |
0.0000 |
682.3 |
618.20 |
40000.00 |
0.1000 |
610.3 |
618.20 |
40000.00 |
0.2000 |
561.0 |
618.20 |
40000.00 |
0.3000 |
529.3 |
618.20 |
40000.00 |
0.4000 |
509.1 |
618.20 |
40000.00 |
0.6000 |
488.2 |
618.20 |
40000.00 |
0.8000 |
481.7 |
618.20 |
40000.00 |
1.0000 |
481.2 |
Mass density, kg/m3
[ref]
Operational condition: Mole fraction =
0.5 (Liquid)
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
456.86 |
664.33 |
458.15 |
664.26 |
483.15 |
617.97 |
483.56 |
618.12 |
498.15 |
584.08 |
498.15 |
583.65 |
503.15 |
570.54 |
503.15 |
570.54 |
508.15 |
557.48 |
510.15 |
549.73 |
510.68 |
550.06 |
521.15 |
523.14 |
521.15 |
523.14 |
533.15 |
464.96 |
537.45 |
465.05 |
543.15 |
425.01 |
543.50 |
423.96 |
546.05 |
425.77 |
546.15 |
298.56 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Temperature, K - Fluid (supercritical or subcritical phases) |
Pressure, kPa - Fluid (supercritical or subcritical phases) |
Mole fraction of Ethanol (1) - Fluid (supercritical or subcritical phases) |
Mass density, kg/m3 - Fluid (supercritical or subcritical phases) |
524.15 |
7270.00 |
0.8000 |
383.33 |
525.15 |
7460.00 |
0.8000 |
383.31 |
526.15 |
7550.00 |
0.8000 |
367.95 |
528.15 |
7710.00 |
0.8000 |
312.86 |
528.15 |
7870.00 |
0.8000 |
367.91 |
528.15 |
8040.00 |
0.8000 |
383.24 |
528.15 |
8410.00 |
0.8000 |
406.33 |
531.15 |
8420.00 |
0.8000 |
367.86 |
533.15 |
4750.00 |
0.8000 |
53.24 |
533.15 |
7070.00 |
0.5000 |
84.52 |
533.15 |
7100.00 |
0.8000 |
115.14 |
533.15 |
8140.00 |
0.8000 |
188.77 |
533.15 |
8270.00 |
0.8000 |
244.11 |
533.15 |
8350.00 |
0.8000 |
284.34 |
533.15 |
8420.00 |
0.8000 |
312.77 |
533.15 |
8440.00 |
0.8000 |
307.44 |
533.15 |
8750.00 |
0.8000 |
367.82 |
533.15 |
8990.00 |
0.8000 |
383.14 |
533.15 |
9460.00 |
0.8000 |
406.22 |
533.15 |
10480.00 |
0.8000 |
440.21 |
533.15 |
10860.00 |
0.8000 |
446.58 |
533.15 |
17410.00 |
0.8000 |
516.16 |
533.15 |
8270.00 |
0.8000 |
260.96 |
533.15 |
10480.00 |
0.8000 |
440.21 |
533.15 |
10860.00 |
0.8000 |
446.58 |
538.15 |
9170.00 |
0.8000 |
312.69 |
538.15 |
27310.00 |
0.8000 |
553.51 |
538.15 |
27310.00 |
0.8000 |
553.51 |
543.15 |
4920.00 |
0.8000 |
53.21 |
543.15 |
7570.00 |
0.5000 |
84.48 |
543.15 |
7610.00 |
0.8000 |
115.08 |
543.15 |
9020.00 |
0.8000 |
188.68 |
543.15 |
9530.00 |
0.8000 |
260.83 |
543.15 |
9680.00 |
0.8000 |
284.19 |
543.15 |
9920.00 |
0.8000 |
312.61 |
543.15 |
10630.00 |
0.8000 |
367.62 |
543.15 |
10940.00 |
0.8000 |
382.93 |
543.15 |
11670.00 |
0.8000 |
406.0 |
548.15 |
7850.00 |
0.8000 |
115.06 |
548.15 |
9420.00 |
0.8000 |
188.63 |
548.15 |
9680.00 |
0.5000 |
294.01 |
548.15 |
9720.00 |
0.5000 |
327.56 |
548.15 |
9980.00 |
0.8000 |
243.92 |
548.15 |
10390.00 |
0.5000 |
421.66 |
548.15 |
10630.00 |
0.8000 |
307.19 |
548.15 |
10680.00 |
0.8000 |
312.53 |
548.15 |
11790.00 |
0.5000 |
464.07 |
548.15 |
11950.00 |
0.8000 |
382.83 |
548.15 |
14420.00 |
0.8000 |
439.83 |
548.15 |
14800.00 |
0.8000 |
446.2 |
548.15 |
17240.00 |
0.5000 |
522.28 |
548.15 |
26570.00 |
0.5000 |
568.89 |
548.15 |
30490.00 |
0.5000 |
581.74 |
548.15 |
14420.00 |
0.8000 |
439.83 |
548.15 |
14800.00 |
0.8000 |
446.2 |
553.15 |
5080.00 |
0.8000 |
53.19 |
553.15 |
6130.00 |
0.5000 |
55.97 |
553.15 |
7190.00 |
0.5000 |
69.28 |
553.15 |
7970.00 |
0.5000 |
84.44 |
553.15 |
9210.00 |
0.5000 |
117.47 |
553.15 |
10090.00 |
0.5000 |
171.33 |
553.15 |
10330.00 |
0.5000 |
234.67 |
553.15 |
10520.00 |
0.5000 |
327.48 |
553.15 |
10600.00 |
0.5000 |
293.93 |
553.15 |
10890.00 |
0.5000 |
385.77 |
553.15 |
11430.00 |
0.8000 |
312.45 |
553.15 |
11790.00 |
0.5000 |
424.77 |
553.15 |
11850.00 |
0.5000 |
419.86 |
553.15 |
12540.00 |
0.8000 |
367.42 |
553.15 |
13460.00 |
0.5000 |
463.93 |
553.15 |
19450.00 |
0.5000 |
522.11 |
553.15 |
25160.00 |
0.8000 |
515.53 |
553.15 |
25720.00 |
0.5000 |
555.9 |
553.15 |
47100.00 |
0.5000 |
614.98 |
558.15 |
8310.00 |
0.8000 |
115.0 |
558.15 |
10340.00 |
0.8000 |
188.54 |
558.15 |
11380.00 |
0.8000 |
260.63 |
558.15 |
11700.00 |
0.8000 |
283.97 |
558.15 |
13990.00 |
0.8000 |
382.62 |
558.15 |
15170.00 |
0.8000 |
405.66 |
563.15 |
6360.00 |
0.5000 |
55.95 |
563.15 |
7510.00 |
0.5000 |
69.25 |
563.15 |
8400.00 |
0.5000 |
84.4 |
563.15 |
8830.00 |
0.2000 |
67.68 |
563.15 |
9900.00 |
0.5000 |
117.41 |
563.15 |
11080.00 |
0.5000 |
171.24 |
563.15 |
12360.00 |
0.5000 |
327.3 |
563.15 |
12940.00 |
0.8000 |
312.28 |
563.15 |
12970.00 |
0.8000 |
312.28 |
563.15 |
13290.00 |
0.5000 |
385.56 |
563.15 |
14460.00 |
0.8000 |
367.22 |
563.15 |
16510.00 |
0.5000 |
463.66 |
563.15 |
23620.00 |
0.5000 |
521.79 |
568.15 |
9040.00 |
0.2000 |
67.66 |
573.15 |
5420.00 |
0.8000 |
53.14 |
573.15 |
6590.00 |
0.5000 |
55.92 |
573.15 |
7820.00 |
0.5000 |
69.21 |
573.15 |
8780.00 |
0.5000 |
84.36 |
573.15 |
8990.00 |
0.8000 |
114.92 |
573.15 |
10460.00 |
0.5000 |
117.35 |
573.15 |
11580.00 |
0.8000 |
188.4 |
573.15 |
12050.00 |
0.5000 |
171.15 |
573.15 |
12840.00 |
0.8000 |
243.61 |
573.15 |
13010.00 |
0.5000 |
234.43 |
573.15 |
13190.00 |
0.8000 |
260.43 |
573.15 |
13610.00 |
0.5000 |
293.62 |
573.15 |
13720.00 |
0.8000 |
283.75 |
573.15 |
14410.00 |
0.8000 |
306.79 |
573.15 |
14490.00 |
0.8000 |
312.12 |
573.15 |
15660.00 |
0.5000 |
385.34 |
573.15 |
16440.00 |
0.8000 |
367.02 |
573.15 |
16820.00 |
0.5000 |
419.39 |
573.15 |
17060.00 |
0.5000 |
421.07 |
573.15 |
17150.00 |
0.8000 |
382.31 |
573.15 |
17210.00 |
0.5000 |
424.29 |
573.15 |
18650.00 |
0.8000 |
405.32 |
573.15 |
20120.00 |
0.5000 |
463.38 |
573.15 |
21340.00 |
0.8000 |
439.21 |
573.15 |
22500.00 |
0.8000 |
451.39 |
573.15 |
28040.00 |
0.5000 |
521.47 |
573.15 |
39960.00 |
0.5000 |
567.95 |
573.15 |
44900.00 |
0.5000 |
580.76 |
573.15 |
21340.00 |
0.8000 |
439.21 |
573.15 |
22500.00 |
0.8000 |
451.39 |
577.15 |
45760.00 |
0.8000 |
552.13 |
577.15 |
45760.00 |
0.8000 |
552.13 |
578.15 |
23390.00 |
0.8000 |
445.43 |
578.15 |
35170.00 |
0.8000 |
514.74 |
578.15 |
38000.00 |
0.5000 |
555.01 |
578.15 |
23390.00 |
0.8000 |
445.43 |
593.15 |
50760.00 |
0.5000 |
567.2 |
598.15 |
5820.00 |
0.8000 |
53.08 |
598.15 |
7080.00 |
0.5000 |
55.85 |
598.15 |
8560.00 |
0.5000 |
69.13 |
598.15 |
9720.00 |
0.5000 |
84.26 |
598.15 |
10060.00 |
0.8000 |
114.78 |
598.15 |
11840.00 |
0.5000 |
117.21 |
598.15 |
12030.00 |
0.2000 |
90.05 |
598.15 |
13600.00 |
0.8000 |
188.16 |
598.15 |
14290.00 |
0.2000 |
138.08 |
598.15 |
15290.00 |
0.2000 |
221.72 |
598.15 |
15460.00 |
0.2000 |
286.74 |
598.15 |
15540.00 |
0.2000 |
308.36 |
598.15 |
15600.00 |
0.8000 |
243.3 |
598.15 |
15640.00 |
0.2000 |
325.01 |
598.15 |
16230.00 |
0.8000 |
260.09 |
598.15 |
16810.00 |
0.2000 |
420.24 |
598.15 |
17080.00 |
0.8000 |
283.38 |
598.15 |
18140.00 |
0.8000 |
306.39 |
598.15 |
18350.00 |
0.8000 |
311.71 |
598.15 |
19160.00 |
0.5000 |
326.69 |
598.15 |
21410.00 |
0.8000 |
366.53 |
598.15 |
21610.00 |
0.5000 |
384.81 |
598.15 |
21850.00 |
0.5000 |
418.8 |
598.15 |
22460.00 |
0.8000 |
381.79 |
598.15 |
24130.00 |
0.5000 |
420.47 |
598.15 |
24210.00 |
0.5000 |
423.68 |
598.15 |
24610.00 |
0.8000 |
404.76 |
598.15 |
27590.00 |
0.2000 |
547.13 |
598.15 |
28350.00 |
0.8000 |
438.59 |
598.15 |
28670.00 |
0.5000 |
462.7 |
598.15 |
38940.00 |
0.5000 |
520.65 |
598.15 |
48240.00 |
0.2000 |
617.36 |
598.15 |
48500.00 |
0.5000 |
554.28 |
598.15 |
28350.00 |
0.8000 |
438.59 |
603.15 |
10470.00 |
0.2000 |
67.54 |
603.15 |
12120.00 |
0.5000 |
117.18 |
603.15 |
14860.00 |
0.5000 |
170.89 |
603.15 |
16860.00 |
0.2000 |
350.86 |
603.15 |
16940.00 |
0.5000 |
234.07 |
603.15 |
18730.00 |
0.5000 |
293.15 |
613.15 |
23290.00 |
0.2000 |
452.8 |
623.15 |
6210.00 |
0.8000 |
53.01 |
623.15 |
7610.00 |
0.5000 |
55.79 |
623.15 |
9230.00 |
0.5000 |
69.05 |
623.15 |
10590.00 |
0.5000 |
84.15 |
623.15 |
11070.00 |
0.8000 |
114.64 |
623.15 |
13180.00 |
0.5000 |
117.07 |
623.15 |
13400.00 |
0.2000 |
89.94 |
623.15 |
15510.00 |
0.8000 |
187.93 |
623.15 |
16770.00 |
0.2000 |
137.9 |
623.15 |
18300.00 |
0.8000 |
242.99 |
623.15 |
19450.00 |
0.2000 |
221.42 |
623.15 |
20470.00 |
0.8000 |
283.01 |
623.15 |
20590.00 |
0.2000 |
286.35 |
623.15 |
21000.00 |
0.2000 |
307.94 |
623.15 |
21380.00 |
0.2000 |
324.56 |
623.15 |
21860.00 |
0.8000 |
305.99 |
623.15 |
21920.00 |
0.2000 |
350.47 |
623.15 |
22240.00 |
0.8000 |
311.3 |
623.15 |
24920.00 |
0.2000 |
420.24 |
623.15 |
26360.00 |
0.8000 |
366.04 |
623.15 |
27820.00 |
0.8000 |
381.27 |
623.15 |
27940.00 |
0.5000 |
384.27 |
623.15 |
30710.00 |
0.8000 |
404.2 |
623.15 |
31220.00 |
0.5000 |
418.2 |
623.15 |
31480.00 |
0.5000 |
419.87 |
623.15 |
31720.00 |
0.5000 |
423.08 |
623.15 |
36430.00 |
0.8000 |
444.29 |
623.15 |
37340.00 |
0.5000 |
462.02 |
623.15 |
41330.00 |
0.2000 |
546.22 |
623.15 |
50360.00 |
0.5000 |
519.83 |
623.15 |
36430.00 |
0.8000 |
444.29 |
628.15 |
19790.00 |
0.8000 |
259.69 |
628.15 |
36970.00 |
0.8000 |
437.84 |
628.15 |
36970.00 |
0.8000 |
437.84 |
633.15 |
11600.00 |
0.2000 |
67.45 |
633.15 |
13740.00 |
0.5000 |
117.01 |
633.15 |
17410.00 |
0.5000 |
170.64 |
633.15 |
23850.00 |
0.5000 |
292.69 |
633.15 |
26000.00 |
0.5000 |
326.07 |
638.15 |
21420.00 |
0.5000 |
233.65 |
643.15 |
35160.00 |
0.2000 |
451.97 |
648.15 |
6600.00 |
0.8000 |
52.95 |
648.15 |
8080.00 |
0.5000 |
55.72 |
648.15 |
9890.00 |
0.5000 |
68.96 |
648.15 |
11430.00 |
0.5000 |
84.05 |
648.15 |
12050.00 |
0.8000 |
114.5 |
648.15 |
14470.00 |
0.5000 |
116.92 |
648.15 |
14680.00 |
0.2000 |
89.83 |
648.15 |
17440.00 |
0.8000 |
187.69 |
648.15 |
19110.00 |
0.2000 |
137.73 |
648.15 |
23400.00 |
0.2000 |
221.13 |
648.15 |
25670.00 |
0.8000 |
305.59 |
648.15 |
25860.00 |
0.2000 |
285.96 |
648.15 |
26120.00 |
0.8000 |
310.89 |
648.15 |
26740.00 |
0.2000 |
307.52 |
648.15 |
28730.00 |
0.2000 |
349.97 |
648.15 |
31420.00 |
0.8000 |
365.54 |
648.15 |
33230.00 |
0.8000 |
380.75 |
648.15 |
33660.00 |
0.2000 |
420.24 |
648.15 |
34330.00 |
0.5000 |
383.73 |
648.15 |
36760.00 |
0.8000 |
403.64 |
648.15 |
39020.00 |
0.5000 |
419.27 |
653.15 |
19550.00 |
0.2000 |
137.7 |
653.15 |
21530.00 |
0.8000 |
242.62 |
653.15 |
22750.00 |
0.8000 |
259.36 |
653.15 |
24460.00 |
0.8000 |
282.58 |
653.15 |
26990.00 |
0.8000 |
310.81 |
653.15 |
28660.00 |
0.2000 |
324.03 |
653.15 |
34300.00 |
0.8000 |
380.65 |
653.15 |
35620.00 |
0.5000 |
383.63 |
653.15 |
40110.00 |
0.5000 |
417.48 |
653.15 |
40890.00 |
0.5000 |
422.34 |
653.15 |
44100.00 |
0.8000 |
437.21 |
653.15 |
48080.00 |
0.5000 |
461.19 |
653.15 |
44100.00 |
0.8000 |
437.21 |
673.15 |
6990.00 |
0.8000 |
52.89 |
673.15 |
8570.00 |
0.5000 |
55.65 |
673.15 |
10540.00 |
0.5000 |
68.88 |
673.15 |
12250.00 |
0.5000 |
83.95 |
673.15 |
12980.00 |
0.2000 |
67.32 |
673.15 |
13010.00 |
0.8000 |
114.36 |
673.15 |
15740.00 |
0.5000 |
116.78 |
673.15 |
15940.00 |
0.2000 |
89.72 |
673.15 |
19310.00 |
0.8000 |
187.46 |
673.15 |
20680.00 |
0.5000 |
170.3 |
673.15 |
21310.00 |
0.2000 |
137.56 |
673.15 |
23620.00 |
0.8000 |
242.38 |
673.15 |
25130.00 |
0.8000 |
259.1 |
673.15 |
25740.00 |
0.5000 |
233.23 |
673.15 |
27230.00 |
0.8000 |
282.28 |
673.15 |
27430.00 |
0.2000 |
220.84 |
673.15 |
29500.00 |
0.8000 |
305.19 |
673.15 |
30040.00 |
0.8000 |
310.49 |
673.15 |
30620.00 |
0.5000 |
292.07 |
673.15 |
31230.00 |
0.2000 |
285.57 |
673.15 |
32510.00 |
0.2000 |
307.09 |
673.15 |
33730.00 |
0.2000 |
323.66 |
673.15 |
34050.00 |
0.5000 |
325.37 |
673.15 |
35510.00 |
0.2000 |
349.48 |
673.15 |
36420.00 |
0.8000 |
365.05 |
673.15 |
38700.00 |
0.8000 |
380.23 |
673.15 |
40850.00 |
0.5000 |
383.2 |
673.15 |
42660.00 |
0.2000 |
420.24 |
673.15 |
42950.00 |
0.8000 |
403.08 |
673.15 |
46620.00 |
0.5000 |
418.66 |
673.15 |
47140.00 |
0.2000 |
451.15 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Water (2) - Liquid |
Mass density, kg/m3 - Liquid |
293.15 |
0.0000 |
789.75 |
293.15 |
0.0501 |
795.99 |
293.15 |
0.0986 |
802.09 |
293.15 |
0.1961 |
814.88 |
293.15 |
0.2961 |
829.05 |
293.15 |
0.3991 |
845.25 |
293.15 |
0.4971 |
862.82 |
293.15 |
0.5989 |
884.07 |
293.15 |
0.6991 |
908.69 |
293.15 |
0.8001 |
937.33 |
293.15 |
0.8996 |
965.71 |
293.15 |
0.9499 |
979.28 |
293.15 |
1.0000 |
998.2 |
298.15 |
0.0000 |
785.46 |
298.15 |
0.0501 |
791.68 |
298.15 |
0.0986 |
797.77 |
298.15 |
0.1961 |
810.54 |
298.15 |
0.2961 |
824.7 |
298.15 |
0.3991 |
840.94 |
298.15 |
0.5989 |
879.89 |
298.15 |
0.6991 |
904.65 |
298.15 |
0.8001 |
933.65 |
298.15 |
0.8996 |
963.24 |
298.15 |
0.9499 |
977.72 |
298.15 |
1.0000 |
997.05 |
303.15 |
0.0000 |
781.15 |
303.15 |
0.0501 |
787.35 |
303.15 |
0.0986 |
793.41 |
303.15 |
0.1961 |
806.14 |
303.15 |
0.2961 |
820.29 |
303.15 |
0.3991 |
836.55 |
303.15 |
0.5989 |
875.63 |
303.15 |
0.6991 |
900.55 |
303.15 |
0.8001 |
929.9 |
303.15 |
0.8996 |
960.61 |
303.15 |
0.9499 |
975.93 |
303.15 |
1.0000 |
995.65 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Water (2) - Liquid |
Mass density, kg/m3 - Liquid |
278.15 |
0.0010 |
802.2 |
278.15 |
0.0021 |
802.34 |
278.15 |
0.0041 |
802.59 |
278.15 |
0.0067 |
802.91 |
278.15 |
0.0093 |
803.22 |
278.15 |
0.0119 |
803.54 |
278.15 |
0.0144 |
803.85 |
278.15 |
0.0179 |
804.29 |
278.15 |
0.0211 |
804.68 |
278.15 |
0.0251 |
805.17 |
278.15 |
0.0292 |
805.69 |
278.15 |
0.0312 |
805.94 |
278.15 |
0.0336 |
806.24 |
278.15 |
0.0366 |
806.61 |
288.15 |
0.0010 |
793.72 |
288.15 |
0.0021 |
793.86 |
288.15 |
0.0041 |
794.1 |
288.15 |
0.0067 |
794.42 |
288.15 |
0.0093 |
794.73 |
288.15 |
0.0119 |
795.06 |
288.15 |
0.0144 |
795.37 |
288.15 |
0.0179 |
795.8 |
288.15 |
0.0211 |
796.2 |
288.15 |
0.0251 |
796.68 |
288.15 |
0.0292 |
797.2 |
288.15 |
0.0312 |
797.46 |
288.15 |
0.0336 |
797.75 |
288.15 |
0.0366 |
798.13 |
298.15 |
0.0010 |
785.15 |
298.15 |
0.0021 |
785.29 |
298.15 |
0.0041 |
785.53 |
298.15 |
0.0067 |
785.85 |
298.15 |
0.0093 |
786.16 |
298.15 |
0.0119 |
786.48 |
298.15 |
0.0144 |
786.79 |
298.15 |
0.0179 |
787.22 |
298.15 |
0.0211 |
787.61 |
298.15 |
0.0251 |
788.1 |
298.15 |
0.0292 |
788.61 |
298.15 |
0.0312 |
788.87 |
298.15 |
0.0336 |
789.16 |
298.15 |
0.0366 |
789.54 |
308.15 |
0.0010 |
776.47 |
308.15 |
0.0021 |
776.61 |
308.15 |
0.0041 |
776.85 |
308.15 |
0.0067 |
777.16 |
308.15 |
0.0093 |
777.47 |
308.15 |
0.0119 |
777.79 |
308.15 |
0.0144 |
778.09 |
308.15 |
0.0179 |
778.52 |
308.15 |
0.0211 |
778.92 |
308.15 |
0.0251 |
779.4 |
308.15 |
0.0292 |
779.91 |
308.15 |
0.0312 |
780.16 |
308.15 |
0.0336 |
780.45 |
308.15 |
0.0366 |
780.83 |
318.15 |
0.0010 |
767.66 |
318.15 |
0.0021 |
767.79 |
318.15 |
0.0041 |
768.03 |
318.15 |
0.0067 |
768.34 |
318.15 |
0.0093 |
768.65 |
318.15 |
0.0119 |
768.96 |
318.15 |
0.0144 |
769.26 |
318.15 |
0.0179 |
769.69 |
318.15 |
0.0211 |
770.08 |
318.15 |
0.0251 |
770.56 |
318.15 |
0.0292 |
771.06 |
318.15 |
0.0312 |
771.31 |
318.15 |
0.0336 |
771.6 |
318.15 |
0.0366 |
771.97 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
84.5 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Molality, mol/kg of Ethanol (1) - Liquid |
Mass density, kg/m3 - Liquid |
288.15 |
0.0216 |
998.9 |
288.15 |
0.0435 |
998.707 |
288.15 |
0.0649 |
998.526 |
288.15 |
0.0865 |
998.318 |
288.15 |
0.1087 |
998.132 |
288.15 |
0.1306 |
997.942 |
288.15 |
0.1749 |
997.562 |
288.15 |
0.2188 |
997.195 |
293.15 |
0.0216 |
998.003 |
293.15 |
0.0435 |
997.81 |
293.15 |
0.0649 |
997.632 |
293.15 |
0.0865 |
997.424 |
293.15 |
0.1087 |
997.24 |
293.15 |
0.1306 |
997.051 |
293.15 |
0.1749 |
996.671 |
293.15 |
0.2188 |
996.303 |
298.15 |
0.0216 |
996.845 |
298.15 |
0.0435 |
996.654 |
298.15 |
0.0649 |
996.474 |
298.15 |
0.0865 |
996.265 |
298.15 |
0.1087 |
996.081 |
298.15 |
0.1306 |
995.892 |
298.15 |
0.1749 |
995.508 |
298.15 |
0.2188 |
995.144 |
303.15 |
0.0216 |
995.446 |
303.15 |
0.0435 |
995.257 |
303.15 |
0.0649 |
995.076 |
303.15 |
0.0865 |
994.87 |
303.15 |
0.1087 |
994.683 |
303.15 |
0.1306 |
994.494 |
303.15 |
0.1749 |
994.111 |
303.15 |
0.2188 |
993.747 |
308.15 |
0.0216 |
993.829 |
308.15 |
0.0435 |
993.639 |
308.15 |
0.0649 |
993.46 |
308.15 |
0.0865 |
993.243 |
308.15 |
0.1087 |
993.05 |
308.15 |
0.1306 |
992.873 |
308.15 |
0.1749 |
992.498 |
308.15 |
0.2188 |
992.123 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
92.3 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol (1) - Liquid |
Mass density, kg/m3 - Liquid |
293.15 |
0.0024 |
997.039 |
293.15 |
0.0202 |
989.382 |
293.15 |
0.0295 |
985.977 |
293.15 |
0.0366 |
983.574 |
293.15 |
0.0513 |
978.913 |
293.15 |
0.0600 |
976.452 |
293.15 |
0.0707 |
973.538 |
293.15 |
0.0801 |
971.049 |
293.15 |
0.0904 |
968.313 |
293.15 |
0.0997 |
965.87 |
293.15 |
0.1294 |
957.918 |
293.15 |
0.1497 |
952.184 |
293.15 |
0.2008 |
937.088 |
293.15 |
0.2503 |
922.612 |
293.15 |
0.2998 |
908.897 |
293.15 |
0.3507 |
895.841 |
293.15 |
0.3992 |
884.433 |
293.15 |
0.4514 |
873.258 |
293.15 |
0.5002 |
863.248 |
293.15 |
0.5494 |
854.117 |
293.15 |
0.6018 |
845.002 |
293.15 |
0.6503 |
837.196 |
293.15 |
0.7006 |
829.434 |
293.15 |
0.7355 |
824.262 |
293.15 |
0.7965 |
815.831 |
293.15 |
0.8433 |
809.567 |
293.15 |
0.8920 |
803.132 |
293.15 |
0.9093 |
800.938 |
293.15 |
0.9207 |
799.51 |
293.15 |
0.9307 |
798.225 |
293.15 |
0.9398 |
797.133 |
293.15 |
0.9483 |
796.043 |
293.15 |
0.9603 |
794.596 |
293.15 |
0.9702 |
793.374 |
293.15 |
0.9801 |
792.038 |
293.15 |
0.9895 |
791.076 |
298.15 |
0.0024 |
995.871 |
298.15 |
0.0202 |
988.159 |
298.15 |
0.0295 |
984.669 |
298.15 |
0.0366 |
982.196 |
298.15 |
0.0513 |
977.287 |
298.15 |
0.0600 |
974.729 |
298.15 |
0.0707 |
971.631 |
298.15 |
0.0801 |
968.969 |
298.15 |
0.0904 |
966.039 |
298.15 |
0.0997 |
963.419 |
298.15 |
0.1294 |
954.963 |
298.15 |
0.1497 |
948.951 |
298.15 |
0.2008 |
933.41 |
298.15 |
0.2503 |
918.708 |
298.15 |
0.2998 |
904.858 |
298.15 |
0.3507 |
891.711 |
298.15 |
0.3992 |
880.239 |
298.15 |
0.4514 |
869.012 |
298.15 |
0.5002 |
858.963 |
298.15 |
0.5494 |
849.801 |
298.15 |
0.6018 |
840.665 |
298.15 |
0.6503 |
832.839 |
298.15 |
0.7006 |
825.07 |
298.15 |
0.7355 |
819.907 |
298.15 |
0.7965 |
811.475 |
298.15 |
0.8433 |
805.219 |
298.15 |
0.8920 |
798.808 |
298.15 |
0.9093 |
796.615 |
298.15 |
0.9207 |
795.193 |
298.15 |
0.9307 |
793.91 |
298.15 |
0.9398 |
792.821 |
298.15 |
0.9483 |
791.735 |
298.15 |
0.9603 |
790.291 |
298.15 |
0.9702 |
789.073 |
298.15 |
0.9801 |
787.741 |
298.15 |
0.9895 |
786.779 |
303.15 |
0.0024 |
994.464 |
303.15 |
0.0202 |
986.01 |
303.15 |
0.0295 |
983.11 |
303.15 |
0.0366 |
980.577 |
303.15 |
0.0513 |
975.532 |
303.15 |
0.0600 |
972.787 |
303.15 |
0.0707 |
969.513 |
303.15 |
0.0801 |
966.689 |
303.15 |
0.0904 |
963.577 |
303.15 |
0.0997 |
960.797 |
303.15 |
0.1294 |
951.878 |
303.15 |
0.1497 |
945.612 |
303.15 |
0.2008 |
929.658 |
303.15 |
0.2503 |
914.742 |
303.15 |
0.2998 |
900.761 |
303.15 |
0.3507 |
887.521 |
303.15 |
0.3992 |
875.988 |
303.15 |
0.4514 |
864.712 |
303.15 |
0.5002 |
854.622 |
303.15 |
0.5494 |
845.433 |
303.15 |
0.6018 |
836.274 |
303.15 |
0.6503 |
828.435 |
303.15 |
0.7006 |
820.66 |
303.15 |
0.7355 |
815.498 |
303.15 |
0.7965 |
807.074 |
303.15 |
0.8433 |
800.833 |
303.15 |
0.8920 |
794.442 |
303.15 |
0.9093 |
792.256 |
303.15 |
0.9207 |
790.841 |
303.15 |
0.9307 |
789.562 |
303.15 |
0.9398 |
788.477 |
303.15 |
0.9483 |
787.394 |
303.15 |
0.9603 |
785.958 |
303.15 |
0.9702 |
784.743 |
303.15 |
0.9801 |
783.417 |
303.15 |
0.9895 |
782.456 |
308.15 |
0.0024 |
992.863 |
308.15 |
0.0202 |
984.706 |
308.15 |
0.0295 |
981.361 |
308.15 |
0.0366 |
978.735 |
308.15 |
0.0513 |
973.534 |
308.15 |
0.0600 |
970.651 |
308.15 |
0.0707 |
967.196 |
308.15 |
0.0801 |
964.224 |
308.15 |
0.0904 |
960.944 |
308.15 |
0.0997 |
958.013 |
308.15 |
0.1294 |
948.682 |
308.15 |
0.1497 |
942.174 |
308.15 |
0.2008 |
925.836 |
308.15 |
0.2503 |
910.712 |
308.15 |
0.2998 |
896.603 |
308.15 |
0.3507 |
883.273 |
308.15 |
0.3992 |
871.678 |
308.15 |
0.4514 |
860.353 |
308.15 |
0.5002 |
850.223 |
308.15 |
0.5494 |
841.009 |
308.15 |
0.6018 |
831.83 |
308.15 |
0.6503 |
823.98 |
308.15 |
0.7006 |
816.2 |
308.15 |
0.7355 |
811.052 |
308.15 |
0.7965 |
802.628 |
308.15 |
0.8433 |
796.401 |
308.15 |
0.8920 |
790.037 |
308.15 |
0.9093 |
787.861 |
308.15 |
0.9207 |
786.448 |
308.15 |
0.9307 |
785.175 |
308.15 |
0.9398 |
784.096 |
308.15 |
0.9483 |
783.019 |
308.15 |
0.9603 |
781.59 |
308.15 |
0.9702 |
780.379 |
308.15 |
0.9801 |
779.061 |
308.15 |
0.9895 |
778.103 |
293.15 |
0.0000 |
998.429 |
298.15 |
0.0000 |
997.267 |
303.15 |
0.0000 |
995.867 |
308.15 |
0.0000 |
994.252 |
293.15 |
1.0000 |
789.547 |
298.15 |
1.0000 |
785.26 |
303.15 |
1.0000 |
780.941 |
308.15 |
1.0000 |
776.592 |
293.15 |
0.0201 |
989.54 |
293.15 |
0.0408 |
982.27 |
293.15 |
0.0497 |
979.54 |
293.15 |
0.0600 |
976.51 |
293.15 |
0.0796 |
971.24 |
293.15 |
0.1004 |
963.75 |
293.15 |
0.1499 |
951.92 |
293.15 |
0.1984 |
935.19 |
293.15 |
0.2499 |
922.7 |
293.15 |
0.3016 |
908.77 |
293.15 |
0.3499 |
896.37 |
293.15 |
0.3990 |
884.54 |
293.15 |
0.4495 |
873.57 |
293.15 |
0.4989 |
864.28 |
293.15 |
0.5495 |
854.95 |
293.15 |
0.6067 |
844.7 |
293.15 |
0.6503 |
837.27 |
293.15 |
0.6956 |
830.42 |
293.15 |
0.7500 |
822.4 |
293.15 |
0.7843 |
817.86 |
293.15 |
0.8475 |
809.97 |
293.15 |
0.8864 |
804.22 |
293.15 |
0.9290 |
798.49 |
298.15 |
0.0201 |
988.31 |
298.15 |
0.0408 |
980.85 |
298.15 |
0.0497 |
977.99 |
298.15 |
0.0600 |
974.31 |
298.15 |
0.0796 |
969.17 |
298.15 |
0.1004 |
961.4 |
298.15 |
0.1499 |
948.9 |
298.15 |
0.1984 |
931.84 |
298.15 |
0.2499 |
918.95 |
298.15 |
0.3016 |
904.86 |
298.15 |
0.3499 |
892.28 |
298.15 |
0.3990 |
880.34 |
298.15 |
0.4495 |
869.34 |
298.15 |
0.4989 |
860.04 |
298.15 |
0.5495 |
850.72 |
298.15 |
0.6067 |
840.19 |
298.15 |
0.6503 |
832.95 |
298.15 |
0.6956 |
826.05 |
298.15 |
0.7500 |
818.03 |
298.15 |
0.7843 |
813.49 |
298.15 |
0.8475 |
805.63 |
298.15 |
0.8864 |
799.93 |
298.15 |
0.9290 |
794.19 |
303.15 |
0.0201 |
986.86 |
303.15 |
0.0408 |
978.54 |
303.15 |
0.0497 |
976.06 |
303.15 |
0.0600 |
971.89 |
303.15 |
0.0796 |
966.81 |
303.15 |
0.1004 |
958.69 |
303.15 |
0.1499 |
945.56 |
303.15 |
0.1984 |
928.77 |
303.15 |
0.2499 |
915.3 |
303.15 |
0.3016 |
900.76 |
303.15 |
0.3499 |
888.09 |
303.15 |
0.3990 |
876.09 |
303.15 |
0.4495 |
865.03 |
303.15 |
0.4989 |
855.7 |
303.15 |
0.5495 |
846.35 |
303.15 |
0.6067 |
835.6 |
303.15 |
0.6503 |
828.55 |
303.15 |
0.6956 |
821.65 |
303.15 |
0.7500 |
813.63 |
303.15 |
0.7843 |
809.09 |
303.15 |
0.8475 |
801.24 |
303.15 |
0.8864 |
795.58 |
303.15 |
0.9290 |
789.85 |
308.15 |
0.0201 |
985.15 |
308.15 |
0.0408 |
976.58 |
308.15 |
0.0497 |
973.32 |
308.15 |
0.0600 |
969.36 |
308.15 |
0.0796 |
964.08 |
308.15 |
0.1004 |
955.87 |
308.15 |
0.1499 |
942.15 |
308.15 |
0.1984 |
925.04 |
308.15 |
0.2499 |
911.28 |
308.15 |
0.3016 |
896.6 |
308.15 |
0.3499 |
883.84 |
308.15 |
0.3990 |
871.78 |
308.15 |
0.4495 |
860.66 |
308.15 |
0.4989 |
851.3 |
308.15 |
0.5495 |
841.93 |
308.15 |
0.6067 |
831.06 |
308.15 |
0.6503 |
824.09 |
308.15 |
0.6956 |
817.19 |
308.15 |
0.7500 |
809.16 |
308.15 |
0.7843 |
804.63 |
308.15 |
0.8475 |
796.81 |
308.15 |
0.8864 |
791.17 |
308.15 |
0.9290 |
785.46 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 100 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Mass density, kg/m3 - Liquid |
1.0000 |
785.5 |
0.7084 |
825.2 |
0.4238 |
876.2 |
0.3870 |
883.5 |
0.2437 |
920.1 |
0.1461 |
950.1 |
0.1270 |
952.3 |
0.0641 |
970.7 |
0.0000 |
997.1 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
85 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mass fraction of Ethanol (1) - Liquid |
Mass density, kg/m3 - Liquid |
298.15 |
0.0400 |
990.13 |
303.15 |
0.0400 |
988.79 |
308.15 |
0.0400 |
987.24 |
313.15 |
0.0400 |
985.42 |
298.15 |
0.0800 |
983.9 |
303.15 |
0.0800 |
982.43 |
308.15 |
0.0800 |
980.77 |
313.15 |
0.0800 |
978.85 |
298.15 |
0.1600 |
972.57 |
303.15 |
0.1600 |
970.69 |
308.15 |
0.1600 |
968.6 |
313.15 |
0.1600 |
966.4 |
Mass density, kg/m3
[ref]
Operational conditions:
- Pressure, kPa = 100 (Liquid)
- Molality, mol/kg = 16 (Liquid)
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
298.15 |
925.8 |
303.15 |
923.139 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 298.2 (Liquid)
- Pressure, kPa = 100 (Liquid)
Mass fraction of Water (2) - Liquid |
Mass density, kg/m3 - Liquid |
0.5080 |
911.41 |
0.4260 |
890.1 |
0.3110 |
865.5 |
0.2470 |
850.5 |
0.2350 |
847.41 |
0.2060 |
841.91 |
Mass density, kg/m3
[ref]
Operational conditions:
- Pressure, kPa = 100 (Liquid)
- Temperature, K = 308.15 (Liquid)
Mass ratio of solute to solvent of Ethanol (1) - Liquid |
Mass density, kg/m3 - Liquid |
0.0500 |
990.6 |
0.1000 |
982.8 |
0.1500 |
971.7 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 298.2 (Liquid)
- Pressure, kPa = 100 (Liquid)
Mass fraction of Water (2) - Liquid |
Mass density, kg/m3 - Liquid |
0.0610 |
802.5 |
0.1240 |
819.5 |
0.1720 |
833.4 |
0.2330 |
848.2 |
0.2760 |
857.9 |
0.3400 |
861.8 |
0.4100 |
887.3 |
0.5000 |
908.8 |
0.6200 |
935.2 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mass fraction of Ethanol (1) - Liquid |
Mass density, kg/m3 - Liquid |
298.15 |
0.1084 |
979.29 |
298.15 |
0.1219 |
977.47 |
298.15 |
0.2859 |
953.33 |
298.15 |
0.2907 |
952.58 |
298.15 |
0.3737 |
937.25 |
298.15 |
0.3750 |
936.69 |
298.15 |
0.4432 |
922.6 |
298.15 |
0.4445 |
922.55 |
298.15 |
0.4998 |
910.43 |
298.15 |
0.5049 |
908.96 |
298.15 |
0.6193 |
882.85 |
298.15 |
0.6275 |
880.81 |
313.15 |
0.1672 |
964.04 |
313.15 |
0.2858 |
943.6 |
313.15 |
0.2894 |
942.82 |
313.15 |
0.3525 |
930.27 |
313.15 |
0.3757 |
925.3 |
313.15 |
0.4420 |
911.19 |
313.15 |
0.4445 |
910.92 |
313.15 |
0.4982 |
898.47 |
313.15 |
0.5018 |
897.76 |
313.15 |
0.6180 |
870.51 |
313.15 |
0.6271 |
868.41 |
313.15 |
0.7114 |
848.29 |
Mass density, kg/m3
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
Molality, mol/kg of Water (2) - Liquid |
Mass density, kg/m3 - Liquid |
0.0000 |
785.207 |
0.2140 |
786.407 |
0.2705 |
786.72 |
0.3199 |
786.998 |
0.3659 |
787.262 |
0.4543 |
787.753 |
0.5541 |
788.3 |
0.6437 |
788.782 |
0.7430 |
789.321 |
0.8349 |
789.775 |
0.9264 |
790.279 |
1.0189 |
790.734 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol (1) - Liquid |
Mass density, kg/m3 - Liquid |
283.15 |
0.0000 |
999.7 |
283.15 |
0.0106 |
994.82 |
283.15 |
0.0206 |
990.75 |
283.15 |
0.0301 |
987.45 |
283.15 |
0.0400 |
984.42 |
283.15 |
0.0513 |
981.3 |
283.15 |
0.0630 |
978.39 |
283.15 |
0.0737 |
975.9 |
283.15 |
0.0903 |
972.21 |
283.15 |
0.0988 |
970.36 |
283.15 |
0.1118 |
967.43 |
283.15 |
0.1274 |
963.79 |
283.15 |
0.1412 |
960.35 |
283.15 |
0.1546 |
956.87 |
283.15 |
0.1712 |
952.38 |
283.15 |
0.1883 |
947.66 |
283.15 |
0.2027 |
943.56 |
283.15 |
0.2245 |
937.39 |
283.15 |
0.2413 |
932.58 |
283.15 |
0.2602 |
927.36 |
283.15 |
0.2810 |
921.7 |
283.15 |
0.3008 |
916.48 |
283.15 |
0.3214 |
911.12 |
283.15 |
0.3422 |
905.93 |
283.15 |
0.3708 |
899.06 |
283.15 |
0.3898 |
894.64 |
283.15 |
0.4225 |
887.34 |
283.15 |
0.4419 |
883.22 |
283.15 |
0.4775 |
875.94 |
283.15 |
0.4998 |
871.65 |
283.15 |
0.5446 |
863.32 |
283.15 |
0.5631 |
860.06 |
283.15 |
0.6134 |
851.45 |
283.15 |
0.6385 |
847.44 |
283.15 |
0.6889 |
839.59 |
283.15 |
0.7182 |
835.36 |
283.15 |
0.7797 |
826.69 |
283.15 |
0.8252 |
820.4 |
283.15 |
0.8740 |
813.94 |
283.15 |
0.9388 |
805.69 |
283.15 |
1.0000 |
797.93 |
288.15 |
0.0000 |
999.1 |
288.15 |
0.0106 |
994.16 |
288.15 |
0.0206 |
990.1 |
288.15 |
0.0301 |
986.69 |
288.15 |
0.0400 |
983.51 |
288.15 |
0.0513 |
980.2 |
288.15 |
0.0630 |
977.08 |
288.15 |
0.0737 |
974.36 |
288.15 |
0.0903 |
970.32 |
288.15 |
0.0988 |
968.26 |
288.15 |
0.1118 |
965.05 |
288.15 |
0.1274 |
961.09 |
288.15 |
0.1412 |
957.42 |
288.15 |
0.1546 |
953.75 |
288.15 |
0.1712 |
949.03 |
288.15 |
0.1883 |
944.18 |
288.15 |
0.2027 |
939.92 |
288.15 |
0.2245 |
933.59 |
288.15 |
0.2413 |
928.78 |
288.15 |
0.2602 |
923.46 |
288.15 |
0.2810 |
917.78 |
288.15 |
0.3008 |
912.42 |
288.15 |
0.3214 |
907.08 |
288.15 |
0.3422 |
901.83 |
288.15 |
0.3708 |
894.93 |
288.15 |
0.3898 |
890.41 |
288.15 |
0.4225 |
883.12 |
288.15 |
0.4419 |
879.04 |
288.15 |
0.4775 |
871.68 |
288.15 |
0.4998 |
867.4 |
288.15 |
0.5446 |
859.02 |
288.15 |
0.5631 |
855.68 |
288.15 |
0.6134 |
847.1 |
288.15 |
0.6385 |
843.05 |
288.15 |
0.6889 |
835.22 |
288.15 |
0.7182 |
830.94 |
288.15 |
0.7797 |
822.24 |
288.15 |
0.8252 |
815.98 |
288.15 |
0.8740 |
809.54 |
288.15 |
0.9388 |
801.31 |
288.15 |
1.0000 |
793.64 |
293.15 |
0.0000 |
998.2 |
293.15 |
0.0106 |
993.29 |
293.15 |
0.0206 |
989.19 |
293.15 |
0.0301 |
985.7 |
293.15 |
0.0400 |
982.4 |
293.15 |
0.0513 |
978.92 |
293.15 |
0.0630 |
975.59 |
293.15 |
0.0737 |
972.67 |
293.15 |
0.0903 |
968.29 |
293.15 |
0.0988 |
966.06 |
293.15 |
0.1118 |
962.58 |
293.15 |
0.1274 |
958.36 |
293.15 |
0.1412 |
954.46 |
293.15 |
0.1546 |
950.63 |
293.15 |
0.1712 |
945.74 |
293.15 |
0.1883 |
940.71 |
293.15 |
0.2027 |
936.37 |
293.15 |
0.2245 |
929.93 |
293.15 |
0.2413 |
925.03 |
293.15 |
0.2602 |
919.65 |
293.15 |
0.2810 |
913.9 |
293.15 |
0.3008 |
908.52 |
293.15 |
0.3214 |
903.14 |
293.15 |
0.3422 |
897.88 |
293.15 |
0.3708 |
890.89 |
293.15 |
0.3898 |
886.45 |
293.15 |
0.4225 |
879.04 |
293.15 |
0.4419 |
874.93 |
293.15 |
0.4775 |
867.54 |
293.15 |
0.4998 |
863.22 |
293.15 |
0.5446 |
854.84 |
293.15 |
0.5631 |
851.52 |
293.15 |
0.6134 |
842.88 |
293.15 |
0.6385 |
838.78 |
293.15 |
0.6889 |
830.97 |
293.15 |
0.7182 |
826.69 |
293.15 |
0.7797 |
818.01 |
293.15 |
0.8252 |
811.73 |
293.15 |
0.8740 |
805.3 |
293.15 |
0.9388 |
797.05 |
293.15 |
1.0000 |
789.33 |
298.15 |
0.0000 |
997.04 |
298.15 |
0.0106 |
992.13 |
298.15 |
0.0206 |
987.96 |
298.15 |
0.0301 |
984.4 |
298.15 |
0.0400 |
981.01 |
298.15 |
0.0513 |
977.36 |
298.15 |
0.0630 |
973.84 |
298.15 |
0.0737 |
970.72 |
298.15 |
0.0903 |
966.02 |
298.15 |
0.0988 |
963.64 |
298.15 |
0.1118 |
959.93 |
298.15 |
0.1274 |
955.44 |
298.15 |
0.1412 |
951.35 |
298.15 |
0.1546 |
947.34 |
298.15 |
0.1712 |
942.26 |
298.15 |
0.1883 |
937.13 |
298.15 |
0.2027 |
932.69 |
298.15 |
0.2245 |
926.16 |
298.15 |
0.2413 |
921.17 |
298.15 |
0.2602 |
915.75 |
298.15 |
0.2810 |
909.9 |
298.15 |
0.3008 |
904.53 |
298.15 |
0.3214 |
899.05 |
298.15 |
0.3422 |
893.76 |
298.15 |
0.3708 |
886.75 |
298.15 |
0.3898 |
882.24 |
298.15 |
0.4225 |
874.82 |
298.15 |
0.4419 |
870.68 |
298.15 |
0.4775 |
863.28 |
298.15 |
0.4998 |
858.98 |
298.15 |
0.5446 |
850.55 |
298.15 |
0.5631 |
847.23 |
298.15 |
0.6134 |
838.56 |
298.15 |
0.6385 |
834.45 |
298.15 |
0.6889 |
826.63 |
298.15 |
0.7182 |
822.35 |
298.15 |
0.7797 |
813.64 |
298.15 |
0.8252 |
807.39 |
298.15 |
0.8740 |
800.98 |
298.15 |
0.9388 |
792.82 |
298.15 |
1.0000 |
785.22 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Molality, mol/kg of Ethanol (1) - Liquid |
Mass density, kg/m3 - Liquid |
293.15 |
14.0 |
936.706 |
293.15 |
16.0 |
930.583 |
293.15 |
18.0 |
924.182 |
298.15 |
14.0 |
933.024 |
298.15 |
16.0 |
926.799 |
298.15 |
18.0 |
920.298 |
303.15 |
14.0 |
929.265 |
303.15 |
16.0 |
922.942 |
303.15 |
18.0 |
916.351 |
308.15 |
14.0 |
925.437 |
308.15 |
16.0 |
919.015 |
308.15 |
18.0 |
912.337 |
313.15 |
14.0 |
921.529 |
313.15 |
16.0 |
915.018 |
313.15 |
18.0 |
908.255 |
293.15 |
20.0 |
918.792 |
293.15 |
22.0 |
913.462 |
298.15 |
20.0 |
914.849 |
298.15 |
22.0 |
909.466 |
303.15 |
20.0 |
910.842 |
303.15 |
22.0 |
905.406 |
308.15 |
20.0 |
906.77 |
308.15 |
22.0 |
901.281 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Water (2) - Liquid |
Mass density, kg/m3 - Liquid |
298.15 |
0.0998 |
797.6 |
298.15 |
0.2018 |
810.78 |
298.15 |
0.3085 |
826.73 |
298.15 |
0.4145 |
843.26 |
298.15 |
0.5001 |
858.65 |
298.15 |
0.6205 |
885.56 |
298.15 |
0.7005 |
904.69 |
298.15 |
0.7992 |
933.6 |
298.15 |
0.9051 |
965.51 |
318.15 |
0.1000 |
780.53 |
318.15 |
0.2010 |
793.6 |
318.15 |
0.3001 |
807.71 |
318.15 |
0.4004 |
823.81 |
318.15 |
0.5003 |
840.31 |
318.15 |
0.5998 |
863.31 |
318.15 |
0.7001 |
888.76 |
318.15 |
0.8001 |
919.19 |
318.15 |
0.9000 |
952.47 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Water (2) - Liquid |
Mass density, kg/m3 - Liquid |
283.15 |
0.0805 |
808.05 |
283.15 |
0.1584 |
818.14 |
283.15 |
0.2376 |
828.89 |
283.15 |
0.3322 |
842.93 |
283.15 |
0.4026 |
854.12 |
283.15 |
0.4910 |
869.86 |
283.15 |
0.5806 |
888.19 |
283.15 |
0.6480 |
903.57 |
283.15 |
0.7185 |
921.65 |
283.15 |
0.8009 |
944.6 |
283.15 |
0.8813 |
965.96 |
283.15 |
0.9605 |
984.04 |
288.15 |
0.0805 |
803.79 |
288.15 |
0.1584 |
813.87 |
288.15 |
0.2376 |
824.61 |
288.15 |
0.3322 |
838.67 |
288.15 |
0.4026 |
849.89 |
288.15 |
0.4910 |
865.67 |
288.15 |
0.5806 |
884.08 |
288.15 |
0.6480 |
899.55 |
288.15 |
0.7185 |
917.78 |
288.15 |
0.8009 |
941.07 |
288.15 |
0.8813 |
963.49 |
288.15 |
0.9605 |
983.11 |
293.15 |
0.0805 |
799.51 |
293.15 |
0.1584 |
809.57 |
293.15 |
0.2376 |
820.29 |
293.15 |
0.3322 |
834.37 |
293.15 |
0.4026 |
845.61 |
293.15 |
0.4910 |
861.44 |
293.15 |
0.5806 |
879.93 |
293.15 |
0.6480 |
895.48 |
293.15 |
0.7185 |
913.84 |
293.15 |
0.8009 |
937.48 |
293.15 |
0.8813 |
960.85 |
293.15 |
0.9605 |
981.89 |
298.15 |
0.0805 |
795.19 |
298.15 |
0.1584 |
805.23 |
298.15 |
0.2376 |
815.93 |
298.15 |
0.3322 |
830.01 |
298.15 |
0.4026 |
841.27 |
298.15 |
0.4910 |
857.16 |
298.15 |
0.5806 |
875.71 |
298.15 |
0.6480 |
891.35 |
298.15 |
0.7185 |
909.85 |
298.15 |
0.8009 |
933.81 |
298.15 |
0.8813 |
958.06 |
298.15 |
0.9605 |
980.42 |
303.15 |
0.0805 |
790.85 |
303.15 |
0.1584 |
800.84 |
303.15 |
0.2376 |
811.53 |
303.15 |
0.3322 |
825.61 |
303.15 |
0.4026 |
836.89 |
303.15 |
0.4910 |
852.81 |
303.15 |
0.5806 |
871.44 |
303.15 |
0.6480 |
887.16 |
303.15 |
0.7185 |
905.8 |
303.15 |
0.8009 |
930.07 |
303.15 |
0.8813 |
955.13 |
303.15 |
0.9605 |
978.75 |
308.15 |
0.0805 |
786.45 |
308.15 |
0.1584 |
796.41 |
308.15 |
0.2376 |
807.07 |
308.15 |
0.3322 |
821.15 |
308.15 |
0.4026 |
832.45 |
308.15 |
0.4910 |
848.4 |
308.15 |
0.5806 |
867.11 |
308.15 |
0.6480 |
882.91 |
308.15 |
0.7185 |
901.68 |
308.15 |
0.8009 |
926.25 |
308.15 |
0.8813 |
952.05 |
308.15 |
0.9605 |
976.91 |
313.15 |
0.0805 |
782.01 |
313.15 |
0.1584 |
791.93 |
313.15 |
0.2376 |
802.5 |
313.15 |
0.3322 |
816.63 |
313.15 |
0.4026 |
827.94 |
313.15 |
0.4910 |
843.95 |
313.15 |
0.5806 |
862.72 |
313.15 |
0.6480 |
878.59 |
313.15 |
0.7185 |
897.49 |
313.15 |
0.8009 |
922.34 |
313.15 |
0.8813 |
948.82 |
313.15 |
0.9605 |
974.89 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Mole fraction of Water (2) - Liquid |
Mass density, kg/m3 - Liquid |
0.0480 |
791.06 |
0.1116 |
799.08 |
0.1599 |
805.32 |
0.1761 |
807.44 |
0.2668 |
820.06 |
0.3010 |
825.06 |
0.3994 |
840.69 |
0.4970 |
858.26 |
0.6122 |
882.42 |
0.7116 |
907.85 |
0.7774 |
926.61 |
0.8145 |
937.62 |
0.8529 |
949.42 |
0.8967 |
960.95 |
0.9481 |
976.77 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Mole fraction of Water (2) - Liquid |
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
0.1000 |
268.10 |
824.9 |
0.1000 |
273.10 |
820.3 |
0.1000 |
278.10 |
815.9 |
0.1000 |
283.10 |
811.4 |
0.1000 |
288.15 |
806.9 |
0.1000 |
293.15 |
802.1 |
0.1000 |
298.15 |
797.7 |
0.1000 |
303.15 |
793.0 |
0.1000 |
308.15 |
788.2 |
0.1000 |
313.15 |
783.6 |
0.1000 |
318.15 |
779.0 |
0.1000 |
323.15 |
774.3 |
0.2000 |
268.10 |
838.2 |
0.2000 |
273.10 |
833.7 |
0.2000 |
278.10 |
829.0 |
0.2000 |
283.10 |
824.7 |
0.2000 |
288.15 |
820.1 |
0.2000 |
293.15 |
815.6 |
0.2000 |
298.15 |
811.0 |
0.2000 |
303.15 |
806.0 |
0.2000 |
308.15 |
801.4 |
0.2000 |
313.15 |
796.8 |
0.2000 |
318.15 |
792.2 |
0.2000 |
323.15 |
787.5 |
0.3000 |
268.10 |
852.2 |
0.3000 |
273.10 |
847.7 |
0.3000 |
278.10 |
842.9 |
0.3000 |
283.10 |
838.5 |
0.3000 |
288.15 |
833.9 |
0.3000 |
293.15 |
829.4 |
0.3000 |
298.15 |
825.1 |
0.3000 |
303.15 |
820.6 |
0.3000 |
308.15 |
816.0 |
0.3000 |
313.15 |
811.1 |
0.3000 |
318.15 |
806.6 |
0.3000 |
323.15 |
801.9 |
0.4000 |
268.10 |
867.7 |
0.4000 |
273.10 |
863.4 |
0.4000 |
278.10 |
858.8 |
0.4000 |
283.10 |
854.1 |
0.4000 |
288.15 |
849.5 |
0.4000 |
293.15 |
845.0 |
0.4000 |
298.15 |
840.6 |
0.4000 |
303.15 |
836.1 |
0.4000 |
308.15 |
831.4 |
0.4000 |
313.15 |
826.9 |
0.4000 |
318.15 |
822.4 |
0.4000 |
323.15 |
817.7 |
0.5000 |
268.10 |
886.6 |
0.5000 |
273.10 |
882.1 |
0.5000 |
278.10 |
877.7 |
0.5000 |
283.10 |
872.8 |
0.5000 |
288.15 |
868.5 |
0.5000 |
293.15 |
863.8 |
0.5000 |
298.15 |
859.2 |
0.5000 |
303.15 |
854.8 |
0.5000 |
308.15 |
850.1 |
0.5000 |
313.15 |
845.2 |
0.5000 |
318.15 |
840.5 |
0.5000 |
323.15 |
835.8 |
0.6000 |
268.10 |
908.1 |
0.6000 |
273.10 |
903.5 |
0.6000 |
278.10 |
899.3 |
0.6000 |
283.10 |
894.6 |
0.6000 |
288.15 |
889.6 |
0.6000 |
293.15 |
885.1 |
0.6000 |
298.15 |
880.6 |
0.6000 |
303.15 |
876.1 |
0.6000 |
308.15 |
871.4 |
0.6000 |
313.15 |
866.8 |
0.6000 |
318.15 |
862.1 |
0.6000 |
323.15 |
857.3 |
0.7000 |
268.10 |
931.6 |
0.7000 |
273.10 |
927.1 |
0.7000 |
278.10 |
922.7 |
0.7000 |
283.10 |
918.7 |
0.7000 |
288.15 |
914.5 |
0.7000 |
293.15 |
909.9 |
0.7000 |
298.15 |
905.3 |
0.7000 |
303.15 |
901.0 |
0.7000 |
308.15 |
896.5 |
0.7000 |
313.15 |
892.0 |
0.7000 |
318.15 |
887.4 |
0.7000 |
323.15 |
883.0 |
0.8000 |
268.10 |
951.0 |
0.8000 |
273.10 |
948.0 |
0.8000 |
278.10 |
945.0 |
0.8000 |
283.10 |
941.4 |
0.8000 |
288.15 |
938.0 |
0.8000 |
293.15 |
934.6 |
0.8000 |
298.15 |
931.3 |
0.8000 |
303.15 |
927.6 |
0.8000 |
308.15 |
923.8 |
0.8000 |
313.15 |
919.5 |
0.8000 |
318.15 |
915.5 |
0.8000 |
323.15 |
911.2 |
0.9000 |
268.10 |
977.3 |
0.9000 |
273.10 |
975.6 |
0.9000 |
278.10 |
973.2 |
0.9000 |
283.10 |
970.8 |
0.9000 |
288.15 |
967.3 |
0.9000 |
293.15 |
963.7 |
0.9000 |
298.15 |
960.3 |
0.9000 |
303.15 |
956.2 |
0.9000 |
308.15 |
952.7 |
0.9000 |
313.15 |
949.0 |
0.9000 |
318.15 |
945.5 |
0.9000 |
323.15 |
942.0 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mass fraction of Water (2) - Liquid |
Mass density, kg/m3 - Liquid |
303.15 |
0.1500 |
822.7 |
303.15 |
0.2000 |
836.0 |
303.15 |
0.2500 |
848.8 |
308.15 |
0.1500 |
818.4 |
308.15 |
0.2000 |
831.8 |
308.15 |
0.2500 |
843.0 |
313.15 |
0.1500 |
813.1 |
313.15 |
0.2000 |
827.1 |
313.15 |
0.2500 |
838.2 |
318.15 |
0.1500 |
807.1 |
318.15 |
0.2000 |
821.0 |
318.15 |
0.2500 |
833.6 |
323.15 |
0.1500 |
801.4 |
323.15 |
0.2000 |
814.6 |
323.15 |
0.2500 |
827.5 |
328.15 |
0.1500 |
796.9 |
328.15 |
0.2000 |
809.1 |
328.15 |
0.2500 |
822.5 |
Mass density, kg/m3
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Volume fraction = 0.5 (Liquid)
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
288.15 |
930.86 |
293.15 |
927.08 |
298.15 |
923.22 |
303.15 |
919.31 |
308.15 |
915.32 |
313.15 |
911.27 |
318.15 |
908.03 |
318.15 |
907.3 |
323.15 |
904.32 |
323.15 |
903.71 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mass fraction of Ethanol (1) - Liquid |
Mass density, kg/m3 - Liquid |
293.15 |
0.1000 |
981.8 |
293.15 |
0.2000 |
968.2 |
293.15 |
0.3000 |
953.6 |
293.15 |
0.4000 |
935.5 |
293.15 |
0.5000 |
913.9 |
303.15 |
0.1000 |
979.0 |
303.15 |
0.2000 |
964.1 |
303.15 |
0.3000 |
947.4 |
303.15 |
0.4000 |
927.2 |
303.15 |
0.5000 |
905.6 |
313.15 |
0.1000 |
974.6 |
313.15 |
0.2000 |
958.7 |
313.15 |
0.3000 |
940.3 |
313.15 |
0.4000 |
919.8 |
313.15 |
0.5000 |
897.6 |
Speed of sound, m/s
[ref]
Operational conditions:
- Pressure, kPa = 84.5 (Liquid)
- Frequency, MHz = 3 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Molality, mol/kg of Ethanol (1) - Liquid |
Speed of sound, m/s - Liquid |
288.15 |
0.0216 |
1467.43 |
288.15 |
0.0435 |
1468.25 |
288.15 |
0.0649 |
1469.09 |
288.15 |
0.0865 |
1470.02 |
288.15 |
0.1087 |
1470.85 |
288.15 |
0.1306 |
1471.71 |
288.15 |
0.1749 |
1473.44 |
288.15 |
0.2188 |
1475.05 |
293.15 |
0.0216 |
1483.38 |
293.15 |
0.0435 |
1484.2 |
293.15 |
0.0649 |
1484.95 |
293.15 |
0.0865 |
1485.8 |
293.15 |
0.1087 |
1486.55 |
293.15 |
0.1306 |
1487.33 |
293.15 |
0.1749 |
1488.87 |
293.15 |
0.2188 |
1490.38 |
298.15 |
0.0216 |
1497.5 |
298.15 |
0.0435 |
1498.25 |
298.15 |
0.0649 |
1498.93 |
298.15 |
0.0865 |
1499.71 |
298.15 |
0.1087 |
1500.38 |
298.15 |
0.1306 |
1501.09 |
298.15 |
0.1749 |
1502.46 |
298.15 |
0.2188 |
1503.85 |
303.15 |
0.0216 |
1509.79 |
303.15 |
0.0435 |
1510.47 |
303.15 |
0.0649 |
1511.1 |
303.15 |
0.0865 |
1511.74 |
303.15 |
0.1087 |
1512.38 |
303.15 |
0.1306 |
1513.01 |
303.15 |
0.1749 |
1514.25 |
303.15 |
0.2188 |
1515.48 |
308.15 |
0.0216 |
1520.37 |
308.15 |
0.0435 |
1521.01 |
308.15 |
0.0649 |
1521.58 |
308.15 |
0.0865 |
1522.16 |
308.15 |
0.1087 |
1522.75 |
308.15 |
0.1306 |
1523.3 |
308.15 |
0.1749 |
1524.38 |
308.15 |
0.2188 |
1525.49 |
Speed of sound, m/s
[ref]
Operational conditions:
- Pressure, kPa = 92.3 (Liquid)
- Frequency, MHz = 3 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol (1) - Liquid |
Speed of sound, m/s - Liquid |
293.15 |
0.0024 |
1487.73 |
293.15 |
0.0202 |
1522.47 |
293.15 |
0.0295 |
1539.98 |
293.15 |
0.0366 |
1552.98 |
293.15 |
0.0513 |
1578.0 |
293.15 |
0.0600 |
1590.75 |
293.15 |
0.0707 |
1604.25 |
293.15 |
0.0801 |
1613.76 |
293.15 |
0.0904 |
1621.49 |
293.15 |
0.0997 |
1625.74 |
293.15 |
0.1294 |
1623.76 |
293.15 |
0.1497 |
1611.87 |
293.15 |
0.2008 |
1566.56 |
293.15 |
0.2503 |
1520.22 |
293.15 |
0.2998 |
1478.23 |
293.15 |
0.3507 |
1440.37 |
293.15 |
0.3992 |
1408.88 |
293.15 |
0.4514 |
1379.03 |
293.15 |
0.5002 |
1353.45 |
293.15 |
0.5494 |
1330.43 |
293.15 |
0.6018 |
1307.82 |
293.15 |
0.6503 |
1288.48 |
293.15 |
0.7006 |
1269.09 |
293.15 |
0.7355 |
1255.96 |
293.15 |
0.7965 |
1234.14 |
293.15 |
0.8433 |
1217.42 |
293.15 |
0.8920 |
1199.65 |
293.15 |
0.9093 |
1193.54 |
293.15 |
0.9207 |
1189.49 |
293.15 |
0.9307 |
1185.76 |
293.15 |
0.9398 |
1182.61 |
293.15 |
0.9483 |
1179.44 |
293.15 |
0.9603 |
1175.34 |
293.15 |
0.9702 |
1171.74 |
293.15 |
0.9801 |
1168.51 |
293.15 |
0.9895 |
1165.01 |
298.15 |
0.0024 |
1501.46 |
298.15 |
0.0202 |
1532.68 |
298.15 |
0.0295 |
1548.2 |
298.15 |
0.0366 |
1559.61 |
298.15 |
0.0513 |
1581.28 |
298.15 |
0.0600 |
1592.07 |
298.15 |
0.0707 |
1603.21 |
298.15 |
0.0801 |
1610.7 |
298.15 |
0.0904 |
1616.37 |
298.15 |
0.0997 |
1618.97 |
298.15 |
0.1294 |
1613.29 |
298.15 |
0.1497 |
1600.11 |
298.15 |
0.2008 |
1553.74 |
298.15 |
0.2503 |
1506.97 |
298.15 |
0.2998 |
1464.53 |
298.15 |
0.3507 |
1426.17 |
298.15 |
0.3992 |
1394.22 |
298.15 |
0.4514 |
1363.91 |
298.15 |
0.5002 |
1337.91 |
298.15 |
0.5494 |
1314.51 |
298.15 |
0.6018 |
1291.54 |
298.15 |
0.6503 |
1271.85 |
298.15 |
0.7006 |
1252.3 |
298.15 |
0.7355 |
1239.1 |
298.15 |
0.7965 |
1217.02 |
298.15 |
0.8433 |
1200.22 |
298.15 |
0.8920 |
1182.48 |
298.15 |
0.9093 |
1176.33 |
298.15 |
0.9207 |
1172.28 |
298.15 |
0.9307 |
1168.56 |
298.15 |
0.9398 |
1165.41 |
298.15 |
0.9483 |
1162.31 |
298.15 |
0.9603 |
1158.13 |
298.15 |
0.9702 |
1154.53 |
298.15 |
0.9801 |
1151.32 |
298.15 |
0.9895 |
1147.81 |
303.15 |
0.0024 |
1513.38 |
303.15 |
0.0202 |
1541.27 |
303.15 |
0.0295 |
1554.96 |
303.15 |
0.0366 |
1564.94 |
303.15 |
0.0513 |
1583.45 |
303.15 |
0.0600 |
1592.43 |
303.15 |
0.0707 |
1601.37 |
303.15 |
0.0801 |
1607.01 |
303.15 |
0.0904 |
1610.77 |
303.15 |
0.0997 |
1611.87 |
303.15 |
0.1294 |
1602.74 |
303.15 |
0.1497 |
1588.34 |
303.15 |
0.2008 |
1540.81 |
303.15 |
0.2503 |
1493.53 |
303.15 |
0.2998 |
1450.63 |
303.15 |
0.3507 |
1411.8 |
303.15 |
0.3992 |
1379.42 |
303.15 |
0.4514 |
1348.69 |
303.15 |
0.5002 |
1322.3 |
303.15 |
0.5494 |
1298.56 |
303.15 |
0.6018 |
1275.24 |
303.15 |
0.6503 |
1255.29 |
303.15 |
0.7006 |
1235.5 |
303.15 |
0.7355 |
1222.17 |
303.15 |
0.7965 |
1199.89 |
303.15 |
0.8433 |
1183.11 |
303.15 |
0.8920 |
1165.38 |
303.15 |
0.9093 |
1159.25 |
303.15 |
0.9207 |
1155.19 |
303.15 |
0.9307 |
1151.48 |
303.15 |
0.9398 |
1148.33 |
303.15 |
0.9483 |
1145.24 |
303.15 |
0.9603 |
1141.09 |
303.15 |
0.9702 |
1137.48 |
303.15 |
0.9801 |
1134.29 |
303.15 |
0.9895 |
1130.78 |
308.15 |
0.0024 |
1523.29 |
308.15 |
0.0202 |
1548.34 |
308.15 |
0.0295 |
1560.33 |
308.15 |
0.0366 |
1568.92 |
308.15 |
0.0513 |
1584.52 |
308.15 |
0.0600 |
1591.83 |
308.15 |
0.0707 |
1598.74 |
308.15 |
0.0801 |
1602.67 |
308.15 |
0.0904 |
1604.68 |
308.15 |
0.0997 |
1604.39 |
308.15 |
0.1294 |
1592.26 |
308.15 |
0.1497 |
1576.55 |
308.15 |
0.2008 |
1527.79 |
308.15 |
0.2503 |
1479.96 |
308.15 |
0.2998 |
1436.64 |
308.15 |
0.3507 |
1397.33 |
308.15 |
0.3992 |
1364.56 |
308.15 |
0.4514 |
1333.43 |
308.15 |
0.5002 |
1306.71 |
308.15 |
0.5494 |
1282.65 |
308.15 |
0.6018 |
1259.01 |
308.15 |
0.6503 |
1238.82 |
308.15 |
0.7006 |
1218.82 |
308.15 |
0.7355 |
1206.33 |
308.15 |
0.7965 |
1183.04 |
308.15 |
0.8433 |
1166.12 |
308.15 |
0.8920 |
1148.65 |
308.15 |
0.9093 |
1142.56 |
308.15 |
0.9207 |
1138.28 |
308.15 |
0.9307 |
1134.56 |
308.15 |
0.9398 |
1131.43 |
308.15 |
0.9483 |
1128.37 |
308.15 |
0.9603 |
1124.21 |
308.15 |
0.9702 |
1120.63 |
308.15 |
0.9801 |
1117.45 |
308.15 |
0.9895 |
1113.96 |
293.15 |
0.0000 |
1482.78 |
298.15 |
0.0000 |
1496.99 |
303.15 |
0.0000 |
1509.32 |
308.15 |
0.0000 |
1519.89 |
293.15 |
1.0000 |
1160.65 |
298.15 |
1.0000 |
1143.5 |
303.15 |
1.0000 |
1126.44 |
308.15 |
1.0000 |
1109.59 |
Speed of sound, m/s
[ref]
Operational conditions:
- Pressure, kPa = 100 (Liquid)
- Temperature, K = 308.15 (Liquid)
Mass ratio of solute to solvent of Ethanol (1) - Liquid |
Speed of sound, m/s - Liquid |
0.0500 |
1542.9 |
0.1000 |
1559.2 |
0.1500 |
1590.4 |
Speed of sound, m/s
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
Molality, mol/kg of Water (2) - Liquid |
Speed of sound, m/s - Liquid |
0.0000 |
1142.1 |
0.2140 |
1144.6 |
0.2705 |
1145.9 |
0.3199 |
1146.8 |
0.3659 |
1148.6 |
0.4543 |
1151.0 |
0.5541 |
1153.2 |
0.6437 |
1154.8 |
0.7430 |
1156.4 |
0.8349 |
1157.7 |
0.9264 |
1159.5 |
1.0189 |
1160.1 |
Speed of sound, m/s
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Volume fraction = 0.5 (Liquid)
Temperature, K - Liquid |
Speed of sound, m/s - Liquid |
288.15 |
1546.7 |
293.15 |
1534.1 |
298.15 |
1521.1 |
303.15 |
1507.9 |
308.15 |
1494.5 |
313.15 |
1480.9 |
318.15 |
1467.0 |
323.15 |
1452.9 |
Speed of sound, m/s
[ref]
Operational conditions:
- Pressure, kPa = 84.5 (Liquid)
- Frequency, MHz = 3 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Molality, mol/kg of Ethanol (1) - Liquid |
Speed of sound, m/s - Liquid |
288.15 |
0.0216 |
1467.43 |
288.15 |
0.0435 |
1468.25 |
288.15 |
0.0649 |
1469.09 |
288.15 |
0.0865 |
1470.02 |
288.15 |
0.1087 |
1470.85 |
288.15 |
0.1306 |
1471.71 |
288.15 |
0.1749 |
1473.44 |
288.15 |
0.2188 |
1475.05 |
293.15 |
0.0216 |
1483.38 |
293.15 |
0.0435 |
1484.2 |
293.15 |
0.0649 |
1484.95 |
293.15 |
0.0865 |
1485.8 |
293.15 |
0.1087 |
1486.55 |
293.15 |
0.1306 |
1487.33 |
293.15 |
0.1749 |
1488.87 |
293.15 |
0.2188 |
1490.38 |
298.15 |
0.0216 |
1497.5 |
298.15 |
0.0435 |
1498.25 |
298.15 |
0.0649 |
1498.93 |
298.15 |
0.0865 |
1499.71 |
298.15 |
0.1087 |
1500.38 |
298.15 |
0.1306 |
1501.09 |
298.15 |
0.1749 |
1502.46 |
298.15 |
0.2188 |
1503.85 |
303.15 |
0.0216 |
1509.79 |
303.15 |
0.0435 |
1510.47 |
303.15 |
0.0649 |
1511.1 |
303.15 |
0.0865 |
1511.74 |
303.15 |
0.1087 |
1512.38 |
303.15 |
0.1306 |
1513.01 |
303.15 |
0.1749 |
1514.25 |
303.15 |
0.2188 |
1515.48 |
308.15 |
0.0216 |
1520.37 |
308.15 |
0.0435 |
1521.01 |
308.15 |
0.0649 |
1521.58 |
308.15 |
0.0865 |
1522.16 |
308.15 |
0.1087 |
1522.75 |
308.15 |
0.1306 |
1523.3 |
308.15 |
0.1749 |
1524.38 |
308.15 |
0.2188 |
1525.49 |
Speed of sound, m/s
[ref]
Operational conditions:
- Pressure, kPa = 92.3 (Liquid)
- Frequency, MHz = 3 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol (1) - Liquid |
Speed of sound, m/s - Liquid |
293.15 |
0.0024 |
1487.73 |
293.15 |
0.0202 |
1522.47 |
293.15 |
0.0295 |
1539.98 |
293.15 |
0.0366 |
1552.98 |
293.15 |
0.0513 |
1578.0 |
293.15 |
0.0600 |
1590.75 |
293.15 |
0.0707 |
1604.25 |
293.15 |
0.0801 |
1613.76 |
293.15 |
0.0904 |
1621.49 |
293.15 |
0.0997 |
1625.74 |
293.15 |
0.1294 |
1623.76 |
293.15 |
0.1497 |
1611.87 |
293.15 |
0.2008 |
1566.56 |
293.15 |
0.2503 |
1520.22 |
293.15 |
0.2998 |
1478.23 |
293.15 |
0.3507 |
1440.37 |
293.15 |
0.3992 |
1408.88 |
293.15 |
0.4514 |
1379.03 |
293.15 |
0.5002 |
1353.45 |
293.15 |
0.5494 |
1330.43 |
293.15 |
0.6018 |
1307.82 |
293.15 |
0.6503 |
1288.48 |
293.15 |
0.7006 |
1269.09 |
293.15 |
0.7355 |
1255.96 |
293.15 |
0.7965 |
1234.14 |
293.15 |
0.8433 |
1217.42 |
293.15 |
0.8920 |
1199.65 |
293.15 |
0.9093 |
1193.54 |
293.15 |
0.9207 |
1189.49 |
293.15 |
0.9307 |
1185.76 |
293.15 |
0.9398 |
1182.61 |
293.15 |
0.9483 |
1179.44 |
293.15 |
0.9603 |
1175.34 |
293.15 |
0.9702 |
1171.74 |
293.15 |
0.9801 |
1168.51 |
293.15 |
0.9895 |
1165.01 |
298.15 |
0.0024 |
1501.46 |
298.15 |
0.0202 |
1532.68 |
298.15 |
0.0295 |
1548.2 |
298.15 |
0.0366 |
1559.61 |
298.15 |
0.0513 |
1581.28 |
298.15 |
0.0600 |
1592.07 |
298.15 |
0.0707 |
1603.21 |
298.15 |
0.0801 |
1610.7 |
298.15 |
0.0904 |
1616.37 |
298.15 |
0.0997 |
1618.97 |
298.15 |
0.1294 |
1613.29 |
298.15 |
0.1497 |
1600.11 |
298.15 |
0.2008 |
1553.74 |
298.15 |
0.2503 |
1506.97 |
298.15 |
0.2998 |
1464.53 |
298.15 |
0.3507 |
1426.17 |
298.15 |
0.3992 |
1394.22 |
298.15 |
0.4514 |
1363.91 |
298.15 |
0.5002 |
1337.91 |
298.15 |
0.5494 |
1314.51 |
298.15 |
0.6018 |
1291.54 |
298.15 |
0.6503 |
1271.85 |
298.15 |
0.7006 |
1252.3 |
298.15 |
0.7355 |
1239.1 |
298.15 |
0.7965 |
1217.02 |
298.15 |
0.8433 |
1200.22 |
298.15 |
0.8920 |
1182.48 |
298.15 |
0.9093 |
1176.33 |
298.15 |
0.9207 |
1172.28 |
298.15 |
0.9307 |
1168.56 |
298.15 |
0.9398 |
1165.41 |
298.15 |
0.9483 |
1162.31 |
298.15 |
0.9603 |
1158.13 |
298.15 |
0.9702 |
1154.53 |
298.15 |
0.9801 |
1151.32 |
298.15 |
0.9895 |
1147.81 |
303.15 |
0.0024 |
1513.38 |
303.15 |
0.0202 |
1541.27 |
303.15 |
0.0295 |
1554.96 |
303.15 |
0.0366 |
1564.94 |
303.15 |
0.0513 |
1583.45 |
303.15 |
0.0600 |
1592.43 |
303.15 |
0.0707 |
1601.37 |
303.15 |
0.0801 |
1607.01 |
303.15 |
0.0904 |
1610.77 |
303.15 |
0.0997 |
1611.87 |
303.15 |
0.1294 |
1602.74 |
303.15 |
0.1497 |
1588.34 |
303.15 |
0.2008 |
1540.81 |
303.15 |
0.2503 |
1493.53 |
303.15 |
0.2998 |
1450.63 |
303.15 |
0.3507 |
1411.8 |
303.15 |
0.3992 |
1379.42 |
303.15 |
0.4514 |
1348.69 |
303.15 |
0.5002 |
1322.3 |
303.15 |
0.5494 |
1298.56 |
303.15 |
0.6018 |
1275.24 |
303.15 |
0.6503 |
1255.29 |
303.15 |
0.7006 |
1235.5 |
303.15 |
0.7355 |
1222.17 |
303.15 |
0.7965 |
1199.89 |
303.15 |
0.8433 |
1183.11 |
303.15 |
0.8920 |
1165.38 |
303.15 |
0.9093 |
1159.25 |
303.15 |
0.9207 |
1155.19 |
303.15 |
0.9307 |
1151.48 |
303.15 |
0.9398 |
1148.33 |
303.15 |
0.9483 |
1145.24 |
303.15 |
0.9603 |
1141.09 |
303.15 |
0.9702 |
1137.48 |
303.15 |
0.9801 |
1134.29 |
303.15 |
0.9895 |
1130.78 |
308.15 |
0.0024 |
1523.29 |
308.15 |
0.0202 |
1548.34 |
308.15 |
0.0295 |
1560.33 |
308.15 |
0.0366 |
1568.92 |
308.15 |
0.0513 |
1584.52 |
308.15 |
0.0600 |
1591.83 |
308.15 |
0.0707 |
1598.74 |
308.15 |
0.0801 |
1602.67 |
308.15 |
0.0904 |
1604.68 |
308.15 |
0.0997 |
1604.39 |
308.15 |
0.1294 |
1592.26 |
308.15 |
0.1497 |
1576.55 |
308.15 |
0.2008 |
1527.79 |
308.15 |
0.2503 |
1479.96 |
308.15 |
0.2998 |
1436.64 |
308.15 |
0.3507 |
1397.33 |
308.15 |
0.3992 |
1364.56 |
308.15 |
0.4514 |
1333.43 |
308.15 |
0.5002 |
1306.71 |
308.15 |
0.5494 |
1282.65 |
308.15 |
0.6018 |
1259.01 |
308.15 |
0.6503 |
1238.82 |
308.15 |
0.7006 |
1218.82 |
308.15 |
0.7355 |
1206.33 |
308.15 |
0.7965 |
1183.04 |
308.15 |
0.8433 |
1166.12 |
308.15 |
0.8920 |
1148.65 |
308.15 |
0.9093 |
1142.56 |
308.15 |
0.9207 |
1138.28 |
308.15 |
0.9307 |
1134.56 |
308.15 |
0.9398 |
1131.43 |
308.15 |
0.9483 |
1128.37 |
308.15 |
0.9603 |
1124.21 |
308.15 |
0.9702 |
1120.63 |
308.15 |
0.9801 |
1117.45 |
308.15 |
0.9895 |
1113.96 |
293.15 |
0.0000 |
1482.78 |
298.15 |
0.0000 |
1496.99 |
303.15 |
0.0000 |
1509.32 |
308.15 |
0.0000 |
1519.89 |
293.15 |
1.0000 |
1160.65 |
298.15 |
1.0000 |
1143.5 |
303.15 |
1.0000 |
1126.44 |
308.15 |
1.0000 |
1109.59 |
Speed of sound, m/s
[ref]
Operational conditions:
- Pressure, kPa = 100 (Liquid)
- Temperature, K = 308.15 (Liquid)
Mass ratio of solute to solvent of Ethanol (1) - Liquid |
Speed of sound, m/s - Liquid |
0.0500 |
1542.9 |
0.1000 |
1559.2 |
0.1500 |
1590.4 |
Speed of sound, m/s
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
Molality, mol/kg of Water (2) - Liquid |
Speed of sound, m/s - Liquid |
0.0000 |
1142.1 |
0.2140 |
1144.6 |
0.2705 |
1145.9 |
0.3199 |
1146.8 |
0.3659 |
1148.6 |
0.4543 |
1151.0 |
0.5541 |
1153.2 |
0.6437 |
1154.8 |
0.7430 |
1156.4 |
0.8349 |
1157.7 |
0.9264 |
1159.5 |
1.0189 |
1160.1 |
Speed of sound, m/s
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Volume fraction = 0.5 (Liquid)
Temperature, K - Liquid |
Speed of sound, m/s - Liquid |
288.15 |
1546.7 |
293.15 |
1534.1 |
298.15 |
1521.1 |
303.15 |
1507.9 |
308.15 |
1494.5 |
313.15 |
1480.9 |
318.15 |
1467.0 |
323.15 |
1452.9 |
Surface tension liquid-gas, N/m
[ref]
Operational conditions:
- Mass fraction = 0.1 (Liquid)
- Temperature, K = 293.15 (Liquid)
Surface tension liquid-gas, N/m - Liquid |
0.0425 |
0.0443 |
Surface tension liquid-gas, N/m
[ref]
Operational condition: Temperature, K =
298.2 (Liquid)
Mass fraction of Water (2) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
0.5080 |
0.0282 |
0.4260 |
0.0267 |
0.3110 |
0.0256 |
0.2470 |
0.0253 |
0.2350 |
0.0251 |
0.2060 |
0.0248 |
Surface tension liquid-gas, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mass fraction of Ethanol (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
298.00 |
0.0000 |
0.0720 |
298.00 |
0.0500 |
0.0551 |
298.00 |
0.1000 |
0.0473 |
298.00 |
0.1500 |
0.0420 |
298.00 |
0.2000 |
0.0382 |
313.00 |
0.0000 |
0.0699 |
313.00 |
0.0500 |
0.0531 |
313.00 |
0.1000 |
0.0459 |
313.00 |
0.1500 |
0.0404 |
313.00 |
0.2000 |
0.0367 |
Surface tension liquid-gas, N/m
[ref]
Operational conditions:
- Mass fraction = 0.1 (Liquid)
- Temperature, K = 293.15 (Liquid)
Surface tension liquid-gas, N/m - Liquid |
0.0425 |
0.0443 |
Surface tension liquid-gas, N/m
[ref]
Operational condition: Temperature, K =
298.2 (Liquid)
Mass fraction of Water (2) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
0.5080 |
0.0282 |
0.4260 |
0.0267 |
0.3110 |
0.0256 |
0.2470 |
0.0253 |
0.2350 |
0.0251 |
0.2060 |
0.0248 |
Surface tension liquid-gas, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mass fraction of Ethanol (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
298.00 |
0.0000 |
0.0720 |
298.00 |
0.0500 |
0.0551 |
298.00 |
0.1000 |
0.0473 |
298.00 |
0.1500 |
0.0420 |
298.00 |
0.2000 |
0.0382 |
313.00 |
0.0000 |
0.0699 |
313.00 |
0.0500 |
0.0531 |
313.00 |
0.1000 |
0.0459 |
313.00 |
0.1500 |
0.0404 |
313.00 |
0.2000 |
0.0367 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
77.3 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.2810 |
348.85 |
0.3560 |
347.75 |
0.4740 |
346.55 |
0.6200 |
345.85 |
0.7630 |
344.95 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
77.3 (Gas)
Mole fraction of Ethanol (1) - Gas |
Boiling temperature at pressure P, K - Liquid |
0.5410 |
348.85 |
0.5790 |
347.75 |
0.6290 |
346.55 |
0.7050 |
345.85 |
0.7980 |
344.95 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.325 (Gas)
Mole fraction of Ethanol (1) - Gas |
Boiling temperature at pressure P, K - Gas |
0.0047 |
373.15 |
0.0721 |
371.75 |
0.1539 |
369.65 |
0.2301 |
367.35 |
0.2851 |
365.65 |
0.3559 |
363.45 |
0.4181 |
361.45 |
0.4534 |
359.55 |
0.5314 |
357.55 |
0.6047 |
354.65 |
0.6518 |
353.35 |
0.6751 |
352.65 |
0.7451 |
351.75 |
0.8005 |
351.55 |
0.8457 |
351.35 |
0.9010 |
351.45 |
0.9721 |
351.55 |
0.9774 |
351.65 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0010 |
373.15 |
0.0061 |
371.75 |
0.0145 |
369.65 |
0.0237 |
367.35 |
0.0310 |
365.65 |
0.0490 |
363.45 |
0.0652 |
361.45 |
0.0968 |
359.55 |
0.1394 |
357.55 |
0.3261 |
354.65 |
0.4635 |
353.35 |
0.5413 |
352.65 |
0.6856 |
351.75 |
0.7760 |
351.55 |
0.8403 |
351.35 |
0.9037 |
351.45 |
0.9725 |
351.55 |
0.9804 |
351.65 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of Ethanol (1) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0630 |
32.86 |
335.16 |
0.0760 |
19.71 |
323.53 |
0.1040 |
32.86 |
332.54 |
0.1170 |
13.15 |
313.71 |
0.1410 |
19.71 |
320.52 |
0.1500 |
32.86 |
330.96 |
0.2410 |
13.15 |
310.70 |
0.2480 |
32.86 |
329.26 |
0.2600 |
19.71 |
318.05 |
0.3830 |
13.15 |
309.53 |
0.3900 |
19.71 |
317.04 |
0.4540 |
32.86 |
326.77 |
0.4920 |
13.15 |
308.82 |
0.4990 |
19.71 |
316.35 |
0.5810 |
32.86 |
326.10 |
0.5900 |
13.15 |
308.36 |
0.5990 |
19.71 |
315.90 |
0.6560 |
13.15 |
308.10 |
0.6570 |
32.86 |
325.89 |
0.6880 |
19.71 |
315.55 |
0.7600 |
32.86 |
325.67 |
0.7710 |
13.15 |
307.70 |
0.7990 |
19.71 |
315.29 |
0.8050 |
19.71 |
315.26 |
0.8390 |
32.86 |
325.53 |
0.8400 |
13.15 |
307.54 |
0.8410 |
19.71 |
315.19 |
0.8540 |
32.86 |
325.51 |
0.8640 |
13.15 |
307.56 |
0.8830 |
19.71 |
315.15 |
0.8970 |
13.15 |
307.51 |
0.9080 |
13.15 |
307.46 |
0.9110 |
13.15 |
307.50 |
0.9130 |
19.71 |
315.16 |
0.9130 |
32.86 |
325.46 |
0.9310 |
19.71 |
315.13 |
0.9310 |
32.86 |
325.43 |
0.9320 |
32.86 |
325.42 |
0.9340 |
13.15 |
307.48 |
0.9450 |
19.71 |
315.13 |
0.9470 |
13.15 |
307.45 |
0.9600 |
19.71 |
315.14 |
0.9640 |
19.71 |
315.14 |
0.9650 |
32.86 |
325.45 |
0.9710 |
13.15 |
307.44 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.6830 |
351.85 |
0.7380 |
351.71 |
0.7820 |
351.56 |
0.8370 |
351.49 |
0.8810 |
351.42 |
0.9430 |
351.45 |
0.9600 |
351.47 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.32 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
373.15 |
0.0180 |
368.38 |
0.0280 |
367.05 |
0.0510 |
363.90 |
0.0810 |
360.69 |
0.1250 |
358.51 |
0.1690 |
357.03 |
0.2280 |
355.92 |
0.3350 |
354.25 |
0.4740 |
353.07 |
0.5560 |
352.51 |
0.6640 |
351.87 |
0.7560 |
351.48 |
0.8930 |
351.31 |
0.9220 |
351.40 |
0.9610 |
351.41 |
1.0000 |
351.45 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
91.4 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
1.0000 |
349.60 |
0.8530 |
349.10 |
0.7380 |
349.50 |
0.6100 |
349.90 |
0.5960 |
349.50 |
0.4980 |
350.40 |
0.3580 |
351.40 |
0.2830 |
351.80 |
0.2560 |
352.50 |
0.2330 |
353.10 |
0.2100 |
353.30 |
0.1480 |
354.70 |
0.0950 |
356.70 |
0.0750 |
358.50 |
0.0520 |
360.80 |
0.0290 |
363.90 |
0.0000 |
370.00 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
373.15 |
0.0150 |
369.27 |
0.0350 |
365.61 |
0.1000 |
359.79 |
0.1830 |
356.66 |
0.2920 |
354.88 |
0.3940 |
353.89 |
0.5010 |
353.06 |
0.5430 |
352.73 |
0.6310 |
352.04 |
0.7490 |
351.67 |
0.7940 |
351.64 |
0.8480 |
351.40 |
0.8990 |
351.33 |
0.9490 |
351.37 |
1.0000 |
351.45 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of Ethanol (1) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
93.79 |
371.50 |
0.0043 |
94.19 |
369.86 |
0.0117 |
94.06 |
367.92 |
0.0131 |
93.79 |
366.90 |
0.0178 |
93.93 |
365.98 |
0.0261 |
93.93 |
364.65 |
0.0351 |
93.93 |
363.12 |
0.0727 |
93.79 |
358.32 |
0.1199 |
93.73 |
355.77 |
0.1708 |
93.73 |
354.54 |
0.2770 |
94.26 |
352.50 |
0.3791 |
93.99 |
351.88 |
0.4694 |
94.13 |
351.37 |
0.5521 |
93.66 |
350.86 |
0.6404 |
93.93 |
350.66 |
0.6639 |
93.99 |
350.45 |
0.7097 |
93.93 |
350.35 |
0.7586 |
93.59 |
350.15 |
0.7876 |
93.99 |
350.05 |
0.7982 |
93.66 |
350.05 |
0.8386 |
93.86 |
350.05 |
0.8814 |
93.73 |
349.94 |
0.9267 |
93.79 |
349.94 |
1.0000 |
93.33 |
349.94 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.9815 |
351.34 |
0.9026 |
351.35 |
0.7987 |
351.50 |
0.7314 |
351.65 |
0.6862 |
351.75 |
0.6193 |
352.03 |
0.5344 |
352.49 |
0.4157 |
353.43 |
0.2669 |
355.21 |
0.1920 |
356.62 |
0.1385 |
358.00 |
0.0850 |
360.63 |
0.0453 |
365.88 |
0.0246 |
369.83 |
0.0148 |
372.52 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of Water (2) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.2000 |
20.00 |
315.45 |
0.2000 |
40.00 |
329.67 |
0.2000 |
60.00 |
338.73 |
0.2000 |
80.00 |
345.64 |
0.2000 |
101.30 |
351.66 |
0.4000 |
20.00 |
316.10 |
0.4000 |
40.00 |
330.43 |
0.4000 |
60.00 |
339.64 |
0.4000 |
80.00 |
346.50 |
0.4000 |
101.30 |
352.57 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.32 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
373.15 |
0.0790 |
360.51 |
0.1430 |
357.49 |
0.1950 |
356.59 |
0.2920 |
354.79 |
0.3780 |
354.23 |
0.4500 |
353.44 |
0.4950 |
353.09 |
0.5810 |
352.32 |
0.6480 |
351.96 |
0.6960 |
351.77 |
0.7940 |
351.46 |
0.8400 |
351.40 |
0.8900 |
351.21 |
1.0000 |
351.55 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
50.66 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0082 |
352.35 |
0.0229 |
348.91 |
0.0298 |
349.77 |
0.0541 |
347.76 |
0.0621 |
345.73 |
0.1842 |
341.01 |
0.2529 |
337.97 |
0.2970 |
337.75 |
0.3594 |
337.42 |
0.3739 |
337.13 |
0.4730 |
336.15 |
0.5949 |
335.51 |
0.7017 |
334.94 |
0.8214 |
334.57 |
0.9313 |
334.28 |
0.9435 |
334.49 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0180 |
368.18 |
0.0790 |
360.50 |
0.0900 |
359.70 |
0.1470 |
357.27 |
0.2440 |
355.38 |
0.3110 |
354.55 |
0.3530 |
354.11 |
0.4250 |
353.45 |
0.4880 |
352.96 |
0.5700 |
352.39 |
0.6160 |
352.11 |
0.6700 |
351.82 |
0.7110 |
351.64 |
0.8020 |
351.37 |
0.8350 |
351.30 |
0.8690 |
351.27 |
0.9010 |
351.26 |
0.9140 |
351.26 |
0.9220 |
351.27 |
0.9400 |
351.29 |
0.9720 |
351.35 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
373.10 |
0.1190 |
359.20 |
0.1540 |
357.30 |
0.2180 |
355.80 |
0.2690 |
354.80 |
0.3220 |
354.50 |
0.3570 |
354.00 |
0.3930 |
353.50 |
0.4250 |
353.40 |
0.4400 |
353.20 |
0.5570 |
351.50 |
0.6500 |
351.40 |
0.7590 |
351.30 |
0.8650 |
351.20 |
1.0000 |
351.20 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of Water (2) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0697 |
30.00 |
323.46 |
0.0326 |
30.00 |
323.46 |
0.0697 |
60.00 |
338.62 |
0.0326 |
60.00 |
338.63 |
0.0697 |
90.00 |
348.46 |
0.0326 |
90.00 |
348.47 |
0.0697 |
101.30 |
351.41 |
0.0326 |
101.30 |
351.42 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Mole fraction of Ethanol (1) - Gas |
Boiling temperature at pressure P, K - Liquid |
0.8160 |
351.07 |
0.8552 |
350.99 |
0.8983 |
350.99 |
0.9175 |
350.96 |
0.9368 |
351.04 |
0.9563 |
351.07 |
0.9780 |
351.08 |
0.9894 |
351.11 |
0.9981 |
351.07 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
100 (Gas)
Mole fraction of Ethanol (1) - Liquid |
Boiling temperature at pressure P, K - Gas |
0.0000 |
372.81 |
0.0017 |
371.86 |
0.0054 |
370.68 |
0.0137 |
368.88 |
0.0215 |
366.61 |
0.0381 |
363.82 |
0.0668 |
360.95 |
0.1033 |
358.62 |
0.1516 |
356.92 |
0.2144 |
355.65 |
0.2660 |
354.89 |
0.3142 |
354.29 |
0.3544 |
353.83 |
0.4030 |
353.39 |
0.4488 |
353.03 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
77.3 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.2810 |
348.85 |
0.3560 |
347.75 |
0.4740 |
346.55 |
0.6200 |
345.85 |
0.7630 |
344.95 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
77.3 (Gas)
Mole fraction of Ethanol (1) - Gas |
Boiling temperature at pressure P, K - Liquid |
0.5410 |
348.85 |
0.5790 |
347.75 |
0.6290 |
346.55 |
0.7050 |
345.85 |
0.7980 |
344.95 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.325 (Gas)
Mole fraction of Ethanol (1) - Gas |
Boiling temperature at pressure P, K - Gas |
0.0047 |
373.15 |
0.0721 |
371.75 |
0.1539 |
369.65 |
0.2301 |
367.35 |
0.2851 |
365.65 |
0.3559 |
363.45 |
0.4181 |
361.45 |
0.4534 |
359.55 |
0.5314 |
357.55 |
0.6047 |
354.65 |
0.6518 |
353.35 |
0.6751 |
352.65 |
0.7451 |
351.75 |
0.8005 |
351.55 |
0.8457 |
351.35 |
0.9010 |
351.45 |
0.9721 |
351.55 |
0.9774 |
351.65 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0010 |
373.15 |
0.0061 |
371.75 |
0.0145 |
369.65 |
0.0237 |
367.35 |
0.0310 |
365.65 |
0.0490 |
363.45 |
0.0652 |
361.45 |
0.0968 |
359.55 |
0.1394 |
357.55 |
0.3261 |
354.65 |
0.4635 |
353.35 |
0.5413 |
352.65 |
0.6856 |
351.75 |
0.7760 |
351.55 |
0.8403 |
351.35 |
0.9037 |
351.45 |
0.9725 |
351.55 |
0.9804 |
351.65 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of Ethanol (1) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0630 |
32.86 |
335.16 |
0.0760 |
19.71 |
323.53 |
0.1040 |
32.86 |
332.54 |
0.1170 |
13.15 |
313.71 |
0.1410 |
19.71 |
320.52 |
0.1500 |
32.86 |
330.96 |
0.2410 |
13.15 |
310.70 |
0.2480 |
32.86 |
329.26 |
0.2600 |
19.71 |
318.05 |
0.3830 |
13.15 |
309.53 |
0.3900 |
19.71 |
317.04 |
0.4540 |
32.86 |
326.77 |
0.4920 |
13.15 |
308.82 |
0.4990 |
19.71 |
316.35 |
0.5810 |
32.86 |
326.10 |
0.5900 |
13.15 |
308.36 |
0.5990 |
19.71 |
315.90 |
0.6560 |
13.15 |
308.10 |
0.6570 |
32.86 |
325.89 |
0.6880 |
19.71 |
315.55 |
0.7600 |
32.86 |
325.67 |
0.7710 |
13.15 |
307.70 |
0.7990 |
19.71 |
315.29 |
0.8050 |
19.71 |
315.26 |
0.8390 |
32.86 |
325.53 |
0.8400 |
13.15 |
307.54 |
0.8410 |
19.71 |
315.19 |
0.8540 |
32.86 |
325.51 |
0.8640 |
13.15 |
307.56 |
0.8830 |
19.71 |
315.15 |
0.8970 |
13.15 |
307.51 |
0.9080 |
13.15 |
307.46 |
0.9110 |
13.15 |
307.50 |
0.9130 |
19.71 |
315.16 |
0.9130 |
32.86 |
325.46 |
0.9310 |
19.71 |
315.13 |
0.9310 |
32.86 |
325.43 |
0.9320 |
32.86 |
325.42 |
0.9340 |
13.15 |
307.48 |
0.9450 |
19.71 |
315.13 |
0.9470 |
13.15 |
307.45 |
0.9600 |
19.71 |
315.14 |
0.9640 |
19.71 |
315.14 |
0.9650 |
32.86 |
325.45 |
0.9710 |
13.15 |
307.44 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.6830 |
351.85 |
0.7380 |
351.71 |
0.7820 |
351.56 |
0.8370 |
351.49 |
0.8810 |
351.42 |
0.9430 |
351.45 |
0.9600 |
351.47 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.32 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
373.15 |
0.0180 |
368.38 |
0.0280 |
367.05 |
0.0510 |
363.90 |
0.0810 |
360.69 |
0.1250 |
358.51 |
0.1690 |
357.03 |
0.2280 |
355.92 |
0.3350 |
354.25 |
0.4740 |
353.07 |
0.5560 |
352.51 |
0.6640 |
351.87 |
0.7560 |
351.48 |
0.8930 |
351.31 |
0.9220 |
351.40 |
0.9610 |
351.41 |
1.0000 |
351.45 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
91.4 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
1.0000 |
349.60 |
0.8530 |
349.10 |
0.7380 |
349.50 |
0.6100 |
349.90 |
0.5960 |
349.50 |
0.4980 |
350.40 |
0.3580 |
351.40 |
0.2830 |
351.80 |
0.2560 |
352.50 |
0.2330 |
353.10 |
0.2100 |
353.30 |
0.1480 |
354.70 |
0.0950 |
356.70 |
0.0750 |
358.50 |
0.0520 |
360.80 |
0.0290 |
363.90 |
0.0000 |
370.00 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
373.15 |
0.0150 |
369.27 |
0.0350 |
365.61 |
0.1000 |
359.79 |
0.1830 |
356.66 |
0.2920 |
354.88 |
0.3940 |
353.89 |
0.5010 |
353.06 |
0.5430 |
352.73 |
0.6310 |
352.04 |
0.7490 |
351.67 |
0.7940 |
351.64 |
0.8480 |
351.40 |
0.8990 |
351.33 |
0.9490 |
351.37 |
1.0000 |
351.45 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of Ethanol (1) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
93.79 |
371.50 |
0.0043 |
94.19 |
369.86 |
0.0117 |
94.06 |
367.92 |
0.0131 |
93.79 |
366.90 |
0.0178 |
93.93 |
365.98 |
0.0261 |
93.93 |
364.65 |
0.0351 |
93.93 |
363.12 |
0.0727 |
93.79 |
358.32 |
0.1199 |
93.73 |
355.77 |
0.1708 |
93.73 |
354.54 |
0.2770 |
94.26 |
352.50 |
0.3791 |
93.99 |
351.88 |
0.4694 |
94.13 |
351.37 |
0.5521 |
93.66 |
350.86 |
0.6404 |
93.93 |
350.66 |
0.6639 |
93.99 |
350.45 |
0.7097 |
93.93 |
350.35 |
0.7586 |
93.59 |
350.15 |
0.7876 |
93.99 |
350.05 |
0.7982 |
93.66 |
350.05 |
0.8386 |
93.86 |
350.05 |
0.8814 |
93.73 |
349.94 |
0.9267 |
93.79 |
349.94 |
1.0000 |
93.33 |
349.94 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.9815 |
351.34 |
0.9026 |
351.35 |
0.7987 |
351.50 |
0.7314 |
351.65 |
0.6862 |
351.75 |
0.6193 |
352.03 |
0.5344 |
352.49 |
0.4157 |
353.43 |
0.2669 |
355.21 |
0.1920 |
356.62 |
0.1385 |
358.00 |
0.0850 |
360.63 |
0.0453 |
365.88 |
0.0246 |
369.83 |
0.0148 |
372.52 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of Water (2) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.2000 |
20.00 |
315.45 |
0.2000 |
40.00 |
329.67 |
0.2000 |
60.00 |
338.73 |
0.2000 |
80.00 |
345.64 |
0.2000 |
101.30 |
351.66 |
0.4000 |
20.00 |
316.10 |
0.4000 |
40.00 |
330.43 |
0.4000 |
60.00 |
339.64 |
0.4000 |
80.00 |
346.50 |
0.4000 |
101.30 |
352.57 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.32 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
373.15 |
0.0790 |
360.51 |
0.1430 |
357.49 |
0.1950 |
356.59 |
0.2920 |
354.79 |
0.3780 |
354.23 |
0.4500 |
353.44 |
0.4950 |
353.09 |
0.5810 |
352.32 |
0.6480 |
351.96 |
0.6960 |
351.77 |
0.7940 |
351.46 |
0.8400 |
351.40 |
0.8900 |
351.21 |
1.0000 |
351.55 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
50.66 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0082 |
352.35 |
0.0229 |
348.91 |
0.0298 |
349.77 |
0.0541 |
347.76 |
0.0621 |
345.73 |
0.1842 |
341.01 |
0.2529 |
337.97 |
0.2970 |
337.75 |
0.3594 |
337.42 |
0.3739 |
337.13 |
0.4730 |
336.15 |
0.5949 |
335.51 |
0.7017 |
334.94 |
0.8214 |
334.57 |
0.9313 |
334.28 |
0.9435 |
334.49 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0180 |
368.18 |
0.0790 |
360.50 |
0.0900 |
359.70 |
0.1470 |
357.27 |
0.2440 |
355.38 |
0.3110 |
354.55 |
0.3530 |
354.11 |
0.4250 |
353.45 |
0.4880 |
352.96 |
0.5700 |
352.39 |
0.6160 |
352.11 |
0.6700 |
351.82 |
0.7110 |
351.64 |
0.8020 |
351.37 |
0.8350 |
351.30 |
0.8690 |
351.27 |
0.9010 |
351.26 |
0.9140 |
351.26 |
0.9220 |
351.27 |
0.9400 |
351.29 |
0.9720 |
351.35 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
373.10 |
0.1190 |
359.20 |
0.1540 |
357.30 |
0.2180 |
355.80 |
0.2690 |
354.80 |
0.3220 |
354.50 |
0.3570 |
354.00 |
0.3930 |
353.50 |
0.4250 |
353.40 |
0.4400 |
353.20 |
0.5570 |
351.50 |
0.6500 |
351.40 |
0.7590 |
351.30 |
0.8650 |
351.20 |
1.0000 |
351.20 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of Water (2) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0697 |
30.00 |
323.46 |
0.0326 |
30.00 |
323.46 |
0.0697 |
60.00 |
338.62 |
0.0326 |
60.00 |
338.63 |
0.0697 |
90.00 |
348.46 |
0.0326 |
90.00 |
348.47 |
0.0697 |
101.30 |
351.41 |
0.0326 |
101.30 |
351.42 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Mole fraction of Ethanol (1) - Gas |
Boiling temperature at pressure P, K - Liquid |
0.8160 |
351.07 |
0.8552 |
350.99 |
0.8983 |
350.99 |
0.9175 |
350.96 |
0.9368 |
351.04 |
0.9563 |
351.07 |
0.9780 |
351.08 |
0.9894 |
351.11 |
0.9981 |
351.07 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
100 (Gas)
Mole fraction of Ethanol (1) - Liquid |
Boiling temperature at pressure P, K - Gas |
0.0000 |
372.81 |
0.0017 |
371.86 |
0.0054 |
370.68 |
0.0137 |
368.88 |
0.0215 |
366.61 |
0.0381 |
363.82 |
0.0668 |
360.95 |
0.1033 |
358.62 |
0.1516 |
356.92 |
0.2144 |
355.65 |
0.2660 |
354.89 |
0.3142 |
354.29 |
0.3544 |
353.83 |
0.4030 |
353.39 |
0.4488 |
353.03 |
Thermal conductivity, W/m/K
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Mass fraction of Water (2) - Liquid |
Temperature, K - Liquid |
Thermal conductivity, W/m/K - Liquid |
0.8999 |
282.71 |
0.5160 |
0.8999 |
292.96 |
0.5300 |
0.8999 |
302.89 |
0.5460 |
0.8999 |
312.70 |
0.5590 |
0.8999 |
322.88 |
0.5680 |
0.8999 |
333.00 |
0.5770 |
0.5999 |
283.04 |
0.3560 |
0.5999 |
293.26 |
0.3620 |
0.5999 |
303.05 |
0.3670 |
0.5999 |
313.15 |
0.3710 |
0.5999 |
322.94 |
0.3750 |
0.5999 |
333.13 |
0.3790 |
0.3000 |
283.10 |
0.2400 |
0.3000 |
293.16 |
0.2400 |
0.3000 |
303.19 |
0.2400 |
0.3000 |
313.02 |
0.2400 |
0.3000 |
323.05 |
0.2390 |
0.3000 |
333.14 |
0.2380 |
0.8000 |
282.89 |
0.4550 |
0.8000 |
292.86 |
0.4670 |
0.8000 |
303.04 |
0.4800 |
0.8000 |
312.98 |
0.4910 |
0.8000 |
323.02 |
0.4990 |
0.8000 |
333.09 |
0.5050 |
0.4993 |
283.23 |
0.3110 |
0.4993 |
293.19 |
0.3140 |
0.4993 |
303.43 |
0.3180 |
0.4993 |
313.23 |
0.3190 |
0.4993 |
323.01 |
0.3210 |
0.4993 |
333.26 |
0.3230 |
0.1996 |
283.07 |
0.2120 |
0.1996 |
293.13 |
0.2110 |
0.1996 |
303.12 |
0.2100 |
0.1996 |
313.19 |
0.2080 |
0.1996 |
323.19 |
0.2070 |
0.1996 |
333.26 |
0.2060 |
0.7001 |
282.92 |
0.4030 |
0.7001 |
292.60 |
0.4120 |
0.7001 |
303.05 |
0.4200 |
0.7001 |
313.03 |
0.4270 |
0.7001 |
323.12 |
0.4340 |
0.7001 |
333.14 |
0.4380 |
0.4000 |
283.02 |
0.2730 |
0.4000 |
293.03 |
0.2740 |
0.4000 |
303.15 |
0.2750 |
0.4000 |
313.00 |
0.2760 |
0.4000 |
323.33 |
0.2770 |
0.4000 |
333.32 |
0.2770 |
0.1000 |
282.85 |
0.1890 |
0.1000 |
293.16 |
0.1860 |
0.1000 |
303.11 |
0.1840 |
0.1000 |
313.18 |
0.1820 |
0.1000 |
323.15 |
0.1800 |
0.1000 |
333.15 |
0.1780 |
1.0000 |
283.10 |
0.5850 |
1.0000 |
293.05 |
0.6020 |
1.0000 |
303.17 |
0.6180 |
1.0000 |
313.34 |
0.6330 |
1.0000 |
323.19 |
0.6460 |
1.0000 |
332.85 |
0.6560 |
1.0000 |
343.02 |
0.6640 |
0.0000 |
283.54 |
0.1680 |
0.0000 |
293.31 |
0.1660 |
0.0000 |
303.28 |
0.1630 |
0.0000 |
313.25 |
0.1600 |
0.0000 |
323.07 |
0.1580 |
0.0000 |
332.97 |
0.1540 |
0.0000 |
342.82 |
0.1520 |
Thermal conductivity, W/m/K
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Mass fraction of Ethanol (1) - Liquid |
Temperature, K - Liquid |
Thermal conductivity, W/m/K - Liquid |
0.1002 |
279.61 |
0.5130 |
0.1002 |
289.19 |
0.5270 |
0.1002 |
298.94 |
0.5400 |
0.1002 |
308.91 |
0.5540 |
0.1002 |
318.50 |
0.5640 |
0.1002 |
328.31 |
0.5740 |
0.1002 |
338.27 |
0.5830 |
0.1998 |
279.37 |
0.4530 |
0.1998 |
289.17 |
0.4650 |
0.1998 |
298.99 |
0.4750 |
0.1998 |
308.78 |
0.4860 |
0.1998 |
318.61 |
0.4940 |
0.1998 |
328.63 |
0.5030 |
0.1998 |
338.50 |
0.5110 |
0.3002 |
279.32 |
0.4010 |
0.3002 |
288.97 |
0.4090 |
0.3002 |
299.12 |
0.4180 |
0.3002 |
309.04 |
0.4260 |
0.3002 |
318.77 |
0.4320 |
0.3002 |
328.34 |
0.4360 |
0.3002 |
338.26 |
0.4410 |
0.4002 |
279.49 |
0.3550 |
0.4002 |
289.08 |
0.3600 |
0.4002 |
299.08 |
0.3650 |
0.4002 |
308.84 |
0.3690 |
0.4002 |
318.69 |
0.3740 |
0.4002 |
328.65 |
0.3790 |
0.4002 |
338.71 |
0.3840 |
0.4981 |
279.46 |
0.3120 |
0.4981 |
289.32 |
0.3170 |
0.4981 |
299.13 |
0.3190 |
0.4981 |
309.03 |
0.3230 |
0.4981 |
318.87 |
0.3250 |
0.4981 |
328.66 |
0.3270 |
0.4981 |
338.41 |
0.3280 |
0.5997 |
279.45 |
0.2740 |
0.5997 |
288.96 |
0.2750 |
0.5997 |
298.95 |
0.2770 |
0.5997 |
308.68 |
0.2780 |
0.5997 |
318.67 |
0.2800 |
0.5997 |
328.68 |
0.2810 |
0.5997 |
338.63 |
0.2830 |
0.7016 |
279.23 |
0.2400 |
0.7016 |
289.17 |
0.2410 |
0.7016 |
299.14 |
0.2410 |
0.7016 |
308.97 |
0.2410 |
0.7016 |
318.79 |
0.2410 |
0.7016 |
328.65 |
0.2400 |
0.7016 |
338.36 |
0.2400 |
0.7996 |
279.65 |
0.2130 |
0.7996 |
289.44 |
0.2120 |
0.7996 |
299.59 |
0.2120 |
0.7996 |
309.40 |
0.2110 |
0.7996 |
318.93 |
0.2090 |
0.7996 |
328.87 |
0.2080 |
0.7996 |
338.51 |
0.2070 |
0.8994 |
279.90 |
0.1910 |
0.8994 |
289.62 |
0.1890 |
0.8994 |
299.35 |
0.1860 |
0.8994 |
309.29 |
0.1840 |
0.8994 |
319.24 |
0.1830 |
0.8994 |
328.86 |
0.1810 |
0.8994 |
338.59 |
0.1790 |
Thermal conductivity, W/m/K
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Mass fraction of Water (2) - Liquid |
Temperature, K - Liquid |
Thermal conductivity, W/m/K - Liquid |
0.8999 |
282.71 |
0.5160 |
0.8999 |
292.96 |
0.5300 |
0.8999 |
302.89 |
0.5460 |
0.8999 |
312.70 |
0.5590 |
0.8999 |
322.88 |
0.5680 |
0.8999 |
333.00 |
0.5770 |
0.5999 |
283.04 |
0.3560 |
0.5999 |
293.26 |
0.3620 |
0.5999 |
303.05 |
0.3670 |
0.5999 |
313.15 |
0.3710 |
0.5999 |
322.94 |
0.3750 |
0.5999 |
333.13 |
0.3790 |
0.3000 |
283.10 |
0.2400 |
0.3000 |
293.16 |
0.2400 |
0.3000 |
303.19 |
0.2400 |
0.3000 |
313.02 |
0.2400 |
0.3000 |
323.05 |
0.2390 |
0.3000 |
333.14 |
0.2380 |
0.8000 |
282.89 |
0.4550 |
0.8000 |
292.86 |
0.4670 |
0.8000 |
303.04 |
0.4800 |
0.8000 |
312.98 |
0.4910 |
0.8000 |
323.02 |
0.4990 |
0.8000 |
333.09 |
0.5050 |
0.4993 |
283.23 |
0.3110 |
0.4993 |
293.19 |
0.3140 |
0.4993 |
303.43 |
0.3180 |
0.4993 |
313.23 |
0.3190 |
0.4993 |
323.01 |
0.3210 |
0.4993 |
333.26 |
0.3230 |
0.1996 |
283.07 |
0.2120 |
0.1996 |
293.13 |
0.2110 |
0.1996 |
303.12 |
0.2100 |
0.1996 |
313.19 |
0.2080 |
0.1996 |
323.19 |
0.2070 |
0.1996 |
333.26 |
0.2060 |
0.7001 |
282.92 |
0.4030 |
0.7001 |
292.60 |
0.4120 |
0.7001 |
303.05 |
0.4200 |
0.7001 |
313.03 |
0.4270 |
0.7001 |
323.12 |
0.4340 |
0.7001 |
333.14 |
0.4380 |
0.4000 |
283.02 |
0.2730 |
0.4000 |
293.03 |
0.2740 |
0.4000 |
303.15 |
0.2750 |
0.4000 |
313.00 |
0.2760 |
0.4000 |
323.33 |
0.2770 |
0.4000 |
333.32 |
0.2770 |
0.1000 |
282.85 |
0.1890 |
0.1000 |
293.16 |
0.1860 |
0.1000 |
303.11 |
0.1840 |
0.1000 |
313.18 |
0.1820 |
0.1000 |
323.15 |
0.1800 |
0.1000 |
333.15 |
0.1780 |
1.0000 |
283.10 |
0.5850 |
1.0000 |
293.05 |
0.6020 |
1.0000 |
303.17 |
0.6180 |
1.0000 |
313.34 |
0.6330 |
1.0000 |
323.19 |
0.6460 |
1.0000 |
332.85 |
0.6560 |
1.0000 |
343.02 |
0.6640 |
0.0000 |
283.54 |
0.1680 |
0.0000 |
293.31 |
0.1660 |
0.0000 |
303.28 |
0.1630 |
0.0000 |
313.25 |
0.1600 |
0.0000 |
323.07 |
0.1580 |
0.0000 |
332.97 |
0.1540 |
0.0000 |
342.82 |
0.1520 |
Thermal conductivity, W/m/K
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Mass fraction of Ethanol (1) - Liquid |
Temperature, K - Liquid |
Thermal conductivity, W/m/K - Liquid |
0.1002 |
279.61 |
0.5130 |
0.1002 |
289.19 |
0.5270 |
0.1002 |
298.94 |
0.5400 |
0.1002 |
308.91 |
0.5540 |
0.1002 |
318.50 |
0.5640 |
0.1002 |
328.31 |
0.5740 |
0.1002 |
338.27 |
0.5830 |
0.1998 |
279.37 |
0.4530 |
0.1998 |
289.17 |
0.4650 |
0.1998 |
298.99 |
0.4750 |
0.1998 |
308.78 |
0.4860 |
0.1998 |
318.61 |
0.4940 |
0.1998 |
328.63 |
0.5030 |
0.1998 |
338.50 |
0.5110 |
0.3002 |
279.32 |
0.4010 |
0.3002 |
288.97 |
0.4090 |
0.3002 |
299.12 |
0.4180 |
0.3002 |
309.04 |
0.4260 |
0.3002 |
318.77 |
0.4320 |
0.3002 |
328.34 |
0.4360 |
0.3002 |
338.26 |
0.4410 |
0.4002 |
279.49 |
0.3550 |
0.4002 |
289.08 |
0.3600 |
0.4002 |
299.08 |
0.3650 |
0.4002 |
308.84 |
0.3690 |
0.4002 |
318.69 |
0.3740 |
0.4002 |
328.65 |
0.3790 |
0.4002 |
338.71 |
0.3840 |
0.4981 |
279.46 |
0.3120 |
0.4981 |
289.32 |
0.3170 |
0.4981 |
299.13 |
0.3190 |
0.4981 |
309.03 |
0.3230 |
0.4981 |
318.87 |
0.3250 |
0.4981 |
328.66 |
0.3270 |
0.4981 |
338.41 |
0.3280 |
0.5997 |
279.45 |
0.2740 |
0.5997 |
288.96 |
0.2750 |
0.5997 |
298.95 |
0.2770 |
0.5997 |
308.68 |
0.2780 |
0.5997 |
318.67 |
0.2800 |
0.5997 |
328.68 |
0.2810 |
0.5997 |
338.63 |
0.2830 |
0.7016 |
279.23 |
0.2400 |
0.7016 |
289.17 |
0.2410 |
0.7016 |
299.14 |
0.2410 |
0.7016 |
308.97 |
0.2410 |
0.7016 |
318.79 |
0.2410 |
0.7016 |
328.65 |
0.2400 |
0.7016 |
338.36 |
0.2400 |
0.7996 |
279.65 |
0.2130 |
0.7996 |
289.44 |
0.2120 |
0.7996 |
299.59 |
0.2120 |
0.7996 |
309.40 |
0.2110 |
0.7996 |
318.93 |
0.2090 |
0.7996 |
328.87 |
0.2080 |
0.7996 |
338.51 |
0.2070 |
0.8994 |
279.90 |
0.1910 |
0.8994 |
289.62 |
0.1890 |
0.8994 |
299.35 |
0.1860 |
0.8994 |
309.29 |
0.1840 |
0.8994 |
319.24 |
0.1830 |
0.8994 |
328.86 |
0.1810 |
0.8994 |
338.59 |
0.1790 |
Binary diffusion coefficient, m2/s
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101.3 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Binary diffusion coefficient, m2/s - Liquid |
0.1000 |
0.0000 |
0.2000 |
0.0000 |
0.3000 |
0.0000 |
0.5000 |
0.0000 |
0.7000 |
0.0000 |
0.9000 |
0.0000 |
Binary diffusion coefficient, m2/s
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101.3 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Binary diffusion coefficient, m2/s - Liquid |
0.1000 |
0.0000 |
0.2000 |
0.0000 |
0.3000 |
0.0000 |
0.5000 |
0.0000 |
0.7000 |
0.0000 |
0.9000 |
0.0000 |
Vapor Liquid Equilibrium at Constant Pressure
[ref]
Operational condition: Pressure, kPa =
12.666 (VLE)
x1[mol/mol] of Ethanol (1) - Liquid |
y1[mol/mol] of Ethanol (1) - Vapour |
0.0035 |
0.0205 |
0.0045 |
0.0275 |
0.0175 |
0.1315 |
0.0585 |
0.3050 |
0.0680 |
0.3615 |
0.0935 |
0.4110 |
0.1650 |
0.5200 |
0.2125 |
0.5455 |
0.2410 |
0.5675 |
0.3615 |
0.6060 |
0.4740 |
0.6505 |
0.4985 |
0.6555 |
0.5815 |
0.6970 |
0.6460 |
0.7290 |
0.6540 |
0.7310 |
0.7230 |
0.7760 |
0.7900 |
0.8200 |
0.8370 |
0.8520 |
0.8731 |
0.8817 |
0.8830 |
0.8885 |
0.8880 |
0.8930 |
0.8973 |
0.9012 |
0.9489 |
0.9502 |
0.9707 |
0.9715 |
0.9825 |
0.9835 |
Vapor Liquid Equilibrium at Constant Pressure
[ref]
Operational condition: Pressure, kPa =
25.33 (VLE)
x1[mol/mol] of Ethanol (1) - Liquid |
y1[mol/mol] of Ethanol (1) - Vapour |
0.0160 |
0.1460 |
0.0370 |
0.2755 |
0.0650 |
0.3650 |
0.0900 |
0.4125 |
0.1580 |
0.5015 |
0.2090 |
0.5455 |
0.2385 |
0.5650 |
0.3535 |
0.6045 |
0.4705 |
0.6445 |
0.4970 |
0.6540 |
0.5805 |
0.6925 |
0.6525 |
0.7260 |
0.7000 |
0.7550 |
0.7200 |
0.7685 |
0.7895 |
0.8152 |
0.8416 |
0.8502 |
0.8735 |
0.8790 |
0.8970 |
0.8990 |
0.9485 |
0.9466 |
0.9600 |
0.9580 |
0.9719 |
0.9700 |
0.9812 |
0.9798 |
Vapor Liquid Equilibrium at Constant Pressure
[ref]
Operational condition: Pressure, kPa =
50.66 (VLE)
x1[mol/mol] of Ethanol (1) - Liquid |
y1[mol/mol] of Ethanol (1) - Vapour |
0.0160 |
0.1470 |
0.0315 |
0.2505 |
0.0600 |
0.3765 |
0.0855 |
0.4300 |
0.1465 |
0.5005 |
0.2060 |
0.5415 |
0.2360 |
0.5600 |
0.3495 |
0.5945 |
0.4675 |
0.6410 |
0.4875 |
0.6425 |
0.5800 |
0.6890 |
0.6525 |
0.7250 |
0.7000 |
0.7495 |
0.7175 |
0.7680 |
0.7890 |
0.8111 |
0.8420 |
0.8488 |
0.8749 |
0.8768 |
0.8967 |
0.8973 |
0.9485 |
0.9440 |
0.9727 |
0.9692 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Temperature, K =
393.15 (Gas)
Mole fraction of Ethanol (1) - Liquid |
Vapor or sublimation pressure, kPa - Gas |
0.0000 |
199.00 |
0.0120 |
227.00 |
0.0160 |
233.00 |
0.0350 |
259.00 |
0.0460 |
272.00 |
0.0600 |
288.00 |
0.0750 |
300.00 |
0.1010 |
318.00 |
0.2030 |
358.00 |
0.3090 |
382.00 |
0.4040 |
396.00 |
0.5520 |
415.00 |
0.6360 |
423.00 |
0.7680 |
430.00 |
0.8940 |
432.00 |
1.0000 |
429.00 |
Azeotropic temperature, K
[ref]
Pressure, kPa - Liquid |
Azeotropic temperature, K - Liquid |
101.30 |
351.32 |
Azeotropic temperature, K
[ref]
Mole fraction of Ethanol (1) - Liquid |
Azeotropic temperature, K - Liquid |
0.8950 |
351.30 |
Azeotropic pressure, kPa
[ref]
Mole fraction of Ethanol (1) - Liquid |
Azeotropic pressure, kPa - Liquid |
0.8950 |
101.30 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Temperature, K =
393.15 (Gas)
Mole fraction of Ethanol (1) - Liquid |
Vapor or sublimation pressure, kPa - Gas |
0.0000 |
199.00 |
0.0120 |
227.00 |
0.0160 |
233.00 |
0.0350 |
259.00 |
0.0460 |
272.00 |
0.0600 |
288.00 |
0.0750 |
300.00 |
0.1010 |
318.00 |
0.2030 |
358.00 |
0.3090 |
382.00 |
0.4040 |
396.00 |
0.5520 |
415.00 |
0.6360 |
423.00 |
0.7680 |
430.00 |
0.8940 |
432.00 |
1.0000 |
429.00 |
Azeotropic temperature, K
[ref]
Pressure, kPa - Liquid |
Azeotropic temperature, K - Liquid |
101.30 |
351.32 |
Azeotropic temperature, K
[ref]
Mole fraction of Ethanol (1) - Liquid |
Azeotropic temperature, K - Liquid |
0.8950 |
351.30 |
Azeotropic pressure, kPa
[ref]
Mole fraction of Ethanol (1) - Liquid |
Azeotropic pressure, kPa - Liquid |
0.8950 |
101.30 |
Sources
-
Dortmund Data Bank Vapor-Liquid Equilibrium Data
-
Volumetric properties of ethanol-water mixtures under high temperatures and pressures
-
Measurement of infinite dilution activity coefficients of 1-alkanols (C1 C5) in water as a function of temperature (273 373 K)
-
Solubility of carbon dioxide in binary and ternary mixtures with ethanol and water
-
Determination of partial molar excess enthalpies at infinite dilution for the systems four alcohols + [bmim]PF6 at different temperatures by isothermal titration calorimeter
-
Experimental measurements of vapor liquid equilibria at low pressure: Systems containing alcohols, esters and organic acids
-
Phase equilibria for reactive distillation of diethyl succinate Part I. System diethyl succinate + ethanol + water
-
Measurements and thermodynamic modeling of the ethanol-water system with emphasis to the azeotropic region
-
Isothermal vapor liquid and vapor liquid liquid equilibrium for the ternary system ethanol + water + diethyl carbonate and constituent binary systems at different temperatures
-
High-temperature vapour liquid equilibrium for the water alcohol systems and modeling with SAFT-VR: 1. Water ethanol
-
A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
-
Phase equilibria and excess properties for binary systems in reactive distillation processes Part II. Ethyl acetate synthesis
-
Experimental study of the density and derived (excess, apparent, and partial molar volumes) properties of binary water+ethanol and ternary water+ethanol+lithium nitrate mixtures at temperatures from 298 K to 448 K and pressures up to 40 MPa
-
Ionic liquids as entrainers for the separation of the ethanol/water system
-
Measurements and correlations of density and viscosity for short chain (C1-C3) n-alcohol - water mixtures in the temperature range from 350.7 K to 476.2 K at pressures up to 40 MPa
-
Use of HS-SPME for analysis of the influence of salt concentration and temperature on the activity coefficient at infinite dilution of ethanol-water-salt systems.
-
Separation of azeotropic mixtures (ethanol and water) enhanced by deep eutectic solvents
-
Measurement and correlation of density and viscosity of n-alcohol-water mixtures at temperatures up to 618 K and at pressures up to 40 MPa
-
Vapor-liquid and liquid-liquid equilibrium modeling of systems involving ethanol, water, and ethyl valerate (valeric acid) using the PC-SAFT equation of state
-
Isothermal vapor-liquid equilibria at 383.15-413.15 K for the binary system methanol + dimethyl carbonate and the pressure dependency of the azeotropic point
-
Measurement and correlation of excess molar enthalpy for(1,2-propanediol, or 1,3-propanediol, or 1,4-butanediol + water) at the temperatures (298.15, 323.15, and 343.15) K
-
(p, v,T,x) Measurements of {(1 - x)H2O + xC2H5OH} mixtures in the near-critical and supercritical regions
-
Density, dynamic viscosity, and derived properties of binary mixtures of methanol or ethanol with water, ethyl acetate, and methyl acetate at T = (293.15, 298.15, and 303.15) K
-
Volumetric properties of dilute solutions of water in ethanol and water-d2 in ethanol-d1 between T = (278.15 and 318.15) K
-
Isobaric (vapor + liquid) equilibria for the ternary system of (ethanol + water + 1,3-propanediol) and three constituent binary systems at P = 101.3 kPa
-
Excess enthalpy for the (benzene + cyclohexane) mixture over a wide range of temperature and pressure
-
Volumetric and compressibility behaviour of poly(propylene glycol) - Amino acid aqueous solutions at different temperatures
-
Vapour-liquid equilibria for (water + ethanol + fructose): Experimental data and thermodynamic modelling
-
Thermodynamics properties of binary mixtures of aqueous solutions of glycols at several temperatures and atmospheric pressure
-
Excess volumes and partial molar volumes of binary liquid mixtures of furfural or 2-methylfuran with alcohols at 298.15 K
-
Microscale calorimetric device for determining reaction parameters
-
Application of Conductance Study to Analyze Micellization Behavior of Cationic Gemini Surfactants in Water and Water Ethanol Solvent Mixed Media
-
Effect of Pressure on the Azeotrope of the Mixture Isoamyl Acetate Isoamyl Alcohol at 50.00, 101.32, 250.00, and 350.00 kPa
-
Isobaric Vapor Liquid Liquid Phase Equilibria Measurements of Three Ternary Water + 2-Butanone + Aliphatic Alcohol (Ethanol, 1-Propanol, 2-Propanol) Systems at 101.3 kPa
-
Volumetric Properties of Sodium Lauroylsarcosinate in Aqueous Alcohol Solutions of Methanol, Ethanol, and 1-Propanol
-
Volumetric Properties, Viscosity, and Refractive Indices of Different Naringenin Solutions at Several Temperatures
-
Investigation on Isobaric Vapor-Liquid Equilibria of the Isopropyl Acetate + Water + Ethanol System
-
Physical Behavior of the Phases from the Liquid-Liquid Equilibrium of Citrus Essential Oils Systems at 298.2 K
-
Determination of Physicochemical Parameters of Sodium Dodecyl Sulfate in Aqueous Micellar Solutions Containing Short-Chain Alcohols
-
Effects of Aliphatic Alcohols on Solubility, Physicochemical Properties, and Morphology of Calcium Sulfate Dihydrate (Gypsum) in Aqueous Sodium Chloride Solution at 35 deg.C
-
Physical Properties of Model and Real Systems Composed of Essential Oils and Hydroalcoholic Solvents at 298.2 K and Atmospheric Pressure
-
Measurement of the Thermal Conductivity of 1-Butyl-3-methylimidazolium l-Tryptophan + Water + Ethanol Mixtures at T = (283.15 to 333.15) K
-
Surface Tension of Aqueous Solutions of Small-Chain Amino and Organic Acids
-
Compositions, Densities, and Refractive Indices of Potassium Chloride + Ethanol + Water and Sodium Chloride + Ethanol + Water Solutions at (298.15 and 313.15) K
-
Vapor-Liquid Equilibria in Alcohol + Cyclohexane + Water Systems
-
Determination of Henry s Law Constants and Activity Coefficients at Infinite Dilution of Flavor Compounds in Water at 298 K with a Gas-Chromatographic Method
-
Measurement of Diffusion Coefficients in Thermodynamically Nonideal Systems
-
Measurement of Activity Coefficients at Infinite Dilution of Benzene, Toluene, Ethanol, Esters, Ketones, and Ethers at Various Temperatures in Water Using the Dilutor Technique
-
Vapor-Liquid Equilibria in the Systems Ethyl Lactate + Ethanol and Ethyl Lactate + Water
-
Compressibility Studies of Binary Solutions Involving Water as a Solute in Nonaqueous Solvents at T ) 298.15 K
-
Effect of NiCl2a6H2O and CoCl2a6H2O on the Viscosity of Aqueous Ethanol Mixtures
-
Densities of Univalent Cation Sulfates in Ethanol + Water Solutions
-
Isobaric Vapor Liquid Equilibrium for the Ethanol + Water + 1,3-Dimethylimidazolium Dimethylphosphate System at 101.3 kPa
-
Isobaric Vapor Liquid Equilibrium for Binary Systems of Toluene + Acrylic Acid, Toluene + Acetic Acid, and Cyclohexane + Acrylic Acid at 20 kPa
-
Isobaric Vapor-Liquid Equilibria for Ethanol + Water + Ethylene Glycol and Its Constituent Three Binary Systems
-
Isobaric Vapor Liquid Equilibrium for the Ethanol + Water + 2-Aminoethanol Tetrafluoroborate System at 101.3 kPa
-
Thermal Conductivity of DMSO + C2H5OH, DMSO + H2O, and DMSO + C2H5OH + H2O Mixtures at T = (278.15 to 338.15) K
-
Measurement and Modeling of Vapor Liquid Equilibria for the Octane + Sulfuric Acid + Water + Ethanol System
-
Volumetric, Viscometric, and Refractive Index Behavior of 7-Hydroxy-4-methylcoumarin in Aqueous Ethanol or 1-Propanol Solutions in the Temperature Range of (293.15 to 313.15) K
-
Fructose solubility in mixed (ethanol + water) solvent: experimental data and comparison among different thermodynamic models.
-
Viscosity and Density of Water + Ethyl Acetate + Ethanol Mixtures at 298.15 and 318.15 K and Atmospheric Pressure
-
Temperature Dependence of the Volumetric Properties of Binary and Ternary Mixtures of Water (1) + Methanol (2) + Ethanol (3) at Ambient Pressure (81.5 kPa)
-
Viscosities and Volumetric Properties of Binary and Ternary Mixtures of Tris(2-hydroxyethyl) Methylammonium Methylsulfate + Water + Ethanol at 298.15 K
-
Density, Viscosity, and Electrical Conductivity Measurements on the Ternary System H2O + C2H5OH + LiCl over the Entire Ranges of Solvent Composition and LiCl Solubility from (-5 to +50) deg C
-
Densities and Viscosities of (1,6-Hexanediamine + Ethanol) and (1,6-Hexanediamine + Ethanol + Water) Mixtures at T ) (303.15 to 328.15) K
-
Experimental Measurement and Modeling of Vapor-Liquid Equilibrium for Ternary Systems Containing Ionic Liquids: A Case Study for the System Water + Ethanol + 1-Hexyl-3-methylimidazolium Chloride
-
Density, Speed of Sound, and Isentropic Compressibility of Triethanolamine (or N-Methyldiethanolamine) + Water + Ethanol Solutions from t = (15 to 50) deg C
-
Refractive Indices of Lithium, Magnesium, and Copper(II) Sulfates in Ethanol-Water Solutions
-
Henry s Law Constants of Organic Compounds in Water and n-Octane at T = 293.2 K
-
Using 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate as an Entrainer for the Extractive Distillation of Ethanol + Water Mixtures
-
Densities and Viscosities of 1,1'-(Pentane-1,5-diyl)-bis(pyridinium) Dibromide in Ethanol + Water from (293.15 to 344.15) K