Datasets
-
Mole fraction (34)
-
η - Viscosity, Pa*s (6)
-
Pc - Critical pressure, kPa (6)
-
Pvap - Vapor or sublimation pressure, kPa (38)
-
Interfacial tension, N/m (2)
-
ρc - Critical density, kg/m3 (2)
-
ρg - Mass density, kg/m3 (2)
-
ρl - Mass density, kg/m3 (14)
-
Tc - Critical temperature, K (6)
-
Vapor or sublimation pressure, kPa (10)
Mole fraction of Carbon dioxide (1)
[ref]
Operational condition: Temperature, K =
291.15 (Liquid)
Mole fraction of Carbon dioxide (1) - Liquid |
Mole fraction of Carbon dioxide (1) - Gas |
0.0810 |
0.9290 |
0.1240 |
0.9530 |
Partial pressure, kPa of Carbon dioxide (1)
[ref]
Operational condition: Temperature, K =
313.15 (Gas)
Molality, mol/kg of Carbon dioxide (1) - Liquid |
Partial pressure, kPa of Carbon dioxide (1) - Gas |
0.0607 |
1105.00 |
0.1001 |
1840.00 |
0.1293 |
2365.00 |
0.1594 |
2862.00 |
0.1690 |
3044.00 |
Mole fraction of Carbon dioxide (1)
[ref]
Operational condition: Temperature, K =
333.15 (Liquid)
Mole fraction of Carbon dioxide (1) - Liquid |
Mole fraction of Carbon dioxide (1) - Gas |
0.1342 |
0.9768 |
0.2118 |
0.9787 |
0.2515 |
0.9799 |
0.3542 |
0.9780 |
0.4442 |
0.9745 |
0.5376 |
0.9641 |
0.7808 |
0.9203 |
Mole fraction of Carbon dioxide (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
323.00 |
406.80 |
0.0174 |
323.00 |
410.30 |
0.0170 |
323.00 |
437.80 |
0.0193 |
373.00 |
761.90 |
0.0170 |
373.00 |
772.20 |
0.0179 |
373.00 |
772.20 |
0.0175 |
Mole fraction of Carbon dioxide (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
288.00 |
123.21 |
0.0088 |
288.00 |
223.42 |
0.0159 |
288.00 |
314.01 |
0.0227 |
288.00 |
433.57 |
0.0320 |
298.00 |
93.12 |
0.0057 |
298.00 |
125.44 |
0.0080 |
298.00 |
195.35 |
0.0119 |
298.00 |
223.42 |
0.0137 |
298.00 |
308.74 |
0.0192 |
298.00 |
324.24 |
0.0203 |
298.00 |
419.18 |
0.0264 |
298.00 |
430.63 |
0.0272 |
298.00 |
538.44 |
0.0343 |
308.00 |
113.28 |
0.0056 |
308.00 |
189.98 |
0.0098 |
308.00 |
278.44 |
0.0147 |
308.00 |
384.93 |
0.0206 |
308.00 |
465.18 |
0.0252 |
323.00 |
85.52 |
0.0033 |
323.00 |
132.13 |
0.0052 |
323.00 |
211.77 |
0.0087 |
323.00 |
289.89 |
0.0126 |
323.00 |
370.24 |
0.0166 |
Mole fraction of Carbon dioxide (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Carbon dioxide (1) - Gas |
Mole fraction of Carbon dioxide (1) - Liquid |
333.00 |
0.9800 |
0.1700 |
333.00 |
0.9780 |
0.1760 |
333.00 |
0.9820 |
0.1740 |
333.00 |
0.9820 |
0.1750 |
333.00 |
0.9830 |
0.1770 |
333.00 |
0.9820 |
0.2810 |
333.00 |
0.9780 |
0.4120 |
333.00 |
0.9560 |
0.6400 |
353.00 |
0.9130 |
0.6010 |
358.00 |
0.9190 |
0.5560 |
363.00 |
0.9210 |
0.5120 |
368.00 |
0.9130 |
0.4820 |
373.00 |
0.9080 |
0.4630 |
Mole fraction of Carbon dioxide (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
303.20 |
1140.00 |
0.0760 |
303.20 |
2130.00 |
0.1510 |
303.20 |
3080.00 |
0.2380 |
303.20 |
3940.00 |
0.2950 |
303.20 |
4980.00 |
0.4140 |
303.20 |
5940.00 |
0.5890 |
323.20 |
1020.00 |
0.0490 |
323.20 |
1980.00 |
0.1010 |
323.20 |
3060.00 |
0.1610 |
323.20 |
4020.00 |
0.2180 |
323.20 |
5110.00 |
0.2820 |
323.20 |
6080.00 |
0.3580 |
Mole fraction of Carbon dioxide (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
293.15 |
716.30 |
0.0530 |
293.15 |
1642.90 |
0.1273 |
293.15 |
2169.00 |
0.1848 |
303.15 |
930.60 |
0.0622 |
303.15 |
1970.30 |
0.1282 |
303.15 |
2903.50 |
0.2061 |
Mole fraction of Carbon dioxide (1)
[ref]
Operational condition: Temperature, K =
313 (Gas)
Pressure, kPa - Gas |
Mole fraction of Carbon dioxide (1) - Gas |
3200.00 |
0.9860 |
4280.00 |
0.9880 |
5380.00 |
0.9890 |
6050.00 |
0.9890 |
7290.00 |
0.9860 |
7640.00 |
0.9800 |
Mole fraction of Carbon dioxide (1)
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (1) - Liquid |
Temperature, K - Liquid |
Mole fraction of Carbon dioxide (1) - Gas |
0.2647 |
323.15 |
0.9840 |
0.2771 |
323.15 |
0.9859 |
0.3058 |
323.15 |
0.9819 |
0.3128 |
323.15 |
0.9837 |
0.4128 |
323.15 |
0.9814 |
0.4795 |
323.15 |
0.9739 |
0.5069 |
323.15 |
0.9764 |
0.5455 |
323.15 |
0.9754 |
0.6348 |
323.15 |
0.9740 |
0.6279 |
323.15 |
0.9671 |
0.6535 |
323.15 |
0.9679 |
0.6875 |
323.15 |
0.9630 |
0.2930 |
343.15 |
0.9679 |
0.3785 |
343.15 |
0.9656 |
0.4260 |
343.15 |
0.9614 |
0.4968 |
343.15 |
0.9484 |
0.6130 |
343.15 |
0.9432 |
0.6910 |
343.15 |
0.9060 |
Mole fraction of Carbon dioxide (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa of Carbon dioxide (1) - Gas |
Mole fraction of Carbon dioxide (1) - Liquid |
283.15 |
82.00 |
0.0075 |
283.15 |
567.00 |
0.0505 |
283.15 |
1059.00 |
0.1010 |
283.15 |
1551.00 |
0.1433 |
283.15 |
2044.00 |
0.1914 |
283.15 |
2468.00 |
0.2369 |
303.15 |
110.00 |
0.0070 |
303.15 |
756.00 |
0.0474 |
303.15 |
1422.00 |
0.0953 |
303.15 |
2109.00 |
0.1364 |
303.15 |
2803.00 |
0.1810 |
303.15 |
3419.00 |
0.2243 |
323.15 |
135.00 |
0.0067 |
323.15 |
943.00 |
0.0450 |
323.15 |
1781.00 |
0.0908 |
323.15 |
2664.00 |
0.1302 |
323.15 |
3565.00 |
0.1727 |
323.15 |
4385.00 |
0.2141 |
343.15 |
157.00 |
0.0065 |
343.15 |
1113.00 |
0.0434 |
343.15 |
2117.00 |
0.0878 |
343.15 |
3187.00 |
0.1262 |
343.15 |
4290.00 |
0.1673 |
343.15 |
5307.00 |
0.2075 |
363.15 |
173.00 |
0.0065 |
363.15 |
1262.00 |
0.0426 |
363.15 |
2472.00 |
0.0840 |
363.15 |
3664.00 |
0.1242 |
363.15 |
4951.00 |
0.1647 |
293.15 |
96.00 |
0.0072 |
293.15 |
661.00 |
0.0489 |
293.15 |
1239.00 |
0.0980 |
293.15 |
1827.00 |
0.1402 |
293.15 |
2418.00 |
0.1860 |
293.15 |
2936.00 |
0.2305 |
313.15 |
124.00 |
0.0068 |
313.15 |
851.00 |
0.0461 |
313.15 |
1603.00 |
0.0929 |
313.15 |
2389.00 |
0.1331 |
313.15 |
3187.00 |
0.1765 |
313.15 |
3905.00 |
0.2188 |
333.15 |
147.00 |
0.0066 |
333.15 |
1029.00 |
0.0441 |
333.15 |
1952.00 |
0.0891 |
333.15 |
2932.00 |
0.1279 |
333.15 |
3937.00 |
0.1696 |
333.15 |
4854.00 |
0.2103 |
353.15 |
166.00 |
0.0065 |
353.15 |
1191.00 |
0.0429 |
353.15 |
2274.00 |
0.0868 |
353.15 |
3432.00 |
0.1249 |
353.15 |
4629.00 |
0.1657 |
353.15 |
5738.00 |
0.2056 |
373.15 |
178.00 |
0.0066 |
373.15 |
1328.00 |
0.0425 |
373.15 |
2612.00 |
0.0838 |
373.15 |
3881.00 |
0.1239 |
373.15 |
5253.00 |
0.1645 |
Mole fraction of Carbon dioxide (1)
[ref]
Operational condition: Temperature, K =
333.4 (Gas)
Mole fraction of Carbon dioxide (1) - Liquid |
Mole fraction of Carbon dioxide (1) - Gas |
0.4934 |
0.9725 |
0.6111 |
0.9532 |
0.8164 |
0.9085 |
Mole fraction of Carbon dioxide (1)
[ref]
Operational condition: Temperature, K =
291.15 (Gas)
Mole fraction of Carbon dioxide (1) - Liquid |
Mole fraction of Carbon dioxide (1) - Gas |
0.1840 |
0.9850 |
0.2270 |
0.9900 |
0.3040 |
0.9940 |
0.4550 |
0.9920 |
0.7280 |
0.9920 |
0.8380 |
0.9940 |
0.9510 |
0.9970 |
0.9830 |
0.9980 |
0.9960 |
0.9990 |
Mole fraction of Carbon dioxide (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa of Carbon dioxide (1) - Gas |
Mole fraction of Carbon dioxide (1) - Liquid |
288.15 |
58.00 |
0.0055 |
288.15 |
167.00 |
0.0157 |
288.15 |
413.00 |
0.0388 |
288.15 |
656.20 |
0.0617 |
288.15 |
846.10 |
0.0795 |
288.15 |
1141.70 |
0.1073 |
288.15 |
1423.50 |
0.1338 |
288.15 |
1643.80 |
0.1545 |
288.15 |
1805.20 |
0.1697 |
288.15 |
2119.70 |
0.1992 |
288.15 |
2462.70 |
0.2315 |
288.15 |
2778.00 |
0.2611 |
288.15 |
3063.50 |
0.2879 |
288.15 |
3372.00 |
0.3169 |
298.15 |
273.20 |
0.0205 |
298.15 |
463.50 |
0.0349 |
298.15 |
778.70 |
0.0586 |
298.15 |
946.20 |
0.0712 |
298.15 |
1211.90 |
0.0911 |
298.15 |
1405.20 |
0.1057 |
298.15 |
1684.60 |
0.1267 |
298.15 |
1823.50 |
0.1371 |
298.15 |
2147.90 |
0.1615 |
298.15 |
2384.60 |
0.1793 |
298.15 |
2566.20 |
0.1930 |
298.15 |
2732.00 |
0.2055 |
298.15 |
2967.80 |
0.2232 |
298.15 |
3258.40 |
0.2451 |
298.15 |
3404.30 |
0.2560 |
298.15 |
3721.90 |
0.2799 |
298.15 |
4133.60 |
0.3109 |
298.15 |
4357.90 |
0.3278 |
308.15 |
272.00 |
0.0172 |
308.15 |
463.00 |
0.0293 |
308.15 |
778.00 |
0.0493 |
308.15 |
1002.70 |
0.0635 |
308.15 |
1297.60 |
0.0822 |
308.15 |
1505.20 |
0.0954 |
308.15 |
1843.10 |
0.1168 |
308.15 |
2023.50 |
0.1282 |
308.15 |
2341.40 |
0.1484 |
308.15 |
2561.90 |
0.1623 |
308.15 |
2886.50 |
0.1829 |
308.15 |
3314.20 |
0.2100 |
308.15 |
3595.00 |
0.2278 |
308.15 |
3831.60 |
0.2428 |
308.15 |
4112.40 |
0.2606 |
308.15 |
4439.70 |
0.2813 |
308.15 |
4796.20 |
0.3039 |
308.15 |
5081.10 |
0.3220 |
318.15 |
239.20 |
0.0130 |
318.15 |
436.50 |
0.0237 |
318.15 |
794.40 |
0.0430 |
318.15 |
1098.10 |
0.0595 |
318.15 |
1427.30 |
0.0773 |
318.15 |
1757.00 |
0.0952 |
318.15 |
1965.60 |
0.1065 |
318.15 |
2196.10 |
0.1190 |
318.15 |
2445.30 |
0.1325 |
318.15 |
2752.80 |
0.1492 |
318.15 |
2998.60 |
0.1625 |
318.15 |
3227.40 |
0.1749 |
318.15 |
3434.30 |
0.1861 |
318.15 |
3732.90 |
0.2023 |
318.15 |
4253.60 |
0.2305 |
318.15 |
4537.80 |
0.2459 |
318.15 |
4799.20 |
0.2600 |
318.15 |
5001.10 |
0.2710 |
318.15 |
5464.90 |
0.2961 |
318.15 |
5716.80 |
0.3098 |
Mole fraction of Carbon dioxide (1)
[ref]
Operational condition: Temperature, K =
313.15 (Liquid)
Pressure, kPa - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
514.00 |
0.0270 |
1155.00 |
0.0630 |
1600.00 |
0.0880 |
2061.00 |
0.1130 |
2120.00 |
0.1170 |
3020.00 |
0.1670 |
3270.00 |
0.1810 |
3810.00 |
0.2120 |
Mole fraction of Carbon dioxide (1)
[ref]
Operational condition: Temperature, K =
333.15 (Liquid)
Mole fraction of Carbon dioxide (1) - Liquid |
Mole fraction of Carbon dioxide (1) - Gas |
0.3483 |
0.9752 |
0.5467 |
0.9571 |
0.7305 |
0.9132 |
Mole fraction of Carbon dioxide (1)
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (1) - Liquid |
Temperature, K - Liquid |
Mole fraction of Carbon dioxide (1) - Gas |
0.0555 |
293.15 |
0.9886 |
0.0606 |
303.15 |
0.9879 |
0.1292 |
293.15 |
0.9948 |
0.1355 |
303.15 |
0.9940 |
0.1755 |
293.15 |
0.9972 |
0.2185 |
303.15 |
0.9972 |
Mole fraction of Carbon dioxide (1)
[ref]
Operational condition: Temperature, K =
291.15 (Liquid)
Mole fraction of Carbon dioxide (1) - Liquid |
Mole fraction of Carbon dioxide (1) - Gas |
0.0810 |
0.9290 |
0.1240 |
0.9530 |
Partial pressure, kPa of Carbon dioxide (1)
[ref]
Operational condition: Temperature, K =
313.15 (Gas)
Molality, mol/kg of Carbon dioxide (1) - Liquid |
Partial pressure, kPa of Carbon dioxide (1) - Gas |
0.0607 |
1105.00 |
0.1001 |
1840.00 |
0.1293 |
2365.00 |
0.1594 |
2862.00 |
0.1690 |
3044.00 |
Mole fraction of Carbon dioxide (1)
[ref]
Operational condition: Temperature, K =
333.15 (Liquid)
Mole fraction of Carbon dioxide (1) - Liquid |
Mole fraction of Carbon dioxide (1) - Gas |
0.1342 |
0.9768 |
0.2118 |
0.9787 |
0.2515 |
0.9799 |
0.3542 |
0.9780 |
0.4442 |
0.9745 |
0.5376 |
0.9641 |
0.7808 |
0.9203 |
Mole fraction of Carbon dioxide (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
323.00 |
406.80 |
0.0174 |
323.00 |
410.30 |
0.0170 |
323.00 |
437.80 |
0.0193 |
373.00 |
761.90 |
0.0170 |
373.00 |
772.20 |
0.0179 |
373.00 |
772.20 |
0.0175 |
Mole fraction of Carbon dioxide (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
288.00 |
123.21 |
0.0088 |
288.00 |
223.42 |
0.0159 |
288.00 |
314.01 |
0.0227 |
288.00 |
433.57 |
0.0320 |
298.00 |
93.12 |
0.0057 |
298.00 |
125.44 |
0.0080 |
298.00 |
195.35 |
0.0119 |
298.00 |
223.42 |
0.0137 |
298.00 |
308.74 |
0.0192 |
298.00 |
324.24 |
0.0203 |
298.00 |
419.18 |
0.0264 |
298.00 |
430.63 |
0.0272 |
298.00 |
538.44 |
0.0343 |
308.00 |
113.28 |
0.0056 |
308.00 |
189.98 |
0.0098 |
308.00 |
278.44 |
0.0147 |
308.00 |
384.93 |
0.0206 |
308.00 |
465.18 |
0.0252 |
323.00 |
85.52 |
0.0033 |
323.00 |
132.13 |
0.0052 |
323.00 |
211.77 |
0.0087 |
323.00 |
289.89 |
0.0126 |
323.00 |
370.24 |
0.0166 |
Mole fraction of Carbon dioxide (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Carbon dioxide (1) - Gas |
Mole fraction of Carbon dioxide (1) - Liquid |
333.00 |
0.9800 |
0.1700 |
333.00 |
0.9780 |
0.1760 |
333.00 |
0.9820 |
0.1740 |
333.00 |
0.9820 |
0.1750 |
333.00 |
0.9830 |
0.1770 |
333.00 |
0.9820 |
0.2810 |
333.00 |
0.9780 |
0.4120 |
333.00 |
0.9560 |
0.6400 |
353.00 |
0.9130 |
0.6010 |
358.00 |
0.9190 |
0.5560 |
363.00 |
0.9210 |
0.5120 |
368.00 |
0.9130 |
0.4820 |
373.00 |
0.9080 |
0.4630 |
Mole fraction of Carbon dioxide (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
303.20 |
1140.00 |
0.0760 |
303.20 |
2130.00 |
0.1510 |
303.20 |
3080.00 |
0.2380 |
303.20 |
3940.00 |
0.2950 |
303.20 |
4980.00 |
0.4140 |
303.20 |
5940.00 |
0.5890 |
323.20 |
1020.00 |
0.0490 |
323.20 |
1980.00 |
0.1010 |
323.20 |
3060.00 |
0.1610 |
323.20 |
4020.00 |
0.2180 |
323.20 |
5110.00 |
0.2820 |
323.20 |
6080.00 |
0.3580 |
Mole fraction of Carbon dioxide (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
293.15 |
716.30 |
0.0530 |
293.15 |
1642.90 |
0.1273 |
293.15 |
2169.00 |
0.1848 |
303.15 |
930.60 |
0.0622 |
303.15 |
1970.30 |
0.1282 |
303.15 |
2903.50 |
0.2061 |
Mole fraction of Carbon dioxide (1)
[ref]
Operational condition: Temperature, K =
313 (Gas)
Pressure, kPa - Gas |
Mole fraction of Carbon dioxide (1) - Gas |
3200.00 |
0.9860 |
4280.00 |
0.9880 |
5380.00 |
0.9890 |
6050.00 |
0.9890 |
7290.00 |
0.9860 |
7640.00 |
0.9800 |
Mole fraction of Carbon dioxide (1)
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (1) - Liquid |
Temperature, K - Liquid |
Mole fraction of Carbon dioxide (1) - Gas |
0.2647 |
323.15 |
0.9840 |
0.2771 |
323.15 |
0.9859 |
0.3058 |
323.15 |
0.9819 |
0.3128 |
323.15 |
0.9837 |
0.4128 |
323.15 |
0.9814 |
0.4795 |
323.15 |
0.9739 |
0.5069 |
323.15 |
0.9764 |
0.5455 |
323.15 |
0.9754 |
0.6348 |
323.15 |
0.9740 |
0.6279 |
323.15 |
0.9671 |
0.6535 |
323.15 |
0.9679 |
0.6875 |
323.15 |
0.9630 |
0.2930 |
343.15 |
0.9679 |
0.3785 |
343.15 |
0.9656 |
0.4260 |
343.15 |
0.9614 |
0.4968 |
343.15 |
0.9484 |
0.6130 |
343.15 |
0.9432 |
0.6910 |
343.15 |
0.9060 |
Mole fraction of Carbon dioxide (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa of Carbon dioxide (1) - Gas |
Mole fraction of Carbon dioxide (1) - Liquid |
283.15 |
82.00 |
0.0075 |
283.15 |
567.00 |
0.0505 |
283.15 |
1059.00 |
0.1010 |
283.15 |
1551.00 |
0.1433 |
283.15 |
2044.00 |
0.1914 |
283.15 |
2468.00 |
0.2369 |
303.15 |
110.00 |
0.0070 |
303.15 |
756.00 |
0.0474 |
303.15 |
1422.00 |
0.0953 |
303.15 |
2109.00 |
0.1364 |
303.15 |
2803.00 |
0.1810 |
303.15 |
3419.00 |
0.2243 |
323.15 |
135.00 |
0.0067 |
323.15 |
943.00 |
0.0450 |
323.15 |
1781.00 |
0.0908 |
323.15 |
2664.00 |
0.1302 |
323.15 |
3565.00 |
0.1727 |
323.15 |
4385.00 |
0.2141 |
343.15 |
157.00 |
0.0065 |
343.15 |
1113.00 |
0.0434 |
343.15 |
2117.00 |
0.0878 |
343.15 |
3187.00 |
0.1262 |
343.15 |
4290.00 |
0.1673 |
343.15 |
5307.00 |
0.2075 |
363.15 |
173.00 |
0.0065 |
363.15 |
1262.00 |
0.0426 |
363.15 |
2472.00 |
0.0840 |
363.15 |
3664.00 |
0.1242 |
363.15 |
4951.00 |
0.1647 |
293.15 |
96.00 |
0.0072 |
293.15 |
661.00 |
0.0489 |
293.15 |
1239.00 |
0.0980 |
293.15 |
1827.00 |
0.1402 |
293.15 |
2418.00 |
0.1860 |
293.15 |
2936.00 |
0.2305 |
313.15 |
124.00 |
0.0068 |
313.15 |
851.00 |
0.0461 |
313.15 |
1603.00 |
0.0929 |
313.15 |
2389.00 |
0.1331 |
313.15 |
3187.00 |
0.1765 |
313.15 |
3905.00 |
0.2188 |
333.15 |
147.00 |
0.0066 |
333.15 |
1029.00 |
0.0441 |
333.15 |
1952.00 |
0.0891 |
333.15 |
2932.00 |
0.1279 |
333.15 |
3937.00 |
0.1696 |
333.15 |
4854.00 |
0.2103 |
353.15 |
166.00 |
0.0065 |
353.15 |
1191.00 |
0.0429 |
353.15 |
2274.00 |
0.0868 |
353.15 |
3432.00 |
0.1249 |
353.15 |
4629.00 |
0.1657 |
353.15 |
5738.00 |
0.2056 |
373.15 |
178.00 |
0.0066 |
373.15 |
1328.00 |
0.0425 |
373.15 |
2612.00 |
0.0838 |
373.15 |
3881.00 |
0.1239 |
373.15 |
5253.00 |
0.1645 |
Mole fraction of Carbon dioxide (1)
[ref]
Operational condition: Temperature, K =
333.4 (Gas)
Mole fraction of Carbon dioxide (1) - Liquid |
Mole fraction of Carbon dioxide (1) - Gas |
0.4934 |
0.9725 |
0.6111 |
0.9532 |
0.8164 |
0.9085 |
Mole fraction of Carbon dioxide (1)
[ref]
Operational condition: Temperature, K =
291.15 (Gas)
Mole fraction of Carbon dioxide (1) - Liquid |
Mole fraction of Carbon dioxide (1) - Gas |
0.1840 |
0.9850 |
0.2270 |
0.9900 |
0.3040 |
0.9940 |
0.4550 |
0.9920 |
0.7280 |
0.9920 |
0.8380 |
0.9940 |
0.9510 |
0.9970 |
0.9830 |
0.9980 |
0.9960 |
0.9990 |
Mole fraction of Carbon dioxide (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa of Carbon dioxide (1) - Gas |
Mole fraction of Carbon dioxide (1) - Liquid |
288.15 |
58.00 |
0.0055 |
288.15 |
167.00 |
0.0157 |
288.15 |
413.00 |
0.0388 |
288.15 |
656.20 |
0.0617 |
288.15 |
846.10 |
0.0795 |
288.15 |
1141.70 |
0.1073 |
288.15 |
1423.50 |
0.1338 |
288.15 |
1643.80 |
0.1545 |
288.15 |
1805.20 |
0.1697 |
288.15 |
2119.70 |
0.1992 |
288.15 |
2462.70 |
0.2315 |
288.15 |
2778.00 |
0.2611 |
288.15 |
3063.50 |
0.2879 |
288.15 |
3372.00 |
0.3169 |
298.15 |
273.20 |
0.0205 |
298.15 |
463.50 |
0.0349 |
298.15 |
778.70 |
0.0586 |
298.15 |
946.20 |
0.0712 |
298.15 |
1211.90 |
0.0911 |
298.15 |
1405.20 |
0.1057 |
298.15 |
1684.60 |
0.1267 |
298.15 |
1823.50 |
0.1371 |
298.15 |
2147.90 |
0.1615 |
298.15 |
2384.60 |
0.1793 |
298.15 |
2566.20 |
0.1930 |
298.15 |
2732.00 |
0.2055 |
298.15 |
2967.80 |
0.2232 |
298.15 |
3258.40 |
0.2451 |
298.15 |
3404.30 |
0.2560 |
298.15 |
3721.90 |
0.2799 |
298.15 |
4133.60 |
0.3109 |
298.15 |
4357.90 |
0.3278 |
308.15 |
272.00 |
0.0172 |
308.15 |
463.00 |
0.0293 |
308.15 |
778.00 |
0.0493 |
308.15 |
1002.70 |
0.0635 |
308.15 |
1297.60 |
0.0822 |
308.15 |
1505.20 |
0.0954 |
308.15 |
1843.10 |
0.1168 |
308.15 |
2023.50 |
0.1282 |
308.15 |
2341.40 |
0.1484 |
308.15 |
2561.90 |
0.1623 |
308.15 |
2886.50 |
0.1829 |
308.15 |
3314.20 |
0.2100 |
308.15 |
3595.00 |
0.2278 |
308.15 |
3831.60 |
0.2428 |
308.15 |
4112.40 |
0.2606 |
308.15 |
4439.70 |
0.2813 |
308.15 |
4796.20 |
0.3039 |
308.15 |
5081.10 |
0.3220 |
318.15 |
239.20 |
0.0130 |
318.15 |
436.50 |
0.0237 |
318.15 |
794.40 |
0.0430 |
318.15 |
1098.10 |
0.0595 |
318.15 |
1427.30 |
0.0773 |
318.15 |
1757.00 |
0.0952 |
318.15 |
1965.60 |
0.1065 |
318.15 |
2196.10 |
0.1190 |
318.15 |
2445.30 |
0.1325 |
318.15 |
2752.80 |
0.1492 |
318.15 |
2998.60 |
0.1625 |
318.15 |
3227.40 |
0.1749 |
318.15 |
3434.30 |
0.1861 |
318.15 |
3732.90 |
0.2023 |
318.15 |
4253.60 |
0.2305 |
318.15 |
4537.80 |
0.2459 |
318.15 |
4799.20 |
0.2600 |
318.15 |
5001.10 |
0.2710 |
318.15 |
5464.90 |
0.2961 |
318.15 |
5716.80 |
0.3098 |
Mole fraction of Carbon dioxide (1)
[ref]
Operational condition: Temperature, K =
313.15 (Liquid)
Pressure, kPa - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
514.00 |
0.0270 |
1155.00 |
0.0630 |
1600.00 |
0.0880 |
2061.00 |
0.1130 |
2120.00 |
0.1170 |
3020.00 |
0.1670 |
3270.00 |
0.1810 |
3810.00 |
0.2120 |
Mole fraction of Carbon dioxide (1)
[ref]
Operational condition: Temperature, K =
333.15 (Liquid)
Mole fraction of Carbon dioxide (1) - Liquid |
Mole fraction of Carbon dioxide (1) - Gas |
0.3483 |
0.9752 |
0.5467 |
0.9571 |
0.7305 |
0.9132 |
Mole fraction of Carbon dioxide (1)
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (1) - Liquid |
Temperature, K - Liquid |
Mole fraction of Carbon dioxide (1) - Gas |
0.0555 |
293.15 |
0.9886 |
0.0606 |
303.15 |
0.9879 |
0.1292 |
293.15 |
0.9948 |
0.1355 |
303.15 |
0.9940 |
0.1755 |
293.15 |
0.9972 |
0.2185 |
303.15 |
0.9972 |
Viscosity, Pa*s
[ref]
Operational condition: Temperature, K =
313.15 (Liquid)
Fixed |
Measured |
Pressure, kPa - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Viscosity, Pa*s - Liquid |
200.00 |
0.0000 |
0.0008 |
1830.00 |
0.1044 |
0.0006 |
3020.00 |
0.1746 |
0.0006 |
3760.00 |
0.2221 |
0.0005 |
5200.00 |
0.3150 |
0.0004 |
Viscosity, Pa*s
[ref]
Operational condition: Temperature, K =
313.15 (Liquid)
Fixed |
Measured |
Pressure, kPa - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Viscosity, Pa*s - Liquid |
10000.00 |
0.0000 |
0.0009 |
10000.00 |
0.1044 |
0.0007 |
10000.00 |
0.1746 |
0.0006 |
10000.00 |
0.2221 |
0.0005 |
10000.00 |
0.3150 |
0.0004 |
20000.00 |
0.0000 |
0.0009 |
20000.00 |
0.1044 |
0.0007 |
20000.00 |
0.1746 |
0.0007 |
20000.00 |
0.2221 |
0.0006 |
20000.00 |
0.3150 |
0.0005 |
Viscosity, Pa*s
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Viscosity, Pa*s - Liquid |
303.20 |
1140.00 |
0.0760 |
0.0008 |
303.20 |
2130.00 |
0.1510 |
0.0007 |
303.20 |
3080.00 |
0.2380 |
0.0006 |
303.20 |
3940.00 |
0.2950 |
0.0005 |
303.20 |
4980.00 |
0.4140 |
0.0004 |
303.20 |
5940.00 |
0.5890 |
0.0002 |
323.20 |
1020.00 |
0.0490 |
0.0006 |
323.20 |
1980.00 |
0.1010 |
0.0005 |
323.20 |
3060.00 |
0.1610 |
0.0004 |
323.20 |
4020.00 |
0.2180 |
0.0004 |
323.20 |
5110.00 |
0.2820 |
0.0003 |
323.20 |
6080.00 |
0.3580 |
0.0003 |
Viscosity, Pa*s
[ref]
Operational condition: Temperature, K =
313.15 (Liquid)
Fixed |
Measured |
Pressure, kPa - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Viscosity, Pa*s - Liquid |
200.00 |
0.0000 |
0.0008 |
1830.00 |
0.1044 |
0.0006 |
3020.00 |
0.1746 |
0.0006 |
3760.00 |
0.2221 |
0.0005 |
5200.00 |
0.3150 |
0.0004 |
Viscosity, Pa*s
[ref]
Operational condition: Temperature, K =
313.15 (Liquid)
Fixed |
Measured |
Pressure, kPa - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Viscosity, Pa*s - Liquid |
10000.00 |
0.0000 |
0.0009 |
10000.00 |
0.1044 |
0.0007 |
10000.00 |
0.1746 |
0.0006 |
10000.00 |
0.2221 |
0.0005 |
10000.00 |
0.3150 |
0.0004 |
20000.00 |
0.0000 |
0.0009 |
20000.00 |
0.1044 |
0.0007 |
20000.00 |
0.1746 |
0.0007 |
20000.00 |
0.2221 |
0.0006 |
20000.00 |
0.3150 |
0.0005 |
Viscosity, Pa*s
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Viscosity, Pa*s - Liquid |
303.20 |
1140.00 |
0.0760 |
0.0008 |
303.20 |
2130.00 |
0.1510 |
0.0007 |
303.20 |
3080.00 |
0.2380 |
0.0006 |
303.20 |
3940.00 |
0.2950 |
0.0005 |
303.20 |
4980.00 |
0.4140 |
0.0004 |
303.20 |
5940.00 |
0.5890 |
0.0002 |
323.20 |
1020.00 |
0.0490 |
0.0006 |
323.20 |
1980.00 |
0.1010 |
0.0005 |
323.20 |
3060.00 |
0.1610 |
0.0004 |
323.20 |
4020.00 |
0.2180 |
0.0004 |
323.20 |
5110.00 |
0.2820 |
0.0003 |
323.20 |
6080.00 |
0.3580 |
0.0003 |
Critical pressure, kPa
[ref]
Mole fraction of Carbon dioxide (1) - Liquid |
Critical pressure, kPa - Liquid |
0.5300 |
13300.00 |
0.7200 |
15300.00 |
0.8800 |
13100.00 |
0.8900 |
10800.00 |
Critical pressure, kPa
[ref]
Mole fraction of Ethanol (2) - Liquid |
Critical pressure, kPa - Liquid |
0.3000 |
14720.00 |
0.8000 |
8870.00 |
Critical pressure, kPa
[ref]
Mole fraction of Carbon dioxide (1) - Liquid |
Critical pressure, kPa - Liquid |
0.8315 |
13860.00 |
0.8380 |
13700.00 |
0.8401 |
13110.00 |
0.8409 |
12540.00 |
0.8420 |
12000.00 |
0.8507 |
11170.00 |
0.8920 |
10450.00 |
0.9010 |
10600.00 |
0.9080 |
9840.00 |
0.9310 |
9100.00 |
Critical pressure, kPa
[ref]
Mole fraction of Carbon dioxide (1) - Liquid |
Critical pressure, kPa - Liquid |
0.5300 |
13300.00 |
0.7200 |
15300.00 |
0.8800 |
13100.00 |
0.8900 |
10800.00 |
Critical pressure, kPa
[ref]
Mole fraction of Ethanol (2) - Liquid |
Critical pressure, kPa - Liquid |
0.3000 |
14720.00 |
0.8000 |
8870.00 |
Critical pressure, kPa
[ref]
Mole fraction of Carbon dioxide (1) - Liquid |
Critical pressure, kPa - Liquid |
0.8315 |
13860.00 |
0.8380 |
13700.00 |
0.8401 |
13110.00 |
0.8409 |
12540.00 |
0.8420 |
12000.00 |
0.8507 |
11170.00 |
0.8920 |
10450.00 |
0.9010 |
10600.00 |
0.9080 |
9840.00 |
0.9310 |
9100.00 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Temperature, K =
291.15 (Liquid)
Mole fraction of Carbon dioxide (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0810 |
1176.00 |
0.1240 |
1493.00 |
0.1600 |
1942.00 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Temperature, K =
333.15 (Liquid)
Mole fraction of Carbon dioxide (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.1342 |
3050.00 |
0.2118 |
4543.00 |
0.2515 |
5318.00 |
0.3542 |
7138.00 |
0.4442 |
8515.00 |
0.5376 |
9561.00 |
0.7808 |
10406.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
313.15 |
0.2590 |
3840.00 |
313.15 |
0.2680 |
3990.00 |
313.15 |
0.5120 |
6130.00 |
313.15 |
0.5180 |
6340.00 |
313.15 |
0.7090 |
6670.00 |
313.15 |
0.7120 |
6880.00 |
333.15 |
0.2590 |
5070.00 |
333.15 |
0.2680 |
5190.00 |
333.15 |
0.5120 |
8420.00 |
333.15 |
0.5180 |
8530.00 |
333.15 |
0.7090 |
10050.00 |
333.15 |
0.7120 |
10010.00 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Temperature, K =
313 (Liquid)
Mole fraction of Carbon dioxide (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.1627 |
3040.00 |
0.2477 |
4310.00 |
0.3220 |
5170.00 |
0.4049 |
6050.00 |
0.4767 |
6110.00 |
0.6110 |
7090.00 |
0.5783 |
7080.00 |
0.6916 |
7390.00 |
0.7083 |
7650.00 |
0.8441 |
7950.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
303.20 |
0.4923 |
5570.00 |
303.20 |
0.5987 |
6020.00 |
303.20 |
0.7069 |
6260.00 |
303.20 |
0.8198 |
6380.00 |
303.20 |
0.9121 |
6580.00 |
313.20 |
0.4923 |
6530.00 |
313.20 |
0.5987 |
7340.00 |
313.20 |
0.7069 |
7560.00 |
313.20 |
0.8198 |
7670.00 |
313.20 |
0.9121 |
7920.00 |
323.20 |
0.4923 |
7720.00 |
323.20 |
0.5987 |
8580.00 |
323.20 |
0.7069 |
8950.00 |
323.20 |
0.8198 |
9120.00 |
323.20 |
0.9121 |
9200.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (1) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.2647 |
323.15 |
4670.00 |
0.2771 |
323.15 |
5120.00 |
0.3058 |
323.15 |
5340.00 |
0.3128 |
323.15 |
5780.00 |
0.4128 |
323.15 |
7070.00 |
0.4795 |
323.15 |
7690.00 |
0.5069 |
323.15 |
7960.00 |
0.5455 |
323.15 |
8160.00 |
0.6348 |
323.15 |
8440.00 |
0.6279 |
323.15 |
8460.00 |
0.6535 |
323.15 |
8510.00 |
0.6875 |
323.15 |
8690.00 |
0.2930 |
343.15 |
7010.00 |
0.3785 |
343.15 |
8050.00 |
0.4260 |
343.15 |
9040.00 |
0.4968 |
343.15 |
9980.00 |
0.6130 |
343.15 |
10980.00 |
0.6910 |
343.15 |
11500.00 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Temperature, K =
333.4 (Liquid)
Mole fraction of Carbon dioxide (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.4934 |
9020.00 |
0.6111 |
9950.00 |
0.8164 |
10660.00 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Mole fraction =
0.4998 (Liquid)
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
305.08 |
5580.00 |
313.08 |
6360.00 |
323.00 |
7420.00 |
333.10 |
9040.00 |
343.39 |
10110.00 |
352.97 |
11140.00 |
363.25 |
12060.00 |
372.50 |
12770.00 |
383.49 |
13470.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
313.15 |
0.3988 |
6320.00 |
313.15 |
0.5748 |
7340.00 |
313.15 |
0.6624 |
7620.00 |
313.15 |
0.7900 |
7880.00 |
323.15 |
0.3988 |
7220.00 |
323.15 |
0.5748 |
8570.00 |
323.15 |
0.6624 |
9040.00 |
323.15 |
0.7900 |
9310.00 |
333.15 |
0.3988 |
8150.00 |
333.15 |
0.5748 |
9780.00 |
333.15 |
0.6624 |
10400.00 |
333.15 |
0.7900 |
10630.00 |
343.15 |
0.7900 |
11910.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
313.15 |
0.2070 |
3150.00 |
313.15 |
0.4110 |
6110.00 |
313.15 |
0.6110 |
7650.00 |
313.15 |
0.8070 |
7760.00 |
333.15 |
0.2070 |
3960.00 |
333.15 |
0.4110 |
8240.00 |
333.15 |
0.6110 |
9700.00 |
333.15 |
0.8070 |
11100.00 |
313.15 |
0.4140 |
6440.00 |
313.15 |
0.6050 |
7380.00 |
333.15 |
0.4140 |
8010.00 |
333.15 |
0.6050 |
9520.00 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Temperature, K =
291.15 (Gas)
Mole fraction of Carbon dioxide (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.1840 |
2094.00 |
0.2270 |
2563.00 |
0.3040 |
3250.00 |
0.4550 |
4278.00 |
0.7280 |
4938.00 |
0.8380 |
5032.00 |
0.9510 |
5191.00 |
0.9830 |
5300.00 |
0.9960 |
5400.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol (2) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
333.20 |
0.2000 |
10630.00 |
333.20 |
0.3000 |
10470.00 |
333.20 |
0.4000 |
9910.00 |
333.20 |
0.5000 |
9240.00 |
333.20 |
0.6000 |
7820.00 |
343.20 |
0.3000 |
11730.00 |
343.20 |
0.4000 |
11130.00 |
343.20 |
0.5000 |
10270.00 |
343.20 |
0.6000 |
8770.00 |
343.20 |
0.7000 |
7000.00 |
353.20 |
0.3000 |
12750.00 |
353.20 |
0.4000 |
12130.00 |
353.20 |
0.5000 |
11290.00 |
353.20 |
0.6000 |
9630.00 |
353.20 |
0.7000 |
7710.00 |
363.20 |
0.3000 |
13660.00 |
363.20 |
0.4000 |
13150.00 |
363.20 |
0.5000 |
12110.00 |
363.20 |
0.6000 |
10330.00 |
363.20 |
0.7000 |
8370.00 |
373.20 |
0.3000 |
14240.00 |
373.20 |
0.4000 |
13980.00 |
373.20 |
0.5000 |
12760.00 |
373.20 |
0.6000 |
11050.00 |
373.20 |
0.7000 |
8920.00 |
383.20 |
0.4000 |
14450.00 |
383.20 |
0.5000 |
13420.00 |
383.20 |
0.6000 |
11530.00 |
383.20 |
0.7000 |
9390.00 |
393.20 |
0.4000 |
14820.00 |
393.20 |
0.5000 |
13960.00 |
393.20 |
0.6000 |
12130.00 |
393.20 |
0.7000 |
9840.00 |
393.20 |
0.8000 |
7050.00 |
403.20 |
0.4000 |
14910.00 |
403.20 |
0.5000 |
14330.00 |
403.20 |
0.6000 |
12580.00 |
403.20 |
0.8000 |
7410.00 |
413.20 |
0.4000 |
14840.00 |
413.20 |
0.5000 |
14530.00 |
413.20 |
0.6000 |
12960.00 |
413.20 |
0.7000 |
10580.00 |
413.20 |
0.8000 |
7780.00 |
423.20 |
0.5000 |
14440.00 |
423.20 |
0.6000 |
13310.00 |
433.20 |
0.5000 |
14150.00 |
433.20 |
0.6000 |
13420.00 |
433.20 |
0.7000 |
11240.00 |
433.20 |
0.8000 |
8420.00 |
443.20 |
0.6000 |
13310.00 |
443.20 |
0.7000 |
11510.00 |
453.20 |
0.6000 |
12850.00 |
453.20 |
0.7000 |
11620.00 |
453.20 |
0.8000 |
9130.00 |
463.20 |
0.7000 |
11580.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol (2) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
473.20 |
0.7000 |
11030.00 |
473.20 |
0.8000 |
9790.00 |
483.00 |
0.8000 |
9730.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (1) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0598 |
363.15 |
1120.00 |
0.0790 |
343.15 |
1440.00 |
0.0970 |
343.15 |
1840.00 |
0.1013 |
363.15 |
1970.00 |
0.1133 |
333.15 |
2150.00 |
0.1315 |
373.15 |
3400.00 |
0.1400 |
363.15 |
3180.00 |
0.1470 |
343.15 |
2930.00 |
0.1748 |
333.15 |
3280.00 |
0.2000 |
363.15 |
4630.00 |
0.2010 |
343.15 |
4080.00 |
0.2127 |
333.15 |
4090.00 |
0.2268 |
373.15 |
5720.00 |
0.2570 |
363.15 |
6010.00 |
0.2650 |
343.15 |
5150.00 |
0.2727 |
363.15 |
6270.00 |
0.3010 |
373.15 |
7410.00 |
0.3090 |
343.15 |
6200.00 |
0.3317 |
333.15 |
6060.00 |
0.3426 |
363.15 |
7820.00 |
0.3608 |
373.15 |
8890.00 |
0.3790 |
343.15 |
7300.00 |
0.3870 |
333.15 |
6830.00 |
0.3930 |
363.15 |
8970.00 |
0.4290 |
343.15 |
8270.00 |
0.4303 |
333.15 |
7590.00 |
0.4507 |
363.15 |
10040.00 |
0.4641 |
363.15 |
10210.00 |
0.4880 |
343.15 |
9350.00 |
0.4980 |
363.15 |
11050.00 |
0.5004 |
333.15 |
8600.00 |
0.5468 |
373.15 |
12360.00 |
0.5554 |
363.15 |
12120.00 |
0.6850 |
363.15 |
13750.00 |
0.6890 |
333.15 |
10500.00 |
0.7700 |
363.15 |
14150.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
293.15 |
0.0530 |
716.30 |
293.15 |
0.1273 |
1642.90 |
293.15 |
0.1848 |
2169.00 |
303.15 |
0.0622 |
930.60 |
303.15 |
0.1282 |
1970.30 |
303.15 |
0.2061 |
2903.50 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Temperature, K =
333.15 (Liquid)
Mole fraction of Carbon dioxide (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.3483 |
7050.00 |
0.5467 |
9470.00 |
0.7305 |
10470.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
291.15 |
0.1920 |
2450.00 |
291.15 |
0.2890 |
3140.00 |
291.15 |
0.3640 |
3810.00 |
291.15 |
0.4880 |
4590.00 |
291.15 |
0.5870 |
5020.00 |
291.15 |
0.7060 |
5180.00 |
291.15 |
0.8000 |
5300.00 |
291.15 |
0.8340 |
5350.00 |
291.15 |
0.8600 |
5400.00 |
291.15 |
0.8930 |
5430.00 |
291.15 |
0.9240 |
5450.00 |
291.15 |
0.9540 |
5490.00 |
291.15 |
0.9850 |
5530.00 |
298.17 |
0.1920 |
2790.00 |
298.17 |
0.2890 |
3820.00 |
298.17 |
0.3640 |
4370.00 |
298.17 |
0.4880 |
5050.00 |
298.17 |
0.5870 |
5490.00 |
298.17 |
0.7060 |
5750.00 |
298.17 |
0.8000 |
5900.00 |
298.17 |
0.8340 |
5950.00 |
298.17 |
0.8600 |
5970.00 |
298.17 |
0.8930 |
5980.00 |
298.17 |
0.9240 |
6080.00 |
298.17 |
0.9540 |
6220.00 |
298.17 |
0.9850 |
6370.00 |
303.12 |
0.1920 |
2990.00 |
303.12 |
0.2890 |
4080.00 |
303.12 |
0.3640 |
4770.00 |
303.12 |
0.4880 |
5630.00 |
303.12 |
0.5870 |
6010.00 |
303.12 |
0.7060 |
6330.00 |
303.12 |
0.8000 |
6480.00 |
303.12 |
0.8340 |
6530.00 |
303.12 |
0.8600 |
6570.00 |
303.12 |
0.8930 |
6620.00 |
303.12 |
0.9240 |
6670.00 |
303.12 |
0.9540 |
6810.00 |
303.12 |
0.9850 |
7040.00 |
308.11 |
0.1920 |
3270.00 |
308.11 |
0.2890 |
4520.00 |
308.11 |
0.3640 |
5170.00 |
308.11 |
0.4880 |
6160.00 |
308.11 |
0.5870 |
6620.00 |
308.11 |
0.7060 |
6900.00 |
308.11 |
0.8000 |
7080.00 |
308.11 |
0.8340 |
7130.00 |
308.11 |
0.8600 |
7180.00 |
308.11 |
0.8930 |
7190.00 |
308.11 |
0.9240 |
7300.00 |
308.11 |
0.9540 |
7440.00 |
308.11 |
0.9850 |
7690.00 |
313.14 |
0.1920 |
3510.00 |
313.14 |
0.2890 |
4860.00 |
313.14 |
0.3640 |
5610.00 |
313.14 |
0.4880 |
6680.00 |
313.14 |
0.5870 |
7180.00 |
313.14 |
0.7060 |
7580.00 |
313.14 |
0.8000 |
7780.00 |
313.14 |
0.8340 |
7830.00 |
313.14 |
0.8600 |
7880.00 |
313.14 |
0.8930 |
7960.00 |
313.14 |
0.9240 |
8050.00 |
313.14 |
0.9540 |
8180.00 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Temperature, K =
313.15 (Liquid)
Mole fraction of Carbon dioxide (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.1000 |
1970.00 |
0.2000 |
3491.00 |
0.3000 |
4802.00 |
0.4000 |
5913.00 |
0.5000 |
6763.00 |
0.6000 |
7291.00 |
0.7000 |
7595.00 |
0.8000 |
7769.00 |
0.8990 |
7960.00 |
0.9500 |
8175.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (1) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0555 |
293.15 |
750.00 |
0.0606 |
303.15 |
950.00 |
0.1292 |
293.15 |
1600.00 |
0.1355 |
303.15 |
2000.00 |
0.1755 |
293.15 |
2220.00 |
0.2185 |
303.15 |
3050.00 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Temperature, K =
291.15 (Liquid)
Mole fraction of Carbon dioxide (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0810 |
1176.00 |
0.1240 |
1493.00 |
0.1600 |
1942.00 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Temperature, K =
333.15 (Liquid)
Mole fraction of Carbon dioxide (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.1342 |
3050.00 |
0.2118 |
4543.00 |
0.2515 |
5318.00 |
0.3542 |
7138.00 |
0.4442 |
8515.00 |
0.5376 |
9561.00 |
0.7808 |
10406.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
313.15 |
0.2590 |
3840.00 |
313.15 |
0.2680 |
3990.00 |
313.15 |
0.5120 |
6130.00 |
313.15 |
0.5180 |
6340.00 |
313.15 |
0.7090 |
6670.00 |
313.15 |
0.7120 |
6880.00 |
333.15 |
0.2590 |
5070.00 |
333.15 |
0.2680 |
5190.00 |
333.15 |
0.5120 |
8420.00 |
333.15 |
0.5180 |
8530.00 |
333.15 |
0.7090 |
10050.00 |
333.15 |
0.7120 |
10010.00 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Temperature, K =
313 (Liquid)
Mole fraction of Carbon dioxide (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.1627 |
3040.00 |
0.2477 |
4310.00 |
0.3220 |
5170.00 |
0.4049 |
6050.00 |
0.4767 |
6110.00 |
0.6110 |
7090.00 |
0.5783 |
7080.00 |
0.6916 |
7390.00 |
0.7083 |
7650.00 |
0.8441 |
7950.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
303.20 |
0.4923 |
5570.00 |
303.20 |
0.5987 |
6020.00 |
303.20 |
0.7069 |
6260.00 |
303.20 |
0.8198 |
6380.00 |
303.20 |
0.9121 |
6580.00 |
313.20 |
0.4923 |
6530.00 |
313.20 |
0.5987 |
7340.00 |
313.20 |
0.7069 |
7560.00 |
313.20 |
0.8198 |
7670.00 |
313.20 |
0.9121 |
7920.00 |
323.20 |
0.4923 |
7720.00 |
323.20 |
0.5987 |
8580.00 |
323.20 |
0.7069 |
8950.00 |
323.20 |
0.8198 |
9120.00 |
323.20 |
0.9121 |
9200.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (1) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.2647 |
323.15 |
4670.00 |
0.2771 |
323.15 |
5120.00 |
0.3058 |
323.15 |
5340.00 |
0.3128 |
323.15 |
5780.00 |
0.4128 |
323.15 |
7070.00 |
0.4795 |
323.15 |
7690.00 |
0.5069 |
323.15 |
7960.00 |
0.5455 |
323.15 |
8160.00 |
0.6348 |
323.15 |
8440.00 |
0.6279 |
323.15 |
8460.00 |
0.6535 |
323.15 |
8510.00 |
0.6875 |
323.15 |
8690.00 |
0.2930 |
343.15 |
7010.00 |
0.3785 |
343.15 |
8050.00 |
0.4260 |
343.15 |
9040.00 |
0.4968 |
343.15 |
9980.00 |
0.6130 |
343.15 |
10980.00 |
0.6910 |
343.15 |
11500.00 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Temperature, K =
333.4 (Liquid)
Mole fraction of Carbon dioxide (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.4934 |
9020.00 |
0.6111 |
9950.00 |
0.8164 |
10660.00 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Mole fraction =
0.4998 (Liquid)
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
305.08 |
5580.00 |
313.08 |
6360.00 |
323.00 |
7420.00 |
333.10 |
9040.00 |
343.39 |
10110.00 |
352.97 |
11140.00 |
363.25 |
12060.00 |
372.50 |
12770.00 |
383.49 |
13470.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
313.15 |
0.3988 |
6320.00 |
313.15 |
0.5748 |
7340.00 |
313.15 |
0.6624 |
7620.00 |
313.15 |
0.7900 |
7880.00 |
323.15 |
0.3988 |
7220.00 |
323.15 |
0.5748 |
8570.00 |
323.15 |
0.6624 |
9040.00 |
323.15 |
0.7900 |
9310.00 |
333.15 |
0.3988 |
8150.00 |
333.15 |
0.5748 |
9780.00 |
333.15 |
0.6624 |
10400.00 |
333.15 |
0.7900 |
10630.00 |
343.15 |
0.7900 |
11910.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
313.15 |
0.2070 |
3150.00 |
313.15 |
0.4110 |
6110.00 |
313.15 |
0.6110 |
7650.00 |
313.15 |
0.8070 |
7760.00 |
333.15 |
0.2070 |
3960.00 |
333.15 |
0.4110 |
8240.00 |
333.15 |
0.6110 |
9700.00 |
333.15 |
0.8070 |
11100.00 |
313.15 |
0.4140 |
6440.00 |
313.15 |
0.6050 |
7380.00 |
333.15 |
0.4140 |
8010.00 |
333.15 |
0.6050 |
9520.00 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Temperature, K =
291.15 (Gas)
Mole fraction of Carbon dioxide (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.1840 |
2094.00 |
0.2270 |
2563.00 |
0.3040 |
3250.00 |
0.4550 |
4278.00 |
0.7280 |
4938.00 |
0.8380 |
5032.00 |
0.9510 |
5191.00 |
0.9830 |
5300.00 |
0.9960 |
5400.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol (2) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
333.20 |
0.2000 |
10630.00 |
333.20 |
0.3000 |
10470.00 |
333.20 |
0.4000 |
9910.00 |
333.20 |
0.5000 |
9240.00 |
333.20 |
0.6000 |
7820.00 |
343.20 |
0.3000 |
11730.00 |
343.20 |
0.4000 |
11130.00 |
343.20 |
0.5000 |
10270.00 |
343.20 |
0.6000 |
8770.00 |
343.20 |
0.7000 |
7000.00 |
353.20 |
0.3000 |
12750.00 |
353.20 |
0.4000 |
12130.00 |
353.20 |
0.5000 |
11290.00 |
353.20 |
0.6000 |
9630.00 |
353.20 |
0.7000 |
7710.00 |
363.20 |
0.3000 |
13660.00 |
363.20 |
0.4000 |
13150.00 |
363.20 |
0.5000 |
12110.00 |
363.20 |
0.6000 |
10330.00 |
363.20 |
0.7000 |
8370.00 |
373.20 |
0.3000 |
14240.00 |
373.20 |
0.4000 |
13980.00 |
373.20 |
0.5000 |
12760.00 |
373.20 |
0.6000 |
11050.00 |
373.20 |
0.7000 |
8920.00 |
383.20 |
0.4000 |
14450.00 |
383.20 |
0.5000 |
13420.00 |
383.20 |
0.6000 |
11530.00 |
383.20 |
0.7000 |
9390.00 |
393.20 |
0.4000 |
14820.00 |
393.20 |
0.5000 |
13960.00 |
393.20 |
0.6000 |
12130.00 |
393.20 |
0.7000 |
9840.00 |
393.20 |
0.8000 |
7050.00 |
403.20 |
0.4000 |
14910.00 |
403.20 |
0.5000 |
14330.00 |
403.20 |
0.6000 |
12580.00 |
403.20 |
0.8000 |
7410.00 |
413.20 |
0.4000 |
14840.00 |
413.20 |
0.5000 |
14530.00 |
413.20 |
0.6000 |
12960.00 |
413.20 |
0.7000 |
10580.00 |
413.20 |
0.8000 |
7780.00 |
423.20 |
0.5000 |
14440.00 |
423.20 |
0.6000 |
13310.00 |
433.20 |
0.5000 |
14150.00 |
433.20 |
0.6000 |
13420.00 |
433.20 |
0.7000 |
11240.00 |
433.20 |
0.8000 |
8420.00 |
443.20 |
0.6000 |
13310.00 |
443.20 |
0.7000 |
11510.00 |
453.20 |
0.6000 |
12850.00 |
453.20 |
0.7000 |
11620.00 |
453.20 |
0.8000 |
9130.00 |
463.20 |
0.7000 |
11580.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol (2) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
473.20 |
0.7000 |
11030.00 |
473.20 |
0.8000 |
9790.00 |
483.00 |
0.8000 |
9730.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (1) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0598 |
363.15 |
1120.00 |
0.0790 |
343.15 |
1440.00 |
0.0970 |
343.15 |
1840.00 |
0.1013 |
363.15 |
1970.00 |
0.1133 |
333.15 |
2150.00 |
0.1315 |
373.15 |
3400.00 |
0.1400 |
363.15 |
3180.00 |
0.1470 |
343.15 |
2930.00 |
0.1748 |
333.15 |
3280.00 |
0.2000 |
363.15 |
4630.00 |
0.2010 |
343.15 |
4080.00 |
0.2127 |
333.15 |
4090.00 |
0.2268 |
373.15 |
5720.00 |
0.2570 |
363.15 |
6010.00 |
0.2650 |
343.15 |
5150.00 |
0.2727 |
363.15 |
6270.00 |
0.3010 |
373.15 |
7410.00 |
0.3090 |
343.15 |
6200.00 |
0.3317 |
333.15 |
6060.00 |
0.3426 |
363.15 |
7820.00 |
0.3608 |
373.15 |
8890.00 |
0.3790 |
343.15 |
7300.00 |
0.3870 |
333.15 |
6830.00 |
0.3930 |
363.15 |
8970.00 |
0.4290 |
343.15 |
8270.00 |
0.4303 |
333.15 |
7590.00 |
0.4507 |
363.15 |
10040.00 |
0.4641 |
363.15 |
10210.00 |
0.4880 |
343.15 |
9350.00 |
0.4980 |
363.15 |
11050.00 |
0.5004 |
333.15 |
8600.00 |
0.5468 |
373.15 |
12360.00 |
0.5554 |
363.15 |
12120.00 |
0.6850 |
363.15 |
13750.00 |
0.6890 |
333.15 |
10500.00 |
0.7700 |
363.15 |
14150.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
293.15 |
0.0530 |
716.30 |
293.15 |
0.1273 |
1642.90 |
293.15 |
0.1848 |
2169.00 |
303.15 |
0.0622 |
930.60 |
303.15 |
0.1282 |
1970.30 |
303.15 |
0.2061 |
2903.50 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Temperature, K =
333.15 (Liquid)
Mole fraction of Carbon dioxide (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.3483 |
7050.00 |
0.5467 |
9470.00 |
0.7305 |
10470.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
291.15 |
0.1920 |
2450.00 |
291.15 |
0.2890 |
3140.00 |
291.15 |
0.3640 |
3810.00 |
291.15 |
0.4880 |
4590.00 |
291.15 |
0.5870 |
5020.00 |
291.15 |
0.7060 |
5180.00 |
291.15 |
0.8000 |
5300.00 |
291.15 |
0.8340 |
5350.00 |
291.15 |
0.8600 |
5400.00 |
291.15 |
0.8930 |
5430.00 |
291.15 |
0.9240 |
5450.00 |
291.15 |
0.9540 |
5490.00 |
291.15 |
0.9850 |
5530.00 |
298.17 |
0.1920 |
2790.00 |
298.17 |
0.2890 |
3820.00 |
298.17 |
0.3640 |
4370.00 |
298.17 |
0.4880 |
5050.00 |
298.17 |
0.5870 |
5490.00 |
298.17 |
0.7060 |
5750.00 |
298.17 |
0.8000 |
5900.00 |
298.17 |
0.8340 |
5950.00 |
298.17 |
0.8600 |
5970.00 |
298.17 |
0.8930 |
5980.00 |
298.17 |
0.9240 |
6080.00 |
298.17 |
0.9540 |
6220.00 |
298.17 |
0.9850 |
6370.00 |
303.12 |
0.1920 |
2990.00 |
303.12 |
0.2890 |
4080.00 |
303.12 |
0.3640 |
4770.00 |
303.12 |
0.4880 |
5630.00 |
303.12 |
0.5870 |
6010.00 |
303.12 |
0.7060 |
6330.00 |
303.12 |
0.8000 |
6480.00 |
303.12 |
0.8340 |
6530.00 |
303.12 |
0.8600 |
6570.00 |
303.12 |
0.8930 |
6620.00 |
303.12 |
0.9240 |
6670.00 |
303.12 |
0.9540 |
6810.00 |
303.12 |
0.9850 |
7040.00 |
308.11 |
0.1920 |
3270.00 |
308.11 |
0.2890 |
4520.00 |
308.11 |
0.3640 |
5170.00 |
308.11 |
0.4880 |
6160.00 |
308.11 |
0.5870 |
6620.00 |
308.11 |
0.7060 |
6900.00 |
308.11 |
0.8000 |
7080.00 |
308.11 |
0.8340 |
7130.00 |
308.11 |
0.8600 |
7180.00 |
308.11 |
0.8930 |
7190.00 |
308.11 |
0.9240 |
7300.00 |
308.11 |
0.9540 |
7440.00 |
308.11 |
0.9850 |
7690.00 |
313.14 |
0.1920 |
3510.00 |
313.14 |
0.2890 |
4860.00 |
313.14 |
0.3640 |
5610.00 |
313.14 |
0.4880 |
6680.00 |
313.14 |
0.5870 |
7180.00 |
313.14 |
0.7060 |
7580.00 |
313.14 |
0.8000 |
7780.00 |
313.14 |
0.8340 |
7830.00 |
313.14 |
0.8600 |
7880.00 |
313.14 |
0.8930 |
7960.00 |
313.14 |
0.9240 |
8050.00 |
313.14 |
0.9540 |
8180.00 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Temperature, K =
313.15 (Liquid)
Mole fraction of Carbon dioxide (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.1000 |
1970.00 |
0.2000 |
3491.00 |
0.3000 |
4802.00 |
0.4000 |
5913.00 |
0.5000 |
6763.00 |
0.6000 |
7291.00 |
0.7000 |
7595.00 |
0.8000 |
7769.00 |
0.8990 |
7960.00 |
0.9500 |
8175.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (1) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0555 |
293.15 |
750.00 |
0.0606 |
303.15 |
950.00 |
0.1292 |
293.15 |
1600.00 |
0.1355 |
303.15 |
2000.00 |
0.1755 |
293.15 |
2220.00 |
0.2185 |
303.15 |
3050.00 |
Interfacial tension, N/m
[ref]
Fixed |
Measured |
Pressure, kPa - Liquid mixture 1 |
Temperature, K - Liquid mixture 1 |
Interfacial tension, N/m - Liquid mixture 1 |
518.00 |
303.20 |
0.0198 |
1024.00 |
303.20 |
0.0187 |
2046.00 |
303.20 |
0.0162 |
3107.00 |
303.20 |
0.0134 |
4019.00 |
303.20 |
0.0107 |
4979.00 |
303.20 |
0.0078 |
6022.00 |
303.20 |
0.0037 |
517.00 |
313.20 |
0.0194 |
1053.00 |
313.20 |
0.0184 |
2024.00 |
313.20 |
0.0159 |
3041.00 |
313.20 |
0.0141 |
4027.00 |
313.20 |
0.0113 |
5105.00 |
313.20 |
0.0087 |
6036.00 |
313.20 |
0.0062 |
521.00 |
323.20 |
0.0187 |
1019.00 |
323.20 |
0.0176 |
2019.00 |
323.20 |
0.0155 |
3020.00 |
323.20 |
0.0138 |
4094.00 |
323.20 |
0.0115 |
5125.00 |
323.20 |
0.0094 |
5976.00 |
323.20 |
0.0075 |
515.00 |
333.20 |
0.0181 |
1005.00 |
333.20 |
0.0173 |
1993.00 |
333.20 |
0.0153 |
3029.00 |
333.20 |
0.0135 |
3996.00 |
333.20 |
0.0117 |
5078.00 |
333.20 |
0.0098 |
5984.00 |
333.20 |
0.0082 |
572.00 |
343.20 |
0.0170 |
1079.00 |
343.20 |
0.0162 |
2049.00 |
343.20 |
0.0147 |
3026.00 |
343.20 |
0.0131 |
4122.00 |
343.20 |
0.0114 |
5067.00 |
343.20 |
0.0099 |
6049.00 |
343.20 |
0.0083 |
500.00 |
353.20 |
0.0163 |
1009.00 |
353.20 |
0.0156 |
2049.00 |
353.20 |
0.0141 |
2997.00 |
353.20 |
0.0127 |
3999.00 |
353.20 |
0.0113 |
5052.00 |
353.20 |
0.0098 |
6128.00 |
353.20 |
0.0083 |
509.00 |
363.20 |
0.0157 |
994.00 |
363.20 |
0.0148 |
1973.00 |
363.20 |
0.0136 |
3043.00 |
363.20 |
0.0122 |
4024.00 |
363.20 |
0.0109 |
5047.00 |
363.20 |
0.0096 |
5775.00 |
363.20 |
0.0087 |
514.00 |
373.10 |
0.0146 |
1025.00 |
373.10 |
0.0139 |
2050.00 |
373.10 |
0.0128 |
2983.00 |
373.10 |
0.0117 |
4051.00 |
373.10 |
0.0104 |
5170.00 |
373.10 |
0.0091 |
5818.00 |
373.10 |
0.0083 |
Interfacial tension, N/m
[ref]
Fixed |
Measured |
Pressure, kPa - Liquid mixture 1 |
Temperature, K - Liquid mixture 1 |
Interfacial tension, N/m - Liquid mixture 1 |
518.00 |
303.20 |
0.0198 |
1024.00 |
303.20 |
0.0187 |
2046.00 |
303.20 |
0.0162 |
3107.00 |
303.20 |
0.0134 |
4019.00 |
303.20 |
0.0107 |
4979.00 |
303.20 |
0.0078 |
6022.00 |
303.20 |
0.0037 |
517.00 |
313.20 |
0.0194 |
1053.00 |
313.20 |
0.0184 |
2024.00 |
313.20 |
0.0159 |
3041.00 |
313.20 |
0.0141 |
4027.00 |
313.20 |
0.0113 |
5105.00 |
313.20 |
0.0087 |
6036.00 |
313.20 |
0.0062 |
521.00 |
323.20 |
0.0187 |
1019.00 |
323.20 |
0.0176 |
2019.00 |
323.20 |
0.0155 |
3020.00 |
323.20 |
0.0138 |
4094.00 |
323.20 |
0.0115 |
5125.00 |
323.20 |
0.0094 |
5976.00 |
323.20 |
0.0075 |
515.00 |
333.20 |
0.0181 |
1005.00 |
333.20 |
0.0173 |
1993.00 |
333.20 |
0.0153 |
3029.00 |
333.20 |
0.0135 |
3996.00 |
333.20 |
0.0117 |
5078.00 |
333.20 |
0.0098 |
5984.00 |
333.20 |
0.0082 |
572.00 |
343.20 |
0.0170 |
1079.00 |
343.20 |
0.0162 |
2049.00 |
343.20 |
0.0147 |
3026.00 |
343.20 |
0.0131 |
4122.00 |
343.20 |
0.0114 |
5067.00 |
343.20 |
0.0099 |
6049.00 |
343.20 |
0.0083 |
500.00 |
353.20 |
0.0163 |
1009.00 |
353.20 |
0.0156 |
2049.00 |
353.20 |
0.0141 |
2997.00 |
353.20 |
0.0127 |
3999.00 |
353.20 |
0.0113 |
5052.00 |
353.20 |
0.0098 |
6128.00 |
353.20 |
0.0083 |
509.00 |
363.20 |
0.0157 |
994.00 |
363.20 |
0.0148 |
1973.00 |
363.20 |
0.0136 |
3043.00 |
363.20 |
0.0122 |
4024.00 |
363.20 |
0.0109 |
5047.00 |
363.20 |
0.0096 |
5775.00 |
363.20 |
0.0087 |
514.00 |
373.10 |
0.0146 |
1025.00 |
373.10 |
0.0139 |
2050.00 |
373.10 |
0.0128 |
2983.00 |
373.10 |
0.0117 |
4051.00 |
373.10 |
0.0104 |
5170.00 |
373.10 |
0.0091 |
5818.00 |
373.10 |
0.0083 |
Critical density, kg/m3
[ref]
Mole fraction of Carbon dioxide (1) - Liquid |
Critical density, kg/m3 - Liquid |
0.5300 |
410.0 |
0.7200 |
460.0 |
0.8800 |
510.0 |
0.8900 |
550.0 |
Critical density, kg/m3
[ref]
Mole fraction of Carbon dioxide (1) - Liquid |
Critical density, kg/m3 - Liquid |
0.5300 |
410.0 |
0.7200 |
460.0 |
0.8800 |
510.0 |
0.8900 |
550.0 |
Mass density, kg/m3
[ref]
Operational condition: Temperature, K =
291.15 (Gas)
Mole fraction of Carbon dioxide (1) - Liquid |
Mass density, kg/m3 - Gas |
0.1840 |
44.1 |
0.2270 |
56.0 |
0.3040 |
75.4 |
0.4550 |
112.0 |
0.7280 |
146.4 |
0.8380 |
152.2 |
0.9510 |
162.6 |
0.9830 |
169.8 |
0.9960 |
178.2 |
Mass density, kg/m3
[ref]
Operational condition: Temperature, K =
291.15 (Gas)
Mole fraction of Carbon dioxide (1) - Liquid |
Mass density, kg/m3 - Gas |
0.1840 |
44.1 |
0.2270 |
56.0 |
0.3040 |
75.4 |
0.4550 |
112.0 |
0.7280 |
146.4 |
0.8380 |
152.2 |
0.9510 |
162.6 |
0.9830 |
169.8 |
0.9960 |
178.2 |
Mass density, kg/m3
[ref]
Operational condition: Temperature, K =
313.15 (Liquid)
Fixed |
Measured |
Pressure, kPa - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Mass density, kg/m3 - Liquid |
200.00 |
0.0000 |
770.7 |
1830.00 |
0.1044 |
788.8 |
3020.00 |
0.1746 |
795.7 |
3760.00 |
0.2221 |
798.4 |
5200.00 |
0.3150 |
806.9 |
Mass density, kg/m3
[ref]
Operational condition: Temperature, K =
313.15 (Liquid)
Fixed |
Measured |
Pressure, kPa - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Mass density, kg/m3 - Liquid |
10000.00 |
0.0000 |
785.3 |
10000.00 |
0.1044 |
798.2 |
10000.00 |
0.1746 |
805.0 |
10000.00 |
0.2221 |
807.8 |
10000.00 |
0.3150 |
814.0 |
20000.00 |
0.0000 |
794.4 |
20000.00 |
0.1044 |
808.6 |
20000.00 |
0.1746 |
818.1 |
20000.00 |
0.2221 |
820.2 |
20000.00 |
0.3150 |
830.6 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Mass density, kg/m3 - Liquid |
303.20 |
1140.00 |
0.0760 |
793.0 |
303.20 |
2130.00 |
0.1510 |
802.0 |
303.20 |
3080.00 |
0.2380 |
812.0 |
303.20 |
3940.00 |
0.2950 |
821.0 |
303.20 |
4980.00 |
0.4140 |
832.0 |
303.20 |
5940.00 |
0.5890 |
840.0 |
323.20 |
1020.00 |
0.0490 |
769.0 |
323.20 |
1980.00 |
0.1010 |
775.0 |
323.20 |
3060.00 |
0.1610 |
782.0 |
323.20 |
4020.00 |
0.2180 |
787.0 |
323.20 |
5110.00 |
0.2820 |
794.0 |
323.20 |
6080.00 |
0.3580 |
798.0 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Pressure, kPa - Liquid |
Mass density, kg/m3 - Liquid |
308.00 |
0.1000 |
5000.00 |
792.1 |
308.00 |
0.1000 |
6000.00 |
793.0 |
308.00 |
0.1000 |
7000.00 |
793.7 |
308.00 |
0.1000 |
8000.00 |
794.5 |
308.00 |
0.1000 |
9000.00 |
795.3 |
308.00 |
0.1000 |
10000.00 |
796.2 |
308.00 |
0.1000 |
11000.00 |
797.1 |
308.00 |
0.1000 |
12000.00 |
798.0 |
308.00 |
0.1000 |
13000.00 |
798.8 |
308.00 |
0.1000 |
14000.00 |
799.7 |
308.00 |
0.1000 |
15000.00 |
800.5 |
308.00 |
0.1000 |
16000.00 |
801.4 |
308.00 |
0.1000 |
17000.00 |
802.3 |
308.00 |
0.1000 |
18000.00 |
803.2 |
308.00 |
0.1000 |
19000.00 |
804.2 |
308.00 |
0.1000 |
20000.00 |
805.1 |
308.00 |
0.1000 |
21000.00 |
806.0 |
308.00 |
0.1000 |
22000.00 |
807.0 |
308.00 |
0.1000 |
23000.00 |
807.9 |
308.00 |
0.1000 |
24000.00 |
808.9 |
308.00 |
0.1000 |
25000.00 |
809.9 |
308.00 |
0.1000 |
26000.00 |
810.9 |
308.00 |
0.1000 |
27000.00 |
811.9 |
308.00 |
0.1000 |
28000.00 |
812.9 |
308.00 |
0.1000 |
29000.00 |
813.7 |
308.00 |
0.1000 |
30000.00 |
815.0 |
308.00 |
0.2000 |
5000.00 |
804.3 |
308.00 |
0.2000 |
6000.00 |
805.1 |
308.00 |
0.2000 |
7000.00 |
806.1 |
308.00 |
0.2000 |
8000.00 |
807.1 |
308.00 |
0.2000 |
9000.00 |
808.2 |
308.00 |
0.2000 |
10000.00 |
809.2 |
308.00 |
0.2000 |
11000.00 |
810.3 |
308.00 |
0.2000 |
12000.00 |
811.4 |
308.00 |
0.2000 |
13000.00 |
812.4 |
308.00 |
0.2000 |
14000.00 |
813.5 |
308.00 |
0.2000 |
15000.00 |
814.6 |
308.00 |
0.2000 |
16000.00 |
815.6 |
308.00 |
0.2000 |
17000.00 |
816.7 |
308.00 |
0.2000 |
18000.00 |
817.8 |
308.00 |
0.2000 |
19000.00 |
818.8 |
308.00 |
0.2000 |
20000.00 |
819.9 |
308.00 |
0.2000 |
21000.00 |
821.0 |
308.00 |
0.2000 |
22000.00 |
822.2 |
308.00 |
0.2000 |
23000.00 |
823.3 |
308.00 |
0.2000 |
24000.00 |
824.4 |
308.00 |
0.2000 |
25000.00 |
825.6 |
308.00 |
0.2000 |
26000.00 |
826.7 |
308.00 |
0.2000 |
27000.00 |
827.9 |
308.00 |
0.2000 |
28000.00 |
829.0 |
308.00 |
0.2000 |
29000.00 |
830.2 |
308.00 |
0.2000 |
30000.00 |
831.5 |
308.00 |
0.3000 |
6000.00 |
814.6 |
308.00 |
0.3000 |
7000.00 |
815.8 |
308.00 |
0.3000 |
8000.00 |
817.2 |
308.00 |
0.3000 |
9000.00 |
818.5 |
308.00 |
0.3000 |
10000.00 |
819.9 |
308.00 |
0.3000 |
11000.00 |
821.2 |
308.00 |
0.3000 |
12000.00 |
822.6 |
308.00 |
0.3000 |
13000.00 |
823.9 |
308.00 |
0.3000 |
14000.00 |
825.2 |
308.00 |
0.3000 |
15000.00 |
826.5 |
308.00 |
0.3000 |
16000.00 |
827.8 |
308.00 |
0.3000 |
17000.00 |
829.1 |
308.00 |
0.3000 |
18000.00 |
830.3 |
308.00 |
0.3000 |
19000.00 |
831.6 |
308.00 |
0.3000 |
20000.00 |
832.9 |
308.00 |
0.3000 |
21000.00 |
834.3 |
308.00 |
0.3000 |
22000.00 |
835.5 |
308.00 |
0.3000 |
23000.00 |
836.9 |
308.00 |
0.3000 |
24000.00 |
838.2 |
308.00 |
0.3000 |
25000.00 |
839.5 |
308.00 |
0.3000 |
26000.00 |
840.8 |
308.00 |
0.3000 |
27000.00 |
842.2 |
308.00 |
0.3000 |
28000.00 |
843.5 |
308.00 |
0.3000 |
29000.00 |
844.9 |
308.00 |
0.3000 |
30000.00 |
846.3 |
308.00 |
0.4000 |
7000.00 |
822.9 |
308.00 |
0.4000 |
8000.00 |
824.4 |
308.00 |
0.4000 |
9000.00 |
826.8 |
308.00 |
0.4000 |
10000.00 |
828.6 |
308.00 |
0.4000 |
11000.00 |
830.3 |
308.00 |
0.4000 |
12000.00 |
832.0 |
308.00 |
0.4000 |
13000.00 |
833.8 |
308.00 |
0.4000 |
14000.00 |
835.4 |
308.00 |
0.4000 |
15000.00 |
837.0 |
308.00 |
0.4000 |
16000.00 |
838.6 |
308.00 |
0.4000 |
17000.00 |
840.2 |
308.00 |
0.4000 |
18000.00 |
841.7 |
308.00 |
0.4000 |
19000.00 |
843.3 |
308.00 |
0.4000 |
20000.00 |
844.9 |
308.00 |
0.4000 |
21000.00 |
846.4 |
308.00 |
0.4000 |
22000.00 |
848.0 |
308.00 |
0.4000 |
23000.00 |
849.5 |
308.00 |
0.4000 |
24000.00 |
851.1 |
308.00 |
0.4000 |
25000.00 |
852.6 |
308.00 |
0.4000 |
26000.00 |
854.2 |
308.00 |
0.4000 |
27000.00 |
855.7 |
308.00 |
0.4000 |
28000.00 |
857.3 |
308.00 |
0.4000 |
29000.00 |
858.9 |
308.00 |
0.4000 |
30000.00 |
860.5 |
308.00 |
0.5000 |
7000.00 |
827.6 |
308.00 |
0.5000 |
8000.00 |
828.0 |
308.00 |
0.5000 |
9000.00 |
830.5 |
308.00 |
0.5000 |
10000.00 |
833.0 |
308.00 |
0.5000 |
11000.00 |
835.3 |
308.00 |
0.5000 |
12000.00 |
837.5 |
308.00 |
0.5000 |
13000.00 |
839.7 |
308.00 |
0.5000 |
14000.00 |
841.9 |
308.00 |
0.5000 |
15000.00 |
844.0 |
308.00 |
0.5000 |
16000.00 |
846.1 |
308.00 |
0.5000 |
17000.00 |
848.2 |
308.00 |
0.5000 |
18000.00 |
850.2 |
308.00 |
0.5000 |
19000.00 |
852.2 |
308.00 |
0.5000 |
20000.00 |
854.1 |
308.00 |
0.5000 |
21000.00 |
856.1 |
308.00 |
0.5000 |
22000.00 |
858.0 |
308.00 |
0.5000 |
23000.00 |
859.9 |
308.00 |
0.5000 |
24000.00 |
861.7 |
308.00 |
0.5000 |
25000.00 |
863.5 |
308.00 |
0.5000 |
26000.00 |
865.5 |
308.00 |
0.5000 |
27000.00 |
867.3 |
308.00 |
0.5000 |
28000.00 |
869.1 |
308.00 |
0.5000 |
29000.00 |
870.9 |
308.00 |
0.5000 |
30000.00 |
872.8 |
323.00 |
0.1000 |
10000.00 |
786.8 |
323.00 |
0.1000 |
20000.00 |
797.2 |
323.00 |
0.1000 |
30000.00 |
807.5 |
323.00 |
0.2000 |
10000.00 |
804.2 |
323.00 |
0.2000 |
20000.00 |
817.0 |
323.00 |
0.2000 |
30000.00 |
829.1 |
323.00 |
0.3000 |
10000.00 |
811.3 |
323.00 |
0.3000 |
20000.00 |
831.8 |
323.00 |
0.3000 |
30000.00 |
849.6 |
Mass density, kg/m3
[ref]
Operational condition: Temperature, K =
291.15 (Liquid)
Mole fraction of Carbon dioxide (1) - Liquid |
Mass density, kg/m3 - Liquid |
0.1840 |
819.5 |
0.2270 |
826.4 |
0.3040 |
836.8 |
0.4550 |
855.1 |
0.7280 |
865.9 |
0.8380 |
856.5 |
0.9510 |
828.0 |
0.9830 |
811.3 |
0.9960 |
800.6 |
Mass density, kg/m3
[ref]
Operational condition: Temperature, K =
313.15 (Fluid (supercritical or subcritical phases))
Fixed |
Measured |
Pressure, kPa - Fluid (supercritical or subcritical phases) |
Mole fraction of Carbon dioxide (1) - Fluid (supercritical or subcritical phases) |
Mass density, kg/m3 - Fluid (supercritical or subcritical phases) |
1000.00 |
0.0000 |
773.1 |
1000.00 |
1.0000 |
17.9 |
2000.00 |
0.0000 |
773.9 |
2000.00 |
0.1000 |
787.2 |
2000.00 |
1.0000 |
37.1 |
3000.00 |
0.0000 |
774.8 |
3000.00 |
0.1000 |
788.2 |
3000.00 |
1.0000 |
58.7 |
4000.00 |
0.0000 |
775.5 |
4000.00 |
0.1000 |
789.2 |
4000.00 |
0.2000 |
799.4 |
4000.00 |
1.0000 |
83.5 |
5000.00 |
0.0000 |
776.4 |
5000.00 |
0.1000 |
790.2 |
5000.00 |
0.2000 |
800.6 |
5000.00 |
1.0000 |
112.7 |
6000.00 |
0.0000 |
777.2 |
6000.00 |
0.1000 |
791.1 |
6000.00 |
0.2000 |
801.9 |
6000.00 |
0.3000 |
811.2 |
6000.00 |
0.4000 |
816.6 |
6000.00 |
1.0000 |
148.8 |
7000.00 |
0.0000 |
778.0 |
7000.00 |
0.1000 |
792.1 |
7000.00 |
0.2000 |
803.1 |
7000.00 |
0.3000 |
812.7 |
7000.00 |
0.4000 |
818.7 |
7000.00 |
0.5000 |
821.1 |
7000.00 |
1.0000 |
197.3 |
8000.00 |
0.0000 |
778.8 |
8000.00 |
0.1000 |
793.1 |
8000.00 |
0.2000 |
804.2 |
8000.00 |
0.3000 |
814.3 |
8000.00 |
0.4000 |
820.8 |
8000.00 |
0.5000 |
824.0 |
8000.00 |
0.6000 |
818.8 |
8000.00 |
0.7000 |
804.5 |
8000.00 |
0.8000 |
771.1 |
8000.00 |
1.0000 |
276.7 |
9000.00 |
0.0000 |
779.6 |
9000.00 |
0.1000 |
794.0 |
9000.00 |
0.2000 |
805.3 |
9000.00 |
0.3000 |
815.7 |
9000.00 |
0.4000 |
822.8 |
9000.00 |
0.5000 |
826.8 |
9000.00 |
0.6000 |
823.0 |
9000.00 |
0.7000 |
811.5 |
9000.00 |
0.8000 |
784.8 |
9000.00 |
0.8990 |
729.1 |
9000.00 |
0.9500 |
667.0 |
9000.00 |
1.0000 |
483.4 |
10000.00 |
0.0000 |
780.4 |
10000.00 |
0.1000 |
795.0 |
10000.00 |
0.2000 |
806.6 |
10000.00 |
0.3000 |
817.2 |
10000.00 |
0.4000 |
824.7 |
10000.00 |
0.5000 |
829.4 |
10000.00 |
0.6000 |
827.0 |
10000.00 |
0.7000 |
817.8 |
10000.00 |
0.8000 |
795.8 |
10000.00 |
0.8990 |
752.3 |
10000.00 |
0.9500 |
709.8 |
10000.00 |
1.0000 |
627.4 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mass density, kg/m3 - Liquid |
313.20 |
100.00 |
768.9 |
313.20 |
2050.00 |
785.8 |
313.20 |
4400.00 |
802.6 |
313.20 |
5860.00 |
813.0 |
313.20 |
6560.00 |
817.2 |
313.20 |
7270.00 |
813.7 |
313.20 |
7840.00 |
793.5 |
313.20 |
8170.00 |
762.5 |
313.20 |
8510.00 |
734.3 |
328.20 |
110.00 |
752.7 |
328.20 |
2200.00 |
766.2 |
328.20 |
4380.00 |
777.2 |
328.20 |
5860.00 |
784.2 |
328.20 |
6440.00 |
786.5 |
328.20 |
7130.00 |
788.3 |
328.20 |
7810.00 |
789.2 |
328.20 |
8170.00 |
788.7 |
328.20 |
8520.00 |
786.6 |
328.20 |
8860.00 |
782.4 |
328.20 |
9210.00 |
774.6 |
328.20 |
9560.00 |
755.2 |
328.20 |
9900.00 |
730.1 |
343.20 |
160.00 |
732.4 |
343.20 |
2270.00 |
742.0 |
343.20 |
4360.00 |
750.5 |
343.20 |
5820.00 |
756.6 |
343.20 |
7170.00 |
758.7 |
343.20 |
7850.00 |
760.0 |
343.20 |
8540.00 |
759.1 |
343.20 |
9240.00 |
757.3 |
343.20 |
9930.00 |
752.8 |
343.20 |
10610.00 |
742.3 |
343.20 |
11220.00 |
726.3 |
Mass density, kg/m3
[ref]
Operational condition: Temperature, K =
313.15 (Liquid)
Fixed |
Measured |
Pressure, kPa - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Mass density, kg/m3 - Liquid |
200.00 |
0.0000 |
770.7 |
1830.00 |
0.1044 |
788.8 |
3020.00 |
0.1746 |
795.7 |
3760.00 |
0.2221 |
798.4 |
5200.00 |
0.3150 |
806.9 |
Mass density, kg/m3
[ref]
Operational condition: Temperature, K =
313.15 (Liquid)
Fixed |
Measured |
Pressure, kPa - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Mass density, kg/m3 - Liquid |
10000.00 |
0.0000 |
785.3 |
10000.00 |
0.1044 |
798.2 |
10000.00 |
0.1746 |
805.0 |
10000.00 |
0.2221 |
807.8 |
10000.00 |
0.3150 |
814.0 |
20000.00 |
0.0000 |
794.4 |
20000.00 |
0.1044 |
808.6 |
20000.00 |
0.1746 |
818.1 |
20000.00 |
0.2221 |
820.2 |
20000.00 |
0.3150 |
830.6 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Mass density, kg/m3 - Liquid |
303.20 |
1140.00 |
0.0760 |
793.0 |
303.20 |
2130.00 |
0.1510 |
802.0 |
303.20 |
3080.00 |
0.2380 |
812.0 |
303.20 |
3940.00 |
0.2950 |
821.0 |
303.20 |
4980.00 |
0.4140 |
832.0 |
303.20 |
5940.00 |
0.5890 |
840.0 |
323.20 |
1020.00 |
0.0490 |
769.0 |
323.20 |
1980.00 |
0.1010 |
775.0 |
323.20 |
3060.00 |
0.1610 |
782.0 |
323.20 |
4020.00 |
0.2180 |
787.0 |
323.20 |
5110.00 |
0.2820 |
794.0 |
323.20 |
6080.00 |
0.3580 |
798.0 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Pressure, kPa - Liquid |
Mass density, kg/m3 - Liquid |
308.00 |
0.1000 |
5000.00 |
792.1 |
308.00 |
0.1000 |
6000.00 |
793.0 |
308.00 |
0.1000 |
7000.00 |
793.7 |
308.00 |
0.1000 |
8000.00 |
794.5 |
308.00 |
0.1000 |
9000.00 |
795.3 |
308.00 |
0.1000 |
10000.00 |
796.2 |
308.00 |
0.1000 |
11000.00 |
797.1 |
308.00 |
0.1000 |
12000.00 |
798.0 |
308.00 |
0.1000 |
13000.00 |
798.8 |
308.00 |
0.1000 |
14000.00 |
799.7 |
308.00 |
0.1000 |
15000.00 |
800.5 |
308.00 |
0.1000 |
16000.00 |
801.4 |
308.00 |
0.1000 |
17000.00 |
802.3 |
308.00 |
0.1000 |
18000.00 |
803.2 |
308.00 |
0.1000 |
19000.00 |
804.2 |
308.00 |
0.1000 |
20000.00 |
805.1 |
308.00 |
0.1000 |
21000.00 |
806.0 |
308.00 |
0.1000 |
22000.00 |
807.0 |
308.00 |
0.1000 |
23000.00 |
807.9 |
308.00 |
0.1000 |
24000.00 |
808.9 |
308.00 |
0.1000 |
25000.00 |
809.9 |
308.00 |
0.1000 |
26000.00 |
810.9 |
308.00 |
0.1000 |
27000.00 |
811.9 |
308.00 |
0.1000 |
28000.00 |
812.9 |
308.00 |
0.1000 |
29000.00 |
813.7 |
308.00 |
0.1000 |
30000.00 |
815.0 |
308.00 |
0.2000 |
5000.00 |
804.3 |
308.00 |
0.2000 |
6000.00 |
805.1 |
308.00 |
0.2000 |
7000.00 |
806.1 |
308.00 |
0.2000 |
8000.00 |
807.1 |
308.00 |
0.2000 |
9000.00 |
808.2 |
308.00 |
0.2000 |
10000.00 |
809.2 |
308.00 |
0.2000 |
11000.00 |
810.3 |
308.00 |
0.2000 |
12000.00 |
811.4 |
308.00 |
0.2000 |
13000.00 |
812.4 |
308.00 |
0.2000 |
14000.00 |
813.5 |
308.00 |
0.2000 |
15000.00 |
814.6 |
308.00 |
0.2000 |
16000.00 |
815.6 |
308.00 |
0.2000 |
17000.00 |
816.7 |
308.00 |
0.2000 |
18000.00 |
817.8 |
308.00 |
0.2000 |
19000.00 |
818.8 |
308.00 |
0.2000 |
20000.00 |
819.9 |
308.00 |
0.2000 |
21000.00 |
821.0 |
308.00 |
0.2000 |
22000.00 |
822.2 |
308.00 |
0.2000 |
23000.00 |
823.3 |
308.00 |
0.2000 |
24000.00 |
824.4 |
308.00 |
0.2000 |
25000.00 |
825.6 |
308.00 |
0.2000 |
26000.00 |
826.7 |
308.00 |
0.2000 |
27000.00 |
827.9 |
308.00 |
0.2000 |
28000.00 |
829.0 |
308.00 |
0.2000 |
29000.00 |
830.2 |
308.00 |
0.2000 |
30000.00 |
831.5 |
308.00 |
0.3000 |
6000.00 |
814.6 |
308.00 |
0.3000 |
7000.00 |
815.8 |
308.00 |
0.3000 |
8000.00 |
817.2 |
308.00 |
0.3000 |
9000.00 |
818.5 |
308.00 |
0.3000 |
10000.00 |
819.9 |
308.00 |
0.3000 |
11000.00 |
821.2 |
308.00 |
0.3000 |
12000.00 |
822.6 |
308.00 |
0.3000 |
13000.00 |
823.9 |
308.00 |
0.3000 |
14000.00 |
825.2 |
308.00 |
0.3000 |
15000.00 |
826.5 |
308.00 |
0.3000 |
16000.00 |
827.8 |
308.00 |
0.3000 |
17000.00 |
829.1 |
308.00 |
0.3000 |
18000.00 |
830.3 |
308.00 |
0.3000 |
19000.00 |
831.6 |
308.00 |
0.3000 |
20000.00 |
832.9 |
308.00 |
0.3000 |
21000.00 |
834.3 |
308.00 |
0.3000 |
22000.00 |
835.5 |
308.00 |
0.3000 |
23000.00 |
836.9 |
308.00 |
0.3000 |
24000.00 |
838.2 |
308.00 |
0.3000 |
25000.00 |
839.5 |
308.00 |
0.3000 |
26000.00 |
840.8 |
308.00 |
0.3000 |
27000.00 |
842.2 |
308.00 |
0.3000 |
28000.00 |
843.5 |
308.00 |
0.3000 |
29000.00 |
844.9 |
308.00 |
0.3000 |
30000.00 |
846.3 |
308.00 |
0.4000 |
7000.00 |
822.9 |
308.00 |
0.4000 |
8000.00 |
824.4 |
308.00 |
0.4000 |
9000.00 |
826.8 |
308.00 |
0.4000 |
10000.00 |
828.6 |
308.00 |
0.4000 |
11000.00 |
830.3 |
308.00 |
0.4000 |
12000.00 |
832.0 |
308.00 |
0.4000 |
13000.00 |
833.8 |
308.00 |
0.4000 |
14000.00 |
835.4 |
308.00 |
0.4000 |
15000.00 |
837.0 |
308.00 |
0.4000 |
16000.00 |
838.6 |
308.00 |
0.4000 |
17000.00 |
840.2 |
308.00 |
0.4000 |
18000.00 |
841.7 |
308.00 |
0.4000 |
19000.00 |
843.3 |
308.00 |
0.4000 |
20000.00 |
844.9 |
308.00 |
0.4000 |
21000.00 |
846.4 |
308.00 |
0.4000 |
22000.00 |
848.0 |
308.00 |
0.4000 |
23000.00 |
849.5 |
308.00 |
0.4000 |
24000.00 |
851.1 |
308.00 |
0.4000 |
25000.00 |
852.6 |
308.00 |
0.4000 |
26000.00 |
854.2 |
308.00 |
0.4000 |
27000.00 |
855.7 |
308.00 |
0.4000 |
28000.00 |
857.3 |
308.00 |
0.4000 |
29000.00 |
858.9 |
308.00 |
0.4000 |
30000.00 |
860.5 |
308.00 |
0.5000 |
7000.00 |
827.6 |
308.00 |
0.5000 |
8000.00 |
828.0 |
308.00 |
0.5000 |
9000.00 |
830.5 |
308.00 |
0.5000 |
10000.00 |
833.0 |
308.00 |
0.5000 |
11000.00 |
835.3 |
308.00 |
0.5000 |
12000.00 |
837.5 |
308.00 |
0.5000 |
13000.00 |
839.7 |
308.00 |
0.5000 |
14000.00 |
841.9 |
308.00 |
0.5000 |
15000.00 |
844.0 |
308.00 |
0.5000 |
16000.00 |
846.1 |
308.00 |
0.5000 |
17000.00 |
848.2 |
308.00 |
0.5000 |
18000.00 |
850.2 |
308.00 |
0.5000 |
19000.00 |
852.2 |
308.00 |
0.5000 |
20000.00 |
854.1 |
308.00 |
0.5000 |
21000.00 |
856.1 |
308.00 |
0.5000 |
22000.00 |
858.0 |
308.00 |
0.5000 |
23000.00 |
859.9 |
308.00 |
0.5000 |
24000.00 |
861.7 |
308.00 |
0.5000 |
25000.00 |
863.5 |
308.00 |
0.5000 |
26000.00 |
865.5 |
308.00 |
0.5000 |
27000.00 |
867.3 |
308.00 |
0.5000 |
28000.00 |
869.1 |
308.00 |
0.5000 |
29000.00 |
870.9 |
308.00 |
0.5000 |
30000.00 |
872.8 |
323.00 |
0.1000 |
10000.00 |
786.8 |
323.00 |
0.1000 |
20000.00 |
797.2 |
323.00 |
0.1000 |
30000.00 |
807.5 |
323.00 |
0.2000 |
10000.00 |
804.2 |
323.00 |
0.2000 |
20000.00 |
817.0 |
323.00 |
0.2000 |
30000.00 |
829.1 |
323.00 |
0.3000 |
10000.00 |
811.3 |
323.00 |
0.3000 |
20000.00 |
831.8 |
323.00 |
0.3000 |
30000.00 |
849.6 |
Mass density, kg/m3
[ref]
Operational condition: Temperature, K =
291.15 (Liquid)
Mole fraction of Carbon dioxide (1) - Liquid |
Mass density, kg/m3 - Liquid |
0.1840 |
819.5 |
0.2270 |
826.4 |
0.3040 |
836.8 |
0.4550 |
855.1 |
0.7280 |
865.9 |
0.8380 |
856.5 |
0.9510 |
828.0 |
0.9830 |
811.3 |
0.9960 |
800.6 |
Mass density, kg/m3
[ref]
Operational condition: Temperature, K =
313.15 (Fluid (supercritical or subcritical phases))
Fixed |
Measured |
Pressure, kPa - Fluid (supercritical or subcritical phases) |
Mole fraction of Carbon dioxide (1) - Fluid (supercritical or subcritical phases) |
Mass density, kg/m3 - Fluid (supercritical or subcritical phases) |
1000.00 |
0.0000 |
773.1 |
1000.00 |
1.0000 |
17.9 |
2000.00 |
0.0000 |
773.9 |
2000.00 |
0.1000 |
787.2 |
2000.00 |
1.0000 |
37.1 |
3000.00 |
0.0000 |
774.8 |
3000.00 |
0.1000 |
788.2 |
3000.00 |
1.0000 |
58.7 |
4000.00 |
0.0000 |
775.5 |
4000.00 |
0.1000 |
789.2 |
4000.00 |
0.2000 |
799.4 |
4000.00 |
1.0000 |
83.5 |
5000.00 |
0.0000 |
776.4 |
5000.00 |
0.1000 |
790.2 |
5000.00 |
0.2000 |
800.6 |
5000.00 |
1.0000 |
112.7 |
6000.00 |
0.0000 |
777.2 |
6000.00 |
0.1000 |
791.1 |
6000.00 |
0.2000 |
801.9 |
6000.00 |
0.3000 |
811.2 |
6000.00 |
0.4000 |
816.6 |
6000.00 |
1.0000 |
148.8 |
7000.00 |
0.0000 |
778.0 |
7000.00 |
0.1000 |
792.1 |
7000.00 |
0.2000 |
803.1 |
7000.00 |
0.3000 |
812.7 |
7000.00 |
0.4000 |
818.7 |
7000.00 |
0.5000 |
821.1 |
7000.00 |
1.0000 |
197.3 |
8000.00 |
0.0000 |
778.8 |
8000.00 |
0.1000 |
793.1 |
8000.00 |
0.2000 |
804.2 |
8000.00 |
0.3000 |
814.3 |
8000.00 |
0.4000 |
820.8 |
8000.00 |
0.5000 |
824.0 |
8000.00 |
0.6000 |
818.8 |
8000.00 |
0.7000 |
804.5 |
8000.00 |
0.8000 |
771.1 |
8000.00 |
1.0000 |
276.7 |
9000.00 |
0.0000 |
779.6 |
9000.00 |
0.1000 |
794.0 |
9000.00 |
0.2000 |
805.3 |
9000.00 |
0.3000 |
815.7 |
9000.00 |
0.4000 |
822.8 |
9000.00 |
0.5000 |
826.8 |
9000.00 |
0.6000 |
823.0 |
9000.00 |
0.7000 |
811.5 |
9000.00 |
0.8000 |
784.8 |
9000.00 |
0.8990 |
729.1 |
9000.00 |
0.9500 |
667.0 |
9000.00 |
1.0000 |
483.4 |
10000.00 |
0.0000 |
780.4 |
10000.00 |
0.1000 |
795.0 |
10000.00 |
0.2000 |
806.6 |
10000.00 |
0.3000 |
817.2 |
10000.00 |
0.4000 |
824.7 |
10000.00 |
0.5000 |
829.4 |
10000.00 |
0.6000 |
827.0 |
10000.00 |
0.7000 |
817.8 |
10000.00 |
0.8000 |
795.8 |
10000.00 |
0.8990 |
752.3 |
10000.00 |
0.9500 |
709.8 |
10000.00 |
1.0000 |
627.4 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mass density, kg/m3 - Liquid |
313.20 |
100.00 |
768.9 |
313.20 |
2050.00 |
785.8 |
313.20 |
4400.00 |
802.6 |
313.20 |
5860.00 |
813.0 |
313.20 |
6560.00 |
817.2 |
313.20 |
7270.00 |
813.7 |
313.20 |
7840.00 |
793.5 |
313.20 |
8170.00 |
762.5 |
313.20 |
8510.00 |
734.3 |
328.20 |
110.00 |
752.7 |
328.20 |
2200.00 |
766.2 |
328.20 |
4380.00 |
777.2 |
328.20 |
5860.00 |
784.2 |
328.20 |
6440.00 |
786.5 |
328.20 |
7130.00 |
788.3 |
328.20 |
7810.00 |
789.2 |
328.20 |
8170.00 |
788.7 |
328.20 |
8520.00 |
786.6 |
328.20 |
8860.00 |
782.4 |
328.20 |
9210.00 |
774.6 |
328.20 |
9560.00 |
755.2 |
328.20 |
9900.00 |
730.1 |
343.20 |
160.00 |
732.4 |
343.20 |
2270.00 |
742.0 |
343.20 |
4360.00 |
750.5 |
343.20 |
5820.00 |
756.6 |
343.20 |
7170.00 |
758.7 |
343.20 |
7850.00 |
760.0 |
343.20 |
8540.00 |
759.1 |
343.20 |
9240.00 |
757.3 |
343.20 |
9930.00 |
752.8 |
343.20 |
10610.00 |
742.3 |
343.20 |
11220.00 |
726.3 |
Critical temperature, K
[ref]
Mole fraction of Carbon dioxide (1) - Liquid |
Critical temperature, K - Liquid |
0.5300 |
453.00 |
0.7200 |
413.00 |
0.8800 |
353.00 |
0.8900 |
333.00 |
Critical temperature, K
[ref]
Mole fraction of Ethanol (2) - Liquid |
Critical temperature, K - Liquid |
0.3000 |
383.20 |
0.8000 |
493.00 |
Critical temperature, K
[ref]
Mole fraction of Carbon dioxide (1) - Liquid |
Critical temperature, K - Liquid |
0.8315 |
364.15 |
0.8380 |
361.65 |
0.8401 |
355.05 |
0.8409 |
348.65 |
0.8420 |
342.65 |
0.8507 |
335.65 |
0.8920 |
330.15 |
0.9010 |
332.15 |
0.9080 |
325.65 |
0.9310 |
321.15 |
Critical temperature, K
[ref]
Mole fraction of Carbon dioxide (1) - Liquid |
Critical temperature, K - Liquid |
0.5300 |
453.00 |
0.7200 |
413.00 |
0.8800 |
353.00 |
0.8900 |
333.00 |
Critical temperature, K
[ref]
Mole fraction of Ethanol (2) - Liquid |
Critical temperature, K - Liquid |
0.3000 |
383.20 |
0.8000 |
493.00 |
Critical temperature, K
[ref]
Mole fraction of Carbon dioxide (1) - Liquid |
Critical temperature, K - Liquid |
0.8315 |
364.15 |
0.8380 |
361.65 |
0.8401 |
355.05 |
0.8409 |
348.65 |
0.8420 |
342.65 |
0.8507 |
335.65 |
0.8920 |
330.15 |
0.9010 |
332.15 |
0.9080 |
325.65 |
0.9310 |
321.15 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Carbon dioxide (1) - Gas |
Vapor or sublimation pressure, kPa - Gas |
333.00 |
0.9800 |
4000.00 |
333.00 |
0.9780 |
4000.00 |
333.00 |
0.9820 |
4000.00 |
333.00 |
0.9820 |
4000.00 |
333.00 |
0.9830 |
4000.00 |
333.00 |
0.9820 |
6000.00 |
333.00 |
0.9780 |
8000.00 |
333.00 |
0.9560 |
10000.00 |
353.00 |
0.9130 |
12000.00 |
358.00 |
0.9190 |
12000.00 |
363.00 |
0.9210 |
12000.00 |
368.00 |
0.9130 |
12000.00 |
373.00 |
0.9080 |
12000.00 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Temperature, K =
313.15 (Liquid)
Mole fraction of Carbon dioxide (1) - Liquid |
Vapor or sublimation pressure, kPa - Gas |
0.1044 |
1830.00 |
0.1746 |
3020.00 |
0.2221 |
3760.00 |
0.3150 |
5200.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Gas |
Mole fraction of Ethanol (2) - Gas |
Vapor or sublimation pressure, kPa - Gas |
333.20 |
0.1000 |
10650.00 |
343.20 |
0.1000 |
11720.00 |
353.20 |
0.1000 |
12260.00 |
353.20 |
0.2000 |
12820.00 |
363.20 |
0.1000 |
12420.00 |
363.20 |
0.2000 |
13570.00 |
373.20 |
0.1000 |
11860.00 |
373.20 |
0.2000 |
14050.00 |
381.20 |
0.1000 |
10490.00 |
383.20 |
0.2000 |
14210.00 |
384.20 |
0.1000 |
6760.00 |
385.20 |
0.1000 |
8483.00 |
393.20 |
0.2000 |
13940.00 |
393.20 |
0.3000 |
14830.00 |
403.20 |
0.2000 |
13310.00 |
403.20 |
0.3000 |
14830.00 |
410.10 |
0.2000 |
12350.00 |
413.20 |
0.3000 |
14460.00 |
413.70 |
0.2000 |
6800.00 |
414.70 |
0.2000 |
10510.00 |
415.70 |
0.2000 |
8580.00 |
423.20 |
0.3000 |
13550.00 |
423.20 |
0.4000 |
14620.00 |
430.40 |
0.3000 |
12460.00 |
431.40 |
0.3000 |
6740.00 |
433.20 |
0.3000 |
11510.00 |
433.20 |
0.4000 |
14000.00 |
433.70 |
0.3000 |
7670.00 |
435.10 |
0.3000 |
9670.00 |
443.20 |
0.4000 |
13120.00 |
443.20 |
0.5000 |
13620.00 |
445.00 |
0.4000 |
6750.00 |
448.40 |
0.4000 |
7630.00 |
448.80 |
0.4000 |
11430.00 |
450.80 |
0.4000 |
9560.00 |
453.20 |
0.5000 |
12780.00 |
458.20 |
0.5000 |
6770.00 |
460.70 |
0.5000 |
11430.00 |
461.70 |
0.5000 |
7650.00 |
463.20 |
0.6000 |
12100.00 |
464.00 |
0.5000 |
9590.00 |
469.30 |
0.6000 |
11470.00 |
470.30 |
0.6000 |
6770.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Gas |
Mole fraction of Ethanol (2) - Gas |
Vapor or sublimation pressure, kPa - Gas |
474.20 |
0.6000 |
7680.00 |
476.20 |
0.6000 |
9640.00 |
482.00 |
0.7000 |
6740.00 |
483.00 |
0.7000 |
10000.00 |
486.00 |
0.7000 |
7650.00 |
487.00 |
0.7000 |
8570.00 |
494.00 |
0.8000 |
6770.00 |
496.00 |
0.8000 |
7680.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Gas |
Mole fraction of Carbon dioxide (1) - Gas |
Vapor or sublimation pressure, kPa - Gas |
313.15 |
0.9850 |
7800.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Carbon dioxide (1) - Gas |
Vapor or sublimation pressure, kPa - Gas |
333.00 |
0.9800 |
4000.00 |
333.00 |
0.9780 |
4000.00 |
333.00 |
0.9820 |
4000.00 |
333.00 |
0.9820 |
4000.00 |
333.00 |
0.9830 |
4000.00 |
333.00 |
0.9820 |
6000.00 |
333.00 |
0.9780 |
8000.00 |
333.00 |
0.9560 |
10000.00 |
353.00 |
0.9130 |
12000.00 |
358.00 |
0.9190 |
12000.00 |
363.00 |
0.9210 |
12000.00 |
368.00 |
0.9130 |
12000.00 |
373.00 |
0.9080 |
12000.00 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Temperature, K =
313.15 (Liquid)
Mole fraction of Carbon dioxide (1) - Liquid |
Vapor or sublimation pressure, kPa - Gas |
0.1044 |
1830.00 |
0.1746 |
3020.00 |
0.2221 |
3760.00 |
0.3150 |
5200.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Gas |
Mole fraction of Ethanol (2) - Gas |
Vapor or sublimation pressure, kPa - Gas |
333.20 |
0.1000 |
10650.00 |
343.20 |
0.1000 |
11720.00 |
353.20 |
0.1000 |
12260.00 |
353.20 |
0.2000 |
12820.00 |
363.20 |
0.1000 |
12420.00 |
363.20 |
0.2000 |
13570.00 |
373.20 |
0.1000 |
11860.00 |
373.20 |
0.2000 |
14050.00 |
381.20 |
0.1000 |
10490.00 |
383.20 |
0.2000 |
14210.00 |
384.20 |
0.1000 |
6760.00 |
385.20 |
0.1000 |
8483.00 |
393.20 |
0.2000 |
13940.00 |
393.20 |
0.3000 |
14830.00 |
403.20 |
0.2000 |
13310.00 |
403.20 |
0.3000 |
14830.00 |
410.10 |
0.2000 |
12350.00 |
413.20 |
0.3000 |
14460.00 |
413.70 |
0.2000 |
6800.00 |
414.70 |
0.2000 |
10510.00 |
415.70 |
0.2000 |
8580.00 |
423.20 |
0.3000 |
13550.00 |
423.20 |
0.4000 |
14620.00 |
430.40 |
0.3000 |
12460.00 |
431.40 |
0.3000 |
6740.00 |
433.20 |
0.3000 |
11510.00 |
433.20 |
0.4000 |
14000.00 |
433.70 |
0.3000 |
7670.00 |
435.10 |
0.3000 |
9670.00 |
443.20 |
0.4000 |
13120.00 |
443.20 |
0.5000 |
13620.00 |
445.00 |
0.4000 |
6750.00 |
448.40 |
0.4000 |
7630.00 |
448.80 |
0.4000 |
11430.00 |
450.80 |
0.4000 |
9560.00 |
453.20 |
0.5000 |
12780.00 |
458.20 |
0.5000 |
6770.00 |
460.70 |
0.5000 |
11430.00 |
461.70 |
0.5000 |
7650.00 |
463.20 |
0.6000 |
12100.00 |
464.00 |
0.5000 |
9590.00 |
469.30 |
0.6000 |
11470.00 |
470.30 |
0.6000 |
6770.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Gas |
Mole fraction of Ethanol (2) - Gas |
Vapor or sublimation pressure, kPa - Gas |
474.20 |
0.6000 |
7680.00 |
476.20 |
0.6000 |
9640.00 |
482.00 |
0.7000 |
6740.00 |
483.00 |
0.7000 |
10000.00 |
486.00 |
0.7000 |
7650.00 |
487.00 |
0.7000 |
8570.00 |
494.00 |
0.8000 |
6770.00 |
496.00 |
0.8000 |
7680.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Gas |
Mole fraction of Carbon dioxide (1) - Gas |
Vapor or sublimation pressure, kPa - Gas |
313.15 |
0.9850 |
7800.00 |
Sources
-
The Precise Measurement of Vapor Liquid Equilibrium Properties of the CO2/Isopentane Binary Mixture, and Fitted Parameters for a Helmholtz Energy Mixture Model
-
CO2 Solubility in Physicochemical Absorbent: Dibutyl Ether/N-Methylethanolamine/Ethanol
-
Solubility of thiopene in carbon dioxide and carbon dioxide + 1-propanol mixtures at temperatures from 313 to 363K
-
Establishing benchmarks for the Second Industrial Fluids Simulation Challenge
-
Solubility of carbon dioxide in binary and ternary mixtures with ethanol and water
-
Experimental determination and calculation of the critical curves for the binary systems of CO2 containing ketone, alkane, ester and alcohol, respectively
-
Measurements of vapor-liquid equilibrium in both binary carbon dioxide-ethanol and ternary carbon dioxide-ethanol-water systemswith a newly developed flow-type apparatus
-
Interfacial tension and adsorption in the binary system ethanol and carbon dioxide: Experiments, molecular simulation and density gradient theory
-
Development of a rolling ball viscometer for simultaneous measurement of viscosity, density, bubble-point pressure of CO2-expanded liquids
-
Experimental measurements and predictions of density, viscosity, and carbon dioxide solubility in methanol, ethanol, and 1-propanol
-
Effect of water content on the equilibrium pressure of (carbon dioxide + decane and + decalin) from T = (313.15 to 333.15) K
-
Assessment, measurement and correlation of (vapour + liquid) equilibrium of (carbon dioxide + butyl, isobutyl, and amyl formate) systems
-
High-pressure (vapour + liquid) equilibria for ternary systems composed by {(E)-2-hexenal or hexanal + carbon dioxide + water}: Partition coefficient measurement
-
Phase equilibrium measurements and thermodynamic modelling for the systems involving valeric acid, ethanol, ethyl valerate and water plus CO2
-
Phase behaviour of the pseudo-ternary system carbon dioxide + ethanol + fish oil at high pressures
-
Solubility of CO2 in methanol, ethanol, 1,2-propanediol and glycerol from 283.15 K to 373.15 K and up to 6.0 MPa
-
Equilibrium Solubilities of Diisooctyl Sebacate in Supercritical Carbon Dioxide
-
Vapor Liquid Equilibrium Measurements for Carbon Dioxide + Cyclohexene + Squalane at High Pressures Using a Synthetic Method
-
Density Measurements of CO2-Expanded Liquids
-
Phase Equilibrium Measurements and Thermodynamic Modeling of the Systems (CO2 + Ethyl Levulinate) and (CO2 + Levulinic Acid)
-
Phase Behavior for the System Carbon Dioxide + p-Nitrobenzaldehyde: Experimental and Modeling
-
High-Pressure Phase Equilibrium for Carbon Dioxide + Ethanol at 291.15 K
-
Phase Boundaries of CO2 + Toluene, CO2 + Acetone, and CO2 + Ethanol at High Temperatures and High Pressures
-
Solubility of CO2 in Alcohols, Glycols, Ethers, and Ketones at High Pressures from (288.15 to 318.15) K
-
Vapor Liquid Equilibrium Measurements of Difluoromethane + [Emim]OTf, Difluoromethane + [Bmim]OTf, Difluoroethane + [Emim]OTf, and Difluoroethane + [Bmim]OTf Systems
-
New High Pressure Vapor Liquid Equilibrium and Density Predictions for the Carbon Dioxide + Ethanol System
-
Isothermal Vapor Liquid Equilibrium Measurements of 1,1-Difluoroethane + N,N-Dimethylformamide and N,N-Dimethylacetamide
-
Equilibrium Solubilities of Iso-eicosane in Supercritical Carbon Dioxide
-
Vapor-Liquid Phase Boundaries of Binary Mixtures of Carbon Dioxide with Ethanol and Acetone
-
Volumetric Properties of Carbon Dioxide + Ethanol at 313.15 K
-
Measurement and Correlation of Vapor-Liquid Equilibrium for the Carbon Dioxide + 1-Butoxy Butane System
-
Density of Carbon Dioxide Expanded Ethanol at (313.2, 328.2, and 343.2) K