Datasets
-
Mole fraction (10)
-
η - Viscosity, Pa*s (4)
-
n0 - Refractive index (Na D-line) (2)
-
ρl - Mass density, kg/m3 (8)
-
csound,fluid - Speed of Sound, m/s (4)
-
γ - Surface tension liquid-gas, N/m (2)
-
Tboil - Boiling temperature at pressure P, K (6)
-
Azeotropic temperature, K (2)
Mole fraction of Water (2)
[ref]
| Fixed |
Measured |
| Mole fraction of Water (2) - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Water (2) - Gas |
| 0.1621 |
74.50 |
0.4263 |
| 0.2954 |
74.50 |
0.5396 |
| 0.3643 |
74.50 |
0.6137 |
| 0.4529 |
74.50 |
0.6805 |
| 0.5199 |
74.50 |
0.7116 |
| 0.5833 |
74.50 |
0.7456 |
| 0.6488 |
74.50 |
0.7949 |
| 0.9468 |
74.50 |
0.9569 |
| 0.1848 |
101.30 |
0.4311 |
| 0.3209 |
101.30 |
0.5721 |
| 0.3745 |
101.30 |
0.6132 |
| 0.4456 |
101.30 |
0.6525 |
| 0.5435 |
101.30 |
0.7436 |
| 0.7020 |
101.30 |
0.8074 |
| 0.8545 |
101.30 |
0.8711 |
| 0.9174 |
101.30 |
0.9212 |
| 0.1879 |
134.00 |
0.4561 |
| 0.3103 |
134.00 |
0.5451 |
| 0.4195 |
134.00 |
0.6440 |
| 0.5131 |
134.00 |
0.7090 |
| 0.6375 |
134.00 |
0.7800 |
| 0.7086 |
134.00 |
0.8070 |
| 0.8653 |
134.00 |
0.8779 |
| 0.9195 |
134.00 |
0.9281 |
Mole fraction of Ethanol, 2-methoxy- (1)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
| Mole fraction of Ethanol, 2-methoxy- (1) - Liquid |
Mole fraction of Ethanol, 2-methoxy- (1) - Gas |
| 1.0000 |
1.0000 |
| 0.9677 |
0.9073 |
| 0.8240 |
0.6011 |
| 0.6484 |
0.4064 |
| 0.5215 |
0.3012 |
| 0.4236 |
0.2342 |
| 0.3415 |
0.2009 |
| 0.2283 |
0.1464 |
| 0.1664 |
0.1283 |
| 0.0710 |
0.0712 |
| 0.0000 |
0.0000 |
Henry's Law constant (molality scale), kPa*kg/mol of Ethanol, 2-methoxy- (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
| Temperature, K - Liquid |
Henry's Law constant (molality scale), kPa*kg/mol of Ethanol, 2-methoxy- (1) - Liquid |
| 298.15 |
0.2234 |
| 311.15 |
0.6650 |
| 332.15 |
3.281 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
| Mole fraction of Water (2) - Liquid |
Mole fraction of Water (2) - Gas |
| 0.0000 |
0.0000 |
| 0.0260 |
0.0880 |
| 0.0510 |
0.1620 |
| 0.0720 |
0.2150 |
| 0.0990 |
0.2770 |
| 0.1580 |
0.3920 |
| 0.1760 |
0.4190 |
| 0.2050 |
0.4620 |
| 0.2670 |
0.5380 |
| 0.3320 |
0.6000 |
| 0.4150 |
0.6650 |
| 0.4920 |
0.7190 |
| 0.5420 |
0.7430 |
| 0.6080 |
0.7790 |
| 0.6750 |
0.8090 |
| 0.7110 |
0.8260 |
| 0.7680 |
0.8510 |
| 0.7900 |
0.8610 |
| 0.8390 |
0.8870 |
| 0.8820 |
0.9110 |
| 0.9110 |
0.9250 |
| 0.9490 |
0.9510 |
| 0.9860 |
0.9840 |
| 1.0000 |
1.0000 |
Azeotropic composition: mole fraction of Water (2)
[ref]
| Pressure, kPa - Liquid |
Azeotropic composition: mole fraction of Water (2) - Liquid |
| 101.30 |
0.9690 |
Mole fraction of Water (2)
[ref]
| Fixed |
Measured |
| Mole fraction of Water (2) - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Water (2) - Gas |
| 0.1621 |
74.50 |
0.4263 |
| 0.2954 |
74.50 |
0.5396 |
| 0.3643 |
74.50 |
0.6137 |
| 0.4529 |
74.50 |
0.6805 |
| 0.5199 |
74.50 |
0.7116 |
| 0.5833 |
74.50 |
0.7456 |
| 0.6488 |
74.50 |
0.7949 |
| 0.9468 |
74.50 |
0.9569 |
| 0.1848 |
101.30 |
0.4311 |
| 0.3209 |
101.30 |
0.5721 |
| 0.3745 |
101.30 |
0.6132 |
| 0.4456 |
101.30 |
0.6525 |
| 0.5435 |
101.30 |
0.7436 |
| 0.7020 |
101.30 |
0.8074 |
| 0.8545 |
101.30 |
0.8711 |
| 0.9174 |
101.30 |
0.9212 |
| 0.1879 |
134.00 |
0.4561 |
| 0.3103 |
134.00 |
0.5451 |
| 0.4195 |
134.00 |
0.6440 |
| 0.5131 |
134.00 |
0.7090 |
| 0.6375 |
134.00 |
0.7800 |
| 0.7086 |
134.00 |
0.8070 |
| 0.8653 |
134.00 |
0.8779 |
| 0.9195 |
134.00 |
0.9281 |
Mole fraction of Ethanol, 2-methoxy- (1)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
| Mole fraction of Ethanol, 2-methoxy- (1) - Liquid |
Mole fraction of Ethanol, 2-methoxy- (1) - Gas |
| 1.0000 |
1.0000 |
| 0.9677 |
0.9073 |
| 0.8240 |
0.6011 |
| 0.6484 |
0.4064 |
| 0.5215 |
0.3012 |
| 0.4236 |
0.2342 |
| 0.3415 |
0.2009 |
| 0.2283 |
0.1464 |
| 0.1664 |
0.1283 |
| 0.0710 |
0.0712 |
| 0.0000 |
0.0000 |
Henry's Law constant (molality scale), kPa*kg/mol of Ethanol, 2-methoxy- (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
| Temperature, K - Liquid |
Henry's Law constant (molality scale), kPa*kg/mol of Ethanol, 2-methoxy- (1) - Liquid |
| 298.15 |
0.2234 |
| 311.15 |
0.6650 |
| 332.15 |
3.281 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
| Mole fraction of Water (2) - Liquid |
Mole fraction of Water (2) - Gas |
| 0.0000 |
0.0000 |
| 0.0260 |
0.0880 |
| 0.0510 |
0.1620 |
| 0.0720 |
0.2150 |
| 0.0990 |
0.2770 |
| 0.1580 |
0.3920 |
| 0.1760 |
0.4190 |
| 0.2050 |
0.4620 |
| 0.2670 |
0.5380 |
| 0.3320 |
0.6000 |
| 0.4150 |
0.6650 |
| 0.4920 |
0.7190 |
| 0.5420 |
0.7430 |
| 0.6080 |
0.7790 |
| 0.6750 |
0.8090 |
| 0.7110 |
0.8260 |
| 0.7680 |
0.8510 |
| 0.7900 |
0.8610 |
| 0.8390 |
0.8870 |
| 0.8820 |
0.9110 |
| 0.9110 |
0.9250 |
| 0.9490 |
0.9510 |
| 0.9860 |
0.9840 |
| 1.0000 |
1.0000 |
Azeotropic composition: mole fraction of Water (2)
[ref]
| Pressure, kPa - Liquid |
Azeotropic composition: mole fraction of Water (2) - Liquid |
| 101.30 |
0.9690 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Ethanol, 2-methoxy- (1) - Liquid |
Viscosity, Pa*s - Liquid |
| 303.15 |
0.0000 |
0.0008 |
| 303.15 |
0.0247 |
0.0011 |
| 303.15 |
0.0540 |
0.0014 |
| 303.15 |
0.0891 |
0.0017 |
| 303.15 |
0.1321 |
0.0020 |
| 303.15 |
0.1858 |
0.0022 |
| 303.15 |
0.2551 |
0.0024 |
| 303.15 |
0.3475 |
0.0024 |
| 303.15 |
0.4773 |
0.0023 |
| 303.15 |
0.6726 |
0.0018 |
| 303.15 |
1.0000 |
0.0014 |
| 308.15 |
0.0000 |
0.0007 |
| 308.15 |
0.0247 |
0.0010 |
| 308.15 |
0.0540 |
0.0012 |
| 308.15 |
0.0891 |
0.0015 |
| 308.15 |
0.1321 |
0.0017 |
| 308.15 |
0.1858 |
0.0019 |
| 308.15 |
0.2551 |
0.0020 |
| 308.15 |
0.3475 |
0.0021 |
| 308.15 |
0.4773 |
0.0019 |
| 308.15 |
0.6726 |
0.0015 |
| 308.15 |
1.0000 |
0.0011 |
| 313.15 |
0.0000 |
0.0007 |
| 313.15 |
0.0247 |
0.0008 |
| 313.15 |
0.0540 |
0.0010 |
| 313.15 |
0.0891 |
0.0012 |
| 313.15 |
0.1321 |
0.0014 |
| 313.15 |
0.1858 |
0.0015 |
| 313.15 |
0.2551 |
0.0017 |
| 313.15 |
0.3475 |
0.0017 |
| 313.15 |
0.4773 |
0.0016 |
| 313.15 |
0.6726 |
0.0013 |
| 313.15 |
1.0000 |
0.0009 |
| 318.15 |
0.0000 |
0.0006 |
| 318.15 |
0.0247 |
0.0007 |
| 318.15 |
0.0540 |
0.0009 |
| 318.15 |
0.0891 |
0.0010 |
| 318.15 |
0.1321 |
0.0012 |
| 318.15 |
0.1858 |
0.0014 |
| 318.15 |
0.2551 |
0.0015 |
| 318.15 |
0.3475 |
0.0015 |
| 318.15 |
0.4773 |
0.0014 |
| 318.15 |
0.6726 |
0.0011 |
| 318.15 |
1.0000 |
0.0008 |
| 323.15 |
0.0000 |
0.0005 |
| 323.15 |
0.0247 |
0.0007 |
| 323.15 |
0.0540 |
0.0008 |
| 323.15 |
0.0891 |
0.0009 |
| 323.15 |
0.1321 |
0.0011 |
| 323.15 |
0.1858 |
0.0012 |
| 323.15 |
0.2551 |
0.0013 |
| 323.15 |
0.3475 |
0.0014 |
| 323.15 |
0.4773 |
0.0013 |
| 323.15 |
0.6726 |
0.0010 |
| 323.15 |
1.0000 |
0.0008 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Molality, mol/kg of Ethanol, 2-methoxy- (1) - Liquid |
Viscosity, Pa*s - Liquid |
| 275.15 |
0.0000 |
0.0017 |
| 275.15 |
0.0097 |
0.0010 |
| 275.15 |
0.0205 |
0.0010 |
| 275.15 |
0.0313 |
0.0010 |
| 275.15 |
0.0393 |
0.0010 |
| 275.15 |
0.0487 |
0.0010 |
| 275.15 |
0.0638 |
0.0010 |
| 275.15 |
0.0719 |
0.0010 |
| 275.15 |
0.0813 |
0.0010 |
| 275.15 |
0.0905 |
0.0010 |
| 275.15 |
0.1020 |
0.0010 |
| 283.15 |
0.0000 |
0.0013 |
| 283.15 |
0.0104 |
0.0010 |
| 283.15 |
0.0193 |
0.0010 |
| 283.15 |
0.0326 |
0.0010 |
| 283.15 |
0.0417 |
0.0010 |
| 283.15 |
0.0492 |
0.0010 |
| 283.15 |
0.0599 |
0.0010 |
| 283.15 |
0.0698 |
0.0010 |
| 283.15 |
0.0804 |
0.0010 |
| 283.15 |
0.0893 |
0.0010 |
| 283.15 |
0.0901 |
0.0010 |
| 283.15 |
0.1000 |
0.0010 |
| 283.15 |
0.1013 |
0.0010 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Ethanol, 2-methoxy- (1) - Liquid |
Viscosity, Pa*s - Liquid |
| 303.15 |
0.0000 |
0.0008 |
| 303.15 |
0.0247 |
0.0011 |
| 303.15 |
0.0540 |
0.0014 |
| 303.15 |
0.0891 |
0.0017 |
| 303.15 |
0.1321 |
0.0020 |
| 303.15 |
0.1858 |
0.0022 |
| 303.15 |
0.2551 |
0.0024 |
| 303.15 |
0.3475 |
0.0024 |
| 303.15 |
0.4773 |
0.0023 |
| 303.15 |
0.6726 |
0.0018 |
| 303.15 |
1.0000 |
0.0014 |
| 308.15 |
0.0000 |
0.0007 |
| 308.15 |
0.0247 |
0.0010 |
| 308.15 |
0.0540 |
0.0012 |
| 308.15 |
0.0891 |
0.0015 |
| 308.15 |
0.1321 |
0.0017 |
| 308.15 |
0.1858 |
0.0019 |
| 308.15 |
0.2551 |
0.0020 |
| 308.15 |
0.3475 |
0.0021 |
| 308.15 |
0.4773 |
0.0019 |
| 308.15 |
0.6726 |
0.0015 |
| 308.15 |
1.0000 |
0.0011 |
| 313.15 |
0.0000 |
0.0007 |
| 313.15 |
0.0247 |
0.0008 |
| 313.15 |
0.0540 |
0.0010 |
| 313.15 |
0.0891 |
0.0012 |
| 313.15 |
0.1321 |
0.0014 |
| 313.15 |
0.1858 |
0.0015 |
| 313.15 |
0.2551 |
0.0017 |
| 313.15 |
0.3475 |
0.0017 |
| 313.15 |
0.4773 |
0.0016 |
| 313.15 |
0.6726 |
0.0013 |
| 313.15 |
1.0000 |
0.0009 |
| 318.15 |
0.0000 |
0.0006 |
| 318.15 |
0.0247 |
0.0007 |
| 318.15 |
0.0540 |
0.0009 |
| 318.15 |
0.0891 |
0.0010 |
| 318.15 |
0.1321 |
0.0012 |
| 318.15 |
0.1858 |
0.0014 |
| 318.15 |
0.2551 |
0.0015 |
| 318.15 |
0.3475 |
0.0015 |
| 318.15 |
0.4773 |
0.0014 |
| 318.15 |
0.6726 |
0.0011 |
| 318.15 |
1.0000 |
0.0008 |
| 323.15 |
0.0000 |
0.0005 |
| 323.15 |
0.0247 |
0.0007 |
| 323.15 |
0.0540 |
0.0008 |
| 323.15 |
0.0891 |
0.0009 |
| 323.15 |
0.1321 |
0.0011 |
| 323.15 |
0.1858 |
0.0012 |
| 323.15 |
0.2551 |
0.0013 |
| 323.15 |
0.3475 |
0.0014 |
| 323.15 |
0.4773 |
0.0013 |
| 323.15 |
0.6726 |
0.0010 |
| 323.15 |
1.0000 |
0.0008 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Molality, mol/kg of Ethanol, 2-methoxy- (1) - Liquid |
Viscosity, Pa*s - Liquid |
| 275.15 |
0.0000 |
0.0017 |
| 275.15 |
0.0097 |
0.0010 |
| 275.15 |
0.0205 |
0.0010 |
| 275.15 |
0.0313 |
0.0010 |
| 275.15 |
0.0393 |
0.0010 |
| 275.15 |
0.0487 |
0.0010 |
| 275.15 |
0.0638 |
0.0010 |
| 275.15 |
0.0719 |
0.0010 |
| 275.15 |
0.0813 |
0.0010 |
| 275.15 |
0.0905 |
0.0010 |
| 275.15 |
0.1020 |
0.0010 |
| 283.15 |
0.0000 |
0.0013 |
| 283.15 |
0.0104 |
0.0010 |
| 283.15 |
0.0193 |
0.0010 |
| 283.15 |
0.0326 |
0.0010 |
| 283.15 |
0.0417 |
0.0010 |
| 283.15 |
0.0492 |
0.0010 |
| 283.15 |
0.0599 |
0.0010 |
| 283.15 |
0.0698 |
0.0010 |
| 283.15 |
0.0804 |
0.0010 |
| 283.15 |
0.0893 |
0.0010 |
| 283.15 |
0.0901 |
0.0010 |
| 283.15 |
0.1000 |
0.0010 |
| 283.15 |
0.1013 |
0.0010 |
Refractive index (Na D-line)
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
| Mole fraction of Ethanol, 2-methoxy- (1) - Liquid |
Refractive index (Na D-line) - Liquid |
| 0.0000 |
1.333 |
| 0.0202 |
1.34 |
| 0.0400 |
1.346 |
| 0.0539 |
1.35 |
| 0.0822 |
1.357 |
| 0.1010 |
1.361 |
| 0.1509 |
1.37 |
| 0.2036 |
1.378 |
| 0.3025 |
1.386 |
| 0.4033 |
1.391 |
| 0.5009 |
1.394 |
| 0.5514 |
1.395 |
| 0.6976 |
1.396 |
| 0.7855 |
1.398 |
| 0.8890 |
1.398 |
| 1.0000 |
1.4002 |
Refractive index (Na D-line)
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
| Mole fraction of Ethanol, 2-methoxy- (1) - Liquid |
Refractive index (Na D-line) - Liquid |
| 0.0000 |
1.333 |
| 0.0202 |
1.34 |
| 0.0400 |
1.346 |
| 0.0539 |
1.35 |
| 0.0822 |
1.357 |
| 0.1010 |
1.361 |
| 0.1509 |
1.37 |
| 0.2036 |
1.378 |
| 0.3025 |
1.386 |
| 0.4033 |
1.391 |
| 0.5009 |
1.394 |
| 0.5514 |
1.395 |
| 0.6976 |
1.396 |
| 0.7855 |
1.398 |
| 0.8890 |
1.398 |
| 1.0000 |
1.4002 |
Mass density, kg/m3
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
| Mole fraction of Ethanol, 2-methoxy- (1) - Liquid |
Mass density, kg/m3 - Liquid |
| 0.0000 |
999.704 |
| 0.0202 |
999.08 |
| 0.0400 |
1001.08 |
| 0.0539 |
1002.4 |
| 0.0822 |
1004.71 |
| 0.1010 |
1005.84 |
| 0.1509 |
1007.02 |
| 0.2036 |
1005.67 |
| 0.3025 |
999.82 |
| 0.4033 |
992.74 |
| 0.5009 |
985.91 |
| 0.5514 |
982.57 |
| 0.6976 |
974.0 |
| 0.7855 |
969.57 |
| 0.8890 |
964.87 |
| 1.0000 |
960.23 |
Mass density, kg/m3
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 275.15 (Liquid)
| Molality, mol/kg of Ethanol, 2-methoxy- (1) - Liquid |
Mass density, kg/m3 - Liquid |
| 0.0000 |
999.94 |
| 0.0097 |
999.96 |
| 0.0205 |
999.99 |
| 0.0313 |
999.99 |
| 0.0393 |
1000.02 |
| 0.0487 |
1000.07 |
| 0.0638 |
1000.09 |
| 0.0719 |
1000.1 |
| 0.0813 |
1000.12 |
| 0.0905 |
1000.12 |
| 0.1020 |
1000.17 |
Mass density, kg/m3
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 283.15 (Liquid)
| Molality, mol/kg of Ethanol, 2-methoxy- (1) - Liquid |
Mass density, kg/m3 - Liquid |
| 0.0000 |
999.7 |
| 0.0104 |
999.73 |
| 0.0193 |
999.73 |
| 0.0326 |
999.76 |
| 0.0417 |
999.81 |
| 0.0492 |
999.79 |
| 0.0599 |
999.88 |
| 0.0698 |
999.93 |
| 0.0804 |
999.91 |
| 0.0893 |
999.94 |
| 0.0901 |
999.94 |
| 0.1000 |
999.95 |
| 0.1013 |
999.97 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Molality, mol/kg of Ethanol, 2-methoxy- (1) - Liquid |
Mass density, kg/m3 - Liquid |
| 288.15 |
0.1766 |
999.359 |
| 288.15 |
0.3377 |
999.461 |
| 288.15 |
0.3987 |
999.495 |
| 288.15 |
0.5117 |
999.548 |
| 288.15 |
0.6355 |
999.593 |
| 288.15 |
0.7947 |
999.638 |
| 288.15 |
1.0116 |
999.666 |
| 298.15 |
0.1766 |
997.221 |
| 298.15 |
0.3377 |
997.304 |
| 298.15 |
0.3987 |
997.331 |
| 298.15 |
0.5117 |
997.377 |
| 298.15 |
0.6355 |
997.421 |
| 298.15 |
0.7947 |
997.462 |
| 298.15 |
1.0116 |
997.507 |
| 308.15 |
0.1766 |
994.075 |
| 308.15 |
0.3377 |
994.169 |
| 308.15 |
0.3987 |
994.202 |
| 308.15 |
0.5117 |
994.256 |
| 308.15 |
0.6355 |
994.305 |
| 308.15 |
0.7947 |
994.361 |
| 308.15 |
1.0116 |
994.412 |
Mass density, kg/m3
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
| Mole fraction of Ethanol, 2-methoxy- (1) - Liquid |
Mass density, kg/m3 - Liquid |
| 0.0000 |
999.704 |
| 0.0202 |
999.08 |
| 0.0400 |
1001.08 |
| 0.0539 |
1002.4 |
| 0.0822 |
1004.71 |
| 0.1010 |
1005.84 |
| 0.1509 |
1007.02 |
| 0.2036 |
1005.67 |
| 0.3025 |
999.82 |
| 0.4033 |
992.74 |
| 0.5009 |
985.91 |
| 0.5514 |
982.57 |
| 0.6976 |
974.0 |
| 0.7855 |
969.57 |
| 0.8890 |
964.87 |
| 1.0000 |
960.23 |
Mass density, kg/m3
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 275.15 (Liquid)
| Molality, mol/kg of Ethanol, 2-methoxy- (1) - Liquid |
Mass density, kg/m3 - Liquid |
| 0.0000 |
999.94 |
| 0.0097 |
999.96 |
| 0.0205 |
999.99 |
| 0.0313 |
999.99 |
| 0.0393 |
1000.02 |
| 0.0487 |
1000.07 |
| 0.0638 |
1000.09 |
| 0.0719 |
1000.1 |
| 0.0813 |
1000.12 |
| 0.0905 |
1000.12 |
| 0.1020 |
1000.17 |
Mass density, kg/m3
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 283.15 (Liquid)
| Molality, mol/kg of Ethanol, 2-methoxy- (1) - Liquid |
Mass density, kg/m3 - Liquid |
| 0.0000 |
999.7 |
| 0.0104 |
999.73 |
| 0.0193 |
999.73 |
| 0.0326 |
999.76 |
| 0.0417 |
999.81 |
| 0.0492 |
999.79 |
| 0.0599 |
999.88 |
| 0.0698 |
999.93 |
| 0.0804 |
999.91 |
| 0.0893 |
999.94 |
| 0.0901 |
999.94 |
| 0.1000 |
999.95 |
| 0.1013 |
999.97 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Molality, mol/kg of Ethanol, 2-methoxy- (1) - Liquid |
Mass density, kg/m3 - Liquid |
| 288.15 |
0.1766 |
999.359 |
| 288.15 |
0.3377 |
999.461 |
| 288.15 |
0.3987 |
999.495 |
| 288.15 |
0.5117 |
999.548 |
| 288.15 |
0.6355 |
999.593 |
| 288.15 |
0.7947 |
999.638 |
| 288.15 |
1.0116 |
999.666 |
| 298.15 |
0.1766 |
997.221 |
| 298.15 |
0.3377 |
997.304 |
| 298.15 |
0.3987 |
997.331 |
| 298.15 |
0.5117 |
997.377 |
| 298.15 |
0.6355 |
997.421 |
| 298.15 |
0.7947 |
997.462 |
| 298.15 |
1.0116 |
997.507 |
| 308.15 |
0.1766 |
994.075 |
| 308.15 |
0.3377 |
994.169 |
| 308.15 |
0.3987 |
994.202 |
| 308.15 |
0.5117 |
994.256 |
| 308.15 |
0.6355 |
994.305 |
| 308.15 |
0.7947 |
994.361 |
| 308.15 |
1.0116 |
994.412 |
Speed of sound, m/s
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
| Mole fraction of Ethanol, 2-methoxy- (1) - Liquid |
Speed of sound, m/s - Liquid |
| 0.0000 |
1496.6 |
| 0.0202 |
1546.5 |
| 0.0400 |
1581.0 |
| 0.0539 |
1600.9 |
| 0.0822 |
1636.5 |
| 0.1010 |
1643.7 |
| 0.1509 |
1654.7 |
| 0.2036 |
1641.7 |
| 0.3025 |
1587.3 |
| 0.4033 |
1532.3 |
| 0.5009 |
1488.5 |
| 0.5514 |
1470.9 |
| 0.6976 |
1418.8 |
| 0.7855 |
1392.0 |
| 0.8890 |
1369.3 |
| 1.0000 |
1341.7 |
Speed of sound, m/s
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Molality, mol/kg of Ethanol, 2-methoxy- (1) - Liquid |
Speed of sound, m/s - Liquid |
| 288.15 |
0.1766 |
1475.29 |
| 288.15 |
0.3377 |
1487.32 |
| 288.15 |
0.3987 |
1486.91 |
| 288.15 |
0.5117 |
1492.9 |
| 288.15 |
0.6355 |
1498.11 |
| 288.15 |
0.7947 |
1506.83 |
| 288.15 |
1.0116 |
1518.14 |
| 298.15 |
0.1766 |
1504.91 |
| 298.15 |
0.3377 |
1511.21 |
| 298.15 |
0.3987 |
1513.82 |
| 298.15 |
0.5117 |
1517.98 |
| 298.15 |
0.6355 |
1522.87 |
| 298.15 |
0.7947 |
1529.32 |
| 298.15 |
1.0116 |
1539.1 |
| 308.15 |
0.1766 |
1526.06 |
| 308.15 |
0.3377 |
1531.64 |
| 308.15 |
0.3987 |
1533.13 |
| 308.15 |
0.5117 |
1537.02 |
| 308.15 |
0.6355 |
1540.5 |
| 308.15 |
0.7947 |
1546.05 |
| 308.15 |
1.0116 |
1553.66 |
Speed of sound, m/s
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
| Mole fraction of Ethanol, 2-methoxy- (1) - Liquid |
Speed of sound, m/s - Liquid |
| 0.0000 |
1496.6 |
| 0.0202 |
1546.5 |
| 0.0400 |
1581.0 |
| 0.0539 |
1600.9 |
| 0.0822 |
1636.5 |
| 0.1010 |
1643.7 |
| 0.1509 |
1654.7 |
| 0.2036 |
1641.7 |
| 0.3025 |
1587.3 |
| 0.4033 |
1532.3 |
| 0.5009 |
1488.5 |
| 0.5514 |
1470.9 |
| 0.6976 |
1418.8 |
| 0.7855 |
1392.0 |
| 0.8890 |
1369.3 |
| 1.0000 |
1341.7 |
Speed of sound, m/s
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Molality, mol/kg of Ethanol, 2-methoxy- (1) - Liquid |
Speed of sound, m/s - Liquid |
| 288.15 |
0.1766 |
1475.29 |
| 288.15 |
0.3377 |
1487.32 |
| 288.15 |
0.3987 |
1486.91 |
| 288.15 |
0.5117 |
1492.9 |
| 288.15 |
0.6355 |
1498.11 |
| 288.15 |
0.7947 |
1506.83 |
| 288.15 |
1.0116 |
1518.14 |
| 298.15 |
0.1766 |
1504.91 |
| 298.15 |
0.3377 |
1511.21 |
| 298.15 |
0.3987 |
1513.82 |
| 298.15 |
0.5117 |
1517.98 |
| 298.15 |
0.6355 |
1522.87 |
| 298.15 |
0.7947 |
1529.32 |
| 298.15 |
1.0116 |
1539.1 |
| 308.15 |
0.1766 |
1526.06 |
| 308.15 |
0.3377 |
1531.64 |
| 308.15 |
0.3987 |
1533.13 |
| 308.15 |
0.5117 |
1537.02 |
| 308.15 |
0.6355 |
1540.5 |
| 308.15 |
0.7947 |
1546.05 |
| 308.15 |
1.0116 |
1553.66 |
Surface tension liquid-gas, N/m
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Ethanol, 2-methoxy- (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
| 298.15 |
0.0000 |
0.0720 |
| 298.15 |
0.0509 |
0.0563 |
| 298.15 |
0.0559 |
0.0551 |
| 298.15 |
0.1052 |
0.0469 |
| 298.15 |
0.1494 |
0.0433 |
| 298.15 |
0.2215 |
0.0397 |
| 298.15 |
0.3373 |
0.0367 |
| 298.15 |
0.4783 |
0.0350 |
| 298.15 |
0.6258 |
0.0329 |
| 298.15 |
0.7814 |
0.0318 |
| 298.15 |
0.8912 |
0.0310 |
| 298.15 |
1.0000 |
0.0308 |
| 308.15 |
0.0000 |
0.0704 |
| 308.15 |
0.0509 |
0.0552 |
| 308.15 |
0.0559 |
0.0540 |
| 308.15 |
0.1052 |
0.0459 |
| 308.15 |
0.1494 |
0.0424 |
| 308.15 |
0.2215 |
0.0388 |
| 308.15 |
0.3373 |
0.0359 |
| 308.15 |
0.4783 |
0.0342 |
| 308.15 |
0.6258 |
0.0320 |
| 308.15 |
0.7814 |
0.0310 |
| 308.15 |
0.8912 |
0.0302 |
| 308.15 |
1.0000 |
0.0300 |
| 318.15 |
0.0000 |
0.0688 |
| 318.15 |
0.0509 |
0.0539 |
| 318.15 |
0.0559 |
0.0528 |
| 318.15 |
0.1052 |
0.0448 |
| 318.15 |
0.1494 |
0.0413 |
| 318.15 |
0.2215 |
0.0378 |
| 318.15 |
0.3373 |
0.0349 |
| 318.15 |
0.4783 |
0.0332 |
| 318.15 |
0.6258 |
0.0311 |
| 318.15 |
0.7814 |
0.0300 |
| 318.15 |
0.8912 |
0.0293 |
| 318.15 |
1.0000 |
0.0291 |
Surface tension liquid-gas, N/m
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Ethanol, 2-methoxy- (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
| 298.15 |
0.0000 |
0.0720 |
| 298.15 |
0.0509 |
0.0563 |
| 298.15 |
0.0559 |
0.0551 |
| 298.15 |
0.1052 |
0.0469 |
| 298.15 |
0.1494 |
0.0433 |
| 298.15 |
0.2215 |
0.0397 |
| 298.15 |
0.3373 |
0.0367 |
| 298.15 |
0.4783 |
0.0350 |
| 298.15 |
0.6258 |
0.0329 |
| 298.15 |
0.7814 |
0.0318 |
| 298.15 |
0.8912 |
0.0310 |
| 298.15 |
1.0000 |
0.0308 |
| 308.15 |
0.0000 |
0.0704 |
| 308.15 |
0.0509 |
0.0552 |
| 308.15 |
0.0559 |
0.0540 |
| 308.15 |
0.1052 |
0.0459 |
| 308.15 |
0.1494 |
0.0424 |
| 308.15 |
0.2215 |
0.0388 |
| 308.15 |
0.3373 |
0.0359 |
| 308.15 |
0.4783 |
0.0342 |
| 308.15 |
0.6258 |
0.0320 |
| 308.15 |
0.7814 |
0.0310 |
| 308.15 |
0.8912 |
0.0302 |
| 308.15 |
1.0000 |
0.0300 |
| 318.15 |
0.0000 |
0.0688 |
| 318.15 |
0.0509 |
0.0539 |
| 318.15 |
0.0559 |
0.0528 |
| 318.15 |
0.1052 |
0.0448 |
| 318.15 |
0.1494 |
0.0413 |
| 318.15 |
0.2215 |
0.0378 |
| 318.15 |
0.3373 |
0.0349 |
| 318.15 |
0.4783 |
0.0332 |
| 318.15 |
0.6258 |
0.0311 |
| 318.15 |
0.7814 |
0.0300 |
| 318.15 |
0.8912 |
0.0293 |
| 318.15 |
1.0000 |
0.0291 |
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 |
| 0.1621 |
74.50 |
379.40 |
| 0.2954 |
74.50 |
375.30 |
| 0.3643 |
74.50 |
372.70 |
| 0.4529 |
74.50 |
370.30 |
| 0.5199 |
74.50 |
369.10 |
| 0.5833 |
74.50 |
367.70 |
| 0.6488 |
74.50 |
366.40 |
| 0.9468 |
74.50 |
365.00 |
| 0.1848 |
101.30 |
388.00 |
| 0.3209 |
101.30 |
383.40 |
| 0.3745 |
101.30 |
381.50 |
| 0.4456 |
101.30 |
379.50 |
| 0.5435 |
101.30 |
376.50 |
| 0.7020 |
101.30 |
374.40 |
| 0.8545 |
101.30 |
373.70 |
| 0.9174 |
101.30 |
373.70 |
| 0.1879 |
134.00 |
395.60 |
| 0.3103 |
134.00 |
391.40 |
| 0.4195 |
134.00 |
387.70 |
| 0.5131 |
134.00 |
384.80 |
| 0.6375 |
134.00 |
382.80 |
| 0.7086 |
134.00 |
382.00 |
| 0.8653 |
134.00 |
381.50 |
| 0.9195 |
134.00 |
381.50 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
| Mole fraction of Ethanol, 2-methoxy- (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
| 1.0000 |
397.67 |
| 0.9677 |
396.02 |
| 0.8240 |
388.51 |
| 0.6484 |
381.98 |
| 0.5215 |
378.32 |
| 0.4236 |
376.20 |
| 0.3415 |
375.15 |
| 0.2283 |
374.05 |
| 0.1664 |
373.55 |
| 0.0710 |
373.45 |
| 0.0000 |
373.19 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
| Mole fraction of Water (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
| 0.0000 |
397.58 |
| 0.0260 |
395.63 |
| 0.0510 |
393.86 |
| 0.0720 |
392.40 |
| 0.0990 |
390.75 |
| 0.1580 |
387.62 |
| 0.1760 |
386.80 |
| 0.2050 |
385.45 |
| 0.2670 |
383.28 |
| 0.3320 |
381.34 |
| 0.4150 |
379.26 |
| 0.4920 |
377.65 |
| 0.5420 |
376.82 |
| 0.6080 |
375.83 |
| 0.6750 |
375.00 |
| 0.7110 |
374.59 |
| 0.7680 |
374.15 |
| 0.7900 |
373.93 |
| 0.8390 |
373.60 |
| 0.8820 |
373.35 |
| 0.9110 |
373.17 |
| 0.9490 |
373.07 |
| 0.9860 |
373.12 |
| 1.0000 |
373.15 |
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 |
| 0.1621 |
74.50 |
379.40 |
| 0.2954 |
74.50 |
375.30 |
| 0.3643 |
74.50 |
372.70 |
| 0.4529 |
74.50 |
370.30 |
| 0.5199 |
74.50 |
369.10 |
| 0.5833 |
74.50 |
367.70 |
| 0.6488 |
74.50 |
366.40 |
| 0.9468 |
74.50 |
365.00 |
| 0.1848 |
101.30 |
388.00 |
| 0.3209 |
101.30 |
383.40 |
| 0.3745 |
101.30 |
381.50 |
| 0.4456 |
101.30 |
379.50 |
| 0.5435 |
101.30 |
376.50 |
| 0.7020 |
101.30 |
374.40 |
| 0.8545 |
101.30 |
373.70 |
| 0.9174 |
101.30 |
373.70 |
| 0.1879 |
134.00 |
395.60 |
| 0.3103 |
134.00 |
391.40 |
| 0.4195 |
134.00 |
387.70 |
| 0.5131 |
134.00 |
384.80 |
| 0.6375 |
134.00 |
382.80 |
| 0.7086 |
134.00 |
382.00 |
| 0.8653 |
134.00 |
381.50 |
| 0.9195 |
134.00 |
381.50 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
| Mole fraction of Ethanol, 2-methoxy- (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
| 1.0000 |
397.67 |
| 0.9677 |
396.02 |
| 0.8240 |
388.51 |
| 0.6484 |
381.98 |
| 0.5215 |
378.32 |
| 0.4236 |
376.20 |
| 0.3415 |
375.15 |
| 0.2283 |
374.05 |
| 0.1664 |
373.55 |
| 0.0710 |
373.45 |
| 0.0000 |
373.19 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
| Mole fraction of Water (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
| 0.0000 |
397.58 |
| 0.0260 |
395.63 |
| 0.0510 |
393.86 |
| 0.0720 |
392.40 |
| 0.0990 |
390.75 |
| 0.1580 |
387.62 |
| 0.1760 |
386.80 |
| 0.2050 |
385.45 |
| 0.2670 |
383.28 |
| 0.3320 |
381.34 |
| 0.4150 |
379.26 |
| 0.4920 |
377.65 |
| 0.5420 |
376.82 |
| 0.6080 |
375.83 |
| 0.6750 |
375.00 |
| 0.7110 |
374.59 |
| 0.7680 |
374.15 |
| 0.7900 |
373.93 |
| 0.8390 |
373.60 |
| 0.8820 |
373.35 |
| 0.9110 |
373.17 |
| 0.9490 |
373.07 |
| 0.9860 |
373.12 |
| 1.0000 |
373.15 |
Azeotropic temperature, K
[ref]
| Pressure, kPa - Liquid |
Azeotropic temperature, K - Liquid |
| 101.30 |
373.05 |
Azeotropic temperature, K
[ref]
| Pressure, kPa - Liquid |
Azeotropic temperature, K - Liquid |
| 101.30 |
373.05 |
Sources
-
Viscosity of aqueous solutions of 2-methoxyethanol, 2-ethoxyethanol, and ethanolamine
-
Thermodynamic and optical studies of some ethylene glycol ethers in aqueous solutions at T = 298.15 K
-
Volumetric and viscometric study of aqueous binary mixtures of some glycol ethers at T = (275.15 and 283.15) K
-
Thermophysical properties of ionic liquid {1-butyl-3-methylimidazolium bromide [bmim][Br] in alkoxyalkanols + water} mixtures at different temperatures
-
Isobaric (vapor + liquid) equilibria for the binary systems (1-methoxy-2- propanol + 2-methoxyethanol), (2-butanone + 2-methoxyethanol) and (water + 2-methoxyethanol) at pressures of (74.5, 101.3, and 134.0) kPa
-
Isobaric Vapor Liquid Equilibria for (Water + 1-Methoxy-2-propanol), (Water + 2-Methoxy-1-propanol), and (1-Methoxy-2-propanol + 2-Methoxy-1-propanol) at 101.3 kPa
-
Experimental Surface Tensions and Derived Surface Properties of Binary Mixtures of Water + Alkoxyethanols (C1Em, m = 1, 2, 3) and Water + Ethylene Glycol Dimethyl Ether (C1E1C1) at (298.15, 308.15, and 318.15) K
-
Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
-
Evaluation of the 2-Methoxyethanol as Entrainer in Ethanol Water and 1-Propanol Water Mixtures
