Operational condition: Pressure, kPa = 93.13 (Gas)
Mole fraction of o-Xylene (2) - Liquid | Mole fraction of o-Xylene (2) - Gas |
---|---|
0.0000 | 0.0000 |
0.0541 | 0.0173 |
0.0888 | 0.0281 |
0.1509 | 0.0492 |
0.2323 | 0.0763 |
0.3590 | 0.1159 |
0.4149 | 0.1249 |
0.5870 | 0.2097 |
0.7345 | 0.3305 |
0.8426 | 0.4525 |
0.9025 | 0.5665 |
0.9498 | 0.7269 |
1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Mole fraction of Carbonic acid, dimethyl ester (1) - Liquid | Mole fraction of Carbonic acid, dimethyl ester (1) - Gas |
---|---|
0.8857 | 0.9432 |
0.7756 | 0.9002 |
0.5892 | 0.8513 |
0.4323 | 0.8143 |
0.3304 | 0.7785 |
0.2627 | 0.7421 |
0.2105 | 0.7052 |
0.1738 | 0.6649 |
0.1451 | 0.6222 |
0.1219 | 0.5759 |
0.1019 | 0.5267 |
0.0839 | 0.4734 |
0.0687 | 0.4201 |
0.0546 | 0.3619 |
0.0410 | 0.2961 |
0.0294 | 0.2295 |
0.0187 | 0.1582 |
0.0091 | 0.0835 |
Operational condition: Pressure, kPa = 93.13 (Gas)
Mole fraction of o-Xylene (2) - Liquid | Mole fraction of o-Xylene (2) - Gas |
---|---|
0.0000 | 0.0000 |
0.0541 | 0.0173 |
0.0888 | 0.0281 |
0.1509 | 0.0492 |
0.2323 | 0.0763 |
0.3590 | 0.1159 |
0.4149 | 0.1249 |
0.5870 | 0.2097 |
0.7345 | 0.3305 |
0.8426 | 0.4525 |
0.9025 | 0.5665 |
0.9498 | 0.7269 |
1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Mole fraction of Carbonic acid, dimethyl ester (1) - Liquid | Mole fraction of Carbonic acid, dimethyl ester (1) - Gas |
---|---|
0.8857 | 0.9432 |
0.7756 | 0.9002 |
0.5892 | 0.8513 |
0.4323 | 0.8143 |
0.3304 | 0.7785 |
0.2627 | 0.7421 |
0.2105 | 0.7052 |
0.1738 | 0.6649 |
0.1451 | 0.6222 |
0.1219 | 0.5759 |
0.1019 | 0.5267 |
0.0839 | 0.4734 |
0.0687 | 0.4201 |
0.0546 | 0.3619 |
0.0410 | 0.2961 |
0.0294 | 0.2295 |
0.0187 | 0.1582 |
0.0091 | 0.0835 |
Operational conditions:
Mole fraction of Carbonic acid, dimethyl ester (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0511 | 0.1112 |
0.1006 | 0.2313 |
0.1503 | 0.3326 |
0.2016 | 0.3898 |
0.2513 | 0.4446 |
0.3024 | 0.5210 |
0.3519 | 0.5745 |
0.3998 | 0.6149 |
0.4514 | 0.6388 |
0.5013 | 0.6503 |
0.5519 | 0.6420 |
0.6007 | 0.6240 |
0.6502 | 0.5946 |
0.7002 | 0.5516 |
0.7504 | 0.5008 |
0.8008 | 0.4340 |
0.8513 | 0.3517 |
0.8998 | 0.2533 |
0.9501 | 0.1349 |
Operational conditions:
Mole fraction of Carbonic acid, dimethyl ester (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.1005 | 0.1363 |
0.1501 | 0.2408 |
0.2014 | 0.3451 |
0.2511 | 0.4269 |
0.2992 | 0.4968 |
0.3516 | 0.5487 |
0.3994 | 0.5861 |
0.4510 | 0.6032 |
0.5009 | 0.6167 |
0.5515 | 0.6100 |
0.6004 | 0.5910 |
0.6499 | 0.5595 |
0.6999 | 0.5166 |
0.7502 | 0.4580 |
0.8006 | 0.3847 |
0.8511 | 0.2965 |
0.8997 | 0.1930 |
Operational conditions:
Mole fraction of Carbonic acid, dimethyl ester (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0511 | 0.1112 |
0.1006 | 0.2313 |
0.1503 | 0.3326 |
0.2016 | 0.3898 |
0.2513 | 0.4446 |
0.3024 | 0.5210 |
0.3519 | 0.5745 |
0.3998 | 0.6149 |
0.4514 | 0.6388 |
0.5013 | 0.6503 |
0.5519 | 0.6420 |
0.6007 | 0.6240 |
0.6502 | 0.5946 |
0.7002 | 0.5516 |
0.7504 | 0.5008 |
0.8008 | 0.4340 |
0.8513 | 0.3517 |
0.8998 | 0.2533 |
0.9501 | 0.1349 |
Operational conditions:
Mole fraction of Carbonic acid, dimethyl ester (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.1005 | 0.1363 |
0.1501 | 0.2408 |
0.2014 | 0.3451 |
0.2511 | 0.4269 |
0.2992 | 0.4968 |
0.3516 | 0.5487 |
0.3994 | 0.5861 |
0.4510 | 0.6032 |
0.5009 | 0.6167 |
0.5515 | 0.6100 |
0.6004 | 0.5910 |
0.6499 | 0.5595 |
0.6999 | 0.5166 |
0.7502 | 0.4580 |
0.8006 | 0.3847 |
0.8511 | 0.2965 |
0.8997 | 0.1930 |
Operational conditions:
Mole fraction of o-Xylene (2) - Liquid | Refractive index (Na D-line) - Liquid |
---|---|
0.0000 | 1.3688 |
0.0450 | 1.377 |
0.1564 | 1.3961 |
0.1622 | 1.3969 |
0.2752 | 1.4149 |
0.3600 | 1.4272 |
0.4516 | 1.4397 |
0.5655 | 1.4556 |
0.6030 | 1.4601 |
0.7134 | 1.4734 |
0.7602 | 1.4795 |
0.8813 | 1.493 |
0.9276 | 1.4973 |
1.0000 | 1.5048 |
Operational conditions:
Mole fraction of o-Xylene (2) - Liquid | Refractive index (Na D-line) - Liquid |
---|---|
0.0000 | 1.3688 |
0.0450 | 1.377 |
0.1564 | 1.3961 |
0.1622 | 1.3969 |
0.2752 | 1.4149 |
0.3600 | 1.4272 |
0.4516 | 1.4397 |
0.5655 | 1.4556 |
0.6030 | 1.4601 |
0.7134 | 1.4734 |
0.7602 | 1.4795 |
0.8813 | 1.493 |
0.9276 | 1.4973 |
1.0000 | 1.5048 |
Operational condition: Pressure, kPa = 93.13 (Gas)
Mole fraction of o-Xylene (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 360.73 |
0.0541 | 361.48 |
0.0888 | 362.09 |
0.1509 | 363.52 |
0.2323 | 365.18 |
0.3590 | 367.71 |
0.4149 | 368.68 |
0.5870 | 374.88 |
0.7345 | 382.02 |
0.8426 | 390.84 |
0.9025 | 397.46 |
0.9498 | 404.50 |
1.0000 | 414.41 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Mole fraction of Carbonic acid, dimethyl ester (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.8857 | 364.68 |
0.7756 | 366.36 |
0.5892 | 369.38 |
0.4323 | 372.39 |
0.3304 | 375.42 |
0.2627 | 378.39 |
0.2105 | 381.38 |
0.1738 | 384.40 |
0.1451 | 387.39 |
0.1219 | 390.41 |
0.1019 | 393.40 |
0.0839 | 396.41 |
0.0687 | 399.42 |
0.0546 | 402.40 |
0.0410 | 405.41 |
0.0294 | 408.43 |
0.0187 | 411.42 |
0.0091 | 414.43 |
1.0000 | 363.36 |
0.0000 | 417.43 |
Operational condition: Pressure, kPa = 93.13 (Gas)
Mole fraction of o-Xylene (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 360.73 |
0.0541 | 361.48 |
0.0888 | 362.09 |
0.1509 | 363.52 |
0.2323 | 365.18 |
0.3590 | 367.71 |
0.4149 | 368.68 |
0.5870 | 374.88 |
0.7345 | 382.02 |
0.8426 | 390.84 |
0.9025 | 397.46 |
0.9498 | 404.50 |
1.0000 | 414.41 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Mole fraction of Carbonic acid, dimethyl ester (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.8857 | 364.68 |
0.7756 | 366.36 |
0.5892 | 369.38 |
0.4323 | 372.39 |
0.3304 | 375.42 |
0.2627 | 378.39 |
0.2105 | 381.38 |
0.1738 | 384.40 |
0.1451 | 387.39 |
0.1219 | 390.41 |
0.1019 | 393.40 |
0.0839 | 396.41 |
0.0687 | 399.42 |
0.0546 | 402.40 |
0.0410 | 405.41 |
0.0294 | 408.43 |
0.0187 | 411.42 |
0.0091 | 414.43 |
1.0000 | 363.36 |
0.0000 | 417.43 |