Mixture of Dimethyl sulfide + Ethanol
Datasets
-
Mole fraction (2)
-
Pvap - Vapor or sublimation pressure, kPa (2)
Mole fraction of Ethanol (2)
[ref]
Fixed |
Measured |
Mole fraction of Ethanol (2) - Liquid |
Temperature, K - Liquid |
Mole fraction of Ethanol (2) - Gas |
1.0000 |
350.38 |
1.0000 |
0.9876 |
350.40 |
0.8825 |
0.9679 |
350.40 |
0.7498 |
0.9481 |
350.39 |
0.6559 |
0.8992 |
350.40 |
0.5109 |
0.8500 |
350.40 |
0.4259 |
0.8011 |
350.39 |
0.3701 |
0.7516 |
350.39 |
0.3294 |
0.7014 |
350.39 |
0.2982 |
0.6516 |
350.39 |
0.2734 |
0.6008 |
350.39 |
0.2525 |
0.5511 |
350.39 |
0.2351 |
0.5010 |
350.39 |
0.2195 |
0.5007 |
350.38 |
0.2194 |
0.4506 |
350.38 |
0.2052 |
0.4005 |
350.38 |
0.1917 |
0.3498 |
350.39 |
0.1783 |
0.3007 |
350.39 |
0.1650 |
0.2509 |
350.39 |
0.1504 |
0.1998 |
350.39 |
0.1333 |
0.1484 |
350.40 |
0.1125 |
0.0977 |
350.39 |
0.0861 |
0.0469 |
350.39 |
0.0494 |
0.0271 |
350.39 |
0.0309 |
0.0055 |
350.40 |
0.0069 |
0.0000 |
350.40 |
0.0000 |
Mole fraction of Ethanol (2)
[ref]
Fixed |
Measured |
Mole fraction of Ethanol (2) - Liquid |
Temperature, K - Liquid |
Mole fraction of Ethanol (2) - Gas |
1.0000 |
350.38 |
1.0000 |
0.9876 |
350.40 |
0.8825 |
0.9679 |
350.40 |
0.7498 |
0.9481 |
350.39 |
0.6559 |
0.8992 |
350.40 |
0.5109 |
0.8500 |
350.40 |
0.4259 |
0.8011 |
350.39 |
0.3701 |
0.7516 |
350.39 |
0.3294 |
0.7014 |
350.39 |
0.2982 |
0.6516 |
350.39 |
0.2734 |
0.6008 |
350.39 |
0.2525 |
0.5511 |
350.39 |
0.2351 |
0.5010 |
350.39 |
0.2195 |
0.5007 |
350.38 |
0.2194 |
0.4506 |
350.38 |
0.2052 |
0.4005 |
350.38 |
0.1917 |
0.3498 |
350.39 |
0.1783 |
0.3007 |
350.39 |
0.1650 |
0.2509 |
350.39 |
0.1504 |
0.1998 |
350.39 |
0.1333 |
0.1484 |
350.40 |
0.1125 |
0.0977 |
350.39 |
0.0861 |
0.0469 |
350.39 |
0.0494 |
0.0271 |
350.39 |
0.0309 |
0.0055 |
350.40 |
0.0069 |
0.0000 |
350.40 |
0.0000 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Ethanol (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
1.0000 |
350.38 |
96.50 |
0.9876 |
350.40 |
108.40 |
0.9679 |
350.40 |
125.60 |
0.9481 |
350.39 |
141.40 |
0.8992 |
350.40 |
175.10 |
0.8500 |
350.40 |
202.80 |
0.8011 |
350.39 |
225.40 |
0.7516 |
350.39 |
244.30 |
0.7014 |
350.39 |
260.40 |
0.6516 |
350.39 |
273.90 |
0.6008 |
350.39 |
285.70 |
0.5511 |
350.39 |
295.80 |
0.5010 |
350.39 |
304.80 |
0.5007 |
350.38 |
304.30 |
0.4506 |
350.38 |
311.40 |
0.4005 |
350.38 |
317.80 |
0.3498 |
350.39 |
323.80 |
0.3007 |
350.39 |
329.00 |
0.2509 |
350.39 |
333.70 |
0.1998 |
350.39 |
337.90 |
0.1484 |
350.40 |
341.40 |
0.0977 |
350.39 |
343.80 |
0.0469 |
350.39 |
344.20 |
0.0271 |
350.39 |
343.60 |
0.0055 |
350.40 |
342.20 |
0.0000 |
350.40 |
341.70 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Ethanol (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
1.0000 |
350.38 |
96.50 |
0.9876 |
350.40 |
108.40 |
0.9679 |
350.40 |
125.60 |
0.9481 |
350.39 |
141.40 |
0.8992 |
350.40 |
175.10 |
0.8500 |
350.40 |
202.80 |
0.8011 |
350.39 |
225.40 |
0.7516 |
350.39 |
244.30 |
0.7014 |
350.39 |
260.40 |
0.6516 |
350.39 |
273.90 |
0.6008 |
350.39 |
285.70 |
0.5511 |
350.39 |
295.80 |
0.5010 |
350.39 |
304.80 |
0.5007 |
350.38 |
304.30 |
0.4506 |
350.38 |
311.40 |
0.4005 |
350.38 |
317.80 |
0.3498 |
350.39 |
323.80 |
0.3007 |
350.39 |
329.00 |
0.2509 |
350.39 |
333.70 |
0.1998 |
350.39 |
337.90 |
0.1484 |
350.40 |
341.40 |
0.0977 |
350.39 |
343.80 |
0.0469 |
350.39 |
344.20 |
0.0271 |
350.39 |
343.60 |
0.0055 |
350.40 |
342.20 |
0.0000 |
350.40 |
341.70 |
Sources