Mixture of Carbon dioxide + n-Propyl chloride
Datasets
-
Mole fraction (2)
-
Pvap - Vapor or sublimation pressure, kPa (2)
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 |
0.1231 |
303.15 |
0.9184 |
0.1688 |
303.15 |
0.9415 |
0.2181 |
303.15 |
0.9631 |
0.3079 |
303.15 |
0.9720 |
0.4243 |
303.15 |
0.9887 |
0.4972 |
303.15 |
0.9895 |
0.5195 |
303.15 |
0.9895 |
0.5659 |
303.15 |
0.9903 |
0.6024 |
303.15 |
0.9861 |
0.6444 |
303.15 |
0.9887 |
0.6901 |
303.15 |
0.9903 |
0.7132 |
303.15 |
0.9946 |
0.7653 |
303.15 |
0.9920 |
0.8184 |
303.15 |
0.9962 |
0.8440 |
303.15 |
0.9962 |
0.8879 |
303.15 |
0.9946 |
0.9135 |
303.15 |
0.9928 |
0.9572 |
303.15 |
0.9946 |
0.9746 |
303.15 |
0.9936 |
0.9828 |
303.15 |
0.9954 |
0.9946 |
303.15 |
0.9995 |
0.2439 |
313.15 |
0.9483 |
0.3028 |
313.15 |
0.9588 |
0.3801 |
313.15 |
0.9701 |
0.5034 |
313.15 |
0.9787 |
0.6135 |
313.15 |
0.9848 |
0.6517 |
313.15 |
0.9868 |
0.6665 |
313.15 |
0.9930 |
0.6848 |
313.15 |
0.9887 |
0.7047 |
313.15 |
0.9887 |
0.7480 |
313.15 |
0.9922 |
0.7524 |
313.15 |
0.9912 |
0.7742 |
313.15 |
0.9879 |
0.8124 |
313.15 |
0.9911 |
0.8393 |
313.15 |
0.9879 |
0.8627 |
313.15 |
0.9922 |
0.8834 |
313.15 |
0.9895 |
0.9149 |
313.15 |
0.9930 |
0.9295 |
313.15 |
0.9911 |
0.9373 |
313.15 |
0.9911 |
0.9451 |
313.15 |
0.9879 |
0.9555 |
313.15 |
0.9868 |
0.1203 |
328.15 |
0.8677 |
0.1962 |
328.15 |
0.9174 |
0.3087 |
328.15 |
0.9495 |
0.3749 |
328.15 |
0.9613 |
0.4518 |
328.15 |
0.9762 |
0.5205 |
328.15 |
0.9788 |
0.6123 |
328.15 |
0.9810 |
0.6874 |
328.15 |
0.9885 |
0.7297 |
328.15 |
0.9877 |
0.7841 |
328.15 |
0.9851 |
0.8289 |
328.15 |
0.9844 |
0.8685 |
328.15 |
0.9892 |
0.9197 |
328.15 |
0.9869 |
0.9546 |
328.15 |
0.9836 |
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 |
0.1231 |
303.15 |
0.9184 |
0.1688 |
303.15 |
0.9415 |
0.2181 |
303.15 |
0.9631 |
0.3079 |
303.15 |
0.9720 |
0.4243 |
303.15 |
0.9887 |
0.4972 |
303.15 |
0.9895 |
0.5195 |
303.15 |
0.9895 |
0.5659 |
303.15 |
0.9903 |
0.6024 |
303.15 |
0.9861 |
0.6444 |
303.15 |
0.9887 |
0.6901 |
303.15 |
0.9903 |
0.7132 |
303.15 |
0.9946 |
0.7653 |
303.15 |
0.9920 |
0.8184 |
303.15 |
0.9962 |
0.8440 |
303.15 |
0.9962 |
0.8879 |
303.15 |
0.9946 |
0.9135 |
303.15 |
0.9928 |
0.9572 |
303.15 |
0.9946 |
0.9746 |
303.15 |
0.9936 |
0.9828 |
303.15 |
0.9954 |
0.9946 |
303.15 |
0.9995 |
0.2439 |
313.15 |
0.9483 |
0.3028 |
313.15 |
0.9588 |
0.3801 |
313.15 |
0.9701 |
0.5034 |
313.15 |
0.9787 |
0.6135 |
313.15 |
0.9848 |
0.6517 |
313.15 |
0.9868 |
0.6665 |
313.15 |
0.9930 |
0.6848 |
313.15 |
0.9887 |
0.7047 |
313.15 |
0.9887 |
0.7480 |
313.15 |
0.9922 |
0.7524 |
313.15 |
0.9912 |
0.7742 |
313.15 |
0.9879 |
0.8124 |
313.15 |
0.9911 |
0.8393 |
313.15 |
0.9879 |
0.8627 |
313.15 |
0.9922 |
0.8834 |
313.15 |
0.9895 |
0.9149 |
313.15 |
0.9930 |
0.9295 |
313.15 |
0.9911 |
0.9373 |
313.15 |
0.9911 |
0.9451 |
313.15 |
0.9879 |
0.9555 |
313.15 |
0.9868 |
0.1203 |
328.15 |
0.8677 |
0.1962 |
328.15 |
0.9174 |
0.3087 |
328.15 |
0.9495 |
0.3749 |
328.15 |
0.9613 |
0.4518 |
328.15 |
0.9762 |
0.5205 |
328.15 |
0.9788 |
0.6123 |
328.15 |
0.9810 |
0.6874 |
328.15 |
0.9885 |
0.7297 |
328.15 |
0.9877 |
0.7841 |
328.15 |
0.9851 |
0.8289 |
328.15 |
0.9844 |
0.8685 |
328.15 |
0.9892 |
0.9197 |
328.15 |
0.9869 |
0.9546 |
328.15 |
0.9836 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (1) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.1231 |
303.15 |
521.00 |
0.1688 |
303.15 |
815.00 |
0.2181 |
303.15 |
1002.00 |
0.3079 |
303.15 |
1515.00 |
0.4243 |
303.15 |
2059.00 |
0.4972 |
303.15 |
2517.00 |
0.5195 |
303.15 |
2674.00 |
0.5659 |
303.15 |
2914.00 |
0.6024 |
303.15 |
3198.00 |
0.6444 |
303.15 |
3448.00 |
0.6901 |
303.15 |
3868.00 |
0.7132 |
303.15 |
4108.00 |
0.7653 |
303.15 |
4546.00 |
0.8184 |
303.15 |
5037.00 |
0.8440 |
303.15 |
5267.00 |
0.8879 |
303.15 |
5664.00 |
0.9135 |
303.15 |
5937.00 |
0.9572 |
303.15 |
6387.00 |
0.9746 |
303.15 |
6648.00 |
0.9828 |
303.15 |
6804.00 |
0.9946 |
303.15 |
7065.00 |
0.2439 |
313.15 |
1365.00 |
0.3028 |
313.15 |
1753.00 |
0.3801 |
313.15 |
2163.00 |
0.5034 |
313.15 |
3089.00 |
0.6135 |
313.15 |
3804.00 |
0.6517 |
313.15 |
4260.00 |
0.6665 |
313.15 |
4424.00 |
0.6848 |
313.15 |
4612.00 |
0.7047 |
313.15 |
4811.00 |
0.7480 |
313.15 |
5151.00 |
0.7524 |
313.15 |
5246.00 |
0.7742 |
313.15 |
5550.00 |
0.8124 |
313.15 |
5913.00 |
0.8393 |
313.15 |
6112.00 |
0.8627 |
313.15 |
6383.00 |
0.8834 |
313.15 |
6640.00 |
0.9149 |
313.15 |
7107.00 |
0.9295 |
313.15 |
7342.00 |
0.9373 |
313.15 |
7461.00 |
0.9451 |
313.15 |
7601.00 |
0.9555 |
313.15 |
7694.00 |
0.1203 |
328.15 |
822.00 |
0.1962 |
328.15 |
1238.30 |
0.3087 |
328.15 |
1927.00 |
0.3749 |
328.15 |
2424.00 |
0.4518 |
328.15 |
2989.00 |
0.5205 |
328.15 |
3612.00 |
0.6123 |
328.15 |
4482.00 |
0.6874 |
328.15 |
5226.00 |
0.7297 |
328.15 |
5734.00 |
0.7841 |
328.15 |
6423.00 |
0.8289 |
328.15 |
6977.00 |
0.8685 |
328.15 |
7542.00 |
0.9197 |
328.15 |
8242.00 |
0.9546 |
328.15 |
8819.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (1) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.1231 |
303.15 |
521.00 |
0.1688 |
303.15 |
815.00 |
0.2181 |
303.15 |
1002.00 |
0.3079 |
303.15 |
1515.00 |
0.4243 |
303.15 |
2059.00 |
0.4972 |
303.15 |
2517.00 |
0.5195 |
303.15 |
2674.00 |
0.5659 |
303.15 |
2914.00 |
0.6024 |
303.15 |
3198.00 |
0.6444 |
303.15 |
3448.00 |
0.6901 |
303.15 |
3868.00 |
0.7132 |
303.15 |
4108.00 |
0.7653 |
303.15 |
4546.00 |
0.8184 |
303.15 |
5037.00 |
0.8440 |
303.15 |
5267.00 |
0.8879 |
303.15 |
5664.00 |
0.9135 |
303.15 |
5937.00 |
0.9572 |
303.15 |
6387.00 |
0.9746 |
303.15 |
6648.00 |
0.9828 |
303.15 |
6804.00 |
0.9946 |
303.15 |
7065.00 |
0.2439 |
313.15 |
1365.00 |
0.3028 |
313.15 |
1753.00 |
0.3801 |
313.15 |
2163.00 |
0.5034 |
313.15 |
3089.00 |
0.6135 |
313.15 |
3804.00 |
0.6517 |
313.15 |
4260.00 |
0.6665 |
313.15 |
4424.00 |
0.6848 |
313.15 |
4612.00 |
0.7047 |
313.15 |
4811.00 |
0.7480 |
313.15 |
5151.00 |
0.7524 |
313.15 |
5246.00 |
0.7742 |
313.15 |
5550.00 |
0.8124 |
313.15 |
5913.00 |
0.8393 |
313.15 |
6112.00 |
0.8627 |
313.15 |
6383.00 |
0.8834 |
313.15 |
6640.00 |
0.9149 |
313.15 |
7107.00 |
0.9295 |
313.15 |
7342.00 |
0.9373 |
313.15 |
7461.00 |
0.9451 |
313.15 |
7601.00 |
0.9555 |
313.15 |
7694.00 |
0.1203 |
328.15 |
822.00 |
0.1962 |
328.15 |
1238.30 |
0.3087 |
328.15 |
1927.00 |
0.3749 |
328.15 |
2424.00 |
0.4518 |
328.15 |
2989.00 |
0.5205 |
328.15 |
3612.00 |
0.6123 |
328.15 |
4482.00 |
0.6874 |
328.15 |
5226.00 |
0.7297 |
328.15 |
5734.00 |
0.7841 |
328.15 |
6423.00 |
0.8289 |
328.15 |
6977.00 |
0.8685 |
328.15 |
7542.00 |
0.9197 |
328.15 |
8242.00 |
0.9546 |
328.15 |
8819.00 |
Sources