Datasets
-
Mole fraction (12)
-
Pvap - Vapor or sublimation pressure, kPa (4)
Mole fraction of Carbon dioxide (2)
[ref]
| Temperature, K - Liquid mixture 1 |
Mole fraction of Carbon dioxide (2) - Liquid mixture 2 |
| 303.15 |
0.9900 |
Mole fraction of Carbon dioxide (2)
[ref]
| Temperature, K - Liquid mixture 1 |
Mole fraction of Carbon dioxide (2) - Liquid mixture 1 |
| 303.15 |
0.5416 |
Mole fraction of Carbon dioxide (2)
[ref]
| Temperature, K - Liquid mixture 1 |
Mole fraction of Carbon dioxide (2) - Gas |
| 303.15 |
0.9940 |
Mole fraction of Carbon dioxide (2)
[ref]
Operational condition: Temperature, K =
303.15 (Liquid mixture 1)
| Pressure, kPa - Liquid mixture 1 |
Mole fraction of Carbon dioxide (2) - Liquid mixture 1 |
| 7185.00 |
0.5416 |
| 7955.00 |
0.5614 |
| 8220.00 |
0.5669 |
| 8825.00 |
0.5704 |
| 9011.00 |
0.5708 |
| 9334.00 |
0.5716 |
| 9826.00 |
0.5727 |
| 10097.00 |
0.5746 |
| 10127.00 |
0.5752 |
| 10405.00 |
0.5766 |
| 10468.00 |
0.5771 |
| 10744.00 |
0.5788 |
| 11771.00 |
0.5804 |
| 12191.00 |
0.5826 |
| 13480.00 |
0.5848 |
| 14957.00 |
0.5868 |
Mole fraction of Carbon dioxide (2)
[ref]
Operational condition: Temperature, K =
303.15 (Liquid mixture 1)
| Pressure, kPa - Liquid mixture 1 |
Mole fraction of Carbon dioxide (2) - Liquid mixture 2 |
| 7185.00 |
0.9900 |
| 7955.00 |
0.9919 |
| 8220.00 |
0.9927 |
| 8825.00 |
0.9925 |
| 9011.00 |
0.9924 |
| 9334.00 |
0.9918 |
| 9826.00 |
0.9916 |
| 10097.00 |
0.9912 |
| 10127.00 |
0.9917 |
| 10405.00 |
0.9914 |
| 10468.00 |
0.9913 |
| 10744.00 |
0.9918 |
| 11771.00 |
0.9911 |
| 12191.00 |
0.9914 |
| 13480.00 |
0.9913 |
| 14957.00 |
0.9911 |
Mole fraction of Carbon dioxide (2)
[ref]
| Fixed |
Measured |
| Mole fraction of Carbon dioxide (2) - Liquid |
Temperature, K - Liquid |
Mole fraction of Carbon dioxide (2) - Gas |
| 0.3066 |
313.15 |
0.9966 |
| 0.3128 |
313.15 |
0.9968 |
| 0.3789 |
313.15 |
0.9976 |
| 0.4518 |
313.15 |
0.9979 |
| 0.4902 |
313.15 |
0.9982 |
| 0.5449 |
313.15 |
0.9984 |
| 0.5867 |
313.15 |
0.9983 |
| 0.6135 |
313.15 |
0.9984 |
| 0.6336 |
313.15 |
0.9984 |
| 0.6344 |
313.15 |
0.9984 |
| 0.6358 |
313.15 |
0.9985 |
| 0.6366 |
313.15 |
0.9984 |
| 0.6385 |
313.15 |
0.9983 |
| 0.6387 |
313.15 |
0.9984 |
| 0.6392 |
313.15 |
0.9984 |
| 0.6498 |
313.15 |
0.9984 |
| 0.6504 |
313.15 |
0.9983 |
| 0.6516 |
313.15 |
0.9984 |
| 0.6532 |
313.15 |
0.9985 |
| 0.6555 |
313.15 |
0.9984 |
| 0.6569 |
313.15 |
0.9984 |
| 0.6572 |
313.15 |
0.9985 |
| 0.6574 |
313.15 |
0.9984 |
| 0.6578 |
313.15 |
0.9983 |
| 0.6582 |
313.15 |
0.9983 |
| 0.6586 |
313.15 |
0.9983 |
| 0.6593 |
313.15 |
0.9981 |
| 0.6598 |
313.15 |
0.9981 |
| 0.6602 |
313.15 |
0.9981 |
| 0.6607 |
313.15 |
0.9981 |
| 0.6631 |
313.15 |
0.9980 |
| 0.6642 |
313.15 |
0.9980 |
| 0.6692 |
313.15 |
0.9979 |
| 0.6715 |
313.15 |
0.9979 |
| 0.6735 |
313.15 |
0.9978 |
| 0.6741 |
313.15 |
0.9978 |
| 0.6764 |
313.15 |
0.9978 |
| 0.6755 |
313.15 |
0.9977 |
| 0.6783 |
313.15 |
0.9977 |
| 0.6798 |
313.15 |
0.9976 |
| 0.2187 |
323.15 |
0.9984 |
| 0.2190 |
323.15 |
0.9984 |
| 0.2191 |
323.15 |
0.9984 |
| 0.2686 |
323.15 |
0.9985 |
| 0.2690 |
323.15 |
0.9985 |
| 0.2691 |
323.15 |
0.9985 |
| 0.2707 |
323.15 |
0.9985 |
| 0.3089 |
323.15 |
0.9988 |
| 0.3091 |
323.15 |
0.9988 |
| 0.3143 |
323.15 |
0.9988 |
| 0.3167 |
323.15 |
0.9988 |
| 0.3451 |
323.15 |
0.9989 |
| 0.3482 |
323.15 |
0.9989 |
| 0.3544 |
323.15 |
0.9989 |
| 0.3872 |
323.15 |
0.9989 |
| 0.3883 |
323.15 |
0.9989 |
| 0.3927 |
323.15 |
0.9989 |
| 0.3934 |
323.15 |
0.9989 |
| 0.4497 |
323.15 |
0.9988 |
| 0.4503 |
323.15 |
0.9988 |
| 0.4567 |
323.15 |
0.9988 |
| 0.4591 |
323.15 |
0.9988 |
| 0.4925 |
323.15 |
0.9989 |
| 0.5347 |
323.15 |
0.9988 |
| 0.5352 |
323.15 |
0.9988 |
| 0.5698 |
323.15 |
0.9987 |
| 0.5749 |
323.15 |
0.9987 |
| 0.6072 |
323.15 |
0.9987 |
| 0.6266 |
323.15 |
0.9986 |
| 0.6295 |
323.15 |
0.9986 |
| 0.6305 |
323.15 |
0.9986 |
| 0.6313 |
323.15 |
0.9986 |
| 0.6409 |
323.15 |
0.9986 |
| 0.6414 |
323.15 |
0.9986 |
| 0.6443 |
323.15 |
0.9985 |
| 0.6467 |
323.15 |
0.9984 |
| 0.6477 |
323.15 |
0.9979 |
| 0.6499 |
323.15 |
0.9978 |
| 0.1116 |
333.15 |
0.9988 |
| 0.1181 |
333.15 |
0.9987 |
| 0.1292 |
333.15 |
0.9988 |
| 0.1559 |
333.15 |
0.9989 |
| 0.1631 |
333.15 |
0.9990 |
| 0.2291 |
333.15 |
0.9992 |
| 0.2327 |
333.15 |
0.9992 |
| 0.2614 |
333.15 |
0.9991 |
| 0.2702 |
333.15 |
0.9991 |
| 0.2874 |
333.15 |
0.9992 |
| 0.3391 |
333.15 |
0.9994 |
| 0.3425 |
333.15 |
0.9995 |
| 0.3515 |
333.15 |
0.9994 |
| 0.3822 |
333.15 |
0.9995 |
| 0.3857 |
333.15 |
0.9996 |
| 0.4119 |
333.15 |
0.9997 |
| 0.4189 |
333.15 |
0.9996 |
| 0.4263 |
333.15 |
0.9996 |
| 0.4968 |
333.15 |
0.9997 |
| 0.5024 |
333.15 |
0.9997 |
| 0.5435 |
333.15 |
0.9995 |
| 0.5452 |
333.15 |
0.9995 |
| 0.5779 |
333.15 |
0.9993 |
| 0.5795 |
333.15 |
0.9993 |
| 0.6255 |
333.15 |
0.9973 |
| 0.6281 |
333.15 |
0.9972 |
| 0.2847 |
303.15 |
0.9918 |
| 0.2993 |
303.15 |
0.9923 |
| 0.3036 |
303.15 |
0.9927 |
| 0.3517 |
303.15 |
0.9941 |
| 0.3599 |
303.15 |
0.9949 |
| 0.3659 |
303.15 |
0.9948 |
| 0.4147 |
303.15 |
0.9946 |
| 0.4245 |
303.15 |
0.9947 |
| 0.4619 |
303.15 |
0.9946 |
| 0.4672 |
303.15 |
0.9946 |
| 0.5026 |
303.15 |
0.9943 |
| 0.5045 |
303.15 |
0.9945 |
| 0.5369 |
303.15 |
0.9935 |
| 0.5371 |
303.15 |
0.9941 |
| 0.5394 |
303.15 |
0.9939 |
| 0.5416 |
303.15 |
0.9940 |
Mole fraction of Carbon dioxide (2)
[ref]
| Temperature, K - Liquid mixture 1 |
Mole fraction of Carbon dioxide (2) - Liquid mixture 2 |
| 303.15 |
0.9900 |
Mole fraction of Carbon dioxide (2)
[ref]
| Temperature, K - Liquid mixture 1 |
Mole fraction of Carbon dioxide (2) - Liquid mixture 1 |
| 303.15 |
0.5416 |
Mole fraction of Carbon dioxide (2)
[ref]
| Temperature, K - Liquid mixture 1 |
Mole fraction of Carbon dioxide (2) - Gas |
| 303.15 |
0.9940 |
Mole fraction of Carbon dioxide (2)
[ref]
Operational condition: Temperature, K =
303.15 (Liquid mixture 1)
| Pressure, kPa - Liquid mixture 1 |
Mole fraction of Carbon dioxide (2) - Liquid mixture 1 |
| 7185.00 |
0.5416 |
| 7955.00 |
0.5614 |
| 8220.00 |
0.5669 |
| 8825.00 |
0.5704 |
| 9011.00 |
0.5708 |
| 9334.00 |
0.5716 |
| 9826.00 |
0.5727 |
| 10097.00 |
0.5746 |
| 10127.00 |
0.5752 |
| 10405.00 |
0.5766 |
| 10468.00 |
0.5771 |
| 10744.00 |
0.5788 |
| 11771.00 |
0.5804 |
| 12191.00 |
0.5826 |
| 13480.00 |
0.5848 |
| 14957.00 |
0.5868 |
Mole fraction of Carbon dioxide (2)
[ref]
Operational condition: Temperature, K =
303.15 (Liquid mixture 1)
| Pressure, kPa - Liquid mixture 1 |
Mole fraction of Carbon dioxide (2) - Liquid mixture 2 |
| 7185.00 |
0.9900 |
| 7955.00 |
0.9919 |
| 8220.00 |
0.9927 |
| 8825.00 |
0.9925 |
| 9011.00 |
0.9924 |
| 9334.00 |
0.9918 |
| 9826.00 |
0.9916 |
| 10097.00 |
0.9912 |
| 10127.00 |
0.9917 |
| 10405.00 |
0.9914 |
| 10468.00 |
0.9913 |
| 10744.00 |
0.9918 |
| 11771.00 |
0.9911 |
| 12191.00 |
0.9914 |
| 13480.00 |
0.9913 |
| 14957.00 |
0.9911 |
Mole fraction of Carbon dioxide (2)
[ref]
| Fixed |
Measured |
| Mole fraction of Carbon dioxide (2) - Liquid |
Temperature, K - Liquid |
Mole fraction of Carbon dioxide (2) - Gas |
| 0.3066 |
313.15 |
0.9966 |
| 0.3128 |
313.15 |
0.9968 |
| 0.3789 |
313.15 |
0.9976 |
| 0.4518 |
313.15 |
0.9979 |
| 0.4902 |
313.15 |
0.9982 |
| 0.5449 |
313.15 |
0.9984 |
| 0.5867 |
313.15 |
0.9983 |
| 0.6135 |
313.15 |
0.9984 |
| 0.6336 |
313.15 |
0.9984 |
| 0.6344 |
313.15 |
0.9984 |
| 0.6358 |
313.15 |
0.9985 |
| 0.6366 |
313.15 |
0.9984 |
| 0.6385 |
313.15 |
0.9983 |
| 0.6387 |
313.15 |
0.9984 |
| 0.6392 |
313.15 |
0.9984 |
| 0.6498 |
313.15 |
0.9984 |
| 0.6504 |
313.15 |
0.9983 |
| 0.6516 |
313.15 |
0.9984 |
| 0.6532 |
313.15 |
0.9985 |
| 0.6555 |
313.15 |
0.9984 |
| 0.6569 |
313.15 |
0.9984 |
| 0.6572 |
313.15 |
0.9985 |
| 0.6574 |
313.15 |
0.9984 |
| 0.6578 |
313.15 |
0.9983 |
| 0.6582 |
313.15 |
0.9983 |
| 0.6586 |
313.15 |
0.9983 |
| 0.6593 |
313.15 |
0.9981 |
| 0.6598 |
313.15 |
0.9981 |
| 0.6602 |
313.15 |
0.9981 |
| 0.6607 |
313.15 |
0.9981 |
| 0.6631 |
313.15 |
0.9980 |
| 0.6642 |
313.15 |
0.9980 |
| 0.6692 |
313.15 |
0.9979 |
| 0.6715 |
313.15 |
0.9979 |
| 0.6735 |
313.15 |
0.9978 |
| 0.6741 |
313.15 |
0.9978 |
| 0.6764 |
313.15 |
0.9978 |
| 0.6755 |
313.15 |
0.9977 |
| 0.6783 |
313.15 |
0.9977 |
| 0.6798 |
313.15 |
0.9976 |
| 0.2187 |
323.15 |
0.9984 |
| 0.2190 |
323.15 |
0.9984 |
| 0.2191 |
323.15 |
0.9984 |
| 0.2686 |
323.15 |
0.9985 |
| 0.2690 |
323.15 |
0.9985 |
| 0.2691 |
323.15 |
0.9985 |
| 0.2707 |
323.15 |
0.9985 |
| 0.3089 |
323.15 |
0.9988 |
| 0.3091 |
323.15 |
0.9988 |
| 0.3143 |
323.15 |
0.9988 |
| 0.3167 |
323.15 |
0.9988 |
| 0.3451 |
323.15 |
0.9989 |
| 0.3482 |
323.15 |
0.9989 |
| 0.3544 |
323.15 |
0.9989 |
| 0.3872 |
323.15 |
0.9989 |
| 0.3883 |
323.15 |
0.9989 |
| 0.3927 |
323.15 |
0.9989 |
| 0.3934 |
323.15 |
0.9989 |
| 0.4497 |
323.15 |
0.9988 |
| 0.4503 |
323.15 |
0.9988 |
| 0.4567 |
323.15 |
0.9988 |
| 0.4591 |
323.15 |
0.9988 |
| 0.4925 |
323.15 |
0.9989 |
| 0.5347 |
323.15 |
0.9988 |
| 0.5352 |
323.15 |
0.9988 |
| 0.5698 |
323.15 |
0.9987 |
| 0.5749 |
323.15 |
0.9987 |
| 0.6072 |
323.15 |
0.9987 |
| 0.6266 |
323.15 |
0.9986 |
| 0.6295 |
323.15 |
0.9986 |
| 0.6305 |
323.15 |
0.9986 |
| 0.6313 |
323.15 |
0.9986 |
| 0.6409 |
323.15 |
0.9986 |
| 0.6414 |
323.15 |
0.9986 |
| 0.6443 |
323.15 |
0.9985 |
| 0.6467 |
323.15 |
0.9984 |
| 0.6477 |
323.15 |
0.9979 |
| 0.6499 |
323.15 |
0.9978 |
| 0.1116 |
333.15 |
0.9988 |
| 0.1181 |
333.15 |
0.9987 |
| 0.1292 |
333.15 |
0.9988 |
| 0.1559 |
333.15 |
0.9989 |
| 0.1631 |
333.15 |
0.9990 |
| 0.2291 |
333.15 |
0.9992 |
| 0.2327 |
333.15 |
0.9992 |
| 0.2614 |
333.15 |
0.9991 |
| 0.2702 |
333.15 |
0.9991 |
| 0.2874 |
333.15 |
0.9992 |
| 0.3391 |
333.15 |
0.9994 |
| 0.3425 |
333.15 |
0.9995 |
| 0.3515 |
333.15 |
0.9994 |
| 0.3822 |
333.15 |
0.9995 |
| 0.3857 |
333.15 |
0.9996 |
| 0.4119 |
333.15 |
0.9997 |
| 0.4189 |
333.15 |
0.9996 |
| 0.4263 |
333.15 |
0.9996 |
| 0.4968 |
333.15 |
0.9997 |
| 0.5024 |
333.15 |
0.9997 |
| 0.5435 |
333.15 |
0.9995 |
| 0.5452 |
333.15 |
0.9995 |
| 0.5779 |
333.15 |
0.9993 |
| 0.5795 |
333.15 |
0.9993 |
| 0.6255 |
333.15 |
0.9973 |
| 0.6281 |
333.15 |
0.9972 |
| 0.2847 |
303.15 |
0.9918 |
| 0.2993 |
303.15 |
0.9923 |
| 0.3036 |
303.15 |
0.9927 |
| 0.3517 |
303.15 |
0.9941 |
| 0.3599 |
303.15 |
0.9949 |
| 0.3659 |
303.15 |
0.9948 |
| 0.4147 |
303.15 |
0.9946 |
| 0.4245 |
303.15 |
0.9947 |
| 0.4619 |
303.15 |
0.9946 |
| 0.4672 |
303.15 |
0.9946 |
| 0.5026 |
303.15 |
0.9943 |
| 0.5045 |
303.15 |
0.9945 |
| 0.5369 |
303.15 |
0.9935 |
| 0.5371 |
303.15 |
0.9941 |
| 0.5394 |
303.15 |
0.9939 |
| 0.5416 |
303.15 |
0.9940 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Mole fraction of Carbon dioxide (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
| 0.3066 |
313.15 |
2709.00 |
| 0.3128 |
313.15 |
2803.00 |
| 0.3789 |
313.15 |
3853.00 |
| 0.4518 |
313.15 |
4995.00 |
| 0.4902 |
313.15 |
5802.00 |
| 0.5449 |
313.15 |
6701.00 |
| 0.5867 |
313.15 |
7640.00 |
| 0.6135 |
313.15 |
8651.00 |
| 0.6336 |
313.15 |
9244.00 |
| 0.6344 |
313.15 |
9316.00 |
| 0.6358 |
313.15 |
9339.00 |
| 0.6366 |
313.15 |
9360.00 |
| 0.6385 |
313.15 |
9381.00 |
| 0.6387 |
313.15 |
9412.00 |
| 0.6392 |
313.15 |
9475.00 |
| 0.6498 |
313.15 |
10799.00 |
| 0.6504 |
313.15 |
10953.00 |
| 0.6516 |
313.15 |
11059.00 |
| 0.6532 |
313.15 |
11500.00 |
| 0.6555 |
313.15 |
11668.00 |
| 0.6569 |
313.15 |
11747.00 |
| 0.6572 |
313.15 |
11831.00 |
| 0.6574 |
313.15 |
11889.00 |
| 0.6578 |
313.15 |
11900.00 |
| 0.6582 |
313.15 |
11998.00 |
| 0.6586 |
313.15 |
12097.00 |
| 0.6593 |
313.15 |
12203.00 |
| 0.6598 |
313.15 |
12275.00 |
| 0.6602 |
313.15 |
12304.00 |
| 0.6607 |
313.15 |
12465.00 |
| 0.6631 |
313.15 |
12746.00 |
| 0.6642 |
313.15 |
12750.00 |
| 0.6692 |
313.15 |
13768.00 |
| 0.6715 |
313.15 |
14023.00 |
| 0.6735 |
313.15 |
14441.00 |
| 0.6741 |
313.15 |
14519.00 |
| 0.6764 |
313.15 |
14785.00 |
| 0.6755 |
313.15 |
14800.00 |
| 0.6783 |
313.15 |
15058.00 |
| 0.6798 |
313.15 |
15398.00 |
| 0.2187 |
323.15 |
2193.00 |
| 0.2190 |
323.15 |
2249.00 |
| 0.2191 |
323.15 |
2289.00 |
| 0.2686 |
323.15 |
2936.00 |
| 0.2690 |
323.15 |
2973.00 |
| 0.2691 |
323.15 |
3019.00 |
| 0.2707 |
323.15 |
3070.00 |
| 0.3089 |
323.15 |
3652.00 |
| 0.3091 |
323.15 |
3714.00 |
| 0.3143 |
323.15 |
3782.00 |
| 0.3167 |
323.15 |
3849.00 |
| 0.3451 |
323.15 |
4508.00 |
| 0.3482 |
323.15 |
4541.00 |
| 0.3544 |
323.15 |
4627.00 |
| 0.3872 |
323.15 |
5332.00 |
| 0.3883 |
323.15 |
5374.00 |
| 0.3927 |
323.15 |
5417.00 |
| 0.3934 |
323.15 |
5454.00 |
| 0.4497 |
323.15 |
6289.00 |
| 0.4503 |
323.15 |
6344.00 |
| 0.4567 |
323.15 |
6377.00 |
| 0.4591 |
323.15 |
6408.00 |
| 0.4925 |
323.15 |
7410.00 |
| 0.5347 |
323.15 |
8333.00 |
| 0.5352 |
323.15 |
8372.00 |
| 0.5698 |
323.15 |
9310.00 |
| 0.5749 |
323.15 |
9359.00 |
| 0.6072 |
323.15 |
10294.00 |
| 0.6266 |
323.15 |
11118.00 |
| 0.6295 |
323.15 |
11914.00 |
| 0.6305 |
323.15 |
11988.00 |
| 0.6313 |
323.15 |
12110.00 |
| 0.6409 |
323.15 |
12569.00 |
| 0.6414 |
323.15 |
12699.00 |
| 0.6443 |
323.15 |
13032.00 |
| 0.6467 |
323.15 |
13314.00 |
| 0.6477 |
323.15 |
14594.00 |
| 0.6499 |
323.15 |
14721.00 |
| 0.1116 |
333.15 |
1127.00 |
| 0.1181 |
333.15 |
1217.00 |
| 0.1292 |
333.15 |
1323.00 |
| 0.1559 |
333.15 |
1723.00 |
| 0.1631 |
333.15 |
1834.00 |
| 0.2291 |
333.15 |
2826.00 |
| 0.2327 |
333.15 |
2997.00 |
| 0.2614 |
333.15 |
3510.00 |
| 0.2702 |
333.15 |
3684.00 |
| 0.2874 |
333.15 |
3827.00 |
| 0.3391 |
333.15 |
4721.00 |
| 0.3425 |
333.15 |
4840.00 |
| 0.3515 |
333.15 |
5006.00 |
| 0.3822 |
333.15 |
5535.00 |
| 0.3857 |
333.15 |
5627.00 |
| 0.4119 |
333.15 |
6240.00 |
| 0.4189 |
333.15 |
6394.00 |
| 0.4263 |
333.15 |
6533.00 |
| 0.4968 |
333.15 |
7758.00 |
| 0.5024 |
333.15 |
7892.00 |
| 0.5435 |
333.15 |
8817.00 |
| 0.5452 |
333.15 |
8903.00 |
| 0.5779 |
333.15 |
9909.00 |
| 0.5795 |
333.15 |
9952.00 |
| 0.6255 |
333.15 |
12527.00 |
| 0.6281 |
333.15 |
12678.00 |
| 0.2847 |
303.15 |
1622.00 |
| 0.2993 |
303.15 |
1746.00 |
| 0.3036 |
303.15 |
1854.00 |
| 0.3517 |
303.15 |
2661.00 |
| 0.3599 |
303.15 |
2834.00 |
| 0.3659 |
303.15 |
2961.00 |
| 0.4147 |
303.15 |
3910.00 |
| 0.4245 |
303.15 |
4068.00 |
| 0.4619 |
303.15 |
4764.00 |
| 0.4672 |
303.15 |
4874.00 |
| 0.5026 |
303.15 |
5601.00 |
| 0.5045 |
303.15 |
5711.00 |
| 0.5369 |
303.15 |
6997.00 |
| 0.5371 |
303.15 |
7003.00 |
| 0.5394 |
303.15 |
7068.00 |
| 0.5416 |
303.15 |
7185.00 |
Vapor or sublimation pressure, kPa
[ref]
| Temperature, K - Liquid mixture 1 |
Vapor or sublimation pressure, kPa - Liquid mixture 1 |
| 284.16 |
4486.00 |
| 285.20 |
4657.00 |
| 286.10 |
4768.00 |
| 286.95 |
4880.00 |
| 287.65 |
4976.00 |
| 289.05 |
5086.00 |
| 289.90 |
5204.00 |
| 290.90 |
5328.00 |
| 291.80 |
5454.00 |
| 292.65 |
5569.00 |
| 292.95 |
5634.00 |
| 293.55 |
5695.00 |
| 294.50 |
5824.00 |
| 295.35 |
5964.00 |
| 296.25 |
6074.00 |
| 297.15 |
6199.00 |
| 298.25 |
6343.00 |
| 299.15 |
6482.00 |
| 300.20 |
6624.00 |
| 300.95 |
6769.00 |
| 302.25 |
6910.00 |
| 302.85 |
7057.00 |
| 303.15 |
7185.00 |
| 303.35 |
7205.00 |
| 304.00 |
7369.00 |
| 304.35 |
7389.00 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Mole fraction of Carbon dioxide (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
| 0.3066 |
313.15 |
2709.00 |
| 0.3128 |
313.15 |
2803.00 |
| 0.3789 |
313.15 |
3853.00 |
| 0.4518 |
313.15 |
4995.00 |
| 0.4902 |
313.15 |
5802.00 |
| 0.5449 |
313.15 |
6701.00 |
| 0.5867 |
313.15 |
7640.00 |
| 0.6135 |
313.15 |
8651.00 |
| 0.6336 |
313.15 |
9244.00 |
| 0.6344 |
313.15 |
9316.00 |
| 0.6358 |
313.15 |
9339.00 |
| 0.6366 |
313.15 |
9360.00 |
| 0.6385 |
313.15 |
9381.00 |
| 0.6387 |
313.15 |
9412.00 |
| 0.6392 |
313.15 |
9475.00 |
| 0.6498 |
313.15 |
10799.00 |
| 0.6504 |
313.15 |
10953.00 |
| 0.6516 |
313.15 |
11059.00 |
| 0.6532 |
313.15 |
11500.00 |
| 0.6555 |
313.15 |
11668.00 |
| 0.6569 |
313.15 |
11747.00 |
| 0.6572 |
313.15 |
11831.00 |
| 0.6574 |
313.15 |
11889.00 |
| 0.6578 |
313.15 |
11900.00 |
| 0.6582 |
313.15 |
11998.00 |
| 0.6586 |
313.15 |
12097.00 |
| 0.6593 |
313.15 |
12203.00 |
| 0.6598 |
313.15 |
12275.00 |
| 0.6602 |
313.15 |
12304.00 |
| 0.6607 |
313.15 |
12465.00 |
| 0.6631 |
313.15 |
12746.00 |
| 0.6642 |
313.15 |
12750.00 |
| 0.6692 |
313.15 |
13768.00 |
| 0.6715 |
313.15 |
14023.00 |
| 0.6735 |
313.15 |
14441.00 |
| 0.6741 |
313.15 |
14519.00 |
| 0.6764 |
313.15 |
14785.00 |
| 0.6755 |
313.15 |
14800.00 |
| 0.6783 |
313.15 |
15058.00 |
| 0.6798 |
313.15 |
15398.00 |
| 0.2187 |
323.15 |
2193.00 |
| 0.2190 |
323.15 |
2249.00 |
| 0.2191 |
323.15 |
2289.00 |
| 0.2686 |
323.15 |
2936.00 |
| 0.2690 |
323.15 |
2973.00 |
| 0.2691 |
323.15 |
3019.00 |
| 0.2707 |
323.15 |
3070.00 |
| 0.3089 |
323.15 |
3652.00 |
| 0.3091 |
323.15 |
3714.00 |
| 0.3143 |
323.15 |
3782.00 |
| 0.3167 |
323.15 |
3849.00 |
| 0.3451 |
323.15 |
4508.00 |
| 0.3482 |
323.15 |
4541.00 |
| 0.3544 |
323.15 |
4627.00 |
| 0.3872 |
323.15 |
5332.00 |
| 0.3883 |
323.15 |
5374.00 |
| 0.3927 |
323.15 |
5417.00 |
| 0.3934 |
323.15 |
5454.00 |
| 0.4497 |
323.15 |
6289.00 |
| 0.4503 |
323.15 |
6344.00 |
| 0.4567 |
323.15 |
6377.00 |
| 0.4591 |
323.15 |
6408.00 |
| 0.4925 |
323.15 |
7410.00 |
| 0.5347 |
323.15 |
8333.00 |
| 0.5352 |
323.15 |
8372.00 |
| 0.5698 |
323.15 |
9310.00 |
| 0.5749 |
323.15 |
9359.00 |
| 0.6072 |
323.15 |
10294.00 |
| 0.6266 |
323.15 |
11118.00 |
| 0.6295 |
323.15 |
11914.00 |
| 0.6305 |
323.15 |
11988.00 |
| 0.6313 |
323.15 |
12110.00 |
| 0.6409 |
323.15 |
12569.00 |
| 0.6414 |
323.15 |
12699.00 |
| 0.6443 |
323.15 |
13032.00 |
| 0.6467 |
323.15 |
13314.00 |
| 0.6477 |
323.15 |
14594.00 |
| 0.6499 |
323.15 |
14721.00 |
| 0.1116 |
333.15 |
1127.00 |
| 0.1181 |
333.15 |
1217.00 |
| 0.1292 |
333.15 |
1323.00 |
| 0.1559 |
333.15 |
1723.00 |
| 0.1631 |
333.15 |
1834.00 |
| 0.2291 |
333.15 |
2826.00 |
| 0.2327 |
333.15 |
2997.00 |
| 0.2614 |
333.15 |
3510.00 |
| 0.2702 |
333.15 |
3684.00 |
| 0.2874 |
333.15 |
3827.00 |
| 0.3391 |
333.15 |
4721.00 |
| 0.3425 |
333.15 |
4840.00 |
| 0.3515 |
333.15 |
5006.00 |
| 0.3822 |
333.15 |
5535.00 |
| 0.3857 |
333.15 |
5627.00 |
| 0.4119 |
333.15 |
6240.00 |
| 0.4189 |
333.15 |
6394.00 |
| 0.4263 |
333.15 |
6533.00 |
| 0.4968 |
333.15 |
7758.00 |
| 0.5024 |
333.15 |
7892.00 |
| 0.5435 |
333.15 |
8817.00 |
| 0.5452 |
333.15 |
8903.00 |
| 0.5779 |
333.15 |
9909.00 |
| 0.5795 |
333.15 |
9952.00 |
| 0.6255 |
333.15 |
12527.00 |
| 0.6281 |
333.15 |
12678.00 |
| 0.2847 |
303.15 |
1622.00 |
| 0.2993 |
303.15 |
1746.00 |
| 0.3036 |
303.15 |
1854.00 |
| 0.3517 |
303.15 |
2661.00 |
| 0.3599 |
303.15 |
2834.00 |
| 0.3659 |
303.15 |
2961.00 |
| 0.4147 |
303.15 |
3910.00 |
| 0.4245 |
303.15 |
4068.00 |
| 0.4619 |
303.15 |
4764.00 |
| 0.4672 |
303.15 |
4874.00 |
| 0.5026 |
303.15 |
5601.00 |
| 0.5045 |
303.15 |
5711.00 |
| 0.5369 |
303.15 |
6997.00 |
| 0.5371 |
303.15 |
7003.00 |
| 0.5394 |
303.15 |
7068.00 |
| 0.5416 |
303.15 |
7185.00 |
Vapor or sublimation pressure, kPa
[ref]
| Temperature, K - Liquid mixture 1 |
Vapor or sublimation pressure, kPa - Liquid mixture 1 |
| 284.16 |
4486.00 |
| 285.20 |
4657.00 |
| 286.10 |
4768.00 |
| 286.95 |
4880.00 |
| 287.65 |
4976.00 |
| 289.05 |
5086.00 |
| 289.90 |
5204.00 |
| 290.90 |
5328.00 |
| 291.80 |
5454.00 |
| 292.65 |
5569.00 |
| 292.95 |
5634.00 |
| 293.55 |
5695.00 |
| 294.50 |
5824.00 |
| 295.35 |
5964.00 |
| 296.25 |
6074.00 |
| 297.15 |
6199.00 |
| 298.25 |
6343.00 |
| 299.15 |
6482.00 |
| 300.20 |
6624.00 |
| 300.95 |
6769.00 |
| 302.25 |
6910.00 |
| 302.85 |
7057.00 |
| 303.15 |
7185.00 |
| 303.35 |
7205.00 |
| 304.00 |
7369.00 |
| 304.35 |
7389.00 |
Sources