Mixture of Carbon dioxide + Ethane, 1,2-dimethoxy-
Datasets
-
Mole fraction (2)
-
Pc - Critical pressure, kPa (2)
-
Tc - Critical temperature, K (2)
-
Vapor or sublimation pressure, kPa (2)
Mole fraction of Carbon dioxide (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Mole fraction of Carbon dioxide (1) - Gas |
313.15 |
0.3779 |
0.9925 |
313.15 |
0.5649 |
0.9961 |
313.15 |
0.6932 |
0.9978 |
313.15 |
0.7805 |
0.9987 |
313.15 |
0.8452 |
0.9993 |
313.15 |
0.8978 |
0.9991 |
313.15 |
0.9567 |
0.9983 |
323.15 |
0.3410 |
0.9883 |
323.15 |
0.5221 |
0.9939 |
323.15 |
0.6254 |
0.9970 |
323.15 |
0.7169 |
0.9978 |
323.15 |
0.7857 |
0.9987 |
323.15 |
0.8439 |
0.9983 |
323.15 |
0.9005 |
0.9975 |
323.15 |
0.9437 |
0.9947 |
333.15 |
0.2958 |
0.9805 |
333.15 |
0.4586 |
0.9905 |
333.15 |
0.5922 |
0.9954 |
333.15 |
0.6657 |
0.9970 |
333.15 |
0.7343 |
0.9976 |
333.15 |
0.7948 |
0.9971 |
333.15 |
0.8455 |
0.9965 |
333.15 |
0.8935 |
0.9918 |
333.15 |
0.9833 |
0.9833 |
343.15 |
0.2636 |
0.9782 |
343.15 |
0.3985 |
0.9887 |
343.15 |
0.5189 |
0.9939 |
343.15 |
0.5975 |
0.9955 |
343.15 |
0.6612 |
0.9958 |
343.15 |
0.7257 |
0.9963 |
343.15 |
0.7855 |
0.9961 |
343.15 |
0.8353 |
0.9949 |
Mole fraction of Carbon dioxide (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Mole fraction of Carbon dioxide (1) - Gas |
313.15 |
0.3779 |
0.9925 |
313.15 |
0.5649 |
0.9961 |
313.15 |
0.6932 |
0.9978 |
313.15 |
0.7805 |
0.9987 |
313.15 |
0.8452 |
0.9993 |
313.15 |
0.8978 |
0.9991 |
313.15 |
0.9567 |
0.9983 |
323.15 |
0.3410 |
0.9883 |
323.15 |
0.5221 |
0.9939 |
323.15 |
0.6254 |
0.9970 |
323.15 |
0.7169 |
0.9978 |
323.15 |
0.7857 |
0.9987 |
323.15 |
0.8439 |
0.9983 |
323.15 |
0.9005 |
0.9975 |
323.15 |
0.9437 |
0.9947 |
333.15 |
0.2958 |
0.9805 |
333.15 |
0.4586 |
0.9905 |
333.15 |
0.5922 |
0.9954 |
333.15 |
0.6657 |
0.9970 |
333.15 |
0.7343 |
0.9976 |
333.15 |
0.7948 |
0.9971 |
333.15 |
0.8455 |
0.9965 |
333.15 |
0.8935 |
0.9918 |
333.15 |
0.9833 |
0.9833 |
343.15 |
0.2636 |
0.9782 |
343.15 |
0.3985 |
0.9887 |
343.15 |
0.5189 |
0.9939 |
343.15 |
0.5975 |
0.9955 |
343.15 |
0.6612 |
0.9958 |
343.15 |
0.7257 |
0.9963 |
343.15 |
0.7855 |
0.9961 |
343.15 |
0.8353 |
0.9949 |
Critical pressure, kPa
[ref]
Mole fraction of Carbon dioxide (1) - Liquid |
Critical pressure, kPa - Liquid |
0.0000 |
3871.00 |
0.8163 |
12790.00 |
0.8362 |
12870.00 |
0.8752 |
12920.00 |
0.8872 |
12940.00 |
0.9066 |
12890.00 |
0.9123 |
12850.00 |
0.9233 |
12740.00 |
0.9348 |
12610.00 |
0.9412 |
12520.00 |
0.9520 |
12290.00 |
0.9601 |
12000.00 |
0.9685 |
11330.00 |
0.9743 |
10830.00 |
0.9794 |
10320.00 |
0.9833 |
9900.00 |
1.0000 |
7383.00 |
Critical pressure, kPa
[ref]
Mole fraction of Carbon dioxide (1) - Liquid |
Critical pressure, kPa - Liquid |
0.0000 |
3871.00 |
0.8163 |
12790.00 |
0.8362 |
12870.00 |
0.8752 |
12920.00 |
0.8872 |
12940.00 |
0.9066 |
12890.00 |
0.9123 |
12850.00 |
0.9233 |
12740.00 |
0.9348 |
12610.00 |
0.9412 |
12520.00 |
0.9520 |
12290.00 |
0.9601 |
12000.00 |
0.9685 |
11330.00 |
0.9743 |
10830.00 |
0.9794 |
10320.00 |
0.9833 |
9900.00 |
1.0000 |
7383.00 |
Critical temperature, K
[ref]
Mole fraction of Carbon dioxide (1) - Liquid |
Critical temperature, K - Liquid |
0.0000 |
536.15 |
0.8163 |
420.05 |
0.8362 |
415.85 |
0.8752 |
408.65 |
0.8872 |
404.55 |
0.9066 |
397.75 |
0.9123 |
393.85 |
0.9233 |
388.05 |
0.9348 |
382.25 |
0.9412 |
380.05 |
0.9520 |
374.55 |
0.9601 |
368.55 |
0.9685 |
354.05 |
0.9743 |
346.05 |
0.9794 |
338.85 |
0.9833 |
333.15 |
1.0000 |
304.21 |
Critical temperature, K
[ref]
Mole fraction of Carbon dioxide (1) - Liquid |
Critical temperature, K - Liquid |
0.0000 |
536.15 |
0.8163 |
420.05 |
0.8362 |
415.85 |
0.8752 |
408.65 |
0.8872 |
404.55 |
0.9066 |
397.75 |
0.9123 |
393.85 |
0.9233 |
388.05 |
0.9348 |
382.25 |
0.9412 |
380.05 |
0.9520 |
374.55 |
0.9601 |
368.55 |
0.9685 |
354.05 |
0.9743 |
346.05 |
0.9794 |
338.85 |
0.9833 |
333.15 |
1.0000 |
304.21 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Vapor or sublimation pressure, kPa - Gas |
313.15 |
0.3779 |
1080.00 |
313.15 |
0.5649 |
2050.00 |
313.15 |
0.6932 |
3070.00 |
313.15 |
0.7805 |
4030.00 |
313.15 |
0.8452 |
5070.00 |
313.15 |
0.8978 |
6020.00 |
313.15 |
0.9567 |
7060.00 |
323.15 |
0.3410 |
1080.00 |
323.15 |
0.5221 |
2090.00 |
323.15 |
0.6254 |
3080.00 |
323.15 |
0.7169 |
4020.00 |
323.15 |
0.7857 |
5060.00 |
323.15 |
0.8439 |
6060.00 |
323.15 |
0.9005 |
7070.00 |
323.15 |
0.9437 |
8050.00 |
333.15 |
0.2958 |
1120.00 |
333.15 |
0.4586 |
2070.00 |
333.15 |
0.5922 |
3100.00 |
333.15 |
0.6657 |
4070.00 |
333.15 |
0.7343 |
5050.00 |
333.15 |
0.7948 |
6070.00 |
333.15 |
0.8455 |
7070.00 |
333.15 |
0.8935 |
8080.00 |
333.15 |
0.9833 |
9900.00 |
343.15 |
0.2636 |
1070.00 |
343.15 |
0.3985 |
2030.00 |
343.15 |
0.5189 |
3060.00 |
343.15 |
0.5975 |
4020.00 |
343.15 |
0.6612 |
5040.00 |
343.15 |
0.7257 |
6030.00 |
343.15 |
0.7855 |
7020.00 |
343.15 |
0.8353 |
8040.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Vapor or sublimation pressure, kPa - Gas |
313.15 |
0.3779 |
1080.00 |
313.15 |
0.5649 |
2050.00 |
313.15 |
0.6932 |
3070.00 |
313.15 |
0.7805 |
4030.00 |
313.15 |
0.8452 |
5070.00 |
313.15 |
0.8978 |
6020.00 |
313.15 |
0.9567 |
7060.00 |
323.15 |
0.3410 |
1080.00 |
323.15 |
0.5221 |
2090.00 |
323.15 |
0.6254 |
3080.00 |
323.15 |
0.7169 |
4020.00 |
323.15 |
0.7857 |
5060.00 |
323.15 |
0.8439 |
6060.00 |
323.15 |
0.9005 |
7070.00 |
323.15 |
0.9437 |
8050.00 |
333.15 |
0.2958 |
1120.00 |
333.15 |
0.4586 |
2070.00 |
333.15 |
0.5922 |
3100.00 |
333.15 |
0.6657 |
4070.00 |
333.15 |
0.7343 |
5050.00 |
333.15 |
0.7948 |
6070.00 |
333.15 |
0.8455 |
7070.00 |
333.15 |
0.8935 |
8080.00 |
333.15 |
0.9833 |
9900.00 |
343.15 |
0.2636 |
1070.00 |
343.15 |
0.3985 |
2030.00 |
343.15 |
0.5189 |
3060.00 |
343.15 |
0.5975 |
4020.00 |
343.15 |
0.6612 |
5040.00 |
343.15 |
0.7257 |
6030.00 |
343.15 |
0.7855 |
7020.00 |
343.15 |
0.8353 |
8040.00 |
Sources