Mixture of Methyl propionate + Ethylene
Datasets
-
Pc - Critical pressure, kPa (2)
-
Pvap - Vapor or sublimation pressure, kPa (2)
-
Tc - Critical temperature, K (2)
Critical pressure, kPa
[ref]
Mole fraction of Ethylene (2) - Liquid |
Critical pressure, kPa - Liquid |
0.4839 |
9038.00 |
0.6404 |
10476.00 |
0.8021 |
10337.00 |
0.9009 |
8301.00 |
Critical pressure, kPa
[ref]
Mole fraction of Ethylene (2) - Liquid |
Critical pressure, kPa - Liquid |
0.4839 |
9038.00 |
0.6404 |
10476.00 |
0.8021 |
10337.00 |
0.9009 |
8301.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Ethylene (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0408 |
346.42 |
544.00 |
0.0408 |
361.37 |
640.00 |
0.0408 |
361.68 |
647.00 |
0.0408 |
377.25 |
780.00 |
0.0408 |
377.36 |
778.00 |
0.0408 |
392.64 |
943.00 |
0.0408 |
408.06 |
1144.00 |
0.0408 |
423.65 |
1392.00 |
0.0408 |
439.04 |
1685.00 |
0.0803 |
331.19 |
855.00 |
0.0803 |
346.27 |
998.00 |
0.0803 |
361.64 |
1158.00 |
0.0803 |
377.07 |
1336.00 |
0.0803 |
392.72 |
1552.00 |
0.0803 |
408.06 |
1795.00 |
0.0803 |
423.89 |
2081.00 |
0.0803 |
439.31 |
2411.00 |
0.1625 |
315.63 |
1468.00 |
0.1625 |
330.70 |
1718.00 |
0.1625 |
346.01 |
1983.00 |
0.1625 |
361.43 |
2263.00 |
0.1625 |
376.75 |
2558.00 |
0.1625 |
392.22 |
2873.00 |
0.1625 |
407.71 |
3209.00 |
0.1625 |
423.23 |
3574.00 |
0.1625 |
438.81 |
3969.00 |
0.3218 |
315.27 |
2887.00 |
0.3218 |
330.44 |
3387.00 |
0.3218 |
345.94 |
3908.00 |
0.3218 |
361.10 |
4428.00 |
0.3218 |
376.56 |
4948.00 |
0.3218 |
392.01 |
5468.00 |
0.3218 |
407.72 |
5989.00 |
0.3218 |
423.65 |
6504.00 |
0.3218 |
439.18 |
6979.00 |
0.4839 |
315.68 |
4336.00 |
0.4839 |
330.43 |
5091.00 |
0.4839 |
330.56 |
5101.00 |
0.4839 |
345.67 |
5881.00 |
0.4839 |
345.89 |
5896.00 |
0.4839 |
361.19 |
6671.00 |
0.4839 |
361.29 |
6681.00 |
0.4839 |
376.61 |
7421.00 |
0.4839 |
376.91 |
7431.00 |
0.4839 |
391.98 |
8116.00 |
0.4839 |
392.02 |
8111.00 |
0.4839 |
407.53 |
8731.00 |
0.4839 |
407.72 |
8746.00 |
0.4839 |
423.10 |
9241.00 |
0.4839 |
423.28 |
9246.00 |
0.4839 |
438.87 |
9556.00 |
0.4839 |
438.88 |
9551.00 |
0.4839 |
454.41 |
9476.00 |
0.4839 |
455.37 |
9451.00 |
0.4839 |
464.80 |
9038.00 |
0.6404 |
315.29 |
5611.00 |
0.6404 |
330.50 |
6681.00 |
0.6404 |
345.71 |
7736.00 |
0.6404 |
361.17 |
8736.00 |
0.6404 |
376.55 |
9611.00 |
0.6404 |
392.33 |
10301.00 |
0.6404 |
407.75 |
10666.00 |
0.6404 |
412.78 |
10716.00 |
0.6404 |
417.98 |
10701.00 |
0.6404 |
423.13 |
10641.00 |
0.6404 |
423.32 |
10646.00 |
0.6404 |
428.43 |
10476.00 |
0.8021 |
297.83 |
5172.00 |
0.8021 |
310.19 |
6237.00 |
0.8021 |
320.25 |
7122.00 |
0.8021 |
330.39 |
7992.00 |
0.8021 |
340.61 |
8802.00 |
0.8021 |
350.84 |
9482.00 |
0.8021 |
355.92 |
9762.00 |
0.8021 |
361.01 |
9997.00 |
0.8021 |
366.18 |
10192.00 |
0.8021 |
369.21 |
10292.00 |
0.8021 |
370.27 |
10322.00 |
0.8021 |
370.81 |
10337.00 |
0.9009 |
283.51 |
4416.00 |
0.9009 |
291.33 |
5101.00 |
0.9009 |
299.27 |
5831.00 |
0.9009 |
307.08 |
6561.00 |
0.9009 |
314.94 |
7266.00 |
0.9009 |
322.86 |
7891.00 |
0.9009 |
326.89 |
8176.00 |
0.9009 |
327.80 |
8236.00 |
0.9009 |
328.79 |
8301.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Ethylene (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0408 |
346.42 |
544.00 |
0.0408 |
361.37 |
640.00 |
0.0408 |
361.68 |
647.00 |
0.0408 |
377.25 |
780.00 |
0.0408 |
377.36 |
778.00 |
0.0408 |
392.64 |
943.00 |
0.0408 |
408.06 |
1144.00 |
0.0408 |
423.65 |
1392.00 |
0.0408 |
439.04 |
1685.00 |
0.0803 |
331.19 |
855.00 |
0.0803 |
346.27 |
998.00 |
0.0803 |
361.64 |
1158.00 |
0.0803 |
377.07 |
1336.00 |
0.0803 |
392.72 |
1552.00 |
0.0803 |
408.06 |
1795.00 |
0.0803 |
423.89 |
2081.00 |
0.0803 |
439.31 |
2411.00 |
0.1625 |
315.63 |
1468.00 |
0.1625 |
330.70 |
1718.00 |
0.1625 |
346.01 |
1983.00 |
0.1625 |
361.43 |
2263.00 |
0.1625 |
376.75 |
2558.00 |
0.1625 |
392.22 |
2873.00 |
0.1625 |
407.71 |
3209.00 |
0.1625 |
423.23 |
3574.00 |
0.1625 |
438.81 |
3969.00 |
0.3218 |
315.27 |
2887.00 |
0.3218 |
330.44 |
3387.00 |
0.3218 |
345.94 |
3908.00 |
0.3218 |
361.10 |
4428.00 |
0.3218 |
376.56 |
4948.00 |
0.3218 |
392.01 |
5468.00 |
0.3218 |
407.72 |
5989.00 |
0.3218 |
423.65 |
6504.00 |
0.3218 |
439.18 |
6979.00 |
0.4839 |
315.68 |
4336.00 |
0.4839 |
330.43 |
5091.00 |
0.4839 |
330.56 |
5101.00 |
0.4839 |
345.67 |
5881.00 |
0.4839 |
345.89 |
5896.00 |
0.4839 |
361.19 |
6671.00 |
0.4839 |
361.29 |
6681.00 |
0.4839 |
376.61 |
7421.00 |
0.4839 |
376.91 |
7431.00 |
0.4839 |
391.98 |
8116.00 |
0.4839 |
392.02 |
8111.00 |
0.4839 |
407.53 |
8731.00 |
0.4839 |
407.72 |
8746.00 |
0.4839 |
423.10 |
9241.00 |
0.4839 |
423.28 |
9246.00 |
0.4839 |
438.87 |
9556.00 |
0.4839 |
438.88 |
9551.00 |
0.4839 |
454.41 |
9476.00 |
0.4839 |
455.37 |
9451.00 |
0.4839 |
464.80 |
9038.00 |
0.6404 |
315.29 |
5611.00 |
0.6404 |
330.50 |
6681.00 |
0.6404 |
345.71 |
7736.00 |
0.6404 |
361.17 |
8736.00 |
0.6404 |
376.55 |
9611.00 |
0.6404 |
392.33 |
10301.00 |
0.6404 |
407.75 |
10666.00 |
0.6404 |
412.78 |
10716.00 |
0.6404 |
417.98 |
10701.00 |
0.6404 |
423.13 |
10641.00 |
0.6404 |
423.32 |
10646.00 |
0.6404 |
428.43 |
10476.00 |
0.8021 |
297.83 |
5172.00 |
0.8021 |
310.19 |
6237.00 |
0.8021 |
320.25 |
7122.00 |
0.8021 |
330.39 |
7992.00 |
0.8021 |
340.61 |
8802.00 |
0.8021 |
350.84 |
9482.00 |
0.8021 |
355.92 |
9762.00 |
0.8021 |
361.01 |
9997.00 |
0.8021 |
366.18 |
10192.00 |
0.8021 |
369.21 |
10292.00 |
0.8021 |
370.27 |
10322.00 |
0.8021 |
370.81 |
10337.00 |
0.9009 |
283.51 |
4416.00 |
0.9009 |
291.33 |
5101.00 |
0.9009 |
299.27 |
5831.00 |
0.9009 |
307.08 |
6561.00 |
0.9009 |
314.94 |
7266.00 |
0.9009 |
322.86 |
7891.00 |
0.9009 |
326.89 |
8176.00 |
0.9009 |
327.80 |
8236.00 |
0.9009 |
328.79 |
8301.00 |
Critical temperature, K
[ref]
Mole fraction of Ethylene (2) - Liquid |
Critical temperature, K - Liquid |
0.4839 |
464.80 |
0.6404 |
428.43 |
0.8021 |
370.81 |
0.9009 |
328.79 |
Critical temperature, K
[ref]
Mole fraction of Ethylene (2) - Liquid |
Critical temperature, K - Liquid |
0.4839 |
464.80 |
0.6404 |
428.43 |
0.8021 |
370.81 |
0.9009 |
328.79 |
Sources