Mixture of Carbon dioxide + Diethyl fumarate

Datasets

1. Mole fraction (2)
2. P_vap - 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
0.1363	373.20	0.9003
0.2414	373.20	0.9095
0.3196	373.20	0.9240
0.4997	373.20	0.9227
0.5624	373.20	0.9277
0.6181	373.20	0.9216
0.7845	373.20	0.9257
0.0865	398.20	0.9151
0.1847	398.20	0.9214
0.2662	398.20	0.9201
0.3124	398.20	0.9191
0.4679	398.20	0.9097
0.5990	398.20	0.8992
0.7286	398.20	0.8996
0.8366	398.20	0.9162
0.2493	423.20	0.9146
0.2948	423.20	0.9243
0.3108	423.20	0.9164
0.3604	423.20	0.9288
0.4209	423.20	0.9257
0.5239	423.20	0.9025
0.5916	423.20	0.9512
0.6089	423.20	0.8874
0.0869	453.20	0.9016
0.1255	453.20	0.9102
0.1935	453.20	0.9098
0.2812	453.20	0.9234
0.3543	453.20	0.9099
0.3928	453.20	0.8909
0.4667	453.20	0.8712
0.5134	453.20	0.8745

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
0.1363	373.20	0.9003
0.2414	373.20	0.9095
0.3196	373.20	0.9240
0.4997	373.20	0.9227
0.5624	373.20	0.9277
0.6181	373.20	0.9216
0.7845	373.20	0.9257
0.0865	398.20	0.9151
0.1847	398.20	0.9214
0.2662	398.20	0.9201
0.3124	398.20	0.9191
0.4679	398.20	0.9097
0.5990	398.20	0.8992
0.7286	398.20	0.8996
0.8366	398.20	0.9162
0.2493	423.20	0.9146
0.2948	423.20	0.9243
0.3108	423.20	0.9164
0.3604	423.20	0.9288
0.4209	423.20	0.9257
0.5239	423.20	0.9025
0.5916	423.20	0.9512
0.6089	423.20	0.8874
0.0869	453.20	0.9016
0.1255	453.20	0.9102
0.1935	453.20	0.9098
0.2812	453.20	0.9234
0.3543	453.20	0.9099
0.3928	453.20	0.8909
0.4667	453.20	0.8712
0.5134	453.20	0.8745

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Carbon dioxide (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.1363	373.20	3210.00
0.2414	373.20	5130.00
0.3196	373.20	7270.00
0.4997	373.20	10600.00
0.5624	373.20	13060.00
0.6181	373.20	14890.00
0.7845	373.20	17440.00
0.0865	398.20	2700.00
0.1847	398.20	5080.00
0.2662	398.20	7050.00
0.3124	398.20	10060.00
0.4679	398.20	12500.00
0.5990	398.20	15730.00
0.7286	398.20	17950.00
0.8366	398.20	19760.00
0.2493	423.20	5490.00
0.2948	423.20	7320.00
0.3108	423.20	10100.00
0.3604	423.20	12540.00
0.4209	423.20	15340.00
0.5239	423.20	17630.00
0.5916	423.20	20200.00
0.6089	423.20	22270.00
0.0869	453.20	3110.00
0.1255	453.20	5205.00
0.1935	453.20	7640.00
0.2812	453.20	10380.00
0.3543	453.20	12540.00
0.3928	453.20	15730.00
0.4667	453.20	18560.00
0.5134	453.20	21380.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Carbon dioxide (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.1363	373.20	3210.00
0.2414	373.20	5130.00
0.3196	373.20	7270.00
0.4997	373.20	10600.00
0.5624	373.20	13060.00
0.6181	373.20	14890.00
0.7845	373.20	17440.00
0.0865	398.20	2700.00
0.1847	398.20	5080.00
0.2662	398.20	7050.00
0.3124	398.20	10060.00
0.4679	398.20	12500.00
0.5990	398.20	15730.00
0.7286	398.20	17950.00
0.8366	398.20	19760.00
0.2493	423.20	5490.00
0.2948	423.20	7320.00
0.3108	423.20	10100.00
0.3604	423.20	12540.00
0.4209	423.20	15340.00
0.5239	423.20	17630.00
0.5916	423.20	20200.00
0.6089	423.20	22270.00
0.0869	453.20	3110.00
0.1255	453.20	5205.00
0.1935	453.20	7640.00
0.2812	453.20	10380.00
0.3543	453.20	12540.00
0.3928	453.20	15730.00
0.4667	453.20	18560.00
0.5134	453.20	21380.00

Sources

• Determination of Vapor Liquid Equilibria of the Binary System of Sub- and Supercritical CO2 and Diethyl Fumarate