Mixture of Acetic anhydride + Carbon dioxide

Datasets

1. P_c - Critical pressure, kPa (2)
2. P_vap - Vapor or sublimation pressure, kPa (2)
3. T_c - Critical temperature, K (2)

Critical pressure, kPa [ref]

Mole fraction of Acetic anhydride (1) - Liquid	Critical pressure, kPa - Liquid
0.0972	14840.00

Critical pressure, kPa [ref]

Mole fraction of Acetic anhydride (1) - Liquid	Critical pressure, kPa - Liquid
0.0972	14840.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Acetic anhydride (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0972	283.09	4070.00
0.0972	293.13	5100.00
0.0972	303.17	6410.00
0.0972	313.21	7660.00
0.0972	323.26	9160.00
0.0972	333.31	10720.00
0.0972	343.16	12230.00
0.0972	353.24	13600.00
0.0972	363.17	14800.00
0.2922	283.08	3220.00
0.2922	293.24	4010.00
0.2922	303.13	4900.00
0.2922	313.24	5900.00
0.2922	323.36	7020.00
0.2922	333.37	8250.00
0.2922	343.18	9370.00
0.2922	353.24	10630.00
0.2922	363.35	11870.00
0.4897	283.09	2390.00
0.4897	293.13	2890.00
0.4897	303.17	3480.00
0.4897	313.19	4160.00
0.4897	323.14	4880.00
0.4897	333.10	5650.00
0.4897	343.13	6420.00
0.4897	353.16	7330.00
0.4897	363.18	8180.00
0.6918	283.18	1290.00
0.6918	293.20	1580.00
0.6918	303.25	1920.00
0.6918	313.19	2300.00
0.6918	323.26	2690.00
0.6918	333.28	3100.00
0.6918	343.19	3530.00
0.6918	353.16	3990.00
0.6918	363.26	4450.00
0.8953	283.13	400.00
0.8953	293.16	500.00
0.8953	303.44	590.00
0.8953	313.19	700.00
0.8953	323.23	820.00
0.8953	333.20	930.00
0.8953	343.26	1080.00
0.8953	353.16	1200.00
0.8953	363.19	1340.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Acetic anhydride (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0972	283.09	4070.00
0.0972	293.13	5100.00
0.0972	303.17	6410.00
0.0972	313.21	7660.00
0.0972	323.26	9160.00
0.0972	333.31	10720.00
0.0972	343.16	12230.00
0.0972	353.24	13600.00
0.0972	363.17	14800.00
0.2922	283.08	3220.00
0.2922	293.24	4010.00
0.2922	303.13	4900.00
0.2922	313.24	5900.00
0.2922	323.36	7020.00
0.2922	333.37	8250.00
0.2922	343.18	9370.00
0.2922	353.24	10630.00
0.2922	363.35	11870.00
0.4897	283.09	2390.00
0.4897	293.13	2890.00
0.4897	303.17	3480.00
0.4897	313.19	4160.00
0.4897	323.14	4880.00
0.4897	333.10	5650.00
0.4897	343.13	6420.00
0.4897	353.16	7330.00
0.4897	363.18	8180.00
0.6918	283.18	1290.00
0.6918	293.20	1580.00
0.6918	303.25	1920.00
0.6918	313.19	2300.00
0.6918	323.26	2690.00
0.6918	333.28	3100.00
0.6918	343.19	3530.00
0.6918	353.16	3990.00
0.6918	363.26	4450.00
0.8953	283.13	400.00
0.8953	293.16	500.00
0.8953	303.44	590.00
0.8953	313.19	700.00
0.8953	323.23	820.00
0.8953	333.20	930.00
0.8953	343.26	1080.00
0.8953	353.16	1200.00
0.8953	363.19	1340.00

Critical temperature, K [ref]

Mole fraction of Acetic anhydride (1) - Liquid	Critical temperature, K - Liquid
0.0972	360.12

Critical temperature, K [ref]

Mole fraction of Acetic anhydride (1) - Liquid	Critical temperature, K - Liquid
0.0972	360.12

Sources

• High pressure vapour liquid equilibria of the binary and some of the ternary and multicomponent mixtures of the carbon dioxide + acetic anhydride + alpha-methylbenzyl alcohol + acetic acid + alpha-methylbenzyl acetate system: Experimental and modelling results