Mixture of Carbon dioxide + Triethylene glycol, hexyl ether

Datasets

1. P_vap - Vapor or sublimation pressure, kPa (2)
2. Vapor or sublimation pressure, kPa (2)

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Triethylene glycol, hexyl ether (2) - Liquid mixture 1	Temperature, K - Liquid mixture 1	Vapor or sublimation pressure, kPa - Liquid mixture 2
0.0096	298.35	6850.00
0.0096	299.72	7300.00
0.0096	301.14	7900.00
0.0096	302.61	8400.00
0.0096	304.17	9000.00
0.0096	305.33	9650.00
0.0138	293.00	6000.00
0.0138	294.07	6530.00
0.0138	295.31	6950.00
0.0138	297.38	7650.00
0.0138	299.51	8660.00
0.0138	301.75	9330.00
0.0198	291.67	6250.00
0.0198	293.28	6850.00
0.0198	295.08	7550.00
0.0198	297.21	8250.00
0.0198	299.18	9050.00
0.0271	288.36	5350.00
0.0271	289.32	5650.00
0.0271	290.73	6200.00
0.0271	292.71	6950.00
0.0271	294.63	7650.00
0.0271	296.87	8400.00
0.0271	299.79	9500.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Triethylene glycol, hexyl ether (2) - Liquid mixture 1	Temperature, K - Liquid mixture 1	Vapor or sublimation pressure, kPa - Liquid mixture 2
0.0096	298.35	6850.00
0.0096	299.72	7300.00
0.0096	301.14	7900.00
0.0096	302.61	8400.00
0.0096	304.17	9000.00
0.0096	305.33	9650.00
0.0138	293.00	6000.00
0.0138	294.07	6530.00
0.0138	295.31	6950.00
0.0138	297.38	7650.00
0.0138	299.51	8660.00
0.0138	301.75	9330.00
0.0198	291.67	6250.00
0.0198	293.28	6850.00
0.0198	295.08	7550.00
0.0198	297.21	8250.00
0.0198	299.18	9050.00
0.0271	288.36	5350.00
0.0271	289.32	5650.00
0.0271	290.73	6200.00
0.0271	292.71	6950.00
0.0271	294.63	7650.00
0.0271	296.87	8400.00
0.0271	299.79	9500.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Triethylene glycol, hexyl ether (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Gas
0.0096	271.67	3350.00
0.0096	274.22	3580.00
0.0096	275.42	3690.00
0.0096	277.42	3890.00
0.0096	278.77	4020.00
0.0096	280.34	4170.00
0.0096	282.08	4380.00
0.0096	283.87	4550.00
0.0096	286.89	4900.00
0.0096	288.68	5110.00
0.0096	290.07	5280.00
0.0096	292.21	5550.00
0.0096	294.21	5820.00
0.0096	296.46	6110.00
0.0096	297.11	6200.00
0.0138	270.65	3230.00
0.0138	272.65	3410.00
0.0138	274.83	3580.00
0.0138	276.84	3800.00
0.0138	278.97	4010.00
0.0138	281.32	4250.00
0.0138	283.78	4520.00
0.0138	286.13	4780.00
0.0138	288.58	5080.00
0.0138	290.04	5250.00
0.0138	291.45	5430.00
0.0198	270.63	3220.00
0.0198	272.50	3380.00
0.0198	274.43	3550.00
0.0198	276.00	3700.00
0.0198	277.86	3880.00
0.0198	279.11	4000.00
0.0198	281.05	4200.00
0.0198	284.00	4520.00
0.0198	285.22	4650.00
0.0198	286.35	4790.00
0.0198	287.64	4940.00
0.0198	288.66	5080.00
0.0198	290.21	5300.00
0.0271	270.85	3240.00
0.0271	272.75	3400.00
0.0271	274.76	3580.00
0.0271	276.82	3780.00
0.0271	278.38	3930.00
0.0271	280.73	4170.00
0.0271	283.32	4440.00
0.0271	285.17	4640.00
0.0271	286.96	4850.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Triethylene glycol, hexyl ether (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Gas
0.0096	271.67	3350.00
0.0096	274.22	3580.00
0.0096	275.42	3690.00
0.0096	277.42	3890.00
0.0096	278.77	4020.00
0.0096	280.34	4170.00
0.0096	282.08	4380.00
0.0096	283.87	4550.00
0.0096	286.89	4900.00
0.0096	288.68	5110.00
0.0096	290.07	5280.00
0.0096	292.21	5550.00
0.0096	294.21	5820.00
0.0096	296.46	6110.00
0.0096	297.11	6200.00
0.0138	270.65	3230.00
0.0138	272.65	3410.00
0.0138	274.83	3580.00
0.0138	276.84	3800.00
0.0138	278.97	4010.00
0.0138	281.32	4250.00
0.0138	283.78	4520.00
0.0138	286.13	4780.00
0.0138	288.58	5080.00
0.0138	290.04	5250.00
0.0138	291.45	5430.00
0.0198	270.63	3220.00
0.0198	272.50	3380.00
0.0198	274.43	3550.00
0.0198	276.00	3700.00
0.0198	277.86	3880.00
0.0198	279.11	4000.00
0.0198	281.05	4200.00
0.0198	284.00	4520.00
0.0198	285.22	4650.00
0.0198	286.35	4790.00
0.0198	287.64	4940.00
0.0198	288.66	5080.00
0.0198	290.21	5300.00
0.0271	270.85	3240.00
0.0271	272.75	3400.00
0.0271	274.76	3580.00
0.0271	276.82	3780.00
0.0271	278.38	3930.00
0.0271	280.73	4170.00
0.0271	283.32	4440.00
0.0271	285.17	4640.00
0.0271	286.96	4850.00

Sources

• Effect of the ethoxy groups distribution on the phase behaviour of the binary systems carbon dioxide CO2 with industrial non-ionic surfactants (CiEOj)