Mixture of Isopropyl Alcohol + Propane, 2-ethoxy-2-methyl-

Datasets

1. Azeotropic composition: mole fraction (6)
2. P_vap - Vapor or sublimation pressure, kPa (2)

Azeotropic composition: mole fraction of Isopropyl Alcohol (1) [ref]

Temperature, K - Liquid	Azeotropic composition: mole fraction of Isopropyl Alcohol (1) - Liquid
333.00	0.2300

Azeotropic composition: mole fraction of Isopropyl Alcohol (1) [ref]

Pressure, kPa - Liquid	Azeotropic composition: mole fraction of Isopropyl Alcohol (1) - Liquid
73.30	0.2300

Mole fraction of Isopropyl Alcohol (1) [ref]

Fixed		Measured
Mole fraction of Isopropyl Alcohol (1) - Liquid	Temperature, K - Liquid	Mole fraction of Isopropyl Alcohol (1) - Gas
0.0000	333.28	0.0000
0.0930	333.31	0.1305
0.1472	333.34	0.1781
0.2025	333.28	0.2144
0.2594	333.30	0.2454
0.3209	333.35	0.2762
0.3776	333.31	0.3019
0.4422	333.29	0.3315
0.4979	333.34	0.3557
0.5597	333.28	0.3849
0.6145	333.28	0.4121
0.6627	333.31	0.4404
0.7102	333.31	0.4700
0.7826	333.27	0.5310
0.8337	333.35	0.5872
0.8700	333.28	0.6370
0.8965	333.28	0.6836
0.9221	333.27	0.7439
0.9467	333.32	0.8035
0.9652	333.31	0.8639
0.9800	333.26	0.9175
0.9924	333.28	0.9677
1.0000	333.28	1.0000

Azeotropic composition: mole fraction of Isopropyl Alcohol (1) [ref]

Temperature, K - Liquid	Azeotropic composition: mole fraction of Isopropyl Alcohol (1) - Liquid
333.00	0.2300

Azeotropic composition: mole fraction of Isopropyl Alcohol (1) [ref]

Pressure, kPa - Liquid	Azeotropic composition: mole fraction of Isopropyl Alcohol (1) - Liquid
73.30	0.2300

Mole fraction of Isopropyl Alcohol (1) [ref]

Fixed		Measured
Mole fraction of Isopropyl Alcohol (1) - Liquid	Temperature, K - Liquid	Mole fraction of Isopropyl Alcohol (1) - Gas
0.0000	333.28	0.0000
0.0930	333.31	0.1305
0.1472	333.34	0.1781
0.2025	333.28	0.2144
0.2594	333.30	0.2454
0.3209	333.35	0.2762
0.3776	333.31	0.3019
0.4422	333.29	0.3315
0.4979	333.34	0.3557
0.5597	333.28	0.3849
0.6145	333.28	0.4121
0.6627	333.31	0.4404
0.7102	333.31	0.4700
0.7826	333.27	0.5310
0.8337	333.35	0.5872
0.8700	333.28	0.6370
0.8965	333.28	0.6836
0.9221	333.27	0.7439
0.9467	333.32	0.8035
0.9652	333.31	0.8639
0.9800	333.26	0.9175
0.9924	333.28	0.9677
1.0000	333.28	1.0000

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Isopropyl Alcohol (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	333.28	67.40
0.0930	333.31	72.30
0.1472	333.34	73.20
0.2025	333.28	73.30
0.2594	333.30	73.20
0.3209	333.35	72.80
0.3776	333.31	72.00
0.4422	333.29	71.10
0.4979	333.34	70.10
0.5597	333.28	68.50
0.6145	333.28	66.90
0.6627	333.31	65.40
0.7102	333.31	63.50
0.7826	333.27	59.70
0.8337	333.35	56.50
0.8700	333.28	53.60
0.8965	333.28	51.20
0.9221	333.27	48.60
0.9467	333.32	45.90
0.9652	333.31	43.70
0.9800	333.26	41.70
0.9924	333.28	39.90
1.0000	333.28	38.80

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Isopropyl Alcohol (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	333.28	67.40
0.0930	333.31	72.30
0.1472	333.34	73.20
0.2025	333.28	73.30
0.2594	333.30	73.20
0.3209	333.35	72.80
0.3776	333.31	72.00
0.4422	333.29	71.10
0.4979	333.34	70.10
0.5597	333.28	68.50
0.6145	333.28	66.90
0.6627	333.31	65.40
0.7102	333.31	63.50
0.7826	333.27	59.70
0.8337	333.35	56.50
0.8700	333.28	53.60
0.8965	333.28	51.20
0.9221	333.27	48.60
0.9467	333.32	45.90
0.9652	333.31	43.70
0.9800	333.26	41.70
0.9924	333.28	39.90
1.0000	333.28	38.80

Sources

• Vapor Liquid Equilibrium for Binary System of 2-Propanol + 2-Ethoxy-2-methylpropane and Ethyl Ethanoate + 2-Ethoxy-2-methylpropane at 333 K and 2-Propanone + 2-Ethoxy-2-methylpropane at 323 K