Mixture of Isopropyl Alcohol + Ethane, 1,1-diethoxy-

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
353.00	0.9160

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

Pressure, kPa - Liquid	Azeotropic composition: mole fraction of Isopropyl Alcohol (1) - Liquid
94.20	0.9160

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	353.38	0.0000
0.0151	353.36	0.0525
0.0450	353.36	0.1479
0.0852	353.37	0.2378
0.1354	353.34	0.3352
0.1767	353.35	0.3934
0.2370	353.35	0.4652
0.2845	353.33	0.5086
0.3321	353.28	0.5468
0.3687	353.28	0.5736
0.4163	353.29	0.6068
0.4580	353.32	0.6329
0.4991	353.32	0.6543
0.5315	353.31	0.6758
0.5715	353.33	0.7015
0.6298	353.34	0.7330
0.6870	353.33	0.7624
0.7350	353.34	0.7913
0.7790	353.34	0.8202
0.8152	353.32	0.8427
0.9162	353.31	0.9158
0.9452	353.32	0.9446
0.9638	353.31	0.9624
0.9826	353.31	0.9812
0.9944	353.35	0.9940
1.0000	353.34	1.0000

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

Temperature, K - Liquid	Azeotropic composition: mole fraction of Isopropyl Alcohol (1) - Liquid
353.00	0.9160

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

Pressure, kPa - Liquid	Azeotropic composition: mole fraction of Isopropyl Alcohol (1) - Liquid
94.20	0.9160

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	353.38	0.0000
0.0151	353.36	0.0525
0.0450	353.36	0.1479
0.0852	353.37	0.2378
0.1354	353.34	0.3352
0.1767	353.35	0.3934
0.2370	353.35	0.4652
0.2845	353.33	0.5086
0.3321	353.28	0.5468
0.3687	353.28	0.5736
0.4163	353.29	0.6068
0.4580	353.32	0.6329
0.4991	353.32	0.6543
0.5315	353.31	0.6758
0.5715	353.33	0.7015
0.6298	353.34	0.7330
0.6870	353.33	0.7624
0.7350	353.34	0.7913
0.7790	353.34	0.8202
0.8152	353.32	0.8427
0.9162	353.31	0.9158
0.9452	353.32	0.9446
0.9638	353.31	0.9624
0.9826	353.31	0.9812
0.9944	353.35	0.9940
1.0000	353.34	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	353.38	48.90
0.0151	353.36	50.90
0.0450	353.36	54.90
0.0852	353.37	59.60
0.1354	353.34	64.60
0.1767	353.35	68.30
0.2370	353.35	72.70
0.2845	353.33	75.80
0.3321	353.28	78.30
0.3687	353.28	80.10
0.4163	353.29	82.30
0.4580	353.32	84.00
0.4991	353.32	85.50
0.5315	353.31	86.60
0.5715	353.33	88.00
0.6298	353.34	89.70
0.6870	353.33	91.20
0.7350	353.34	92.60
0.7790	353.34	93.50
0.8152	353.32	93.90
0.9162	353.31	94.20
0.9452	353.32	94.00
0.9638	353.31	94.00
0.9826	353.31	93.90
0.9944	353.35	93.90
1.0000	353.34	93.90

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	353.38	48.90
0.0151	353.36	50.90
0.0450	353.36	54.90
0.0852	353.37	59.60
0.1354	353.34	64.60
0.1767	353.35	68.30
0.2370	353.35	72.70
0.2845	353.33	75.80
0.3321	353.28	78.30
0.3687	353.28	80.10
0.4163	353.29	82.30
0.4580	353.32	84.00
0.4991	353.32	85.50
0.5315	353.31	86.60
0.5715	353.33	88.00
0.6298	353.34	89.70
0.6870	353.33	91.20
0.7350	353.34	92.60
0.7790	353.34	93.50
0.8152	353.32	93.90
0.9162	353.31	94.20
0.9452	353.32	94.00
0.9638	353.31	94.00
0.9826	353.31	93.90
0.9944	353.35	93.90
1.0000	353.34	93.90

Sources

• Vapor Liquid Equilibrium for Binary System of 2-Propanol + 1,1-Diethoxyethane at 353 K and Ethyl ethanoate + 1,1-Diethoxyethane at 348 K and 2-Propanone + 1,1-Diethoxyethane at 328 K