Mixture of 1-Propanol, 2,2-dimethyl- + Propane, 2-methoxy-2-methyl-

Datasets

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

Mole fraction of Propane, 2-methoxy-2-methyl- (2) [ref]

Fixed		Measured
Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid	Temperature, K - Liquid	Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Gas
0.0000	320.00	0.0000
0.0000	330.00	0.0000
0.0000	340.00	0.0000
0.3021	340.00	0.8169
0.3708	330.00	0.8792
0.3905	340.00	0.8615
0.4158	330.00	0.8955
0.4395	340.00	0.8828
0.4549	320.00	0.9149
0.4655	330.00	0.9110
0.4805	340.00	0.8955
0.4960	330.00	0.9200
0.5257	320.00	0.9366
0.5263	340.00	0.9115
0.5849	340.00	0.9253
0.5857	330.00	0.9402
0.6532	320.00	0.9616
0.6642	330.00	0.9543
0.7408	320.00	0.9723
0.7435	330.00	0.9667
0.8084	320.00	0.9792
0.8718	330.00	0.9842
0.8763	320.00	0.9874
0.9340	320.00	0.9935
0.9343	330.00	0.9922
0.9604	320.00	0.9962
0.9890	320.00	0.9989
1.0000	320.00	1.0000
1.0000	330.00	1.0000
1.0000	340.00	1.0000

Mole fraction of Propane, 2-methoxy-2-methyl- (2) [ref]

Fixed		Measured
Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid	Temperature, K - Liquid	Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Gas
0.0000	320.00	0.0000
0.0000	330.00	0.0000
0.0000	340.00	0.0000
0.3021	340.00	0.8169
0.3708	330.00	0.8792
0.3905	340.00	0.8615
0.4158	330.00	0.8955
0.4395	340.00	0.8828
0.4549	320.00	0.9149
0.4655	330.00	0.9110
0.4805	340.00	0.8955
0.4960	330.00	0.9200
0.5257	320.00	0.9366
0.5263	340.00	0.9115
0.5849	340.00	0.9253
0.5857	330.00	0.9402
0.6532	320.00	0.9616
0.6642	330.00	0.9543
0.7408	320.00	0.9723
0.7435	330.00	0.9667
0.8084	320.00	0.9792
0.8718	330.00	0.9842
0.8763	320.00	0.9874
0.9340	320.00	0.9935
0.9343	330.00	0.9922
0.9604	320.00	0.9962
0.9890	320.00	0.9989
1.0000	320.00	1.0000
1.0000	330.00	1.0000
1.0000	340.00	1.0000

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	320.00	5.11
0.0000	330.00	8.83
0.0000	340.00	14.66
0.3021	340.00	58.88
0.3708	330.00	48.59
0.3905	340.00	70.53
0.4158	330.00	53.14
0.4395	340.00	77.12
0.4549	320.00	40.17
0.4655	330.00	57.65
0.4805	340.00	81.16
0.4960	330.00	61.12
0.5257	320.00	44.97
0.5263	340.00	87.91
0.5849	340.00	94.48
0.5857	330.00	68.92
0.6532	320.00	53.63
0.6642	330.00	75.99
0.7408	320.00	59.04
0.7435	330.00	83.36
0.8084	320.00	63.59
0.8718	330.00	95.60
0.8763	320.00	68.11
0.9340	320.00	72.31
0.9343	330.00	101.56
0.9604	320.00	74.09
0.9890	320.00	76.08
1.0000	320.00	76.17
1.0000	330.00	108.14
1.0000	340.00	146.97

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	320.00	5.11
0.0000	330.00	8.83
0.0000	340.00	14.66
0.3021	340.00	58.88
0.3708	330.00	48.59
0.3905	340.00	70.53
0.4158	330.00	53.14
0.4395	340.00	77.12
0.4549	320.00	40.17
0.4655	330.00	57.65
0.4805	340.00	81.16
0.4960	330.00	61.12
0.5257	320.00	44.97
0.5263	340.00	87.91
0.5849	340.00	94.48
0.5857	330.00	68.92
0.6532	320.00	53.63
0.6642	330.00	75.99
0.7408	320.00	59.04
0.7435	330.00	83.36
0.8084	320.00	63.59
0.8718	330.00	95.60
0.8763	320.00	68.11
0.9340	320.00	72.31
0.9343	330.00	101.56
0.9604	320.00	74.09
0.9890	320.00	76.08
1.0000	320.00	76.17
1.0000	330.00	108.14
1.0000	340.00	146.97

Sources

• Isothermal vapour liquid equilibria in the binary and ternary systems composed of tert-butyl methyl ether, 3,3-dimethyl-2-butanone and 2,2-dimethyl-1-propanol