Mixture of Propane, 2-methoxy-2-methyl- + Cyclohexane, methyl-

Datasets

1. Mole fraction (2)

Mole fraction of Propane, 2-methoxy-2-methyl- (1) [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid	Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Gas
0.0202	0.1326
0.0504	0.2704
0.0737	0.3556
0.1000	0.4227
0.1492	0.5359
0.1988	0.6193
0.2487	0.6716
0.2989	0.7148
0.3496	0.7598
0.3976	0.7900
0.4488	0.8138
0.4986	0.8421
0.5489	0.8574
0.5992	0.8794
0.6479	0.8912
0.6976	0.9123
0.7486	0.9280
0.8000	0.9339
0.8504	0.9504
0.9006	0.9648
0.9239	0.9762
0.9476	0.9802
0.9800	0.9916

Mole fraction of Propane, 2-methoxy-2-methyl- (1) [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid	Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Gas
0.0202	0.1326
0.0504	0.2704
0.0737	0.3556
0.1000	0.4227
0.1492	0.5359
0.1988	0.6193
0.2487	0.6716
0.2989	0.7148
0.3496	0.7598
0.3976	0.7900
0.4488	0.8138
0.4986	0.8421
0.5489	0.8574
0.5992	0.8794
0.6479	0.8912
0.6976	0.9123
0.7486	0.9280
0.8000	0.9339
0.8504	0.9504
0.9006	0.9648
0.9239	0.9762
0.9476	0.9802
0.9800	0.9916

Sources

• Vapor-Liquid Equilibria for the Ternary Systems of Methyl tert-Butyl Ether + Methanol + Methylcyclohexane and Methyl tert-Butyl Ether + Methanol + n-Heptane and Constituent Binary Systems at 313.15 K