Mixture of Methane + Propane, 2-methoxy-2-methyl- + Water

Datasets

1. Mole fraction (10)
2. P_vap - Vapor or sublimation pressure, kPa (2)

Mole fraction of Methane (1) [ref]

Operational condition: Temperature, K = 275.15 (Liquid mixture 1)

Mole fraction of Methane (1) - Gas	Mole fraction of Methane (1) - Liquid mixture 1
0.8812	0.0172
0.9815	0.0240
0.9863	0.0691

Mole fraction of Methane (1) [ref]

Operational condition: Temperature, K = 275.15 (Liquid mixture 2)

Mole fraction of Methane (1) - Gas	Mole fraction of Methane (1) - Liquid mixture 2
0.8812	0.0001
0.9815	0.0004
0.9863	0.0007

Mole fraction of Water (3) [ref]

Operational condition: Temperature, K = 275.15 (Gas)

Mole fraction of Methane (1) - Gas	Mole fraction of Water (3) - Gas
0.8812	0.0074
0.9815	0.0008
0.9863	0.0007

Mole fraction of Water (3) [ref]

Operational condition: Temperature, K = 275.15 (Liquid mixture 1)

Mole fraction of Methane (1) - Gas	Mole fraction of Water (3) - Liquid mixture 1
0.8812	0.0733
0.9815	0.0614
0.9863	0.0634

Mole fraction of Water (3) [ref]

Operational condition: Temperature, K = 275.15 (Liquid mixture 2)

Mole fraction of Methane (1) - Gas	Mole fraction of Water (3) - Liquid mixture 2
0.8812	0.9966
0.9815	0.9953
0.9863	0.9943

Mole fraction of Methane (1) [ref]

Operational condition: Temperature, K = 275.15 (Liquid mixture 1)

Mole fraction of Methane (1) - Gas	Mole fraction of Methane (1) - Liquid mixture 1
0.8812	0.0172
0.9815	0.0240
0.9863	0.0691

Mole fraction of Methane (1) [ref]

Operational condition: Temperature, K = 275.15 (Liquid mixture 2)

Mole fraction of Methane (1) - Gas	Mole fraction of Methane (1) - Liquid mixture 2
0.8812	0.0001
0.9815	0.0004
0.9863	0.0007

Mole fraction of Water (3) [ref]

Operational condition: Temperature, K = 275.15 (Gas)

Mole fraction of Methane (1) - Gas	Mole fraction of Water (3) - Gas
0.8812	0.0074
0.9815	0.0008
0.9863	0.0007

Mole fraction of Water (3) [ref]

Operational condition: Temperature, K = 275.15 (Liquid mixture 1)

Mole fraction of Methane (1) - Gas	Mole fraction of Water (3) - Liquid mixture 1
0.8812	0.0733
0.9815	0.0614
0.9863	0.0634

Mole fraction of Water (3) [ref]

Operational condition: Temperature, K = 275.15 (Liquid mixture 2)

Mole fraction of Methane (1) - Gas	Mole fraction of Water (3) - Liquid mixture 2
0.8812	0.9966
0.9815	0.9953
0.9863	0.9943

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 275.5 (Liquid mixture 1)

Mole fraction of Methane (1) - Gas	Vapor or sublimation pressure, kPa - Liquid mixture 1
0.8812	120.00
0.9815	1000.00
0.9863	2000.00

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 275.5 (Liquid mixture 1)

Mole fraction of Methane (1) - Gas	Vapor or sublimation pressure, kPa - Liquid mixture 1
0.8812	120.00
0.9815	1000.00
0.9863	2000.00

Sources

• Liquid-liquid equilibrium data of water with neohexane, methylcyclohexane, tert-butyl methyl ether, n-heptane and vapor -liquid-liquid equilibrium with methane