Mixture of Ethane, 1,2-dichloro- + Water

Datasets

1. Mole fraction (6)

Mole fraction of Ethane, 1,2-dichloro- (1) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Ethane, 1,2-dichloro- (1) - Liquid mixture 1
283.60	0.0014
292.60	0.0014
302.30	0.0013

Mass fraction of Water (2) [ref]

Operational conditions:

• Pressure, kPa = 100 (Liquid mixture 1)
• Temperature, K = 298.15 (Liquid mixture 1)

Mass fraction of Water (2) - Liquid mixture 1
0.9387
0.0771

Henry's Law constant (molality scale), kPa*kg/mol of Ethane, 1,2-dichloro- (1) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid	Henry's Law constant (molality scale), kPa*kg/mol of Ethane, 1,2-dichloro- (1) - Liquid
274.15	42.87
294.65	98.2
294.65	102.1
296.15	104.9
310.15	211.4
320.15	389.0
331.15	516.91

Mole fraction of Ethane, 1,2-dichloro- (1) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Ethane, 1,2-dichloro- (1) - Liquid mixture 1
283.60	0.0014
292.60	0.0014
302.30	0.0013

Mass fraction of Water (2) [ref]

Operational conditions:

• Pressure, kPa = 100 (Liquid mixture 1)
• Temperature, K = 298.15 (Liquid mixture 1)

Mass fraction of Water (2) - Liquid mixture 1
0.9387
0.0771

Henry's Law constant (molality scale), kPa*kg/mol of Ethane, 1,2-dichloro- (1) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Temperature, K - Liquid	Henry's Law constant (molality scale), kPa*kg/mol of Ethane, 1,2-dichloro- (1) - Liquid
274.15	42.87
294.65	98.2
294.65	102.1
296.15	104.9
310.15	211.4
320.15	389.0
331.15	516.91

Sources

• A simple apparatus for data solubility determination
• Salting-out effect on the (liquid + liquid) equilibrium for the ternary systems (water + phosphoric acid + dichloromethane or 1,2-dichloroethane)
• Determination of Henry's Law Constants Using Internal Standards with Benchmark Values