Mixture of Methyl formate + Water

Datasets

1. Activity coefficient (2)
2. Interfacial tension, N/m (2)
3. ρ_l - Mass density, kg/m3 (4)

Activity coefficient of Methyl formate (1) [ref]

Operational conditions:

• Pressure, kPa = 101.325 (Liquid)
• Mole fraction = 0 (Liquid)

Temperature, K - Liquid	Activity coefficient of Methyl formate (1) - Liquid
303.25	18.7
313.25	19.1
323.25	19.5
333.25	19.8

Activity coefficient of Methyl formate (1) [ref]

Operational conditions:

• Pressure, kPa = 101.325 (Liquid)
• Mole fraction = 0 (Liquid)

Temperature, K - Liquid	Activity coefficient of Methyl formate (1) - Liquid
303.25	18.7
313.25	19.1
323.25	19.5
333.25	19.8

Interfacial tension, N/m [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Interfacial tension, N/m - Liquid mixture 1
278.15	0.0006
288.15	0.0008

Interfacial tension, N/m [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Interfacial tension, N/m - Liquid mixture 1
278.15	0.0006
288.15	0.0008

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mass density, kg/m3 - Liquid mixture 1
278.15	1019.8
288.15	1016.75

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)

Temperature, K - Liquid mixture 2	Mass density, kg/m3 - Liquid mixture 2
278.15	1001.25
288.15	990.05

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mass density, kg/m3 - Liquid mixture 1
278.15	1019.8
288.15	1016.75

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)

Temperature, K - Liquid mixture 2	Mass density, kg/m3 - Liquid mixture 2
278.15	1001.25
288.15	990.05

Sources

• Densities and interfacial tensions for fatty acid methyl esters (from methyl formate to methyl heptanoate) + water demixed mixtures at atmospheric pressure conditions
• Measurement of Activity Coefficients at Infinite Dilution of Benzene, Toluene, Ethanol, Esters, Ketones, and Ethers at Various Temperatures in Water Using the Dilutor Technique