Mixture of Benzene, fluoro- + Heptane

Datasets

1. Mole fraction (4)
2. T_boil - Boiling temperature at pressure P, K (4)

Mole fraction of Benzene, fluoro- (1) [ref]

Fixed		Measured
Mole fraction of Benzene, fluoro- (1) - Liquid	Pressure, kPa - Gas	Mole fraction of Benzene, fluoro- (1) - Gas
0.0000	100.60	0.0000
0.0734	100.69	0.1472
0.1923	100.71	0.3248
0.2952	100.69	0.4401
0.4257	100.67	0.5559
0.5564	100.66	0.6519
0.7017	100.61	0.7504
0.7989	100.61	0.8197
0.8959	100.59	0.8953
0.9373	100.64	0.9334
0.9836	100.61	0.9817
1.0000	100.55	1.0000

Mole fraction of Heptane (2) [ref]

Operational condition: Pressure, kPa = 101.4 (Gas)

Mole fraction of Heptane (2) - Liquid	Mole fraction of Heptane (2) - Gas
0.0230	0.0310
0.0480	0.0570
0.1040	0.1060
0.1660	0.1530
0.2590	0.2090
0.3180	0.2520
0.3990	0.2960
0.4300	0.3230
0.4660	0.3480
0.5090	0.3740
0.5780	0.4290
0.6480	0.4910
0.7420	0.5910
0.8160	0.6750
0.8450	0.7340
0.9130	0.8400
0.9520	0.9020
0.9820	0.9630

Mole fraction of Benzene, fluoro- (1) [ref]

Fixed		Measured
Mole fraction of Benzene, fluoro- (1) - Liquid	Pressure, kPa - Gas	Mole fraction of Benzene, fluoro- (1) - Gas
0.0000	100.60	0.0000
0.0734	100.69	0.1472
0.1923	100.71	0.3248
0.2952	100.69	0.4401
0.4257	100.67	0.5559
0.5564	100.66	0.6519
0.7017	100.61	0.7504
0.7989	100.61	0.8197
0.8959	100.59	0.8953
0.9373	100.64	0.9334
0.9836	100.61	0.9817
1.0000	100.55	1.0000

Mole fraction of Heptane (2) [ref]

Operational condition: Pressure, kPa = 101.4 (Gas)

Mole fraction of Heptane (2) - Liquid	Mole fraction of Heptane (2) - Gas
0.0230	0.0310
0.0480	0.0570
0.1040	0.1060
0.1660	0.1530
0.2590	0.2090
0.3180	0.2520
0.3990	0.2960
0.4300	0.3230
0.4660	0.3480
0.5090	0.3740
0.5780	0.4290
0.6480	0.4910
0.7420	0.5910
0.8160	0.6750
0.8450	0.7340
0.9130	0.8400
0.9520	0.9020
0.9820	0.9630

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of Benzene, fluoro- (1) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	100.60	371.30
0.0734	100.69	368.50
0.1923	100.71	364.90
0.2952	100.69	362.50
0.4257	100.67	360.40
0.5564	100.66	358.90
0.7017	100.61	357.80
0.7989	100.61	357.40
0.8959	100.59	357.20
0.9373	100.64	357.30
0.9836	100.61	357.40
1.0000	100.55	357.50

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.4 (Gas)

Mole fraction of Heptane (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0230	357.30
0.0480	357.70
0.1040	357.60
0.1660	357.80
0.2590	358.20
0.3180	358.50
0.3990	359.00
0.4300	359.30
0.4660	359.60
0.5090	359.90
0.5780	360.60
0.6480	361.70
0.7420	363.40
0.8160	365.10
0.8450	366.00
0.9130	368.10
0.9520	369.10
0.9820	370.30

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of Benzene, fluoro- (1) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	100.60	371.30
0.0734	100.69	368.50
0.1923	100.71	364.90
0.2952	100.69	362.50
0.4257	100.67	360.40
0.5564	100.66	358.90
0.7017	100.61	357.80
0.7989	100.61	357.40
0.8959	100.59	357.20
0.9373	100.64	357.30
0.9836	100.61	357.40
1.0000	100.55	357.50

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.4 (Gas)

Mole fraction of Heptane (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0230	357.30
0.0480	357.70
0.1040	357.60
0.1660	357.80
0.2590	358.20
0.3180	358.50
0.3990	359.00
0.4300	359.30
0.4660	359.60
0.5090	359.90
0.5780	360.60
0.6480	361.70
0.7420	363.40
0.8160	365.10
0.8450	366.00
0.9130	368.10
0.9520	369.10
0.9820	370.30

Sources

• Isobaric vapour liquid equilibria for binary mixtures of n-heptane with bromobenzene, chlorobenzene and fluorobenzene at atmospheric pressure
• Measurements and Calculation of Vapor-Liquid Equilibria for the Binary Mixtures of Fluorobenzene and Alkanes at a Pressure of 101.4 kPa