Mixture of Toluene + Butane, 1-chloro-

Datasets

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

Mole fraction of Butane, 1-chloro- (2) [ref]

Fixed		Measured
Mole fraction of Butane, 1-chloro- (2) - Liquid	Pressure, kPa - Gas	Mole fraction of Butane, 1-chloro- (2) - Gas
0.0000	101.30	0.0000
0.1480	101.30	0.3079
0.1725	101.30	0.3498
0.2528	101.30	0.4668
0.2771	101.30	0.5098
0.3280	101.30	0.5728
0.3495	101.30	0.5962
0.4074	101.30	0.6584
0.4353	101.30	0.6928
0.4868	101.30	0.7292
0.5211	101.30	0.7538
0.5340	101.30	0.7632
0.5716	101.30	0.7989
0.6059	101.30	0.8215
0.6402	101.30	0.8338
0.7228	101.30	0.8848
0.7657	101.30	0.9062
0.8076	101.30	0.9256
0.8451	101.30	0.9438
0.8848	101.30	0.9599
1.0000	101.30	1.0000
0.0000	80.00	0.0000
0.1339	80.00	0.2873
0.1564	80.00	0.3474
0.1993	80.00	0.4085
0.2637	80.00	0.4889
0.3184	80.00	0.5559
0.3506	80.00	0.5962
0.4031	80.00	0.6584
0.4332	80.00	0.6896
0.4868	80.00	0.7260
0.5179	80.00	0.7561
0.5726	80.00	0.7989
0.6069	80.00	0.8215
0.6369	80.00	0.8315
0.7249	80.00	0.8826
0.7625	80.00	0.9052
0.8097	80.00	0.9277
0.8419	80.00	0.9449
0.8859	80.00	0.9599
1.0000	80.00	1.0000
0.0000	53.30	0.0000
0.1285	53.30	0.2862
0.1618	53.30	0.3474
0.1972	53.30	0.4128
0.2401	53.30	0.4686
0.3173	53.30	0.5629
0.3506	53.30	0.6069
0.4031	53.30	0.6595
0.4332	53.30	0.6863
0.4868	53.30	0.7273
0.5104	53.30	0.7549
0.5716	53.30	0.7893
0.6069	53.30	0.8258
0.6359	53.30	0.8312
0.7249	53.30	0.8848
0.7693	53.30	0.9041
0.8108	53.30	0.9277
0.8419	53.30	0.9416
0.8848	53.30	0.9609
1.0000	53.30	1.0000

Mole fraction of Butane, 1-chloro- (2) [ref]

Fixed		Measured
Mole fraction of Butane, 1-chloro- (2) - Liquid	Pressure, kPa - Gas	Mole fraction of Butane, 1-chloro- (2) - Gas
0.0000	101.30	0.0000
0.1480	101.30	0.3079
0.1725	101.30	0.3498
0.2528	101.30	0.4668
0.2771	101.30	0.5098
0.3280	101.30	0.5728
0.3495	101.30	0.5962
0.4074	101.30	0.6584
0.4353	101.30	0.6928
0.4868	101.30	0.7292
0.5211	101.30	0.7538
0.5340	101.30	0.7632
0.5716	101.30	0.7989
0.6059	101.30	0.8215
0.6402	101.30	0.8338
0.7228	101.30	0.8848
0.7657	101.30	0.9062
0.8076	101.30	0.9256
0.8451	101.30	0.9438
0.8848	101.30	0.9599
1.0000	101.30	1.0000
0.0000	80.00	0.0000
0.1339	80.00	0.2873
0.1564	80.00	0.3474
0.1993	80.00	0.4085
0.2637	80.00	0.4889
0.3184	80.00	0.5559
0.3506	80.00	0.5962
0.4031	80.00	0.6584
0.4332	80.00	0.6896
0.4868	80.00	0.7260
0.5179	80.00	0.7561
0.5726	80.00	0.7989
0.6069	80.00	0.8215
0.6369	80.00	0.8315
0.7249	80.00	0.8826
0.7625	80.00	0.9052
0.8097	80.00	0.9277
0.8419	80.00	0.9449
0.8859	80.00	0.9599
1.0000	80.00	1.0000
0.0000	53.30	0.0000
0.1285	53.30	0.2862
0.1618	53.30	0.3474
0.1972	53.30	0.4128
0.2401	53.30	0.4686
0.3173	53.30	0.5629
0.3506	53.30	0.6069
0.4031	53.30	0.6595
0.4332	53.30	0.6863
0.4868	53.30	0.7273
0.5104	53.30	0.7549
0.5716	53.30	0.7893
0.6069	53.30	0.8258
0.6359	53.30	0.8312
0.7249	53.30	0.8848
0.7693	53.30	0.9041
0.8108	53.30	0.9277
0.8419	53.30	0.9416
0.8848	53.30	0.9609
1.0000	53.30	1.0000

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of Butane, 1-chloro- (2) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	101.30	383.76
0.1480	101.30	377.39
0.1725	101.30	376.38
0.2528	101.30	373.13
0.2771	101.30	371.92
0.3280	101.30	369.81
0.3495	101.30	368.94
0.4074	101.30	367.04
0.4353	101.30	365.93
0.4868	101.30	364.50
0.5211	101.30	363.30
0.5340	101.30	362.91
0.5716	101.30	361.70
0.6059	101.30	360.74
0.6402	101.30	359.81
0.7228	101.30	357.84
0.7657	101.30	356.79
0.8076	101.30	355.77
0.8451	101.30	354.99
0.8848	101.30	353.99
1.0000	101.30	351.53
0.0000	80.00	375.66
0.1339	80.00	369.51
0.1564	80.00	368.34
0.1993	80.00	366.46
0.2637	80.00	364.23
0.3184	80.00	362.10
0.3506	80.00	360.98
0.4031	80.00	359.26
0.4332	80.00	358.32
0.4868	80.00	356.92
0.5179	80.00	355.78
0.5726	80.00	354.35
0.6069	80.00	353.24
0.6369	80.00	352.79
0.7249	80.00	350.43
0.7625	80.00	349.48
0.8097	80.00	348.41
0.8419	80.00	347.55
0.8859	80.00	346.69
1.0000	80.00	344.14
0.0000	53.30	362.64
0.1285	53.30	356.60
0.1618	53.30	355.31
0.1972	53.30	353.85
0.2401	53.30	352.32
0.3173	53.30	349.64
0.3506	53.30	348.42
0.4031	53.30	346.90
0.4332	53.30	345.97
0.4868	53.30	344.40
0.5104	53.30	343.66
0.5716	53.30	342.27
0.6069	53.30	340.88
0.6359	53.30	340.64
0.7249	53.30	338.36
0.7693	53.30	337.53
0.8108	53.30	336.39
0.8419	53.30	335.74
0.8848	53.30	334.77
1.0000	53.30	332.28

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of Butane, 1-chloro- (2) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	101.30	383.76
0.1480	101.30	377.39
0.1725	101.30	376.38
0.2528	101.30	373.13
0.2771	101.30	371.92
0.3280	101.30	369.81
0.3495	101.30	368.94
0.4074	101.30	367.04
0.4353	101.30	365.93
0.4868	101.30	364.50
0.5211	101.30	363.30
0.5340	101.30	362.91
0.5716	101.30	361.70
0.6059	101.30	360.74
0.6402	101.30	359.81
0.7228	101.30	357.84
0.7657	101.30	356.79
0.8076	101.30	355.77
0.8451	101.30	354.99
0.8848	101.30	353.99
1.0000	101.30	351.53
0.0000	80.00	375.66
0.1339	80.00	369.51
0.1564	80.00	368.34
0.1993	80.00	366.46
0.2637	80.00	364.23
0.3184	80.00	362.10
0.3506	80.00	360.98
0.4031	80.00	359.26
0.4332	80.00	358.32
0.4868	80.00	356.92
0.5179	80.00	355.78
0.5726	80.00	354.35
0.6069	80.00	353.24
0.6369	80.00	352.79
0.7249	80.00	350.43
0.7625	80.00	349.48
0.8097	80.00	348.41
0.8419	80.00	347.55
0.8859	80.00	346.69
1.0000	80.00	344.14
0.0000	53.30	362.64
0.1285	53.30	356.60
0.1618	53.30	355.31
0.1972	53.30	353.85
0.2401	53.30	352.32
0.3173	53.30	349.64
0.3506	53.30	348.42
0.4031	53.30	346.90
0.4332	53.30	345.97
0.4868	53.30	344.40
0.5104	53.30	343.66
0.5716	53.30	342.27
0.6069	53.30	340.88
0.6359	53.30	340.64
0.7249	53.30	338.36
0.7693	53.30	337.53
0.8108	53.30	336.39
0.8419	53.30	335.74
0.8848	53.30	334.77
1.0000	53.30	332.28

Sources

• Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa