Mixture of Toluene + Butane, 2-chloro-

Datasets

1. Mole fraction (2)
2. T_boil - Boiling temperature at pressure P, K (2)
3. Excess molar volume, m3/mol (2)

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

Fixed		Measured
Mole fraction of Butane, 2-chloro- (2) - Liquid	Pressure, kPa - Gas	Mole fraction of Butane, 2-chloro- (2) - Gas
0.0000	101.30	0.0000
0.0331	101.30	0.1170
0.1232	101.30	0.3239
0.1661	101.30	0.4179
0.2017	101.30	0.4797
0.2355	101.30	0.5354
0.3237	101.30	0.6521
0.3663	101.30	0.6895
0.4158	101.30	0.7322
0.4483	101.30	0.7532
0.5059	101.30	0.8017
0.5532	101.30	0.8314
0.6190	101.30	0.8667
0.6667	101.30	0.8903
0.7296	101.30	0.9123
0.7706	101.30	0.9296
0.7963	101.30	0.9384
0.8224	101.30	0.9503
0.8684	101.30	0.9596
0.9293	101.30	0.9890
1.0000	101.30	1.0000
0.0000	80.00	0.0000
0.0351	80.00	0.1276
0.0794	80.00	0.2393
0.1347	80.00	0.3704
0.1930	80.00	0.4816
0.2142	80.00	0.5167
0.2554	80.00	0.5868
0.2856	80.00	0.6195
0.2956	80.00	0.6376
0.3258	80.00	0.6567
0.3761	80.00	0.7180
0.4516	80.00	0.7832
0.5149	80.00	0.8184
0.5904	80.00	0.8630
0.6497	80.00	0.8856
0.7413	80.00	0.9194
0.8389	80.00	0.9596
0.9384	80.00	0.9897
1.0000	80.00	1.0000
0.0000	53.30	0.0000
0.0461	53.30	0.1472
0.0592	53.30	0.1850
0.1538	53.30	0.4021
0.1759	53.30	0.4428
0.1829	53.30	0.4591
0.1961	53.30	0.5021
0.2574	53.30	0.5927
0.3046	53.30	0.6537
0.3100	53.30	0.6615
0.3399	53.30	0.6950
0.4575	53.30	0.7983
0.4756	53.30	0.8088
0.5139	53.30	0.8267
0.5773	53.30	0.8589
0.6588	53.30	0.8952
0.7402	53.30	0.9284
0.8389	53.30	0.9505
0.9465	53.30	0.9897
1.0000	53.30	1.0000

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

Fixed		Measured
Mole fraction of Butane, 2-chloro- (2) - Liquid	Pressure, kPa - Gas	Mole fraction of Butane, 2-chloro- (2) - Gas
0.0000	101.30	0.0000
0.0331	101.30	0.1170
0.1232	101.30	0.3239
0.1661	101.30	0.4179
0.2017	101.30	0.4797
0.2355	101.30	0.5354
0.3237	101.30	0.6521
0.3663	101.30	0.6895
0.4158	101.30	0.7322
0.4483	101.30	0.7532
0.5059	101.30	0.8017
0.5532	101.30	0.8314
0.6190	101.30	0.8667
0.6667	101.30	0.8903
0.7296	101.30	0.9123
0.7706	101.30	0.9296
0.7963	101.30	0.9384
0.8224	101.30	0.9503
0.8684	101.30	0.9596
0.9293	101.30	0.9890
1.0000	101.30	1.0000
0.0000	80.00	0.0000
0.0351	80.00	0.1276
0.0794	80.00	0.2393
0.1347	80.00	0.3704
0.1930	80.00	0.4816
0.2142	80.00	0.5167
0.2554	80.00	0.5868
0.2856	80.00	0.6195
0.2956	80.00	0.6376
0.3258	80.00	0.6567
0.3761	80.00	0.7180
0.4516	80.00	0.7832
0.5149	80.00	0.8184
0.5904	80.00	0.8630
0.6497	80.00	0.8856
0.7413	80.00	0.9194
0.8389	80.00	0.9596
0.9384	80.00	0.9897
1.0000	80.00	1.0000
0.0000	53.30	0.0000
0.0461	53.30	0.1472
0.0592	53.30	0.1850
0.1538	53.30	0.4021
0.1759	53.30	0.4428
0.1829	53.30	0.4591
0.1961	53.30	0.5021
0.2574	53.30	0.5927
0.3046	53.30	0.6537
0.3100	53.30	0.6615
0.3399	53.30	0.6950
0.4575	53.30	0.7983
0.4756	53.30	0.8088
0.5139	53.30	0.8267
0.5773	53.30	0.8589
0.6588	53.30	0.8952
0.7402	53.30	0.9284
0.8389	53.30	0.9505
0.9465	53.30	0.9897
1.0000	53.30	1.0000

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of Butane, 2-chloro- (2) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	101.30	383.76
0.0331	101.30	381.04
0.1232	101.30	375.65
0.1661	101.30	372.75
0.2017	101.30	370.25
0.2355	101.30	368.15
0.3237	101.30	363.25
0.3663	101.30	361.40
0.4158	101.30	359.05
0.4483	101.30	357.80
0.5059	101.30	355.25
0.5532	101.30	353.65
0.6190	101.30	351.49
0.6667	101.30	349.95
0.7296	101.30	347.95
0.7706	101.30	347.05
0.7963	101.30	346.30
0.8224	101.30	345.34
0.8684	101.30	344.45
0.9293	101.30	342.80
1.0000	101.30	341.23
0.0000	80.00	375.66
0.0351	80.00	372.78
0.0794	80.00	369.94
0.1347	80.00	366.16
0.1930	80.00	362.51
0.2142	80.00	361.37
0.2554	80.00	358.61
0.2856	80.00	357.21
0.2956	80.00	356.41
0.3258	80.00	355.26
0.3761	80.00	352.64
0.4516	80.00	348.99
0.5149	80.00	346.94
0.5904	80.00	344.46
0.6497	80.00	342.37
0.7413	80.00	339.92
0.8389	80.00	337.41
0.9384	80.00	335.26
1.0000	80.00	334.01
0.0000	53.30	362.64
0.0461	53.30	359.52
0.0592	53.30	358.58
0.1538	53.30	352.90
0.1759	53.30	351.54
0.1829	53.30	350.97
0.1961	53.30	349.47
0.2574	53.30	346.15
0.3046	53.30	343.46
0.3100	53.30	343.45
0.3399	53.30	341.66
0.4575	53.30	336.35
0.4756	53.30	335.91
0.5139	53.30	334.81
0.5773	53.30	332.64
0.6588	53.30	330.30
0.7402	53.30	328.11
0.8389	53.30	325.82
0.9465	53.30	323.46
1.0000	53.30	322.42

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of Butane, 2-chloro- (2) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	101.30	383.76
0.0331	101.30	381.04
0.1232	101.30	375.65
0.1661	101.30	372.75
0.2017	101.30	370.25
0.2355	101.30	368.15
0.3237	101.30	363.25
0.3663	101.30	361.40
0.4158	101.30	359.05
0.4483	101.30	357.80
0.5059	101.30	355.25
0.5532	101.30	353.65
0.6190	101.30	351.49
0.6667	101.30	349.95
0.7296	101.30	347.95
0.7706	101.30	347.05
0.7963	101.30	346.30
0.8224	101.30	345.34
0.8684	101.30	344.45
0.9293	101.30	342.80
1.0000	101.30	341.23
0.0000	80.00	375.66
0.0351	80.00	372.78
0.0794	80.00	369.94
0.1347	80.00	366.16
0.1930	80.00	362.51
0.2142	80.00	361.37
0.2554	80.00	358.61
0.2856	80.00	357.21
0.2956	80.00	356.41
0.3258	80.00	355.26
0.3761	80.00	352.64
0.4516	80.00	348.99
0.5149	80.00	346.94
0.5904	80.00	344.46
0.6497	80.00	342.37
0.7413	80.00	339.92
0.8389	80.00	337.41
0.9384	80.00	335.26
1.0000	80.00	334.01
0.0000	53.30	362.64
0.0461	53.30	359.52
0.0592	53.30	358.58
0.1538	53.30	352.90
0.1759	53.30	351.54
0.1829	53.30	350.97
0.1961	53.30	349.47
0.2574	53.30	346.15
0.3046	53.30	343.46
0.3100	53.30	343.45
0.3399	53.30	341.66
0.4575	53.30	336.35
0.4756	53.30	335.91
0.5139	53.30	334.81
0.5773	53.30	332.64
0.6588	53.30	330.30
0.7402	53.30	328.11
0.8389	53.30	325.82
0.9465	53.30	323.46
1.0000	53.30	322.42

Excess molar volume, m3/mol [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 298.15 (Liquid)

Mole fraction of Butane, 2-chloro- (2) - Liquid	Excess molar volume, m3/mol - Liquid
0.0856	-6.6000e-08
0.1276	-9.6000e-08
0.2495	-1.7300e-07
0.3441	-2.1200e-07
0.4723	-2.3200e-07
0.5018	-2.3400e-07
0.5569	-2.3200e-07
0.6025	-2.2100e-07
0.6712	-2.0600e-07
0.7991	-1.4600e-07
0.9046	-7.2000e-08
0.9432	-4.4000e-08

Excess molar volume, m3/mol [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 298.15 (Liquid)

Mole fraction of Butane, 2-chloro- (2) - Liquid	Excess molar volume, m3/mol - Liquid
0.0856	-6.6000e-08
0.1276	-9.6000e-08
0.2495	-1.7300e-07
0.3441	-2.1200e-07
0.4723	-2.3200e-07
0.5018	-2.3400e-07
0.5569	-2.3200e-07
0.6025	-2.2100e-07
0.6712	-2.0600e-07
0.7991	-1.4600e-07
0.9046	-7.2000e-08
0.9432	-4.4000e-08

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
• Molar Excess Volume of sec- and tert-Butyl Chloride with Aromatic Hydrocarbons at T = 298.15 K