Mixture of Diisopropyl ether + Propane, 1-chloro-2-methyl-

Datasets

1. Mole fraction (2)
2. η - Viscosity, Pa*s (2)
3. Excess molar enthalpy (molar enthalpy (2)
4. P_vap - Vapor or sublimation pressure, kPa (2)
5. n₀ - Refractive index (Na D-line) (2)
6. ρ_l - Mass density, kg/m3 (4)
7. c_sound,fluid - Speed of Sound, m/s (2)

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

Fixed		Measured
Mole fraction of Propane, 1-chloro-2-methyl- (2) - Liquid	Temperature, K - Liquid	Mole fraction of Propane, 1-chloro-2-methyl- (2) - Gas
0.0897	288.15	0.0932
0.0943	308.15	0.0985
0.0990	298.15	0.1003
0.1395	298.15	0.1427
0.1420	308.15	0.1461
0.1448	288.15	0.1465
0.2211	288.15	0.2275
0.2385	308.15	0.2397
0.2548	298.15	0.2570
0.2913	288.15	0.2925
0.3628	288.15	0.3685
0.3631	308.15	0.3655
0.3685	298.15	0.3700
0.4004	298.15	0.4035
0.4095	288.15	0.4137
0.4613	308.15	0.4612
0.4950	298.15	0.4962
0.5362	288.15	0.5363
0.5386	308.15	0.5364
0.5495	298.15	0.5492
0.6470	308.15	0.6424
0.6481	298.15	0.6460
0.6628	288.15	0.6625
0.7247	308.15	0.7202
0.7426	298.15	0.7421
0.7829	288.15	0.7803
0.8323	308.15	0.8285
0.8603	298.15	0.8568
0.8604	288.15	0.8562
0.9285	308.15	0.9276
0.9320	288.15	0.9315
0.9350	298.15	0.9318

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

Fixed		Measured
Mole fraction of Propane, 1-chloro-2-methyl- (2) - Liquid	Temperature, K - Liquid	Mole fraction of Propane, 1-chloro-2-methyl- (2) - Gas
0.0897	288.15	0.0932
0.0943	308.15	0.0985
0.0990	298.15	0.1003
0.1395	298.15	0.1427
0.1420	308.15	0.1461
0.1448	288.15	0.1465
0.2211	288.15	0.2275
0.2385	308.15	0.2397
0.2548	298.15	0.2570
0.2913	288.15	0.2925
0.3628	288.15	0.3685
0.3631	308.15	0.3655
0.3685	298.15	0.3700
0.4004	298.15	0.4035
0.4095	288.15	0.4137
0.4613	308.15	0.4612
0.4950	298.15	0.4962
0.5362	288.15	0.5363
0.5386	308.15	0.5364
0.5495	298.15	0.5492
0.6470	308.15	0.6424
0.6481	298.15	0.6460
0.6628	288.15	0.6625
0.7247	308.15	0.7202
0.7426	298.15	0.7421
0.7829	288.15	0.7803
0.8323	308.15	0.8285
0.8603	298.15	0.8568
0.8604	288.15	0.8562
0.9285	308.15	0.9276
0.9320	288.15	0.9315
0.9350	298.15	0.9318

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Propane, 1-chloro-2-methyl- (2) - Liquid	Viscosity, Pa*s - Liquid
283.15	0.0000	0.0004
283.15	0.0549	0.0004
283.15	0.0910	0.0004
283.15	0.1977	0.0004
283.15	0.2934	0.0004
283.15	0.3911	0.0004
283.15	0.5137	0.0004
283.15	0.6034	0.0004
283.15	0.6769	0.0005
283.15	0.8059	0.0005
283.15	0.9111	0.0005
283.15	0.9646	0.0005
283.15	1.0000	0.0005
288.15	0.0000	0.0003
288.15	0.0549	0.0004
288.15	0.0910	0.0004
288.15	0.1977	0.0004
288.15	0.2934	0.0004
288.15	0.3911	0.0004
288.15	0.5137	0.0004
288.15	0.6034	0.0004
288.15	0.6769	0.0004
288.15	0.8059	0.0004
288.15	0.9111	0.0005
288.15	0.9646	0.0005
288.15	1.0000	0.0005
293.15	0.0000	0.0003
293.15	0.0549	0.0003
293.15	0.0910	0.0003
293.15	0.1977	0.0004
293.15	0.2934	0.0004
293.15	0.3911	0.0004
293.15	0.5137	0.0004
293.15	0.6034	0.0004
293.15	0.6769	0.0004
293.15	0.8059	0.0004
293.15	0.9111	0.0004
293.15	0.9646	0.0004
293.15	1.0000	0.0005
298.15	0.0000	0.0003
298.15	0.0549	0.0003
298.15	0.0910	0.0003
298.15	0.1977	0.0003
298.15	0.2934	0.0003
298.15	0.3911	0.0004
298.15	0.5137	0.0004
298.15	0.6034	0.0004
298.15	0.6769	0.0004
298.15	0.8059	0.0004
298.15	0.9111	0.0004
298.15	0.9646	0.0004
298.15	1.0000	0.0004
303.15	0.0000	0.0003
303.15	0.0549	0.0003
303.15	0.0910	0.0003
303.15	0.1977	0.0003
303.15	0.2934	0.0003
303.15	0.3911	0.0003
303.15	0.5137	0.0003
303.15	0.6034	0.0004
303.15	0.6769	0.0004
303.15	0.8059	0.0004
303.15	0.9111	0.0004
303.15	0.9646	0.0004
303.15	1.0000	0.0004
308.15	0.0000	0.0003
308.15	0.0549	0.0003
308.15	0.0910	0.0003
308.15	0.1977	0.0003
308.15	0.2934	0.0003
308.15	0.3911	0.0003
308.15	0.5137	0.0003
308.15	0.6034	0.0003
308.15	0.6769	0.0003
308.15	0.8059	0.0004
308.15	0.9111	0.0004
308.15	0.9646	0.0004
308.15	1.0000	0.0004
313.15	0.0000	0.0003
313.15	0.0549	0.0003
313.15	0.0910	0.0003
313.15	0.1977	0.0003
313.15	0.2934	0.0003
313.15	0.3911	0.0003
313.15	0.5137	0.0003
313.15	0.6034	0.0003
313.15	0.6769	0.0003
313.15	0.8059	0.0003
313.15	0.9111	0.0004
313.15	0.9646	0.0004
313.15	1.0000	0.0004

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Propane, 1-chloro-2-methyl- (2) - Liquid	Viscosity, Pa*s - Liquid
283.15	0.0000	0.0004
283.15	0.0549	0.0004
283.15	0.0910	0.0004
283.15	0.1977	0.0004
283.15	0.2934	0.0004
283.15	0.3911	0.0004
283.15	0.5137	0.0004
283.15	0.6034	0.0004
283.15	0.6769	0.0005
283.15	0.8059	0.0005
283.15	0.9111	0.0005
283.15	0.9646	0.0005
283.15	1.0000	0.0005
288.15	0.0000	0.0003
288.15	0.0549	0.0004
288.15	0.0910	0.0004
288.15	0.1977	0.0004
288.15	0.2934	0.0004
288.15	0.3911	0.0004
288.15	0.5137	0.0004
288.15	0.6034	0.0004
288.15	0.6769	0.0004
288.15	0.8059	0.0004
288.15	0.9111	0.0005
288.15	0.9646	0.0005
288.15	1.0000	0.0005
293.15	0.0000	0.0003
293.15	0.0549	0.0003
293.15	0.0910	0.0003
293.15	0.1977	0.0004
293.15	0.2934	0.0004
293.15	0.3911	0.0004
293.15	0.5137	0.0004
293.15	0.6034	0.0004
293.15	0.6769	0.0004
293.15	0.8059	0.0004
293.15	0.9111	0.0004
293.15	0.9646	0.0004
293.15	1.0000	0.0005
298.15	0.0000	0.0003
298.15	0.0549	0.0003
298.15	0.0910	0.0003
298.15	0.1977	0.0003
298.15	0.2934	0.0003
298.15	0.3911	0.0004
298.15	0.5137	0.0004
298.15	0.6034	0.0004
298.15	0.6769	0.0004
298.15	0.8059	0.0004
298.15	0.9111	0.0004
298.15	0.9646	0.0004
298.15	1.0000	0.0004
303.15	0.0000	0.0003
303.15	0.0549	0.0003
303.15	0.0910	0.0003
303.15	0.1977	0.0003
303.15	0.2934	0.0003
303.15	0.3911	0.0003
303.15	0.5137	0.0003
303.15	0.6034	0.0004
303.15	0.6769	0.0004
303.15	0.8059	0.0004
303.15	0.9111	0.0004
303.15	0.9646	0.0004
303.15	1.0000	0.0004
308.15	0.0000	0.0003
308.15	0.0549	0.0003
308.15	0.0910	0.0003
308.15	0.1977	0.0003
308.15	0.2934	0.0003
308.15	0.3911	0.0003
308.15	0.5137	0.0003
308.15	0.6034	0.0003
308.15	0.6769	0.0003
308.15	0.8059	0.0004
308.15	0.9111	0.0004
308.15	0.9646	0.0004
308.15	1.0000	0.0004
313.15	0.0000	0.0003
313.15	0.0549	0.0003
313.15	0.0910	0.0003
313.15	0.1977	0.0003
313.15	0.2934	0.0003
313.15	0.3911	0.0003
313.15	0.5137	0.0003
313.15	0.6034	0.0003
313.15	0.6769	0.0003
313.15	0.8059	0.0003
313.15	0.9111	0.0004
313.15	0.9646	0.0004
313.15	1.0000	0.0004

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

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

Mole fraction of Propane, 1-chloro-2-methyl- (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0907	-0.0302
0.1815	-0.0541
0.2726	-0.0732
0.3634	-0.0863
0.4544	-0.0948
0.5453	-0.0957
0.6361	-0.0915
0.7270	-0.0791
0.8179	-0.0615
0.9090	-0.0344

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

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

Mole fraction of Propane, 1-chloro-2-methyl- (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0907	-0.0302
0.1815	-0.0541
0.2726	-0.0732
0.3634	-0.0863
0.4544	-0.0948
0.5453	-0.0957
0.6361	-0.0915
0.7270	-0.0791
0.8179	-0.0615
0.9090	-0.0344

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Propane, 1-chloro-2-methyl- (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0897	288.15	12.71
0.0943	308.15	30.55
0.0990	298.15	20.12
0.1395	298.15	20.12
0.1420	308.15	30.56
0.1448	288.15	12.73
0.2211	288.15	12.79
0.2385	308.15	30.60
0.2548	298.15	20.21
0.2913	288.15	12.82
0.3628	288.15	12.89
0.3631	308.15	30.67
0.3685	298.15	20.27
0.4004	298.15	20.29
0.4095	288.15	12.89
0.4613	308.15	30.68
0.4950	298.15	20.33
0.5362	288.15	12.94
0.5386	308.15	30.64
0.5495	298.15	20.38
0.6470	308.15	30.58
0.6481	298.15	20.41
0.6628	288.15	13.00
0.7247	308.15	30.57
0.7426	298.15	20.37
0.7829	288.15	13.01
0.8323	308.15	30.54
0.8603	298.15	20.38
0.8604	288.15	13.01
0.9285	308.15	30.50
0.9320	288.15	13.01
0.9350	298.15	20.37

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Propane, 1-chloro-2-methyl- (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0897	288.15	12.71
0.0943	308.15	30.55
0.0990	298.15	20.12
0.1395	298.15	20.12
0.1420	308.15	30.56
0.1448	288.15	12.73
0.2211	288.15	12.79
0.2385	308.15	30.60
0.2548	298.15	20.21
0.2913	288.15	12.82
0.3628	288.15	12.89
0.3631	308.15	30.67
0.3685	298.15	20.27
0.4004	298.15	20.29
0.4095	288.15	12.89
0.4613	308.15	30.68
0.4950	298.15	20.33
0.5362	288.15	12.94
0.5386	308.15	30.64
0.5495	298.15	20.38
0.6470	308.15	30.58
0.6481	298.15	20.41
0.6628	288.15	13.00
0.7247	308.15	30.57
0.7426	298.15	20.37
0.7829	288.15	13.01
0.8323	308.15	30.54
0.8603	298.15	20.38
0.8604	288.15	13.01
0.9285	308.15	30.50
0.9320	288.15	13.01
0.9350	298.15	20.37

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Propane, 1-chloro-2-methyl- (2) - Liquid	Refractive index (Na D-line) - Liquid
283.15	0.0549	1.3749
283.15	0.0910	1.3759
283.15	0.1977	1.3787
283.15	0.2934	1.3813
283.15	0.3911	1.384
283.15	0.5137	1.3876
283.15	0.6034	1.3903
283.15	0.6769	1.3926
283.15	0.8059	1.3968
283.15	0.9111	1.4004
283.15	0.9646	1.4023
288.15	0.0549	1.3722
288.15	0.0910	1.3732
288.15	0.1977	1.376
288.15	0.2934	1.3785
288.15	0.3911	1.3813
288.15	0.5137	1.3849
288.15	0.6034	1.3876
288.15	0.6769	1.3899
288.15	0.8059	1.3941
288.15	0.9111	1.3976
288.15	0.9646	1.3995
293.15	0.0549	1.3695
293.15	0.0910	1.3704
293.15	0.1977	1.3732
293.15	0.2934	1.3758
293.15	0.3911	1.3786
293.15	0.5137	1.3821
293.15	0.6034	1.3848
293.15	0.6769	1.3871
293.15	0.8059	1.3913
293.15	0.9111	1.3949
293.15	0.9646	1.3967
298.15	0.0549	1.3666
298.15	0.0910	1.3676
298.15	0.1977	1.3704
298.15	0.2934	1.373
298.15	0.3911	1.3758
298.15	0.5137	1.3793
298.15	0.6034	1.382
298.15	0.6769	1.3844
298.15	0.8059	1.3885
298.15	0.9111	1.3921
298.15	0.9646	1.394
303.15	0.0549	1.3638
303.15	0.0910	1.3647
303.15	0.1977	1.3675
303.15	0.2934	1.3701
303.15	0.3911	1.3729
303.15	0.5137	1.3765
303.15	0.6034	1.3792
303.15	0.6769	1.3815
303.15	0.8059	1.3857
303.15	0.9111	1.3893
303.15	0.9646	1.3912
308.15	0.0549	1.3609
308.15	0.0910	1.3619
308.15	0.1977	1.3647
308.15	0.2934	1.3673
308.15	0.3911	1.3701
308.15	0.5137	1.3737
308.15	0.6034	1.3764
308.15	0.6769	1.3787
308.15	0.8059	1.3828
308.15	0.9111	1.3864
308.15	0.9646	1.3883
313.15	0.0549	1.3581
313.15	0.0910	1.359
313.15	0.1977	1.3618
313.15	0.2934	1.3644
313.15	0.3911	1.3672
313.15	0.5137	1.3708
313.15	0.6034	1.3735
313.15	0.6769	1.3759
313.15	0.8059	1.38
313.15	0.9111	1.3836
313.15	0.9646	1.3855

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Propane, 1-chloro-2-methyl- (2) - Liquid	Refractive index (Na D-line) - Liquid
283.15	0.0549	1.3749
283.15	0.0910	1.3759
283.15	0.1977	1.3787
283.15	0.2934	1.3813
283.15	0.3911	1.384
283.15	0.5137	1.3876
283.15	0.6034	1.3903
283.15	0.6769	1.3926
283.15	0.8059	1.3968
283.15	0.9111	1.4004
283.15	0.9646	1.4023
288.15	0.0549	1.3722
288.15	0.0910	1.3732
288.15	0.1977	1.376
288.15	0.2934	1.3785
288.15	0.3911	1.3813
288.15	0.5137	1.3849
288.15	0.6034	1.3876
288.15	0.6769	1.3899
288.15	0.8059	1.3941
288.15	0.9111	1.3976
288.15	0.9646	1.3995
293.15	0.0549	1.3695
293.15	0.0910	1.3704
293.15	0.1977	1.3732
293.15	0.2934	1.3758
293.15	0.3911	1.3786
293.15	0.5137	1.3821
293.15	0.6034	1.3848
293.15	0.6769	1.3871
293.15	0.8059	1.3913
293.15	0.9111	1.3949
293.15	0.9646	1.3967
298.15	0.0549	1.3666
298.15	0.0910	1.3676
298.15	0.1977	1.3704
298.15	0.2934	1.373
298.15	0.3911	1.3758
298.15	0.5137	1.3793
298.15	0.6034	1.382
298.15	0.6769	1.3844
298.15	0.8059	1.3885
298.15	0.9111	1.3921
298.15	0.9646	1.394
303.15	0.0549	1.3638
303.15	0.0910	1.3647
303.15	0.1977	1.3675
303.15	0.2934	1.3701
303.15	0.3911	1.3729
303.15	0.5137	1.3765
303.15	0.6034	1.3792
303.15	0.6769	1.3815
303.15	0.8059	1.3857
303.15	0.9111	1.3893
303.15	0.9646	1.3912
308.15	0.0549	1.3609
308.15	0.0910	1.3619
308.15	0.1977	1.3647
308.15	0.2934	1.3673
308.15	0.3911	1.3701
308.15	0.5137	1.3737
308.15	0.6034	1.3764
308.15	0.6769	1.3787
308.15	0.8059	1.3828
308.15	0.9111	1.3864
308.15	0.9646	1.3883
313.15	0.0549	1.3581
313.15	0.0910	1.359
313.15	0.1977	1.3618
313.15	0.2934	1.3644
313.15	0.3911	1.3672
313.15	0.5137	1.3708
313.15	0.6034	1.3735
313.15	0.6769	1.3759
313.15	0.8059	1.38
313.15	0.9111	1.3836
313.15	0.9646	1.3855

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Propane, 1-chloro-2-methyl- (2) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0000	733.833
283.15	0.0549	740.509
283.15	0.0910	745.071
283.15	0.1977	758.96
283.15	0.2934	772.077
283.15	0.3911	785.941
283.15	0.5137	804.21
283.15	0.6034	818.258
283.15	0.6769	830.206
283.15	0.8059	852.473
283.15	0.9111	871.773
283.15	0.9646	881.981
283.15	1.0000	888.845
288.15	0.0000	728.692
288.15	0.0549	735.346
288.15	0.0910	739.888
288.15	0.1977	753.737
288.15	0.2934	766.807
288.15	0.3911	780.617
288.15	0.5137	798.831
288.15	0.6034	812.821
288.15	0.6769	824.734
288.15	0.8059	846.936
288.15	0.9111	866.179
288.15	0.9646	876.368
288.15	1.0000	883.211
293.15	0.0000	723.509
293.15	0.0549	730.142
293.15	0.0910	734.678
293.15	0.1977	748.467
293.15	0.2934	761.481
293.15	0.3911	775.245
293.15	0.5137	793.406
293.15	0.6034	807.35
293.15	0.6769	819.228
293.15	0.8059	841.356
293.15	0.9111	860.549
293.15	0.9646	870.717
293.15	1.0000	877.539
298.15	0.0000	718.289
298.15	0.0549	724.887
298.15	0.0910	729.395
298.15	0.1977	743.114
298.15	0.2934	756.06
298.15	0.3911	769.763
298.15	0.5137	787.825
298.15	0.6034	801.699
298.15	0.6769	813.519
298.15	0.8059	835.53
298.15	0.9111	854.603
298.15	0.9646	864.749
298.15	1.0000	871.533
303.15	0.0000	713.032
303.15	0.0549	719.603
303.15	0.0910	724.11
303.15	0.1977	737.798
303.15	0.2934	750.738
303.15	0.3911	764.421
303.15	0.5137	782.446
303.15	0.6034	796.305
303.15	0.6769	808.11
303.15	0.8059	830.111
303.15	0.9111	849.196
303.15	0.9646	859.307
303.15	1.0000	866.096
308.15	0.0000	707.727
308.15	0.0549	714.28
308.15	0.0910	718.759
308.15	0.1977	732.397
308.15	0.2934	745.3
308.15	0.3911	758.935
308.15	0.5137	776.901
308.15	0.6034	790.719
308.15	0.6769	802.492
308.15	0.8059	824.422
308.15	0.9111	843.468
308.15	0.9646	853.542
308.15	1.0000	860.319
313.15	0.0000	702.378
313.15	0.0549	708.887
313.15	0.0910	713.334
313.15	0.1977	726.882
313.15	0.2934	739.693
313.15	0.3911	753.227
313.15	0.5137	771.077
313.15	0.6034	784.802
313.15	0.6769	796.487
313.15	0.8059	818.264
313.15	0.9111	837.168
313.15	0.9646	847.176
313.15	1.0000	853.902

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Propane, 1-chloro-2-methyl- (2) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0549	740.509
283.15	0.0910	745.071
283.15	0.1977	758.96
283.15	0.2934	772.077
283.15	0.3911	785.941
283.15	0.5137	804.21
283.15	0.6034	818.258
283.15	0.6769	830.206
283.15	0.8059	852.473
283.15	0.9111	871.773
283.15	0.9646	881.981
288.15	0.0549	735.346
288.15	0.0910	739.888
288.15	0.1977	753.737
288.15	0.2934	766.807
288.15	0.3911	780.617
288.15	0.5137	798.831
288.15	0.6034	812.821
288.15	0.6769	824.734
288.15	0.8059	846.936
288.15	0.9111	866.179
288.15	0.9646	876.368
293.15	0.0549	730.142
293.15	0.0910	734.678
293.15	0.1977	748.467
293.15	0.2934	761.481
293.15	0.3911	775.245
293.15	0.5137	793.406
293.15	0.6034	807.35
293.15	0.6769	819.228
293.15	0.8059	841.356
293.15	0.9111	860.549
293.15	0.9646	870.717
298.15	0.0549	724.887
298.15	0.0910	729.395
298.15	0.1977	743.114
298.15	0.2934	756.06
298.15	0.3911	769.763
298.15	0.5137	787.825
298.15	0.6034	801.699
298.15	0.6769	813.519
298.15	0.8059	835.53
298.15	0.9111	854.603
298.15	0.9646	864.749
303.15	0.0549	719.603
303.15	0.0910	724.11
303.15	0.1977	737.798
303.15	0.2934	750.738
303.15	0.3911	764.421
303.15	0.5137	782.446
303.15	0.6034	796.305
303.15	0.6769	808.11
303.15	0.8059	830.111
303.15	0.9111	849.196
303.15	0.9646	859.307
308.15	0.0549	714.28
308.15	0.0910	718.759
308.15	0.1977	732.397
308.15	0.2934	745.3
308.15	0.3911	758.935
308.15	0.5137	776.901
308.15	0.6034	790.719
308.15	0.6769	802.492
308.15	0.8059	824.422
308.15	0.9111	843.468
308.15	0.9646	853.542
313.15	0.0549	708.887
313.15	0.0910	713.334
313.15	0.1977	726.882
313.15	0.2934	739.693
313.15	0.3911	753.227
313.15	0.5137	771.077
313.15	0.6034	784.802
313.15	0.6769	796.487
313.15	0.8059	818.264
313.15	0.9111	837.168
313.15	0.9646	847.176

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Propane, 1-chloro-2-methyl- (2) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0000	733.833
283.15	0.0549	740.509
283.15	0.0910	745.071
283.15	0.1977	758.96
283.15	0.2934	772.077
283.15	0.3911	785.941
283.15	0.5137	804.21
283.15	0.6034	818.258
283.15	0.6769	830.206
283.15	0.8059	852.473
283.15	0.9111	871.773
283.15	0.9646	881.981
283.15	1.0000	888.845
288.15	0.0000	728.692
288.15	0.0549	735.346
288.15	0.0910	739.888
288.15	0.1977	753.737
288.15	0.2934	766.807
288.15	0.3911	780.617
288.15	0.5137	798.831
288.15	0.6034	812.821
288.15	0.6769	824.734
288.15	0.8059	846.936
288.15	0.9111	866.179
288.15	0.9646	876.368
288.15	1.0000	883.211
293.15	0.0000	723.509
293.15	0.0549	730.142
293.15	0.0910	734.678
293.15	0.1977	748.467
293.15	0.2934	761.481
293.15	0.3911	775.245
293.15	0.5137	793.406
293.15	0.6034	807.35
293.15	0.6769	819.228
293.15	0.8059	841.356
293.15	0.9111	860.549
293.15	0.9646	870.717
293.15	1.0000	877.539
298.15	0.0000	718.289
298.15	0.0549	724.887
298.15	0.0910	729.395
298.15	0.1977	743.114
298.15	0.2934	756.06
298.15	0.3911	769.763
298.15	0.5137	787.825
298.15	0.6034	801.699
298.15	0.6769	813.519
298.15	0.8059	835.53
298.15	0.9111	854.603
298.15	0.9646	864.749
298.15	1.0000	871.533
303.15	0.0000	713.032
303.15	0.0549	719.603
303.15	0.0910	724.11
303.15	0.1977	737.798
303.15	0.2934	750.738
303.15	0.3911	764.421
303.15	0.5137	782.446
303.15	0.6034	796.305
303.15	0.6769	808.11
303.15	0.8059	830.111
303.15	0.9111	849.196
303.15	0.9646	859.307
303.15	1.0000	866.096
308.15	0.0000	707.727
308.15	0.0549	714.28
308.15	0.0910	718.759
308.15	0.1977	732.397
308.15	0.2934	745.3
308.15	0.3911	758.935
308.15	0.5137	776.901
308.15	0.6034	790.719
308.15	0.6769	802.492
308.15	0.8059	824.422
308.15	0.9111	843.468
308.15	0.9646	853.542
308.15	1.0000	860.319
313.15	0.0000	702.378
313.15	0.0549	708.887
313.15	0.0910	713.334
313.15	0.1977	726.882
313.15	0.2934	739.693
313.15	0.3911	753.227
313.15	0.5137	771.077
313.15	0.6034	784.802
313.15	0.6769	796.487
313.15	0.8059	818.264
313.15	0.9111	837.168
313.15	0.9646	847.176
313.15	1.0000	853.902

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Propane, 1-chloro-2-methyl- (2) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0549	740.509
283.15	0.0910	745.071
283.15	0.1977	758.96
283.15	0.2934	772.077
283.15	0.3911	785.941
283.15	0.5137	804.21
283.15	0.6034	818.258
283.15	0.6769	830.206
283.15	0.8059	852.473
283.15	0.9111	871.773
283.15	0.9646	881.981
288.15	0.0549	735.346
288.15	0.0910	739.888
288.15	0.1977	753.737
288.15	0.2934	766.807
288.15	0.3911	780.617
288.15	0.5137	798.831
288.15	0.6034	812.821
288.15	0.6769	824.734
288.15	0.8059	846.936
288.15	0.9111	866.179
288.15	0.9646	876.368
293.15	0.0549	730.142
293.15	0.0910	734.678
293.15	0.1977	748.467
293.15	0.2934	761.481
293.15	0.3911	775.245
293.15	0.5137	793.406
293.15	0.6034	807.35
293.15	0.6769	819.228
293.15	0.8059	841.356
293.15	0.9111	860.549
293.15	0.9646	870.717
298.15	0.0549	724.887
298.15	0.0910	729.395
298.15	0.1977	743.114
298.15	0.2934	756.06
298.15	0.3911	769.763
298.15	0.5137	787.825
298.15	0.6034	801.699
298.15	0.6769	813.519
298.15	0.8059	835.53
298.15	0.9111	854.603
298.15	0.9646	864.749
303.15	0.0549	719.603
303.15	0.0910	724.11
303.15	0.1977	737.798
303.15	0.2934	750.738
303.15	0.3911	764.421
303.15	0.5137	782.446
303.15	0.6034	796.305
303.15	0.6769	808.11
303.15	0.8059	830.111
303.15	0.9111	849.196
303.15	0.9646	859.307
308.15	0.0549	714.28
308.15	0.0910	718.759
308.15	0.1977	732.397
308.15	0.2934	745.3
308.15	0.3911	758.935
308.15	0.5137	776.901
308.15	0.6034	790.719
308.15	0.6769	802.492
308.15	0.8059	824.422
308.15	0.9111	843.468
308.15	0.9646	853.542
313.15	0.0549	708.887
313.15	0.0910	713.334
313.15	0.1977	726.882
313.15	0.2934	739.693
313.15	0.3911	753.227
313.15	0.5137	771.077
313.15	0.6034	784.802
313.15	0.6769	796.487
313.15	0.8059	818.264
313.15	0.9111	837.168
313.15	0.9646	847.176

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Propane, 1-chloro-2-methyl- (2) - Liquid	Speed of sound, m/s - Liquid
283.15	0.0549	1069.14
283.15	0.0910	1071.67
283.15	0.1977	1079.63
283.15	0.2934	1086.95
283.15	0.3911	1094.41
283.15	0.5137	1103.67
283.15	0.6034	1110.5
283.15	0.6769	1116.19
283.15	0.8059	1126.32
283.15	0.9111	1134.68
283.15	0.9646	1138.96
288.15	0.0549	1046.83
288.15	0.0910	1049.41
288.15	0.1977	1057.45
288.15	0.2934	1064.82
288.15	0.3911	1072.34
288.15	0.5137	1081.75
288.15	0.6034	1088.69
288.15	0.6769	1094.49
288.15	0.8059	1104.87
288.15	0.9111	1113.53
288.15	0.9646	1117.89
293.15	0.0549	1024.37
293.15	0.0910	1026.98
293.15	0.1977	1035.1
293.15	0.2934	1042.64
293.15	0.3911	1050.31
293.15	0.5137	1059.87
293.15	0.6034	1066.92
293.15	0.6769	1072.79
293.15	0.8059	1083.43
293.15	0.9111	1092.23
293.15	0.9646	1096.78
298.15	0.0549	1002.07
298.15	0.0910	1004.7
298.15	0.1977	1012.95
298.15	0.2934	1020.53
298.15	0.3911	1028.23
298.15	0.5137	1037.95
298.15	0.6034	1045.15
298.15	0.6769	1051.15
298.15	0.8059	1062.03
298.15	0.9111	1071.05
298.15	0.9646	1075.61
303.15	0.0549	979.86
303.15	0.0910	982.53
303.15	0.1977	990.87
303.15	0.2934	998.49
303.15	0.3911	1006.34
303.15	0.5137	1016.23
303.15	0.6034	1023.55
303.15	0.6769	1029.65
303.15	0.8059	1040.75
303.15	0.9111	1050.02
303.15	0.9646	1054.76
308.15	0.0549	957.82
308.15	0.0910	960.52
308.15	0.1977	968.88
308.15	0.2934	976.54
308.15	0.3911	984.48
308.15	0.5137	994.58
308.15	0.6034	1002.01
308.15	0.6769	1008.22
308.15	0.8059	1019.58
308.15	0.9111	1028.98
308.15	0.9646	1033.83
313.15	0.0549	935.95
313.15	0.0910	938.67
313.15	0.1977	947.16
313.15	0.2934	954.94
313.15	0.3911	963.0
313.15	0.5137	973.17
313.15	0.6034	980.73
313.15	0.6769	987.04
313.15	0.8059	998.57
313.15	0.9111	1008.12
313.15	0.9646	1013.05

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Propane, 1-chloro-2-methyl- (2) - Liquid	Speed of sound, m/s - Liquid
283.15	0.0549	1069.14
283.15	0.0910	1071.67
283.15	0.1977	1079.63
283.15	0.2934	1086.95
283.15	0.3911	1094.41
283.15	0.5137	1103.67
283.15	0.6034	1110.5
283.15	0.6769	1116.19
283.15	0.8059	1126.32
283.15	0.9111	1134.68
283.15	0.9646	1138.96
288.15	0.0549	1046.83
288.15	0.0910	1049.41
288.15	0.1977	1057.45
288.15	0.2934	1064.82
288.15	0.3911	1072.34
288.15	0.5137	1081.75
288.15	0.6034	1088.69
288.15	0.6769	1094.49
288.15	0.8059	1104.87
288.15	0.9111	1113.53
288.15	0.9646	1117.89
293.15	0.0549	1024.37
293.15	0.0910	1026.98
293.15	0.1977	1035.1
293.15	0.2934	1042.64
293.15	0.3911	1050.31
293.15	0.5137	1059.87
293.15	0.6034	1066.92
293.15	0.6769	1072.79
293.15	0.8059	1083.43
293.15	0.9111	1092.23
293.15	0.9646	1096.78
298.15	0.0549	1002.07
298.15	0.0910	1004.7
298.15	0.1977	1012.95
298.15	0.2934	1020.53
298.15	0.3911	1028.23
298.15	0.5137	1037.95
298.15	0.6034	1045.15
298.15	0.6769	1051.15
298.15	0.8059	1062.03
298.15	0.9111	1071.05
298.15	0.9646	1075.61
303.15	0.0549	979.86
303.15	0.0910	982.53
303.15	0.1977	990.87
303.15	0.2934	998.49
303.15	0.3911	1006.34
303.15	0.5137	1016.23
303.15	0.6034	1023.55
303.15	0.6769	1029.65
303.15	0.8059	1040.75
303.15	0.9111	1050.02
303.15	0.9646	1054.76
308.15	0.0549	957.82
308.15	0.0910	960.52
308.15	0.1977	968.88
308.15	0.2934	976.54
308.15	0.3911	984.48
308.15	0.5137	994.58
308.15	0.6034	1002.01
308.15	0.6769	1008.22
308.15	0.8059	1019.58
308.15	0.9111	1028.98
308.15	0.9646	1033.83
313.15	0.0549	935.95
313.15	0.0910	938.67
313.15	0.1977	947.16
313.15	0.2934	954.94
313.15	0.3911	963.0
313.15	0.5137	973.17
313.15	0.6034	980.73
313.15	0.6769	987.04
313.15	0.8059	998.57
313.15	0.9111	1008.12
313.15	0.9646	1013.05

Sources

• Viscosities of Binary Mixtures Containing Isomeric Chlorobutanes and Diisopropylether: Experimental and Predicted Values
• Isothermal vapour-liquid equilibria and excess enthalpies for the binary mixtures containing an isomeric chlorobutane and diisopropyl ether
• Volumetric, Acoustic, and Refractive Properties of Isomeric Chlorobutanes with Diisopropyl Ether