Mixture of Diisopropyl ether + Butane, 2-chloro-

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 Butane, 2-chloro- (2) [ref]

Fixed		Measured
Mole fraction of Butane, 2-chloro- (2) - Liquid	Temperature, K - Liquid	Mole fraction of Butane, 2-chloro- (2) - Gas
0.0631	288.15	0.0700
0.0631	298.15	0.0699
0.0631	308.15	0.0709
0.1353	288.15	0.1466
0.1361	308.15	0.1464
0.1365	298.15	0.1474
0.2132	288.15	0.2279
0.2141	308.15	0.2264
0.2147	298.15	0.2279
0.2898	288.15	0.3086
0.2905	308.15	0.3017
0.2941	298.15	0.3086
0.3788	288.15	0.3933
0.3805	298.15	0.3933
0.3806	308.15	0.3806
0.4677	288.15	0.4803
0.4695	308.15	0.4778
0.4703	298.15	0.4807
0.5584	288.15	0.5686
0.5586	308.15	0.5648
0.5587	298.15	0.5661
0.6460	288.15	0.6532
0.6461	308.15	0.6497
0.6468	298.15	0.6515
0.7270	288.15	0.7317
0.7278	308.15	0.7286
0.7280	298.15	0.7308
0.8155	288.15	0.8179
0.8157	308.15	0.8150
0.8164	298.15	0.8180
0.8691	288.15	0.8707
0.8694	308.15	0.8685
0.8699	298.15	0.8707
0.9741	288.15	0.9742
0.9744	298.15	0.9741
0.9744	308.15	0.9739

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

Fixed		Measured
Mole fraction of Butane, 2-chloro- (2) - Liquid	Temperature, K - Liquid	Mole fraction of Butane, 2-chloro- (2) - Gas
0.0631	288.15	0.0700
0.0631	298.15	0.0699
0.0631	308.15	0.0709
0.1353	288.15	0.1466
0.1361	308.15	0.1464
0.1365	298.15	0.1474
0.2132	288.15	0.2279
0.2141	308.15	0.2264
0.2147	298.15	0.2279
0.2898	288.15	0.3086
0.2905	308.15	0.3017
0.2941	298.15	0.3086
0.3788	288.15	0.3933
0.3805	298.15	0.3933
0.3806	308.15	0.3806
0.4677	288.15	0.4803
0.4695	308.15	0.4778
0.4703	298.15	0.4807
0.5584	288.15	0.5686
0.5586	308.15	0.5648
0.5587	298.15	0.5661
0.6460	288.15	0.6532
0.6461	308.15	0.6497
0.6468	298.15	0.6515
0.7270	288.15	0.7317
0.7278	308.15	0.7286
0.7280	298.15	0.7308
0.8155	288.15	0.8179
0.8157	308.15	0.8150
0.8164	298.15	0.8180
0.8691	288.15	0.8707
0.8694	308.15	0.8685
0.8699	298.15	0.8707
0.9741	288.15	0.9742
0.9744	298.15	0.9741
0.9744	308.15	0.9739

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 2-chloro- (2) - Liquid	Viscosity, Pa*s - Liquid
283.15	0.0000	0.0004
283.15	0.0519	0.0004
283.15	0.0988	0.0004
283.15	0.2006	0.0004
283.15	0.3211	0.0004
283.15	0.4201	0.0004
283.15	0.5320	0.0004
283.15	0.6244	0.0004
283.15	0.7260	0.0004
283.15	0.8163	0.0004
283.15	0.8817	0.0004
283.15	0.9634	0.0005
283.15	1.0000	0.0005
288.15	0.0000	0.0003
288.15	0.0519	0.0004
288.15	0.0988	0.0004
288.15	0.2006	0.0004
288.15	0.3211	0.0004
288.15	0.4201	0.0004
288.15	0.5320	0.0004
288.15	0.6244	0.0004
288.15	0.7260	0.0004
288.15	0.8163	0.0004
288.15	0.8817	0.0004
288.15	0.9634	0.0004
288.15	1.0000	0.0004
293.15	0.0000	0.0003
293.15	0.0519	0.0003
293.15	0.0988	0.0003
293.15	0.2006	0.0003
293.15	0.3211	0.0004
293.15	0.4201	0.0004
293.15	0.5320	0.0004
293.15	0.6244	0.0004
293.15	0.7260	0.0004
293.15	0.8163	0.0004
293.15	0.8817	0.0004
293.15	0.9634	0.0004
293.15	1.0000	0.0004
298.15	0.0000	0.0003
298.15	0.0519	0.0003
298.15	0.0988	0.0003
298.15	0.2006	0.0003
298.15	0.3211	0.0003
298.15	0.4201	0.0003
298.15	0.5320	0.0004
298.15	0.6244	0.0004
298.15	0.7260	0.0004
298.15	0.8163	0.0004
298.15	0.8817	0.0004
298.15	0.9634	0.0004
298.15	1.0000	0.0004
303.15	0.0000	0.0003
303.15	0.0519	0.0003
303.15	0.0988	0.0003
303.15	0.2006	0.0003
303.15	0.3211	0.0003
303.15	0.4201	0.0003
303.15	0.5320	0.0003
303.15	0.6244	0.0003
303.15	0.7260	0.0004
303.15	0.8163	0.0004
303.15	0.8817	0.0004
303.15	0.9634	0.0004
303.15	1.0000	0.0004
308.15	0.0000	0.0003
308.15	0.0519	0.0003
308.15	0.0988	0.0003
308.15	0.2006	0.0003
308.15	0.3211	0.0003
308.15	0.4201	0.0003
308.15	0.5320	0.0003
308.15	0.6244	0.0003
308.15	0.7260	0.0003
308.15	0.8163	0.0003
308.15	0.8817	0.0004
308.15	0.9634	0.0004
308.15	1.0000	0.0004
313.15	0.0000	0.0003
313.15	0.0519	0.0003
313.15	0.0988	0.0003
313.15	0.2006	0.0003
313.15	0.3211	0.0003
313.15	0.4201	0.0003
313.15	0.5320	0.0003
313.15	0.6244	0.0003
313.15	0.7260	0.0003
313.15	0.8163	0.0003
313.15	0.8817	0.0003
313.15	0.9634	0.0003
313.15	1.0000	0.0003

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 2-chloro- (2) - Liquid	Viscosity, Pa*s - Liquid
283.15	0.0000	0.0004
283.15	0.0519	0.0004
283.15	0.0988	0.0004
283.15	0.2006	0.0004
283.15	0.3211	0.0004
283.15	0.4201	0.0004
283.15	0.5320	0.0004
283.15	0.6244	0.0004
283.15	0.7260	0.0004
283.15	0.8163	0.0004
283.15	0.8817	0.0004
283.15	0.9634	0.0005
283.15	1.0000	0.0005
288.15	0.0000	0.0003
288.15	0.0519	0.0004
288.15	0.0988	0.0004
288.15	0.2006	0.0004
288.15	0.3211	0.0004
288.15	0.4201	0.0004
288.15	0.5320	0.0004
288.15	0.6244	0.0004
288.15	0.7260	0.0004
288.15	0.8163	0.0004
288.15	0.8817	0.0004
288.15	0.9634	0.0004
288.15	1.0000	0.0004
293.15	0.0000	0.0003
293.15	0.0519	0.0003
293.15	0.0988	0.0003
293.15	0.2006	0.0003
293.15	0.3211	0.0004
293.15	0.4201	0.0004
293.15	0.5320	0.0004
293.15	0.6244	0.0004
293.15	0.7260	0.0004
293.15	0.8163	0.0004
293.15	0.8817	0.0004
293.15	0.9634	0.0004
293.15	1.0000	0.0004
298.15	0.0000	0.0003
298.15	0.0519	0.0003
298.15	0.0988	0.0003
298.15	0.2006	0.0003
298.15	0.3211	0.0003
298.15	0.4201	0.0003
298.15	0.5320	0.0004
298.15	0.6244	0.0004
298.15	0.7260	0.0004
298.15	0.8163	0.0004
298.15	0.8817	0.0004
298.15	0.9634	0.0004
298.15	1.0000	0.0004
303.15	0.0000	0.0003
303.15	0.0519	0.0003
303.15	0.0988	0.0003
303.15	0.2006	0.0003
303.15	0.3211	0.0003
303.15	0.4201	0.0003
303.15	0.5320	0.0003
303.15	0.6244	0.0003
303.15	0.7260	0.0004
303.15	0.8163	0.0004
303.15	0.8817	0.0004
303.15	0.9634	0.0004
303.15	1.0000	0.0004
308.15	0.0000	0.0003
308.15	0.0519	0.0003
308.15	0.0988	0.0003
308.15	0.2006	0.0003
308.15	0.3211	0.0003
308.15	0.4201	0.0003
308.15	0.5320	0.0003
308.15	0.6244	0.0003
308.15	0.7260	0.0003
308.15	0.8163	0.0003
308.15	0.8817	0.0004
308.15	0.9634	0.0004
308.15	1.0000	0.0004
313.15	0.0000	0.0003
313.15	0.0519	0.0003
313.15	0.0988	0.0003
313.15	0.2006	0.0003
313.15	0.3211	0.0003
313.15	0.4201	0.0003
313.15	0.5320	0.0003
313.15	0.6244	0.0003
313.15	0.7260	0.0003
313.15	0.8163	0.0003
313.15	0.8817	0.0003
313.15	0.9634	0.0003
313.15	1.0000	0.0003

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

Operational conditions:

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

Mole fraction of Butane, 2-chloro- (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0909	-0.0154
0.1819	-0.0300
0.2726	-0.0434
0.3636	-0.0523
0.4546	-0.0575
0.5454	-0.0601
0.6365	-0.0599
0.7273	-0.0530
0.8182	-0.0412
0.9092	-0.0251

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

Operational conditions:

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

Mole fraction of Butane, 2-chloro- (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0909	-0.0154
0.1819	-0.0300
0.2726	-0.0434
0.3636	-0.0523
0.4546	-0.0575
0.5454	-0.0601
0.6365	-0.0599
0.7273	-0.0530
0.8182	-0.0412
0.9092	-0.0251

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Butane, 2-chloro- (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0631	288.15	12.70
0.0631	298.15	20.09
0.0631	308.15	30.59
0.1353	288.15	12.79
0.1361	308.15	30.75
0.1365	298.15	20.26
0.2132	288.15	12.88
0.2141	308.15	31.05
0.2147	298.15	20.38
0.2898	288.15	12.96
0.2905	308.15	31.18
0.2941	298.15	20.52
0.3788	288.15	13.04
0.3805	298.15	20.62
0.3806	308.15	31.30
0.4677	288.15	13.10
0.4695	308.15	31.39
0.4703	298.15	20.70
0.5584	288.15	13.18
0.5586	308.15	31.48
0.5587	298.15	20.76
0.6460	288.15	13.22
0.6461	308.15	31.50
0.6468	298.15	20.82
0.7270	288.15	13.28
0.7278	308.15	31.52
0.7280	298.15	20.83
0.8155	288.15	13.32
0.8157	308.15	31.54
0.8164	298.15	20.86
0.8691	288.15	13.33
0.8694	308.15	31.55
0.8699	298.15	20.89
0.9741	288.15	13.35
0.9744	298.15	20.89
0.9744	308.15	31.52

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Butane, 2-chloro- (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0631	288.15	12.70
0.0631	298.15	20.09
0.0631	308.15	30.59
0.1353	288.15	12.79
0.1361	308.15	30.75
0.1365	298.15	20.26
0.2132	288.15	12.88
0.2141	308.15	31.05
0.2147	298.15	20.38
0.2898	288.15	12.96
0.2905	308.15	31.18
0.2941	298.15	20.52
0.3788	288.15	13.04
0.3805	298.15	20.62
0.3806	308.15	31.30
0.4677	288.15	13.10
0.4695	308.15	31.39
0.4703	298.15	20.70
0.5584	288.15	13.18
0.5586	308.15	31.48
0.5587	298.15	20.76
0.6460	288.15	13.22
0.6461	308.15	31.50
0.6468	298.15	20.82
0.7270	288.15	13.28
0.7278	308.15	31.52
0.7280	298.15	20.83
0.8155	288.15	13.32
0.8157	308.15	31.54
0.8164	298.15	20.86
0.8691	288.15	13.33
0.8694	308.15	31.55
0.8699	298.15	20.89
0.9741	288.15	13.35
0.9744	298.15	20.89
0.9744	308.15	31.52

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 2-chloro- (2) - Liquid	Refractive index (Na D-line) - Liquid
283.15	0.0519	1.3748
283.15	0.0988	1.3759
283.15	0.2006	1.3784
283.15	0.3211	1.3816
283.15	0.4201	1.3843
283.15	0.5320	1.3874
283.15	0.6244	1.3902
283.15	0.7260	1.3932
283.15	0.8163	1.3961
283.15	0.8817	1.3982
283.15	0.9634	1.401
288.15	0.0519	1.372
288.15	0.0988	1.3731
288.15	0.2006	1.3757
288.15	0.3211	1.3788
288.15	0.4201	1.3815
288.15	0.5320	1.3847
288.15	0.6244	1.3874
288.15	0.7260	1.3905
288.15	0.8163	1.3934
288.15	0.8817	1.3955
288.15	0.9634	1.3983
293.15	0.0519	1.3693
293.15	0.0988	1.3704
293.15	0.2006	1.3729
293.15	0.3211	1.3761
293.15	0.4201	1.3788
293.15	0.5320	1.382
293.15	0.6244	1.3847
293.15	0.7260	1.3878
293.15	0.8163	1.3906
293.15	0.8817	1.3927
293.15	0.9634	1.3955
298.15	0.0519	1.3664
298.15	0.0988	1.3676
298.15	0.2006	1.3701
298.15	0.3211	1.3733
298.15	0.4201	1.376
298.15	0.5320	1.3792
298.15	0.6244	1.3819
298.15	0.7260	1.385
298.15	0.8163	1.3878
298.15	0.8817	1.39
298.15	0.9634	1.3928
303.15	0.0519	1.3636
303.15	0.0988	1.3647
303.15	0.2006	1.3673
303.15	0.3211	1.3704
303.15	0.4201	1.3732
303.15	0.5320	1.3764
303.15	0.6244	1.3791
303.15	0.7260	1.3822
303.15	0.8163	1.3851
303.15	0.8817	1.3872
303.15	0.9634	1.39
308.15	0.0519	1.3608
308.15	0.0988	1.3619
308.15	0.2006	1.3644
308.15	0.3211	1.3676
308.15	0.4201	1.3703
308.15	0.5320	1.3735
308.15	0.6244	1.3763
308.15	0.7260	1.3794
308.15	0.8163	1.3822
308.15	0.8817	1.3844
308.15	0.9634	1.3872
313.15	0.0519	1.3579
313.15	0.0988	1.359
313.15	0.2006	1.3616
313.15	0.3211	1.3647
313.15	0.4201	1.3675
313.15	0.5320	1.3707
313.15	0.6244	1.3734
313.15	0.7260	1.3765
313.15	0.8163	1.3794
313.15	0.8817	1.3815
313.15	0.9634	1.3843

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 2-chloro- (2) - Liquid	Refractive index (Na D-line) - Liquid
283.15	0.0519	1.3748
283.15	0.0988	1.3759
283.15	0.2006	1.3784
283.15	0.3211	1.3816
283.15	0.4201	1.3843
283.15	0.5320	1.3874
283.15	0.6244	1.3902
283.15	0.7260	1.3932
283.15	0.8163	1.3961
283.15	0.8817	1.3982
283.15	0.9634	1.401
288.15	0.0519	1.372
288.15	0.0988	1.3731
288.15	0.2006	1.3757
288.15	0.3211	1.3788
288.15	0.4201	1.3815
288.15	0.5320	1.3847
288.15	0.6244	1.3874
288.15	0.7260	1.3905
288.15	0.8163	1.3934
288.15	0.8817	1.3955
288.15	0.9634	1.3983
293.15	0.0519	1.3693
293.15	0.0988	1.3704
293.15	0.2006	1.3729
293.15	0.3211	1.3761
293.15	0.4201	1.3788
293.15	0.5320	1.382
293.15	0.6244	1.3847
293.15	0.7260	1.3878
293.15	0.8163	1.3906
293.15	0.8817	1.3927
293.15	0.9634	1.3955
298.15	0.0519	1.3664
298.15	0.0988	1.3676
298.15	0.2006	1.3701
298.15	0.3211	1.3733
298.15	0.4201	1.376
298.15	0.5320	1.3792
298.15	0.6244	1.3819
298.15	0.7260	1.385
298.15	0.8163	1.3878
298.15	0.8817	1.39
298.15	0.9634	1.3928
303.15	0.0519	1.3636
303.15	0.0988	1.3647
303.15	0.2006	1.3673
303.15	0.3211	1.3704
303.15	0.4201	1.3732
303.15	0.5320	1.3764
303.15	0.6244	1.3791
303.15	0.7260	1.3822
303.15	0.8163	1.3851
303.15	0.8817	1.3872
303.15	0.9634	1.39
308.15	0.0519	1.3608
308.15	0.0988	1.3619
308.15	0.2006	1.3644
308.15	0.3211	1.3676
308.15	0.4201	1.3703
308.15	0.5320	1.3735
308.15	0.6244	1.3763
308.15	0.7260	1.3794
308.15	0.8163	1.3822
308.15	0.8817	1.3844
308.15	0.9634	1.3872
313.15	0.0519	1.3579
313.15	0.0988	1.359
313.15	0.2006	1.3616
313.15	0.3211	1.3647
313.15	0.4201	1.3675
313.15	0.5320	1.3707
313.15	0.6244	1.3734
313.15	0.7260	1.3765
313.15	0.8163	1.3794
313.15	0.8817	1.3815
313.15	0.9634	1.3843

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 2-chloro- (2) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0000	733.833
283.15	0.0519	740.159
283.15	0.0988	745.897
283.15	0.2006	758.792
283.15	0.3211	774.756
283.15	0.4201	788.575
283.15	0.5320	804.971
283.15	0.6244	819.223
283.15	0.7260	835.602
283.15	0.8163	850.907
283.15	0.8817	862.411
283.15	0.9634	877.39
283.15	1.0000	884.34
288.15	0.0000	728.692
288.15	0.0519	734.981
288.15	0.0988	740.712
288.15	0.2006	753.569
288.15	0.3211	769.483
288.15	0.4201	783.251
288.15	0.5320	799.602
288.15	0.6244	813.814
288.15	0.7260	830.144
288.15	0.8163	845.414
288.15	0.8817	856.901
288.15	0.9634	871.819
288.15	1.0000	878.756
293.15	0.0000	723.509
293.15	0.0519	729.792
293.15	0.0988	735.485
293.15	0.2006	748.303
293.15	0.3211	764.161
293.15	0.4201	777.889
293.15	0.6244	808.369
293.15	0.7260	824.657
293.15	0.8163	839.877
293.15	0.8817	851.332
293.15	0.9634	866.214
293.15	1.0000	873.13
298.15	0.0000	718.289
298.15	0.0519	724.535
298.15	0.0988	730.22
298.15	0.2006	742.995
298.15	0.3211	758.802
298.15	0.4201	772.485
298.15	0.5320	788.75
298.15	0.6244	802.882
298.15	0.7260	819.123
298.15	0.8163	834.307
298.15	0.8817	845.724
298.15	0.9634	860.57
298.15	1.0000	867.474
303.15	0.0000	713.032
303.15	0.0519	719.276
303.15	0.0988	724.919
303.15	0.2006	737.649
303.15	0.3211	753.411
303.15	0.4201	767.06
303.15	0.5320	783.263
303.15	0.6244	797.355
303.15	0.7260	813.555
303.15	0.8163	828.698
303.15	0.8817	840.084
303.15	0.9634	854.895
303.15	1.0000	861.779
308.15	0.0000	707.727
308.15	0.0519	713.939
308.15	0.0988	719.569
308.15	0.2006	732.261
308.15	0.3211	747.973
308.15	0.4201	761.571
308.15	0.5320	777.737
308.15	0.6244	791.784
308.15	0.7260	807.944
308.15	0.8163	823.046
308.15	0.8817	834.402
308.15	0.9634	849.179
308.15	1.0000	856.044
313.15	0.0000	702.378
313.15	0.0519	708.573
313.15	0.0988	714.181
313.15	0.2006	726.833
313.15	0.3211	742.484
313.15	0.4201	756.049
313.15	0.5320	772.166
313.15	0.6244	786.18
313.15	0.7260	802.287
313.15	0.8163	817.349
313.15	0.8817	828.683
313.15	0.9634	843.42
313.15	1.0000	850.266

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 2-chloro- (2) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0519	740.159
283.15	0.0988	745.897
283.15	0.2006	758.792
283.15	0.3211	774.756
283.15	0.4201	788.575
283.15	0.5320	804.971
283.15	0.6244	819.223
283.15	0.7260	835.602
283.15	0.8163	850.907
283.15	0.8817	862.411
283.15	0.9634	877.39
288.15	0.0519	734.981
288.15	0.0988	740.712
288.15	0.2006	753.569
288.15	0.3211	769.483
288.15	0.4201	783.251
288.15	0.5320	799.602
288.15	0.6244	813.814
288.15	0.7260	830.144
288.15	0.8163	845.414
288.15	0.8817	856.901
288.15	0.9634	871.819
293.15	0.0519	729.792
293.15	0.0988	735.485
293.15	0.2006	748.303
293.15	0.3211	764.161
293.15	0.4201	777.889
293.15	0.5320	794.197
293.15	0.6244	808.369
293.15	0.7260	824.657
293.15	0.8163	839.877
293.15	0.8817	851.332
293.15	0.9634	866.214
298.15	0.0519	724.535
298.15	0.0988	730.22
298.15	0.2006	742.995
298.15	0.3211	758.802
298.15	0.4201	772.485
298.15	0.5320	788.75
298.15	0.6244	802.882
298.15	0.7260	819.123
298.15	0.8163	834.307
298.15	0.8817	845.724
298.15	0.9634	860.57
303.15	0.0519	719.276
303.15	0.0988	724.919
303.15	0.2006	737.649
303.15	0.3211	753.411
303.15	0.4201	767.06
303.15	0.5320	783.263
303.15	0.6244	797.355
303.15	0.7260	813.555
303.15	0.8163	828.698
303.15	0.8817	840.084
303.15	0.9634	854.895
308.15	0.0519	713.939
308.15	0.0988	719.569
308.15	0.2006	732.261
308.15	0.3211	747.973
308.15	0.4201	761.571
308.15	0.5320	777.737
308.15	0.6244	791.784
308.15	0.7260	807.944
308.15	0.8163	823.046
308.15	0.8817	834.402
308.15	0.9634	849.179
313.15	0.0519	708.573
313.15	0.0988	714.181
313.15	0.2006	726.833
313.15	0.3211	742.484
313.15	0.4201	756.049
313.15	0.5320	772.166
313.15	0.6244	786.18
313.15	0.7260	802.287
313.15	0.8163	817.349
313.15	0.8817	828.683
313.15	0.9634	843.442

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 2-chloro- (2) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0000	733.833
283.15	0.0519	740.159
283.15	0.0988	745.897
283.15	0.2006	758.792
283.15	0.3211	774.756
283.15	0.4201	788.575
283.15	0.5320	804.971
283.15	0.6244	819.223
283.15	0.7260	835.602
283.15	0.8163	850.907
283.15	0.8817	862.411
283.15	0.9634	877.39
283.15	1.0000	884.34
288.15	0.0000	728.692
288.15	0.0519	734.981
288.15	0.0988	740.712
288.15	0.2006	753.569
288.15	0.3211	769.483
288.15	0.4201	783.251
288.15	0.5320	799.602
288.15	0.6244	813.814
288.15	0.7260	830.144
288.15	0.8163	845.414
288.15	0.8817	856.901
288.15	0.9634	871.819
288.15	1.0000	878.756
293.15	0.0000	723.509
293.15	0.0519	729.792
293.15	0.0988	735.485
293.15	0.2006	748.303
293.15	0.3211	764.161
293.15	0.4201	777.889
293.15	0.6244	808.369
293.15	0.7260	824.657
293.15	0.8163	839.877
293.15	0.8817	851.332
293.15	0.9634	866.214
293.15	1.0000	873.13
298.15	0.0000	718.289
298.15	0.0519	724.535
298.15	0.0988	730.22
298.15	0.2006	742.995
298.15	0.3211	758.802
298.15	0.4201	772.485
298.15	0.5320	788.75
298.15	0.6244	802.882
298.15	0.7260	819.123
298.15	0.8163	834.307
298.15	0.8817	845.724
298.15	0.9634	860.57
298.15	1.0000	867.474
303.15	0.0000	713.032
303.15	0.0519	719.276
303.15	0.0988	724.919
303.15	0.2006	737.649
303.15	0.3211	753.411
303.15	0.4201	767.06
303.15	0.5320	783.263
303.15	0.6244	797.355
303.15	0.7260	813.555
303.15	0.8163	828.698
303.15	0.8817	840.084
303.15	0.9634	854.895
303.15	1.0000	861.779
308.15	0.0000	707.727
308.15	0.0519	713.939
308.15	0.0988	719.569
308.15	0.2006	732.261
308.15	0.3211	747.973
308.15	0.4201	761.571
308.15	0.5320	777.737
308.15	0.6244	791.784
308.15	0.7260	807.944
308.15	0.8163	823.046
308.15	0.8817	834.402
308.15	0.9634	849.179
308.15	1.0000	856.044
313.15	0.0000	702.378
313.15	0.0519	708.573
313.15	0.0988	714.181
313.15	0.2006	726.833
313.15	0.3211	742.484
313.15	0.4201	756.049
313.15	0.5320	772.166
313.15	0.6244	786.18
313.15	0.7260	802.287
313.15	0.8163	817.349
313.15	0.8817	828.683
313.15	0.9634	843.42
313.15	1.0000	850.266

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 2-chloro- (2) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0519	740.159
283.15	0.0988	745.897
283.15	0.2006	758.792
283.15	0.3211	774.756
283.15	0.4201	788.575
283.15	0.5320	804.971
283.15	0.6244	819.223
283.15	0.7260	835.602
283.15	0.8163	850.907
283.15	0.8817	862.411
283.15	0.9634	877.39
288.15	0.0519	734.981
288.15	0.0988	740.712
288.15	0.2006	753.569
288.15	0.3211	769.483
288.15	0.4201	783.251
288.15	0.5320	799.602
288.15	0.6244	813.814
288.15	0.7260	830.144
288.15	0.8163	845.414
288.15	0.8817	856.901
288.15	0.9634	871.819
293.15	0.0519	729.792
293.15	0.0988	735.485
293.15	0.2006	748.303
293.15	0.3211	764.161
293.15	0.4201	777.889
293.15	0.5320	794.197
293.15	0.6244	808.369
293.15	0.7260	824.657
293.15	0.8163	839.877
293.15	0.8817	851.332
293.15	0.9634	866.214
298.15	0.0519	724.535
298.15	0.0988	730.22
298.15	0.2006	742.995
298.15	0.3211	758.802
298.15	0.4201	772.485
298.15	0.5320	788.75
298.15	0.6244	802.882
298.15	0.7260	819.123
298.15	0.8163	834.307
298.15	0.8817	845.724
298.15	0.9634	860.57
303.15	0.0519	719.276
303.15	0.0988	724.919
303.15	0.2006	737.649
303.15	0.3211	753.411
303.15	0.4201	767.06
303.15	0.5320	783.263
303.15	0.6244	797.355
303.15	0.7260	813.555
303.15	0.8163	828.698
303.15	0.8817	840.084
303.15	0.9634	854.895
308.15	0.0519	713.939
308.15	0.0988	719.569
308.15	0.2006	732.261
308.15	0.3211	747.973
308.15	0.4201	761.571
308.15	0.5320	777.737
308.15	0.6244	791.784
308.15	0.7260	807.944
308.15	0.8163	823.046
308.15	0.8817	834.402
308.15	0.9634	849.179
313.15	0.0519	708.573
313.15	0.0988	714.181
313.15	0.2006	726.833
313.15	0.3211	742.484
313.15	0.4201	756.049
313.15	0.5320	772.166
313.15	0.6244	786.18
313.15	0.7260	802.287
313.15	0.8163	817.349
313.15	0.8817	828.683
313.15	0.9634	843.442

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 2-chloro- (2) - Liquid	Speed of sound, m/s - Liquid
283.15	0.0519	1068.8
283.15	0.0988	1071.68
283.15	0.2006	1077.96
283.15	0.3211	1085.36
283.15	0.4201	1091.48
283.15	0.5320	1098.51
283.15	0.6244	1104.33
283.15	0.7260	1110.74
283.15	0.8163	1116.35
283.15	0.8817	1120.43
283.15	0.9634	1125.49
288.15	0.0519	1046.49
288.15	0.0988	1049.43
288.15	0.2006	1055.82
288.15	0.3211	1063.39
288.15	0.4201	1069.66
288.15	0.5320	1076.88
288.15	0.6244	1082.89
288.15	0.7260	1089.55
288.15	0.8163	1095.36
288.15	0.8817	1099.58
288.15	0.9634	1104.89
293.15	0.0519	1024.05
293.15	0.0988	1027.08
293.15	0.2006	1033.66
293.15	0.3211	1041.42
293.15	0.4201	1047.87
293.15	0.5320	1055.32
293.15	0.6244	1061.53
293.15	0.7260	1068.3
293.15	0.8163	1074.39
293.15	0.8817	1078.74
293.15	0.9634	1084.29
298.15	0.0519	1001.8
298.15	0.0988	1004.88
298.15	0.2006	1011.53
298.15	0.3211	1019.42
298.15	0.4201	1026.06
298.15	0.5320	1033.77
298.15	0.6244	1040.17
298.15	0.7260	1047.2
298.15	0.8163	1053.45
298.15	0.8817	1057.92
298.15	0.9634	1063.65
303.15	0.0519	979.57
303.15	0.0988	982.73
303.15	0.2006	989.5
303.15	0.3211	997.66
303.15	0.4201	1004.4
303.15	0.5320	1012.26
303.15	0.6244	1018.82
303.15	0.7260	1026.06
303.15	0.8163	1032.57
303.15	0.8817	1037.21
303.15	0.9634	1043.19
308.15	0.0519	957.51
308.15	0.0988	960.7
308.15	0.2006	967.56
308.15	0.3211	975.92
308.15	0.4201	982.81
308.15	0.5320	990.84
308.15	0.6244	997.54
308.15	0.7260	1004.99
308.15	0.8163	1011.61
308.15	0.8817	1016.4
308.15	0.9634	1022.56
313.15	0.0519	935.64
313.15	0.0988	938.87
313.15	0.2006	945.88
313.15	0.3211	954.34
313.15	0.4201	961.42
313.15	0.5320	969.67
313.15	0.6244	976.57
313.15	0.7260	984.26
313.15	0.8163	991.15
313.15	0.8817	996.09
313.15	0.9634	1002.46

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 2-chloro- (2) - Liquid	Speed of sound, m/s - Liquid
283.15	0.0519	1068.8
283.15	0.0988	1071.68
283.15	0.2006	1077.96
283.15	0.3211	1085.36
283.15	0.4201	1091.48
283.15	0.5320	1098.51
283.15	0.6244	1104.33
283.15	0.7260	1110.74
283.15	0.8163	1116.35
283.15	0.8817	1120.43
283.15	0.9634	1125.49
288.15	0.0519	1046.49
288.15	0.0988	1049.43
288.15	0.2006	1055.82
288.15	0.3211	1063.39
288.15	0.4201	1069.66
288.15	0.5320	1076.88
288.15	0.6244	1082.89
288.15	0.7260	1089.55
288.15	0.8163	1095.36
288.15	0.8817	1099.58
288.15	0.9634	1104.89
293.15	0.0519	1024.05
293.15	0.0988	1027.08
293.15	0.2006	1033.66
293.15	0.3211	1041.42
293.15	0.4201	1047.87
293.15	0.5320	1055.32
293.15	0.6244	1061.53
293.15	0.7260	1068.3
293.15	0.8163	1074.39
293.15	0.8817	1078.74
293.15	0.9634	1084.29
298.15	0.0519	1001.8
298.15	0.0988	1004.88
298.15	0.2006	1011.53
298.15	0.3211	1019.42
298.15	0.4201	1026.06
298.15	0.5320	1033.77
298.15	0.6244	1040.17
298.15	0.7260	1047.2
298.15	0.8163	1053.45
298.15	0.8817	1057.92
298.15	0.9634	1063.65
303.15	0.0519	979.57
303.15	0.0988	982.73
303.15	0.2006	989.5
303.15	0.3211	997.66
303.15	0.4201	1004.4
303.15	0.5320	1012.26
303.15	0.6244	1018.82
303.15	0.7260	1026.06
303.15	0.8163	1032.57
303.15	0.8817	1037.21
303.15	0.9634	1043.19
308.15	0.0519	957.51
308.15	0.0988	960.7
308.15	0.2006	967.56
308.15	0.3211	975.92
308.15	0.4201	982.81
308.15	0.5320	990.84
308.15	0.6244	997.54
308.15	0.7260	1004.99
308.15	0.8163	1011.61
308.15	0.8817	1016.4
308.15	0.9634	1022.56
313.15	0.0519	935.64
313.15	0.0988	938.87
313.15	0.2006	945.88
313.15	0.3211	954.34
313.15	0.4201	961.42
313.15	0.5320	969.67
313.15	0.6244	976.57
313.15	0.7260	984.26
313.15	0.8163	991.15
313.15	0.8817	996.09
313.15	0.9634	1002.46

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