Mixture of Diisopropyl ether + Butane, 1-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, 1-chloro- (2) [ref]

Fixed		Measured
Mole fraction of Butane, 1-chloro- (2) - Liquid	Temperature, K - Liquid	Mole fraction of Butane, 1-chloro- (2) - Gas
0.0535	308.15	0.0405
0.0542	298.15	0.0413
0.0635	288.15	0.0405
0.1210	308.15	0.0924
0.1232	298.15	0.0909
0.1276	288.15	0.0909
0.1864	288.15	0.1593
0.1985	298.15	0.1522
0.2013	308.15	0.1593
0.3048	288.15	0.2378
0.3062	308.15	0.2399
0.3069	298.15	0.2406
0.4069	308.15	0.3294
0.4115	298.15	0.3334
0.4194	288.15	0.3334
0.4984	308.15	0.4096
0.5035	298.15	0.4161
0.5078	288.15	0.4109
0.6030	308.15	0.5110
0.6071	298.15	0.5110
0.6095	288.15	0.5234
0.7175	308.15	0.6353
0.7214	298.15	0.6377
0.7259	288.15	0.6336
0.8011	298.15	0.7281
0.8011	308.15	0.7309
0.8027	288.15	0.7242
0.8982	298.15	0.8563
0.8987	308.15	0.8568
0.9039	288.15	0.8536
0.9598	288.15	0.9408
0.9603	298.15	0.9393
0.9603	308.15	0.9398

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

Fixed		Measured
Mole fraction of Butane, 1-chloro- (2) - Liquid	Temperature, K - Liquid	Mole fraction of Butane, 1-chloro- (2) - Gas
0.0535	308.15	0.0405
0.0542	298.15	0.0413
0.0635	288.15	0.0405
0.1210	308.15	0.0924
0.1232	298.15	0.0909
0.1276	288.15	0.0909
0.1864	288.15	0.1593
0.1985	298.15	0.1522
0.2013	308.15	0.1593
0.3048	288.15	0.2378
0.3062	308.15	0.2399
0.3069	298.15	0.2406
0.4069	308.15	0.3294
0.4115	298.15	0.3334
0.4194	288.15	0.3334
0.4984	308.15	0.4096
0.5035	298.15	0.4161
0.5078	288.15	0.4109
0.6030	308.15	0.5110
0.6071	298.15	0.5110
0.6095	288.15	0.5234
0.7175	308.15	0.6353
0.7214	298.15	0.6377
0.7259	288.15	0.6336
0.8011	298.15	0.7281
0.8011	308.15	0.7309
0.8027	288.15	0.7242
0.8982	298.15	0.8563
0.8987	308.15	0.8568
0.9039	288.15	0.8536
0.9598	288.15	0.9408
0.9603	298.15	0.9393
0.9603	308.15	0.9398

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 1-chloro- (2) - Liquid	Viscosity, Pa*s - Liquid
283.15	0.0000	0.0004
283.15	0.0466	0.0004
283.15	0.0991	0.0004
283.15	0.1918	0.0004
283.15	0.3234	0.0004
283.15	0.4199	0.0004
283.15	0.5160	0.0004
283.15	0.6230	0.0004
283.15	0.7154	0.0005
283.15	0.8157	0.0005
283.15	0.9098	0.0005
283.15	0.9559	0.0005
283.15	1.0000	0.0005
288.15	0.0000	0.0003
288.15	0.0466	0.0004
288.15	0.0991	0.0004
288.15	0.1918	0.0004
288.15	0.3234	0.0004
288.15	0.4199	0.0004
288.15	0.5160	0.0004
288.15	0.6230	0.0004
288.15	0.7154	0.0004
288.15	0.8157	0.0004
288.15	0.9098	0.0005
288.15	0.9559	0.0005
288.15	1.0000	0.0005
293.15	0.0000	0.0003
293.15	0.0466	0.0003
293.15	0.0991	0.0003
293.15	0.1918	0.0004
293.15	0.3234	0.0004
293.15	0.4199	0.0004
293.15	0.5160	0.0004
293.15	0.6230	0.0004
293.15	0.7154	0.0004
293.15	0.8157	0.0004
293.15	0.9098	0.0004
293.15	0.9559	0.0004
293.15	1.0000	0.0004
298.15	0.0000	0.0003
298.15	0.0466	0.0003
298.15	0.0991	0.0003
298.15	0.1918	0.0003
298.15	0.3234	0.0003
298.15	0.4199	0.0004
298.15	0.5160	0.0004
298.15	0.6230	0.0004
298.15	0.7154	0.0004
298.15	0.8157	0.0004
298.15	0.9098	0.0004
298.15	0.9559	0.0004
298.15	1.0000	0.0004
303.15	0.0000	0.0003
303.15	0.0466	0.0003
303.15	0.0991	0.0003
303.15	0.1918	0.0003
303.15	0.3234	0.0003
303.15	0.4199	0.0003
303.15	0.5160	0.0004
303.15	0.6230	0.0004
303.15	0.7154	0.0004
303.15	0.8157	0.0004
303.15	0.9098	0.0004
303.15	0.9559	0.0004
303.15	1.0000	0.0004
308.15	0.0000	0.0003
308.15	0.0466	0.0003
308.15	0.0991	0.0003
308.15	0.1918	0.0003
308.15	0.3234	0.0003
308.15	0.4199	0.0003
308.15	0.5160	0.0003
308.15	0.6230	0.0003
308.15	0.7154	0.0004
308.15	0.8157	0.0004
308.15	0.9098	0.0004
308.15	0.9559	0.0004
308.15	1.0000	0.0004
313.15	0.0000	0.0003
313.15	0.0466	0.0003
313.15	0.0991	0.0003
313.15	0.1918	0.0003
313.15	0.3234	0.0003
313.15	0.4199	0.0003
313.15	0.5160	0.0003
313.15	0.6230	0.0003
313.15	0.7154	0.0003
313.15	0.8157	0.0003
313.15	0.9098	0.0004
313.15	0.9559	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 Butane, 1-chloro- (2) - Liquid	Viscosity, Pa*s - Liquid
283.15	0.0000	0.0004
283.15	0.0466	0.0004
283.15	0.0991	0.0004
283.15	0.1918	0.0004
283.15	0.3234	0.0004
283.15	0.4199	0.0004
283.15	0.5160	0.0004
283.15	0.6230	0.0004
283.15	0.7154	0.0005
283.15	0.8157	0.0005
283.15	0.9098	0.0005
283.15	0.9559	0.0005
283.15	1.0000	0.0005
288.15	0.0000	0.0003
288.15	0.0466	0.0004
288.15	0.0991	0.0004
288.15	0.1918	0.0004
288.15	0.3234	0.0004
288.15	0.4199	0.0004
288.15	0.5160	0.0004
288.15	0.6230	0.0004
288.15	0.7154	0.0004
288.15	0.8157	0.0004
288.15	0.9098	0.0005
288.15	0.9559	0.0005
288.15	1.0000	0.0005
293.15	0.0000	0.0003
293.15	0.0466	0.0003
293.15	0.0991	0.0003
293.15	0.1918	0.0004
293.15	0.3234	0.0004
293.15	0.4199	0.0004
293.15	0.5160	0.0004
293.15	0.6230	0.0004
293.15	0.7154	0.0004
293.15	0.8157	0.0004
293.15	0.9098	0.0004
293.15	0.9559	0.0004
293.15	1.0000	0.0004
298.15	0.0000	0.0003
298.15	0.0466	0.0003
298.15	0.0991	0.0003
298.15	0.1918	0.0003
298.15	0.3234	0.0003
298.15	0.4199	0.0004
298.15	0.5160	0.0004
298.15	0.6230	0.0004
298.15	0.7154	0.0004
298.15	0.8157	0.0004
298.15	0.9098	0.0004
298.15	0.9559	0.0004
298.15	1.0000	0.0004
303.15	0.0000	0.0003
303.15	0.0466	0.0003
303.15	0.0991	0.0003
303.15	0.1918	0.0003
303.15	0.3234	0.0003
303.15	0.4199	0.0003
303.15	0.5160	0.0004
303.15	0.6230	0.0004
303.15	0.7154	0.0004
303.15	0.8157	0.0004
303.15	0.9098	0.0004
303.15	0.9559	0.0004
303.15	1.0000	0.0004
308.15	0.0000	0.0003
308.15	0.0466	0.0003
308.15	0.0991	0.0003
308.15	0.1918	0.0003
308.15	0.3234	0.0003
308.15	0.4199	0.0003
308.15	0.5160	0.0003
308.15	0.6230	0.0003
308.15	0.7154	0.0004
308.15	0.8157	0.0004
308.15	0.9098	0.0004
308.15	0.9559	0.0004
308.15	1.0000	0.0004
313.15	0.0000	0.0003
313.15	0.0466	0.0003
313.15	0.0991	0.0003
313.15	0.1918	0.0003
313.15	0.3234	0.0003
313.15	0.4199	0.0003
313.15	0.5160	0.0003
313.15	0.6230	0.0003
313.15	0.7154	0.0003
313.15	0.8157	0.0003
313.15	0.9098	0.0004
313.15	0.9559	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 Butane, 1-chloro- (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0908	-0.0286
0.1817	-0.0547
0.2726	-0.0732
0.3636	-0.0873
0.4545	-0.0954
0.5453	-0.0954
0.6363	-0.0903
0.7273	-0.0785
0.8180	-0.0587
0.9090	-0.0324

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, 1-chloro- (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0908	-0.0286
0.1817	-0.0547
0.2726	-0.0732
0.3636	-0.0873
0.4545	-0.0954
0.5453	-0.0954
0.6363	-0.0903
0.7273	-0.0785
0.8180	-0.0587
0.9090	-0.0324

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Butane, 1-chloro- (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0535	308.15	30.01
0.0542	298.15	19.68
0.0635	288.15	12.26
0.1210	308.15	29.46
0.1232	298.15	19.23
0.1276	288.15	12.06
0.1864	288.15	11.87
0.1985	298.15	18.66
0.2013	308.15	28.66
0.3048	288.15	11.38
0.3062	308.15	27.83
0.3069	298.15	18.18
0.4069	308.15	26.96
0.4115	298.15	17.57
0.4194	288.15	10.89
0.4984	308.15	26.16
0.5035	298.15	16.98
0.5078	288.15	10.55
0.6030	308.15	25.19
0.6071	298.15	16.29
0.6095	288.15	10.29
0.7175	308.15	24.19
0.7214	298.15	15.51
0.7259	288.15	9.78
0.8011	298.15	14.96
0.8011	308.15	23.23
0.8027	288.15	9.46
0.8982	298.15	14.20
0.8987	308.15	22.32
0.9039	288.15	8.85
0.9598	288.15	8.61
0.9603	298.15	13.72
0.9603	308.15	21.55

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Butane, 1-chloro- (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0535	308.15	30.01
0.0542	298.15	19.68
0.0635	288.15	12.26
0.1210	308.15	29.46
0.1232	298.15	19.23
0.1276	288.15	12.06
0.1864	288.15	11.87
0.1985	298.15	18.66
0.2013	308.15	28.66
0.3048	288.15	11.38
0.3062	308.15	27.83
0.3069	298.15	18.18
0.4069	308.15	26.96
0.4115	298.15	17.57
0.4194	288.15	10.89
0.4984	308.15	26.16
0.5035	298.15	16.98
0.5078	288.15	10.55
0.6030	308.15	25.19
0.6071	298.15	16.29
0.6095	288.15	10.29
0.7175	308.15	24.19
0.7214	298.15	15.51
0.7259	288.15	9.78
0.8011	298.15	14.96
0.8011	308.15	23.23
0.8027	288.15	9.46
0.8982	298.15	14.20
0.8987	308.15	22.32
0.9039	288.15	8.85
0.9598	288.15	8.61
0.9603	298.15	13.72
0.9603	308.15	21.55

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 1-chloro- (2) - Liquid	Refractive index (Na D-line) - Liquid
283.15	0.0466	1.3749
283.15	0.0991	1.3764
283.15	0.1918	1.3791
283.15	0.3200	1.3833
283.15	0.4199	1.3864
283.15	0.5160	1.3897
283.15	0.6230	1.3934
283.15	0.7154	1.3967
283.15	0.8157	1.4004
283.15	0.9098	1.404
283.15	0.9559	1.4057
288.15	0.0466	1.3721
288.15	0.0991	1.3736
288.15	0.1918	1.3764
288.15	0.3200	1.3806
288.15	0.4199	1.3837
288.15	0.5160	1.387
288.15	0.6230	1.3907
288.15	0.7154	1.394
288.15	0.8157	1.3977
288.15	0.9098	1.4013
288.15	0.9559	1.403
293.15	0.0466	1.3694
293.15	0.0991	1.3709
293.15	0.1918	1.3737
293.15	0.3200	1.3779
293.15	0.4199	1.381
293.15	0.5160	1.3843
293.15	0.6230	1.388
293.15	0.7154	1.3913
293.15	0.8157	1.395
293.15	0.9098	1.3986
293.15	0.9559	1.4003
298.15	0.0466	1.3666
298.15	0.0991	1.3681
298.15	0.1918	1.3709
298.15	0.3200	1.3751
298.15	0.4199	1.3783
298.15	0.5160	1.3815
298.15	0.6230	1.3853
298.15	0.7154	1.3886
298.15	0.8157	1.3923
298.15	0.9098	1.3959
298.15	0.9559	1.3977
303.15	0.0466	1.3637
303.15	0.0991	1.3652
303.15	0.1918	1.3681
303.15	0.3200	1.3723
303.15	0.4199	1.3754
303.15	0.5160	1.3787
303.15	0.6230	1.3825
303.15	0.7154	1.3858
303.15	0.8157	1.3895
303.15	0.9098	1.3932
303.15	0.9559	1.3949
308.15	0.0466	1.3609
308.15	0.0991	1.3624
308.15	0.1918	1.3652
308.15	0.3200	1.3694
308.15	0.4199	1.3726
308.15	0.5160	1.3759
308.15	0.6230	1.3797
308.15	0.7154	1.383
308.15	0.8157	1.3868
308.15	0.9098	1.3904
308.15	0.9559	1.3922
313.15	0.0466	1.358
313.15	0.0991	1.3595
313.15	0.1918	1.3624
313.15	0.3200	1.3666
313.15	0.4199	1.3698
313.15	0.5160	1.3731
313.15	0.6230	1.3769
313.15	0.7154	1.3803
313.15	0.8157	1.3841
313.15	0.9098	1.3877
313.15	0.9559	1.3895

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 1-chloro- (2) - Liquid	Refractive index (Na D-line) - Liquid
283.15	0.0466	1.3749
283.15	0.0991	1.3764
283.15	0.1918	1.3791
283.15	0.3200	1.3833
283.15	0.4199	1.3864
283.15	0.5160	1.3897
283.15	0.6230	1.3934
283.15	0.7154	1.3967
283.15	0.8157	1.4004
283.15	0.9098	1.404
283.15	0.9559	1.4057
288.15	0.0466	1.3721
288.15	0.0991	1.3736
288.15	0.1918	1.3764
288.15	0.3200	1.3806
288.15	0.4199	1.3837
288.15	0.5160	1.387
288.15	0.6230	1.3907
288.15	0.7154	1.394
288.15	0.8157	1.3977
288.15	0.9098	1.4013
288.15	0.9559	1.403
293.15	0.0466	1.3694
293.15	0.0991	1.3709
293.15	0.1918	1.3737
293.15	0.3200	1.3779
293.15	0.4199	1.381
293.15	0.5160	1.3843
293.15	0.6230	1.388
293.15	0.7154	1.3913
293.15	0.8157	1.395
293.15	0.9098	1.3986
293.15	0.9559	1.4003
298.15	0.0466	1.3666
298.15	0.0991	1.3681
298.15	0.1918	1.3709
298.15	0.3200	1.3751
298.15	0.4199	1.3783
298.15	0.5160	1.3815
298.15	0.6230	1.3853
298.15	0.7154	1.3886
298.15	0.8157	1.3923
298.15	0.9098	1.3959
298.15	0.9559	1.3977
303.15	0.0466	1.3637
303.15	0.0991	1.3652
303.15	0.1918	1.3681
303.15	0.3200	1.3723
303.15	0.4199	1.3754
303.15	0.5160	1.3787
303.15	0.6230	1.3825
303.15	0.7154	1.3858
303.15	0.8157	1.3895
303.15	0.9098	1.3932
303.15	0.9559	1.3949
308.15	0.0466	1.3609
308.15	0.0991	1.3624
308.15	0.1918	1.3652
308.15	0.3200	1.3694
308.15	0.4199	1.3726
308.15	0.5160	1.3759
308.15	0.6230	1.3797
308.15	0.7154	1.383
308.15	0.8157	1.3868
308.15	0.9098	1.3904
308.15	0.9559	1.3922
313.15	0.0466	1.358
313.15	0.0991	1.3595
313.15	0.1918	1.3624
313.15	0.3200	1.3666
313.15	0.4199	1.3698
313.15	0.5160	1.3731
313.15	0.6230	1.3769
313.15	0.7154	1.3803
313.15	0.8157	1.3841
313.15	0.9098	1.3877
313.15	0.9559	1.3895

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 1-chloro- (2) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0000	733.833
283.15	0.0466	740.095
283.15	0.0991	747.139
283.15	0.1918	759.833
283.15	0.3234	778.726
283.15	0.4199	793.339
283.15	0.5160	808.586
283.15	0.6230	826.434
283.15	0.7154	842.63
283.15	0.8157	861.003
283.15	0.9098	879.099
283.15	0.9559	888.28
283.15	1.0000	897.339
288.15	0.0000	728.692
288.15	0.0466	734.99
288.15	0.0991	741.966
288.15	0.1918	754.629
288.15	0.3234	773.471
288.15	0.4199	788.055
288.15	0.5160	803.274
288.15	0.6230	821.073
288.15	0.7154	837.246
288.15	0.8157	855.588
288.15	0.9098	873.635
288.15	0.9559	882.81
288.15	1.0000	891.855
293.15	0.0000	723.509
293.15	0.0466	729.792
293.15	0.0991	736.75
293.15	0.1918	749.383
293.15	0.3234	768.192
293.15	0.4199	782.731
293.15	0.5160	797.924
293.15	0.6230	815.68
293.15	0.7154	831.821
293.15	0.8157	850.133
293.15	0.9098	868.142
293.15	0.9559	877.303
293.15	1.0000	886.335
298.15	0.0000	718.289
298.15	0.0466	724.56
298.15	0.0991	731.492
298.15	0.1918	744.091
298.15	0.3234	762.854
298.15	0.4199	777.351
298.15	0.5160	792.506
298.15	0.6230	810.177
298.15	0.7154	826.321
298.15	0.8157	844.587
298.15	0.9098	862.556
298.15	0.9559	871.691
298.15	1.0000	880.705
303.15	0.0000	713.032
303.15	0.0466	719.283
303.15	0.0991	726.204
303.15	0.1918	738.777
303.15	0.3234	757.526
303.15	0.4199	771.984
303.15	0.5160	787.119
303.15	0.6230	804.761
303.15	0.7154	820.882
303.15	0.8157	839.124
303.15	0.9098	857.076
303.15	0.9559	866.204
303.15	1.0000	875.204
308.15	0.0000	707.727
308.15	0.0466	713.967
308.15	0.0991	720.87
308.15	0.1918	733.414
308.15	0.3234	752.126
308.15	0.4199	766.553
308.15	0.5160	781.656
308.15	0.6230	799.266
308.15	0.7154	815.358
308.15	0.8157	833.567
308.15	0.9098	851.486
308.15	0.9559	860.595
308.15	1.0000	869.585
313.15	0.0000	702.378
313.15	0.0466	708.604
313.15	0.0991	715.486
313.15	0.1918	728.002
313.15	0.3234	746.649
313.15	0.4199	761.063
313.15	0.5160	776.136
313.15	0.6230	793.704
313.15	0.7154	809.769
313.15	0.8157	827.935
313.15	0.9098	845.816
313.15	0.9559	854.913
313.15	1.0000	863.882

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 1-chloro- (2) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0466	740.095
283.15	0.0991	747.139
283.15	0.1918	759.833
283.15	0.3200	778.726
283.15	0.4199	793.339
283.15	0.5160	808.586
283.15	0.6230	826.434
283.15	0.7154	842.63
283.15	0.8157	861.003
283.15	0.9098	879.099
283.15	0.9559	888.28
288.15	0.0466	734.99
288.15	0.0991	741.966
288.15	0.1918	754.629
288.15	0.3200	773.471
288.15	0.4199	788.055
288.15	0.5160	803.274
288.15	0.6230	821.073
288.15	0.7154	837.246
288.15	0.8157	855.588
288.15	0.9098	873.635
288.15	0.9559	882.81
293.15	0.0466	729.792
293.15	0.0991	736.75
293.15	0.1918	749.383
293.15	0.3200	768.192
293.15	0.4199	782.731
293.15	0.5160	797.924
293.15	0.6230	815.68
293.15	0.7154	831.821
293.15	0.8157	850.133
293.15	0.9098	868.142
293.15	0.9559	877.303
298.15	0.0466	724.56
298.15	0.0991	731.492
298.15	0.1918	744.091
298.15	0.3200	762.854
298.15	0.4199	777.351
298.15	0.5160	792.506
298.15	0.6230	810.177
298.15	0.7154	826.321
298.15	0.8157	844.587
298.15	0.9098	862.556
298.15	0.9559	871.691
303.15	0.0466	719.283
303.15	0.0991	726.204
303.15	0.1918	738.777
303.15	0.3200	757.526
303.15	0.4199	771.984
303.15	0.5160	787.119
303.15	0.6230	804.761
303.15	0.7154	820.882
303.15	0.8157	839.124
303.15	0.9098	857.076
303.15	0.9559	866.204
308.15	0.0466	713.967
308.15	0.0991	720.87
308.15	0.1918	733.414
308.15	0.3200	752.126
308.15	0.4199	766.553
308.15	0.5160	781.656
308.15	0.6230	799.266
308.15	0.7154	815.358
308.15	0.8157	833.567
308.15	0.9098	851.486
308.15	0.9559	860.595
313.15	0.0466	708.604
313.15	0.0991	715.486
313.15	0.1918	728.002
313.15	0.3200	746.649
313.15	0.4199	761.063
313.15	0.5160	776.136
313.15	0.6230	793.704
313.15	0.7154	809.769
313.15	0.8157	827.935
313.15	0.9098	845.816
313.15	0.9559	854.913

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 1-chloro- (2) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0000	733.833
283.15	0.0466	740.095
283.15	0.0991	747.139
283.15	0.1918	759.833
283.15	0.3234	778.726
283.15	0.4199	793.339
283.15	0.5160	808.586
283.15	0.6230	826.434
283.15	0.7154	842.63
283.15	0.8157	861.003
283.15	0.9098	879.099
283.15	0.9559	888.28
283.15	1.0000	897.339
288.15	0.0000	728.692
288.15	0.0466	734.99
288.15	0.0991	741.966
288.15	0.1918	754.629
288.15	0.3234	773.471
288.15	0.4199	788.055
288.15	0.5160	803.274
288.15	0.6230	821.073
288.15	0.7154	837.246
288.15	0.8157	855.588
288.15	0.9098	873.635
288.15	0.9559	882.81
288.15	1.0000	891.855
293.15	0.0000	723.509
293.15	0.0466	729.792
293.15	0.0991	736.75
293.15	0.1918	749.383
293.15	0.3234	768.192
293.15	0.4199	782.731
293.15	0.5160	797.924
293.15	0.6230	815.68
293.15	0.7154	831.821
293.15	0.8157	850.133
293.15	0.9098	868.142
293.15	0.9559	877.303
293.15	1.0000	886.335
298.15	0.0000	718.289
298.15	0.0466	724.56
298.15	0.0991	731.492
298.15	0.1918	744.091
298.15	0.3234	762.854
298.15	0.4199	777.351
298.15	0.5160	792.506
298.15	0.6230	810.177
298.15	0.7154	826.321
298.15	0.8157	844.587
298.15	0.9098	862.556
298.15	0.9559	871.691
298.15	1.0000	880.705
303.15	0.0000	713.032
303.15	0.0466	719.283
303.15	0.0991	726.204
303.15	0.1918	738.777
303.15	0.3234	757.526
303.15	0.4199	771.984
303.15	0.5160	787.119
303.15	0.6230	804.761
303.15	0.7154	820.882
303.15	0.8157	839.124
303.15	0.9098	857.076
303.15	0.9559	866.204
303.15	1.0000	875.204
308.15	0.0000	707.727
308.15	0.0466	713.967
308.15	0.0991	720.87
308.15	0.1918	733.414
308.15	0.3234	752.126
308.15	0.4199	766.553
308.15	0.5160	781.656
308.15	0.6230	799.266
308.15	0.7154	815.358
308.15	0.8157	833.567
308.15	0.9098	851.486
308.15	0.9559	860.595
308.15	1.0000	869.585
313.15	0.0000	702.378
313.15	0.0466	708.604
313.15	0.0991	715.486
313.15	0.1918	728.002
313.15	0.3234	746.649
313.15	0.4199	761.063
313.15	0.5160	776.136
313.15	0.6230	793.704
313.15	0.7154	809.769
313.15	0.8157	827.935
313.15	0.9098	845.816
313.15	0.9559	854.913
313.15	1.0000	863.882

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 1-chloro- (2) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0466	740.095
283.15	0.0991	747.139
283.15	0.1918	759.833
283.15	0.3200	778.726
283.15	0.4199	793.339
283.15	0.5160	808.586
283.15	0.6230	826.434
283.15	0.7154	842.63
283.15	0.8157	861.003
283.15	0.9098	879.099
283.15	0.9559	888.28
288.15	0.0466	734.99
288.15	0.0991	741.966
288.15	0.1918	754.629
288.15	0.3200	773.471
288.15	0.4199	788.055
288.15	0.5160	803.274
288.15	0.6230	821.073
288.15	0.7154	837.246
288.15	0.8157	855.588
288.15	0.9098	873.635
288.15	0.9559	882.81
293.15	0.0466	729.792
293.15	0.0991	736.75
293.15	0.1918	749.383
293.15	0.3200	768.192
293.15	0.4199	782.731
293.15	0.5160	797.924
293.15	0.6230	815.68
293.15	0.7154	831.821
293.15	0.8157	850.133
293.15	0.9098	868.142
293.15	0.9559	877.303
298.15	0.0466	724.56
298.15	0.0991	731.492
298.15	0.1918	744.091
298.15	0.3200	762.854
298.15	0.4199	777.351
298.15	0.5160	792.506
298.15	0.6230	810.177
298.15	0.7154	826.321
298.15	0.8157	844.587
298.15	0.9098	862.556
298.15	0.9559	871.691
303.15	0.0466	719.283
303.15	0.0991	726.204
303.15	0.1918	738.777
303.15	0.3200	757.526
303.15	0.4199	771.984
303.15	0.5160	787.119
303.15	0.6230	804.761
303.15	0.7154	820.882
303.15	0.8157	839.124
303.15	0.9098	857.076
303.15	0.9559	866.204
308.15	0.0466	713.967
308.15	0.0991	720.87
308.15	0.1918	733.414
308.15	0.3200	752.126
308.15	0.4199	766.553
308.15	0.5160	781.656
308.15	0.6230	799.266
308.15	0.7154	815.358
308.15	0.8157	833.567
308.15	0.9098	851.486
308.15	0.9559	860.595
313.15	0.0466	708.604
313.15	0.0991	715.486
313.15	0.1918	728.002
313.15	0.3200	746.649
313.15	0.4199	761.063
313.15	0.5160	776.136
313.15	0.6230	793.704
313.15	0.7154	809.769
313.15	0.8157	827.935
313.15	0.9098	845.816
313.15	0.9559	854.913

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 1-chloro- (2) - Liquid	Speed of sound, m/s - Liquid
283.15	0.0466	1070.94
283.15	0.0991	1076.63
283.15	0.1918	1086.97
283.15	0.3200	1101.49
283.15	0.4199	1112.26
283.15	0.5160	1123.26
283.15	0.6230	1135.48
283.15	0.7154	1146.28
283.15	0.8157	1158.15
283.15	0.9098	1169.28
283.15	0.9559	1174.88
288.15	0.0466	1048.63
288.15	0.0991	1054.31
288.15	0.1918	1064.7
288.15	0.3200	1079.41
288.15	0.4199	1090.33
288.15	0.5160	1101.47
288.15	0.6230	1113.95
288.15	0.7154	1124.95
288.15	0.8157	1137.0
288.15	0.9098	1148.42
288.15	0.9559	1154.23
293.15	0.0466	1026.19
293.15	0.0991	1031.97
293.15	0.1918	1042.47
293.15	0.3200	1057.3
293.15	0.4199	1068.41
293.15	0.5160	1079.68
293.15	0.6230	1092.43
293.15	0.7154	1103.58
293.15	0.8157	1115.86
293.15	0.9098	1127.56
293.15	0.9559	1133.39
298.15	0.0466	1003.77
298.15	0.0991	1009.67
298.15	0.1918	1020.24
298.15	0.3200	1035.21
298.15	0.4199	1046.59
298.15	0.5160	1058.01
298.15	0.6230	1070.96
298.15	0.7154	1082.29
298.15	0.8157	1094.78
298.15	0.9098	1106.64
298.15	0.9559	1112.67
303.15	0.0466	981.56
303.15	0.0991	987.54
303.15	0.1918	998.37
303.15	0.3200	1013.56
303.15	0.4199	1024.85
303.15	0.5160	1036.48
303.15	0.6230	1049.62
303.15	0.7154	1061.13
303.15	0.8157	1073.77
303.15	0.9098	1085.89
303.15	0.9559	1092.02
308.15	0.0466	959.5
308.15	0.0991	965.54
308.15	0.1918	976.43
308.15	0.3200	991.71
308.15	0.4199	1003.29
308.15	0.5160	1015.04
308.15	0.6230	1028.36
308.15	0.7154	1040.06
308.15	0.8157	1052.97
308.15	0.9098	1065.28
308.15	0.9559	1071.45
313.15	0.0466	937.74
313.15	0.0991	943.72
313.15	0.1918	954.72
313.15	0.3200	970.22
313.15	0.4199	981.83
313.15	0.5160	993.77
313.15	0.6230	1007.26
313.15	0.7154	1019.07
313.15	0.8157	1032.2
313.15	0.9098	1044.76
313.15	0.9559	1051.09

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 1-chloro- (2) - Liquid	Speed of sound, m/s - Liquid
283.15	0.0466	1070.94
283.15	0.0991	1076.63
283.15	0.1918	1086.97
283.15	0.3200	1101.49
283.15	0.4199	1112.26
283.15	0.5160	1123.26
283.15	0.6230	1135.48
283.15	0.7154	1146.28
283.15	0.8157	1158.15
283.15	0.9098	1169.28
283.15	0.9559	1174.88
288.15	0.0466	1048.63
288.15	0.0991	1054.31
288.15	0.1918	1064.7
288.15	0.3200	1079.41
288.15	0.4199	1090.33
288.15	0.5160	1101.47
288.15	0.6230	1113.95
288.15	0.7154	1124.95
288.15	0.8157	1137.0
288.15	0.9098	1148.42
288.15	0.9559	1154.23
293.15	0.0466	1026.19
293.15	0.0991	1031.97
293.15	0.1918	1042.47
293.15	0.3200	1057.3
293.15	0.4199	1068.41
293.15	0.5160	1079.68
293.15	0.6230	1092.43
293.15	0.7154	1103.58
293.15	0.8157	1115.86
293.15	0.9098	1127.56
293.15	0.9559	1133.39
298.15	0.0466	1003.77
298.15	0.0991	1009.67
298.15	0.1918	1020.24
298.15	0.3200	1035.21
298.15	0.4199	1046.59
298.15	0.5160	1058.01
298.15	0.6230	1070.96
298.15	0.7154	1082.29
298.15	0.8157	1094.78
298.15	0.9098	1106.64
298.15	0.9559	1112.67
303.15	0.0466	981.56
303.15	0.0991	987.54
303.15	0.1918	998.37
303.15	0.3200	1013.56
303.15	0.4199	1024.85
303.15	0.5160	1036.48
303.15	0.6230	1049.62
303.15	0.7154	1061.13
303.15	0.8157	1073.77
303.15	0.9098	1085.89
303.15	0.9559	1092.02
308.15	0.0466	959.5
308.15	0.0991	965.54
308.15	0.1918	976.43
308.15	0.3200	991.71
308.15	0.4199	1003.29
308.15	0.5160	1015.04
308.15	0.6230	1028.36
308.15	0.7154	1040.06
308.15	0.8157	1052.97
308.15	0.9098	1065.28
308.15	0.9559	1071.45
313.15	0.0466	937.74
313.15	0.0991	943.72
313.15	0.1918	954.72
313.15	0.3200	970.22
313.15	0.4199	981.83
313.15	0.5160	993.77
313.15	0.6230	1007.26
313.15	0.7154	1019.07
313.15	0.8157	1032.2
313.15	0.9098	1044.76
313.15	0.9559	1051.09

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