Mixture of Diisopropyl ether + Propane, 2-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, 2-chloro-2-methyl- (2) [ref]

Fixed		Measured
Mole fraction of Propane, 2-chloro-2-methyl- (2) - Liquid	Temperature, K - Liquid	Mole fraction of Propane, 2-chloro-2-methyl- (2) - Gas
0.0369	298.15	0.0797
0.0379	288.15	0.0827
0.0379	308.15	0.0777
0.1126	288.15	0.2213
0.1136	298.15	0.2100
0.1224	308.15	0.2166
0.1844	288.15	0.3144
0.1949	308.15	0.3289
0.1987	298.15	0.3244
0.2926	288.15	0.4482
0.3126	298.15	0.4680
0.3126	308.15	0.4637
0.3852	288.15	0.5670
0.4090	298.15	0.5736
0.4116	308.15	0.5728
0.4946	288.15	0.6823
0.5201	308.15	0.6711
0.5209	298.15	0.6735
0.5528	288.15	0.7231
0.5761	298.15	0.7216
0.5811	308.15	0.7208
0.6870	288.15	0.8206
0.6941	308.15	0.8042
0.6949	298.15	0.8124
0.7929	288.15	0.8817
0.7989	308.15	0.8803
0.8004	298.15	0.8832
0.8948	288.15	0.9431
0.8970	308.15	0.9352
0.8977	298.15	0.9402
0.9359	288.15	0.9660
0.9459	298.15	0.9674
0.9474	308.15	0.9681

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

Fixed		Measured
Mole fraction of Propane, 2-chloro-2-methyl- (2) - Liquid	Temperature, K - Liquid	Mole fraction of Propane, 2-chloro-2-methyl- (2) - Gas
0.0369	298.15	0.0797
0.0379	288.15	0.0827
0.0379	308.15	0.0777
0.1126	288.15	0.2213
0.1136	298.15	0.2100
0.1224	308.15	0.2166
0.1844	288.15	0.3144
0.1949	308.15	0.3289
0.1987	298.15	0.3244
0.2926	288.15	0.4482
0.3126	298.15	0.4680
0.3126	308.15	0.4637
0.3852	288.15	0.5670
0.4090	298.15	0.5736
0.4116	308.15	0.5728
0.4946	288.15	0.6823
0.5201	308.15	0.6711
0.5209	298.15	0.6735
0.5528	288.15	0.7231
0.5761	298.15	0.7216
0.5811	308.15	0.7208
0.6870	288.15	0.8206
0.6941	308.15	0.8042
0.6949	298.15	0.8124
0.7929	288.15	0.8817
0.7989	308.15	0.8803
0.8004	298.15	0.8832
0.8948	288.15	0.9431
0.8970	308.15	0.9352
0.8977	298.15	0.9402
0.9359	288.15	0.9660
0.9459	298.15	0.9674
0.9474	308.15	0.9681

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Propane, 2-chloro-2-methyl- (2) - Liquid	Viscosity, Pa*s - Liquid
283.15	0.0000	0.0004
283.15	0.0490	0.0004
283.15	0.0996	0.0004
283.15	0.1991	0.0004
283.15	0.3212	0.0004
283.15	0.4189	0.0004
283.15	0.5148	0.0004
283.15	0.6213	0.0005
283.15	0.7152	0.0005
283.15	0.8138	0.0005
283.15	0.9079	0.0006
283.15	0.9552	0.0006
283.15	1.0000	0.0006
288.15	0.0000	0.0003
288.15	0.0490	0.0004
288.15	0.0996	0.0004
288.15	0.1991	0.0004
288.15	0.3212	0.0004
288.15	0.4189	0.0004
288.15	0.5148	0.0004
288.15	0.6213	0.0004
288.15	0.7152	0.0005
288.15	0.8138	0.0005
288.15	0.9079	0.0005
288.15	0.9552	0.0005
288.15	1.0000	0.0006
293.15	0.0000	0.0003
293.15	0.0490	0.0003
293.15	0.0996	0.0003
293.15	0.1991	0.0004
293.15	0.3212	0.0004
293.15	0.4189	0.0004
293.15	0.5148	0.0004
293.15	0.6213	0.0004
293.15	0.7152	0.0004
293.15	0.8138	0.0005
293.15	0.9079	0.0005
293.15	0.9552	0.0005
293.15	1.0000	0.0005
298.15	0.0000	0.0003
298.15	0.0490	0.0003
298.15	0.0996	0.0003
298.15	0.1991	0.0003
298.15	0.3212	0.0003
298.15	0.4189	0.0004
298.15	0.5148	0.0004
298.15	0.6213	0.0004
298.15	0.7152	0.0004
298.15	0.8138	0.0004
298.15	0.9079	0.0004
298.15	0.9552	0.0005
298.15	1.0000	0.0005
303.15	0.0000	0.0003
303.15	0.0490	0.0003
303.15	0.0996	0.0003
303.15	0.1991	0.0003
303.15	0.3212	0.0003
303.15	0.4189	0.0003
303.15	0.5148	0.0003
303.15	0.6213	0.0004
303.15	0.7152	0.0004
303.15	0.8138	0.0004
303.15	0.9079	0.0004
303.15	0.9552	0.0004
303.15	1.0000	0.0004
308.15	0.0000	0.0003
308.15	0.0490	0.0003
308.15	0.0996	0.0003
308.15	0.1991	0.0003
308.15	0.3212	0.0003
308.15	0.4189	0.0003
308.15	0.5148	0.0003
308.15	0.6213	0.0003
308.15	0.7152	0.0004
308.15	0.8138	0.0004
308.15	0.9079	0.0004
308.15	0.9552	0.0004
308.15	1.0000	0.0004
313.15	0.0000	0.0003
313.15	0.0490	0.0003
313.15	0.0996	0.0003
313.15	0.1991	0.0003
313.15	0.3212	0.0003
313.15	0.4189	0.0003
313.15	0.5148	0.0003
313.15	0.6213	0.0003
313.15	0.7152	0.0003
313.15	0.8138	0.0004
313.15	0.9079	0.0004
313.15	0.9552	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, 2-chloro-2-methyl- (2) - Liquid	Viscosity, Pa*s - Liquid
283.15	0.0000	0.0004
283.15	0.0490	0.0004
283.15	0.0996	0.0004
283.15	0.1991	0.0004
283.15	0.3212	0.0004
283.15	0.4189	0.0004
283.15	0.5148	0.0004
283.15	0.6213	0.0005
283.15	0.7152	0.0005
283.15	0.8138	0.0005
283.15	0.9079	0.0006
283.15	0.9552	0.0006
283.15	1.0000	0.0006
288.15	0.0000	0.0003
288.15	0.0490	0.0004
288.15	0.0996	0.0004
288.15	0.1991	0.0004
288.15	0.3212	0.0004
288.15	0.4189	0.0004
288.15	0.5148	0.0004
288.15	0.6213	0.0004
288.15	0.7152	0.0005
288.15	0.8138	0.0005
288.15	0.9079	0.0005
288.15	0.9552	0.0005
288.15	1.0000	0.0006
293.15	0.0000	0.0003
293.15	0.0490	0.0003
293.15	0.0996	0.0003
293.15	0.1991	0.0004
293.15	0.3212	0.0004
293.15	0.4189	0.0004
293.15	0.5148	0.0004
293.15	0.6213	0.0004
293.15	0.7152	0.0004
293.15	0.8138	0.0005
293.15	0.9079	0.0005
293.15	0.9552	0.0005
293.15	1.0000	0.0005
298.15	0.0000	0.0003
298.15	0.0490	0.0003
298.15	0.0996	0.0003
298.15	0.1991	0.0003
298.15	0.3212	0.0003
298.15	0.4189	0.0004
298.15	0.5148	0.0004
298.15	0.6213	0.0004
298.15	0.7152	0.0004
298.15	0.8138	0.0004
298.15	0.9079	0.0004
298.15	0.9552	0.0005
298.15	1.0000	0.0005
303.15	0.0000	0.0003
303.15	0.0490	0.0003
303.15	0.0996	0.0003
303.15	0.1991	0.0003
303.15	0.3212	0.0003
303.15	0.4189	0.0003
303.15	0.5148	0.0003
303.15	0.6213	0.0004
303.15	0.7152	0.0004
303.15	0.8138	0.0004
303.15	0.9079	0.0004
303.15	0.9552	0.0004
303.15	1.0000	0.0004
308.15	0.0000	0.0003
308.15	0.0490	0.0003
308.15	0.0996	0.0003
308.15	0.1991	0.0003
308.15	0.3212	0.0003
308.15	0.4189	0.0003
308.15	0.5148	0.0003
308.15	0.6213	0.0003
308.15	0.7152	0.0004
308.15	0.8138	0.0004
308.15	0.9079	0.0004
308.15	0.9552	0.0004
308.15	1.0000	0.0004
313.15	0.0000	0.0003
313.15	0.0490	0.0003
313.15	0.0996	0.0003
313.15	0.1991	0.0003
313.15	0.3212	0.0003
313.15	0.4189	0.0003
313.15	0.5148	0.0003
313.15	0.6213	0.0003
313.15	0.7152	0.0003
313.15	0.8138	0.0004
313.15	0.9079	0.0004
313.15	0.9552	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, 2-chloro-2-methyl- (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1093	0.0045
0.2192	0.0070
0.3295	0.0080
0.4402	0.0082
0.5512	0.0071
0.6628	0.0053
0.7747	0.0035
0.8872	0.0013

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, 2-chloro-2-methyl- (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1093	0.0045
0.2192	0.0070
0.3295	0.0080
0.4402	0.0082
0.5512	0.0071
0.6628	0.0053
0.7747	0.0035
0.8872	0.0013

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Propane, 2-chloro-2-methyl- (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0369	298.15	20.95
0.0379	288.15	13.26
0.0379	308.15	31.78
0.1126	288.15	14.49
0.1136	298.15	22.74
0.1224	308.15	34.48
0.1844	288.15	15.43
0.1949	308.15	36.91
0.1987	298.15	24.50
0.2926	288.15	17.21
0.3126	298.15	26.92
0.3126	308.15	40.34
0.3852	288.15	18.52
0.4090	298.15	28.95
0.4116	308.15	43.40
0.4946	288.15	19.98
0.5201	308.15	46.40
0.5209	298.15	31.11
0.5528	288.15	20.76
0.5761	298.15	32.16
0.5811	308.15	48.12
0.6870	288.15	22.42
0.6941	308.15	51.37
0.6949	298.15	34.53
0.7929	288.15	23.85
0.7989	308.15	54.12
0.8004	298.15	36.42
0.8948	288.15	25.19
0.8970	308.15	56.73
0.8977	298.15	38.23
0.9359	288.15	25.57
0.9459	298.15	39.08
0.9474	308.15	58.07

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Propane, 2-chloro-2-methyl- (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0369	298.15	20.95
0.0379	288.15	13.26
0.0379	308.15	31.78
0.1126	288.15	14.49
0.1136	298.15	22.74
0.1224	308.15	34.48
0.1844	288.15	15.43
0.1949	308.15	36.91
0.1987	298.15	24.50
0.2926	288.15	17.21
0.3126	298.15	26.92
0.3126	308.15	40.34
0.3852	288.15	18.52
0.4090	298.15	28.95
0.4116	308.15	43.40
0.4946	288.15	19.98
0.5201	308.15	46.40
0.5209	298.15	31.11
0.5528	288.15	20.76
0.5761	298.15	32.16
0.5811	308.15	48.12
0.6870	288.15	22.42
0.6941	308.15	51.37
0.6949	298.15	34.53
0.7929	288.15	23.85
0.7989	308.15	54.12
0.8004	298.15	36.42
0.8948	288.15	25.19
0.8970	308.15	56.73
0.8977	298.15	38.23
0.9359	288.15	25.57
0.9459	298.15	39.08
0.9474	308.15	58.07

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Propane, 2-chloro-2-methyl- (2) - Liquid	Refractive index (Na D-line) - Liquid
283.15	0.0490	1.3743
283.15	0.0996	1.375
283.15	0.1991	1.3764
283.15	0.3212	1.3783
283.15	0.4189	1.3799
283.15	0.5148	1.3816
283.15	0.6213	1.3835
283.15	0.7152	1.3852
283.15	0.8138	1.3872
283.15	0.9079	1.3891
283.15	0.9552	1.3902
288.15	0.0490	1.3715
288.15	0.0996	1.3722
288.15	0.1991	1.3737
288.15	0.3212	1.3756
288.15	0.4189	1.3771
288.15	0.5148	1.3787
288.15	0.6213	1.3806
288.15	0.7152	1.3824
288.15	0.8138	1.3843
288.15	0.9079	1.3862
288.15	0.9552	1.3872
293.15	0.0490	1.3688
293.15	0.0996	1.3695
293.15	0.1991	1.3709
293.15	0.3212	1.3728
293.15	0.4189	1.3743
293.15	0.5148	1.3759
293.15	0.6213	1.3778
293.15	0.7152	1.3795
293.15	0.8138	1.3814
293.15	0.9079	1.3833
293.15	0.9552	1.3843
298.15	0.0490	1.3659
298.15	0.0996	1.3666
298.15	0.1991	1.368
298.15	0.3212	1.3699
298.15	0.4189	1.3714
298.15	0.5148	1.373
298.15	0.6213	1.3748
298.15	0.7152	1.3765
298.15	0.8138	1.3784
298.15	0.9079	1.3803
298.15	0.9552	1.3813
303.15	0.0490	1.3631
303.15	0.0996	1.3638
303.15	0.1991	1.3652
303.15	0.3212	1.367
303.15	0.4189	1.3685
303.15	0.5148	1.3701
303.15	0.6213	1.3719
303.15	0.7152	1.3736
303.15	0.8138	1.3754
303.15	0.9079	1.3773
303.15	0.9552	1.3783
308.15	0.0490	1.3602
308.15	0.0996	1.3609
308.15	0.1991	1.3623
308.15	0.3212	1.3641
308.15	0.4189	1.3656
308.15	0.5148	1.3671
308.15	0.6213	1.3689
308.15	0.7152	1.3706
308.15	0.8138	1.3724
308.15	0.9079	1.3743
308.15	0.9552	1.3753
313.15	0.0490	1.3573
313.15	0.0996	1.358
313.15	0.1991	1.3594
313.15	0.3212	1.3611
313.15	0.4189	1.3626
313.15	0.5148	1.3642
313.15	0.6213	1.3659
313.15	0.7152	1.3676
313.15	0.8138	1.3694
313.15	0.9079	1.3712
313.15	0.9552	1.3722

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Propane, 2-chloro-2-methyl- (2) - Liquid	Refractive index (Na D-line) - Liquid
283.15	0.0490	1.3743
283.15	0.0996	1.375
283.15	0.1991	1.3764
283.15	0.3212	1.3783
283.15	0.4189	1.3799
283.15	0.5148	1.3816
283.15	0.6213	1.3835
283.15	0.7152	1.3852
283.15	0.8138	1.3872
283.15	0.9079	1.3891
283.15	0.9552	1.3902
288.15	0.0490	1.3715
288.15	0.0996	1.3722
288.15	0.1991	1.3737
288.15	0.3212	1.3756
288.15	0.4189	1.3771
288.15	0.5148	1.3787
288.15	0.6213	1.3806
288.15	0.7152	1.3824
288.15	0.8138	1.3843
288.15	0.9079	1.3862
288.15	0.9552	1.3872
293.15	0.0490	1.3688
293.15	0.0996	1.3695
293.15	0.1991	1.3709
293.15	0.3212	1.3728
293.15	0.4189	1.3743
293.15	0.5148	1.3759
293.15	0.6213	1.3778
293.15	0.7152	1.3795
293.15	0.8138	1.3814
293.15	0.9079	1.3833
293.15	0.9552	1.3843
298.15	0.0490	1.3659
298.15	0.0996	1.3666
298.15	0.1991	1.368
298.15	0.3212	1.3699
298.15	0.4189	1.3714
298.15	0.5148	1.373
298.15	0.6213	1.3748
298.15	0.7152	1.3765
298.15	0.8138	1.3784
298.15	0.9079	1.3803
298.15	0.9552	1.3813
303.15	0.0490	1.3631
303.15	0.0996	1.3638
303.15	0.1991	1.3652
303.15	0.3212	1.367
303.15	0.4189	1.3685
303.15	0.5148	1.3701
303.15	0.6213	1.3719
303.15	0.7152	1.3736
303.15	0.8138	1.3754
303.15	0.9079	1.3773
303.15	0.9552	1.3783
308.15	0.0490	1.3602
308.15	0.0996	1.3609
308.15	0.1991	1.3623
308.15	0.3212	1.3641
308.15	0.4189	1.3656
308.15	0.5148	1.3671
308.15	0.6213	1.3689
308.15	0.7152	1.3706
308.15	0.8138	1.3724
308.15	0.9079	1.3743
308.15	0.9552	1.3753
313.15	0.0490	1.3573
313.15	0.0996	1.358
313.15	0.1991	1.3594
313.15	0.3212	1.3611
313.15	0.4189	1.3626
313.15	0.5148	1.3642
313.15	0.6213	1.3659
313.15	0.7152	1.3676
313.15	0.8138	1.3694
313.15	0.9079	1.3712
313.15	0.9552	1.3722

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Propane, 2-chloro-2-methyl- (2) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0000	733.833
283.15	0.0490	738.51
283.15	0.0996	743.477
283.15	0.1991	753.625
283.15	0.3212	766.738
283.15	0.4189	777.752
283.15	0.5148	789.053
283.15	0.6213	802.211
283.15	0.7152	814.386
283.15	0.8138	827.842
283.15	0.9079	841.347
283.15	0.9552	848.401
283.15	1.0000	855.249
288.15	0.0000	728.692
288.15	0.0490	733.338
288.15	0.0996	738.271
288.15	0.1991	748.35
288.15	0.3212	761.373
288.15	0.4189	772.308
288.15	0.5148	783.527
288.15	0.6213	796.59
288.15	0.7152	808.683
288.15	0.8138	822.038
288.15	0.9079	835.446
288.15	0.9552	842.442
288.15	1.0000	849.243
293.15	0.0000	723.509
293.15	0.0490	728.121
293.15	0.0996	733.024
293.15	0.1991	743.024
293.15	0.3212	755.959
293.15	0.4189	766.815
293.15	0.5148	777.959
293.15	0.6213	790.929
293.15	0.7152	802.935
293.15	0.8138	816.186
293.15	0.9079	829.489
293.15	0.9552	836.437
293.15	1.0000	843.191
298.15	0.0000	718.289
298.15	0.0490	722.867
298.15	0.0996	727.738
298.15	0.1991	737.666
298.15	0.3212	750.506
298.15	0.4189	761.288
298.15	0.5148	772.351
298.15	0.6213	785.231
298.15	0.7152	797.145
298.15	0.8138	810.301
298.15	0.9079	823.502
298.15	0.9552	830.397
298.15	1.0000	837.096
303.15	0.0000	713.032
303.15	0.0490	717.578
303.15	0.0996	722.412
303.15	0.1991	732.264
303.15	0.3212	745.013
303.15	0.4189	755.716
303.15	0.5148	766.702
303.15	0.6213	779.484
303.15	0.7152	791.308
303.15	0.8138	804.365
303.15	0.9079	817.467
303.15	0.9552	824.312
303.15	1.0000	830.958
308.15	0.0000	707.727
308.15	0.0490	712.24
308.15	0.0996	717.039
308.15	0.1991	726.821
308.15	0.3212	739.479
308.15	0.4189	750.102
308.15	0.5148	761.005
308.15	0.6213	773.688
308.15	0.7152	785.436
308.15	0.8138	798.392
308.15	0.9079	811.393
308.15	0.9552	818.179
308.15	1.0000	824.772
313.15	0.0000	702.378
313.15	0.0490	706.856
313.15	0.0996	711.61
313.15	0.1991	721.328
313.15	0.3212	733.893
313.15	0.4189	744.44
313.15	0.5148	755.257
313.15	0.6213	767.848
313.15	0.7152	779.502
313.15	0.8138	792.362
313.15	0.9079	805.256
313.15	0.9552	811.996
313.15	1.0000	818.536

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Propane, 2-chloro-2-methyl- (2) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0490	738.51
283.15	0.0996	743.477
283.15	0.1991	753.625
283.15	0.3212	766.738
283.15	0.4189	777.752
283.15	0.5148	789.053
283.15	0.6213	802.211
283.15	0.7152	814.386
283.15	0.8138	827.84
283.15	0.9079	841.342
283.15	0.9552	848.393
288.15	0.0490	733.338
288.15	0.0996	738.271
288.15	0.1991	748.35
288.15	0.3212	761.373
288.15	0.4189	772.305
288.15	0.5148	783.527
288.15	0.6213	796.59
288.15	0.7152	808.683
288.15	0.8138	822.038
288.15	0.9079	835.444
288.15	0.9552	842.442
293.15	0.0490	728.121
293.15	0.0996	733.024
293.15	0.1991	743.024
293.15	0.3212	755.959
293.15	0.4189	766.815
293.15	0.5148	777.959
293.15	0.6213	790.929
293.15	0.7152	802.935
293.15	0.8138	816.189
293.15	0.9079	829.491
293.15	0.9552	836.437
298.15	0.0490	722.867
298.15	0.0996	727.738
298.15	0.1991	737.666
298.15	0.3212	750.506
298.15	0.4189	761.286
298.15	0.5148	772.351
298.15	0.6213	785.228
298.15	0.7152	797.145
298.15	0.8138	810.301
298.15	0.9079	823.502
298.15	0.9552	830.397
303.15	0.0490	717.578
303.15	0.0996	722.411
303.15	0.1991	732.264
303.15	0.3212	745.015
303.15	0.4189	755.716
303.15	0.5148	766.702
303.15	0.6213	779.48
303.15	0.7152	791.311
303.15	0.8138	804.371
303.15	0.9079	817.469
303.15	0.9552	824.312
308.15	0.0490	712.24
308.15	0.0996	717.041
308.15	0.1991	726.821
308.15	0.3212	739.479
308.15	0.4189	750.102
308.15	0.5148	761.005
308.15	0.6213	773.688
308.15	0.7152	785.433
308.15	0.8138	798.394
308.15	0.9079	811.393
308.15	0.9552	818.179
313.15	0.0490	706.86
313.15	0.0996	711.627
313.15	0.1991	721.331
313.15	0.3212	733.893
313.15	0.4189	744.44
313.15	0.5148	755.257
313.15	0.6213	767.848
313.15	0.7152	779.502
313.15	0.8138	792.364
313.15	0.9079	805.264
313.15	0.9552	811.999

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Propane, 2-chloro-2-methyl- (2) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0000	733.833
283.15	0.0490	738.51
283.15	0.0996	743.477
283.15	0.1991	753.625
283.15	0.3212	766.738
283.15	0.4189	777.752
283.15	0.5148	789.053
283.15	0.6213	802.211
283.15	0.7152	814.386
283.15	0.8138	827.842
283.15	0.9079	841.347
283.15	0.9552	848.401
283.15	1.0000	855.249
288.15	0.0000	728.692
288.15	0.0490	733.338
288.15	0.0996	738.271
288.15	0.1991	748.35
288.15	0.3212	761.373
288.15	0.4189	772.308
288.15	0.5148	783.527
288.15	0.6213	796.59
288.15	0.7152	808.683
288.15	0.8138	822.038
288.15	0.9079	835.446
288.15	0.9552	842.442
288.15	1.0000	849.243
293.15	0.0000	723.509
293.15	0.0490	728.121
293.15	0.0996	733.024
293.15	0.1991	743.024
293.15	0.3212	755.959
293.15	0.4189	766.815
293.15	0.5148	777.959
293.15	0.6213	790.929
293.15	0.7152	802.935
293.15	0.8138	816.186
293.15	0.9079	829.489
293.15	0.9552	836.437
293.15	1.0000	843.191
298.15	0.0000	718.289
298.15	0.0490	722.867
298.15	0.0996	727.738
298.15	0.1991	737.666
298.15	0.3212	750.506
298.15	0.4189	761.288
298.15	0.5148	772.351
298.15	0.6213	785.231
298.15	0.7152	797.145
298.15	0.8138	810.301
298.15	0.9079	823.502
298.15	0.9552	830.397
298.15	1.0000	837.096
303.15	0.0000	713.032
303.15	0.0490	717.578
303.15	0.0996	722.412
303.15	0.1991	732.264
303.15	0.3212	745.013
303.15	0.4189	755.716
303.15	0.5148	766.702
303.15	0.6213	779.484
303.15	0.7152	791.308
303.15	0.8138	804.365
303.15	0.9079	817.467
303.15	0.9552	824.312
303.15	1.0000	830.958
308.15	0.0000	707.727
308.15	0.0490	712.24
308.15	0.0996	717.039
308.15	0.1991	726.821
308.15	0.3212	739.479
308.15	0.4189	750.102
308.15	0.5148	761.005
308.15	0.6213	773.688
308.15	0.7152	785.436
308.15	0.8138	798.392
308.15	0.9079	811.393
308.15	0.9552	818.179
308.15	1.0000	824.772
313.15	0.0000	702.378
313.15	0.0490	706.856
313.15	0.0996	711.61
313.15	0.1991	721.328
313.15	0.3212	733.893
313.15	0.4189	744.44
313.15	0.5148	755.257
313.15	0.6213	767.848
313.15	0.7152	779.502
313.15	0.8138	792.362
313.15	0.9079	805.256
313.15	0.9552	811.996
313.15	1.0000	818.536

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Propane, 2-chloro-2-methyl- (2) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0490	738.51
283.15	0.0996	743.477
283.15	0.1991	753.625
283.15	0.3212	766.738
283.15	0.4189	777.752
283.15	0.5148	789.053
283.15	0.6213	802.211
283.15	0.7152	814.386
283.15	0.8138	827.84
283.15	0.9079	841.342
283.15	0.9552	848.393
288.15	0.0490	733.338
288.15	0.0996	738.271
288.15	0.1991	748.35
288.15	0.3212	761.373
288.15	0.4189	772.305
288.15	0.5148	783.527
288.15	0.6213	796.59
288.15	0.7152	808.683
288.15	0.8138	822.038
288.15	0.9079	835.444
288.15	0.9552	842.442
293.15	0.0490	728.121
293.15	0.0996	733.024
293.15	0.1991	743.024
293.15	0.3212	755.959
293.15	0.4189	766.815
293.15	0.5148	777.959
293.15	0.6213	790.929
293.15	0.7152	802.935
293.15	0.8138	816.189
293.15	0.9079	829.491
293.15	0.9552	836.437
298.15	0.0490	722.867
298.15	0.0996	727.738
298.15	0.1991	737.666
298.15	0.3212	750.506
298.15	0.4189	761.286
298.15	0.5148	772.351
298.15	0.6213	785.228
298.15	0.7152	797.145
298.15	0.8138	810.301
298.15	0.9079	823.502
298.15	0.9552	830.397
303.15	0.0490	717.578
303.15	0.0996	722.411
303.15	0.1991	732.264
303.15	0.3212	745.015
303.15	0.4189	755.716
303.15	0.5148	766.702
303.15	0.6213	779.48
303.15	0.7152	791.311
303.15	0.8138	804.371
303.15	0.9079	817.469
303.15	0.9552	824.312
308.15	0.0490	712.24
308.15	0.0996	717.041
308.15	0.1991	726.821
308.15	0.3212	739.479
308.15	0.4189	750.102
308.15	0.5148	761.005
308.15	0.6213	773.688
308.15	0.7152	785.433
308.15	0.8138	798.394
308.15	0.9079	811.393
308.15	0.9552	818.179
313.15	0.0490	706.86
313.15	0.0996	711.627
313.15	0.1991	721.331
313.15	0.3212	733.893
313.15	0.4189	744.44
313.15	0.5148	755.257
313.15	0.6213	767.848
313.15	0.7152	779.502
313.15	0.8138	792.364
313.15	0.9079	805.264
313.15	0.9552	811.999

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Propane, 2-chloro-2-methyl- (2) - Liquid	Speed of sound, m/s - Liquid
283.15	0.0490	1064.88
283.15	0.0996	1064.14
283.15	0.1991	1062.65
283.15	0.3212	1060.71
283.15	0.4189	1059.09
283.15	0.5148	1057.41
283.15	0.6213	1055.41
283.15	0.7152	1053.53
283.15	0.8138	1051.4
283.15	0.9079	1049.23
283.15	0.9552	1048.07
288.15	0.0490	1042.52
288.15	0.0996	1041.81
288.15	0.1991	1040.4
288.15	0.3212	1038.55
288.15	0.4189	1037.01
288.15	0.5148	1035.42
288.15	0.6213	1033.55
288.15	0.7152	1031.77
288.15	0.8138	1029.76
288.15	0.9079	1027.68
288.15	0.9552	1026.56
293.15	0.0490	1020.02
293.15	0.0996	1019.36
293.15	0.1991	1018.03
293.15	0.3212	1016.3
293.15	0.4189	1014.87
293.15	0.5148	1013.38
293.15	0.6213	1011.65
293.15	0.7152	1009.96
293.15	0.8138	1008.07
293.15	0.9079	1006.15
293.15	0.9552	1005.09
298.15	0.0490	997.71
298.15	0.0996	997.09
298.15	0.1991	995.89
298.15	0.3212	994.32
298.15	0.4189	993.03
298.15	0.5148	991.68
298.15	0.6213	990.11
298.15	0.7152	988.62
298.15	0.8138	986.91
298.15	0.9079	985.13
298.15	0.9552	984.18
303.15	0.0490	975.46
303.15	0.0996	974.84
303.15	0.1991	973.65
303.15	0.3212	972.13
303.15	0.4189	970.88
303.15	0.5148	969.59
303.15	0.6213	968.1
303.15	0.7152	966.67
303.15	0.8138	965.04
303.15	0.9079	963.34
303.15	0.9552	962.38
308.15	0.0490	953.42
308.15	0.0996	952.84
308.15	0.1991	951.71
308.15	0.3212	950.28
308.15	0.4189	949.13
308.15	0.5148	947.93
308.15	0.6213	946.56
308.15	0.7152	945.25
308.15	0.8138	943.74
308.15	0.9079	942.17
308.15	0.9552	941.27
313.15	0.0490	931.51
313.15	0.0996	930.96
313.15	0.1991	929.87
313.15	0.3212	928.52
313.15	0.4189	927.44
313.15	0.5148	926.35
313.15	0.6213	925.1
313.15	0.7152	923.88
313.15	0.8138	922.47
313.15	0.9079	921.0
313.15	0.9552	920.15

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Propane, 2-chloro-2-methyl- (2) - Liquid	Speed of sound, m/s - Liquid
283.15	0.0490	1064.88
283.15	0.0996	1064.14
283.15	0.1991	1062.65
283.15	0.3212	1060.71
283.15	0.4189	1059.09
283.15	0.5148	1057.41
283.15	0.6213	1055.41
283.15	0.7152	1053.53
283.15	0.8138	1051.4
283.15	0.9079	1049.23
283.15	0.9552	1048.07
288.15	0.0490	1042.52
288.15	0.0996	1041.81
288.15	0.1991	1040.4
288.15	0.3212	1038.55
288.15	0.4189	1037.01
288.15	0.5148	1035.42
288.15	0.6213	1033.55
288.15	0.7152	1031.77
288.15	0.8138	1029.76
288.15	0.9079	1027.68
288.15	0.9552	1026.56
293.15	0.0490	1020.02
293.15	0.0996	1019.36
293.15	0.1991	1018.03
293.15	0.3212	1016.3
293.15	0.4189	1014.87
293.15	0.5148	1013.38
293.15	0.6213	1011.65
293.15	0.7152	1009.96
293.15	0.8138	1008.07
293.15	0.9079	1006.15
293.15	0.9552	1005.09
298.15	0.0490	997.71
298.15	0.0996	997.09
298.15	0.1991	995.89
298.15	0.3212	994.32
298.15	0.4189	993.03
298.15	0.5148	991.68
298.15	0.6213	990.11
298.15	0.7152	988.62
298.15	0.8138	986.91
298.15	0.9079	985.13
298.15	0.9552	984.18
303.15	0.0490	975.46
303.15	0.0996	974.84
303.15	0.1991	973.65
303.15	0.3212	972.13
303.15	0.4189	970.88
303.15	0.5148	969.59
303.15	0.6213	968.1
303.15	0.7152	966.67
303.15	0.8138	965.04
303.15	0.9079	963.34
303.15	0.9552	962.38
308.15	0.0490	953.42
308.15	0.0996	952.84
308.15	0.1991	951.71
308.15	0.3212	950.28
308.15	0.4189	949.13
308.15	0.5148	947.93
308.15	0.6213	946.56
308.15	0.7152	945.25
308.15	0.8138	943.74
308.15	0.9079	942.17
308.15	0.9552	941.27
313.15	0.0490	931.51
313.15	0.0996	930.96
313.15	0.1991	929.87
313.15	0.3212	928.52
313.15	0.4189	927.44
313.15	0.5148	926.35
313.15	0.6213	925.1
313.15	0.7152	923.88
313.15	0.8138	922.47
313.15	0.9079	921.0
313.15	0.9552	920.15

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