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

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Diisopropyl ether

Name
Diisopropyl ether
InChI
InChI=1S/C6H14O/c1-5(2)7-6(3)4/h5-6H,1-4H3
InChI Key
ZAFNJMIOTHYJRJ-UHFFFAOYSA-N
Formula
C6H14O
SMILES
CC(C)OC(C)C
Mol. Weight (g/mol)
102.17
CAS
108-20-3

Propane, 1-chloro-2-methyl-

Name
Propane, 1-chloro-2-methyl-
InChI
InChI=1S/C4H9Cl/c1-4(2)3-5/h4H,3H2,1-2H3
InChI Key
QTBFPMKWQKYFLR-UHFFFAOYSA-N
Formula
C4H9Cl
SMILES
CC(C)CCl
Mol. Weight (g/mol)
92.57
CAS
513-36-0
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Datasets

  1. Mole fraction (2)
  2. η - Viscosity, Pa*s (2)
  3. Excess molar enthalpy (molar enthalpy (2)
  4. Pvap - Vapor or sublimation pressure, kPa (2)
  5. n0 - Refractive index (Na D-line) (2)
  6. ρl - Mass density, kg/m3 (4)
  7. csound,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:

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:

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