Mixture of Propane, 1-chloro-2-methyl- + Furan, tetrahydro-2-methyl-

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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

Furan, tetrahydro-2-methyl-

Name
Furan, tetrahydro-2-methyl-
InChI
InChI=1S/C5H10O/c1-5-3-2-4-6-5/h5H,2-4H2,1H3
InChI Key
JWUJQDFVADABEY-UHFFFAOYSA-N
Formula
C5H10O
SMILES
CC1CCCO1
Mol. Weight (g/mol)
86.13
CAS
96-47-9
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Datasets

  1. Excess molar enthalpy (molar enthalpy (2)
  2. ν - Kinematic viscosity, m2/s (2)
  3. ρl - Mass density, kg/m3 (4)
  4. csound,fluid - Speed of Sound, m/s (2)

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

Operational conditions:

Mole fraction of Furan, tetrahydro-2-methyl- (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0600 -0.0330
0.1090 -0.0670
0.2100 -0.1320
0.3090 -0.1740
0.4110 -0.2110
0.5110 -0.2240
0.6090 -0.2200
0.7070 -0.1960
0.8060 -0.1510
0.9040 -0.0840
0.9540 -0.0430

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

Operational conditions:

Mole fraction of Furan, tetrahydro-2-methyl- (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0600 -0.0330
0.1090 -0.0670
0.2100 -0.1320
0.3090 -0.1740
0.4110 -0.2110
0.5110 -0.2240
0.6090 -0.2200
0.7070 -0.1960
0.8060 -0.1510
0.9040 -0.0840
0.9540 -0.0430

Kinematic viscosity, m2/s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Propane, 1-chloro-2-methyl- (1) - Liquid Kinematic viscosity, m2/s - Liquid
298.15 0.0000 5.5930e-07
298.15 0.0484 5.5560e-07
298.15 0.0999 5.5160e-07
298.15 0.1962 5.4410e-07
298.15 0.3105 5.3540e-07
298.15 0.4006 5.2860e-07
298.15 0.4775 5.2300e-07
298.15 0.6006 5.1460e-07
298.15 0.7031 5.0820e-07
298.15 0.8026 5.0260e-07
298.15 0.9059 4.9700e-07
298.15 0.9506 4.9460e-07
298.15 1.0000 4.9200e-07
313.15 0.0000 4.9160e-07
313.15 0.0484 4.8840e-07
313.15 0.0999 4.8480e-07
313.15 0.1962 4.7810e-07
313.15 0.3105 4.7050e-07
313.15 0.4006 4.6460e-07
313.15 0.4775 4.5980e-07
313.15 0.6006 4.5210e-07
313.15 0.7031 4.4600e-07
313.15 0.8026 4.4010e-07
313.15 0.9059 4.3410e-07
313.15 0.9506 4.3160e-07
313.15 1.0000 4.2870e-07

Kinematic viscosity, m2/s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Propane, 1-chloro-2-methyl- (1) - Liquid Kinematic viscosity, m2/s - Liquid
298.15 0.0000 5.5930e-07
298.15 0.0484 5.5560e-07
298.15 0.0999 5.5160e-07
298.15 0.1962 5.4410e-07
298.15 0.3105 5.3540e-07
298.15 0.4006 5.2860e-07
298.15 0.4775 5.2300e-07
298.15 0.6006 5.1460e-07
298.15 0.7031 5.0820e-07
298.15 0.8026 5.0260e-07
298.15 0.9059 4.9700e-07
298.15 0.9506 4.9460e-07
298.15 1.0000 4.9200e-07
313.15 0.0000 4.9160e-07
313.15 0.0484 4.8840e-07
313.15 0.0999 4.8480e-07
313.15 0.1962 4.7810e-07
313.15 0.3105 4.7050e-07
313.15 0.4006 4.6460e-07
313.15 0.4775 4.5980e-07
313.15 0.6006 4.5210e-07
313.15 0.7031 4.4600e-07
313.15 0.8026 4.4010e-07
313.15 0.9059 4.3410e-07
313.15 0.9506 4.3160e-07
313.15 1.0000 4.2870e-07

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Furan, tetrahydro-2-methyl- (2) - Liquid Mass density, kg/m3 - Liquid
298.15 0.0515 870.05
298.15 0.1006 869.23
298.15 0.2026 867.39
298.15 0.3059 865.41
298.15 0.4062 863.41
298.15 0.5050 861.34
298.15 0.6022 859.23
298.15 0.7035 856.92
298.15 0.8012 854.57
298.15 0.9099 851.75
298.15 0.9492 850.66
313.15 0.0553 852.78
313.15 0.1014 852.08
313.15 0.1992 850.48
313.15 0.3000 848.74
313.15 0.4072 846.78
313.15 0.5015 844.98
313.15 0.6050 842.9
313.15 0.7022 840.83
313.15 0.8000 838.61
313.15 0.8967 836.35
313.15 0.9491 835.09

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- (1) - Liquid Mass density, kg/m3 - Liquid
298.15 0.0000 849.28
298.15 0.0484 850.43
298.15 0.0999 852.07
298.15 0.1962 854.44
298.15 0.3105 857.3
298.15 0.4006 859.25
298.15 0.4775 860.99
298.15 0.6006 863.58
298.15 0.7031 865.6
298.15 0.8026 867.49
298.15 0.9059 869.22
298.15 0.9506 870.2
298.15 1.0000 870.93
313.15 0.0000 834.01
313.15 0.0484 834.97
313.15 0.0999 836.22
313.15 0.1962 838.53
313.15 0.3105 841.23
313.15 0.4006 843.09
313.15 0.4775 844.5
313.15 0.6006 846.94
313.15 0.7031 848.88
313.15 0.8026 850.49
313.15 0.9059 852.11
313.15 0.9506 852.87
313.15 1.0000 853.51

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Furan, tetrahydro-2-methyl- (2) - Liquid Mass density, kg/m3 - Liquid
298.15 0.0515 870.05
298.15 0.1006 869.23
298.15 0.2026 867.39
298.15 0.3059 865.41
298.15 0.4062 863.41
298.15 0.5050 861.34
298.15 0.6022 859.23
298.15 0.7035 856.92
298.15 0.8012 854.57
298.15 0.9099 851.75
298.15 0.9492 850.66
313.15 0.0553 852.78
313.15 0.1014 852.08
313.15 0.1992 850.48
313.15 0.3000 848.74
313.15 0.4072 846.78
313.15 0.5015 844.98
313.15 0.6050 842.9
313.15 0.7022 840.83
313.15 0.8000 838.61
313.15 0.8967 836.35
313.15 0.9491 835.09

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- (1) - Liquid Mass density, kg/m3 - Liquid
298.15 0.0000 849.28
298.15 0.0484 850.43
298.15 0.0999 852.07
298.15 0.1962 854.44
298.15 0.3105 857.3
298.15 0.4006 859.25
298.15 0.4775 860.99
298.15 0.6006 863.58
298.15 0.7031 865.6
298.15 0.8026 867.49
298.15 0.9059 869.22
298.15 0.9506 870.2
298.15 1.0000 870.93
313.15 0.0000 834.01
313.15 0.0484 834.97
313.15 0.0999 836.22
313.15 0.1962 838.53
313.15 0.3105 841.23
313.15 0.4006 843.09
313.15 0.4775 844.5
313.15 0.6006 846.94
313.15 0.7031 848.88
313.15 0.8026 850.49
313.15 0.9059 852.11
313.15 0.9506 852.87
313.15 1.0000 853.51

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Furan, tetrahydro-2-methyl- (2) - Liquid Speed of sound, m/s - Liquid
298.15 0.0515 1085.4
298.15 0.1006 1091.3
298.15 0.2026 1103.8
298.15 0.3059 1116.6
298.15 0.4062 1129.1
298.15 0.5050 1141.4
298.15 0.6022 1153.5
298.15 0.7035 1166.1
298.15 0.8012 1178.2
298.15 0.9099 1191.6
298.15 0.9492 1196.4
313.15 0.0553 1023.0
313.15 0.1014 1028.6
313.15 0.1992 1040.5
313.15 0.3000 1052.7
313.15 0.4072 1065.7
313.15 0.5015 1077.0
313.15 0.6050 1089.3
313.15 0.7022 1100.8
313.15 0.8000 1112.4
313.15 0.8967 1123.8
313.15 0.9491 1130.0

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Furan, tetrahydro-2-methyl- (2) - Liquid Speed of sound, m/s - Liquid
298.15 0.0515 1085.4
298.15 0.1006 1091.3
298.15 0.2026 1103.8
298.15 0.3059 1116.6
298.15 0.4062 1129.1
298.15 0.5050 1141.4
298.15 0.6022 1153.5
298.15 0.7035 1166.1
298.15 0.8012 1178.2
298.15 0.9099 1191.6
298.15 0.9492 1196.4
313.15 0.0553 1023.0
313.15 0.1014 1028.6
313.15 0.1992 1040.5
313.15 0.3000 1052.7
313.15 0.4072 1065.7
313.15 0.5015 1077.0
313.15 0.6050 1089.3
313.15 0.7022 1100.8
313.15 0.8000 1112.4
313.15 0.8967 1123.8
313.15 0.9491 1130.0

Sources