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

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Butane, 1-chloro-

Name
Butane, 1-chloro-
InChI
InChI=1S/C4H9Cl/c1-2-3-4-5/h2-4H2,1H3
InChI Key
VFWCMGCRMGJXDK-UHFFFAOYSA-N
Formula
C4H9Cl
SMILES
CCCCCl
Mol. Weight (g/mol)
92.57
CAS
109-69-3

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
0.0570 -0.0280
0.1040 -0.0580
0.2010 -0.1160
0.2980 -0.1590
0.3980 -0.1950
0.4970 -0.2100
0.5970 -0.2070
0.6960 -0.1880
0.7990 -0.1470
0.9010 -0.0850
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
0.0570 -0.0280
0.1040 -0.0580
0.2010 -0.1160
0.2980 -0.1590
0.3980 -0.1950
0.4970 -0.2100
0.5970 -0.2070
0.6960 -0.1880
0.7990 -0.1470
0.9010 -0.0850
0.9540 -0.0430

Kinematic viscosity, m2/s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Butane, 1-chloro- (1) - Liquid Kinematic viscosity, m2/s - Liquid
298.15 0.0000 5.5930e-07
298.15 0.0494 5.5560e-07
298.15 0.1008 5.5160e-07
298.15 0.2030 5.4320e-07
298.15 0.3004 5.3480e-07
298.15 0.3963 5.2670e-07
298.15 0.4969 5.1810e-07
298.15 0.5976 5.0950e-07
298.15 0.6993 5.0120e-07
298.15 0.7993 4.9320e-07
298.15 0.8988 4.8530e-07
298.15 0.9483 4.8190e-07
298.15 1.0000 4.7830e-07
313.15 0.0000 4.9160e-07
313.15 0.0494 4.8810e-07
313.15 0.1008 4.8460e-07
313.15 0.2030 4.7780e-07
313.15 0.3004 4.7100e-07
313.15 0.3963 4.6390e-07
313.15 0.4969 4.5640e-07
313.15 0.5976 4.4890e-07
313.15 0.6993 4.4140e-07
313.15 0.7993 4.3420e-07
313.15 0.8988 4.2750e-07
313.15 0.9483 4.2420e-07
313.15 1.0000 4.2090e-07

Kinematic viscosity, m2/s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Butane, 1-chloro- (1) - Liquid Kinematic viscosity, m2/s - Liquid
298.15 0.0000 5.5930e-07
298.15 0.0494 5.5560e-07
298.15 0.1008 5.5160e-07
298.15 0.2030 5.4320e-07
298.15 0.3004 5.3480e-07
298.15 0.3963 5.2670e-07
298.15 0.4969 5.1810e-07
298.15 0.5976 5.0950e-07
298.15 0.6993 5.0120e-07
298.15 0.7993 4.9320e-07
298.15 0.8988 4.8530e-07
298.15 0.9483 4.8190e-07
298.15 1.0000 4.7830e-07
313.15 0.0000 4.9160e-07
313.15 0.0494 4.8810e-07
313.15 0.1008 4.8460e-07
313.15 0.2030 4.7780e-07
313.15 0.3004 4.7100e-07
313.15 0.3963 4.6390e-07
313.15 0.4969 4.5640e-07
313.15 0.5976 4.4890e-07
313.15 0.6993 4.4140e-07
313.15 0.7993 4.3420e-07
313.15 0.8988 4.2750e-07
313.15 0.9483 4.2420e-07
313.15 1.0000 4.2090e-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 0.0535 879.23
298.15 0.0972 878.04
298.15 0.1958 875.19
298.15 0.2975 872.17
298.15 0.4006 869.04
298.15 0.5031 865.88
298.15 0.6017 862.77
298.15 0.6986 859.63
298.15 0.8009 856.27
298.15 0.9005 852.87
298.15 0.9489 851.15
313.15 0.0507 862.5
313.15 0.1022 861.16
313.15 0.2014 858.46
313.15 0.3019 855.6
313.15 0.4047 852.6
313.15 0.5017 849.72
313.15 0.6026 846.65
313.15 0.7017 843.55
313.15 0.7994 840.43
313.15 0.9009 837.13
313.15 0.9487 835.54

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Butane, 1-chloro- (1) - Liquid Mass density, kg/m3 - Liquid
298.15 0.0000 849.28
298.15 0.0494 850.97
298.15 0.1008 852.97
298.15 0.2030 856.41
298.15 0.3004 859.76
298.15 0.3963 862.73
298.15 0.4969 865.86
298.15 0.5976 869.09
298.15 0.6993 872.11
298.15 0.7993 874.9
298.15 0.8988 878.01
298.15 0.9483 879.23
298.15 1.0000 880.62
313.15 0.0000 834.01
313.15 0.0494 835.48
313.15 0.1008 837.19
313.15 0.2030 840.52
313.15 0.3004 843.74
313.15 0.3963 846.73
313.15 0.4969 849.69
313.15 0.5976 852.75
313.15 0.6993 855.69
313.15 0.7993 858.36
313.15 0.8988 861.05
313.15 0.9483 862.56
313.15 1.0000 863.86

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 0.0535 879.23
298.15 0.0972 878.04
298.15 0.1958 875.19
298.15 0.2975 872.17
298.15 0.4006 869.04
298.15 0.5031 865.88
298.15 0.6017 862.77
298.15 0.6986 859.63
298.15 0.8009 856.27
298.15 0.9005 852.87
298.15 0.9489 851.15
313.15 0.0507 862.5
313.15 0.1022 861.16
313.15 0.2014 858.46
313.15 0.3019 855.6
313.15 0.4047 852.6
313.15 0.5017 849.72
313.15 0.6026 846.65
313.15 0.7017 843.55
313.15 0.7994 840.43
313.15 0.9009 837.13
313.15 0.9487 835.54

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Butane, 1-chloro- (1) - Liquid Mass density, kg/m3 - Liquid
298.15 0.0000 849.28
298.15 0.0494 850.97
298.15 0.1008 852.97
298.15 0.2030 856.41
298.15 0.3004 859.76
298.15 0.3963 862.73
298.15 0.4969 865.86
298.15 0.5976 869.09
298.15 0.6993 872.11
298.15 0.7993 874.9
298.15 0.8988 878.01
298.15 0.9483 879.23
298.15 1.0000 880.62
313.15 0.0000 834.01
313.15 0.0494 835.48
313.15 0.1008 837.19
313.15 0.2030 840.52
313.15 0.3004 843.74
313.15 0.3963 846.73
313.15 0.4969 849.69
313.15 0.5976 852.75
313.15 0.6993 855.69
313.15 0.7993 858.36
313.15 0.8988 861.05
313.15 0.9483 862.56
313.15 1.0000 863.86

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 0.0535 1123.2
298.15 0.0972 1126.8
298.15 0.1958 1134.9
298.15 0.2975 1143.3
298.15 0.4006 1151.9
298.15 0.5031 1160.5
298.15 0.6017 1168.8
298.15 0.6986 1177.0
298.15 0.8009 1185.6
298.15 0.9005 1194.1
298.15 0.9489 1198.2
313.15 0.0507 1061.0
313.15 0.1022 1065.0
313.15 0.2014 1072.6
313.15 0.3019 1080.3
313.15 0.4047 1088.5
313.15 0.5017 1096.2
313.15 0.6026 1104.3
313.15 0.7017 1112.3
313.15 0.7994 1120.2
313.15 0.9009 1128.3
313.15 0.9487 1132.2

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 0.0535 1123.2
298.15 0.0972 1126.8
298.15 0.1958 1134.9
298.15 0.2975 1143.3
298.15 0.4006 1151.9
298.15 0.5031 1160.5
298.15 0.6017 1168.8
298.15 0.6986 1177.0
298.15 0.8009 1185.6
298.15 0.9005 1194.1
298.15 0.9489 1198.2
313.15 0.0507 1061.0
313.15 0.1022 1065.0
313.15 0.2014 1072.6
313.15 0.3019 1080.3
313.15 0.4047 1088.5
313.15 0.5017 1096.2
313.15 0.6026 1104.3
313.15 0.7017 1112.3
313.15 0.7994 1120.2
313.15 0.9009 1128.3
313.15 0.9487 1132.2

Sources