Mixture of Phenol, 3-methyl- + Ethanol

Excel

Phenol, 3-methyl-

Name
Phenol, 3-methyl-
InChI
InChI=1S/C7H8O/c1-6-3-2-4-7(8)5-6/h2-5,8H,1H3
InChI Key
RLSSMJSEOOYNOY-UHFFFAOYSA-N
Formula
C7H8O
SMILES
Cc1cccc(O)c1
Mol. Weight (g/mol)
108.14
CAS
108-39-4

Ethanol

Name
Ethanol
InChI
InChI=1S/C2H6O/c1-2-3/h3H,2H2,1H3
InChI Key
LFQSCWFLJHTTHZ-UHFFFAOYSA-N
Formula
C2H6O
SMILES
CCO
Mol. Weight (g/mol)
46.07
CAS
64-17-5
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry. Do not hesitate to contact us for your projects.

Datasets

  1. Excess molar enthalpy (molar enthalpy (2)
  2. ρl - Mass density, kg/m3 (2)
  3. csound,fluid - Speed of Sound, m/s (2)
  4. Tboil - Boiling temperature at pressure P, K (2)

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

Operational conditions:

Mole fraction of Phenol, 3-methyl- (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.2003 -0.7920
0.4097 -1.2277
0.5861 -1.1462
0.7875 -0.6874

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

Operational conditions:

Mole fraction of Phenol, 3-methyl- (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.2003 -0.7920
0.4097 -1.2277
0.5861 -1.1462
0.7875 -0.6874

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanol (2) - Liquid Mass density, kg/m3 - Liquid
303.15 0.0000 1025.71
303.15 0.1400 1005.48
303.15 0.2637 985.23
303.15 0.3738 964.94
303.15 0.4724 944.63
303.15 0.5612 924.32
303.15 0.6417 903.96
303.15 0.7149 883.56
303.15 0.7817 863.15
303.15 0.8431 842.67
303.15 0.8995 822.2
303.15 0.9517 801.66
303.15 1.0000 781.08
308.15 0.0000 1021.7
308.15 0.1400 1001.45
308.15 0.2637 981.17
308.15 0.3738 960.82
308.15 0.4724 940.47
308.15 0.5612 920.08
308.15 0.6417 899.68
308.15 0.7149 879.25
308.15 0.7817 858.83
308.15 0.8431 838.32
308.15 0.8995 817.81
308.15 0.9517 797.22
308.15 1.0000 776.59
313.15 0.0000 1017.69
313.15 0.1400 997.42
313.15 0.2637 977.1
313.15 0.3738 956.72
313.15 0.4724 936.35
313.15 0.5612 915.95
313.15 0.6417 895.51
313.15 0.7149 875.06
313.15 0.7817 854.61
313.15 0.8431 834.07
313.15 0.8995 813.53
313.15 0.9517 792.9
313.15 1.0000 772.23
318.15 0.0000 1013.65
318.15 0.1400 993.36
318.15 0.2637 972.97
318.15 0.3738 952.53
318.15 0.4724 932.08
318.15 0.5612 911.64
318.15 0.6417 891.18
318.15 0.7149 870.68
318.15 0.7817 850.21
318.15 0.8431 829.62
318.15 0.8995 809.06
318.15 0.9517 788.34
318.15 1.0000 767.61

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanol (2) - Liquid Mass density, kg/m3 - Liquid
303.15 0.0000 1025.71
303.15 0.1400 1005.48
303.15 0.2637 985.23
303.15 0.3738 964.94
303.15 0.4724 944.63
303.15 0.5612 924.32
303.15 0.6417 903.96
303.15 0.7149 883.56
303.15 0.7817 863.15
303.15 0.8431 842.67
303.15 0.8995 822.2
303.15 0.9517 801.66
303.15 1.0000 781.08
308.15 0.0000 1021.7
308.15 0.1400 1001.45
308.15 0.2637 981.17
308.15 0.3738 960.82
308.15 0.4724 940.47
308.15 0.5612 920.08
308.15 0.6417 899.68
308.15 0.7149 879.25
308.15 0.7817 858.83
308.15 0.8431 838.32
308.15 0.8995 817.81
308.15 0.9517 797.22
308.15 1.0000 776.59
313.15 0.0000 1017.69
313.15 0.1400 997.42
313.15 0.2637 977.1
313.15 0.3738 956.72
313.15 0.4724 936.35
313.15 0.5612 915.95
313.15 0.6417 895.51
313.15 0.7149 875.06
313.15 0.7817 854.61
313.15 0.8431 834.07
313.15 0.8995 813.53
313.15 0.9517 792.9
313.15 1.0000 772.23
318.15 0.0000 1013.65
318.15 0.1400 993.36
318.15 0.2637 972.97
318.15 0.3738 952.53
318.15 0.4724 932.08
318.15 0.5612 911.64
318.15 0.6417 891.18
318.15 0.7149 870.68
318.15 0.7817 850.21
318.15 0.8431 829.62
318.15 0.8995 809.06
318.15 0.9517 788.34
318.15 1.0000 767.61

Speed of sound, m/s [ref]

Operational conditions:

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanol (2) - Liquid Speed of sound, m/s - Liquid
303.15 0.0000 1466.13
303.15 0.1400 1426.7
303.15 0.2637 1384.7
303.15 0.3738 1344.9
303.15 0.4724 1308.5
303.15 0.5612 1275.8
303.15 0.6417 1246.6
303.15 0.7149 1220.5
303.15 0.7817 1197.2
303.15 0.8431 1176.3
303.15 0.8995 1157.8
303.15 0.9517 1141.4
303.15 1.0000 1127.01
313.15 0.0000 1436.09
313.15 0.1400 1398.2
313.15 0.2637 1355.0
313.15 0.3738 1313.8
313.15 0.4724 1276.5
313.15 0.5612 1243.4
313.15 0.6417 1214.0
313.15 0.7149 1188.0
313.15 0.7817 1164.7
313.15 0.8431 1143.9
313.15 0.8995 1125.3
313.15 0.9517 1108.7
313.15 1.0000 1094.03

Speed of sound, m/s [ref]

Operational conditions:

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanol (2) - Liquid Speed of sound, m/s - Liquid
303.15 0.0000 1466.13
303.15 0.1400 1426.7
303.15 0.2637 1384.7
303.15 0.3738 1344.9
303.15 0.4724 1308.5
303.15 0.5612 1275.8
303.15 0.6417 1246.6
303.15 0.7149 1220.5
303.15 0.7817 1197.2
303.15 0.8431 1176.3
303.15 0.8995 1157.8
303.15 0.9517 1141.4
303.15 1.0000 1127.01
313.15 0.0000 1436.09
313.15 0.1400 1398.2
313.15 0.2637 1355.0
313.15 0.3738 1313.8
313.15 0.4724 1276.5
313.15 0.5612 1243.4
313.15 0.6417 1214.0
313.15 0.7149 1188.0
313.15 0.7817 1164.7
313.15 0.8431 1143.9
313.15 0.8995 1125.3
313.15 0.9517 1108.7
313.15 1.0000 1094.03

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 95.5 (Liquid)

Mole fraction of Ethanol (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 473.75
0.0602 462.05
0.1145 449.95
0.2298 424.15
0.3005 410.35
0.3734 398.25
0.4720 384.95
0.5612 375.35
0.6417 368.25
0.7105 363.15
0.7818 358.85
0.9148 352.65
0.9504 351.45
1.0000 349.95

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 95.5 (Liquid)

Mole fraction of Ethanol (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 473.75
0.0602 462.05
0.1145 449.95
0.2298 424.15
0.3005 410.35
0.3734 398.25
0.4720 384.95
0.5612 375.35
0.6417 368.25
0.7105 363.15
0.7818 358.85
0.9148 352.65
0.9504 351.45
1.0000 349.95

Sources