Mixture of Phenol, 2-methyl- + Ethanol

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Phenol, 2-methyl-

Name
Phenol, 2-methyl-
InChI
InChI=1S/C7H8O/c1-6-4-2-3-5-7(6)8/h2-5,8H,1H3
InChI Key
QWVGKYWNOKOFNN-UHFFFAOYSA-N
Formula
C7H8O
SMILES
Cc1ccccc1O
Mol. Weight (g/mol)
108.14
CAS
95-48-7

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
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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 (4)

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

Operational conditions:

Mole fraction of Phenol, 2-methyl- (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1954 -1.112
0.4127 -1.6207
0.6007 -1.6522
0.8013 -0.9436

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

Operational conditions:

Mole fraction of Phenol, 2-methyl- (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1954 -1.112
0.4127 -1.6207
0.6007 -1.6522
0.8013 -0.9436

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 1037.02
303.15 0.1387 1015.95
303.15 0.2617 994.82
303.15 0.3713 973.68
303.15 0.4698 952.47
303.15 0.5586 931.22
303.15 0.6392 909.96
303.15 0.7127 888.59
303.15 0.7799 867.19
303.15 0.8417 845.72
303.15 0.8986 824.22
303.15 0.9510 802.69
303.15 1.0000 781.08
308.15 0.0000 1032.58
308.15 0.1387 1011.54
308.15 0.2617 990.39
308.15 0.3713 969.21
308.15 0.4698 947.97
308.15 0.5586 926.73
308.15 0.6392 905.45
308.15 0.7127 884.08
308.15 0.7799 862.71
308.15 0.8417 841.26
308.15 0.8986 819.77
308.15 0.9510 798.22
308.15 1.0000 776.59
313.15 0.0000 1028.19
313.15 0.1387 1007.18
313.15 0.2617 986.02
313.15 0.3713 964.81
313.15 0.4698 943.57
313.15 0.5586 922.33
313.15 0.6392 901.08
313.15 0.7127 879.74
313.15 0.7799 858.37
313.15 0.8417 836.92
313.15 0.8986 815.43
313.15 0.9510 793.89
313.15 1.0000 772.23
318.15 0.0000 1023.82
318.15 0.1387 1002.83
318.15 0.2617 981.62
318.15 0.3713 960.38
318.15 0.4698 939.1
318.15 0.5586 917.85
318.15 0.6392 896.59
318.15 0.7127 875.23
318.15 0.7799 853.88
318.15 0.8417 832.43
318.15 0.8986 810.91
318.15 0.9510 789.33
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 1037.02
303.15 0.1387 1015.95
303.15 0.2617 994.82
303.15 0.3713 973.68
303.15 0.4698 952.47
303.15 0.5586 931.22
303.15 0.6392 909.96
303.15 0.7127 888.59
303.15 0.7799 867.19
303.15 0.8417 845.72
303.15 0.8986 824.22
303.15 0.9510 802.69
303.15 1.0000 781.08
308.15 0.0000 1032.58
308.15 0.1387 1011.54
308.15 0.2617 990.39
308.15 0.3713 969.21
308.15 0.4698 947.97
308.15 0.5586 926.73
308.15 0.6392 905.45
308.15 0.7127 884.08
308.15 0.7799 862.71
308.15 0.8417 841.26
308.15 0.8986 819.77
308.15 0.9510 798.22
308.15 1.0000 776.59
313.15 0.0000 1028.19
313.15 0.1387 1007.18
313.15 0.2617 986.02
313.15 0.3713 964.81
313.15 0.4698 943.57
313.15 0.5586 922.33
313.15 0.6392 901.08
313.15 0.7127 879.74
313.15 0.7799 858.37
313.15 0.8417 836.92
313.15 0.8986 815.43
313.15 0.9510 793.89
313.15 1.0000 772.23
318.15 0.0000 1023.82
318.15 0.1387 1002.83
318.15 0.2617 981.62
318.15 0.3713 960.38
318.15 0.4698 939.1
318.15 0.5586 917.85
318.15 0.6392 896.59
318.15 0.7127 875.23
318.15 0.7799 853.88
318.15 0.8417 832.43
318.15 0.8986 810.91
318.15 0.9510 789.33
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 1488.12
303.15 0.1387 1435.4
303.15 0.2617 1391.2
303.15 0.3713 1351.2
303.15 0.4698 1314.2
303.15 0.5586 1280.2
303.15 0.6392 1249.3
303.15 0.7127 1221.5
303.15 0.7799 1196.9
303.15 0.8417 1175.2
303.15 0.8986 1156.5
303.15 0.9510 1140.6
303.15 1.0000 1127.01
313.15 0.0000 1453.02
313.15 0.1387 1401.2
313.15 0.2617 1355.4
313.15 0.3713 1314.6
313.15 0.4698 1277.9
313.15 0.5586 1245.0
313.15 0.6392 1215.3
313.15 0.7127 1188.6
313.15 0.7799 1164.8
313.15 0.8417 1143.6
313.15 0.8986 1124.8
313.15 0.9510 1108.4
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 1488.12
303.15 0.1387 1435.4
303.15 0.2617 1391.2
303.15 0.3713 1351.2
303.15 0.4698 1314.2
303.15 0.5586 1280.2
303.15 0.6392 1249.3
303.15 0.7127 1221.5
303.15 0.7799 1196.9
303.15 0.8417 1175.2
303.15 0.8986 1156.5
303.15 0.9510 1140.6
303.15 1.0000 1127.01
313.15 0.0000 1453.02
313.15 0.1387 1401.2
313.15 0.2617 1355.4
313.15 0.3713 1314.6
313.15 0.4698 1277.9
313.15 0.5586 1245.0
313.15 0.6392 1215.3
313.15 0.7127 1188.6
313.15 0.7799 1164.8
313.15 0.8417 1143.6
313.15 0.8986 1124.8
313.15 0.9510 1108.4
313.15 1.0000 1094.03

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 95.76 (Liquid)

Mole fraction of Ethanol (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 461.85
0.0512 434.85
0.1002 419.35
0.1505 408.15
0.1926 400.85
0.3003 387.15
0.4005 378.05
0.5003 370.85
0.6096 364.55
0.7002 360.15
0.8226 355.35
0.9003 352.85
0.9511 351.35
1.0000 350.05

Boiling temperature at pressure P, K [ref]

Fixed Measured
Pressure, kPa - Liquid Mole fraction of Phenol, 2-methyl- (1) - Liquid Boiling temperature at pressure P, K - Liquid
9.00 0.0970 302.23
9.00 0.2060 305.46
9.00 0.3040 308.67
9.00 0.3900 312.21
9.00 0.5070 319.01
9.00 0.5970 326.79
9.00 0.6990 333.07
9.00 0.7910 342.80
9.00 0.8980 359.99
15.00 0.0970 311.87
15.00 0.2060 315.32
15.00 0.3040 319.29
15.00 0.3900 322.19
15.00 0.5070 329.86
15.00 0.5970 336.50
15.00 0.6990 344.12
15.00 0.7910 354.31
15.00 0.8980 373.10
35.10 0.0970 329.36
35.10 0.2060 333.25
35.10 0.3040 337.22
35.10 0.3900 340.16
35.10 0.5070 348.90
35.10 0.5970 356.03
35.10 0.6990 363.84
35.10 0.7910 375.90
55.10 0.0970 339.54
55.10 0.2060 343.48
55.10 0.3040 347.87
55.10 0.3900 350.35
55.10 0.5070 360.29
55.10 0.5970 367.82
55.10 0.6990 376.33
55.10 0.7910 389.39
75.00 0.0970 346.85
75.00 0.2060 351.09
75.00 0.3040 355.53
75.00 0.3900 357.50
75.00 0.5070 368.40
75.00 0.5970 376.10
75.00 0.6990 385.84
85.10 0.0970 349.95
85.10 0.2060 354.17
85.10 0.3040 358.80
85.10 0.3900 360.75
85.10 0.5070 371.88
85.10 0.5970 379.52
85.10 0.6990 389.62
99.10 0.0970 353.75
97.70 0.2060 357.95
99.70 0.3040 363.05
99.90 0.3900 364.60
99.10 0.5070 374.97
98.50 0.5970 384.56
99.40 0.6990 394.11

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 95.76 (Liquid)

Mole fraction of Ethanol (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 461.85
0.0512 434.85
0.1002 419.35
0.1505 408.15
0.1926 400.85
0.3003 387.15
0.4005 378.05
0.5003 370.85
0.6096 364.55
0.7002 360.15
0.8226 355.35
0.9003 352.85
0.9511 351.35
1.0000 350.05

Boiling temperature at pressure P, K [ref]

Fixed Measured
Pressure, kPa - Liquid Mole fraction of Phenol, 2-methyl- (1) - Liquid Boiling temperature at pressure P, K - Liquid
9.00 0.0970 302.23
9.00 0.2060 305.46
9.00 0.3040 308.67
9.00 0.3900 312.21
9.00 0.5070 319.01
9.00 0.5970 326.79
9.00 0.6990 333.07
9.00 0.7910 342.80
9.00 0.8980 359.99
15.00 0.0970 311.87
15.00 0.2060 315.32
15.00 0.3040 319.29
15.00 0.3900 322.19
15.00 0.5070 329.86
15.00 0.5970 336.50
15.00 0.6990 344.12
15.00 0.7910 354.31
15.00 0.8980 373.10
35.10 0.0970 329.36
35.10 0.2060 333.25
35.10 0.3040 337.22
35.10 0.3900 340.16
35.10 0.5070 348.90
35.10 0.5970 356.03
35.10 0.6990 363.84
35.10 0.7910 375.90
55.10 0.0970 339.54
55.10 0.2060 343.48
55.10 0.3040 347.87
55.10 0.3900 350.35
55.10 0.5070 360.29
55.10 0.5970 367.82
55.10 0.6990 376.33
55.10 0.7910 389.39
75.00 0.0970 346.85
75.00 0.2060 351.09
75.00 0.3040 355.53
75.00 0.3900 357.50
75.00 0.5070 368.40
75.00 0.5970 376.10
75.00 0.6990 385.84
85.10 0.0970 349.95
85.10 0.2060 354.17
85.10 0.3040 358.80
85.10 0.3900 360.75
85.10 0.5070 371.88
85.10 0.5970 379.52
85.10 0.6990 389.62
99.10 0.0970 353.75
97.70 0.2060 357.95
99.70 0.3040 363.05
99.90 0.3900 364.60
99.10 0.5070 374.97
98.50 0.5970 384.56
99.40 0.6990 394.11

Sources