Mixture of 2,3-Butanediol + Methyl Alcohol

Excel

2,3-Butanediol

Name
2,3-Butanediol
InChI
InChI=1S/C4H10O2/c1-3(5)4(2)6/h3-6H,1-2H3
InChI Key
OWBTYPJTUOEWEK-UHFFFAOYSA-N
Formula
C4H10O2
SMILES
CC(O)C(C)O
Mol. Weight (g/mol)
90.12
CAS
513-85-9

Methyl Alcohol

Name
Methyl Alcohol
InChI
InChI=1S/CH4O/c1-2/h2H,1H3
InChI Key
OKKJLVBELUTLKV-UHFFFAOYSA-N
Formula
CH4O
SMILES
CO
Mol. Weight (g/mol)
32.04
CAS
67-56-1
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Datasets

  1. Cp,liquid - Molar heat capacity at constant pressure, J/K/mol (2)

Molar heat capacity at constant pressure, J/K/mol [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 2,3-Butanediol (1) - Liquid Molar heat capacity at constant pressure, J/K/mol - Liquid
293.15 0.0000 80.46
293.15 0.0456 86.73
293.15 0.0847 92.44
293.15 0.1972 108.82
293.15 0.2792 121.32
293.15 0.3824 136.66
293.15 0.4673 150.38
293.15 0.5862 168.13
293.15 0.7041 186.64
293.15 0.8094 441.97
293.15 0.8169 204.52
293.15 0.8832 214.76
293.15 0.9271 221.76
293.15 0.9501 225.38
293.15 1.0000 233.95
298.15 0.0000 81.39
298.15 0.0456 87.80
298.15 0.0847 93.66
298.15 0.1972 110.30
298.15 0.2792 122.96
298.15 0.3824 138.56
298.15 0.4673 152.39
298.15 0.5862 170.37
298.15 0.7041 189.05
298.15 0.8094 448.38
298.15 0.8169 207.14
298.15 0.8832 217.34
298.15 0.9271 224.59
298.15 0.9501 228.00
298.15 1.0000 236.66
303.15 0.0000 82.38
303.15 0.0456 88.95
303.15 0.0847 94.92
303.15 0.1972 111.78
303.15 0.2792 124.65
303.15 0.3824 140.46
303.15 0.4673 154.41
303.15 0.5862 172.69
303.15 0.7041 191.46
303.15 0.8094 455.02
303.15 0.8169 209.84
303.15 0.8832 220.01
303.15 0.9271 227.34
303.15 0.9501 230.70
303.15 1.0000 239.36
308.15 0.0000 83.44
308.15 0.0456 90.13
308.15 0.0847 96.21
308.15 0.1972 113.35
308.15 0.2792 126.34
308.15 0.3824 142.41
308.15 0.4673 156.48
308.15 0.5862 174.93
308.15 0.7041 193.94
308.15 0.8094 461.66
308.15 0.8169 212.55
308.15 0.8832 222.68
308.15 0.9271 230.18
308.15 0.9501 233.32
308.15 1.0000 242.07
313.15 0.0000 84.56
313.15 0.0456 91.37
313.15 0.0847 97.54
313.15 0.1972 114.96
313.15 0.2792 128.08
313.15 0.3824 144.36
313.15 0.4673 158.55
313.15 0.5862 177.25
313.15 0.7041 196.41
313.15 0.8094 468.54
313.15 0.8169 215.17
313.15 0.8832 225.26
313.15 0.9271 233.01
313.15 0.9501 236.11
313.15 1.0000 244.77
318.15 0.0000 85.78
318.15 0.0456 92.66
318.15 0.0847 98.95
318.15 0.1972 116.61
318.15 0.2792 129.81
318.15 0.3824 146.37
318.15 0.4673 160.68
318.15 0.5862 179.63
318.15 0.7041 198.89
318.15 0.8094 475.41
318.15 0.8169 217.87
318.15 0.8832 227.93
318.15 0.9271 235.93
318.15 0.9501 238.82
318.15 1.0000 247.47
323.15 0.0000 87.03
323.15 0.0456 94.01
323.15 0.0847 100.35
323.15 0.1972 118.31
323.15 0.2792 131.60
323.15 0.3824 148.43
323.15 0.4673 162.81
323.15 0.5862 182.01
323.15 0.7041 201.45
323.15 0.8094 482.53
323.15 0.8169 220.58
323.15 0.8832 230.59
323.15 0.9271 238.77
323.15 0.9501 241.61
323.15 1.0000 250.18

Molar heat capacity at constant pressure, J/K/mol [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 2,3-Butanediol (1) - Liquid Molar heat capacity at constant pressure, J/K/mol - Liquid
293.15 0.0000 80.46
293.15 0.0456 86.73
293.15 0.0847 92.44
293.15 0.1972 108.82
293.15 0.2792 121.32
293.15 0.3824 136.66
293.15 0.4673 150.38
293.15 0.5862 168.13
293.15 0.7041 186.64
293.15 0.8094 441.97
293.15 0.8169 204.52
293.15 0.8832 214.76
293.15 0.9271 221.76
293.15 0.9501 225.38
293.15 1.0000 233.95
298.15 0.0000 81.39
298.15 0.0456 87.80
298.15 0.0847 93.66
298.15 0.1972 110.30
298.15 0.2792 122.96
298.15 0.3824 138.56
298.15 0.4673 152.39
298.15 0.5862 170.37
298.15 0.7041 189.05
298.15 0.8094 448.38
298.15 0.8169 207.14
298.15 0.8832 217.34
298.15 0.9271 224.59
298.15 0.9501 228.00
298.15 1.0000 236.66
303.15 0.0000 82.38
303.15 0.0456 88.95
303.15 0.0847 94.92
303.15 0.1972 111.78
303.15 0.2792 124.65
303.15 0.3824 140.46
303.15 0.4673 154.41
303.15 0.5862 172.69
303.15 0.7041 191.46
303.15 0.8094 455.02
303.15 0.8169 209.84
303.15 0.8832 220.01
303.15 0.9271 227.34
303.15 0.9501 230.70
303.15 1.0000 239.36
308.15 0.0000 83.44
308.15 0.0456 90.13
308.15 0.0847 96.21
308.15 0.1972 113.35
308.15 0.2792 126.34
308.15 0.3824 142.41
308.15 0.4673 156.48
308.15 0.5862 174.93
308.15 0.7041 193.94
308.15 0.8094 461.66
308.15 0.8169 212.55
308.15 0.8832 222.68
308.15 0.9271 230.18
308.15 0.9501 233.32
308.15 1.0000 242.07
313.15 0.0000 84.56
313.15 0.0456 91.37
313.15 0.0847 97.54
313.15 0.1972 114.96
313.15 0.2792 128.08
313.15 0.3824 144.36
313.15 0.4673 158.55
313.15 0.5862 177.25
313.15 0.7041 196.41
313.15 0.8094 468.54
313.15 0.8169 215.17
313.15 0.8832 225.26
313.15 0.9271 233.01
313.15 0.9501 236.11
313.15 1.0000 244.77
318.15 0.0000 85.78
318.15 0.0456 92.66
318.15 0.0847 98.95
318.15 0.1972 116.61
318.15 0.2792 129.81
318.15 0.3824 146.37
318.15 0.4673 160.68
318.15 0.5862 179.63
318.15 0.7041 198.89
318.15 0.8094 475.41
318.15 0.8169 217.87
318.15 0.8832 227.93
318.15 0.9271 235.93
318.15 0.9501 238.82
318.15 1.0000 247.47
323.15 0.0000 87.03
323.15 0.0456 94.01
323.15 0.0847 100.35
323.15 0.1972 118.31
323.15 0.2792 131.60
323.15 0.3824 148.43
323.15 0.4673 162.81
323.15 0.5862 182.01
323.15 0.7041 201.45
323.15 0.8094 482.53
323.15 0.8169 220.58
323.15 0.8832 230.59
323.15 0.9271 238.77
323.15 0.9501 241.61
323.15 1.0000 250.18

Sources