Mixture of 2-Propanol, 2-methyl- + Methyl propionate

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2-Propanol, 2-methyl-

Name
2-Propanol, 2-methyl-
InChI
InChI=1S/C4H10O/c1-4(2,3)5/h5H,1-3H3
InChI Key
DKGAVHZHDRPRBM-UHFFFAOYSA-N
Formula
C4H10O
SMILES
CC(C)(C)O
Mol. Weight (g/mol)
74.12
CAS
75-65-0

Methyl propionate

Name
Methyl propionate
InChI
InChI=1S/C4H8O2/c1-3-4(5)6-2/h3H2,1-2H3
InChI Key
RJUFJBKOKNCXHH-UHFFFAOYSA-N
Formula
C4H8O2
SMILES
CCC(=O)OC
Mol. Weight (g/mol)
88.11
CAS
554-12-1
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Datasets

  1. Mole fraction (2)
  2. Excess molar enthalpy (molar enthalpy (2)
  3. Tboil - Boiling temperature at pressure P, K (2)
  4. Excess molar volume, m3/mol (2)

Mole fraction of Methyl propionate (2) [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Mole fraction of Methyl propionate (2) - Liquid Mole fraction of Methyl propionate (2) - Gas
0.0220 0.0314
0.0433 0.0614
0.0609 0.0854
0.0748 0.1041
0.0901 0.1235
0.0924 0.1270
0.1043 0.1436
0.1146 0.1568
0.1332 0.1781
0.1359 0.1819
0.1597 0.2115
0.1879 0.2451
0.2014 0.2609
0.2120 0.2729
0.2371 0.3001
0.2484 0.3112
0.2690 0.3332
0.2821 0.3469
0.2975 0.3623
0.3228 0.3877
0.3465 0.4106
0.3773 0.4396
0.4024 0.4626
0.4401 0.4965
0.4715 0.5218
0.4965 0.5448
0.5299 0.5699
0.5566 0.5927
0.5792 0.6111
0.6053 0.6326
0.6341 0.6551
0.6617 0.6775
0.6864 0.6969
0.7162 0.7193
0.7365 0.7345
0.7506 0.7446
0.7676 0.7579
0.7755 0.7642
0.7809 0.7692
0.7983 0.7832
0.8278 0.8098
0.8892 0.8710
0.9099 0.8926
0.9464 0.9336
0.9583 0.9476
0.9753 0.9684

Mole fraction of Methyl propionate (2) [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Mole fraction of Methyl propionate (2) - Liquid Mole fraction of Methyl propionate (2) - Gas
0.0220 0.0314
0.0433 0.0614
0.0609 0.0854
0.0748 0.1041
0.0901 0.1235
0.0924 0.1270
0.1043 0.1436
0.1146 0.1568
0.1332 0.1781
0.1359 0.1819
0.1597 0.2115
0.1879 0.2451
0.2014 0.2609
0.2120 0.2729
0.2371 0.3001
0.2484 0.3112
0.2690 0.3332
0.2821 0.3469
0.2975 0.3623
0.3228 0.3877
0.3465 0.4106
0.3773 0.4396
0.4024 0.4626
0.4401 0.4965
0.4715 0.5218
0.4965 0.5448
0.5299 0.5699
0.5566 0.5927
0.5792 0.6111
0.6053 0.6326
0.6341 0.6551
0.6617 0.6775
0.6864 0.6969
0.7162 0.7193
0.7365 0.7345
0.7506 0.7446
0.7676 0.7579
0.7755 0.7642
0.7809 0.7692
0.7983 0.7832
0.8278 0.8098
0.8892 0.8710
0.9099 0.8926
0.9464 0.9336
0.9583 0.9476
0.9753 0.9684

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

Operational condition: Pressure, kPa = 101.32 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Methyl propionate (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
299.15 0.0603 0.4195
299.15 0.1414 0.8898
299.15 0.2285 1.3268
299.15 0.3164 1.6535
299.15 0.3971 1.8511
299.15 0.4573 1.9286
299.15 0.4705 1.9394
299.15 0.5159 1.9522
299.15 0.5343 1.9439
299.15 0.5899 1.8955
299.15 0.6328 1.8205
299.15 0.6447 1.7921
299.15 0.7116 1.6194
299.15 0.7778 1.3709
299.15 0.8496 1.019
299.15 0.9351 0.4815
318.15 0.0486 0.3261
318.15 0.1007 0.6391
318.15 0.1707 1.0034
318.15 0.2374 1.2986
318.15 0.3021 1.5231
318.15 0.3578 1.6747
318.15 0.4076 1.779
318.15 0.4404 1.838
318.15 0.4827 1.8619
318.15 0.5312 1.8831
318.15 0.5820 1.8465
318.15 0.6358 1.7688
318.15 0.6986 1.6462
318.15 0.7666 1.4054
318.15 0.8289 1.138
318.15 0.8931 0.7910
318.15 0.9582 0.3913

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

Operational condition: Pressure, kPa = 101.32 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Methyl propionate (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
299.15 0.0603 0.4195
299.15 0.1414 0.8898
299.15 0.2285 1.3268
299.15 0.3164 1.6535
299.15 0.3971 1.8511
299.15 0.4573 1.9286
299.15 0.4705 1.9394
299.15 0.5159 1.9522
299.15 0.5343 1.9439
299.15 0.5899 1.8955
299.15 0.6328 1.8205
299.15 0.6447 1.7921
299.15 0.7116 1.6194
299.15 0.7778 1.3709
299.15 0.8496 1.019
299.15 0.9351 0.4815
318.15 0.0486 0.3261
318.15 0.1007 0.6391
318.15 0.1707 1.0034
318.15 0.2374 1.2986
318.15 0.3021 1.5231
318.15 0.3578 1.6747
318.15 0.4076 1.779
318.15 0.4404 1.838
318.15 0.4827 1.8619
318.15 0.5312 1.8831
318.15 0.5820 1.8465
318.15 0.6358 1.7688
318.15 0.6986 1.6462
318.15 0.7666 1.4054
318.15 0.8289 1.138
318.15 0.8931 0.7910
318.15 0.9582 0.3913

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Mole fraction of Methyl propionate (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0220 355.33
0.0433 355.00
0.0609 354.76
0.0748 354.56
0.0901 354.38
0.0924 354.34
0.1043 354.20
0.1146 354.07
0.1332 353.84
0.1359 353.82
0.1597 353.52
0.1879 353.21
0.2014 353.07
0.2120 352.96
0.2371 352.70
0.2484 352.56
0.2690 352.34
0.2821 352.24
0.2975 352.11
0.3228 351.88
0.3465 351.70
0.3773 351.47
0.4024 351.31
0.4401 351.07
0.4715 350.91
0.4965 350.78
0.5299 350.66
0.5566 350.57
0.5792 350.54
0.6053 350.51
0.6341 350.48
0.6617 350.45
0.6864 350.44
0.7162 350.43
0.7365 350.47
0.7506 350.52
0.7676 350.58
0.7755 350.60
0.7809 350.61
0.7983 350.67
0.8278 350.77
0.8892 351.03
0.9099 351.11
0.9464 351.32
0.9583 351.42
0.9753 351.50

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Mole fraction of Methyl propionate (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0220 355.33
0.0433 355.00
0.0609 354.76
0.0748 354.56
0.0901 354.38
0.0924 354.34
0.1043 354.20
0.1146 354.07
0.1332 353.84
0.1359 353.82
0.1597 353.52
0.1879 353.21
0.2014 353.07
0.2120 352.96
0.2371 352.70
0.2484 352.56
0.2690 352.34
0.2821 352.24
0.2975 352.11
0.3228 351.88
0.3465 351.70
0.3773 351.47
0.4024 351.31
0.4401 351.07
0.4715 350.91
0.4965 350.78
0.5299 350.66
0.5566 350.57
0.5792 350.54
0.6053 350.51
0.6341 350.48
0.6617 350.45
0.6864 350.44
0.7162 350.43
0.7365 350.47
0.7506 350.52
0.7676 350.58
0.7755 350.60
0.7809 350.61
0.7983 350.67
0.8278 350.77
0.8892 351.03
0.9099 351.11
0.9464 351.32
0.9583 351.42
0.9753 351.50

Excess molar volume, m3/mol [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Methyl propionate (2) - Liquid Excess molar volume, m3/mol - Liquid
303.15 0.0517 1.5200e-07
303.15 0.1081 2.9300e-07
303.15 0.1525 3.8800e-07
303.15 0.2020 4.7100e-07
303.15 0.2516 5.4300e-07
303.15 0.3129 6.1000e-07
303.15 0.3638 6.4800e-07
303.15 0.4060 6.6700e-07
303.15 0.4603 6.7800e-07
303.15 0.5167 6.7900e-07
303.15 0.5558 6.6800e-07
303.15 0.6086 6.4100e-07
303.15 0.6546 6.0700e-07
303.15 0.7197 5.4300e-07
303.15 0.7520 4.9100e-07
303.15 0.8122 4.1500e-07
303.15 0.8545 3.4800e-07
303.15 0.9065 2.5300e-07
303.15 0.9394 1.7300e-07
318.15 0.0750 1.9400e-07
318.15 0.1476 3.1500e-07
318.15 0.1952 4.1600e-07
318.15 0.2636 4.9800e-07
318.15 0.3159 5.5900e-07
318.15 0.3628 6.0600e-07
318.15 0.4165 6.3900e-07
318.15 0.4931 6.4800e-07
318.15 0.5472 6.4100e-07
318.15 0.6296 6.0900e-07
318.15 0.6429 5.8700e-07
318.15 0.7013 5.4100e-07
318.15 0.7950 4.2700e-07
318.15 0.8267 3.6800e-07
318.15 0.8822 2.8100e-07
318.15 0.9493 1.3900e-07

Excess molar volume, m3/mol [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Methyl propionate (2) - Liquid Excess molar volume, m3/mol - Liquid
303.15 0.0517 1.5200e-07
303.15 0.1081 2.9300e-07
303.15 0.1525 3.8800e-07
303.15 0.2020 4.7100e-07
303.15 0.2516 5.4300e-07
303.15 0.3129 6.1000e-07
303.15 0.3638 6.4800e-07
303.15 0.4060 6.6700e-07
303.15 0.4603 6.7800e-07
303.15 0.5167 6.7900e-07
303.15 0.5558 6.6800e-07
303.15 0.6086 6.4100e-07
303.15 0.6546 6.0700e-07
303.15 0.7197 5.4300e-07
303.15 0.7520 4.9100e-07
303.15 0.8122 4.1500e-07
303.15 0.8545 3.4800e-07
303.15 0.9065 2.5300e-07
303.15 0.9394 1.7300e-07
318.15 0.0750 1.9400e-07
318.15 0.1476 3.1500e-07
318.15 0.1952 4.1600e-07
318.15 0.2636 4.9800e-07
318.15 0.3159 5.5900e-07
318.15 0.3628 6.0600e-07
318.15 0.4165 6.3900e-07
318.15 0.4931 6.4800e-07
318.15 0.5472 6.4100e-07
318.15 0.6296 6.0900e-07
318.15 0.6429 5.8700e-07
318.15 0.7013 5.4100e-07
318.15 0.7950 4.2700e-07
318.15 0.8267 3.6800e-07
318.15 0.8822 2.8100e-07
318.15 0.9493 1.3900e-07

Sources