Mixture of 2-Propanol, 2-methyl- + Butanoic acid, methyl ester

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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

Butanoic acid, methyl ester

Name
Butanoic acid, methyl ester
InChI
InChI=1S/C5H10O2/c1-3-4-5(6)7-2/h3-4H2,1-2H3
InChI Key
UUIQMZJEGPQKFD-UHFFFAOYSA-N
Formula
C5H10O2
SMILES
CCCC(=O)OC
Mol. Weight (g/mol)
102.13
CAS
623-42-7
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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 Butanoic acid, methyl ester (2) [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Mole fraction of Butanoic acid, methyl ester (2) - Liquid Mole fraction of Butanoic acid, methyl ester (2) - Gas
0.0112 0.0080
0.0426 0.0310
0.0786 0.0577
0.1092 0.0801
0.1403 0.1017
0.1813 0.1298
0.2134 0.1527
0.2561 0.1810
0.3012 0.2101
0.3356 0.2335
0.3655 0.2539
0.4077 0.2789
0.4505 0.3085
0.4825 0.3328
0.5237 0.3614
0.5633 0.3925
0.6019 0.4239
0.6401 0.4537
0.6664 0.4781
0.6915 0.5035
0.7208 0.5326
0.7409 0.5542
0.7674 0.5845
0.7693 0.5864
0.7881 0.6085
0.7939 0.6147
0.8135 0.6418
0.8303 0.6650
0.8449 0.6857
0.8586 0.7063
0.8767 0.7331
0.8961 0.7698
0.9136 0.8016
0.9335 0.8411
0.9505 0.8779
0.9676 0.9175
0.9809 0.9505

Mole fraction of Butanoic acid, methyl ester (2) [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Mole fraction of Butanoic acid, methyl ester (2) - Liquid Mole fraction of Butanoic acid, methyl ester (2) - Gas
0.0112 0.0080
0.0426 0.0310
0.0786 0.0577
0.1092 0.0801
0.1403 0.1017
0.1813 0.1298
0.2134 0.1527
0.2561 0.1810
0.3012 0.2101
0.3356 0.2335
0.3655 0.2539
0.4077 0.2789
0.4505 0.3085
0.4825 0.3328
0.5237 0.3614
0.5633 0.3925
0.6019 0.4239
0.6401 0.4537
0.6664 0.4781
0.6915 0.5035
0.7208 0.5326
0.7409 0.5542
0.7674 0.5845
0.7693 0.5864
0.7881 0.6085
0.7939 0.6147
0.8135 0.6418
0.8303 0.6650
0.8449 0.6857
0.8586 0.7063
0.8767 0.7331
0.8961 0.7698
0.9136 0.8016
0.9335 0.8411
0.9505 0.8779
0.9676 0.9175
0.9809 0.9505

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 Butanoic acid, methyl ester (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
299.15 0.0487 0.3278
299.15 0.1046 0.6598
299.15 0.1632 0.9792
299.15 0.2233 1.2519
299.15 0.2830 1.4698
299.15 0.3383 1.6272
299.15 0.3915 1.7368
299.15 0.4395 1.8021
299.15 0.4853 1.8378
299.15 0.5221 1.844
299.15 0.5268 1.8469
299.15 0.5545 1.8377
299.15 0.5745 1.8296
299.15 0.6360 1.7437
299.15 0.7063 1.5873
299.15 0.7780 1.3525
299.15 0.8552 1.0059
299.15 0.9325 0.5399
318.15 0.0458 0.2920
318.15 0.1000 0.5896
318.15 0.1556 0.8653
318.15 0.2136 1.1453
318.15 0.2734 1.3753
318.15 0.3313 1.5465
318.15 0.3854 1.6771
318.15 0.4221 1.738
318.15 0.4655 1.7855
318.15 0.5127 1.8039
318.15 0.5632 1.7953
318.15 0.6217 1.7397
318.15 0.6845 1.625
318.15 0.7505 1.4409
318.15 0.8187 1.1714
318.15 0.8840 0.8154
318.15 0.9472 0.4257

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 Butanoic acid, methyl ester (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
299.15 0.0487 0.3278
299.15 0.1046 0.6598
299.15 0.1632 0.9792
299.15 0.2233 1.2519
299.15 0.2830 1.4698
299.15 0.3383 1.6272
299.15 0.3915 1.7368
299.15 0.4395 1.8021
299.15 0.4853 1.8378
299.15 0.5221 1.844
299.15 0.5268 1.8469
299.15 0.5545 1.8377
299.15 0.5745 1.8296
299.15 0.6360 1.7437
299.15 0.7063 1.5873
299.15 0.7780 1.3525
299.15 0.8552 1.0059
299.15 0.9325 0.5399
318.15 0.0458 0.2920
318.15 0.1000 0.5896
318.15 0.1556 0.8653
318.15 0.2136 1.1453
318.15 0.2734 1.3753
318.15 0.3313 1.5465
318.15 0.3854 1.6771
318.15 0.4221 1.738
318.15 0.4655 1.7855
318.15 0.5127 1.8039
318.15 0.5632 1.7953
318.15 0.6217 1.7397
318.15 0.6845 1.625
318.15 0.7505 1.4409
318.15 0.8187 1.1714
318.15 0.8840 0.8154
318.15 0.9472 0.4257

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Mole fraction of Butanoic acid, methyl ester (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0112 355.66
0.0426 355.80
0.0786 356.04
0.1092 356.28
0.1403 356.46
0.1813 356.79
0.2134 357.11
0.2561 357.53
0.3012 358.01
0.3356 358.37
0.3655 358.72
0.4077 359.08
0.4505 359.58
0.4825 360.00
0.5237 360.58
0.5633 361.19
0.6019 361.92
0.6401 362.56
0.6664 363.16
0.6915 363.81
0.7208 364.40
0.7409 364.91
0.7674 365.72
0.7693 365.91
0.7881 366.34
0.7939 366.51
0.8135 367.09
0.8303 367.62
0.8449 368.07
0.8586 368.62
0.8767 369.29
0.8961 370.07
0.9136 370.80
0.9335 371.61
0.9505 372.40
0.9676 373.29
0.9809 373.94

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Mole fraction of Butanoic acid, methyl ester (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0112 355.66
0.0426 355.80
0.0786 356.04
0.1092 356.28
0.1403 356.46
0.1813 356.79
0.2134 357.11
0.2561 357.53
0.3012 358.01
0.3356 358.37
0.3655 358.72
0.4077 359.08
0.4505 359.58
0.4825 360.00
0.5237 360.58
0.5633 361.19
0.6019 361.92
0.6401 362.56
0.6664 363.16
0.6915 363.81
0.7208 364.40
0.7409 364.91
0.7674 365.72
0.7693 365.91
0.7881 366.34
0.7939 366.51
0.8135 367.09
0.8303 367.62
0.8449 368.07
0.8586 368.62
0.8767 369.29
0.8961 370.07
0.9136 370.80
0.9335 371.61
0.9505 372.40
0.9676 373.29
0.9809 373.94

Excess molar volume, m3/mol [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Butanoic acid, methyl ester (2) - Liquid Excess molar volume, m3/mol - Liquid
303.15 0.0628 1.6000e-07
303.15 0.0928 2.3600e-07
303.15 0.1566 3.6800e-07
303.15 0.1940 4.3000e-07
303.15 0.2507 5.0700e-07
303.15 0.3088 5.6900e-07
303.15 0.3502 6.0400e-07
303.15 0.3916 6.3000e-07
303.15 0.4530 6.4900e-07
303.15 0.5059 6.5100e-07
303.15 0.5463 6.4000e-07
303.15 0.6022 6.1700e-07
303.15 0.6588 5.7100e-07
303.15 0.6980 5.3700e-07
303.15 0.7527 4.7300e-07
303.15 0.7928 4.2000e-07
303.15 0.8510 3.2100e-07
303.15 0.9115 2.0600e-07
303.15 0.9420 1.4000e-07
318.15 0.1079 2.3500e-07
318.15 0.1326 2.9100e-07
318.15 0.1749 3.6800e-07
318.15 0.2201 4.3400e-07
318.15 0.2751 5.0300e-07
318.15 0.3257 5.5400e-07
318.15 0.3949 6.0500e-07
318.15 0.4521 6.3000e-07
318.15 0.4783 6.3600e-07
318.15 0.5500 6.3100e-07
318.15 0.5996 6.1600e-07
318.15 0.6675 5.7400e-07
318.15 0.7318 5.2400e-07
318.15 0.8163 4.0400e-07
318.15 0.8728 3.1700e-07

Excess molar volume, m3/mol [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Butanoic acid, methyl ester (2) - Liquid Excess molar volume, m3/mol - Liquid
303.15 0.0628 1.6000e-07
303.15 0.0928 2.3600e-07
303.15 0.1566 3.6800e-07
303.15 0.1940 4.3000e-07
303.15 0.2507 5.0700e-07
303.15 0.3088 5.6900e-07
303.15 0.3502 6.0400e-07
303.15 0.3916 6.3000e-07
303.15 0.4530 6.4900e-07
303.15 0.5059 6.5100e-07
303.15 0.5463 6.4000e-07
303.15 0.6022 6.1700e-07
303.15 0.6588 5.7100e-07
303.15 0.6980 5.3700e-07
303.15 0.7527 4.7300e-07
303.15 0.7928 4.2000e-07
303.15 0.8510 3.2100e-07
303.15 0.9115 2.0600e-07
303.15 0.9420 1.4000e-07
318.15 0.1079 2.3500e-07
318.15 0.1326 2.9100e-07
318.15 0.1749 3.6800e-07
318.15 0.2201 4.3400e-07
318.15 0.2751 5.0300e-07
318.15 0.3257 5.5400e-07
318.15 0.3949 6.0500e-07
318.15 0.4521 6.3000e-07
318.15 0.4783 6.3600e-07
318.15 0.5500 6.3100e-07
318.15 0.5996 6.1600e-07
318.15 0.6675 5.7400e-07
318.15 0.7318 5.2400e-07
318.15 0.8163 4.0400e-07
318.15 0.8728 3.1700e-07

Sources