Mixture of 2-Propanol, 2-methyl- + Carbonic acid, dimethyl 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

Carbonic acid, dimethyl ester

Name
Carbonic acid, dimethyl ester
InChI
InChI=1S/C3H6O3/c1-5-3(4)6-2/h1-2H3
InChI Key
IEJIGPNLZYLLBP-UHFFFAOYSA-N
Formula
C3H6O3
SMILES
COC(=O)OC
Mol. Weight (g/mol)
90.08
CAS
616-38-6
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Datasets

  1. Excess molar enthalpy (molar enthalpy (2)
  2. Tboil - Boiling temperature at pressure P, K (2)

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

Operational condition: Pressure, kPa = 1000 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Carbonic acid, dimethyl ester (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15 0.0500 0.5360
298.15 0.1000 0.9932
298.15 0.1500 1.3757
298.15 0.2000 1.6901
298.15 0.2500 1.9583
298.15 0.3000 2.1605
298.15 0.3500 2.318
298.15 0.4000 2.4467
298.15 0.4500 2.5235
298.15 0.5000 2.5527
298.15 0.5500 2.5314
298.15 0.6000 2.4584
298.15 0.6500 2.3625
298.15 0.7000 2.2059
298.15 0.7500 1.9822
298.15 0.8000 1.7235
298.15 0.9000 1.0533
298.15 0.9500 0.5618
328.15 0.0500 0.5207
328.15 0.1000 0.9562
328.15 0.1500 1.3351
328.15 0.2000 1.6691
328.15 0.2500 1.9328
328.15 0.3000 2.1566
328.15 0.3500 2.3247
328.15 0.4000 2.4397
328.15 0.4500 2.5189
328.15 0.5000 2.5452
328.15 0.5500 2.5246
328.15 0.6000 2.4646
328.15 0.6500 2.3525
328.15 0.7000 2.1996
328.15 0.7500 1.9643
328.15 0.8000 1.7203
328.15 0.9000 1.0263
328.15 0.9500 0.5369

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

Operational condition: Pressure, kPa = 1000 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Carbonic acid, dimethyl ester (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15 0.0500 0.5360
298.15 0.1000 0.9932
298.15 0.1500 1.3757
298.15 0.2000 1.6901
298.15 0.2500 1.9583
298.15 0.3000 2.1605
298.15 0.3500 2.318
298.15 0.4000 2.4467
298.15 0.4500 2.5235
298.15 0.5000 2.5527
298.15 0.5500 2.5314
298.15 0.6000 2.4584
298.15 0.6500 2.3625
298.15 0.7000 2.2059
298.15 0.7500 1.9822
298.15 0.8000 1.7235
298.15 0.9000 1.0533
298.15 0.9500 0.5618
328.15 0.0500 0.5207
328.15 0.1000 0.9562
328.15 0.1500 1.3351
328.15 0.2000 1.6691
328.15 0.2500 1.9328
328.15 0.3000 2.1566
328.15 0.3500 2.3247
328.15 0.4000 2.4397
328.15 0.4500 2.5189
328.15 0.5000 2.5452
328.15 0.5500 2.5246
328.15 0.6000 2.4646
328.15 0.6500 2.3525
328.15 0.7000 2.1996
328.15 0.7500 1.9643
328.15 0.8000 1.7203
328.15 0.9000 1.0263
328.15 0.9500 0.5369

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 95.8 (Liquid)

Mole fraction of 2-Propanol, 2-methyl- (1) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 361.25
0.1510 355.95
0.2630 353.95
0.3430 353.05
0.4162 352.35
0.5510 351.95
0.6200 351.85
0.7101 351.95
0.8302 352.35
0.9072 352.95
1.0000 353.15

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 95.8 (Liquid)

Mole fraction of 2-Propanol, 2-methyl- (1) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 361.25
0.1510 355.95
0.2630 353.95
0.3430 353.05
0.4162 352.35
0.5510 351.95
0.6200 351.85
0.7101 351.95
0.8302 352.35
0.9072 352.95
1.0000 353.15

Sources