Mixture of Acetic acid, pentyl ester + Heptane

Excel

Acetic acid, pentyl ester

Name
Acetic acid, pentyl ester
InChI
InChI=1S/C7H14O2/c1-3-4-5-6-9-7(2)8/h3-6H2,1-2H3
InChI Key
PGMYKACGEOXYJE-UHFFFAOYSA-N
Formula
C7H14O2
SMILES
CCCCCOC(C)=O
Mol. Weight (g/mol)
130.18
CAS
628-63-7

Heptane

Name
Heptane
InChI
InChI=1S/C7H16/c1-3-5-7-6-4-2/h3-7H2,1-2H3
InChI Key
IMNFDUFMRHMDMM-UHFFFAOYSA-N
Formula
C7H16
SMILES
CCCCCCC
Mol. Weight (g/mol)
100.20
CAS
142-82-5
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry. Do not hesitate to contact us for your projects.

Datasets

  1. Activity coefficient (2)
  2. Excess molar enthalpy (molar enthalpy (2)
  3. γ - Surface tension liquid-gas, N/m (2)
  4. Excess molar volume, m3/mol (2)

Activity coefficient of Heptane (2) [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of Heptane (2) - Liquid Pressure, kPa - Liquid Activity coefficient of Heptane (2) - Liquid
298.15 0.0000 101.33 1.9

Activity coefficient of Heptane (2) [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of Heptane (2) - Liquid Pressure, kPa - Liquid Activity coefficient of Heptane (2) - Liquid
298.15 0.0000 101.33 1.9

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

Operational conditions:

Mole fraction of Acetic acid, pentyl ester (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0544 0.2370
0.1187 0.4341
0.1801 0.5913
0.2428 0.7059
0.3049 0.8030
0.3645 0.8569
0.4174 0.8828
0.4680 0.8869
0.4720 0.8859
0.5161 0.8764
0.5646 0.8477
0.6163 0.8006
0.6696 0.7373
0.7277 0.6496
0.7889 0.5338
0.8473 0.4040
0.9078 0.2572
0.9594 0.1162

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

Operational conditions:

Mole fraction of Acetic acid, pentyl ester (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0544 0.2370
0.1187 0.4341
0.1801 0.5913
0.2428 0.7059
0.3049 0.8030
0.3645 0.8569
0.4174 0.8828
0.4680 0.8869
0.4720 0.8859
0.5161 0.8764
0.5646 0.8477
0.6163 0.8006
0.6696 0.7373
0.7277 0.6496
0.7889 0.5338
0.8473 0.4040
0.9078 0.2572
0.9594 0.1162

Surface tension liquid-gas, N/m [ref]

Operational condition: Temperature, K = 298.15 (Liquid)

Mole fraction of Heptane (2) - Liquid Surface tension liquid-gas, N/m - Liquid
0.0521 0.0255
0.1046 0.0250
0.1515 0.0245
0.2070 0.0242
0.2557 0.0238
0.3087 0.0234
0.3546 0.0231
0.4072 0.0227
0.4518 0.0225
0.5075 0.0221
0.5529 0.0219
0.6072 0.0216
0.6547 0.0214
0.7086 0.0211
0.7556 0.0208
0.8047 0.0206
0.8567 0.0204
0.9000 0.0203

Surface tension liquid-gas, N/m [ref]

Operational condition: Temperature, K = 298.15 (Liquid)

Mole fraction of Heptane (2) - Liquid Surface tension liquid-gas, N/m - Liquid
0.0521 0.0255
0.1046 0.0250
0.1515 0.0245
0.2070 0.0242
0.2557 0.0238
0.3087 0.0234
0.3546 0.0231
0.4072 0.0227
0.4518 0.0225
0.5075 0.0221
0.5529 0.0219
0.6072 0.0216
0.6547 0.0214
0.7086 0.0211
0.7556 0.0208
0.8047 0.0206
0.8567 0.0204
0.9000 0.0203

Excess molar volume, m3/mol [ref]

Operational conditions:

Mole fraction of Acetic acid, pentyl ester (1) - Liquid Excess molar volume, m3/mol - Liquid
0.0546 1.2900e-07
0.1048 2.1400e-07
0.1515 2.6500e-07
0.2014 3.0700e-07
0.2488 3.4500e-07
0.3009 3.8100e-07
0.3474 3.9900e-07
0.3999 4.1100e-07
0.4426 4.0900e-07
0.4977 3.9700e-07
0.5503 3.7200e-07
0.5881 3.5500e-07
0.6360 3.2300e-07
0.7502 2.5100e-07
0.8467 1.7100e-07
0.9288 9.4000e-08

Excess molar volume, m3/mol [ref]

Operational conditions:

Mole fraction of Acetic acid, pentyl ester (1) - Liquid Excess molar volume, m3/mol - Liquid
0.0546 1.2900e-07
0.1048 2.1400e-07
0.1515 2.6500e-07
0.2014 3.0700e-07
0.2488 3.4500e-07
0.3009 3.8100e-07
0.3474 3.9900e-07
0.3999 4.1100e-07
0.4426 4.0900e-07
0.4977 3.9700e-07
0.5503 3.7200e-07
0.5881 3.5500e-07
0.6360 3.2300e-07
0.7502 2.5100e-07
0.8467 1.7100e-07
0.9288 9.4000e-08

Sources