Mixture of Triethylamine + 1-Butanol

Excel

Triethylamine

Name
Triethylamine
InChI
InChI=1S/C6H15N/c1-4-7(5-2)6-3/h4-6H2,1-3H3
InChI Key
ZMANZCXQSJIPKH-UHFFFAOYSA-N
Formula
C6H15N
SMILES
CCN(CC)CC
Mol. Weight (g/mol)
101.19
CAS
121-44-8

1-Butanol

Name
1-Butanol
InChI
InChI=1S/C4H10O/c1-2-3-4-5/h5H,2-4H2,1H3
InChI Key
LRHPLDYGYMQRHN-UHFFFAOYSA-N
Formula
C4H10O
SMILES
CCCCO
Mol. Weight (g/mol)
74.12
CAS
71-36-3
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Datasets

  1. η - Viscosity, Pa*s (2)
  2. Excess molar enthalpy (molar enthalpy (2)
  3. Excess molar volume, m3/mol (2)

Viscosity, Pa*s [ref]

Operational conditions:

Molality, mol/kg of Triethylamine (1) - Liquid Viscosity, Pa*s - Liquid
0.1482 0.0022
0.3064 0.0022
0.4546 0.0022
0.5880 0.0021
0.7471 0.0021
0.8993 0.0021
1.0564 0.0021
1.2402 0.0020
1.4181 0.0020

Viscosity, Pa*s [ref]

Operational conditions:

Molality, mol/kg of Triethylamine (1) - Liquid Viscosity, Pa*s - Liquid
0.1482 0.0022
0.3064 0.0022
0.4546 0.0022
0.5880 0.0021
0.7471 0.0021
0.8993 0.0021
1.0564 0.0021
1.2402 0.0020
1.4181 0.0020

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

Operational conditions:

Mole fraction of 1-Butanol (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0501 -0.0888
0.1000 -0.3294
0.1502 -0.5433
0.1999 -0.6528
0.2536 -0.8191
0.3001 -0.9537
0.3499 -1.1112
0.3999 -1.1813
0.4499 -1.2706
0.5000 -1.3473
0.5499 -1.384
0.5999 -1.4047
0.6499 -1.38
0.7001 -1.3193
0.7501 -1.2221
0.7999 -1.0834
0.8500 -0.9156
0.8999 -0.6930
0.9499 -0.3679
0.9792 -0.1720

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

Operational conditions:

Mole fraction of 1-Butanol (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0501 -0.0888
0.1000 -0.3294
0.1502 -0.5433
0.1999 -0.6528
0.2536 -0.8191
0.3001 -0.9537
0.3499 -1.1112
0.3999 -1.1813
0.4499 -1.2706
0.5000 -1.3473
0.5499 -1.384
0.5999 -1.4047
0.6499 -1.38
0.7001 -1.3193
0.7501 -1.2221
0.7999 -1.0834
0.8500 -0.9156
0.8999 -0.6930
0.9499 -0.3679
0.9792 -0.1720

Excess molar volume, m3/mol [ref]

Operational conditions:

Mole fraction of 1-Butanol (2) - Liquid Excess molar volume, m3/mol - Liquid
0.0478 -3.4400e-07
0.0486 -3.4800e-07
0.0970 -6.6200e-07
0.0986 -6.7300e-07
0.1448 -9.3900e-07
0.1466 -9.5000e-07
0.2001 -1.2230e-06
0.2463 -1.4300e-06
0.2479 -1.4350e-06
0.2958 -1.6180e-06
0.2977 -1.6270e-06
0.3536 -1.7980e-06
0.3538 -1.8020e-06
0.4000 -1.9130e-06
0.4474 -1.9920e-06
0.4498 -1.9980e-06
0.4994 -2.0430e-06
0.5004 -2.0460e-06
0.5540 -2.0570e-06
0.5570 -2.0510e-06
0.6054 -2.0150e-06
0.6062 -2.0190e-06
0.6501 -1.9460e-06
0.6527 -1.9430e-06
0.7047 -1.8090e-06
0.7525 -1.6440e-06
0.7526 -1.6410e-06
0.8031 -1.4130e-06
0.8075 -1.3920e-06
0.8521 -1.1380e-06
0.8533 -1.1330e-06
0.9029 -7.9900e-07
0.9044 -7.9100e-07
0.9534 -4.0800e-07
0.9535 -4.0600e-07

Excess molar volume, m3/mol [ref]

Operational conditions:

Mole fraction of 1-Butanol (2) - Liquid Excess molar volume, m3/mol - Liquid
0.0478 -3.4400e-07
0.0486 -3.4800e-07
0.0970 -6.6200e-07
0.0986 -6.7300e-07
0.1448 -9.3900e-07
0.1466 -9.5000e-07
0.2001 -1.2230e-06
0.2463 -1.4300e-06
0.2479 -1.4350e-06
0.2958 -1.6180e-06
0.2977 -1.6270e-06
0.3536 -1.7980e-06
0.3538 -1.8020e-06
0.4000 -1.9130e-06
0.4474 -1.9920e-06
0.4498 -1.9980e-06
0.4994 -2.0430e-06
0.5004 -2.0460e-06
0.5540 -2.0570e-06
0.5570 -2.0510e-06
0.6054 -2.0150e-06
0.6062 -2.0190e-06
0.6501 -1.9460e-06
0.6527 -1.9430e-06
0.7047 -1.8090e-06
0.7525 -1.6440e-06
0.7526 -1.6410e-06
0.8031 -1.4130e-06
0.8075 -1.3920e-06
0.8521 -1.1380e-06
0.8533 -1.1330e-06
0.9029 -7.9900e-07
0.9044 -7.9100e-07
0.9534 -4.0800e-07
0.9535 -4.0600e-07

Sources