Mixture of Diisopropyl ether + Pentane, 3-methyl-

Excel

Diisopropyl ether

Name
Diisopropyl ether
InChI
InChI=1S/C6H14O/c1-5(2)7-6(3)4/h5-6H,1-4H3
InChI Key
ZAFNJMIOTHYJRJ-UHFFFAOYSA-N
Formula
C6H14O
SMILES
CC(C)OC(C)C
Mol. Weight (g/mol)
102.17
CAS
108-20-3

Pentane, 3-methyl-

Name
Pentane, 3-methyl-
InChI
InChI=1S/C6H14/c1-4-6(3)5-2/h6H,4-5H2,1-3H3
InChI Key
PFEOZHBOMNWTJB-UHFFFAOYSA-N
Formula
C6H14
SMILES
CCC(C)CC
Mol. Weight (g/mol)
86.18
CAS
96-14-0
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Datasets

  1. Excess molar enthalpy (molar enthalpy (2)
  2. ν - Kinematic viscosity, m2/s (2)

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

Operational conditions:

Mole fraction of Diisopropyl ether (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0500 0.0422
0.1000 0.0786
0.1499 0.1097
0.2000 0.1361
0.2503 0.1555
0.2998 0.1716
0.3501 0.1838
0.3997 0.1923
0.4500 0.1974
0.5003 0.1976
0.5502 0.1938
0.5998 0.1873
0.6500 0.1767
0.7002 0.1621
0.7501 0.1436
0.8003 0.1215
0.8500 0.0937
0.9000 0.0659
0.9500 0.0358

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

Operational conditions:

Mole fraction of Diisopropyl ether (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0500 0.0422
0.1000 0.0786
0.1499 0.1097
0.2000 0.1361
0.2503 0.1555
0.2998 0.1716
0.3501 0.1838
0.3997 0.1923
0.4500 0.1974
0.5003 0.1976
0.5502 0.1938
0.5998 0.1873
0.6500 0.1767
0.7002 0.1621
0.7501 0.1436
0.8003 0.1215
0.8500 0.0937
0.9000 0.0659
0.9500 0.0358

Kinematic viscosity, m2/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Diisopropyl ether (1) - Liquid Kinematic viscosity, m2/s - Liquid
283.15 0.0000 4.9280e-07
283.15 0.0498 4.9140e-07
283.15 0.1011 4.9030e-07
283.15 0.2010 4.8860e-07
283.15 0.3018 4.8770e-07
283.15 0.4014 4.8710e-07
283.15 0.5010 4.8760e-07
283.15 0.5993 4.8830e-07
283.15 0.6973 4.8970e-07
283.15 0.8014 4.9120e-07
283.15 0.8997 4.9340e-07
283.15 0.9501 4.9470e-07
283.15 1.0000 4.9590e-07
298.15 0.0000 4.3660e-07
298.15 0.0498 4.3640e-07
298.15 0.1011 4.3550e-07
298.15 0.2010 4.3480e-07
298.15 0.3018 4.3420e-07
298.15 0.4014 4.3390e-07
298.15 0.5010 4.3380e-07
298.15 0.5993 4.3440e-07
298.15 0.6973 4.3520e-07
298.15 0.8014 4.3660e-07
298.15 0.8997 4.3770e-07
298.15 0.9501 4.3850e-07
298.15 1.0000 4.3920e-07
313.15 0.0000 3.8810e-07
313.15 0.0498 3.8720e-07
313.15 0.1011 3.8610e-07
313.15 0.2010 3.8470e-07
313.15 0.3018 3.8370e-07
313.15 0.4014 3.8300e-07
313.15 0.5010 3.8270e-07
313.15 0.5993 3.8310e-07
313.15 0.6973 3.8330e-07
313.15 0.8014 3.8420e-07
313.15 0.8997 3.8490e-07
313.15 0.9501 3.8540e-07
313.15 1.0000 3.8610e-07

Kinematic viscosity, m2/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Diisopropyl ether (1) - Liquid Kinematic viscosity, m2/s - Liquid
283.15 0.0000 4.9280e-07
283.15 0.0498 4.9140e-07
283.15 0.1011 4.9030e-07
283.15 0.2010 4.8860e-07
283.15 0.3018 4.8770e-07
283.15 0.4014 4.8710e-07
283.15 0.5010 4.8760e-07
283.15 0.5993 4.8830e-07
283.15 0.6973 4.8970e-07
283.15 0.8014 4.9120e-07
283.15 0.8997 4.9340e-07
283.15 0.9501 4.9470e-07
283.15 1.0000 4.9590e-07
298.15 0.0000 4.3660e-07
298.15 0.0498 4.3640e-07
298.15 0.1011 4.3550e-07
298.15 0.2010 4.3480e-07
298.15 0.3018 4.3420e-07
298.15 0.4014 4.3390e-07
298.15 0.5010 4.3380e-07
298.15 0.5993 4.3440e-07
298.15 0.6973 4.3520e-07
298.15 0.8014 4.3660e-07
298.15 0.8997 4.3770e-07
298.15 0.9501 4.3850e-07
298.15 1.0000 4.3920e-07
313.15 0.0000 3.8810e-07
313.15 0.0498 3.8720e-07
313.15 0.1011 3.8610e-07
313.15 0.2010 3.8470e-07
313.15 0.3018 3.8370e-07
313.15 0.4014 3.8300e-07
313.15 0.5010 3.8270e-07
313.15 0.5993 3.8310e-07
313.15 0.6973 3.8330e-07
313.15 0.8014 3.8420e-07
313.15 0.8997 3.8490e-07
313.15 0.9501 3.8540e-07
313.15 1.0000 3.8610e-07

Sources