Mixture of Di-n-propyl ether + n-Butyl ether + Tetrahydrofuran

Excel

Di-n-propyl ether

Name
Di-n-propyl ether
InChI
InChI=1S/C6H14O/c1-3-5-7-6-4-2/h3-6H2,1-2H3
InChI Key
POLCUAVZOMRGSN-UHFFFAOYSA-N
Formula
C6H14O
SMILES
CCCOCCC
Mol. Weight (g/mol)
102.17
CAS
111-43-3

n-Butyl ether

Name
n-Butyl ether
InChI
InChI=1S/C8H18O/c1-3-5-7-9-8-6-4-2/h3-8H2,1-2H3
InChI Key
DURPTKYDGMDSBL-UHFFFAOYSA-N
Formula
C8H18O
SMILES
CCCCOCCCC
Mol. Weight (g/mol)
130.23
CAS
142-96-1

Tetrahydrofuran

Name
Tetrahydrofuran
InChI
InChI=1S/C4H8O/c1-2-4-5-3-1/h1-4H2
InChI Key
WYURNTSHIVDZCO-UHFFFAOYSA-N
Formula
C4H8O
SMILES
C1CCOC1
Mol. Weight (g/mol)
72.11
CAS
109-99-9
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Datasets

  1. Excess molar enthalpy (molar enthalpy (2)

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

Operational conditions:

Fixed Measured
Mole fraction of Di-n-propyl ether (1) - Liquid Solvent: Amount ratio of component to other component of binary solvent of n-Butyl ether (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0500 0.3333 0.0212
0.0500 1.0004 0.0065
0.0500 3.0 0.0019
0.1000 0.3333 0.0388
0.1000 1.0004 0.0126
0.1000 3.0 0.0035
0.1500 0.3333 0.0553
0.1500 1.0004 0.0179
0.1555 3.0 0.0050
0.2000 1.0004 0.0228
0.2000 3.0 0.0060
0.2002 0.3333 0.0692
0.2498 3.0 0.0069
0.2502 0.3333 0.0809
0.2503 1.0004 0.0270
0.2999 3.0 0.0076
0.3000 0.3333 0.0908
0.3002 1.0004 0.0302
0.3499 0.3333 0.0984
0.3499 1.0004 0.0329
0.3502 3.0 0.0082
0.4002 0.3333 0.1042
0.4002 1.0004 0.0351
0.4002 3.0 0.0085
0.4497 0.3333 0.1068
0.4502 1.0004 0.0365
0.4503 3.0 0.0088
0.5001 0.3333 0.1081
0.5001 1.0004 0.0373
0.5001 3.0 0.0089
0.5001 0.3333 0.1081
0.5001 3.0 0.0089
0.5002 1.0004 0.0373
0.5501 0.3333 0.1072
0.5501 1.0004 0.0372
0.5501 3.0 0.0089
0.5998 1.0004 0.0366
0.5999 0.3333 0.1046
0.6000 3.0 0.0087
0.6500 1.0004 0.0351
0.6501 3.0 0.0083
0.6503 0.3333 0.0989
0.7000 1.0004 0.0332
0.7001 3.0 0.0078
0.7016 0.3333 0.0913
0.7498 1.0004 0.0303
0.7498 3.0 0.0071
0.7501 0.3333 0.0828
0.8000 0.3333 0.0708
0.8000 3.0 0.0063
0.8001 1.0004 0.0267
0.8500 0.3333 0.0582
0.8500 1.0004 0.0219
0.8500 3.0 0.0051
0.9000 1.0004 0.0159
0.9000 3.0 0.0037
0.9001 0.3333 0.0425
0.9500 0.3333 0.0241
0.9500 1.0004 0.0087
0.9500 3.0 0.0020

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

Operational conditions:

Fixed Measured
Mole fraction of Di-n-propyl ether (1) - Liquid Solvent: Amount ratio of component to other component of binary solvent of n-Butyl ether (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0500 0.3333 0.0212
0.0500 1.0004 0.0065
0.0500 3.0 0.0019
0.1000 0.3333 0.0388
0.1000 1.0004 0.0126
0.1000 3.0 0.0035
0.1500 0.3333 0.0553
0.1500 1.0004 0.0179
0.1555 3.0 0.0050
0.2000 1.0004 0.0228
0.2000 3.0 0.0060
0.2002 0.3333 0.0692
0.2498 3.0 0.0069
0.2502 0.3333 0.0809
0.2503 1.0004 0.0270
0.2999 3.0 0.0076
0.3000 0.3333 0.0908
0.3002 1.0004 0.0302
0.3499 0.3333 0.0984
0.3499 1.0004 0.0329
0.3502 3.0 0.0082
0.4002 0.3333 0.1042
0.4002 1.0004 0.0351
0.4002 3.0 0.0085
0.4497 0.3333 0.1068
0.4502 1.0004 0.0365
0.4503 3.0 0.0088
0.5001 0.3333 0.1081
0.5001 1.0004 0.0373
0.5001 3.0 0.0089
0.5001 0.3333 0.1081
0.5001 3.0 0.0089
0.5002 1.0004 0.0373
0.5501 0.3333 0.1072
0.5501 1.0004 0.0372
0.5501 3.0 0.0089
0.5998 1.0004 0.0366
0.5999 0.3333 0.1046
0.6000 3.0 0.0087
0.6500 1.0004 0.0351
0.6501 3.0 0.0083
0.6503 0.3333 0.0989
0.7000 1.0004 0.0332
0.7001 3.0 0.0078
0.7016 0.3333 0.0913
0.7498 1.0004 0.0303
0.7498 3.0 0.0071
0.7501 0.3333 0.0828
0.8000 0.3333 0.0708
0.8000 3.0 0.0063
0.8001 1.0004 0.0267
0.8500 0.3333 0.0582
0.8500 1.0004 0.0219
0.8500 3.0 0.0051
0.9000 1.0004 0.0159
0.9000 3.0 0.0037
0.9001 0.3333 0.0425
0.9500 0.3333 0.0241
0.9500 1.0004 0.0087
0.9500 3.0 0.0020

Sources