Mixture of 1-Hexene + Di-n-propyl ether + n-Butyl ether

Excel

1-Hexene

Name
1-Hexene
InChI
InChI=1S/C6H12/c1-3-5-6-4-2/h3H,1,4-6H2,2H3
InChI Key
LIKMAJRDDDTEIG-UHFFFAOYSA-N
Formula
C6H12
SMILES
C=CCCCC
Mol. Weight (g/mol)
84.16
CAS
592-41-6

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
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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 (2) - Liquid Solvent: Amount ratio of component to other component of binary solvent of n-Butyl ether (3) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0500 0.3333 0.0052
0.0500 0.9996 0.0043
0.0500 3.0 0.0030
0.1000 0.3333 0.0096
0.1000 0.9996 0.0082
0.1000 3.0 0.0058
0.1499 0.9996 0.0117
0.1500 0.3333 0.0136
0.1500 3.0 0.0084
0.1998 0.3333 0.0170
0.1999 3.0 0.0107
0.2001 0.9996 0.0147
0.2499 0.9996 0.0173
0.2501 0.3333 0.0200
0.2501 3.0 0.0127
0.2999 0.9996 0.0195
0.3001 0.3333 0.0223
0.3001 3.0 0.0144
0.3499 3.0 0.0158
0.3501 0.3333 0.0243
0.3502 0.9996 0.0212
0.4000 3.0 0.0169
0.4001 0.3333 0.0256
0.4001 0.9996 0.0226
0.4496 0.3333 0.0264
0.4501 3.0 0.0176
0.4502 0.9996 0.0234
0.4996 3.0 0.0181
0.4997 3.0 0.0182
0.5000 0.9996 0.0239
0.5000 0.9996 0.0239
0.5002 0.3333 0.0267
0.5002 0.3333 0.0268
0.5497 3.0 0.0183
0.5500 0.9996 0.0239
0.5503 0.3333 0.0266
0.5999 0.3333 0.0260
0.6001 3.0 0.0181
0.6003 0.9996 0.0235
0.6497 3.0 0.0175
0.6500 0.9996 0.0225
0.6501 0.3333 0.0249
0.6997 3.0 0.0168
0.7001 0.9996 0.0213
0.7003 0.3333 0.0234
0.7497 3.0 0.0154
0.7499 0.9996 0.0196
0.7500 0.3333 0.0214
0.7998 0.3333 0.0190
0.7998 3.0 0.0139
0.8001 0.9996 0.0173
0.8497 3.0 0.0121
0.8500 0.3333 0.0158
0.8500 0.9996 0.0147
0.9000 0.3333 0.0122
0.9000 0.9996 0.0117
0.9000 3.0 0.0097
0.9500 0.3333 0.0071
0.9500 0.9996 0.0078
0.9500 3.0 0.0064

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

Operational conditions:

Fixed Measured
Mole fraction of Di-n-propyl ether (2) - Liquid Solvent: Amount ratio of component to other component of binary solvent of n-Butyl ether (3) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0500 0.3333 0.0052
0.0500 0.9996 0.0043
0.0500 3.0 0.0030
0.1000 0.3333 0.0096
0.1000 0.9996 0.0082
0.1000 3.0 0.0058
0.1499 0.9996 0.0117
0.1500 0.3333 0.0136
0.1500 3.0 0.0084
0.1998 0.3333 0.0170
0.1999 3.0 0.0107
0.2001 0.9996 0.0147
0.2499 0.9996 0.0173
0.2501 0.3333 0.0200
0.2501 3.0 0.0127
0.2999 0.9996 0.0195
0.3001 0.3333 0.0223
0.3001 3.0 0.0144
0.3499 3.0 0.0158
0.3501 0.3333 0.0243
0.3502 0.9996 0.0212
0.4000 3.0 0.0169
0.4001 0.3333 0.0256
0.4001 0.9996 0.0226
0.4496 0.3333 0.0264
0.4501 3.0 0.0176
0.4502 0.9996 0.0234
0.4996 3.0 0.0181
0.4997 3.0 0.0182
0.5000 0.9996 0.0239
0.5000 0.9996 0.0239
0.5002 0.3333 0.0267
0.5002 0.3333 0.0268
0.5497 3.0 0.0183
0.5500 0.9996 0.0239
0.5503 0.3333 0.0266
0.5999 0.3333 0.0260
0.6001 3.0 0.0181
0.6003 0.9996 0.0235
0.6497 3.0 0.0175
0.6500 0.9996 0.0225
0.6501 0.3333 0.0249
0.6997 3.0 0.0168
0.7001 0.9996 0.0213
0.7003 0.3333 0.0234
0.7497 3.0 0.0154
0.7499 0.9996 0.0196
0.7500 0.3333 0.0214
0.7998 0.3333 0.0190
0.7998 3.0 0.0139
0.8001 0.9996 0.0173
0.8497 3.0 0.0121
0.8500 0.3333 0.0158
0.8500 0.9996 0.0147
0.9000 0.3333 0.0122
0.9000 0.9996 0.0117
0.9000 3.0 0.0097
0.9500 0.3333 0.0071
0.9500 0.9996 0.0078
0.9500 3.0 0.0064

Sources