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Mixture of 1-Hexene + 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

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)
  2. Pvap - Vapor or sublimation pressure, kPa (2)

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

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of n-Butyl ether (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15 0.0503 -0.0031
298.15 0.1001 -0.0058
298.15 0.1501 -0.0108
298.15 0.2000 -0.0138
298.15 0.2500 -0.0168
298.15 0.2998 -0.0189
298.15 0.3502 -0.0204
298.15 0.3994 -0.0217
298.15 0.4502 -0.0223
298.15 0.4995 -0.0227
298.15 0.5494 -0.0223
298.15 0.5996 -0.0214
298.15 0.6491 -0.0201
298.15 0.7001 -0.0183
298.15 0.7491 -0.0160
298.15 0.7995 -0.0124
298.15 0.8501 -0.0097
298.15 0.8996 -0.0065
298.15 0.9504 -0.0030
313.15 0.0503 -0.0042
313.15 0.1500 -0.0124
313.15 0.2000 -0.0160
313.15 0.2500 -0.0187
313.15 0.2997 -0.0208
313.15 0.3503 -0.0226
313.15 0.3995 -0.0237
313.15 0.4503 -0.0243
313.15 0.4997 -0.0245
313.15 0.5495 -0.0242
313.15 0.5997 -0.0233
313.15 0.6493 -0.0218
313.15 0.7002 -0.0196
313.15 0.7492 -0.0178
313.15 0.7996 -0.0151
313.15 0.8501 -0.0119
313.15 0.8996 -0.0085
313.15 0.9504 -0.0045

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

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of n-Butyl ether (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15 0.0503 -0.0031
298.15 0.1001 -0.0058
298.15 0.1501 -0.0108
298.15 0.2000 -0.0138
298.15 0.2500 -0.0168
298.15 0.2998 -0.0189
298.15 0.3502 -0.0204
298.15 0.3994 -0.0217
298.15 0.4502 -0.0223
298.15 0.4995 -0.0227
298.15 0.5494 -0.0223
298.15 0.5996 -0.0214
298.15 0.6491 -0.0201
298.15 0.7001 -0.0183
298.15 0.7491 -0.0160
298.15 0.7995 -0.0124
298.15 0.8501 -0.0097
298.15 0.8996 -0.0065
298.15 0.9504 -0.0030
313.15 0.0503 -0.0042
313.15 0.1500 -0.0124
313.15 0.2000 -0.0160
313.15 0.2500 -0.0187
313.15 0.2997 -0.0208
313.15 0.3503 -0.0226
313.15 0.3995 -0.0237
313.15 0.4503 -0.0243
313.15 0.4997 -0.0245
313.15 0.5495 -0.0242
313.15 0.5997 -0.0233
313.15 0.6493 -0.0218
313.15 0.7002 -0.0196
313.15 0.7492 -0.0178
313.15 0.7996 -0.0151
313.15 0.8501 -0.0119
313.15 0.8996 -0.0085
313.15 0.9504 -0.0045

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of n-Butyl ether (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 44.95
0.0494 42.80
0.1032 40.44
0.1597 37.98
0.2103 35.78
0.2566 33.76
0.3044 31.73
0.3096 31.45
0.3584 29.33
0.4012 27.47
0.4076 27.20
0.4513 25.30
0.4572 25.02
0.5010 23.14
0.5070 22.86
0.5513 20.97
0.5556 20.78
0.5997 18.86
0.6055 18.63
0.6519 16.62
0.6865 15.14
0.6968 14.71
0.7431 12.75
0.7939 10.60
0.8462 8.41
0.8900 6.58
0.9416 4.45
1.0000 2.07

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of n-Butyl ether (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 44.95
0.0494 42.80
0.1032 40.44
0.1597 37.98
0.2103 35.78
0.2566 33.76
0.3044 31.73
0.3096 31.45
0.3584 29.33
0.4012 27.47
0.4076 27.20
0.4513 25.30
0.4572 25.02
0.5010 23.14
0.5070 22.86
0.5513 20.97
0.5556 20.78
0.5997 18.86
0.6055 18.63
0.6519 16.62
0.6865 15.14
0.6968 14.71
0.7431 12.75
0.7939 10.60
0.8462 8.41
0.8900 6.58
0.9416 4.45
1.0000 2.07

Sources