Mixture of n-Butyl ether + Cyclohexane

Excel

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

Cyclohexane

Name
Cyclohexane
InChI
InChI=1S/C6H12/c1-2-4-6-5-3-1/h1-6H2
InChI Key
XDTMQSROBMDMFD-UHFFFAOYSA-N
Formula
C6H12
SMILES
C1CCCCC1
Mol. Weight (g/mol)
84.16
CAS
110-82-7
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Datasets

  1. Excess molar enthalpy (molar enthalpy (4)
  2. Pvap - Vapor or sublimation pressure, kPa (4)

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

Operational conditions:

Mole fraction of n-Butyl ether (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0498 0.0738
0.0997 0.1291
0.1502 0.1713
0.2003 0.2032
0.2498 0.2246
0.3001 0.2398
0.3502 0.2470
0.3999 0.2496
0.4499 0.2474
0.4992 0.2414
0.5497 0.2299
0.6002 0.2166
0.6493 0.1984
0.6993 0.1777
0.7502 0.1535
0.7991 0.1251
0.8500 0.0981
0.9001 0.0659
0.9506 0.0327

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

Operational conditions:

Mole fraction of n-Butyl ether (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0499 0.0752
0.0997 0.1341
0.1502 0.1804
0.2002 0.2145
0.2497 0.2385
0.2999 0.2554
0.3500 0.2649
0.3996 0.2686
0.4497 0.2664
0.4990 0.2596
0.5495 0.2481
0.6000 0.2326
0.6491 0.2139
0.6992 0.1911
0.7501 0.1641
0.7990 0.1367
0.8500 0.1041
0.9001 0.0693
0.9507 0.0328

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

Operational conditions:

Mole fraction of n-Butyl ether (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0498 0.0738
0.0997 0.1291
0.1502 0.1713
0.2003 0.2032
0.2498 0.2246
0.3001 0.2398
0.3502 0.2470
0.3999 0.2496
0.4499 0.2474
0.4992 0.2414
0.5497 0.2299
0.6002 0.2166
0.6493 0.1984
0.6993 0.1777
0.7502 0.1535
0.7991 0.1251
0.8500 0.0981
0.9001 0.0659
0.9506 0.0327

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

Operational conditions:

Mole fraction of n-Butyl ether (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0499 0.0752
0.0997 0.1341
0.1502 0.1804
0.2002 0.2145
0.2497 0.2385
0.2999 0.2554
0.3500 0.2649
0.3996 0.2686
0.4497 0.2664
0.4990 0.2596
0.5495 0.2481
0.6000 0.2326
0.6491 0.2139
0.6992 0.1911
0.7501 0.1641
0.7990 0.1367
0.8500 0.1041
0.9001 0.0693
0.9507 0.0328

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of n-Butyl ether (1) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 24.62
0.0464 23.57
0.1048 22.24
0.1511 21.21
0.1998 20.12
0.2524 18.93
0.3011 17.83
0.3044 17.76
0.3502 16.73
0.3973 15.65
0.4003 15.58
0.4479 14.49
0.4484 14.49
0.4985 13.35
0.5006 13.30
0.5470 12.25
0.5478 12.23
0.5980 11.09
0.5991 11.07
0.6534 9.85
0.6988 8.81
0.7560 7.52
0.7999 6.53
0.8381 5.68
0.8539 5.31
0.8964 4.35
0.9550 3.06
1.0000 2.06

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of n-Butyl ether (1) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.2975 17.90
0.3153 17.55
0.6878 9.10
0.7139 8.51

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of n-Butyl ether (1) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 24.62
0.0464 23.57
0.1048 22.24
0.1511 21.21
0.1998 20.12
0.2524 18.93
0.3011 17.83
0.3044 17.76
0.3502 16.73
0.3973 15.65
0.4003 15.58
0.4479 14.49
0.4484 14.49
0.4985 13.35
0.5006 13.30
0.5470 12.25
0.5478 12.23
0.5980 11.09
0.5991 11.07
0.6534 9.85
0.6988 8.81
0.7560 7.52
0.7999 6.53
0.8381 5.68
0.8539 5.31
0.8964 4.35
0.9550 3.06
1.0000 2.06

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of n-Butyl ether (1) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.2975 17.90
0.3153 17.55
0.6878 9.10
0.7139 8.51

Sources