Mixture of 2-Pentanol + Pentane, 2,2,4-trimethyl-

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2-Pentanol

Name
2-Pentanol
InChI
InChI=1S/C5H12O/c1-3-4-5(2)6/h5-6H,3-4H2,1-2H3
InChI Key
JYVLIDXNZAXMDK-UHFFFAOYSA-N
Formula
C5H12O
SMILES
CCCC(C)O
Mol. Weight (g/mol)
88.15
CAS
6032-29-7

Pentane, 2,2,4-trimethyl-

Name
Pentane, 2,2,4-trimethyl-
InChI
InChI=1S/C8H18/c1-7(2)6-8(3,4)5/h7H,6H2,1-5H3
InChI Key
NHTMVDHEPJAVLT-UHFFFAOYSA-N
Formula
C8H18
SMILES
CC(C)CC(C)(C)C
Mol. Weight (g/mol)
114.23
CAS
540-84-1
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Datasets

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

Mole fraction of 2-Pentanol (1) [ref]

Operational condition: Temperature, K = 313.15 (Gas)

Mole fraction of 2-Pentanol (1) - Liquid Mole fraction of 2-Pentanol (1) - Gas
0.0000 0.0000
0.0499 0.0560
0.0988 0.0740
0.1490 0.0839
0.1996 0.0917
0.2501 0.0991
0.2999 0.1063
0.3501 0.1134
0.4002 0.1205
0.4006 0.1205
0.4500 0.1276
0.4506 0.1277
0.5001 0.1352
0.5008 0.1353
0.5502 0.1436
0.5509 0.1438
0.6001 0.1533
0.6007 0.1535
0.6508 0.1652
0.7008 0.1797
0.7512 0.1987
0.8012 0.2248
0.8513 0.2642
0.9009 0.3314
0.9501 0.4749
1.0000 1.0000

Mole fraction of 2-Pentanol (1) [ref]

Operational condition: Temperature, K = 313.15 (Gas)

Mole fraction of 2-Pentanol (1) - Liquid Mole fraction of 2-Pentanol (1) - Gas
0.0000 0.0000
0.0499 0.0560
0.0988 0.0740
0.1490 0.0839
0.1996 0.0917
0.2501 0.0991
0.2999 0.1063
0.3501 0.1134
0.4002 0.1205
0.4006 0.1205
0.4500 0.1276
0.4506 0.1277
0.5001 0.1352
0.5008 0.1353
0.5502 0.1436
0.5509 0.1438
0.6001 0.1533
0.6007 0.1535
0.6508 0.1652
0.7008 0.1797
0.7512 0.1987
0.8012 0.2248
0.8513 0.2642
0.9009 0.3314
0.9501 0.4749
1.0000 1.0000

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

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 2-Pentanol (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15 0.0000 0.0000
298.15 0.0507 0.4765
298.15 0.0997 0.6438
298.15 0.1498 0.7258
298.15 0.2009 0.7949
298.15 0.2500 0.8472
298.15 0.3022 0.8921
298.15 0.3503 0.9215
298.15 0.4011 0.9510
298.15 0.4521 0.9586
298.15 0.5011 0.9563
298.15 0.5521 0.9215
298.15 0.6010 0.8793
298.15 0.6517 0.8186
298.15 0.7019 0.7407
298.15 0.7517 0.6467
298.15 0.8009 0.5368
298.15 0.8510 0.4173
298.15 0.9002 0.2831
298.15 0.9500 0.1414
298.15 1.0000 0.0000
313.15 0.0000 0.0000
313.15 0.0507 0.6096
313.15 0.0998 0.8221
313.15 0.1499 0.9375
313.15 0.2009 1.0167
313.15 0.2499 1.0785
313.15 0.3023 1.1206
313.15 0.3502 1.1338
313.15 0.4010 1.1434
313.15 0.4520 1.1365
313.15 0.5010 1.1178
313.15 0.5520 1.0863
313.15 0.6010 1.0359
313.15 0.6516 0.9645
313.15 0.7018 0.8833
313.15 0.7516 0.7748
313.15 0.8008 0.6599
313.15 0.8510 0.5120
313.15 0.9002 0.3578
313.15 0.9500 0.1847
313.15 1.0000 0.0000

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

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 2-Pentanol (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15 0.0000 0.0000
298.15 0.0507 0.4765
298.15 0.0997 0.6438
298.15 0.1498 0.7258
298.15 0.2009 0.7949
298.15 0.2500 0.8472
298.15 0.3022 0.8921
298.15 0.3503 0.9215
298.15 0.4011 0.9510
298.15 0.4521 0.9586
298.15 0.5011 0.9563
298.15 0.5521 0.9215
298.15 0.6010 0.8793
298.15 0.6517 0.8186
298.15 0.7019 0.7407
298.15 0.7517 0.6467
298.15 0.8009 0.5368
298.15 0.8510 0.4173
298.15 0.9002 0.2831
298.15 0.9500 0.1414
298.15 1.0000 0.0000
313.15 0.0000 0.0000
313.15 0.0507 0.6096
313.15 0.0998 0.8221
313.15 0.1499 0.9375
313.15 0.2009 1.0167
313.15 0.2499 1.0785
313.15 0.3023 1.1206
313.15 0.3502 1.1338
313.15 0.4010 1.1434
313.15 0.4520 1.1365
313.15 0.5010 1.1178
313.15 0.5520 1.0863
313.15 0.6010 1.0359
313.15 0.6516 0.9645
313.15 0.7018 0.8833
313.15 0.7516 0.7748
313.15 0.8008 0.6599
313.15 0.8510 0.5120
313.15 0.9002 0.3578
313.15 0.9500 0.1847
313.15 1.0000 0.0000

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of 2-Pentanol (1) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 12.97
0.0499 13.26
0.0988 13.23
0.1490 13.16
0.1996 13.04
0.2501 12.90
0.2999 12.69
0.3501 12.53
0.4002 12.32
0.4006 12.29
0.4500 12.06
0.4506 12.05
0.5001 11.78
0.5008 11.79
0.5502 11.46
0.5509 11.46
0.6001 11.06
0.6007 11.09
0.6508 10.64
0.7008 10.11
0.7512 9.45
0.8012 8.64
0.8513 7.61
0.9009 6.30
0.9501 4.60
1.0000 2.31

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of 2-Pentanol (1) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 12.97
0.0499 13.26
0.0988 13.23
0.1490 13.16
0.1996 13.04
0.2501 12.90
0.2999 12.69
0.3501 12.53
0.4002 12.32
0.4006 12.29
0.4500 12.06
0.4506 12.05
0.5001 11.78
0.5008 11.79
0.5502 11.46
0.5509 11.46
0.6001 11.06
0.6007 11.09
0.6508 10.64
0.7008 10.11
0.7512 9.45
0.8012 8.64
0.8513 7.61
0.9009 6.30
0.9501 4.60
1.0000 2.31

Sources