Mixture of 1-Pentanol + Benzene, 1,2,4-trimethyl-

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1-Pentanol

Name
1-Pentanol
InChI
InChI=1S/C5H12O/c1-2-3-4-5-6/h6H,2-5H2,1H3
InChI Key
AMQJEAYHLZJPGS-UHFFFAOYSA-N
Formula
C5H12O
SMILES
CCCCCO
Mol. Weight (g/mol)
88.15
CAS
71-41-0

Benzene, 1,2,4-trimethyl-

Name
Benzene, 1,2,4-trimethyl-
InChI
InChI=1S/C9H12/c1-7-4-5-8(2)9(3)6-7/h4-6H,1-3H3
InChI Key
GWHJZXXIDMPWGX-UHFFFAOYSA-N
Formula
C9H12
SMILES
Cc1ccc(C)c(C)c1
Mol. Weight (g/mol)
120.19
CAS
95-63-6
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Datasets

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

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

Operational condition: Temperature, K = 313.15 (Gas)

Mole fraction of 1-Pentanol (1) - Liquid Mole fraction of 1-Pentanol (1) - Gas
0.0000 0.0000
0.0500 0.3638
0.0997 0.3928
0.1499 0.4053
0.1997 0.4184
0.2498 0.4314
0.2996 0.4427
0.3498 0.4529
0.3999 0.4640
0.4002 0.4641
0.4499 0.4781
0.4502 0.4782
0.5000 0.4970
0.5003 0.4971
0.5500 0.5214
0.5502 0.5215
0.6000 0.5507
0.6002 0.5508
0.6503 0.5832
0.6912 0.6102
0.7503 0.6488
0.8004 0.6823
0.8505 0.7228
0.9005 0.7825
0.9503 0.8769
1.0000 1.0000

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

Operational condition: Temperature, K = 313.15 (Gas)

Mole fraction of 1-Pentanol (1) - Liquid Mole fraction of 1-Pentanol (1) - Gas
0.0000 0.0000
0.0500 0.3638
0.0997 0.3928
0.1499 0.4053
0.1997 0.4184
0.2498 0.4314
0.2996 0.4427
0.3498 0.4529
0.3999 0.4640
0.4002 0.4641
0.4499 0.4781
0.4502 0.4782
0.5000 0.4970
0.5003 0.4971
0.5500 0.5214
0.5502 0.5215
0.6000 0.5507
0.6002 0.5508
0.6503 0.5832
0.6912 0.6102
0.7503 0.6488
0.8004 0.6823
0.8505 0.7228
0.9005 0.7825
0.9503 0.8769
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 1-Pentanol (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15 0.0000 0.0000
298.15 0.0503 0.5200
298.15 0.0995 0.7339
298.15 0.1500 0.8550
298.15 0.1995 0.9186
298.15 0.2501 0.9749
298.15 0.2997 1.0066
298.15 0.3481 1.015
298.15 0.3998 1.0051
298.15 0.4481 0.9790
298.15 0.4995 0.9342
298.15 0.5495 0.8804
298.15 0.5985 0.8118
298.15 0.6482 0.7332
298.15 0.6985 0.6414
298.15 0.7494 0.5394
298.15 0.7991 0.4345
298.15 0.8492 0.3253
298.15 0.8997 0.2206
298.15 0.9505 0.1058
298.15 1.0000 0.0000
313.15 0.0000 0.0000
313.15 0.0503 0.5815
313.15 0.0995 0.8640
313.15 0.1500 1.0363
313.15 0.1995 1.1412
313.15 0.2502 1.2074
313.15 0.2997 1.2417
313.15 0.3481 1.2572
313.15 0.3998 1.2546
313.15 0.4482 1.2326
313.15 0.4995 1.1825
313.15 0.5496 1.122
313.15 0.5986 1.0469
313.15 0.6482 0.9514
313.15 0.6986 0.8475
313.15 0.7495 0.7233
313.15 0.7991 0.5937
313.15 0.8492 0.4523
313.15 0.8997 0.3051
313.15 0.9505 0.1480
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 1-Pentanol (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15 0.0000 0.0000
298.15 0.0503 0.5200
298.15 0.0995 0.7339
298.15 0.1500 0.8550
298.15 0.1995 0.9186
298.15 0.2501 0.9749
298.15 0.2997 1.0066
298.15 0.3481 1.015
298.15 0.3998 1.0051
298.15 0.4481 0.9790
298.15 0.4995 0.9342
298.15 0.5495 0.8804
298.15 0.5985 0.8118
298.15 0.6482 0.7332
298.15 0.6985 0.6414
298.15 0.7494 0.5394
298.15 0.7991 0.4345
298.15 0.8492 0.3253
298.15 0.8997 0.2206
298.15 0.9505 0.1058
298.15 1.0000 0.0000
313.15 0.0000 0.0000
313.15 0.0503 0.5815
313.15 0.0995 0.8640
313.15 0.1500 1.0363
313.15 0.1995 1.1412
313.15 0.2502 1.2074
313.15 0.2997 1.2417
313.15 0.3481 1.2572
313.15 0.3998 1.2546
313.15 0.4482 1.2326
313.15 0.4995 1.1825
313.15 0.5496 1.122
313.15 0.5986 1.0469
313.15 0.6482 0.9514
313.15 0.6986 0.8475
313.15 0.7495 0.7233
313.15 0.7991 0.5937
313.15 0.8492 0.4523
313.15 0.8997 0.3051
313.15 0.9505 0.1480
313.15 1.0000 0.0000

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Gas)

Mole fraction of 1-Pentanol (1) - Liquid Vapor or sublimation pressure, kPa - Gas
0.0000 0.73
0.0500 1.08
0.0997 1.11
0.1499 1.14
0.1997 1.15
0.2498 1.16
0.2996 1.17
0.3498 1.18
0.3999 1.18
0.4002 1.17
0.4499 1.18
0.4502 1.17
0.5000 1.18
0.5003 1.18
0.5500 1.18
0.5502 1.17
0.6000 1.18
0.6002 1.17
0.6503 1.17
0.6912 1.16
0.7503 1.14
0.8004 1.12
0.8505 1.09
0.9005 1.04
0.9503 0.99
1.0000 0.92

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Gas)

Mole fraction of 1-Pentanol (1) - Liquid Vapor or sublimation pressure, kPa - Gas
0.0000 0.73
0.0500 1.08
0.0997 1.11
0.1499 1.14
0.1997 1.15
0.2498 1.16
0.2996 1.17
0.3498 1.18
0.3999 1.18
0.4002 1.17
0.4499 1.18
0.4502 1.17
0.5000 1.18
0.5003 1.18
0.5500 1.18
0.5502 1.17
0.6000 1.18
0.6002 1.17
0.6503 1.17
0.6912 1.16
0.7503 1.14
0.8004 1.12
0.8505 1.09
0.9005 1.04
0.9503 0.99
1.0000 0.92

Sources