Mixture of Benzene, 1,3-dimethyl- + 1-Butanol

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Benzene, 1,3-dimethyl-

Name
Benzene, 1,3-dimethyl-
InChI
InChI=1S/C8H10/c1-7-4-3-5-8(2)6-7/h3-6H,1-2H3
InChI Key
IVSZLXZYQVIEFR-UHFFFAOYSA-N
Formula
C8H10
SMILES
Cc1cccc(C)c1
Mol. Weight (g/mol)
106.17
CAS
108-38-3

1-Butanol

Name
1-Butanol
InChI
InChI=1S/C4H10O/c1-2-3-4-5/h5H,2-4H2,1H3
InChI Key
LRHPLDYGYMQRHN-UHFFFAOYSA-N
Formula
C4H10O
SMILES
CCCCO
Mol. Weight (g/mol)
74.12
CAS
71-36-3
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Datasets

  1. Mole fraction (2)
  2. Pvap - Vapor or sublimation pressure, kPa (2)
  3. Tboil - Boiling temperature at pressure P, K (2)
  4. Vapor Liquid Equilibrium at Constant Pressure (2)
  5. Vapor Liquid Equilibrium at Constant Temperature

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

Operational condition: Pressure, kPa = 101.33 (Liquid)

Mole fraction of 1-Butanol (2) - Liquid Mole fraction of 1-Butanol (2) - Gas
0.0000 0.0000
0.0367 0.1460
0.1487 0.3884
0.2405 0.4990
0.2980 0.5336
0.3112 0.5448
0.3846 0.5968
0.4787 0.6287
0.4974 0.6515
0.5376 0.6530
0.6008 0.6854
0.6597 0.7136
0.7180 0.7435
0.7716 0.7882
0.8315 0.8220
0.8709 0.8498
0.8972 0.8734
0.9250 0.9058
0.9444 0.9276
0.9582 0.9467
1.0000 1.0000

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

Operational condition: Pressure, kPa = 101.33 (Liquid)

Mole fraction of 1-Butanol (2) - Liquid Mole fraction of 1-Butanol (2) - Gas
0.0000 0.0000
0.0367 0.1460
0.1487 0.3884
0.2405 0.4990
0.2980 0.5336
0.3112 0.5448
0.3846 0.5968
0.4787 0.6287
0.4974 0.6515
0.5376 0.6530
0.6008 0.6854
0.6597 0.7136
0.7180 0.7435
0.7716 0.7882
0.8315 0.8220
0.8709 0.8498
0.8972 0.8734
0.9250 0.9058
0.9444 0.9276
0.9582 0.9467
1.0000 1.0000

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 308.15 (Liquid)

Mole fraction of 1-Butanol (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0530 2.20
0.1110 2.45
0.1715 2.69
0.2505 2.95
0.3190 3.08
0.3925 3.20
0.4425 3.23
0.5090 3.27
0.5925 3.31
0.6495 3.27
0.7260 3.21
0.8315 2.91
0.8945 2.57
0.9460 2.16

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 308.15 (Liquid)

Mole fraction of 1-Butanol (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0530 2.20
0.1110 2.45
0.1715 2.69
0.2505 2.95
0.3190 3.08
0.3925 3.20
0.4425 3.23
0.5090 3.27
0.5925 3.31
0.6495 3.27
0.7260 3.21
0.8315 2.91
0.8945 2.57
0.9460 2.16

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.33 (Liquid)

Mole fraction of 1-Butanol (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 412.27
0.0367 407.08
0.1487 398.57
0.2405 396.13
0.2980 394.63
0.3112 393.36
0.3846 392.75
0.4787 391.58
0.4974 391.21
0.5376 390.58
0.6008 390.09
0.6597 389.81
0.7180 389.63
0.7716 389.55
0.8315 389.59
0.8709 389.70
0.8972 389.82
0.9250 390.01
0.9444 390.18
0.9582 390.32
1.0000 390.85

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.33 (Liquid)

Mole fraction of 1-Butanol (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 412.27
0.0367 407.08
0.1487 398.57
0.2405 396.13
0.2980 394.63
0.3112 393.36
0.3846 392.75
0.4787 391.58
0.4974 391.21
0.5376 390.58
0.6008 390.09
0.6597 389.81
0.7180 389.63
0.7716 389.55
0.8315 389.59
0.8709 389.70
0.8972 389.82
0.9250 390.01
0.9444 390.18
0.9582 390.32
1.0000 390.85

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 0.9733 (VLE)

Fixed Measured
P [kPa] - VLE x1[mol/mol] of 1-Butanol (2) - Liquid y1[mol/mol] of 1-Butanol (2) - Vapour
100.792 0.0060 0.0860
100.792 0.0400 0.2550
99.192 0.0420 0.3000
100.925 0.1960 0.5590
100.658 0.2840 0.5960
100.392 0.3620 0.6260
100.125 0.4380 0.6450
99.992 0.5040 0.6700
100.125 0.5880 0.6940
100.125 0.5920 0.6960
100.125 0.6070 0.7020
100.125 0.6450 0.7180
100.525 0.6870 0.7360
99.059 0.7240 0.7520
98.925 0.7400 0.7620
98.925 0.7590 0.7720
100.258 0.7810 0.7860
99.725 0.8520 0.8310
100.258 0.8790 0.8550
100.258 0.8840 0.8550
100.258 0.9190 0.8950
99.858 0.9840 0.9730

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 95 (VLE)

T [K] - VLE x1[mol/mol] of 1-Butanol (2) - Liquid
407.95 0.0000
398.15 0.0930
394.25 0.2011
392.45 0.3020
391.25 0.3900
390.15 0.5030
389.65 0.6030
389.15 0.6950
388.85 0.7960
389.05 0.9015
389.05 1.0000

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 308.15 (VLE)

P [kPa] - VLE x1[mol/mol] of 1-Butanol (2) - Liquid
2.2 0.0530
2.4505 0.1110
2.6904 0.1715
2.9504 0.2505
3.08 0.3190
3.2 0.3925
3.2304 0.4425
3.2704 0.5090
3.3104 0.5925
3.2704 0.6495
3.2104 0.7260
2.9104 0.8315
2.5705 0.8945
2.16 0.9460
1.7905 1.0000

Sources