Mixture of p-Xylene + Benzene, 1,3-dimethyl-

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p-Xylene

Name
p-Xylene
InChI
InChI=1S/C8H10/c1-7-3-5-8(2)6-4-7/h3-6H,1-2H3
InChI Key
URLKBWYHVLBVBO-UHFFFAOYSA-N
Formula
C8H10
SMILES
Cc1ccc(C)cc1
Mol. Weight (g/mol)
106.17
CAS
106-42-3

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
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Datasets

  1. Mole fraction (2)
  2. Vapor Liquid Equilibrium at Constant Pressure (3)

Mole fraction of p-Xylene (1) [ref]

Operational condition: Pressure, kPa = 101.33 (Liquid)

Mole fraction of p-Xylene (1) - Liquid Mole fraction of p-Xylene (1) - Gas
1.0000 1.0000
0.9503 0.9515
0.8908 0.8930
0.8380 0.8410
0.7692 0.7731
0.7132 0.7175
0.6667 0.6713
0.6110 0.6158
0.5506 0.5556
0.4922 0.4971
0.4433 0.4480
0.3759 0.3803
0.3388 0.3428
0.2946 0.2983
0.2372 0.2404
0.1959 0.1986
0.1601 0.1624
0.1221 0.1239
0.0682 0.0692
0.0000 0.0000

Mole fraction of p-Xylene (1) [ref]

Operational condition: Pressure, kPa = 101.33 (Liquid)

Mole fraction of p-Xylene (1) - Liquid Mole fraction of p-Xylene (1) - Gas
1.0000 1.0000
0.9503 0.9515
0.8908 0.8930
0.8380 0.8410
0.7692 0.7731
0.7132 0.7175
0.6667 0.6713
0.6110 0.6158
0.5506 0.5556
0.4922 0.4971
0.4433 0.4480
0.3759 0.3803
0.3388 0.3428
0.2946 0.2983
0.2372 0.2404
0.1959 0.1986
0.1601 0.1624
0.1221 0.1239
0.0682 0.0692
0.0000 0.0000

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

T [K] - VLE x1[mol/mol] of p-Xylene (1) - Liquid
412.24 0.0000
412.17 0.1000
412.09 0.2000
412.01 0.3000
411.94 0.4000
411.88 0.5000
411.8 0.6000
411.71 0.7000
411.64 0.8000
411.56 0.9000
411.49 1.0000

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of p-Xylene (1) - Liquid y1[mol/mol] of p-Xylene (1) - Vapour
412.25 0.0000 0.0000
412.18 0.1000 0.1018
412.1 0.2000 0.2032
412.03 0.3000 0.3042
411.95 0.4000 0.4048
411.88 0.5000 0.5050
411.8 0.6000 0.6048
411.73 0.7000 0.7042
411.65 0.8000 0.8032
411.58 0.9000 0.9018
411.5 1.0000 1.0000

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 6.66 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of p-Xylene (1) - Liquid y1[mol/mol] of p-Xylene (1) - Vapour
333.25 0.0000 0.0000
333.15 0.0840 0.0870
333.1 0.1550 0.1600
333.05 0.2440 0.2510
332.95 0.3310 0.3390
332.85 0.4090 0.4190
332.8 0.4900 0.5000
332.75 0.5710 0.5800
332.65 0.6530 0.6640
332.6 0.7360 0.7460
332.5 0.8160 0.8240
332.45 0.8960 0.8990
332.4 0.9480 0.9480
332.35 1.0000 1.0000

Sources