Mixture of n-Hexane + p-Xylene

Excel

n-Hexane

Name
n-Hexane
InChI
InChI=1S/C6H14/c1-3-5-6-4-2/h3-6H2,1-2H3
InChI Key
VLKZOEOYAKHREP-UHFFFAOYSA-N
Formula
C6H14
SMILES
CCCCCC
Mol. Weight (g/mol)
86.18
CAS
110-54-3

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
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry. Do not hesitate to contact us for your projects.

Datasets

  1. Mole fraction (2)
  2. η - Viscosity, Pa*s (2)
  3. ρl - Mass density, kg/m3 (6)
  4. γ - Surface tension liquid-gas, N/m (2)
  5. Vapor Liquid Equilibrium at Constant Pressure (2)
  6. Vapor Liquid Equilibrium at Constant Temperature

Mole fraction of n-Hexane (1) [ref]

Operational conditions:

Mole fraction of n-Hexane (1) - Liquid mixture 1
0.9290
0.8590
0.7900
0.7340
0.6010
0.4700
0.3470
0.2160

Mole fraction of n-Hexane (1) [ref]

Operational conditions:

Mole fraction of n-Hexane (1) - Liquid mixture 1
0.9290
0.8590
0.7900
0.7340
0.6010
0.4700
0.3470
0.2160

Viscosity, Pa*s [ref]

Operational conditions:

Mole fraction of n-Hexane (1) - Liquid Viscosity, Pa*s - Liquid
0.0423 0.0006
0.1073 0.0005
0.2137 0.0005
0.2956 0.0004
0.3769 0.0004
0.4201 0.0004
0.5355 0.0004
0.5620 0.0004
0.6427 0.0004
0.7455 0.0003
0.7909 0.0003
0.8792 0.0003
0.9599 0.0003

Viscosity, Pa*s [ref]

Operational conditions:

Mole fraction of n-Hexane (1) - Liquid Viscosity, Pa*s - Liquid
0.0423 0.0006
0.1073 0.0005
0.2137 0.0005
0.2956 0.0004
0.3769 0.0004
0.4201 0.0004
0.5355 0.0004
0.5620 0.0004
0.6427 0.0004
0.7455 0.0003
0.7909 0.0003
0.8792 0.0003
0.9599 0.0003

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of n-Hexane (1) - Liquid Mass density, kg/m3 - Liquid
0.0423 847.8
0.1073 834.45
0.2137 812.6
0.2956 795.81
0.3769 779.21
0.4201 770.42
0.5355 747.03
0.5620 741.69
0.6427 725.47
0.7455 704.95
0.7909 695.94
0.8792 678.48
0.9599 662.62

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of n-Hexane (1) - Liquid Mass density, kg/m3 - Liquid
0.0000 856.59
0.0480 847.14
0.0980 836.82
0.1960 816.92
0.2920 797.23
0.3940 776.41
0.4920 756.57
0.5910 736.73
0.6920 716.48
0.7920 696.69
0.8920 676.71
0.9480 665.7
1.0000 655.19

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of n-Hexane (1) - Liquid Mass density, kg/m3 - Liquid
0.0393 848.42
0.0869 838.63
0.1535 824.96
0.2080 813.78
0.3063 793.59
0.3524 784.21
0.4333 767.75
0.4867 756.93
0.5404 746.02
0.5836 737.32
0.6380 726.41
0.6903 715.94
0.7872 696.69
0.8297 688.25
0.8952 675.28
0.9417 666.19

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of n-Hexane (1) - Liquid Mass density, kg/m3 - Liquid
0.0423 847.8
0.1073 834.45
0.2137 812.6
0.2956 795.81
0.3769 779.21
0.4201 770.42
0.5355 747.03
0.5620 741.69
0.6427 725.47
0.7455 704.95
0.7909 695.94
0.8792 678.48
0.9599 662.62

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of n-Hexane (1) - Liquid Mass density, kg/m3 - Liquid
0.0000 856.59
0.0480 847.14
0.0980 836.82
0.1960 816.92
0.2920 797.23
0.3940 776.41
0.4920 756.57
0.5910 736.73
0.6920 716.48
0.7920 696.69
0.8920 676.71
0.9480 665.7
1.0000 655.19

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of n-Hexane (1) - Liquid Mass density, kg/m3 - Liquid
0.0393 848.42
0.0869 838.63
0.1535 824.96
0.2080 813.78
0.3063 793.59
0.3524 784.21
0.4333 767.75
0.4867 756.93
0.5404 746.02
0.5836 737.32
0.6380 726.41
0.6903 715.94
0.7872 696.69
0.8297 688.25
0.8952 675.28
0.9417 666.19

Surface tension liquid-gas, N/m [ref]

Operational condition: Temperature, K = 298.15 (Liquid)

Mole fraction of n-Hexane (1) - Liquid Surface tension liquid-gas, N/m - Liquid
0.0535 0.0268
0.0718 0.0266
0.1265 0.0258
0.1341 0.0257
0.3083 0.0234
0.3397 0.0231
0.3990 0.0225
0.4670 0.0218
0.4920 0.0216
0.5267 0.0213
0.6034 0.0207
0.6394 0.0204
0.6877 0.0201
0.7826 0.0194
0.8126 0.0192
0.8798 0.0188

Surface tension liquid-gas, N/m [ref]

Operational condition: Temperature, K = 298.15 (Liquid)

Mole fraction of n-Hexane (1) - Liquid Surface tension liquid-gas, N/m - Liquid
0.0535 0.0268
0.0718 0.0266
0.1265 0.0258
0.1341 0.0257
0.3083 0.0234
0.3397 0.0231
0.3990 0.0225
0.4670 0.0218
0.4920 0.0216
0.5267 0.0213
0.6034 0.0207
0.6394 0.0204
0.6877 0.0201
0.7826 0.0194
0.8126 0.0192
0.8798 0.0188

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of n-Hexane (1) - Liquid y1[mol/mol] of n-Hexane (1) - Vapour
409.25 0.0110 0.0690
403.15 0.0420 0.2250
391.45 0.1230 0.4870
385.25 0.1650 0.5870
382.95 0.1920 0.6250
369.45 0.3390 0.7850
364.45 0.4090 0.8310
359.75 0.4970 0.8670
356.05 0.5780 0.8980
351.35 0.7010 0.9410
347.95 0.7970 0.9660
345.75 0.8680 0.9780
343.15 0.9530 0.9930

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 95.8 (VLE)

T [K] - VLE x1[mol/mol] of n-Hexane (1) - Liquid
409.35 0.0000
378.75 0.1588
361.81 0.4303
352.55 0.6338
347.25 0.7756
342.75 0.9122
340.25 1.0000

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 313.15 (VLE)

P [kPa] - VLE x1[mol/mol] of n-Hexane (1) - Liquid
2.6544 0.0000
5.44 0.0560
9.239 0.1433
11.848 0.2071
15.871 0.3155
17.503 0.3627
19.438 0.4251
22.362 0.5200
24.511 0.5861
26.278 0.6454
28.111 0.7107
28.678 0.7252
30.553 0.7904
33.031 0.8718
34.982 0.9329
37.25 1.0000

Sources