Mixture of n-Hexane + Acetonitrile

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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

Acetonitrile

Name
Acetonitrile
InChI
InChI=1S/C2H3N/c1-2-3/h1H3
InChI Key
WEVYAHXRMPXWCK-UHFFFAOYSA-N
Formula
C2H3N
SMILES
CC#N
Mol. Weight (g/mol)
41.05
CAS
75-05-8
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Datasets

  1. Mole fraction (6)
  2. Pvap - Vapor or sublimation pressure, kPa (2)
  3. Vapor Liquid Equilibrium at Constant Temperature

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

Operational condition: Pressure, kPa = 350 (Liquid mixture 1)

Temperature, K - Liquid mixture 1 Mole fraction of n-Hexane (1) - Liquid mixture 1
348.22 0.3120
344.43 0.2770
337.55 0.2210
331.36 0.1760
321.94 0.1090
313.13 0.0620

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

Operational condition: Pressure, kPa = 350 (Liquid mixture 1)

Temperature, K - Liquid mixture 1 Mole fraction of n-Hexane (1) - Liquid mixture 2
348.22 0.6540
344.43 0.7290
337.55 0.8050
331.36 0.8450
321.94 0.8890
313.13 0.9190

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

Operational condition: Temperature, K = 348.2 (Liquid)

Mole fraction of n-Hexane (1) - Liquid Mole fraction of n-Hexane (1) - Gas
0.0000 0.0000
0.0420 0.4750
0.0640 0.5250
0.0810 0.5650
0.0990 0.5950
0.1320 0.6240
0.3120 0.6500
0.6540 0.6500
0.8720 0.6740
0.9160 0.7140
0.9340 0.7560
0.9710 0.8150
0.9890 0.8990
1.0000 1.0000

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

Operational condition: Pressure, kPa = 350 (Liquid mixture 1)

Temperature, K - Liquid mixture 1 Mole fraction of n-Hexane (1) - Liquid mixture 1
348.22 0.3120
344.43 0.2770
337.55 0.2210
331.36 0.1760
321.94 0.1090
313.13 0.0620

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

Operational condition: Pressure, kPa = 350 (Liquid mixture 1)

Temperature, K - Liquid mixture 1 Mole fraction of n-Hexane (1) - Liquid mixture 2
348.22 0.6540
344.43 0.7290
337.55 0.8050
331.36 0.8450
321.94 0.8890
313.13 0.9190

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

Operational condition: Temperature, K = 348.2 (Liquid)

Mole fraction of n-Hexane (1) - Liquid Mole fraction of n-Hexane (1) - Gas
0.0000 0.0000
0.0420 0.4750
0.0640 0.5250
0.0810 0.5650
0.0990 0.5950
0.1320 0.6240
0.3120 0.6500
0.6540 0.6500
0.8720 0.6740
0.9160 0.7140
0.9340 0.7560
0.9710 0.8150
0.9890 0.8990
1.0000 1.0000

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 348.2 (Liquid)

Mole fraction of n-Hexane (1) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 83.70
0.0420 138.00
0.0640 151.50
0.0810 162.20
0.0990 171.80
0.1320 184.00
0.3120 188.00
0.6540 188.00
0.8720 184.40
0.9160 176.20
0.9340 169.10
0.9710 156.50
0.9890 140.50
1.0000 125.30

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 348.2 (Liquid)

Mole fraction of n-Hexane (1) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 83.70
0.0420 138.00
0.0640 151.50
0.0810 162.20
0.0990 171.80
0.1320 184.00
0.3120 188.00
0.6540 188.00
0.8720 184.40
0.9160 176.20
0.9340 169.10
0.9710 156.50
0.9890 140.50
1.0000 125.30

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 348.2 (VLE)

Fixed Measured
P [kPa] - VLE x1[mol/mol] of n-Hexane (1) - Liquid y1[mol/mol] of n-Hexane (1) - Vapour
83.7 0.0000 0.0000
137.999 0.0420 0.4750
151.5 0.0640 0.5250
162.2 0.0810 0.5650
171.801 0.0990 0.5950
184.0 0.1320 0.6240
188.001 0.3120 0.6500
188.001 0.6540 0.6500
184.399 0.8720 0.6740
176.2 0.9160 0.7140
169.099 0.9340 0.7560
156.5 0.9710 0.8150
140.5 0.9890 0.8990
125.3 1.0000 1.0000

Sources