Mixture of Benzene + Hexadecane

Excel

Benzene

Name
Benzene
InChI
InChI=1S/C6H6/c1-2-4-6-5-3-1/h1-6H
InChI Key
UHOVQNZJYSORNB-UHFFFAOYSA-N
Formula
C6H6
SMILES
c1ccccc1
Mol. Weight (g/mol)
78.11
CAS
71-43-2

Hexadecane

Name
Hexadecane
InChI
InChI=1S/C16H34/c1-3-5-7-9-11-13-15-16-14-12-10-8-6-4-2/h3-16H2,1-2H3
InChI Key
DCAYPVUWAIABOU-UHFFFAOYSA-N
Formula
C16H34
SMILES
CCCCCCCCCCCCCCCC
Mol. Weight (g/mol)
226.44
CAS
544-76-3
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Datasets

  1. Pvap - Vapor or sublimation pressure, kPa (4)
  2. Vapor Liquid Equilibrium at Constant Temperature (3)

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of Hexadecane (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
293.15 0.2190 92700.00
293.15 0.2554 87200.00
293.15 0.3363 72740.00
293.15 0.4200 61580.00
293.15 0.5123 51050.00
293.15 0.5851 43470.00
293.15 0.6579 35890.00
293.15 0.7375 28690.00
293.15 0.8171 21500.00
293.15 0.8908 16020.00
293.15 0.9645 10550.00
293.15 1.0000 9210.00
303.15 0.2190 146020.00
303.15 0.2554 140140.00
303.15 0.3363 128400.00
303.15 0.4200 114090.00
303.15 0.5123 99540.00
303.15 0.5851 92000.00
303.15 0.6579 84450.00
303.15 0.7375 75130.00
303.15 0.8171 65810.00
303.15 0.8908 59900.00
303.15 0.9645 53980.00
303.15 1.0000 50650.00
313.15 0.2190 206840.00
313.15 0.2554 198750.00
313.15 0.3363 188350.00
313.15 0.4200 170800.00
313.15 0.5123 153170.00
313.15 0.5851 145190.00
313.15 0.6579 137210.00
313.15 0.7375 125990.00
313.15 0.8171 114770.00
313.15 0.8908 108000.00
313.15 0.9645 101240.00
313.15 1.0000 95560.00
323.15 0.2190 270640.00
323.15 0.2554 261740.00
323.15 0.3363 247640.00
323.15 0.4200 231720.00
323.15 0.5123 211940.00
323.15 0.5851 203050.00
323.15 0.6579 194170.00
323.15 0.7375 181260.00
323.15 0.8171 168350.00
323.15 0.8908 160330.00
323.15 0.9645 149990.00
323.15 1.0000 143920.00
333.15 0.2190 343010.00
333.15 0.2554 334110.00
333.15 0.3363 317000.00
333.15 0.4200 296840.00
333.15 0.5123 275860.00
333.15 0.5851 265590.00
333.15 0.6579 255310.00
333.15 0.7375 240940.00
333.15 0.8171 226580.00
333.15 0.8908 216880.00
333.15 0.9645 206300.00
333.15 1.0000 195740.00
343.15 0.2190 418600.00
343.15 0.2554 410870.00
343.15 0.3363 394000.00
343.15 0.4200 366170.00
343.15 0.5123 344920.00
343.15 0.5851 332790.00
343.15 0.6579 320660.00
343.15 0.7375 305040.00
343.15 0.8171 289430.00
343.15 0.8908 277660.00
343.15 0.9645 256570.00
343.15 1.0000 251030.00

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of Hexadecane (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
293.15 0.0000 53620.00
293.15 0.0199 61780.00
293.15 0.1009 81540.00
293.15 0.1197 88180.00
293.15 0.1750 98470.00
303.15 0.0000 92220.00
303.15 0.0199 102500.00
303.15 0.1009 128090.00
303.15 0.1197 135460.00
303.15 0.1750 150110.00
313.15 0.0000 133290.00
313.15 0.0199 147400.00
313.15 0.1009 176630.00
313.15 0.1197 185840.00
313.15 0.1750 204540.00
323.15 0.0000 176820.00
323.15 0.0199 192480.00
323.15 0.1009 227150.00
323.15 0.1197 239320.00
323.15 0.1750 261780.00
333.15 0.0000 222810.00
333.15 0.0199 239070.00
333.15 0.1009 279650.00
333.15 0.1197 295890.00
333.15 0.1750 321820.00
343.15 0.0000 271270.00
343.15 0.0199 287170.00
343.15 0.1009 338440.00
343.15 0.1197 352350.00
343.15 0.1750 384660.00

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of Hexadecane (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
293.15 0.2190 92700.00
293.15 0.2554 87200.00
293.15 0.3363 72740.00
293.15 0.4200 61580.00
293.15 0.5123 51050.00
293.15 0.5851 43470.00
293.15 0.6579 35890.00
293.15 0.7375 28690.00
293.15 0.8171 21500.00
293.15 0.8908 16020.00
293.15 0.9645 10550.00
293.15 1.0000 9210.00
303.15 0.2190 146020.00
303.15 0.2554 140140.00
303.15 0.3363 128400.00
303.15 0.4200 114090.00
303.15 0.5123 99540.00
303.15 0.5851 92000.00
303.15 0.6579 84450.00
303.15 0.7375 75130.00
303.15 0.8171 65810.00
303.15 0.8908 59900.00
303.15 0.9645 53980.00
303.15 1.0000 50650.00
313.15 0.2190 206840.00
313.15 0.2554 198750.00
313.15 0.3363 188350.00
313.15 0.4200 170800.00
313.15 0.5123 153170.00
313.15 0.5851 145190.00
313.15 0.6579 137210.00
313.15 0.7375 125990.00
313.15 0.8171 114770.00
313.15 0.8908 108000.00
313.15 0.9645 101240.00
313.15 1.0000 95560.00
323.15 0.2190 270640.00
323.15 0.2554 261740.00
323.15 0.3363 247640.00
323.15 0.4200 231720.00
323.15 0.5123 211940.00
323.15 0.5851 203050.00
323.15 0.6579 194170.00
323.15 0.7375 181260.00
323.15 0.8171 168350.00
323.15 0.8908 160330.00
323.15 0.9645 149990.00
323.15 1.0000 143920.00
333.15 0.2190 343010.00
333.15 0.2554 334110.00
333.15 0.3363 317000.00
333.15 0.4200 296840.00
333.15 0.5123 275860.00
333.15 0.5851 265590.00
333.15 0.6579 255310.00
333.15 0.7375 240940.00
333.15 0.8171 226580.00
333.15 0.8908 216880.00
333.15 0.9645 206300.00
333.15 1.0000 195740.00
343.15 0.2190 418600.00
343.15 0.2554 410870.00
343.15 0.3363 394000.00
343.15 0.4200 366170.00
343.15 0.5123 344920.00
343.15 0.5851 332790.00
343.15 0.6579 320660.00
343.15 0.7375 305040.00
343.15 0.8171 289430.00
343.15 0.8908 277660.00
343.15 0.9645 256570.00
343.15 1.0000 251030.00

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of Hexadecane (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
293.15 0.0000 53620.00
293.15 0.0199 61780.00
293.15 0.1009 81540.00
293.15 0.1197 88180.00
293.15 0.1750 98470.00
303.15 0.0000 92220.00
303.15 0.0199 102500.00
303.15 0.1009 128090.00
303.15 0.1197 135460.00
303.15 0.1750 150110.00
313.15 0.0000 133290.00
313.15 0.0199 147400.00
313.15 0.1009 176630.00
313.15 0.1197 185840.00
313.15 0.1750 204540.00
323.15 0.0000 176820.00
323.15 0.0199 192480.00
323.15 0.1009 227150.00
323.15 0.1197 239320.00
323.15 0.1750 261780.00
333.15 0.0000 222810.00
333.15 0.0199 239070.00
333.15 0.1009 279650.00
333.15 0.1197 295890.00
333.15 0.1750 321820.00
343.15 0.0000 271270.00
343.15 0.0199 287170.00
343.15 0.1009 338440.00
343.15 0.1197 352350.00
343.15 0.1750 384660.00

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 313.15 (VLE)

P [kPa] - VLE x1[mol/mol] of Benzene (1) - Liquid
8.599 0.3490
10.919 0.4430
12.532 0.5090
14.465 0.5800
15.919 0.6350
17.759 0.7140
18.798 0.7650
20.118 0.8180
20.798 0.8500
22.491 0.9170
23.251 0.9570
24.078 0.9940
24.331 1.0000

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 333.15 (VLE)

P [kPa] - VLE x1[mol/mol] of Benzene (1) - Liquid
0.0027 0.0000
7.719 0.1560
9.226 0.1860
12.972 0.2600
18.119 0.3590
22.758 0.4430
26.305 0.5090
30.198 0.5800
33.424 0.6350
37.317 0.7140
39.903 0.7650
42.676 0.8180
44.41 0.8500
48.023 0.9170
49.889 0.9570
51.676 0.9940
52.022 1.0000

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 353.15 (VLE)

P [kPa] - VLE x1[mol/mol] of Benzene (1) - Liquid
0.0147 0.0000
11.199 0.1230
15.919 0.1760
21.198 0.2330
22.478 0.2460
33.304 0.3590
41.943 0.4430
49.116 0.5090
56.889 0.5800
63.021 0.6350
71.061 0.7140
76.727 0.7650
81.993 0.8180
85.42 0.8500
92.859 0.9170
96.619 0.9570
100.552 1.0000

Sources