Datasets
-
Pvap - Vapor or sublimation pressure, kPa (4)
-
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