Datasets
-
Pvap - Vapor or sublimation pressure, kPa (2)
-
Tfus - Solid-liquid equilibrium temperature, K (4)
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Tridecane (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
293.15 |
0.0624 |
622920.00 |
293.15 |
0.1001 |
511920.00 |
293.15 |
0.1687 |
400920.00 |
293.15 |
0.2588 |
349060.00 |
293.15 |
0.3404 |
297210.00 |
293.15 |
0.4159 |
267710.00 |
293.15 |
0.4995 |
238200.00 |
293.15 |
0.5798 |
217950.00 |
293.15 |
0.6594 |
201260.00 |
293.15 |
0.7382 |
180780.00 |
293.15 |
0.8185 |
173710.00 |
293.15 |
0.8995 |
150380.00 |
293.15 |
0.9788 |
148100.00 |
293.15 |
1.0000 |
133010.00 |
303.15 |
0.0624 |
785650.00 |
303.15 |
0.1001 |
644020.00 |
303.15 |
0.1687 |
502390.00 |
303.15 |
0.2588 |
438360.00 |
303.15 |
0.3404 |
374320.00 |
303.15 |
0.4159 |
343210.00 |
303.15 |
0.4995 |
312100.00 |
303.15 |
0.5798 |
285830.00 |
303.15 |
0.6594 |
267380.00 |
303.15 |
0.7382 |
245040.00 |
303.15 |
0.8185 |
238270.00 |
303.15 |
0.8995 |
218700.00 |
303.15 |
0.9788 |
214950.00 |
303.15 |
1.0000 |
197130.00 |
313.15 |
0.0624 |
948380.00 |
313.15 |
0.1001 |
777770.00 |
313.15 |
0.1687 |
607150.00 |
313.15 |
0.2588 |
533350.00 |
313.15 |
0.3404 |
459550.00 |
313.15 |
0.4159 |
425680.00 |
313.15 |
0.4995 |
391810.00 |
313.15 |
0.5798 |
360590.00 |
313.15 |
0.6594 |
339930.00 |
313.15 |
0.7382 |
316600.00 |
313.15 |
0.8185 |
308250.00 |
313.15 |
0.8995 |
290310.00 |
313.15 |
0.9788 |
285920.00 |
313.15 |
1.0000 |
265400.00 |
323.15 |
0.0624 |
1111110.00 |
323.15 |
0.1001 |
913160.00 |
323.15 |
0.1687 |
715220.00 |
323.15 |
0.2588 |
634050.00 |
323.15 |
0.3404 |
552880.00 |
323.15 |
0.4159 |
515100.00 |
323.15 |
0.4995 |
477310.00 |
323.15 |
0.5798 |
442230.00 |
323.15 |
0.6594 |
418930.00 |
323.15 |
0.7382 |
395440.00 |
323.15 |
0.8185 |
383670.00 |
323.15 |
0.8995 |
365190.00 |
323.15 |
0.9788 |
361000.00 |
323.15 |
1.0000 |
337830.00 |
333.15 |
0.0624 |
1273840.00 |
333.15 |
0.1001 |
1050210.00 |
333.15 |
0.1687 |
826580.00 |
333.15 |
0.2588 |
740450.00 |
333.15 |
0.3404 |
654310.00 |
333.15 |
0.4159 |
611470.00 |
333.15 |
0.4995 |
568630.00 |
333.15 |
0.5798 |
530760.00 |
333.15 |
0.6594 |
504380.00 |
333.15 |
0.7382 |
481580.00 |
333.15 |
0.8185 |
464520.00 |
333.15 |
0.8995 |
443360.00 |
333.15 |
0.9788 |
440200.00 |
333.15 |
1.0000 |
414420.00 |
343.15 |
0.0624 |
1436570.00 |
343.15 |
0.1001 |
1188900.00 |
343.15 |
0.1687 |
941240.00 |
343.15 |
0.2588 |
852550.00 |
343.15 |
0.3404 |
763860.00 |
343.15 |
0.4159 |
714800.00 |
343.15 |
0.4995 |
665750.00 |
343.15 |
0.5798 |
626170.00 |
343.15 |
0.6594 |
596260.00 |
343.15 |
0.7382 |
575010.00 |
343.15 |
0.8185 |
550800.00 |
343.15 |
0.8995 |
524800.00 |
343.15 |
0.9788 |
523520.00 |
343.15 |
1.0000 |
495180.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Tridecane (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
293.15 |
0.0624 |
622920.00 |
293.15 |
0.1001 |
511920.00 |
293.15 |
0.1687 |
400920.00 |
293.15 |
0.2588 |
349060.00 |
293.15 |
0.3404 |
297210.00 |
293.15 |
0.4159 |
267710.00 |
293.15 |
0.4995 |
238200.00 |
293.15 |
0.5798 |
217950.00 |
293.15 |
0.6594 |
201260.00 |
293.15 |
0.7382 |
180780.00 |
293.15 |
0.8185 |
173710.00 |
293.15 |
0.8995 |
150380.00 |
293.15 |
0.9788 |
148100.00 |
293.15 |
1.0000 |
133010.00 |
303.15 |
0.0624 |
785650.00 |
303.15 |
0.1001 |
644020.00 |
303.15 |
0.1687 |
502390.00 |
303.15 |
0.2588 |
438360.00 |
303.15 |
0.3404 |
374320.00 |
303.15 |
0.4159 |
343210.00 |
303.15 |
0.4995 |
312100.00 |
303.15 |
0.5798 |
285830.00 |
303.15 |
0.6594 |
267380.00 |
303.15 |
0.7382 |
245040.00 |
303.15 |
0.8185 |
238270.00 |
303.15 |
0.8995 |
218700.00 |
303.15 |
0.9788 |
214950.00 |
303.15 |
1.0000 |
197130.00 |
313.15 |
0.0624 |
948380.00 |
313.15 |
0.1001 |
777770.00 |
313.15 |
0.1687 |
607150.00 |
313.15 |
0.2588 |
533350.00 |
313.15 |
0.3404 |
459550.00 |
313.15 |
0.4159 |
425680.00 |
313.15 |
0.4995 |
391810.00 |
313.15 |
0.5798 |
360590.00 |
313.15 |
0.6594 |
339930.00 |
313.15 |
0.7382 |
316600.00 |
313.15 |
0.8185 |
308250.00 |
313.15 |
0.8995 |
290310.00 |
313.15 |
0.9788 |
285920.00 |
313.15 |
1.0000 |
265400.00 |
323.15 |
0.0624 |
1111110.00 |
323.15 |
0.1001 |
913160.00 |
323.15 |
0.1687 |
715220.00 |
323.15 |
0.2588 |
634050.00 |
323.15 |
0.3404 |
552880.00 |
323.15 |
0.4159 |
515100.00 |
323.15 |
0.4995 |
477310.00 |
323.15 |
0.5798 |
442230.00 |
323.15 |
0.6594 |
418930.00 |
323.15 |
0.7382 |
395440.00 |
323.15 |
0.8185 |
383670.00 |
323.15 |
0.8995 |
365190.00 |
323.15 |
0.9788 |
361000.00 |
323.15 |
1.0000 |
337830.00 |
333.15 |
0.0624 |
1273840.00 |
333.15 |
0.1001 |
1050210.00 |
333.15 |
0.1687 |
826580.00 |
333.15 |
0.2588 |
740450.00 |
333.15 |
0.3404 |
654310.00 |
333.15 |
0.4159 |
611470.00 |
333.15 |
0.4995 |
568630.00 |
333.15 |
0.5798 |
530760.00 |
333.15 |
0.6594 |
504380.00 |
333.15 |
0.7382 |
481580.00 |
333.15 |
0.8185 |
464520.00 |
333.15 |
0.8995 |
443360.00 |
333.15 |
0.9788 |
440200.00 |
333.15 |
1.0000 |
414420.00 |
343.15 |
0.0624 |
1436570.00 |
343.15 |
0.1001 |
1188900.00 |
343.15 |
0.1687 |
941240.00 |
343.15 |
0.2588 |
852550.00 |
343.15 |
0.3404 |
763860.00 |
343.15 |
0.4159 |
714800.00 |
343.15 |
0.4995 |
665750.00 |
343.15 |
0.5798 |
626170.00 |
343.15 |
0.6594 |
596260.00 |
343.15 |
0.7382 |
575010.00 |
343.15 |
0.8185 |
550800.00 |
343.15 |
0.8995 |
524800.00 |
343.15 |
0.9788 |
523520.00 |
343.15 |
1.0000 |
495180.00 |
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Mole fraction of Tridecane (1) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
0.4898 |
255.00 |
0.5076 |
255.80 |
0.5200 |
256.29 |
0.5413 |
257.14 |
0.5633 |
258.00 |
0.5854 |
258.62 |
0.6044 |
259.33 |
0.6474 |
260.55 |
0.6783 |
261.48 |
0.7217 |
262.60 |
0.7457 |
263.17 |
0.7794 |
264.08 |
0.8003 |
264.65 |
0.8421 |
265.85 |
0.8968 |
267.11 |
0.9537 |
268.08 |
1.0000 |
269.01 |
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Mole fraction of Tridecane (1) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
0.0962 |
237.79 |
0.1227 |
239.70 |
0.1553 |
241.93 |
0.1774 |
243.33 |
0.2325 |
245.52 |
0.2591 |
246.93 |
0.2837 |
248.77 |
0.3145 |
249.45 |
0.3364 |
250.68 |
0.3872 |
252.53 |
0.4181 |
253.39 |
0.4464 |
254.01 |
0.4593 |
254.25 |
0.4776 |
254.59 |
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Mole fraction of Tridecane (1) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
0.4898 |
255.00 |
0.5076 |
255.80 |
0.5200 |
256.29 |
0.5413 |
257.14 |
0.5633 |
258.00 |
0.5854 |
258.62 |
0.6044 |
259.33 |
0.6474 |
260.55 |
0.6783 |
261.48 |
0.7217 |
262.60 |
0.7457 |
263.17 |
0.7794 |
264.08 |
0.8003 |
264.65 |
0.8421 |
265.85 |
0.8968 |
267.11 |
0.9537 |
268.08 |
1.0000 |
269.01 |
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Mole fraction of Tridecane (1) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
0.0962 |
237.79 |
0.1227 |
239.70 |
0.1553 |
241.93 |
0.1774 |
243.33 |
0.2325 |
245.52 |
0.2591 |
246.93 |
0.2837 |
248.77 |
0.3145 |
249.45 |
0.3364 |
250.68 |
0.3872 |
252.53 |
0.4181 |
253.39 |
0.4464 |
254.01 |
0.4593 |
254.25 |
0.4776 |
254.59 |
Sources