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 |
0.0312 |
505230.00 |
293.15 |
0.1007 |
393930.00 |
293.15 |
0.1798 |
334430.00 |
293.15 |
0.2589 |
274930.00 |
293.15 |
0.3403 |
247510.00 |
293.15 |
0.4196 |
226700.00 |
293.15 |
0.4994 |
206590.00 |
293.15 |
0.5616 |
199010.00 |
293.15 |
0.6587 |
184210.00 |
293.15 |
0.7391 |
170900.00 |
293.15 |
0.8084 |
162000.00 |
293.15 |
0.9001 |
149100.00 |
293.15 |
0.9791 |
138180.00 |
293.15 |
1.0000 |
133010.00 |
303.15 |
0.0312 |
599850.00 |
303.15 |
0.1007 |
486550.00 |
303.15 |
0.1798 |
423040.00 |
303.15 |
0.2589 |
359530.00 |
303.15 |
0.3403 |
330800.00 |
303.15 |
0.4196 |
311940.00 |
303.15 |
0.4994 |
284740.00 |
303.15 |
0.5616 |
270760.00 |
303.15 |
0.6587 |
254490.00 |
303.15 |
0.7391 |
241220.00 |
303.15 |
0.8084 |
229340.00 |
303.15 |
0.9001 |
218700.00 |
303.15 |
0.9791 |
205250.00 |
303.15 |
1.0000 |
197130.00 |
313.15 |
0.0312 |
688490.00 |
313.15 |
0.1007 |
574190.00 |
313.15 |
0.1798 |
509620.00 |
313.15 |
0.2589 |
445060.00 |
313.15 |
0.3403 |
419350.00 |
313.15 |
0.4196 |
394500.00 |
313.15 |
0.4994 |
367320.00 |
313.15 |
0.5616 |
349670.00 |
313.15 |
0.6587 |
329290.00 |
313.15 |
0.7391 |
315730.00 |
313.15 |
0.8084 |
299820.00 |
313.15 |
0.9001 |
290040.00 |
313.15 |
0.9791 |
276070.00 |
313.15 |
1.0000 |
265400.00 |
323.15 |
0.0312 |
776120.00 |
323.15 |
0.1007 |
656860.00 |
323.15 |
0.1798 |
594180.00 |
323.15 |
0.2589 |
531500.00 |
323.15 |
0.3403 |
513180.00 |
323.15 |
0.4196 |
482920.00 |
323.15 |
0.4994 |
454350.00 |
323.15 |
0.5616 |
435740.00 |
323.15 |
0.6587 |
408610.00 |
323.15 |
0.7391 |
394440.00 |
323.15 |
0.8084 |
376760.00 |
323.15 |
0.9001 |
363100.00 |
323.15 |
0.9791 |
350650.00 |
323.15 |
1.0000 |
337830.00 |
333.15 |
0.0312 |
863820.00 |
333.15 |
0.1007 |
734560.00 |
333.15 |
0.1798 |
676720.00 |
333.15 |
0.2589 |
618870.00 |
333.15 |
0.3403 |
599600.00 |
333.15 |
0.4196 |
577190.00 |
333.15 |
0.4994 |
545820.00 |
333.15 |
0.5616 |
528970.00 |
333.15 |
0.6587 |
492450.00 |
333.15 |
0.7391 |
477350.00 |
333.15 |
0.8084 |
460160.00 |
333.15 |
0.9001 |
437900.00 |
333.15 |
0.9791 |
428980.00 |
333.15 |
1.0000 |
414420.00 |
343.15 |
0.0312 |
969260.00 |
343.15 |
0.1007 |
825000.00 |
343.15 |
0.1798 |
786500.00 |
343.15 |
0.2589 |
748000.00 |
343.15 |
0.3403 |
707000.00 |
343.15 |
0.4196 |
677320.00 |
343.15 |
0.4994 |
641730.00 |
343.15 |
0.5616 |
620900.00 |
343.15 |
0.6587 |
580810.00 |
343.15 |
0.7391 |
564450.00 |
343.15 |
0.8084 |
550030.00 |
343.15 |
0.9001 |
514420.00 |
343.15 |
0.9791 |
498100.00 |
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 |
0.0312 |
505230.00 |
293.15 |
0.1007 |
393930.00 |
293.15 |
0.1798 |
334430.00 |
293.15 |
0.2589 |
274930.00 |
293.15 |
0.3403 |
247510.00 |
293.15 |
0.4196 |
226700.00 |
293.15 |
0.4994 |
206590.00 |
293.15 |
0.5616 |
199010.00 |
293.15 |
0.6587 |
184210.00 |
293.15 |
0.7391 |
170900.00 |
293.15 |
0.8084 |
162000.00 |
293.15 |
0.9001 |
149100.00 |
293.15 |
0.9791 |
138180.00 |
293.15 |
1.0000 |
133010.00 |
303.15 |
0.0312 |
599850.00 |
303.15 |
0.1007 |
486550.00 |
303.15 |
0.1798 |
423040.00 |
303.15 |
0.2589 |
359530.00 |
303.15 |
0.3403 |
330800.00 |
303.15 |
0.4196 |
311940.00 |
303.15 |
0.4994 |
284740.00 |
303.15 |
0.5616 |
270760.00 |
303.15 |
0.6587 |
254490.00 |
303.15 |
0.7391 |
241220.00 |
303.15 |
0.8084 |
229340.00 |
303.15 |
0.9001 |
218700.00 |
303.15 |
0.9791 |
205250.00 |
303.15 |
1.0000 |
197130.00 |
313.15 |
0.0312 |
688490.00 |
313.15 |
0.1007 |
574190.00 |
313.15 |
0.1798 |
509620.00 |
313.15 |
0.2589 |
445060.00 |
313.15 |
0.3403 |
419350.00 |
313.15 |
0.4196 |
394500.00 |
313.15 |
0.4994 |
367320.00 |
313.15 |
0.5616 |
349670.00 |
313.15 |
0.6587 |
329290.00 |
313.15 |
0.7391 |
315730.00 |
313.15 |
0.8084 |
299820.00 |
313.15 |
0.9001 |
290040.00 |
313.15 |
0.9791 |
276070.00 |
313.15 |
1.0000 |
265400.00 |
323.15 |
0.0312 |
776120.00 |
323.15 |
0.1007 |
656860.00 |
323.15 |
0.1798 |
594180.00 |
323.15 |
0.2589 |
531500.00 |
323.15 |
0.3403 |
513180.00 |
323.15 |
0.4196 |
482920.00 |
323.15 |
0.4994 |
454350.00 |
323.15 |
0.5616 |
435740.00 |
323.15 |
0.6587 |
408610.00 |
323.15 |
0.7391 |
394440.00 |
323.15 |
0.8084 |
376760.00 |
323.15 |
0.9001 |
363100.00 |
323.15 |
0.9791 |
350650.00 |
323.15 |
1.0000 |
337830.00 |
333.15 |
0.0312 |
863820.00 |
333.15 |
0.1007 |
734560.00 |
333.15 |
0.1798 |
676720.00 |
333.15 |
0.2589 |
618870.00 |
333.15 |
0.3403 |
599600.00 |
333.15 |
0.4196 |
577190.00 |
333.15 |
0.4994 |
545820.00 |
333.15 |
0.5616 |
528970.00 |
333.15 |
0.6587 |
492450.00 |
333.15 |
0.7391 |
477350.00 |
333.15 |
0.8084 |
460160.00 |
333.15 |
0.9001 |
437900.00 |
333.15 |
0.9791 |
428980.00 |
333.15 |
1.0000 |
414420.00 |
343.15 |
0.0312 |
969260.00 |
343.15 |
0.1007 |
825000.00 |
343.15 |
0.1798 |
786500.00 |
343.15 |
0.2589 |
748000.00 |
343.15 |
0.3403 |
707000.00 |
343.15 |
0.4196 |
677320.00 |
343.15 |
0.4994 |
641730.00 |
343.15 |
0.5616 |
620900.00 |
343.15 |
0.6587 |
580810.00 |
343.15 |
0.7391 |
564450.00 |
343.15 |
0.8084 |
550030.00 |
343.15 |
0.9001 |
514420.00 |
343.15 |
0.9791 |
498100.00 |
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 |
0.4103 |
255.32 |
0.4282 |
255.78 |
0.4480 |
256.65 |
0.4714 |
257.43 |
0.5056 |
258.44 |
0.5451 |
259.37 |
0.5745 |
260.06 |
0.6053 |
260.95 |
0.6397 |
262.05 |
0.6663 |
262.72 |
0.6957 |
263.31 |
0.7338 |
264.45 |
0.7731 |
265.30 |
0.8093 |
266.00 |
0.8372 |
266.74 |
0.8774 |
267.47 |
0.9203 |
268.13 |
0.9697 |
268.81 |
1.0000 |
269.01 |
Mole fraction of Tridecane (1)
Solid-liquid equilibrium temperature, K
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Mole fraction of Tridecane (1) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
0.0035 |
231.94 |
0.0665 |
240.75 |
0.1057 |
245.25 |
0.1473 |
247.76 |
0.1744 |
248.79 |
0.1981 |
249.62 |
0.2314 |
250.91 |
0.2593 |
251.64 |
0.2904 |
252.69 |
0.3058 |
253.15 |
0.3321 |
253.55 |
0.3457 |
253.77 |
0.3556 |
253.81 |
0.3702 |
254.12 |
0.3828 |
254.37 |
Mole fraction of Tridecane (1)
Solid-liquid equilibrium temperature, K
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Mole fraction of Tridecane (1) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
0.4103 |
255.32 |
0.4282 |
255.78 |
0.4480 |
256.65 |
0.4714 |
257.43 |
0.5056 |
258.44 |
0.5451 |
259.37 |
0.5745 |
260.06 |
0.6053 |
260.95 |
0.6397 |
262.05 |
0.6663 |
262.72 |
0.6957 |
263.31 |
0.7338 |
264.45 |
0.7731 |
265.30 |
0.8093 |
266.00 |
0.8372 |
266.74 |
0.8774 |
267.47 |
0.9203 |
268.13 |
0.9697 |
268.81 |
1.0000 |
269.01 |
Mole fraction of Tridecane (1)
Solid-liquid equilibrium temperature, K
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Mole fraction of Tridecane (1) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
0.0035 |
231.94 |
0.0665 |
240.75 |
0.1057 |
245.25 |
0.1473 |
247.76 |
0.1744 |
248.79 |
0.1981 |
249.62 |
0.2314 |
250.91 |
0.2593 |
251.64 |
0.2904 |
252.69 |
0.3058 |
253.15 |
0.3321 |
253.55 |
0.3457 |
253.77 |
0.3556 |
253.81 |
0.3702 |
254.12 |
0.3828 |
254.37 |
Mole fraction of Tridecane (1)
Solid-liquid equilibrium temperature, K
Sources