Datasets
-
Mole fraction (2)
-
Tboil - Boiling temperature at pressure P, K (2)
-
Tfus - Solid-liquid equilibrium temperature, K (8)
Mole fraction of Tetradecanoic acid, ethyl ester (2)
[ref]
Fixed |
Measured |
Mole fraction of Tetradecanoic acid, ethyl ester (2) - Liquid |
Pressure, kPa - Gas |
Mole fraction of Tetradecanoic acid, ethyl ester (2) - Gas |
0.0000 |
0.50 |
0.0000 |
0.0794 |
0.50 |
0.2103 |
0.0998 |
0.50 |
0.2538 |
0.1420 |
0.50 |
0.3369 |
0.2222 |
0.50 |
0.4673 |
0.3126 |
0.50 |
0.5823 |
0.4304 |
0.50 |
0.6988 |
0.5193 |
0.50 |
0.7673 |
0.5843 |
0.50 |
0.8105 |
0.6338 |
0.50 |
0.8401 |
0.7618 |
0.50 |
0.9064 |
0.8665 |
0.50 |
0.9512 |
0.9271 |
0.50 |
0.9743 |
1.0000 |
0.50 |
1.0000 |
0.0000 |
1.00 |
0.0000 |
0.0829 |
1.00 |
0.2110 |
0.0999 |
1.00 |
0.2421 |
0.1569 |
1.00 |
0.3495 |
0.2543 |
1.00 |
0.4970 |
0.3691 |
1.00 |
0.6283 |
0.4882 |
1.00 |
0.7331 |
0.5282 |
1.00 |
0.7632 |
0.5907 |
1.00 |
0.8029 |
0.7077 |
1.00 |
0.8722 |
0.8114 |
1.00 |
0.9236 |
0.8675 |
1.00 |
0.9480 |
0.9264 |
1.00 |
0.9718 |
1.0000 |
1.00 |
1.0000 |
0.0000 |
1.50 |
0.0000 |
0.0961 |
1.50 |
0.2299 |
0.1162 |
1.50 |
0.2689 |
0.1678 |
1.50 |
0.3608 |
0.2360 |
1.50 |
0.4627 |
0.3502 |
1.50 |
0.5988 |
0.4475 |
1.50 |
0.6912 |
0.5032 |
1.50 |
0.7366 |
0.5542 |
1.50 |
0.7741 |
0.6900 |
1.50 |
0.8594 |
0.7693 |
1.50 |
0.9009 |
0.8231 |
1.50 |
0.9266 |
0.9320 |
1.50 |
0.9699 |
1.0000 |
1.50 |
1.0000 |
Mole fraction of Tetradecanoic acid, ethyl ester (2)
[ref]
Fixed |
Measured |
Mole fraction of Tetradecanoic acid, ethyl ester (2) - Liquid |
Pressure, kPa - Gas |
Mole fraction of Tetradecanoic acid, ethyl ester (2) - Gas |
0.0000 |
0.50 |
0.0000 |
0.0794 |
0.50 |
0.2103 |
0.0998 |
0.50 |
0.2538 |
0.1420 |
0.50 |
0.3369 |
0.2222 |
0.50 |
0.4673 |
0.3126 |
0.50 |
0.5823 |
0.4304 |
0.50 |
0.6988 |
0.5193 |
0.50 |
0.7673 |
0.5843 |
0.50 |
0.8105 |
0.6338 |
0.50 |
0.8401 |
0.7618 |
0.50 |
0.9064 |
0.8665 |
0.50 |
0.9512 |
0.9271 |
0.50 |
0.9743 |
1.0000 |
0.50 |
1.0000 |
0.0000 |
1.00 |
0.0000 |
0.0829 |
1.00 |
0.2110 |
0.0999 |
1.00 |
0.2421 |
0.1569 |
1.00 |
0.3495 |
0.2543 |
1.00 |
0.4970 |
0.3691 |
1.00 |
0.6283 |
0.4882 |
1.00 |
0.7331 |
0.5282 |
1.00 |
0.7632 |
0.5907 |
1.00 |
0.8029 |
0.7077 |
1.00 |
0.8722 |
0.8114 |
1.00 |
0.9236 |
0.8675 |
1.00 |
0.9480 |
0.9264 |
1.00 |
0.9718 |
1.0000 |
1.00 |
1.0000 |
0.0000 |
1.50 |
0.0000 |
0.0961 |
1.50 |
0.2299 |
0.1162 |
1.50 |
0.2689 |
0.1678 |
1.50 |
0.3608 |
0.2360 |
1.50 |
0.4627 |
0.3502 |
1.50 |
0.5988 |
0.4475 |
1.50 |
0.6912 |
0.5032 |
1.50 |
0.7366 |
0.5542 |
1.50 |
0.7741 |
0.6900 |
1.50 |
0.8594 |
0.7693 |
1.50 |
0.9009 |
0.8231 |
1.50 |
0.9266 |
0.9320 |
1.50 |
0.9699 |
1.0000 |
1.50 |
1.0000 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of Tetradecanoic acid, ethyl ester (2) - Liquid |
Pressure, kPa - Gas |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
0.50 |
442.68 |
0.0794 |
0.50 |
440.18 |
0.0998 |
0.50 |
439.46 |
0.1420 |
0.50 |
437.96 |
0.2222 |
0.50 |
435.52 |
0.3126 |
0.50 |
433.10 |
0.4304 |
0.50 |
430.33 |
0.5193 |
0.50 |
428.53 |
0.5843 |
0.50 |
427.18 |
0.6338 |
0.50 |
426.34 |
0.7618 |
0.50 |
424.16 |
0.8665 |
0.50 |
422.68 |
0.9271 |
0.50 |
421.79 |
1.0000 |
0.50 |
420.46 |
0.0000 |
1.00 |
457.98 |
0.0829 |
1.00 |
455.23 |
0.0999 |
1.00 |
454.10 |
0.1569 |
1.00 |
452.21 |
0.2543 |
1.00 |
449.20 |
0.3691 |
1.00 |
446.21 |
0.4882 |
1.00 |
443.40 |
0.5282 |
1.00 |
441.74 |
0.5907 |
1.00 |
440.64 |
0.7077 |
1.00 |
438.47 |
0.8114 |
1.00 |
436.91 |
0.8675 |
1.00 |
436.05 |
0.9264 |
1.00 |
435.58 |
1.0000 |
1.00 |
434.98 |
0.0000 |
1.50 |
468.07 |
0.0961 |
1.50 |
464.75 |
0.1162 |
1.50 |
463.97 |
0.1678 |
1.50 |
462.20 |
0.2360 |
1.50 |
460.15 |
0.3502 |
1.50 |
457.06 |
0.4475 |
1.50 |
454.73 |
0.5032 |
1.50 |
453.46 |
0.5542 |
1.50 |
452.38 |
0.6900 |
1.50 |
449.72 |
0.7693 |
1.50 |
448.38 |
0.8231 |
1.50 |
447.50 |
0.9320 |
1.50 |
445.91 |
1.0000 |
1.50 |
444.05 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of Tetradecanoic acid, ethyl ester (2) - Liquid |
Pressure, kPa - Gas |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
0.50 |
442.68 |
0.0794 |
0.50 |
440.18 |
0.0998 |
0.50 |
439.46 |
0.1420 |
0.50 |
437.96 |
0.2222 |
0.50 |
435.52 |
0.3126 |
0.50 |
433.10 |
0.4304 |
0.50 |
430.33 |
0.5193 |
0.50 |
428.53 |
0.5843 |
0.50 |
427.18 |
0.6338 |
0.50 |
426.34 |
0.7618 |
0.50 |
424.16 |
0.8665 |
0.50 |
422.68 |
0.9271 |
0.50 |
421.79 |
1.0000 |
0.50 |
420.46 |
0.0000 |
1.00 |
457.98 |
0.0829 |
1.00 |
455.23 |
0.0999 |
1.00 |
454.10 |
0.1569 |
1.00 |
452.21 |
0.2543 |
1.00 |
449.20 |
0.3691 |
1.00 |
446.21 |
0.4882 |
1.00 |
443.40 |
0.5282 |
1.00 |
441.74 |
0.5907 |
1.00 |
440.64 |
0.7077 |
1.00 |
438.47 |
0.8114 |
1.00 |
436.91 |
0.8675 |
1.00 |
436.05 |
0.9264 |
1.00 |
435.58 |
1.0000 |
1.00 |
434.98 |
0.0000 |
1.50 |
468.07 |
0.0961 |
1.50 |
464.75 |
0.1162 |
1.50 |
463.97 |
0.1678 |
1.50 |
462.20 |
0.2360 |
1.50 |
460.15 |
0.3502 |
1.50 |
457.06 |
0.4475 |
1.50 |
454.73 |
0.5032 |
1.50 |
453.46 |
0.5542 |
1.50 |
452.38 |
0.6900 |
1.50 |
449.72 |
0.7693 |
1.50 |
448.38 |
0.8231 |
1.50 |
447.50 |
0.9320 |
1.50 |
445.91 |
1.0000 |
1.50 |
444.05 |
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Mole fraction of Tetradecanoic acid, ethyl ester (2) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
0.0000 |
298.23 |
0.0518 |
297.12 |
0.0982 |
296.76 |
0.1955 |
294.94 |
0.3103 |
292.68 |
0.4036 |
290.50 |
0.4861 |
288.24 |
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Mole fraction of Tetradecanoic acid, ethyl ester (2) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
0.8999 |
284.38 |
0.9476 |
284.94 |
1.0000 |
287.23 |
Solid-liquid equilibrium temperature, K
[ref]
Fixed |
Measured |
Pressure, kPa - Liquid |
Mole fraction of Tetradecanoic acid, ethyl ester (2) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
100.00 |
0.0000 |
297.60 |
100.00 |
0.2009 |
294.60 |
100.00 |
0.3993 |
291.30 |
100.00 |
0.5006 |
288.80 |
100.00 |
0.5992 |
285.10 |
100.00 |
0.6981 |
283.40 |
20000.00 |
0.0000 |
302.00 |
20000.00 |
0.2009 |
299.30 |
20000.00 |
0.3993 |
296.20 |
20000.00 |
0.5006 |
293.30 |
20000.00 |
0.5992 |
289.20 |
20000.00 |
0.6981 |
287.70 |
40000.00 |
0.0000 |
306.40 |
40000.00 |
0.2009 |
303.70 |
40000.00 |
0.3993 |
301.10 |
40000.00 |
0.5006 |
298.00 |
40000.00 |
0.5992 |
293.90 |
40000.00 |
0.6981 |
292.10 |
60000.00 |
0.0000 |
310.30 |
60000.00 |
0.2009 |
307.80 |
60000.00 |
0.3993 |
305.40 |
60000.00 |
0.5006 |
302.40 |
60000.00 |
0.5992 |
297.90 |
60000.00 |
0.6981 |
295.80 |
80000.00 |
0.0000 |
314.30 |
80000.00 |
0.2009 |
311.80 |
80000.00 |
0.3993 |
309.20 |
80000.00 |
0.5006 |
306.30 |
80000.00 |
0.5992 |
301.50 |
80000.00 |
0.6981 |
299.10 |
Solid-liquid equilibrium temperature, K
[ref]
Fixed |
Measured |
Pressure, kPa - Liquid |
Mole fraction of Tetradecanoic acid, ethyl ester (2) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
100.00 |
0.7489 |
282.60 |
100.00 |
0.7996 |
282.80 |
100.00 |
0.8997 |
284.20 |
100.00 |
1.0000 |
285.80 |
20000.00 |
0.7489 |
286.80 |
20000.00 |
0.7996 |
287.10 |
20000.00 |
0.8997 |
288.60 |
20000.00 |
1.0000 |
289.90 |
40000.00 |
0.7489 |
290.80 |
40000.00 |
0.7996 |
291.30 |
40000.00 |
0.8997 |
292.20 |
40000.00 |
1.0000 |
294.10 |
60000.00 |
0.7489 |
294.50 |
60000.00 |
0.7996 |
295.20 |
60000.00 |
0.8997 |
296.00 |
60000.00 |
1.0000 |
298.00 |
80000.00 |
0.7489 |
298.50 |
80000.00 |
0.7996 |
298.90 |
80000.00 |
0.8997 |
299.50 |
80000.00 |
1.0000 |
301.90 |
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Mole fraction of Tetradecanoic acid, ethyl ester (2) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
0.0000 |
298.23 |
0.0518 |
297.12 |
0.0982 |
296.76 |
0.1955 |
294.94 |
0.3103 |
292.68 |
0.4036 |
290.50 |
0.4861 |
288.24 |
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Mole fraction of Tetradecanoic acid, ethyl ester (2) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
0.8999 |
284.38 |
0.9476 |
284.94 |
1.0000 |
287.23 |
Solid-liquid equilibrium temperature, K
[ref]
Fixed |
Measured |
Pressure, kPa - Liquid |
Mole fraction of Tetradecanoic acid, ethyl ester (2) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
100.00 |
0.0000 |
297.60 |
100.00 |
0.2009 |
294.60 |
100.00 |
0.3993 |
291.30 |
100.00 |
0.5006 |
288.80 |
100.00 |
0.5992 |
285.10 |
100.00 |
0.6981 |
283.40 |
20000.00 |
0.0000 |
302.00 |
20000.00 |
0.2009 |
299.30 |
20000.00 |
0.3993 |
296.20 |
20000.00 |
0.5006 |
293.30 |
20000.00 |
0.5992 |
289.20 |
20000.00 |
0.6981 |
287.70 |
40000.00 |
0.0000 |
306.40 |
40000.00 |
0.2009 |
303.70 |
40000.00 |
0.3993 |
301.10 |
40000.00 |
0.5006 |
298.00 |
40000.00 |
0.5992 |
293.90 |
40000.00 |
0.6981 |
292.10 |
60000.00 |
0.0000 |
310.30 |
60000.00 |
0.2009 |
307.80 |
60000.00 |
0.3993 |
305.40 |
60000.00 |
0.5006 |
302.40 |
60000.00 |
0.5992 |
297.90 |
60000.00 |
0.6981 |
295.80 |
80000.00 |
0.0000 |
314.30 |
80000.00 |
0.2009 |
311.80 |
80000.00 |
0.3993 |
309.20 |
80000.00 |
0.5006 |
306.30 |
80000.00 |
0.5992 |
301.50 |
80000.00 |
0.6981 |
299.10 |
Solid-liquid equilibrium temperature, K
[ref]
Fixed |
Measured |
Pressure, kPa - Liquid |
Mole fraction of Tetradecanoic acid, ethyl ester (2) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
100.00 |
0.7489 |
282.60 |
100.00 |
0.7996 |
282.80 |
100.00 |
0.8997 |
284.20 |
100.00 |
1.0000 |
285.80 |
20000.00 |
0.7489 |
286.80 |
20000.00 |
0.7996 |
287.10 |
20000.00 |
0.8997 |
288.60 |
20000.00 |
1.0000 |
289.90 |
40000.00 |
0.7489 |
290.80 |
40000.00 |
0.7996 |
291.30 |
40000.00 |
0.8997 |
292.20 |
40000.00 |
1.0000 |
294.10 |
60000.00 |
0.7489 |
294.50 |
60000.00 |
0.7996 |
295.20 |
60000.00 |
0.8997 |
296.00 |
60000.00 |
1.0000 |
298.00 |
80000.00 |
0.7489 |
298.50 |
80000.00 |
0.7996 |
298.90 |
80000.00 |
0.8997 |
299.50 |
80000.00 |
1.0000 |
301.90 |
Sources