Datasets
-
Eutectic temperature, K (2)
-
Tfus - Solid-liquid equilibrium temperature, K (16)
-
Ttriple - Triple point temperature, K (4)
Eutectic temperature, K
[ref]
Mole fraction of Dodecanoic acid, ethyl ester (1) - Liquid |
Eutectic temperature, K - Liquid |
0.9106 |
268.81 |
Eutectic temperature, K
[ref]
Mole fraction of Dodecanoic acid, ethyl ester (1) - Liquid |
Eutectic temperature, K - Liquid |
0.9106 |
268.81 |
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Mole fraction of Dodecanoic acid, ethyl ester (1) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
0.0000 |
298.23 |
0.1281 |
295.52 |
0.2077 |
294.31 |
0.3060 |
292.40 |
0.3935 |
291.17 |
0.5029 |
288.48 |
0.5929 |
285.75 |
0.7033 |
282.10 |
0.7868 |
278.23 |
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Mole fraction of Dodecanoic acid, ethyl ester (1) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
0.9502 |
271.38 |
1.0000 |
273.20 |
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
100 (Crystal)
Mole fraction of Dodecanoic acid, ethyl ester (1) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
0.0000 |
298.23 |
0.1281 |
295.52 |
0.2077 |
294.31 |
0.3060 |
292.40 |
0.3935 |
291.17 |
0.5029 |
288.48 |
0.5929 |
285.75 |
0.7033 |
282.10 |
0.7868 |
278.23 |
0.8502 |
272.00 |
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
100 (Crystal)
Mole fraction of Dodecanoic acid, ethyl ester (1) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
0.9502 |
271.38 |
1.0000 |
273.20 |
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Mole fraction of Dodecanoic acid, ethyl ester (1) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
0.0000 |
298.23 |
0.1281 |
295.52 |
0.2077 |
294.31 |
0.3060 |
292.40 |
0.3935 |
291.17 |
0.5029 |
288.48 |
0.5929 |
285.75 |
0.7033 |
282.10 |
0.7868 |
278.23 |
0.8502 |
272.00 |
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Mole fraction of Dodecanoic acid, ethyl ester (1) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
0.9502 |
271.38 |
1.0000 |
273.20 |
Solid-liquid equilibrium temperature, K
[ref]
Fixed |
Measured |
Pressure, kPa - Liquid |
Mole fraction of Dodecanoic acid, ethyl ester (1) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
100.00 |
0.0000 |
297.60 |
100.00 |
0.2002 |
295.70 |
100.00 |
0.4013 |
293.40 |
100.00 |
0.6004 |
288.50 |
100.00 |
0.6979 |
284.60 |
100.00 |
0.8003 |
279.10 |
100.00 |
0.8478 |
275.30 |
20000.00 |
0.0000 |
302.00 |
20000.00 |
0.2002 |
300.50 |
20000.00 |
0.4013 |
297.60 |
20000.00 |
0.6004 |
292.40 |
20000.00 |
0.6979 |
289.90 |
20000.00 |
0.8003 |
284.00 |
20000.00 |
0.8478 |
279.40 |
40000.00 |
0.0000 |
306.40 |
40000.00 |
0.2002 |
304.90 |
40000.00 |
0.4013 |
302.00 |
40000.00 |
0.6004 |
296.60 |
40000.00 |
0.6979 |
293.70 |
40000.00 |
0.8003 |
288.50 |
40000.00 |
0.8478 |
282.80 |
60000.00 |
0.0000 |
310.30 |
60000.00 |
0.2002 |
308.50 |
60000.00 |
0.4013 |
306.50 |
60000.00 |
0.6004 |
300.90 |
60000.00 |
0.6979 |
297.50 |
60000.00 |
0.8003 |
292.00 |
60000.00 |
0.8478 |
286.70 |
80000.00 |
0.0000 |
314.30 |
80000.00 |
0.2002 |
312.70 |
80000.00 |
0.4013 |
311.10 |
80000.00 |
0.6004 |
305.30 |
80000.00 |
0.6979 |
301.80 |
80000.00 |
0.8003 |
295.10 |
80000.00 |
0.8478 |
290.90 |
Solid-liquid equilibrium temperature, K
[ref]
Fixed |
Measured |
Pressure, kPa - Liquid |
Mole fraction of Dodecanoic acid, ethyl ester (1) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
100.00 |
0.9003 |
269.80 |
100.00 |
1.0000 |
272.30 |
20000.00 |
0.9003 |
273.90 |
20000.00 |
1.0000 |
276.40 |
40000.00 |
0.9003 |
277.80 |
40000.00 |
1.0000 |
280.30 |
60000.00 |
0.9003 |
281.80 |
60000.00 |
1.0000 |
284.00 |
80000.00 |
0.9003 |
285.60 |
80000.00 |
1.0000 |
287.40 |
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Mole fraction of Dodecanoic acid, ethyl ester (1) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
0.0000 |
298.23 |
0.1281 |
295.52 |
0.2077 |
294.31 |
0.3060 |
292.40 |
0.3935 |
291.17 |
0.5029 |
288.48 |
0.5929 |
285.75 |
0.7033 |
282.10 |
0.7868 |
278.23 |
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Mole fraction of Dodecanoic acid, ethyl ester (1) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
0.9502 |
271.38 |
1.0000 |
273.20 |
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
100 (Crystal)
Mole fraction of Dodecanoic acid, ethyl ester (1) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
0.0000 |
298.23 |
0.1281 |
295.52 |
0.2077 |
294.31 |
0.3060 |
292.40 |
0.3935 |
291.17 |
0.5029 |
288.48 |
0.5929 |
285.75 |
0.7033 |
282.10 |
0.7868 |
278.23 |
0.8502 |
272.00 |
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
100 (Crystal)
Mole fraction of Dodecanoic acid, ethyl ester (1) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
0.9502 |
271.38 |
1.0000 |
273.20 |
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Mole fraction of Dodecanoic acid, ethyl ester (1) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
0.0000 |
298.23 |
0.1281 |
295.52 |
0.2077 |
294.31 |
0.3060 |
292.40 |
0.3935 |
291.17 |
0.5029 |
288.48 |
0.5929 |
285.75 |
0.7033 |
282.10 |
0.7868 |
278.23 |
0.8502 |
272.00 |
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Mole fraction of Dodecanoic acid, ethyl ester (1) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
0.9502 |
271.38 |
1.0000 |
273.20 |
Solid-liquid equilibrium temperature, K
[ref]
Fixed |
Measured |
Pressure, kPa - Liquid |
Mole fraction of Dodecanoic acid, ethyl ester (1) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
100.00 |
0.0000 |
297.60 |
100.00 |
0.2002 |
295.70 |
100.00 |
0.4013 |
293.40 |
100.00 |
0.6004 |
288.50 |
100.00 |
0.6979 |
284.60 |
100.00 |
0.8003 |
279.10 |
100.00 |
0.8478 |
275.30 |
20000.00 |
0.0000 |
302.00 |
20000.00 |
0.2002 |
300.50 |
20000.00 |
0.4013 |
297.60 |
20000.00 |
0.6004 |
292.40 |
20000.00 |
0.6979 |
289.90 |
20000.00 |
0.8003 |
284.00 |
20000.00 |
0.8478 |
279.40 |
40000.00 |
0.0000 |
306.40 |
40000.00 |
0.2002 |
304.90 |
40000.00 |
0.4013 |
302.00 |
40000.00 |
0.6004 |
296.60 |
40000.00 |
0.6979 |
293.70 |
40000.00 |
0.8003 |
288.50 |
40000.00 |
0.8478 |
282.80 |
60000.00 |
0.0000 |
310.30 |
60000.00 |
0.2002 |
308.50 |
60000.00 |
0.4013 |
306.50 |
60000.00 |
0.6004 |
300.90 |
60000.00 |
0.6979 |
297.50 |
60000.00 |
0.8003 |
292.00 |
60000.00 |
0.8478 |
286.70 |
80000.00 |
0.0000 |
314.30 |
80000.00 |
0.2002 |
312.70 |
80000.00 |
0.4013 |
311.10 |
80000.00 |
0.6004 |
305.30 |
80000.00 |
0.6979 |
301.80 |
80000.00 |
0.8003 |
295.10 |
80000.00 |
0.8478 |
290.90 |
Solid-liquid equilibrium temperature, K
[ref]
Fixed |
Measured |
Pressure, kPa - Liquid |
Mole fraction of Dodecanoic acid, ethyl ester (1) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
100.00 |
0.9003 |
269.80 |
100.00 |
1.0000 |
272.30 |
20000.00 |
0.9003 |
273.90 |
20000.00 |
1.0000 |
276.40 |
40000.00 |
0.9003 |
277.80 |
40000.00 |
1.0000 |
280.30 |
60000.00 |
0.9003 |
281.80 |
60000.00 |
1.0000 |
284.00 |
80000.00 |
0.9003 |
285.60 |
80000.00 |
1.0000 |
287.40 |
Triple point temperature, K
[ref]
Mole fraction of Dodecanoic acid, ethyl ester (1) - Liquid |
Triple point temperature, K - Liquid |
0.9106 |
269.16 |
Triple point temperature, K
[ref]
Mole fraction of Dodecanoic acid, ethyl ester (1) - Liquid |
Triple point temperature, K - Liquid |
0.9106 |
269.16 |
Triple point temperature, K
[ref]
Mole fraction of Dodecanoic acid, ethyl ester (1) - Liquid |
Triple point temperature, K - Liquid |
0.9106 |
269.16 |
Triple point temperature, K
[ref]
Mole fraction of Dodecanoic acid, ethyl ester (1) - Liquid |
Triple point temperature, K - Liquid |
0.9106 |
269.16 |
Sources