Datasets
-
Pvap - Vapor or sublimation pressure, kPa (2)
-
Tfus - Solid-liquid equilibrium temperature, K (2)
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Cyclohexane (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0000 |
293.15 |
697870.00 |
0.0000 |
303.15 |
807350.00 |
0.0000 |
313.15 |
947230.00 |
0.0000 |
323.15 |
1117520.00 |
0.0000 |
333.15 |
1318200.00 |
0.0000 |
343.15 |
1549280.00 |
0.0844 |
293.15 |
304240.00 |
0.0844 |
303.15 |
377550.00 |
0.0844 |
313.15 |
464650.00 |
0.0844 |
323.15 |
565540.00 |
0.0844 |
333.15 |
680210.00 |
0.0844 |
343.15 |
808660.00 |
0.1822 |
293.15 |
266420.00 |
0.1822 |
303.15 |
336810.00 |
0.1822 |
313.15 |
407370.00 |
0.1822 |
323.15 |
478090.00 |
0.1822 |
333.15 |
548980.00 |
0.1822 |
343.15 |
620040.00 |
0.2609 |
293.15 |
228980.00 |
0.2609 |
303.15 |
301490.00 |
0.2609 |
313.15 |
372950.00 |
0.2609 |
323.15 |
443380.00 |
0.2609 |
333.15 |
512780.00 |
0.2609 |
343.15 |
581140.00 |
0.3406 |
293.15 |
203780.00 |
0.3406 |
303.15 |
270090.00 |
0.3406 |
313.15 |
339970.00 |
0.3406 |
323.15 |
413420.00 |
0.3406 |
333.15 |
490440.00 |
0.3406 |
343.15 |
571040.00 |
0.4235 |
293.15 |
173330.00 |
0.4235 |
303.15 |
235000.00 |
0.4235 |
313.15 |
300420.00 |
0.4235 |
323.15 |
369600.00 |
0.4235 |
333.15 |
442530.00 |
0.4235 |
343.15 |
519210.00 |
0.5003 |
293.15 |
156530.00 |
0.5003 |
303.15 |
210950.00 |
0.5003 |
313.15 |
270990.00 |
0.5003 |
323.15 |
336630.00 |
0.5003 |
333.15 |
407880.00 |
0.5003 |
343.15 |
484750.00 |
0.5291 |
293.15 |
152660.00 |
0.5291 |
303.15 |
205580.00 |
0.5291 |
313.15 |
262230.00 |
0.5291 |
323.15 |
322590.00 |
0.5291 |
333.15 |
386690.00 |
0.5291 |
343.15 |
454500.00 |
0.5805 |
293.15 |
142920.00 |
0.5805 |
303.15 |
190580.00 |
0.5805 |
313.15 |
241660.00 |
0.5805 |
323.15 |
296170.00 |
0.5805 |
333.15 |
354110.00 |
0.5805 |
343.15 |
415480.00 |
0.6200 |
293.15 |
137420.00 |
0.6200 |
303.15 |
184480.00 |
0.6200 |
313.15 |
233440.00 |
0.6200 |
323.15 |
284290.00 |
0.6200 |
333.15 |
337040.00 |
0.6200 |
343.15 |
391690.00 |
0.7401 |
293.15 |
118720.00 |
0.7401 |
303.15 |
154570.00 |
0.7401 |
313.15 |
192820.00 |
0.7401 |
323.15 |
233450.00 |
0.7401 |
333.15 |
276480.00 |
0.7401 |
343.15 |
321890.00 |
0.8988 |
293.15 |
71960.00 |
0.8988 |
303.15 |
97300.00 |
0.8988 |
313.15 |
124720.00 |
0.8988 |
323.15 |
154240.00 |
0.8988 |
333.15 |
185840.00 |
0.8988 |
343.15 |
219530.00 |
0.9798 |
293.15 |
38520.00 |
0.9798 |
303.15 |
61280.00 |
0.9798 |
313.15 |
84210.00 |
0.9798 |
323.15 |
107310.00 |
0.9798 |
333.15 |
130590.00 |
0.9798 |
343.15 |
154050.00 |
1.0000 |
293.15 |
23390.00 |
1.0000 |
303.15 |
45610.00 |
1.0000 |
313.15 |
67600.00 |
1.0000 |
323.15 |
89340.00 |
1.0000 |
333.15 |
110840.00 |
1.0000 |
343.15 |
132100.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Cyclohexane (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0000 |
293.15 |
697870.00 |
0.0000 |
303.15 |
807350.00 |
0.0000 |
313.15 |
947230.00 |
0.0000 |
323.15 |
1117520.00 |
0.0000 |
333.15 |
1318200.00 |
0.0000 |
343.15 |
1549280.00 |
0.0844 |
293.15 |
304240.00 |
0.0844 |
303.15 |
377550.00 |
0.0844 |
313.15 |
464650.00 |
0.0844 |
323.15 |
565540.00 |
0.0844 |
333.15 |
680210.00 |
0.0844 |
343.15 |
808660.00 |
0.1822 |
293.15 |
266420.00 |
0.1822 |
303.15 |
336810.00 |
0.1822 |
313.15 |
407370.00 |
0.1822 |
323.15 |
478090.00 |
0.1822 |
333.15 |
548980.00 |
0.1822 |
343.15 |
620040.00 |
0.2609 |
293.15 |
228980.00 |
0.2609 |
303.15 |
301490.00 |
0.2609 |
313.15 |
372950.00 |
0.2609 |
323.15 |
443380.00 |
0.2609 |
333.15 |
512780.00 |
0.2609 |
343.15 |
581140.00 |
0.3406 |
293.15 |
203780.00 |
0.3406 |
303.15 |
270090.00 |
0.3406 |
313.15 |
339970.00 |
0.3406 |
323.15 |
413420.00 |
0.3406 |
333.15 |
490440.00 |
0.3406 |
343.15 |
571040.00 |
0.4235 |
293.15 |
173330.00 |
0.4235 |
303.15 |
235000.00 |
0.4235 |
313.15 |
300420.00 |
0.4235 |
323.15 |
369600.00 |
0.4235 |
333.15 |
442530.00 |
0.4235 |
343.15 |
519210.00 |
0.5003 |
293.15 |
156530.00 |
0.5003 |
303.15 |
210950.00 |
0.5003 |
313.15 |
270990.00 |
0.5003 |
323.15 |
336630.00 |
0.5003 |
333.15 |
407880.00 |
0.5003 |
343.15 |
484750.00 |
0.5291 |
293.15 |
152660.00 |
0.5291 |
303.15 |
205580.00 |
0.5291 |
313.15 |
262230.00 |
0.5291 |
323.15 |
322590.00 |
0.5291 |
333.15 |
386690.00 |
0.5291 |
343.15 |
454500.00 |
0.5805 |
293.15 |
142920.00 |
0.5805 |
303.15 |
190580.00 |
0.5805 |
313.15 |
241660.00 |
0.5805 |
323.15 |
296170.00 |
0.5805 |
333.15 |
354110.00 |
0.5805 |
343.15 |
415480.00 |
0.6200 |
293.15 |
137420.00 |
0.6200 |
303.15 |
184480.00 |
0.6200 |
313.15 |
233440.00 |
0.6200 |
323.15 |
284290.00 |
0.6200 |
333.15 |
337040.00 |
0.6200 |
343.15 |
391690.00 |
0.7401 |
293.15 |
118720.00 |
0.7401 |
303.15 |
154570.00 |
0.7401 |
313.15 |
192820.00 |
0.7401 |
323.15 |
233450.00 |
0.7401 |
333.15 |
276480.00 |
0.7401 |
343.15 |
321890.00 |
0.8988 |
293.15 |
71960.00 |
0.8988 |
303.15 |
97300.00 |
0.8988 |
313.15 |
124720.00 |
0.8988 |
323.15 |
154240.00 |
0.8988 |
333.15 |
185840.00 |
0.8988 |
343.15 |
219530.00 |
0.9798 |
293.15 |
38520.00 |
0.9798 |
303.15 |
61280.00 |
0.9798 |
313.15 |
84210.00 |
0.9798 |
323.15 |
107310.00 |
0.9798 |
333.15 |
130590.00 |
0.9798 |
343.15 |
154050.00 |
1.0000 |
293.15 |
23390.00 |
1.0000 |
303.15 |
45610.00 |
1.0000 |
313.15 |
67600.00 |
1.0000 |
323.15 |
89340.00 |
1.0000 |
333.15 |
110840.00 |
1.0000 |
343.15 |
132100.00 |
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Mole fraction of Cyclohexane (2) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
0.0544 |
229.15 |
0.0701 |
231.67 |
0.1011 |
236.12 |
0.1144 |
237.99 |
0.1252 |
238.97 |
0.1414 |
240.97 |
0.1545 |
242.30 |
0.1712 |
243.89 |
0.1929 |
245.62 |
0.2168 |
247.32 |
0.2377 |
248.96 |
0.2578 |
250.36 |
0.2876 |
251.61 |
0.3073 |
252.16 |
0.3231 |
252.63 |
0.3394 |
253.10 |
0.3506 |
253.37 |
0.3667 |
253.68 |
0.3855 |
254.18 |
0.4032 |
254.64 |
0.4205 |
255.28 |
0.4392 |
255.60 |
0.4552 |
255.70 |
0.4700 |
256.24 |
0.4865 |
256.54 |
0.5050 |
256.81 |
0.5227 |
256.81 |
0.5420 |
257.21 |
0.5596 |
257.46 |
0.5790 |
257.57 |
0.6003 |
258.10 |
0.6269 |
258.11 |
0.6491 |
258.16 |
0.6729 |
258.76 |
0.6962 |
258.95 |
0.7210 |
259.30 |
0.7441 |
259.77 |
0.7740 |
260.25 |
0.7930 |
260.96 |
0.8156 |
261.49 |
0.8365 |
262.12 |
0.8606 |
263.25 |
0.8785 |
264.49 |
0.9001 |
265.52 |
0.9180 |
266.88 |
0.9362 |
269.46 |
0.9544 |
271.91 |
0.9730 |
274.22 |
0.9920 |
277.53 |
0.9950 |
278.47 |
0.9965 |
279.15 |
1.0000 |
280.10 |
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Mole fraction of Cyclohexane (2) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
0.0544 |
229.15 |
0.0701 |
231.67 |
0.1011 |
236.12 |
0.1144 |
237.99 |
0.1252 |
238.97 |
0.1414 |
240.97 |
0.1545 |
242.30 |
0.1712 |
243.89 |
0.1929 |
245.62 |
0.2168 |
247.32 |
0.2377 |
248.96 |
0.2578 |
250.36 |
0.2876 |
251.61 |
0.3073 |
252.16 |
0.3231 |
252.63 |
0.3394 |
253.10 |
0.3506 |
253.37 |
0.3667 |
253.68 |
0.3855 |
254.18 |
0.4032 |
254.64 |
0.4205 |
255.28 |
0.4392 |
255.60 |
0.4552 |
255.70 |
0.4700 |
256.24 |
0.4865 |
256.54 |
0.5050 |
256.81 |
0.5227 |
256.81 |
0.5420 |
257.21 |
0.5596 |
257.46 |
0.5790 |
257.57 |
0.6003 |
258.10 |
0.6269 |
258.11 |
0.6491 |
258.16 |
0.6729 |
258.76 |
0.6962 |
258.95 |
0.7210 |
259.30 |
0.7441 |
259.77 |
0.7740 |
260.25 |
0.7930 |
260.96 |
0.8156 |
261.49 |
0.8365 |
262.12 |
0.8606 |
263.25 |
0.8785 |
264.49 |
0.9001 |
265.52 |
0.9180 |
266.88 |
0.9362 |
269.46 |
0.9544 |
271.91 |
0.9730 |
274.22 |
0.9920 |
277.53 |
0.9950 |
278.47 |
0.9965 |
279.15 |
1.0000 |
280.10 |
Sources