Liquid-Solid Phase Equilibria and Thermodynamic Modeling for Binary Organic Carbonates Ding, M.S.; Journal of Chemical & Engineering Data 2004, 49, 276-282
Data
P = 101.325 kPa
T (K) Cp (J mol-1 K-1)
181.0 132.6
190.0 133.4
280.0 150.1
281.0 150.4
282.0 150.6
283.0 150.8
284.0 150.9
285.0 151.1
286.0 151.3
287.0 151.5
288.0 151.7
289.0 151.8
191.0 133.5
290.0 152.0
291.0 152.3
292.0 152.6
293.0 152.7
294.0 152.8
295.0 152.9
296.0 153.2
297.0 153.4
298.0 153.6
299.0 153.7
192.0 133.7
300.0 153.9
301.0 154.0
302.0 154.2
303.0 154.5
304.0 154.7
305.0 154.9
306.0 155.0
307.0 155.1
308.0 155.3
309.0 155.5
193.0 133.7
310.0 155.7
311.0 155.9
312.0 156.0
313.0 156.2
314.0 156.4
315.0 156.6
316.0 156.7
317.0 156.8
318.0 157.0
319.0 157.2
194.0 134.1
320.0 157.4
195.0 134.2
196.0 134.3
197.0 134.5
198.0 134.5
199.0 134.8
182.0 132.5
200.0 134.9
201.0 135.0
202.0 135.3
203.0 135.5
204.0 135.5
205.0 135.7
206.0 135.9
207.0 136.0
208.0 136.2
209.0 136.3
183.0 132.2
210.0 136.4
211.0 136.6
212.0 136.8
213.0 137.0
214.0 137.3
215.0 137.4
216.0 137.5
217.0 137.7
218.0 137.7
219.0 137.8
184.0 132.3
220.0 138.1
221.0 138.3
222.0 138.4
223.0 138.5
224.0 138.7
225.0 138.9
226.0 138.9
227.0 139.1
228.0 139.3
229.0 139.5
185.0 132.4
230.0 139.5
231.0 139.6
232.0 139.8
233.0 139.9
234.0 140.2
235.0 140.4
236.0 140.5
237.0 140.8
238.0 141.0
239.0 141.0
186.0 132.5
240.0 141.1
241.0 141.4
242.0 141.6
243.0 141.8
244.0 142.0
245.0 142.4
246.0 142.6
247.0 142.7
248.0 143.0
249.0 143.1
187.0 132.8
250.0 143.4
251.0 143.7
252.0 143.9
253.0 144.1
254.0 144.3
255.0 144.5
256.0 144.7
257.0 145.0
258.0 145.2
259.0 145.4
188.0 133.0
260.0 145.7
261.0 146.0
262.0 146.2
263.0 146.4
264.0 146.5
265.0 146.8
266.0 147.1
267.0 147.3
268.0 147.6
269.0 147.7
189.0 133.2
270.0 147.8
271.0 148.2
272.0 148.4
273.0 148.6
274.0 148.8
275.0 149.1
276.0 149.3
277.0 149.6
278.0 149.8
279.0 149.9
126; propylene carbonate; 00074