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)
180.0 69.78
189.0 72.67
279.0 106.8
280.0 107.2
281.0 107.6
282.0 108.1
283.0 108.7
284.0 109.2
285.0 109.7
286.0 110.2
287.0 110.7
288.0 111.2
190.0 73.09
289.0 111.7
290.0 112.3
291.0 112.9
292.0 113.4
293.0 114.0
294.0 114.6
295.0 115.2
296.0 115.9
297.0 116.5
298.0 116.8
191.0 73.57
299.0 117.6
192.0 73.84
193.0 74.17
194.0 74.64
195.0 75.08
196.0 75.37
197.0 75.72
198.0 75.96
181.0 70.04
199.0 76.14
200.0 76.71
201.0 77.18
202.0 77.37
203.0 77.64
204.0 78.01
205.0 78.27
206.0 78.72
207.0 78.85
208.0 79.04
182.0 70.35
209.0 79.73
210.0 80.18
211.0 80.44
212.0 80.82
213.0 81.11
214.0 81.32
215.0 81.61
216.0 82.12
217.0 82.62
218.0 82.83
183.0 70.59
219.0 83.12
220.0 83.36
221.0 83.7
222.0 84.01
223.0 84.46
224.0 84.93
225.0 85.21
226.0 85.47
227.0 85.85
228.0 86.2
184.0 70.94
229.0 86.51
230.0 86.89
231.0 87.33
232.0 87.63
233.0 87.87
234.0 88.09
235.0 88.4
236.0 88.82
237.0 89.3
238.0 89.64
185.0 71.36
239.0 89.86
240.0 90.13
241.0 90.53
242.0 90.94
243.0 91.27
244.0 91.65
245.0 92.08
246.0 92.36
247.0 92.62
248.0 93.0
186.0 71.73
249.0 93.45
250.0 93.88
251.0 94.32
252.0 94.77
253.0 95.17
254.0 95.4
255.0 95.72
256.0 96.18
257.0 96.54
258.0 96.92
187.0 72.05
259.0 97.42
260.0 97.98
261.0 98.45
262.0 98.83
263.0 99.18
264.0 99.55
265.0 100.0
266.0 100.6
267.0 100.9
268.0 101.3
188.0 72.45
269.0 101.8
270.0 102.3
271.0 102.8
272.0 103.3
273.0 103.8
274.0 104.4
275.0 104.8
276.0 105.3
277.0 105.9
278.0 106.4
429; ethylene carbonate; 00189