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)
202.0 197.5
211.0 200.6
301.0 230.4
302.0 230.5
303.0 230.9
304.0 231.3
305.0 231.7
306.0 232.1
307.0 232.3
308.0 232.6
309.0 232.8
310.0 233.2
212.0 200.8
311.0 233.4
312.0 233.7
313.0 234.0
314.0 234.4
315.0 234.8
316.0 235.0
317.0 235.1
318.0 235.4
319.0 235.8
320.0 236.2
213.0 201.0
214.0 201.3
215.0 201.5
216.0 201.7
217.0 201.8
218.0 201.9
219.0 202.4
220.0 202.8
203.0 198.3
221.0 203.0
222.0 203.4
223.0 203.5
224.0 203.6
225.0 203.9
226.0 204.2
227.0 204.6
228.0 205.0
229.0 205.3
230.0 205.5
204.0 198.8
231.0 205.9
232.0 206.3
233.0 206.6
234.0 207.2
235.0 207.5
236.0 207.6
237.0 208.0
238.0 208.4
239.0 209.0
240.0 209.4
205.0 198.5
241.0 209.6
242.0 209.8
243.0 210.0
244.0 210.4
245.0 211.1
246.0 211.6
247.0 211.6
248.0 211.9
249.0 212.2
250.0 212.7
206.0 198.6
251.0 213.3
252.0 213.4
253.0 213.5
254.0 214.0
255.0 214.4
256.0 214.8
257.0 215.1
258.0 215.6
259.0 215.9
260.0 216.2
207.0 199.1
261.0 216.6
262.0 216.9
263.0 217.1
264.0 217.3
265.0 217.8
266.0 218.3
267.0 218.9
268.0 219.2
269.0 219.4
270.0 219.8
208.0 199.4
271.0 220.1
272.0 220.5
273.0 220.9
274.0 221.2
275.0 221.6
276.0 222.0
277.0 222.4
278.0 222.8
279.0 223.0
280.0 223.4
209.0 199.8
281.0 223.9
282.0 224.3
283.0 224.7
284.0 225.0
285.0 225.2
286.0 225.5
287.0 225.9
288.0 226.1
289.0 226.4
290.0 226.8
210.0 200.2
291.0 227.2
292.0 227.5
293.0 227.8
294.0 228.2
295.0 228.6
296.0 228.9
297.0 229.1
298.0 229.4
299.0 229.8
300.0 230.1
124; diethyl carbonate; 00072