Mixture of Ethanamine, N-ethyl- + Water

Datasets

1. Mole fraction
2. ρ_l - Mass density, kg/m3
3. T_boil - Boiling temperature at pressure P, K (2)

Mole fraction of Ethanamine, N-ethyl- (1) [ref]

Operational condition: Pressure, kPa = 101.33 (Gas)

Mole fraction of Ethanamine, N-ethyl- (1) - Liquid	Mole fraction of Ethanamine, N-ethyl- (1) - Gas
0.0000	0.0000
0.0030	0.2610
0.0070	0.4550
0.0170	0.5880
0.0430	0.6700
0.0740	0.7000
0.1160	0.7040
0.1710	0.7080
0.2390	0.7230
0.3310	0.7470
0.4470	0.7740
0.6290	0.8370
0.7580	0.8930
1.0000	1.0000

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Mole fraction of Ethanamine, N-ethyl- (1) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0000	278.15	999.964
0.0000	288.15	999.097
0.0000	293.15	998.201
0.0000	298.15	997.041
0.0000	308.15	994.027
0.0006	278.15	999.491
0.0006	288.15	998.664
0.0006	293.15	997.751
0.0006	298.15	996.626
0.0006	308.15	993.562
0.0024	278.15	997.912
0.0024	288.15	997.039
0.0024	293.15	996.154
0.0024	298.15	994.988
0.0024	308.15	991.942
0.0035	278.15	996.932
0.0035	288.15	996.037
0.0035	293.15	995.136
0.0035	298.15	993.969
0.0035	308.15	990.903
0.0044	278.15	996.139
0.0044	288.15	995.23
0.0044	293.15	994.323
0.0044	298.15	993.151
0.0044	308.15	990.065
0.0056	278.15	995.225
0.0056	288.15	994.285
0.0056	293.15	993.371
0.0056	298.15	992.182
0.0056	308.15	989.066
0.0064	278.15	994.57
0.0064	288.15	993.602
0.0064	293.15	992.679
0.0064	298.15	991.472
0.0064	308.15	988.353
0.0081	278.15	993.249
0.0081	288.15	992.212
0.0081	293.15	991.279
0.0081	298.15	990.04
0.0081	308.15	986.873
0.0097	278.15	992.04
0.0097	288.15	990.934
0.0097	293.15	989.98
0.0097	298.15	988.714
0.0097	308.15	985.476
0.0172	278.15	987.17
0.0172	288.15	985.63
0.0172	293.15	984.539
0.0172	298.15	983.09
0.0172	308.15	979.496
0.0291	278.15	980.983
0.0291	288.15	978.376
0.0291	293.15	976.96
0.0291	298.15	975.088
0.0291	308.15	970.666
0.0400	278.15	976.381
0.0400	288.15	972.612
0.0400	293.15	970.596
0.0400	298.15	968.411
0.0400	308.15	962.812
0.0799	278.15	957.078
0.0799	288.15	949.316
0.0799	293.15	945.543
0.0799	298.15	941.882
0.0799	308.15	936.416
0.0962	288.15	939.288
0.0962	298.15	932.747
0.0962	308.15	927.169
0.1023	288.15	935.289
0.1023	298.15	928.614
0.1023	308.15	923.171
0.1157	288.15	927.131
0.1157	298.15	918.262
0.1191	278.15	933.215
0.1191	288.15	925.183
0.1191	293.15	920.953
0.1191	298.15	916.971
0.1191	308.15	910.193
0.1717	278.15	905.317
0.1717	288.15	896.85
0.1717	293.15	892.377
0.1717	298.15	888.178
0.1717	308.15	883.177
0.2290	288.15	871.09
0.2382	278.15	876.611
0.2382	288.15	867.217
0.2382	293.15	863.096
0.2382	298.15	858.163
0.2382	308.15	848.844
0.2939	278.15	859.045
0.2939	293.15	842.233
0.2939	298.15	837.568
0.2939	308.15	827.974
0.3003	278.15	857.537
0.3003	288.15	844.712
0.3003	293.15	839.967
0.3003	298.15	835.41
0.3003	308.15	825.737
0.3501	288.15	829.202
0.3501	293.15	824.477
0.3501	298.15	819.781
0.3501	308.15	810.104
0.3558	278.15	838.534
0.3558	293.15	822.73
0.3558	298.15	817.933
0.3558	308.15	808.149
0.3911	298.15	809.086
0.4057	288.15	814.027
0.4057	293.15	809.021
0.4057	308.15	794.354
0.4407	278.15	815.342
0.4407	298.15	795.926
0.4625	278.15	810.256
0.4625	288.15	799.75
0.4625	293.15	795.056
0.4625	298.15	789.779
0.4625	308.15	779.967
0.4844	278.15	805.352
0.4844	298.15	784.888
0.5091	278.15	799.695
0.5091	308.15	769.213
0.5230	293.15	781.055
0.5230	308.15	766.718
0.5287	298.15	775.014
0.6144	278.15	779.133
0.6144	288.15	768.288
0.6144	293.15	763.538
0.6144	298.15	759.804
0.6144	308.15	748.753
0.6304	278.15	775.979
0.6304	293.15	760.21
0.6304	308.15	745.249
0.7017	278.15	763.313
0.7017	293.15	747.769
0.7017	298.15	742.589
0.7017	308.15	732.049
0.7022	288.15	752.772
0.7022	298.15	742.461
0.7022	308.15	732.247
0.7260	293.15	742.965
0.7549	293.15	738.917
0.7549	298.15	733.676
0.7549	308.15	723.048
0.7771	278.15	751.837
0.7771	293.15	735.541
0.7771	298.15	730.331
0.7771	308.15	719.687
0.8050	278.15	749.039
0.8050	288.15	737.02
0.8050	293.15	731.853
0.8050	298.15	726.558
0.8523	278.15	741.596
0.8523	288.15	729.358
0.8523	293.15	724.287
0.8523	298.15	718.777
0.8523	308.15	708.199
0.8755	278.15	735.261
0.8755	298.15	715.631
0.8822	288.15	725.559
0.8822	293.15	719.965
0.8822	298.15	714.728
0.8941	293.15	718.394
0.8941	298.15	713.135
0.8941	308.15	702.403
0.9019	278.15	732.413
0.9019	298.15	712.05
0.9310	288.15	718.71
0.9310	293.15	713.312
0.9310	298.15	708.033
0.9410	278.15	726.848
0.9410	293.15	712.088
0.9410	298.15	706.818
0.9410	308.15	696.061
0.9589	278.15	724.66
0.9589	298.15	704.314
0.9727	293.15	708.394
0.9727	298.15	703.131
0.9727	308.15	692.387
0.9790	278.15	721.447
0.9790	298.15	701.729
1.0000	278.15	719.94
1.0000	288.15	709.52
1.0000	293.15	704.59
1.0000	298.15	698.97
1.0000	308.15	688.29

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.33 (Gas)

Mole fraction of Ethanamine, N-ethyl- (1) - Liquid	Boiling temperature at pressure P, K - Gas
0.0000	373.00
0.0030	367.00
0.0070	359.20
0.0170	351.90
0.0430	345.60
0.0740	344.00
0.1160	343.00
0.1710	342.00
0.2390	340.70
0.3310	338.80
0.4470	336.00
0.6290	332.60
0.7580	330.40
1.0000	328.30

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of Ethanamine, N-ethyl- (1) - Gas	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.1210	101.33	370.40

Sources

• Volumetric study of diethylamine-water mixtures between 278.15 K and 308.15 K
• Evolution of the Liquid Vapor Equilibrium Properties of Several Unsymmetrical Amines: Determination of Their Binary Isobaric Diagrams and Applications to the Distillation

Note: These property values are available through the Cheméo API. A free account gives you an access key.