Mixture of Aniline + 1-Propanol

Datasets

1. ρ_l - Mass density, kg/m3 (2)

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Aniline (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	803.71
293.15	0.0582	819.8
293.15	0.1177	835.75
293.15	0.1628	847.49
293.15	0.2056	858.38
293.15	0.2582	871.43
293.15	0.3156	885.26
293.15	0.3612	895.95
293.15	0.4112	907.36
293.15	0.4585	917.88
293.15	0.5106	929.18
293.15	0.5574	939.05
293.15	0.6141	950.71
293.15	0.6603	959.93
293.15	0.7209	971.73
293.15	0.7646	980.01
293.15	0.8114	988.68
293.15	0.8624	997.9
293.15	0.9041	1005.28
293.15	0.9525	1013.66
293.15	1.0000	1021.71
298.15	0.0000	799.74
298.15	0.0582	815.77
298.15	0.1177	831.66
298.15	0.1628	843.36
298.15	0.2056	854.21
298.15	0.2582	867.22
298.15	0.3156	881.01
298.15	0.3612	891.67
298.15	0.4112	903.06
298.15	0.4585	913.56
298.15	0.5106	924.84
298.15	0.5574	934.71
298.15	0.6141	946.36
298.15	0.6603	955.59
298.15	0.7209	967.39
298.15	0.7646	975.67
298.15	0.8114	984.34
298.15	0.8624	993.58
298.15	0.9041	1000.97
298.15	0.9525	1009.37
298.15	1.0000	1017.44
303.15	0.0000	795.77
303.15	0.0582	811.74
303.15	0.1177	827.56
303.15	0.1628	839.22
303.15	0.2056	850.04
303.15	0.2582	863.01
303.15	0.3156	876.76
303.15	0.3612	887.39
303.15	0.4112	898.76
303.15	0.4585	909.24
303.15	0.5106	920.5
303.15	0.5574	930.36
303.15	0.6141	941.99
303.15	0.6603	951.22
303.15	0.7209	963.02
303.15	0.7646	971.31
303.15	0.8114	980.0
303.15	0.8624	989.25
303.15	0.9041	996.66
303.15	0.9525	1005.08
303.15	1.0000	1013.17
308.15	0.0000	791.8
308.15	0.0582	807.7
308.15	0.1177	823.47
308.15	0.1628	835.09
308.15	0.2056	845.87
308.15	0.2582	858.8
308.15	0.3156	872.51
308.15	0.3612	883.11
308.15	0.4112	894.46
308.15	0.4585	904.92
308.15	0.5106	916.16
308.15	0.5574	926.01
308.15	0.6141	937.62
308.15	0.6603	946.85
308.15	0.7209	958.66
308.15	0.7646	966.96
308.15	0.8114	975.67
308.15	0.8624	984.93
308.15	0.9041	992.35
308.15	0.9525	1000.79
308.15	1.0000	1008.9
313.15	0.0000	787.83
313.15	0.0582	803.67
313.15	0.1177	819.38
313.15	0.1628	830.96
313.15	0.2056	841.7
313.15	0.2582	854.59
313.15	0.3156	868.26
313.15	0.3612	878.83
313.15	0.4112	890.16
313.15	0.4585	900.6
313.15	0.5106	911.82
313.15	0.5574	921.66
313.15	0.6141	933.26
313.15	0.6603	942.5
313.15	0.7209	954.31
313.15	0.7646	962.61
313.15	0.8114	971.33
313.15	0.8624	980.61
313.15	0.9041	988.04
313.15	0.9525	996.5
313.15	1.0000	1004.63
318.15	0.0000	783.86
318.15	0.0582	799.64
318.15	0.1177	815.29
318.15	0.1628	826.83
318.15	0.2056	837.53
318.15	0.2582	850.38
318.15	0.3156	864.01
318.15	0.3612	874.55
318.15	0.4112	885.86
318.15	0.4585	896.28
318.15	0.5106	907.48
318.15	0.5574	917.32
318.15	0.6141	928.91
318.15	0.6603	938.16
318.15	0.7209	949.97
318.15	0.7646	958.27
318.15	0.8114	966.99
318.15	0.8624	976.29
318.15	0.9041	983.73
318.15	0.9525	992.21
318.15	1.0000	1000.36

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Aniline (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	803.71
293.15	0.0582	819.8
293.15	0.1177	835.75
293.15	0.1628	847.49
293.15	0.2056	858.38
293.15	0.2582	871.43
293.15	0.3156	885.26
293.15	0.3612	895.95
293.15	0.4112	907.36
293.15	0.4585	917.88
293.15	0.5106	929.18
293.15	0.5574	939.05
293.15	0.6141	950.71
293.15	0.6603	959.93
293.15	0.7209	971.73
293.15	0.7646	980.01
293.15	0.8114	988.68
293.15	0.8624	997.9
293.15	0.9041	1005.28
293.15	0.9525	1013.66
293.15	1.0000	1021.71
298.15	0.0000	799.74
298.15	0.0582	815.77
298.15	0.1177	831.66
298.15	0.1628	843.36
298.15	0.2056	854.21
298.15	0.2582	867.22
298.15	0.3156	881.01
298.15	0.3612	891.67
298.15	0.4112	903.06
298.15	0.4585	913.56
298.15	0.5106	924.84
298.15	0.5574	934.71
298.15	0.6141	946.36
298.15	0.6603	955.59
298.15	0.7209	967.39
298.15	0.7646	975.67
298.15	0.8114	984.34
298.15	0.8624	993.58
298.15	0.9041	1000.97
298.15	0.9525	1009.37
298.15	1.0000	1017.44
303.15	0.0000	795.77
303.15	0.0582	811.74
303.15	0.1177	827.56
303.15	0.1628	839.22
303.15	0.2056	850.04
303.15	0.2582	863.01
303.15	0.3156	876.76
303.15	0.3612	887.39
303.15	0.4112	898.76
303.15	0.4585	909.24
303.15	0.5106	920.5
303.15	0.5574	930.36
303.15	0.6141	941.99
303.15	0.6603	951.22
303.15	0.7209	963.02
303.15	0.7646	971.31
303.15	0.8114	980.0
303.15	0.8624	989.25
303.15	0.9041	996.66
303.15	0.9525	1005.08
303.15	1.0000	1013.17
308.15	0.0000	791.8
308.15	0.0582	807.7
308.15	0.1177	823.47
308.15	0.1628	835.09
308.15	0.2056	845.87
308.15	0.2582	858.8
308.15	0.3156	872.51
308.15	0.3612	883.11
308.15	0.4112	894.46
308.15	0.4585	904.92
308.15	0.5106	916.16
308.15	0.5574	926.01
308.15	0.6141	937.62
308.15	0.6603	946.85
308.15	0.7209	958.66
308.15	0.7646	966.96
308.15	0.8114	975.67
308.15	0.8624	984.93
308.15	0.9041	992.35
308.15	0.9525	1000.79
308.15	1.0000	1008.9
313.15	0.0000	787.83
313.15	0.0582	803.67
313.15	0.1177	819.38
313.15	0.1628	830.96
313.15	0.2056	841.7
313.15	0.2582	854.59
313.15	0.3156	868.26
313.15	0.3612	878.83
313.15	0.4112	890.16
313.15	0.4585	900.6
313.15	0.5106	911.82
313.15	0.5574	921.66
313.15	0.6141	933.26
313.15	0.6603	942.5
313.15	0.7209	954.31
313.15	0.7646	962.61
313.15	0.8114	971.33
313.15	0.8624	980.61
313.15	0.9041	988.04
313.15	0.9525	996.5
313.15	1.0000	1004.63
318.15	0.0000	783.86
318.15	0.0582	799.64
318.15	0.1177	815.29
318.15	0.1628	826.83
318.15	0.2056	837.53
318.15	0.2582	850.38
318.15	0.3156	864.01
318.15	0.3612	874.55
318.15	0.4112	885.86
318.15	0.4585	896.28
318.15	0.5106	907.48
318.15	0.5574	917.32
318.15	0.6141	928.91
318.15	0.6603	938.16
318.15	0.7209	949.97
318.15	0.7646	958.27
318.15	0.8114	966.99
318.15	0.8624	976.29
318.15	0.9041	983.73
318.15	0.9525	992.21
318.15	1.0000	1000.36

Sources

• Densities and Volumetric Properties of Binary Mixtures of Aniline with 1-Propanol, 2-Propanol, 2-Methyl-1-Propanol, and 2-Methyl-2-Propanol at Temperatures from 293.15 to 318.15 K