Mixture of Aniline + 1-Propanol, 2-methyl-

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	801.48
293.15	0.0556	814.64
293.15	0.1093	827.24
293.15	0.1610	839.26
293.15	0.2145	851.59
293.15	0.2596	861.89
293.15	0.3099	873.31
293.15	0.3580	884.13
293.15	0.4058	894.79
293.15	0.4573	906.19
293.15	0.5038	916.41
293.15	0.5523	927.0
293.15	0.6061	938.66
293.15	0.6526	948.65
293.15	0.7087	960.66
293.15	0.7512	969.68
293.15	0.8090	981.89
293.15	0.8572	991.99
293.15	0.9051	1002.0
293.15	0.9562	1012.63
293.15	1.0000	1021.71
298.15	0.0000	797.54
298.15	0.0556	810.62
298.15	0.1093	823.15
298.15	0.1610	835.11
298.15	0.2145	847.39
298.15	0.2596	857.65
298.15	0.3099	869.03
298.15	0.3580	879.81
298.15	0.4058	890.44
298.15	0.4573	901.82
298.15	0.5038	912.02
298.15	0.5523	922.59
298.15	0.6061	934.24
298.15	0.6526	944.23
298.15	0.7087	956.24
298.15	0.7512	965.28
298.15	0.8090	977.51
298.15	0.8572	987.64
298.15	0.9051	997.67
298.15	0.9562	1008.33
298.15	1.0000	1017.44
303.15	0.0000	793.6
303.15	0.0556	806.6
303.15	0.1093	819.06
303.15	0.1610	830.96
303.15	0.2145	843.19
303.15	0.2596	853.41
303.15	0.3099	864.75
303.15	0.3580	875.49
303.15	0.4058	886.09
303.15	0.4573	897.45
303.15	0.5038	907.63
303.15	0.5523	918.18
303.15	0.6061	929.82
303.15	0.6526	939.81
303.15	0.7087	951.83
303.15	0.7512	960.88
303.15	0.8090	973.13
303.15	0.8572	983.29
303.15	0.9051	993.34
303.15	0.9562	1004.03
303.15	1.0000	1013.17
308.15	0.0000	789.66
308.15	0.0556	802.58
308.15	0.1093	814.97
308.15	0.1610	826.81
308.15	0.2145	838.99
308.15	0.2596	849.17
308.15	0.3099	860.47
308.15	0.3580	871.17
308.15	0.4058	881.74
308.15	0.4573	893.08
308.15	0.5038	903.24
308.15	0.5523	913.77
308.15	0.6061	925.42
308.15	0.6526	935.41
308.15	0.7087	947.43
308.15	0.7512	956.48
308.15	0.8090	968.75
308.15	0.8572	978.93
308.15	0.9051	989.01
308.15	0.9562	999.73
308.15	1.0000	1008.9
313.15	0.0000	785.72
313.15	0.0556	798.56
313.15	0.1093	810.88
313.15	0.1610	822.66
313.15	0.2145	834.79
313.15	0.2596	844.93
313.15	0.3099	856.19
313.15	0.3580	866.85
313.15	0.4058	877.39
313.15	0.4573	888.71
313.15	0.5038	898.85
313.15	0.5523	909.37
313.15	0.6061	921.02
313.15	0.6526	931.01
313.15	0.7087	943.03
313.15	0.7512	952.08
313.15	0.8090	964.37
313.15	0.8572	974.57
313.15	0.9051	984.68
313.15	0.9562	995.43
313.15	1.0000	1004.63
318.15	0.0000	781.78
318.15	0.0556	794.54
318.15	0.1093	806.8
318.15	0.1610	818.52
318.15	0.2145	830.59
318.15	0.2596	840.69
318.15	0.3099	851.91
318.15	0.3580	862.53
318.15	0.4058	873.05
318.15	0.4573	884.34
318.15	0.5038	894.46
318.15	0.5523	904.98
318.15	0.6061	916.62
318.15	0.6526	926.61
318.15	0.7087	938.63
318.15	0.7512	947.68
318.15	0.8090	959.99
318.15	0.8572	970.21
318.15	0.9051	980.35
318.15	0.9562	991.13
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	801.48
293.15	0.0556	814.64
293.15	0.1093	827.24
293.15	0.1610	839.26
293.15	0.2145	851.59
293.15	0.2596	861.89
293.15	0.3099	873.31
293.15	0.3580	884.13
293.15	0.4058	894.79
293.15	0.4573	906.19
293.15	0.5038	916.41
293.15	0.5523	927.0
293.15	0.6061	938.66
293.15	0.6526	948.65
293.15	0.7087	960.66
293.15	0.7512	969.68
293.15	0.8090	981.89
293.15	0.8572	991.99
293.15	0.9051	1002.0
293.15	0.9562	1012.63
293.15	1.0000	1021.71
298.15	0.0000	797.54
298.15	0.0556	810.62
298.15	0.1093	823.15
298.15	0.1610	835.11
298.15	0.2145	847.39
298.15	0.2596	857.65
298.15	0.3099	869.03
298.15	0.3580	879.81
298.15	0.4058	890.44
298.15	0.4573	901.82
298.15	0.5038	912.02
298.15	0.5523	922.59
298.15	0.6061	934.24
298.15	0.6526	944.23
298.15	0.7087	956.24
298.15	0.7512	965.28
298.15	0.8090	977.51
298.15	0.8572	987.64
298.15	0.9051	997.67
298.15	0.9562	1008.33
298.15	1.0000	1017.44
303.15	0.0000	793.6
303.15	0.0556	806.6
303.15	0.1093	819.06
303.15	0.1610	830.96
303.15	0.2145	843.19
303.15	0.2596	853.41
303.15	0.3099	864.75
303.15	0.3580	875.49
303.15	0.4058	886.09
303.15	0.4573	897.45
303.15	0.5038	907.63
303.15	0.5523	918.18
303.15	0.6061	929.82
303.15	0.6526	939.81
303.15	0.7087	951.83
303.15	0.7512	960.88
303.15	0.8090	973.13
303.15	0.8572	983.29
303.15	0.9051	993.34
303.15	0.9562	1004.03
303.15	1.0000	1013.17
308.15	0.0000	789.66
308.15	0.0556	802.58
308.15	0.1093	814.97
308.15	0.1610	826.81
308.15	0.2145	838.99
308.15	0.2596	849.17
308.15	0.3099	860.47
308.15	0.3580	871.17
308.15	0.4058	881.74
308.15	0.4573	893.08
308.15	0.5038	903.24
308.15	0.5523	913.77
308.15	0.6061	925.42
308.15	0.6526	935.41
308.15	0.7087	947.43
308.15	0.7512	956.48
308.15	0.8090	968.75
308.15	0.8572	978.93
308.15	0.9051	989.01
308.15	0.9562	999.73
308.15	1.0000	1008.9
313.15	0.0000	785.72
313.15	0.0556	798.56
313.15	0.1093	810.88
313.15	0.1610	822.66
313.15	0.2145	834.79
313.15	0.2596	844.93
313.15	0.3099	856.19
313.15	0.3580	866.85
313.15	0.4058	877.39
313.15	0.4573	888.71
313.15	0.5038	898.85
313.15	0.5523	909.37
313.15	0.6061	921.02
313.15	0.6526	931.01
313.15	0.7087	943.03
313.15	0.7512	952.08
313.15	0.8090	964.37
313.15	0.8572	974.57
313.15	0.9051	984.68
313.15	0.9562	995.43
313.15	1.0000	1004.63
318.15	0.0000	781.78
318.15	0.0556	794.54
318.15	0.1093	806.8
318.15	0.1610	818.52
318.15	0.2145	830.59
318.15	0.2596	840.69
318.15	0.3099	851.91
318.15	0.3580	862.53
318.15	0.4058	873.05
318.15	0.4573	884.34
318.15	0.5038	894.46
318.15	0.5523	904.98
318.15	0.6061	916.62
318.15	0.6526	926.61
318.15	0.7087	938.63
318.15	0.7512	947.68
318.15	0.8090	959.99
318.15	0.8572	970.21
318.15	0.9051	980.35
318.15	0.9562	991.13
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