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

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 (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	785.75
293.15	0.0538	799.32
293.15	0.1082	812.94
293.15	0.1526	823.96
293.15	0.2066	837.3
293.15	0.2552	849.15
293.15	0.3075	861.87
293.15	0.3523	872.64
293.15	0.4074	885.77
293.15	0.4586	897.89
293.15	0.5064	909.11
293.15	0.5532	920.06
293.15	0.6076	932.71
293.15	0.6522	942.96
293.15	0.7028	954.55
293.15	0.7542	966.31
293.15	0.8062	978.12
293.15	0.8544	989.01
293.15	0.9012	999.55
293.15	0.9536	1011.32
293.15	1.0000	1021.71
298.15	0.0000	780.63
298.15	0.0538	794.16
298.15	0.1082	807.75
298.15	0.1526	818.75
298.15	0.2066	832.07
298.15	0.2552	843.91
298.15	0.3075	856.61
298.15	0.3523	867.39
298.15	0.4074	880.55
298.15	0.4586	892.7
298.15	0.5064	903.96
298.15	0.5532	914.96
298.15	0.6076	927.68
298.15	0.6522	937.98
298.15	0.7028	949.67
298.15	0.7542	961.5
298.15	0.8062	973.41
298.15	0.8544	984.4
298.15	0.9012	995.04
298.15	0.9536	1006.93
298.15	1.0000	1017.44
303.15	0.0000	775.51
303.15	0.0538	789.0
303.15	0.1082	802.56
303.15	0.1526	813.54
303.15	0.2066	826.84
303.15	0.2552	838.68
303.15	0.3075	851.36
303.15	0.3523	862.16
303.15	0.4074	875.35
303.15	0.4586	887.53
303.15	0.5064	898.82
303.15	0.5532	909.87
303.15	0.6076	922.65
303.15	0.6522	933.01
303.15	0.7028	944.79
303.15	0.7542	956.69
303.15	0.8062	968.7
303.15	0.8544	979.79
303.15	0.9012	990.52
303.15	0.9536	1002.54
303.15	1.0000	1013.17
308.15	0.0000	770.39
308.15	0.0538	783.84
308.15	0.1082	797.37
308.15	0.1526	808.33
308.15	0.2066	821.61
308.15	0.2552	833.45
308.15	0.3075	846.12
308.15	0.3523	856.93
308.15	0.4074	870.14
308.15	0.4586	882.37
308.15	0.5064	893.69
308.15	0.5532	904.78
308.15	0.6076	917.63
308.15	0.6522	928.05
308.15	0.7028	939.91
308.15	0.7542	951.88
308.15	0.8062	963.99
308.15	0.8544	975.17
308.15	0.9012	986.0
308.15	0.9536	998.14
308.15	1.0000	1008.9
313.15	0.0000	765.26
313.15	0.0538	778.68
313.15	0.1082	792.18
313.15	0.1526	803.12
313.15	0.2066	816.38
313.15	0.2552	828.22
313.15	0.3075	840.89
313.15	0.3523	851.71
313.15	0.4074	864.94
313.15	0.4586	877.21
313.15	0.5064	888.57
313.15	0.5532	899.69
313.15	0.6076	912.61
313.15	0.6522	923.09
313.15	0.7028	935.02
313.15	0.7542	947.08
313.15	0.8062	959.28
313.15	0.8544	970.55
313.15	0.9012	981.48
313.15	0.9536	993.75
313.15	1.0000	1004.63
318.15	0.0000	760.13
318.15	0.0538	773.52
318.15	0.1082	786.99
318.15	0.1526	797.91
318.15	0.2066	811.16
318.15	0.2552	822.99
318.15	0.3075	835.67
318.15	0.3523	846.49
318.15	0.4074	859.75
318.15	0.4586	872.06
318.15	0.5064	883.45
318.15	0.5532	894.61
318.15	0.6076	907.6
318.15	0.6522	918.13
318.15	0.7028	930.13
318.15	0.7542	942.28
318.15	0.8062	954.57
318.15	0.8544	965.93
318.15	0.9012	976.97
318.15	0.9536	989.36
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 (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	785.75
293.15	0.0538	799.32
293.15	0.1082	812.94
293.15	0.1526	823.96
293.15	0.2066	837.3
293.15	0.2552	849.15
293.15	0.3075	861.87
293.15	0.3523	872.64
293.15	0.4074	885.77
293.15	0.4586	897.89
293.15	0.5064	909.11
293.15	0.5532	920.06
293.15	0.6076	932.71
293.15	0.6522	942.96
293.15	0.7028	954.55
293.15	0.7542	966.31
293.15	0.8062	978.12
293.15	0.8544	989.01
293.15	0.9012	999.55
293.15	0.9536	1011.32
293.15	1.0000	1021.71
298.15	0.0000	780.63
298.15	0.0538	794.16
298.15	0.1082	807.75
298.15	0.1526	818.75
298.15	0.2066	832.07
298.15	0.2552	843.91
298.15	0.3075	856.61
298.15	0.3523	867.39
298.15	0.4074	880.55
298.15	0.4586	892.7
298.15	0.5064	903.96
298.15	0.5532	914.96
298.15	0.6076	927.68
298.15	0.6522	937.98
298.15	0.7028	949.67
298.15	0.7542	961.5
298.15	0.8062	973.41
298.15	0.8544	984.4
298.15	0.9012	995.04
298.15	0.9536	1006.93
298.15	1.0000	1017.44
303.15	0.0000	775.51
303.15	0.0538	789.0
303.15	0.1082	802.56
303.15	0.1526	813.54
303.15	0.2066	826.84
303.15	0.2552	838.68
303.15	0.3075	851.36
303.15	0.3523	862.16
303.15	0.4074	875.35
303.15	0.4586	887.53
303.15	0.5064	898.82
303.15	0.5532	909.87
303.15	0.6076	922.65
303.15	0.6522	933.01
303.15	0.7028	944.79
303.15	0.7542	956.69
303.15	0.8062	968.7
303.15	0.8544	979.79
303.15	0.9012	990.52
303.15	0.9536	1002.54
303.15	1.0000	1013.17
308.15	0.0000	770.39
308.15	0.0538	783.84
308.15	0.1082	797.37
308.15	0.1526	808.33
308.15	0.2066	821.61
308.15	0.2552	833.45
308.15	0.3075	846.12
308.15	0.3523	856.93
308.15	0.4074	870.14
308.15	0.4586	882.37
308.15	0.5064	893.69
308.15	0.5532	904.78
308.15	0.6076	917.63
308.15	0.6522	928.05
308.15	0.7028	939.91
308.15	0.7542	951.88
308.15	0.8062	963.99
308.15	0.8544	975.17
308.15	0.9012	986.0
308.15	0.9536	998.14
308.15	1.0000	1008.9
313.15	0.0000	765.26
313.15	0.0538	778.68
313.15	0.1082	792.18
313.15	0.1526	803.12
313.15	0.2066	816.38
313.15	0.2552	828.22
313.15	0.3075	840.89
313.15	0.3523	851.71
313.15	0.4074	864.94
313.15	0.4586	877.21
313.15	0.5064	888.57
313.15	0.5532	899.69
313.15	0.6076	912.61
313.15	0.6522	923.09
313.15	0.7028	935.02
313.15	0.7542	947.08
313.15	0.8062	959.28
313.15	0.8544	970.55
313.15	0.9012	981.48
313.15	0.9536	993.75
313.15	1.0000	1004.63
318.15	0.0000	760.13
318.15	0.0538	773.52
318.15	0.1082	786.99
318.15	0.1526	797.91
318.15	0.2066	811.16
318.15	0.2552	822.99
318.15	0.3075	835.67
318.15	0.3523	846.49
318.15	0.4074	859.75
318.15	0.4586	872.06
318.15	0.5064	883.45
318.15	0.5532	894.61
318.15	0.6076	907.6
318.15	0.6522	918.13
318.15	0.7028	930.13
318.15	0.7542	942.28
318.15	0.8062	954.57
318.15	0.8544	965.93
318.15	0.9012	976.97
318.15	0.9536	989.36
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