Mixture of 1-Butanol + 4-Morpholineethanol

Datasets

1. ρ_l - Mass density, kg/m3 (2)

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of 4-Morpholineethanol (2) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0652	293.15	832.8
0.0652	298.15	829.0
0.0652	303.15	825.1
0.0652	313.15	817.44
0.0652	323.15	809.9
0.1125	293.15	849.1
0.1125	298.15	845.21
0.1125	303.15	841.24
0.1125	313.15	833.54
0.1125	323.15	826.03
0.1865	293.15	873.74
0.1865	298.15	869.7
0.1865	303.15	865.64
0.1865	313.15	857.88
0.1865	323.15	850.45
0.2436	293.15	891.83
0.2436	298.15	887.69
0.2436	303.15	883.56
0.2436	313.15	875.77
0.2436	323.15	868.41
0.2865	293.15	905.09
0.2865	298.15	900.87
0.2865	303.15	896.69
0.2865	313.15	888.88
0.2865	323.15	881.58
0.3275	293.15	917.49
0.3275	298.15	913.2
0.3275	303.15	908.97
0.3275	313.15	901.14
0.3275	323.15	893.89
0.3852	293.15	934.26
0.3852	298.15	929.86
0.3852	303.15	925.57
0.3852	313.15	917.73
0.3852	323.15	910.57
0.4259	293.15	945.77
0.4259	298.15	941.31
0.4259	303.15	936.97
0.4259	313.15	929.12
0.4259	323.15	922.02
0.4784	293.15	960.02
0.4784	298.15	955.47
0.4784	303.15	951.09
0.4784	313.15	943.23
0.4784	323.15	936.22
0.5248	293.15	972.29
0.5248	298.15	967.67
0.5248	303.15	963.24
0.5248	313.15	955.38
0.5248	323.15	948.45
0.5649	293.15	982.5
0.5649	298.15	977.82
0.5649	303.15	973.35
0.5649	313.15	965.5
0.5649	323.15	958.65
0.6126	293.15	994.28
0.6126	298.15	989.52
0.6126	303.15	985.02
0.6126	313.15	977.16
0.6126	323.15	970.4
0.6539	293.15	1004.15
0.6539	298.15	999.34
0.6539	303.15	994.8
0.6539	313.15	986.96
0.6539	323.15	980.27
0.6898	293.15	1012.51
0.6898	298.15	1007.64
0.6898	303.15	1003.08
0.6898	313.15	995.25
0.6898	323.15	988.63
0.7353	293.15	1022.74
0.7353	298.15	1017.81
0.7353	303.15	1013.21
0.7353	313.15	1005.4
0.7353	323.15	998.88
0.7962	293.15	1035.87
0.7962	298.15	1030.87
0.7962	303.15	1026.23
0.7962	313.15	1018.44
0.7962	323.15	1012.05
0.8367	293.15	1044.36
0.8367	298.15	1039.31
0.8367	303.15	1034.64
0.8367	313.15	1026.87
0.8367	323.15	1020.56
0.8823	293.15	1053.64
0.8823	298.15	1048.53
0.8823	303.15	1043.84
0.8823	313.15	1036.07
0.8823	323.15	1029.88
0.9248	293.15	1062.23
0.9248	298.15	1057.07
0.9248	303.15	1052.35
0.9248	313.15	1044.62
0.9248	323.15	1038.5
0.9844	293.15	1073.74
0.9844	298.15	1068.51
0.9844	303.15	1063.75
0.9844	313.15	1056.05
0.9844	323.15	1050.07

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of 4-Morpholineethanol (2) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0652	293.15	832.8
0.0652	298.15	829.0
0.0652	303.15	825.1
0.0652	313.15	817.44
0.0652	323.15	809.9
0.1125	293.15	849.1
0.1125	298.15	845.21
0.1125	303.15	841.24
0.1125	313.15	833.54
0.1125	323.15	826.03
0.1865	293.15	873.74
0.1865	298.15	869.7
0.1865	303.15	865.64
0.1865	313.15	857.88
0.1865	323.15	850.45
0.2436	293.15	891.83
0.2436	298.15	887.69
0.2436	303.15	883.56
0.2436	313.15	875.77
0.2436	323.15	868.41
0.2865	293.15	905.09
0.2865	298.15	900.87
0.2865	303.15	896.69
0.2865	313.15	888.88
0.2865	323.15	881.58
0.3275	293.15	917.49
0.3275	298.15	913.2
0.3275	303.15	908.97
0.3275	313.15	901.14
0.3275	323.15	893.89
0.3852	293.15	934.26
0.3852	298.15	929.86
0.3852	303.15	925.57
0.3852	313.15	917.73
0.3852	323.15	910.57
0.4259	293.15	945.77
0.4259	298.15	941.31
0.4259	303.15	936.97
0.4259	313.15	929.12
0.4259	323.15	922.02
0.4784	293.15	960.02
0.4784	298.15	955.47
0.4784	303.15	951.09
0.4784	313.15	943.23
0.4784	323.15	936.22
0.5248	293.15	972.29
0.5248	298.15	967.67
0.5248	303.15	963.24
0.5248	313.15	955.38
0.5248	323.15	948.45
0.5649	293.15	982.5
0.5649	298.15	977.82
0.5649	303.15	973.35
0.5649	313.15	965.5
0.5649	323.15	958.65
0.6126	293.15	994.28
0.6126	298.15	989.52
0.6126	303.15	985.02
0.6126	313.15	977.16
0.6126	323.15	970.4
0.6539	293.15	1004.15
0.6539	298.15	999.34
0.6539	303.15	994.8
0.6539	313.15	986.96
0.6539	323.15	980.27
0.6898	293.15	1012.51
0.6898	298.15	1007.64
0.6898	303.15	1003.08
0.6898	313.15	995.25
0.6898	323.15	988.63
0.7353	293.15	1022.74
0.7353	298.15	1017.81
0.7353	303.15	1013.21
0.7353	313.15	1005.4
0.7353	323.15	998.88
0.7962	293.15	1035.87
0.7962	298.15	1030.87
0.7962	303.15	1026.23
0.7962	313.15	1018.44
0.7962	323.15	1012.05
0.8367	293.15	1044.36
0.8367	298.15	1039.31
0.8367	303.15	1034.64
0.8367	313.15	1026.87
0.8367	323.15	1020.56
0.8823	293.15	1053.64
0.8823	298.15	1048.53
0.8823	303.15	1043.84
0.8823	313.15	1036.07
0.8823	323.15	1029.88
0.9248	293.15	1062.23
0.9248	298.15	1057.07
0.9248	303.15	1052.35
0.9248	313.15	1044.62
0.9248	323.15	1038.5
0.9844	293.15	1073.74
0.9844	298.15	1068.51
0.9844	303.15	1063.75
0.9844	313.15	1056.05
0.9844	323.15	1050.07

Sources

• Densities and volumetric properties of (N-(2-hydroxyethyl)morpholine + ethanol, + 1-propanol, + 2-propanol, + 1-butanol, and + 2-butanol) at (293.15, 298.15, 303.15, 313.15, and 323.15) K