Mixture of Isopropyl Alcohol + 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
0.0543	293.15	810.11
0.0543	298.15	806.22
0.0543	303.15	801.63
0.0543	313.15	792.98
0.0543	323.15	784.44
0.1127	293.15	835.5
0.1127	298.15	831.48
0.1127	303.15	826.84
0.1127	313.15	818.19
0.1127	323.15	809.79
0.1873	293.15	865.79
0.1873	298.15	861.61
0.1873	303.15	856.92
0.1873	313.15	848.29
0.1873	323.15	840.07
0.2468	293.15	888.39
0.2468	298.15	884.1
0.2468	303.15	879.38
0.2468	313.15	870.77
0.2468	323.15	862.71
0.2874	293.15	903.13
0.2874	298.15	898.77
0.2874	303.15	894.03
0.2874	313.15	885.45
0.2874	323.15	877.5
0.3248	293.15	916.03
0.3248	298.15	911.6
0.3248	303.15	906.84
0.3248	313.15	898.29
0.3248	323.15	890.46
0.3873	293.15	936.59
0.3873	298.15	932.06
0.3873	303.15	927.29
0.3873	313.15	918.79
0.3873	323.15	911.14
0.4267	293.15	948.75
0.4267	298.15	944.16
0.4267	303.15	939.38
0.4267	313.15	930.92
0.4267	323.15	923.4
0.4882	293.15	967.0
0.4882	298.15	962.32
0.4882	303.15	957.53
0.4882	313.15	949.14
0.4882	323.15	941.81
0.5237	293.15	976.91
0.5237	298.15	972.17
0.5237	303.15	967.38
0.5237	313.15	959.03
0.5237	323.15	951.82
0.5894	293.15	994.19
0.5894	298.15	989.37
0.5894	303.15	984.57
0.5894	313.15	976.32
0.5894	323.15	969.32
0.6422	293.15	1007.31
0.6422	298.15	1002.43
0.6422	303.15	997.63
0.6422	313.15	989.46
0.6422	323.15	982.63
0.6899	293.15	1018.36
0.6899	298.15	1013.43
0.6899	303.15	1008.64
0.6899	313.15	1000.53
0.6899	323.15	993.87
0.7439	293.15	1030.26
0.7439	298.15	1025.27
0.7439	303.15	1020.49
0.7439	313.15	1012.47
0.7439	323.15	1005.99
0.7855	293.15	1038.88
0.7855	298.15	1033.86
0.7855	303.15	1029.09
0.7855	313.15	1021.13
0.7855	323.15	1014.79
0.8238	293.15	1046.42
0.8238	298.15	1041.36
0.8238	303.15	1036.59
0.8238	313.15	1028.7
0.8238	323.15	1022.49
0.8841	293.15	1057.54
0.8841	298.15	1052.43
0.8841	303.15	1047.69
0.8841	313.15	1039.9
0.8841	323.15	1033.9
0.9247	293.15	1064.51
0.9247	298.15	1059.37
0.9247	303.15	1054.64
0.9247	313.15	1046.93
0.9247	323.15	1041.06
0.9544	293.15	1069.21
0.9544	298.15	1064.05
0.9544	303.15	1059.33
0.9544	313.15	1051.68
0.9544	323.15	1045.92
0.9844	293.15	1074.11
0.9844	298.15	1068.93
0.9844	303.15	1064.23
0.9844	313.15	1056.62
0.9844	323.15	1050.96

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
0.0543	293.15	810.11
0.0543	298.15	806.22
0.0543	303.15	801.63
0.0543	313.15	792.98
0.0543	323.15	784.44
0.1127	293.15	835.5
0.1127	298.15	831.48
0.1127	303.15	826.84
0.1127	313.15	818.19
0.1127	323.15	809.79
0.1873	293.15	865.79
0.1873	298.15	861.61
0.1873	303.15	856.92
0.1873	313.15	848.29
0.1873	323.15	840.07
0.2468	293.15	888.39
0.2468	298.15	884.1
0.2468	303.15	879.38
0.2468	313.15	870.77
0.2468	323.15	862.71
0.2874	293.15	903.13
0.2874	298.15	898.77
0.2874	303.15	894.03
0.2874	313.15	885.45
0.2874	323.15	877.5
0.3248	293.15	916.03
0.3248	298.15	911.6
0.3248	303.15	906.84
0.3248	313.15	898.29
0.3248	323.15	890.46
0.3873	293.15	936.59
0.3873	298.15	932.06
0.3873	303.15	927.29
0.3873	313.15	918.79
0.3873	323.15	911.14
0.4267	293.15	948.75
0.4267	298.15	944.16
0.4267	303.15	939.38
0.4267	313.15	930.92
0.4267	323.15	923.4
0.4882	293.15	967.0
0.4882	298.15	962.32
0.4882	303.15	957.53
0.4882	313.15	949.14
0.4882	323.15	941.81
0.5237	293.15	976.91
0.5237	298.15	972.17
0.5237	303.15	967.38
0.5237	313.15	959.03
0.5237	323.15	951.82
0.5894	293.15	994.19
0.5894	298.15	989.37
0.5894	303.15	984.57
0.5894	313.15	976.32
0.5894	323.15	969.32
0.6422	293.15	1007.31
0.6422	298.15	1002.43
0.6422	303.15	997.63
0.6422	313.15	989.46
0.6422	323.15	982.63
0.6899	293.15	1018.36
0.6899	298.15	1013.43
0.6899	303.15	1008.64
0.6899	313.15	1000.53
0.6899	323.15	993.87
0.7439	293.15	1030.26
0.7439	298.15	1025.27
0.7439	303.15	1020.49
0.7439	313.15	1012.47
0.7439	323.15	1005.99
0.7855	293.15	1038.88
0.7855	298.15	1033.86
0.7855	303.15	1029.09
0.7855	313.15	1021.13
0.7855	323.15	1014.79
0.8238	293.15	1046.42
0.8238	298.15	1041.36
0.8238	303.15	1036.59
0.8238	313.15	1028.7
0.8238	323.15	1022.49
0.8841	293.15	1057.54
0.8841	298.15	1052.43
0.8841	303.15	1047.69
0.8841	313.15	1039.9
0.8841	323.15	1033.9
0.9247	293.15	1064.51
0.9247	298.15	1059.37
0.9247	303.15	1054.64
0.9247	313.15	1046.93
0.9247	323.15	1041.06
0.9544	293.15	1069.21
0.9544	298.15	1064.05
0.9544	303.15	1059.33
0.9544	313.15	1051.68
0.9544	323.15	1045.92
0.9844	293.15	1074.11
0.9844	298.15	1068.93
0.9844	303.15	1064.23
0.9844	313.15	1056.62
0.9844	323.15	1050.96

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