Mixture of 1-Propanol + 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
0.0441	293.15	830.17
0.0441	298.15	823.23
0.0441	303.15	815.35
0.0441	313.15	807.23
0.0441	323.15	799.06
0.1025	293.15	854.6
0.1025	298.15	847.85
0.1025	303.15	839.76
0.1025	313.15	831.61
0.1025	323.15	823.54
0.1771	293.15	883.51
0.1771	298.15	877.01
0.1771	303.15	868.66
0.1771	313.15	860.49
0.1771	323.15	852.56
0.2366	293.15	905.01
0.2366	298.15	898.71
0.2366	303.15	890.18
0.2366	313.15	882.0
0.2366	323.15	874.19
0.2772	293.15	919.15
0.2772	298.15	912.99
0.2772	303.15	904.34
0.2772	313.15	896.16
0.2772	323.15	888.43
0.3146	293.15	931.56
0.3146	298.15	925.53
0.3146	303.15	916.77
0.3146	313.15	908.59
0.3146	323.15	900.94
0.3771	293.15	951.28
0.3771	298.15	945.46
0.3771	303.15	936.54
0.3771	313.15	928.37
0.3771	323.15	920.85
0.4165	293.15	962.97
0.4165	298.15	957.29
0.4165	303.15	948.27
0.4165	313.15	940.11
0.4165	323.15	932.69
0.4780	293.15	980.28
0.4780	298.15	974.81
0.4780	303.15	965.64
0.4780	313.15	957.51
0.4780	323.15	950.23
0.5135	293.15	989.72
0.5135	298.15	984.38
0.5135	303.15	975.14
0.5135	313.15	967.02
0.5135	323.15	959.82
0.5792	293.15	1006.06
0.5792	298.15	1000.96
0.5792	303.15	991.58
0.5792	313.15	983.5
0.5792	323.15	976.47
0.6320	293.15	1018.06
0.6320	298.15	1013.14
0.6320	303.15	1003.67
0.6320	313.15	995.64
0.6320	323.15	988.74
0.6797	293.15	1028.12
0.6797	298.15	1023.38
0.6797	303.15	1013.83
0.6797	313.15	1005.84
0.6797	323.15	999.07
0.7337	293.15	1038.68
0.7337	298.15	1034.12
0.7337	303.15	1024.5
0.7337	313.15	1016.57
0.7337	323.15	1009.94
0.7753	293.15	1046.19
0.7753	298.15	1041.78
0.7753	303.15	1032.12
0.7753	313.15	1024.22
0.7753	323.15	1017.71
0.8136	293.15	1052.76
0.8136	298.15	1048.48
0.8136	303.15	1038.78
0.8136	313.15	1030.93
0.8136	323.15	1024.51
0.8739	293.15	1062.19
0.8739	298.15	1058.11
0.8739	303.15	1048.36
0.8739	313.15	1040.58
0.8739	323.15	1034.34
0.9145	293.15	1067.81
0.9145	298.15	1063.88
0.9145	303.15	1054.1
0.9145	313.15	1046.38
0.9145	323.15	1040.25
0.9442	293.15	1071.98
0.9442	298.15	1068.14
0.9442	303.15	1058.34
0.9442	313.15	1050.66
0.9442	323.15	1044.61
0.9742	293.15	1076.35
0.9742	298.15	1072.61
0.9742	303.15	1062.79
0.9742	313.15	1055.14
0.9742	323.15	1049.16

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
0.0441	293.15	830.17
0.0441	298.15	823.23
0.0441	303.15	815.35
0.0441	313.15	807.23
0.0441	323.15	799.06
0.1025	293.15	854.6
0.1025	298.15	847.85
0.1025	303.15	839.76
0.1025	313.15	831.61
0.1025	323.15	823.54
0.1771	293.15	883.51
0.1771	298.15	877.01
0.1771	303.15	868.66
0.1771	313.15	860.49
0.1771	323.15	852.56
0.2366	293.15	905.01
0.2366	298.15	898.71
0.2366	303.15	890.18
0.2366	313.15	882.0
0.2366	323.15	874.19
0.2772	293.15	919.15
0.2772	298.15	912.99
0.2772	303.15	904.34
0.2772	313.15	896.16
0.2772	323.15	888.43
0.3146	293.15	931.56
0.3146	298.15	925.53
0.3146	303.15	916.77
0.3146	313.15	908.59
0.3146	323.15	900.94
0.3771	293.15	951.28
0.3771	298.15	945.46
0.3771	303.15	936.54
0.3771	313.15	928.37
0.3771	323.15	920.85
0.4165	293.15	962.97
0.4165	298.15	957.29
0.4165	303.15	948.27
0.4165	313.15	940.11
0.4165	323.15	932.69
0.4780	293.15	980.28
0.4780	298.15	974.81
0.4780	303.15	965.64
0.4780	313.15	957.51
0.4780	323.15	950.23
0.5135	293.15	989.72
0.5135	298.15	984.38
0.5135	303.15	975.14
0.5135	313.15	967.02
0.5135	323.15	959.82
0.5792	293.15	1006.06
0.5792	298.15	1000.96
0.5792	303.15	991.58
0.5792	313.15	983.5
0.5792	323.15	976.47
0.6320	293.15	1018.06
0.6320	298.15	1013.14
0.6320	303.15	1003.67
0.6320	313.15	995.64
0.6320	323.15	988.74
0.6797	293.15	1028.12
0.6797	298.15	1023.38
0.6797	303.15	1013.83
0.6797	313.15	1005.84
0.6797	323.15	999.07
0.7337	293.15	1038.68
0.7337	298.15	1034.12
0.7337	303.15	1024.5
0.7337	313.15	1016.57
0.7337	323.15	1009.94
0.7753	293.15	1046.19
0.7753	298.15	1041.78
0.7753	303.15	1032.12
0.7753	313.15	1024.22
0.7753	323.15	1017.71
0.8136	293.15	1052.76
0.8136	298.15	1048.48
0.8136	303.15	1038.78
0.8136	313.15	1030.93
0.8136	323.15	1024.51
0.8739	293.15	1062.19
0.8739	298.15	1058.11
0.8739	303.15	1048.36
0.8739	313.15	1040.58
0.8739	323.15	1034.34
0.9145	293.15	1067.81
0.9145	298.15	1063.88
0.9145	303.15	1054.1
0.9145	313.15	1046.38
0.9145	323.15	1040.25
0.9442	293.15	1071.98
0.9442	298.15	1068.14
0.9442	303.15	1058.34
0.9442	313.15	1050.66
0.9442	323.15	1044.61
0.9742	293.15	1076.35
0.9742	298.15	1072.61
0.9742	303.15	1062.79
0.9742	313.15	1055.14
0.9742	323.15	1049.16

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