Mixture of Water + 4-Morpholineethanol

Datasets

1. C_p,liquid - Molar heat capacity at constant pressure, J/K/mol (2)
2. η - Viscosity, Pa*s (2)
3. Excess molar enthalpy (molar enthalpy (2)
4. ρ_l - Mass density, kg/m3 (2)

Molar heat capacity at constant pressure, J/K/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 4-Morpholineethanol (2) - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
298.15	0.0998	101.00
303.15	0.0998	102.40
308.15	0.0998	103.80
313.15	0.0998	105.40
318.15	0.0998	107.20
323.15	0.0998	109.00
328.15	0.0998	111.40
333.15	0.0998	114.20
338.15	0.0998	117.40
343.15	0.0998	121.10
348.15	0.0998	125.90
353.15	0.0998	131.90
298.15	0.1985	120.80
303.15	0.1985	123.60
308.15	0.1985	125.70
313.15	0.1985	127.90
318.15	0.1985	130.40
323.15	0.1985	133.00
328.15	0.1985	136.00
333.15	0.1985	139.30
338.15	0.1985	143.20
343.15	0.1985	147.70
348.15	0.1985	152.90
353.15	0.1985	159.50
298.15	0.2979	140.30
303.15	0.2979	142.60
308.15	0.2979	144.60
313.15	0.2979	146.70
318.15	0.2979	148.90
323.15	0.2979	152.30
328.15	0.2979	156.30
333.15	0.2979	160.30
338.15	0.2979	165.00
343.15	0.2979	170.60
348.15	0.2979	178.70
353.15	0.2979	187.00
298.15	0.3969	159.50
303.15	0.3969	162.40
308.15	0.3969	165.00
313.15	0.3969	167.80
318.15	0.3969	171.00
323.15	0.3969	174.40
328.15	0.3969	178.40
333.15	0.3969	183.00
338.15	0.3969	188.60
343.15	0.3969	194.60
348.15	0.3969	201.60
353.15	0.3969	209.90
298.15	0.4952	177.40
303.15	0.4952	180.00
308.15	0.4952	182.60
313.15	0.4952	185.50
318.15	0.4952	188.60
323.15	0.4952	191.80
328.15	0.4952	195.50
333.15	0.4952	199.70
338.15	0.4952	204.60
343.15	0.4952	209.90
348.15	0.4952	215.90
353.15	0.4952	222.50
298.15	0.6017	195.60
303.15	0.6017	198.00
308.15	0.6017	200.30
313.15	0.6017	203.00
318.15	0.6017	205.90
323.15	0.6017	208.70
328.15	0.6017	211.80
333.15	0.6017	215.60
338.15	0.6017	220.10
343.15	0.6017	225.40
348.15	0.6017	231.00
353.15	0.6017	236.40
298.15	0.7031	212.80
303.15	0.7031	214.70
308.15	0.7031	217.10
313.15	0.7031	219.70
318.15	0.7031	222.50
323.15	0.7031	225.50
328.15	0.7031	228.70
333.15	0.7031	232.50
338.15	0.7031	237.00
343.15	0.7031	241.60
348.15	0.7031	246.60
353.15	0.7031	252.20
298.15	0.7657	223.50
303.15	0.7657	226.00
308.15	0.7657	228.30
313.15	0.7657	230.80
318.15	0.7657	233.30
323.15	0.7657	235.80
328.15	0.7657	238.60
333.15	0.7657	242.50
338.15	0.7657	246.30
343.15	0.7657	250.30
348.15	0.7657	254.80
353.15	0.7657	259.40
298.15	0.8977	246.50
303.15	0.8977	248.40
308.15	0.8977	250.80
313.15	0.8977	253.10
318.15	0.8977	255.00
323.15	0.8977	257.00
328.15	0.8977	259.10
333.15	0.8977	261.70
338.15	0.8977	264.70
343.15	0.8977	267.90
348.15	0.8977	271.20
353.15	0.8977	274.80
298.15	1.0000	263.90
303.15	1.0000	265.30
308.15	1.0000	267.10
313.15	1.0000	269.20
318.15	1.0000	270.80
323.15	1.0000	272.60
328.15	1.0000	274.30
333.15	1.0000	276.20
338.15	1.0000	278.70
343.15	1.0000	281.00
348.15	1.0000	283.20
353.15	1.0000	284.90

Molar heat capacity at constant pressure, J/K/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 4-Morpholineethanol (2) - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
298.15	0.0998	101.00
303.15	0.0998	102.40
308.15	0.0998	103.80
313.15	0.0998	105.40
318.15	0.0998	107.20
323.15	0.0998	109.00
328.15	0.0998	111.40
333.15	0.0998	114.20
338.15	0.0998	117.40
343.15	0.0998	121.10
348.15	0.0998	125.90
353.15	0.0998	131.90
298.15	0.1985	120.80
303.15	0.1985	123.60
308.15	0.1985	125.70
313.15	0.1985	127.90
318.15	0.1985	130.40
323.15	0.1985	133.00
328.15	0.1985	136.00
333.15	0.1985	139.30
338.15	0.1985	143.20
343.15	0.1985	147.70
348.15	0.1985	152.90
353.15	0.1985	159.50
298.15	0.2979	140.30
303.15	0.2979	142.60
308.15	0.2979	144.60
313.15	0.2979	146.70
318.15	0.2979	148.90
323.15	0.2979	152.30
328.15	0.2979	156.30
333.15	0.2979	160.30
338.15	0.2979	165.00
343.15	0.2979	170.60
348.15	0.2979	178.70
353.15	0.2979	187.00
298.15	0.3969	159.50
303.15	0.3969	162.40
308.15	0.3969	165.00
313.15	0.3969	167.80
318.15	0.3969	171.00
323.15	0.3969	174.40
328.15	0.3969	178.40
333.15	0.3969	183.00
338.15	0.3969	188.60
343.15	0.3969	194.60
348.15	0.3969	201.60
353.15	0.3969	209.90
298.15	0.4952	177.40
303.15	0.4952	180.00
308.15	0.4952	182.60
313.15	0.4952	185.50
318.15	0.4952	188.60
323.15	0.4952	191.80
328.15	0.4952	195.50
333.15	0.4952	199.70
338.15	0.4952	204.60
343.15	0.4952	209.90
348.15	0.4952	215.90
353.15	0.4952	222.50
298.15	0.6017	195.60
303.15	0.6017	198.00
308.15	0.6017	200.30
313.15	0.6017	203.00
318.15	0.6017	205.90
323.15	0.6017	208.70
328.15	0.6017	211.80
333.15	0.6017	215.60
338.15	0.6017	220.10
343.15	0.6017	225.40
348.15	0.6017	231.00
353.15	0.6017	236.40
298.15	0.7031	212.80
303.15	0.7031	214.70
308.15	0.7031	217.10
313.15	0.7031	219.70
318.15	0.7031	222.50
323.15	0.7031	225.50
328.15	0.7031	228.70
333.15	0.7031	232.50
338.15	0.7031	237.00
343.15	0.7031	241.60
348.15	0.7031	246.60
353.15	0.7031	252.20
298.15	0.7657	223.50
303.15	0.7657	226.00
308.15	0.7657	228.30
313.15	0.7657	230.80
318.15	0.7657	233.30
323.15	0.7657	235.80
328.15	0.7657	238.60
333.15	0.7657	242.50
338.15	0.7657	246.30
343.15	0.7657	250.30
348.15	0.7657	254.80
353.15	0.7657	259.40
298.15	0.8977	246.50
303.15	0.8977	248.40
308.15	0.8977	250.80
313.15	0.8977	253.10
318.15	0.8977	255.00
323.15	0.8977	257.00
328.15	0.8977	259.10
333.15	0.8977	261.70
338.15	0.8977	264.70
343.15	0.8977	267.90
348.15	0.8977	271.20
353.15	0.8977	274.80
298.15	1.0000	263.90
303.15	1.0000	265.30
308.15	1.0000	267.10
313.15	1.0000	269.20
318.15	1.0000	270.80
323.15	1.0000	272.60
328.15	1.0000	274.30
333.15	1.0000	276.20
338.15	1.0000	278.70
343.15	1.0000	281.00
348.15	1.0000	283.20
353.15	1.0000	284.90

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 4-Morpholineethanol (2) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0010
293.15	0.0628	0.0145
293.15	0.1126	0.0230
293.15	0.1985	0.0333
293.15	0.2887	0.0393
293.15	0.3459	0.0418
293.15	0.4127	0.0432
293.15	0.4852	0.0440
293.15	0.5842	0.0433
293.15	0.6438	0.0423
293.15	0.7439	0.0398
293.15	0.8238	0.0363
293.15	0.8846	0.0336
293.15	1.0000	0.0266
303.15	0.0000	0.0008
303.15	0.0628	0.0097
303.15	0.1126	0.0180
303.15	0.1985	0.0275
303.15	0.2887	0.0335
303.15	0.3459	0.0357
303.15	0.4127	0.0373
303.15	0.4852	0.0374
303.15	0.5842	0.0362
303.15	0.6438	0.0349
303.15	0.7439	0.0329
303.15	0.8238	0.0303
303.15	0.8846	0.0271
303.15	1.0000	0.0220
313.15	0.0000	0.0007
313.15	0.0628	0.0081
313.15	0.1126	0.0136
313.15	0.1985	0.0226
313.15	0.2887	0.0283
313.15	0.3459	0.0309
313.15	0.4127	0.0316
313.15	0.4852	0.0314
313.15	0.5842	0.0296
313.15	0.6438	0.0280
313.15	0.7439	0.0256
313.15	0.8238	0.0234
313.15	0.8846	0.0222
313.15	1.0000	0.0173
323.15	0.0000	0.0006
323.15	0.0628	0.0068
323.15	0.1126	0.0114
323.15	0.1985	0.0178
323.15	0.2887	0.0231
323.15	0.3459	0.0255
323.15	0.4127	0.0259
323.15	0.4852	0.0254
323.15	0.5842	0.0232
323.15	0.6438	0.0213
323.15	0.7439	0.0196
323.15	0.8238	0.0180
323.15	0.8846	0.0170
323.15	1.0000	0.0129
333.15	0.0000	0.0005
333.15	0.0628	0.0044
333.15	0.1126	0.0092
333.15	0.1985	0.0139
333.15	0.2887	0.0178
333.15	0.3459	0.0199
333.15	0.4127	0.0201
333.15	0.4852	0.0197
333.15	0.5842	0.0186
333.15	0.6438	0.0162
333.15	0.7439	0.0141
333.15	0.8238	0.0127
333.15	0.8846	0.0113
333.15	1.0000	0.0083

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 4-Morpholineethanol (2) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0010
293.15	0.0628	0.0145
293.15	0.1126	0.0230
293.15	0.1985	0.0333
293.15	0.2887	0.0393
293.15	0.3459	0.0418
293.15	0.4127	0.0432
293.15	0.4852	0.0440
293.15	0.5842	0.0433
293.15	0.6438	0.0423
293.15	0.7439	0.0398
293.15	0.8238	0.0363
293.15	0.8846	0.0336
293.15	1.0000	0.0266
303.15	0.0000	0.0008
303.15	0.0628	0.0097
303.15	0.1126	0.0180
303.15	0.1985	0.0275
303.15	0.2887	0.0335
303.15	0.3459	0.0357
303.15	0.4127	0.0373
303.15	0.4852	0.0374
303.15	0.5842	0.0362
303.15	0.6438	0.0349
303.15	0.7439	0.0329
303.15	0.8238	0.0303
303.15	0.8846	0.0271
303.15	1.0000	0.0220
313.15	0.0000	0.0007
313.15	0.0628	0.0081
313.15	0.1126	0.0136
313.15	0.1985	0.0226
313.15	0.2887	0.0283
313.15	0.3459	0.0309
313.15	0.4127	0.0316
313.15	0.4852	0.0314
313.15	0.5842	0.0296
313.15	0.6438	0.0280
313.15	0.7439	0.0256
313.15	0.8238	0.0234
313.15	0.8846	0.0222
313.15	1.0000	0.0173
323.15	0.0000	0.0006
323.15	0.0628	0.0068
323.15	0.1126	0.0114
323.15	0.1985	0.0178
323.15	0.2887	0.0231
323.15	0.3459	0.0255
323.15	0.4127	0.0259
323.15	0.4852	0.0254
323.15	0.5842	0.0232
323.15	0.6438	0.0213
323.15	0.7439	0.0196
323.15	0.8238	0.0180
323.15	0.8846	0.0170
323.15	1.0000	0.0129
333.15	0.0000	0.0005
333.15	0.0628	0.0044
333.15	0.1126	0.0092
333.15	0.1985	0.0139
333.15	0.2887	0.0178
333.15	0.3459	0.0199
333.15	0.4127	0.0201
333.15	0.4852	0.0197
333.15	0.5842	0.0186
333.15	0.6438	0.0162
333.15	0.7439	0.0141
333.15	0.8238	0.0127
333.15	0.8846	0.0113
333.15	1.0000	0.0083

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 4-Morpholineethanol (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15	0.0301	-0.6120
298.15	0.0700	-1.185
298.15	0.1000	-1.502
298.15	0.1500	-1.931
298.15	0.2005	-2.233
298.15	0.3002	-2.426
298.15	0.4049	-2.465
298.15	0.4989	-2.2633
298.15	0.5970	-2.0438
298.15	0.6949	-1.7936
298.15	0.8055	-1.414
298.15	0.9258	-0.9048
313.15	0.0297	-0.5630
313.15	0.0699	-1.117
313.15	0.1007	-1.465
313.15	0.1510	-1.878
313.15	0.1992	-2.162
313.15	0.3012	-2.373
313.15	0.4035	-2.367
313.15	0.5051	-2.125
313.15	0.6037	-1.855
313.15	0.6954	-1.659
313.15	0.8001	-1.297
313.15	0.9000	-0.8860
333.15	0.0300	-0.4760
333.15	0.0695	-1.06
333.15	0.0999	-1.409
333.15	0.1508	-1.839
333.15	0.2003	-2.089
333.15	0.3005	-2.306
333.15	0.3838	-2.315
333.15	0.4810	-2.023
333.15	0.6044	-1.726
333.15	0.6994	-1.443
333.15	0.8055	-1.208
333.15	0.8969	-0.8120

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 4-Morpholineethanol (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15	0.0301	-0.6120
298.15	0.0700	-1.185
298.15	0.1000	-1.502
298.15	0.1500	-1.931
298.15	0.2005	-2.233
298.15	0.3002	-2.426
298.15	0.4049	-2.465
298.15	0.4989	-2.2633
298.15	0.5970	-2.0438
298.15	0.6949	-1.7936
298.15	0.8055	-1.414
298.15	0.9258	-0.9048
313.15	0.0297	-0.5630
313.15	0.0699	-1.117
313.15	0.1007	-1.465
313.15	0.1510	-1.878
313.15	0.1992	-2.162
313.15	0.3012	-2.373
313.15	0.4035	-2.367
313.15	0.5051	-2.125
313.15	0.6037	-1.855
313.15	0.6954	-1.659
313.15	0.8001	-1.297
313.15	0.9000	-0.8860
333.15	0.0300	-0.4760
333.15	0.0695	-1.06
333.15	0.0999	-1.409
333.15	0.1508	-1.839
333.15	0.2003	-2.089
333.15	0.3005	-2.306
333.15	0.3838	-2.315
333.15	0.4810	-2.023
333.15	0.6044	-1.726
333.15	0.6994	-1.443
333.15	0.8055	-1.208
333.15	0.8969	-0.8120

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 4-Morpholineethanol (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	998.23
293.15	0.0628	1041.44
293.15	0.1126	1061.42
293.15	0.1985	1078.87
293.15	0.2466	1083.81
293.15	0.2887	1086.11
293.15	0.3459	1087.54
293.15	0.4127	1087.67
293.15	0.4852	1086.69
293.15	0.5438	1085.22
293.15	0.5842	1084.37
293.15	0.6438	1082.81
293.15	0.6878	1081.6
293.15	0.7439	1080.31
293.15	0.8238	1078.68
293.15	0.8846	1077.69
293.15	0.9486	1077.17
293.15	1.0000	1076.58
303.15	0.0000	995.85
303.15	0.0628	1033.11
303.15	0.1126	1052.36
303.15	0.1985	1069.04
303.15	0.2466	1073.73
303.15	0.2887	1075.86
303.15	0.3459	1077.13
303.15	0.4127	1077.14
303.15	0.4852	1076.07
303.15	0.5438	1074.56
303.15	0.5842	1073.69
303.15	0.6438	1072.11
303.15	0.6878	1070.89
303.15	0.7439	1069.59
303.15	0.8238	1068.19
303.15	0.8846	1067.27
303.15	0.9486	1066.94
303.15	1.0000	1066.51
313.15	0.0000	992.02
313.15	0.0628	1024.47
313.15	0.1126	1043.65
313.15	0.1985	1060.34
313.15	0.2466	1065.05
313.15	0.2887	1067.22
313.15	0.3459	1068.55
313.15	0.4127	1068.64
313.15	0.4852	1067.65
313.15	0.5438	1066.2
313.15	0.5842	1065.37
313.15	0.6438	1063.85
313.15	0.6878	1062.67
313.15	0.7439	1061.41
313.15	0.8238	1060.06
313.15	0.8846	1059.5
313.15	0.9486	1059.41
313.15	1.0000	1059.19
323.15	0.0000	988.21
323.15	0.0628	1017.66
323.15	0.1126	1035.57
323.15	0.1985	1052.34
323.15	0.2466	1057.12
323.15	0.2887	1059.03
323.15	0.3459	1060.61
323.15	0.4127	1061.07
323.15	0.4852	1060.28
323.15	0.5438	1058.66
323.15	0.5842	1057.87
323.15	0.6438	1056.41
323.15	0.6878	1055.27
323.15	0.7439	1054.22
323.15	0.8238	1053.44
323.15	0.8846	1052.95
323.15	0.9486	1052.79
323.15	1.0000	1052.64
333.15	0.0000	983.35
333.15	0.0628	1012.27
333.15	0.1126	1029.49
333.15	0.1985	1044.12
333.15	0.2466	1048.47
333.15	0.2887	1050.37
333.15	0.3459	1051.89
333.15	0.4127	1052.63
333.15	0.4852	1052.39
333.15	0.5438	1051.46
333.15	0.5842	1050.71
333.15	0.6438	1049.64
333.15	0.6878	1048.84
333.15	0.7439	1047.82
333.15	0.8238	1047.09
333.15	0.8846	1046.7
333.15	0.9486	1046.54
333.15	1.0000	1046.43

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 4-Morpholineethanol (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	998.23
293.15	0.0628	1041.44
293.15	0.1126	1061.42
293.15	0.1985	1078.87
293.15	0.2466	1083.81
293.15	0.2887	1086.11
293.15	0.3459	1087.54
293.15	0.4127	1087.67
293.15	0.4852	1086.69
293.15	0.5438	1085.22
293.15	0.5842	1084.37
293.15	0.6438	1082.81
293.15	0.6878	1081.6
293.15	0.7439	1080.31
293.15	0.8238	1078.68
293.15	0.8846	1077.69
293.15	0.9486	1077.17
293.15	1.0000	1076.58
303.15	0.0000	995.85
303.15	0.0628	1033.11
303.15	0.1126	1052.36
303.15	0.1985	1069.04
303.15	0.2466	1073.73
303.15	0.2887	1075.86
303.15	0.3459	1077.13
303.15	0.4127	1077.14
303.15	0.4852	1076.07
303.15	0.5438	1074.56
303.15	0.5842	1073.69
303.15	0.6438	1072.11
303.15	0.6878	1070.89
303.15	0.7439	1069.59
303.15	0.8238	1068.19
303.15	0.8846	1067.27
303.15	0.9486	1066.94
303.15	1.0000	1066.51
313.15	0.0000	992.02
313.15	0.0628	1024.47
313.15	0.1126	1043.65
313.15	0.1985	1060.34
313.15	0.2466	1065.05
313.15	0.2887	1067.22
313.15	0.3459	1068.55
313.15	0.4127	1068.64
313.15	0.4852	1067.65
313.15	0.5438	1066.2
313.15	0.5842	1065.37
313.15	0.6438	1063.85
313.15	0.6878	1062.67
313.15	0.7439	1061.41
313.15	0.8238	1060.06
313.15	0.8846	1059.5
313.15	0.9486	1059.41
313.15	1.0000	1059.19
323.15	0.0000	988.21
323.15	0.0628	1017.66
323.15	0.1126	1035.57
323.15	0.1985	1052.34
323.15	0.2466	1057.12
323.15	0.2887	1059.03
323.15	0.3459	1060.61
323.15	0.4127	1061.07
323.15	0.4852	1060.28
323.15	0.5438	1058.66
323.15	0.5842	1057.87
323.15	0.6438	1056.41
323.15	0.6878	1055.27
323.15	0.7439	1054.22
323.15	0.8238	1053.44
323.15	0.8846	1052.95
323.15	0.9486	1052.79
323.15	1.0000	1052.64
333.15	0.0000	983.35
333.15	0.0628	1012.27
333.15	0.1126	1029.49
333.15	0.1985	1044.12
333.15	0.2466	1048.47
333.15	0.2887	1050.37
333.15	0.3459	1051.89
333.15	0.4127	1052.63
333.15	0.4852	1052.39
333.15	0.5438	1051.46
333.15	0.5842	1050.71
333.15	0.6438	1049.64
333.15	0.6878	1048.84
333.15	0.7439	1047.82
333.15	0.8238	1047.09
333.15	0.8846	1046.7
333.15	0.9486	1046.54
333.15	1.0000	1046.43

Sources

• Volumetric and viscometric properties of aqueous solutions of N-(2-hydroxyethyl)morpholine at T = (293.15, 303.15, 313.15, 323.15, 333.15) K
• Molar excess enthalpy (Hm E) for systems of aqueous piperazine derivatives
• Molar Heat Capacity (Cp) of Aqueous Cyclic Amine Solutions from (298.15 to 353.15) K