Datasets
-
η - Viscosity, Pa*s (10)
-
Excess molar enthalpy (molar enthalpy (2)
-
ρl - Mass density, kg/m3 (8)
-
γ - Surface tension liquid-gas, N/m (4)
-
Tfus - Solid-liquid equilibrium temperature, K (2)
-
Binary diffusion coefficient, m2/s (2)
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of N,N-Diethyl-2-aminoethanol (1) - Liquid |
Viscosity, Pa*s - Liquid |
293.15 |
0.0000 |
0.0010 |
293.15 |
0.1001 |
0.0079 |
293.15 |
0.2005 |
0.0170 |
293.15 |
0.2997 |
0.0205 |
293.15 |
0.3978 |
0.0203 |
293.15 |
0.4997 |
0.0177 |
293.15 |
0.5992 |
0.0148 |
293.15 |
0.6897 |
0.0124 |
293.15 |
0.7997 |
0.0097 |
293.15 |
0.8997 |
0.0073 |
293.15 |
1.0000 |
0.0048 |
303.15 |
0.0000 |
0.0008 |
303.15 |
0.1001 |
0.0055 |
303.15 |
0.2005 |
0.0100 |
303.15 |
0.2997 |
0.0110 |
303.15 |
0.3978 |
0.0100 |
303.15 |
0.4997 |
0.0091 |
303.15 |
0.5992 |
0.0084 |
303.15 |
0.6897 |
0.0071 |
303.15 |
0.7997 |
0.0060 |
303.15 |
0.8997 |
0.0049 |
303.15 |
1.0000 |
0.0034 |
313.15 |
0.0000 |
0.0007 |
313.15 |
0.1001 |
0.0037 |
313.15 |
0.2005 |
0.0063 |
313.15 |
0.2997 |
0.0072 |
313.15 |
0.3978 |
0.0061 |
313.15 |
0.4997 |
0.0055 |
313.15 |
0.5992 |
0.0051 |
313.15 |
0.6897 |
0.0047 |
313.15 |
0.7997 |
0.0039 |
313.15 |
0.8997 |
0.0034 |
313.15 |
1.0000 |
0.0025 |
323.15 |
0.0000 |
0.0006 |
323.15 |
0.1001 |
0.0026 |
323.15 |
0.2005 |
0.0042 |
323.15 |
0.2997 |
0.0046 |
323.15 |
0.3978 |
0.0041 |
323.15 |
0.4997 |
0.0036 |
323.15 |
0.5992 |
0.0031 |
323.15 |
0.6897 |
0.0027 |
323.15 |
0.7997 |
0.0022 |
323.15 |
0.8997 |
0.0021 |
323.15 |
1.0000 |
0.0019 |
333.15 |
0.0000 |
0.0005 |
333.15 |
0.1001 |
0.0019 |
333.15 |
0.2005 |
0.0029 |
333.15 |
0.2997 |
0.0032 |
333.15 |
0.3978 |
0.0030 |
333.15 |
0.4997 |
0.0026 |
333.15 |
0.5992 |
0.0024 |
333.15 |
0.6897 |
0.0021 |
333.15 |
0.7997 |
0.0018 |
333.15 |
0.8997 |
0.0016 |
333.15 |
1.0000 |
0.0014 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Mass fraction of N,N-Diethyl-2-aminoethanol (1) - Liquid |
Temperature, K - Liquid |
Viscosity, Pa*s - Liquid |
0.1500 |
303.15 |
0.0015 |
0.1500 |
313.15 |
0.0012 |
0.1500 |
323.15 |
0.0009 |
0.1500 |
333.15 |
0.0008 |
0.1500 |
343.15 |
0.0006 |
0.1500 |
353.15 |
0.0005 |
0.3000 |
353.15 |
0.0008 |
0.3000 |
303.15 |
0.0029 |
0.3000 |
313.15 |
0.0021 |
0.3000 |
323.15 |
0.0015 |
0.3000 |
333.15 |
0.0012 |
0.3000 |
343.15 |
0.0010 |
0.4500 |
353.15 |
0.0011 |
0.4500 |
303.15 |
0.0052 |
0.4500 |
313.15 |
0.0035 |
0.4500 |
323.15 |
0.0025 |
0.4500 |
333.15 |
0.0019 |
0.4500 |
343.15 |
0.0014 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Mass fraction of N,N-Diethyl-2-aminoethanol (1) - Liquid |
Temperature, K - Liquid |
Viscosity, Pa*s - Liquid |
0.3000 |
303.15 |
0.0030 |
0.3000 |
313.15 |
0.0021 |
0.3000 |
323.15 |
0.0016 |
0.3000 |
333.15 |
0.0013 |
0.3000 |
343.15 |
0.0010 |
0.3000 |
353.15 |
0.0008 |
0.4000 |
303.15 |
0.0045 |
0.4000 |
313.15 |
0.0031 |
0.4000 |
323.15 |
0.0022 |
0.4000 |
333.15 |
0.0018 |
0.4000 |
343.15 |
0.0014 |
0.4000 |
353.15 |
0.0012 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of N,N-Diethyl-2-aminoethanol (1) - Liquid |
Viscosity, Pa*s - Liquid |
298.15 |
0.0000 |
0.0009 |
303.15 |
0.0000 |
0.0008 |
313.15 |
0.0000 |
0.0006 |
323.15 |
0.0000 |
0.0006 |
333.15 |
0.0000 |
0.0005 |
298.15 |
0.0201 |
0.0022 |
303.15 |
0.0201 |
0.0014 |
313.15 |
0.0201 |
0.0011 |
323.15 |
0.0201 |
0.0009 |
333.15 |
0.0201 |
0.0008 |
298.15 |
0.0455 |
0.0036 |
303.15 |
0.0455 |
0.0023 |
313.15 |
0.0455 |
0.0017 |
323.15 |
0.0455 |
0.0013 |
333.15 |
0.0455 |
0.0010 |
298.15 |
0.0788 |
0.0056 |
303.15 |
0.0788 |
0.0036 |
313.15 |
0.0788 |
0.0024 |
323.15 |
0.0788 |
0.0017 |
333.15 |
0.0788 |
0.0012 |
298.15 |
0.1252 |
0.0080 |
303.15 |
0.1252 |
0.0057 |
313.15 |
0.1252 |
0.0038 |
323.15 |
0.1252 |
0.0026 |
333.15 |
0.1252 |
0.0019 |
298.15 |
0.1933 |
0.0116 |
303.15 |
0.1933 |
0.0080 |
313.15 |
0.1933 |
0.0053 |
323.15 |
0.1933 |
0.0037 |
333.15 |
0.1933 |
0.0025 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of N,N-Diethyl-2-aminoethanol (1) - Liquid |
Viscosity, Pa*s - Liquid |
298.15 |
0.0000 |
0.0009 |
298.15 |
0.0100 |
0.0012 |
298.15 |
0.0202 |
0.0015 |
298.15 |
0.0300 |
0.0019 |
298.15 |
0.0401 |
0.0024 |
298.15 |
0.0595 |
0.0035 |
298.15 |
0.0615 |
0.0035 |
298.15 |
0.0703 |
0.0041 |
298.15 |
0.0876 |
0.0052 |
298.15 |
0.0901 |
0.0053 |
298.15 |
0.1100 |
0.0066 |
298.15 |
0.1200 |
0.0072 |
298.15 |
0.1301 |
0.0079 |
298.15 |
0.1401 |
0.0085 |
298.15 |
0.1483 |
0.0090 |
298.15 |
0.1603 |
0.0097 |
298.15 |
0.1704 |
0.0103 |
298.15 |
0.1905 |
0.0113 |
298.15 |
0.2004 |
0.0118 |
298.15 |
0.2104 |
0.0122 |
298.15 |
0.2200 |
0.0127 |
298.15 |
0.2301 |
0.0130 |
298.15 |
0.2401 |
0.0134 |
298.15 |
0.2530 |
0.0138 |
298.15 |
0.2674 |
0.0142 |
298.15 |
0.2701 |
0.0143 |
298.15 |
0.2801 |
0.0145 |
298.15 |
0.2900 |
0.0148 |
298.15 |
0.3022 |
0.0150 |
298.15 |
0.3500 |
0.0154 |
298.15 |
0.3999 |
0.0150 |
298.15 |
0.4507 |
0.0146 |
298.15 |
0.5001 |
0.0134 |
298.15 |
0.5504 |
0.0123 |
298.15 |
0.6001 |
0.0110 |
298.15 |
0.6514 |
0.0097 |
298.15 |
0.7000 |
0.0086 |
298.15 |
0.7508 |
0.0075 |
298.15 |
0.8001 |
0.0066 |
298.15 |
0.8508 |
0.0057 |
298.15 |
0.9001 |
0.0051 |
298.15 |
0.9501 |
0.0045 |
298.15 |
1.0000 |
0.0040 |
303.15 |
0.0000 |
0.0008 |
303.15 |
0.0100 |
0.0011 |
303.15 |
0.0202 |
0.0013 |
303.15 |
0.0398 |
0.0020 |
303.15 |
0.0502 |
0.0025 |
303.15 |
0.0603 |
0.0029 |
303.15 |
0.0700 |
0.0034 |
303.15 |
0.0805 |
0.0039 |
303.15 |
0.0898 |
0.0043 |
303.15 |
0.1100 |
0.0053 |
303.15 |
0.1200 |
0.0057 |
303.15 |
0.1301 |
0.0062 |
303.15 |
0.1401 |
0.0067 |
303.15 |
0.1511 |
0.0072 |
303.15 |
0.1603 |
0.0075 |
303.15 |
0.1704 |
0.0080 |
303.15 |
0.1897 |
0.0087 |
303.15 |
0.1998 |
0.0090 |
303.15 |
0.2104 |
0.0094 |
303.15 |
0.2200 |
0.0097 |
303.15 |
0.2301 |
0.0100 |
303.15 |
0.2401 |
0.0103 |
303.15 |
0.2498 |
0.0105 |
303.15 |
0.2674 |
0.0108 |
303.15 |
0.2701 |
0.0109 |
303.15 |
0.2801 |
0.0110 |
303.15 |
0.2900 |
0.0112 |
303.15 |
0.3003 |
0.0112 |
303.15 |
0.3500 |
0.0115 |
303.15 |
0.3997 |
0.0115 |
303.15 |
0.4330 |
0.0111 |
303.15 |
0.4995 |
0.0102 |
303.15 |
0.5498 |
0.0094 |
303.15 |
0.5997 |
0.0085 |
303.15 |
0.6499 |
0.0076 |
303.15 |
0.7001 |
0.0067 |
303.15 |
0.7498 |
0.0060 |
303.15 |
0.8000 |
0.0053 |
303.15 |
0.8499 |
0.0047 |
303.15 |
0.9000 |
0.0042 |
303.15 |
0.9500 |
0.0037 |
303.15 |
1.0000 |
0.0034 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of N,N-Diethyl-2-aminoethanol (1) - Liquid |
Viscosity, Pa*s - Liquid |
293.15 |
0.0000 |
0.0010 |
293.15 |
0.1001 |
0.0079 |
293.15 |
0.2005 |
0.0170 |
293.15 |
0.2997 |
0.0205 |
293.15 |
0.3978 |
0.0203 |
293.15 |
0.4997 |
0.0177 |
293.15 |
0.5992 |
0.0148 |
293.15 |
0.6897 |
0.0124 |
293.15 |
0.7997 |
0.0097 |
293.15 |
0.8997 |
0.0073 |
293.15 |
1.0000 |
0.0048 |
303.15 |
0.0000 |
0.0008 |
303.15 |
0.1001 |
0.0055 |
303.15 |
0.2005 |
0.0100 |
303.15 |
0.2997 |
0.0110 |
303.15 |
0.3978 |
0.0100 |
303.15 |
0.4997 |
0.0091 |
303.15 |
0.5992 |
0.0084 |
303.15 |
0.6897 |
0.0071 |
303.15 |
0.7997 |
0.0060 |
303.15 |
0.8997 |
0.0049 |
303.15 |
1.0000 |
0.0034 |
313.15 |
0.0000 |
0.0007 |
313.15 |
0.1001 |
0.0037 |
313.15 |
0.2005 |
0.0063 |
313.15 |
0.2997 |
0.0072 |
313.15 |
0.3978 |
0.0061 |
313.15 |
0.4997 |
0.0055 |
313.15 |
0.5992 |
0.0051 |
313.15 |
0.6897 |
0.0047 |
313.15 |
0.7997 |
0.0039 |
313.15 |
0.8997 |
0.0034 |
313.15 |
1.0000 |
0.0025 |
323.15 |
0.0000 |
0.0006 |
323.15 |
0.1001 |
0.0026 |
323.15 |
0.2005 |
0.0042 |
323.15 |
0.2997 |
0.0046 |
323.15 |
0.3978 |
0.0041 |
323.15 |
0.4997 |
0.0036 |
323.15 |
0.5992 |
0.0031 |
323.15 |
0.6897 |
0.0027 |
323.15 |
0.7997 |
0.0022 |
323.15 |
0.8997 |
0.0021 |
323.15 |
1.0000 |
0.0019 |
333.15 |
0.0000 |
0.0005 |
333.15 |
0.1001 |
0.0019 |
333.15 |
0.2005 |
0.0029 |
333.15 |
0.2997 |
0.0032 |
333.15 |
0.3978 |
0.0030 |
333.15 |
0.4997 |
0.0026 |
333.15 |
0.5992 |
0.0024 |
333.15 |
0.6897 |
0.0021 |
333.15 |
0.7997 |
0.0018 |
333.15 |
0.8997 |
0.0016 |
333.15 |
1.0000 |
0.0014 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Mass fraction of N,N-Diethyl-2-aminoethanol (1) - Liquid |
Temperature, K - Liquid |
Viscosity, Pa*s - Liquid |
0.1500 |
303.15 |
0.0015 |
0.1500 |
313.15 |
0.0012 |
0.1500 |
323.15 |
0.0009 |
0.1500 |
333.15 |
0.0008 |
0.1500 |
343.15 |
0.0006 |
0.1500 |
353.15 |
0.0005 |
0.3000 |
353.15 |
0.0008 |
0.3000 |
303.15 |
0.0029 |
0.3000 |
313.15 |
0.0021 |
0.3000 |
323.15 |
0.0015 |
0.3000 |
333.15 |
0.0012 |
0.3000 |
343.15 |
0.0010 |
0.4500 |
353.15 |
0.0011 |
0.4500 |
303.15 |
0.0052 |
0.4500 |
313.15 |
0.0035 |
0.4500 |
323.15 |
0.0025 |
0.4500 |
333.15 |
0.0019 |
0.4500 |
343.15 |
0.0014 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Mass fraction of N,N-Diethyl-2-aminoethanol (1) - Liquid |
Temperature, K - Liquid |
Viscosity, Pa*s - Liquid |
0.3000 |
303.15 |
0.0030 |
0.3000 |
313.15 |
0.0021 |
0.3000 |
323.15 |
0.0016 |
0.3000 |
333.15 |
0.0013 |
0.3000 |
343.15 |
0.0010 |
0.3000 |
353.15 |
0.0008 |
0.4000 |
303.15 |
0.0045 |
0.4000 |
313.15 |
0.0031 |
0.4000 |
323.15 |
0.0022 |
0.4000 |
333.15 |
0.0018 |
0.4000 |
343.15 |
0.0014 |
0.4000 |
353.15 |
0.0012 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of N,N-Diethyl-2-aminoethanol (1) - Liquid |
Viscosity, Pa*s - Liquid |
298.15 |
0.0000 |
0.0009 |
303.15 |
0.0000 |
0.0008 |
313.15 |
0.0000 |
0.0006 |
323.15 |
0.0000 |
0.0006 |
333.15 |
0.0000 |
0.0005 |
298.15 |
0.0201 |
0.0022 |
303.15 |
0.0201 |
0.0014 |
313.15 |
0.0201 |
0.0011 |
323.15 |
0.0201 |
0.0009 |
333.15 |
0.0201 |
0.0008 |
298.15 |
0.0455 |
0.0036 |
303.15 |
0.0455 |
0.0023 |
313.15 |
0.0455 |
0.0017 |
323.15 |
0.0455 |
0.0013 |
333.15 |
0.0455 |
0.0010 |
298.15 |
0.0788 |
0.0056 |
303.15 |
0.0788 |
0.0036 |
313.15 |
0.0788 |
0.0024 |
323.15 |
0.0788 |
0.0017 |
333.15 |
0.0788 |
0.0012 |
298.15 |
0.1252 |
0.0080 |
303.15 |
0.1252 |
0.0057 |
313.15 |
0.1252 |
0.0038 |
323.15 |
0.1252 |
0.0026 |
333.15 |
0.1252 |
0.0019 |
298.15 |
0.1933 |
0.0116 |
303.15 |
0.1933 |
0.0080 |
313.15 |
0.1933 |
0.0053 |
323.15 |
0.1933 |
0.0037 |
333.15 |
0.1933 |
0.0025 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of N,N-Diethyl-2-aminoethanol (1) - Liquid |
Viscosity, Pa*s - Liquid |
298.15 |
0.0000 |
0.0009 |
298.15 |
0.0100 |
0.0012 |
298.15 |
0.0202 |
0.0015 |
298.15 |
0.0300 |
0.0019 |
298.15 |
0.0401 |
0.0024 |
298.15 |
0.0595 |
0.0035 |
298.15 |
0.0615 |
0.0035 |
298.15 |
0.0703 |
0.0041 |
298.15 |
0.0876 |
0.0052 |
298.15 |
0.0901 |
0.0053 |
298.15 |
0.1100 |
0.0066 |
298.15 |
0.1200 |
0.0072 |
298.15 |
0.1301 |
0.0079 |
298.15 |
0.1401 |
0.0085 |
298.15 |
0.1483 |
0.0090 |
298.15 |
0.1603 |
0.0097 |
298.15 |
0.1704 |
0.0103 |
298.15 |
0.1905 |
0.0113 |
298.15 |
0.2004 |
0.0118 |
298.15 |
0.2104 |
0.0122 |
298.15 |
0.2200 |
0.0127 |
298.15 |
0.2301 |
0.0130 |
298.15 |
0.2401 |
0.0134 |
298.15 |
0.2530 |
0.0138 |
298.15 |
0.2674 |
0.0142 |
298.15 |
0.2701 |
0.0143 |
298.15 |
0.2801 |
0.0145 |
298.15 |
0.2900 |
0.0148 |
298.15 |
0.3022 |
0.0150 |
298.15 |
0.3500 |
0.0154 |
298.15 |
0.3999 |
0.0150 |
298.15 |
0.4507 |
0.0146 |
298.15 |
0.5001 |
0.0134 |
298.15 |
0.5504 |
0.0123 |
298.15 |
0.6001 |
0.0110 |
298.15 |
0.6514 |
0.0097 |
298.15 |
0.7000 |
0.0086 |
298.15 |
0.7508 |
0.0075 |
298.15 |
0.8001 |
0.0066 |
298.15 |
0.8508 |
0.0057 |
298.15 |
0.9001 |
0.0051 |
298.15 |
0.9501 |
0.0045 |
298.15 |
1.0000 |
0.0040 |
303.15 |
0.0000 |
0.0008 |
303.15 |
0.0100 |
0.0011 |
303.15 |
0.0202 |
0.0013 |
303.15 |
0.0398 |
0.0020 |
303.15 |
0.0502 |
0.0025 |
303.15 |
0.0603 |
0.0029 |
303.15 |
0.0700 |
0.0034 |
303.15 |
0.0805 |
0.0039 |
303.15 |
0.0898 |
0.0043 |
303.15 |
0.1100 |
0.0053 |
303.15 |
0.1200 |
0.0057 |
303.15 |
0.1301 |
0.0062 |
303.15 |
0.1401 |
0.0067 |
303.15 |
0.1511 |
0.0072 |
303.15 |
0.1603 |
0.0075 |
303.15 |
0.1704 |
0.0080 |
303.15 |
0.1897 |
0.0087 |
303.15 |
0.1998 |
0.0090 |
303.15 |
0.2104 |
0.0094 |
303.15 |
0.2200 |
0.0097 |
303.15 |
0.2301 |
0.0100 |
303.15 |
0.2401 |
0.0103 |
303.15 |
0.2498 |
0.0105 |
303.15 |
0.2674 |
0.0108 |
303.15 |
0.2701 |
0.0109 |
303.15 |
0.2801 |
0.0110 |
303.15 |
0.2900 |
0.0112 |
303.15 |
0.3003 |
0.0112 |
303.15 |
0.3500 |
0.0115 |
303.15 |
0.3997 |
0.0115 |
303.15 |
0.4330 |
0.0111 |
303.15 |
0.4995 |
0.0102 |
303.15 |
0.5498 |
0.0094 |
303.15 |
0.5997 |
0.0085 |
303.15 |
0.6499 |
0.0076 |
303.15 |
0.7001 |
0.0067 |
303.15 |
0.7498 |
0.0060 |
303.15 |
0.8000 |
0.0053 |
303.15 |
0.8499 |
0.0047 |
303.15 |
0.9000 |
0.0042 |
303.15 |
0.9500 |
0.0037 |
303.15 |
1.0000 |
0.0034 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of N,N-Diethyl-2-aminoethanol (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
303.15 |
0.0504 |
-1.058 |
303.15 |
0.1001 |
-1.577 |
303.15 |
0.2008 |
-2.185 |
303.15 |
0.3010 |
-2.538 |
303.15 |
0.3688 |
-2.592 |
303.15 |
0.3870 |
-2.617 |
303.15 |
0.4002 |
-2.598 |
303.15 |
0.4522 |
-2.558 |
303.15 |
0.5002 |
-2.504 |
303.15 |
0.5998 |
-2.21 |
303.15 |
0.7003 |
-1.75 |
303.15 |
0.8007 |
-1.204 |
303.15 |
0.9010 |
-0.6020 |
323.15 |
0.0502 |
-0.8020 |
323.15 |
0.1009 |
-1.237 |
323.15 |
0.1951 |
-1.703 |
323.15 |
0.3002 |
-2.017 |
323.15 |
0.3690 |
-2.089 |
323.15 |
0.4006 |
-2.099 |
323.15 |
0.5005 |
-1.996 |
323.15 |
0.6000 |
-1.764 |
323.15 |
0.6191 |
-1.615 |
323.15 |
0.6997 |
-1.425 |
323.15 |
0.8005 |
-1.055 |
323.15 |
0.9006 |
-0.5010 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of N,N-Diethyl-2-aminoethanol (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
303.15 |
0.0504 |
-1.058 |
303.15 |
0.1001 |
-1.577 |
303.15 |
0.2008 |
-2.185 |
303.15 |
0.3010 |
-2.538 |
303.15 |
0.3688 |
-2.592 |
303.15 |
0.3870 |
-2.617 |
303.15 |
0.4002 |
-2.598 |
303.15 |
0.4522 |
-2.558 |
303.15 |
0.5002 |
-2.504 |
303.15 |
0.5998 |
-2.21 |
303.15 |
0.7003 |
-1.75 |
303.15 |
0.8007 |
-1.204 |
303.15 |
0.9010 |
-0.6020 |
323.15 |
0.0502 |
-0.8020 |
323.15 |
0.1009 |
-1.237 |
323.15 |
0.1951 |
-1.703 |
323.15 |
0.3002 |
-2.017 |
323.15 |
0.3690 |
-2.089 |
323.15 |
0.4006 |
-2.099 |
323.15 |
0.5005 |
-1.996 |
323.15 |
0.6000 |
-1.764 |
323.15 |
0.6191 |
-1.615 |
323.15 |
0.6997 |
-1.425 |
323.15 |
0.8005 |
-1.055 |
323.15 |
0.9006 |
-0.5010 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of N,N-Diethyl-2-aminoethanol (1) - Liquid |
Mass density, kg/m3 - Liquid |
293.15 |
0.0000 |
998.2 |
293.15 |
0.1001 |
982.0 |
293.15 |
0.2005 |
962.4 |
293.15 |
0.2997 |
946.6 |
293.15 |
0.3978 |
933.4 |
293.15 |
0.4997 |
922.2 |
293.15 |
0.5992 |
914.4 |
293.15 |
0.6897 |
906.3 |
293.15 |
0.7997 |
899.6 |
293.15 |
0.8997 |
895.5 |
293.15 |
1.0000 |
891.2 |
303.15 |
0.0000 |
995.7 |
303.15 |
0.1001 |
974.2 |
303.15 |
0.2005 |
953.0 |
303.15 |
0.2997 |
936.8 |
303.15 |
0.3978 |
923.2 |
303.15 |
0.4997 |
912.0 |
303.15 |
0.5992 |
903.2 |
303.15 |
0.6897 |
894.8 |
303.15 |
0.7997 |
887.4 |
303.15 |
0.8997 |
880.8 |
303.15 |
1.0000 |
874.4 |
313.15 |
0.0000 |
992.3 |
313.15 |
0.1001 |
966.6 |
313.15 |
0.2005 |
944.3 |
313.15 |
0.2997 |
926.9 |
313.15 |
0.3978 |
913.9 |
313.15 |
0.4997 |
901.8 |
313.15 |
0.5992 |
892.8 |
313.15 |
0.6897 |
884.2 |
313.15 |
0.7997 |
876.9 |
313.15 |
0.8997 |
870.7 |
313.15 |
1.0000 |
865.4 |
323.15 |
0.0000 |
988.1 |
323.15 |
0.1001 |
958.5 |
323.15 |
0.2005 |
935.0 |
323.15 |
0.2997 |
917.5 |
323.15 |
0.3978 |
903.7 |
323.15 |
0.4997 |
892.0 |
323.15 |
0.5992 |
882.3 |
323.15 |
0.6897 |
873.9 |
323.15 |
0.7997 |
867.4 |
323.15 |
0.8997 |
861.4 |
323.15 |
1.0000 |
856.4 |
333.15 |
0.0000 |
983.3 |
333.15 |
0.1001 |
950.1 |
333.15 |
0.2005 |
925.6 |
333.15 |
0.2997 |
907.6 |
333.15 |
0.3978 |
893.9 |
333.15 |
0.4997 |
882.4 |
333.15 |
0.5992 |
872.5 |
333.15 |
0.6897 |
864.7 |
333.15 |
0.7997 |
857.3 |
333.15 |
0.8997 |
851.9 |
333.15 |
1.0000 |
845.6 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Mass fraction of N,N-Diethyl-2-aminoethanol (1) - Liquid |
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
0.1500 |
298.15 |
993.03 |
0.1500 |
303.15 |
990.95 |
0.1500 |
313.15 |
986.24 |
0.1500 |
323.15 |
980.89 |
0.1500 |
333.15 |
974.93 |
0.1500 |
343.15 |
968.49 |
0.1500 |
353.15 |
961.55 |
0.3000 |
298.15 |
986.96 |
0.3000 |
303.15 |
983.79 |
0.3000 |
313.15 |
977.15 |
0.3000 |
323.15 |
970.11 |
0.3000 |
333.15 |
962.69 |
0.3000 |
343.15 |
954.88 |
0.3000 |
353.15 |
946.71 |
0.4500 |
298.15 |
975.72 |
0.4500 |
303.15 |
971.87 |
0.4500 |
313.15 |
963.92 |
0.4500 |
323.15 |
955.68 |
0.4500 |
333.15 |
947.12 |
0.4500 |
343.15 |
938.27 |
0.4500 |
353.15 |
929.11 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Mass fraction of N,N-Diethyl-2-aminoethanol (1) - Liquid |
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
0.3000 |
298.15 |
987.24 |
0.3000 |
303.15 |
984.1 |
0.3000 |
313.15 |
977.49 |
0.3000 |
323.15 |
970.47 |
0.3000 |
333.15 |
963.06 |
0.3000 |
343.15 |
955.26 |
0.3000 |
353.15 |
947.1 |
0.4000 |
298.15 |
980.18 |
0.4000 |
303.15 |
976.55 |
0.4000 |
313.15 |
969.01 |
0.4000 |
323.15 |
961.13 |
0.4000 |
333.15 |
952.94 |
0.4000 |
343.15 |
944.42 |
0.4000 |
353.15 |
935.57 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of N,N-Diethyl-2-aminoethanol (1) - Liquid |
Mass density, kg/m3 - Liquid |
298.15 |
0.0000 |
997.04 |
313.15 |
0.0000 |
992.22 |
333.15 |
0.0000 |
983.2 |
298.15 |
0.0201 |
993.744 |
313.15 |
0.0201 |
987.552 |
333.15 |
0.0201 |
976.86 |
298.15 |
0.0455 |
990.151 |
313.15 |
0.0455 |
981.577 |
333.15 |
0.0455 |
968.366 |
298.15 |
0.0788 |
983.322 |
313.15 |
0.0788 |
972.648 |
333.15 |
0.0788 |
957.191 |
298.15 |
0.1252 |
971.858 |
313.15 |
0.1252 |
959.656 |
333.15 |
0.1252 |
942.334 |
298.15 |
0.1933 |
961.569 |
313.15 |
0.1933 |
948.632 |
333.15 |
0.1933 |
930.379 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of N,N-Diethyl-2-aminoethanol (1) - Liquid |
Mass density, kg/m3 - Liquid |
293.15 |
0.0000 |
998.2 |
293.15 |
0.1001 |
982.0 |
293.15 |
0.2005 |
962.4 |
293.15 |
0.2997 |
946.6 |
293.15 |
0.3978 |
933.4 |
293.15 |
0.4997 |
922.2 |
293.15 |
0.5992 |
914.4 |
293.15 |
0.6897 |
906.3 |
293.15 |
0.7997 |
899.6 |
293.15 |
0.8997 |
895.5 |
293.15 |
1.0000 |
891.2 |
303.15 |
0.0000 |
995.7 |
303.15 |
0.1001 |
974.2 |
303.15 |
0.2005 |
953.0 |
303.15 |
0.2997 |
936.8 |
303.15 |
0.3978 |
923.2 |
303.15 |
0.4997 |
912.0 |
303.15 |
0.5992 |
903.2 |
303.15 |
0.6897 |
894.8 |
303.15 |
0.7997 |
887.4 |
303.15 |
0.8997 |
880.8 |
303.15 |
1.0000 |
874.4 |
313.15 |
0.0000 |
992.3 |
313.15 |
0.1001 |
966.6 |
313.15 |
0.2005 |
944.3 |
313.15 |
0.2997 |
926.9 |
313.15 |
0.3978 |
913.9 |
313.15 |
0.4997 |
901.8 |
313.15 |
0.5992 |
892.8 |
313.15 |
0.6897 |
884.2 |
313.15 |
0.7997 |
876.9 |
313.15 |
0.8997 |
870.7 |
313.15 |
1.0000 |
865.4 |
323.15 |
0.0000 |
988.1 |
323.15 |
0.1001 |
958.5 |
323.15 |
0.2005 |
935.0 |
323.15 |
0.2997 |
917.5 |
323.15 |
0.3978 |
903.7 |
323.15 |
0.4997 |
892.0 |
323.15 |
0.5992 |
882.3 |
323.15 |
0.6897 |
873.9 |
323.15 |
0.7997 |
867.4 |
323.15 |
0.8997 |
861.4 |
323.15 |
1.0000 |
856.4 |
333.15 |
0.0000 |
983.3 |
333.15 |
0.1001 |
950.1 |
333.15 |
0.2005 |
925.6 |
333.15 |
0.2997 |
907.6 |
333.15 |
0.3978 |
893.9 |
333.15 |
0.4997 |
882.4 |
333.15 |
0.5992 |
872.5 |
333.15 |
0.6897 |
864.7 |
333.15 |
0.7997 |
857.3 |
333.15 |
0.8997 |
851.9 |
333.15 |
1.0000 |
845.6 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Mass fraction of N,N-Diethyl-2-aminoethanol (1) - Liquid |
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
0.1500 |
298.15 |
993.03 |
0.1500 |
303.15 |
990.95 |
0.1500 |
313.15 |
986.24 |
0.1500 |
323.15 |
980.89 |
0.1500 |
333.15 |
974.93 |
0.1500 |
343.15 |
968.49 |
0.1500 |
353.15 |
961.55 |
0.3000 |
298.15 |
986.96 |
0.3000 |
303.15 |
983.79 |
0.3000 |
313.15 |
977.15 |
0.3000 |
323.15 |
970.11 |
0.3000 |
333.15 |
962.69 |
0.3000 |
343.15 |
954.88 |
0.3000 |
353.15 |
946.71 |
0.4500 |
298.15 |
975.72 |
0.4500 |
303.15 |
971.87 |
0.4500 |
313.15 |
963.92 |
0.4500 |
323.15 |
955.68 |
0.4500 |
333.15 |
947.12 |
0.4500 |
343.15 |
938.27 |
0.4500 |
353.15 |
929.11 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Mass fraction of N,N-Diethyl-2-aminoethanol (1) - Liquid |
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
0.3000 |
298.15 |
987.24 |
0.3000 |
303.15 |
984.1 |
0.3000 |
313.15 |
977.49 |
0.3000 |
323.15 |
970.47 |
0.3000 |
333.15 |
963.06 |
0.3000 |
343.15 |
955.26 |
0.3000 |
353.15 |
947.1 |
0.4000 |
298.15 |
980.18 |
0.4000 |
303.15 |
976.55 |
0.4000 |
313.15 |
969.01 |
0.4000 |
323.15 |
961.13 |
0.4000 |
333.15 |
952.94 |
0.4000 |
343.15 |
944.42 |
0.4000 |
353.15 |
935.57 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of N,N-Diethyl-2-aminoethanol (1) - Liquid |
Mass density, kg/m3 - Liquid |
298.15 |
0.0000 |
997.04 |
313.15 |
0.0000 |
992.22 |
333.15 |
0.0000 |
983.2 |
298.15 |
0.0201 |
993.744 |
313.15 |
0.0201 |
987.552 |
333.15 |
0.0201 |
976.86 |
298.15 |
0.0455 |
990.151 |
313.15 |
0.0455 |
981.577 |
333.15 |
0.0455 |
968.366 |
298.15 |
0.0788 |
983.322 |
313.15 |
0.0788 |
972.648 |
333.15 |
0.0788 |
957.191 |
298.15 |
0.1252 |
971.858 |
313.15 |
0.1252 |
959.656 |
333.15 |
0.1252 |
942.334 |
298.15 |
0.1933 |
961.569 |
313.15 |
0.1933 |
948.632 |
333.15 |
0.1933 |
930.379 |
Surface tension liquid-gas, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mass fraction of N,N-Diethyl-2-aminoethanol (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
303.20 |
0.1000 |
0.0412 |
303.20 |
0.1370 |
0.0401 |
303.20 |
0.2000 |
0.0365 |
303.20 |
0.2130 |
0.0363 |
303.20 |
0.3000 |
0.0349 |
303.20 |
0.4000 |
0.0336 |
303.20 |
0.4830 |
0.0329 |
303.20 |
0.5000 |
0.0327 |
303.20 |
0.5800 |
0.0318 |
303.20 |
0.6000 |
0.0313 |
303.20 |
0.6850 |
0.0307 |
303.20 |
0.7000 |
0.0303 |
303.20 |
0.8000 |
0.0296 |
303.20 |
0.8140 |
0.0295 |
303.20 |
0.9000 |
0.0287 |
303.20 |
0.9100 |
0.0286 |
303.20 |
1.0000 |
0.0277 |
313.20 |
0.1000 |
0.0392 |
313.20 |
0.2000 |
0.0347 |
313.20 |
0.3000 |
0.0332 |
313.20 |
0.4000 |
0.0321 |
313.20 |
0.5000 |
0.0312 |
313.20 |
0.6000 |
0.0298 |
313.20 |
0.7000 |
0.0287 |
313.20 |
0.8000 |
0.0280 |
313.20 |
0.9000 |
0.0273 |
313.20 |
1.0000 |
0.0264 |
323.20 |
0.1000 |
0.0373 |
323.20 |
0.2000 |
0.0331 |
323.20 |
0.3000 |
0.0317 |
323.20 |
0.4000 |
0.0307 |
323.20 |
0.5000 |
0.0299 |
323.20 |
0.6000 |
0.0283 |
323.20 |
0.7000 |
0.0273 |
323.20 |
0.8000 |
0.0266 |
323.20 |
0.9000 |
0.0260 |
323.20 |
1.0000 |
0.0252 |
Surface tension liquid-gas, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of N,N-Diethyl-2-aminoethanol (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
283.15 |
0.0000 |
0.0737 |
283.15 |
0.0010 |
0.0629 |
283.15 |
0.0011 |
0.0628 |
283.15 |
0.0013 |
0.0623 |
283.15 |
0.0034 |
0.0553 |
283.15 |
0.0050 |
0.0540 |
283.15 |
0.0068 |
0.0510 |
283.15 |
0.0237 |
0.0437 |
283.15 |
0.0400 |
0.0391 |
283.15 |
0.0601 |
0.0372 |
283.15 |
0.0728 |
0.0363 |
283.15 |
0.1253 |
0.0348 |
283.15 |
0.1749 |
0.0334 |
283.15 |
0.2503 |
0.0327 |
283.15 |
0.3515 |
0.0319 |
283.15 |
0.4018 |
0.0313 |
283.15 |
0.5038 |
0.0310 |
283.15 |
0.6080 |
0.0306 |
283.15 |
0.7120 |
0.0304 |
283.15 |
0.7503 |
0.0301 |
283.15 |
0.8542 |
0.0297 |
283.15 |
1.0000 |
0.0288 |
288.15 |
0.0000 |
0.0731 |
288.15 |
0.0010 |
0.0621 |
288.15 |
0.0011 |
0.0620 |
288.15 |
0.0013 |
0.0615 |
288.15 |
0.0034 |
0.0543 |
288.15 |
0.0050 |
0.0531 |
288.15 |
0.0068 |
0.0499 |
288.15 |
0.0237 |
0.0426 |
288.15 |
0.0400 |
0.0384 |
288.15 |
0.0601 |
0.0366 |
288.15 |
0.0728 |
0.0358 |
288.15 |
0.1253 |
0.0344 |
288.15 |
0.1749 |
0.0326 |
288.15 |
0.2503 |
0.0322 |
288.15 |
0.3515 |
0.0312 |
288.15 |
0.4018 |
0.0307 |
288.15 |
0.5038 |
0.0306 |
288.15 |
0.6080 |
0.0302 |
288.15 |
0.7120 |
0.0300 |
288.15 |
0.7503 |
0.0297 |
288.15 |
0.8542 |
0.0293 |
288.15 |
1.0000 |
0.0284 |
293.15 |
0.0000 |
0.0726 |
293.15 |
0.0010 |
0.0614 |
293.15 |
0.0011 |
0.0613 |
293.15 |
0.0013 |
0.0606 |
293.15 |
0.0034 |
0.0534 |
293.15 |
0.0050 |
0.0524 |
293.15 |
0.0068 |
0.0486 |
293.15 |
0.0237 |
0.0419 |
293.15 |
0.0400 |
0.0376 |
293.15 |
0.0601 |
0.0360 |
293.15 |
0.0728 |
0.0351 |
293.15 |
0.1253 |
0.0339 |
293.15 |
0.1749 |
0.0322 |
293.15 |
0.2503 |
0.0318 |
293.15 |
0.3515 |
0.0307 |
293.15 |
0.4018 |
0.0302 |
293.15 |
0.5038 |
0.0302 |
293.15 |
0.6080 |
0.0297 |
293.15 |
0.7120 |
0.0297 |
293.15 |
0.7503 |
0.0293 |
293.15 |
0.8542 |
0.0288 |
293.15 |
1.0000 |
0.0280 |
298.15 |
0.0000 |
0.0718 |
298.15 |
0.0010 |
0.0608 |
298.15 |
0.0011 |
0.0607 |
298.15 |
0.0013 |
0.0599 |
298.15 |
0.0034 |
0.0526 |
298.15 |
0.0050 |
0.0514 |
298.15 |
0.0068 |
0.0474 |
298.15 |
0.0237 |
0.0408 |
298.15 |
0.0400 |
0.0369 |
298.15 |
0.0601 |
0.0352 |
298.15 |
0.0728 |
0.0346 |
298.15 |
0.1253 |
0.0332 |
298.15 |
0.1749 |
0.0316 |
298.15 |
0.2503 |
0.0312 |
298.15 |
0.3515 |
0.0302 |
298.15 |
0.4018 |
0.0297 |
298.15 |
0.5038 |
0.0297 |
298.15 |
0.6080 |
0.0292 |
298.15 |
0.7120 |
0.0291 |
298.15 |
0.7503 |
0.0288 |
298.15 |
0.8542 |
0.0284 |
298.15 |
1.0000 |
0.0276 |
303.15 |
0.0000 |
0.0712 |
303.15 |
0.0010 |
0.0601 |
303.15 |
0.0011 |
0.0600 |
303.15 |
0.0013 |
0.0592 |
303.15 |
0.0034 |
0.0519 |
303.15 |
0.0050 |
0.0505 |
303.15 |
0.0068 |
0.0465 |
303.15 |
0.0237 |
0.0399 |
303.15 |
0.0400 |
0.0360 |
303.15 |
0.0601 |
0.0345 |
303.15 |
0.0728 |
0.0339 |
303.15 |
0.1253 |
0.0325 |
303.15 |
0.1749 |
0.0308 |
303.15 |
0.2503 |
0.0308 |
303.15 |
0.3515 |
0.0297 |
303.15 |
0.4018 |
0.0293 |
303.15 |
0.5038 |
0.0292 |
303.15 |
0.6080 |
0.0288 |
303.15 |
0.7120 |
0.0286 |
303.15 |
0.7503 |
0.0283 |
303.15 |
0.8542 |
0.0279 |
303.15 |
1.0000 |
0.0272 |
Surface tension liquid-gas, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mass fraction of N,N-Diethyl-2-aminoethanol (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
303.20 |
0.1000 |
0.0412 |
303.20 |
0.1370 |
0.0401 |
303.20 |
0.2000 |
0.0365 |
303.20 |
0.2130 |
0.0363 |
303.20 |
0.3000 |
0.0349 |
303.20 |
0.4000 |
0.0336 |
303.20 |
0.4830 |
0.0329 |
303.20 |
0.5000 |
0.0327 |
303.20 |
0.5800 |
0.0318 |
303.20 |
0.6000 |
0.0313 |
303.20 |
0.6850 |
0.0307 |
303.20 |
0.7000 |
0.0303 |
303.20 |
0.8000 |
0.0296 |
303.20 |
0.8140 |
0.0295 |
303.20 |
0.9000 |
0.0287 |
303.20 |
0.9100 |
0.0286 |
303.20 |
1.0000 |
0.0277 |
313.20 |
0.1000 |
0.0392 |
313.20 |
0.2000 |
0.0347 |
313.20 |
0.3000 |
0.0332 |
313.20 |
0.4000 |
0.0321 |
313.20 |
0.5000 |
0.0312 |
313.20 |
0.6000 |
0.0298 |
313.20 |
0.7000 |
0.0287 |
313.20 |
0.8000 |
0.0280 |
313.20 |
0.9000 |
0.0273 |
313.20 |
1.0000 |
0.0264 |
323.20 |
0.1000 |
0.0373 |
323.20 |
0.2000 |
0.0331 |
323.20 |
0.3000 |
0.0317 |
323.20 |
0.4000 |
0.0307 |
323.20 |
0.5000 |
0.0299 |
323.20 |
0.6000 |
0.0283 |
323.20 |
0.7000 |
0.0273 |
323.20 |
0.8000 |
0.0266 |
323.20 |
0.9000 |
0.0260 |
323.20 |
1.0000 |
0.0252 |
Surface tension liquid-gas, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of N,N-Diethyl-2-aminoethanol (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
283.15 |
0.0000 |
0.0737 |
283.15 |
0.0010 |
0.0629 |
283.15 |
0.0011 |
0.0628 |
283.15 |
0.0013 |
0.0623 |
283.15 |
0.0034 |
0.0553 |
283.15 |
0.0050 |
0.0540 |
283.15 |
0.0068 |
0.0510 |
283.15 |
0.0237 |
0.0437 |
283.15 |
0.0400 |
0.0391 |
283.15 |
0.0601 |
0.0372 |
283.15 |
0.0728 |
0.0363 |
283.15 |
0.1253 |
0.0348 |
283.15 |
0.1749 |
0.0334 |
283.15 |
0.2503 |
0.0327 |
283.15 |
0.3515 |
0.0319 |
283.15 |
0.4018 |
0.0313 |
283.15 |
0.5038 |
0.0310 |
283.15 |
0.6080 |
0.0306 |
283.15 |
0.7120 |
0.0304 |
283.15 |
0.7503 |
0.0301 |
283.15 |
0.8542 |
0.0297 |
283.15 |
1.0000 |
0.0288 |
288.15 |
0.0000 |
0.0731 |
288.15 |
0.0010 |
0.0621 |
288.15 |
0.0011 |
0.0620 |
288.15 |
0.0013 |
0.0615 |
288.15 |
0.0034 |
0.0543 |
288.15 |
0.0050 |
0.0531 |
288.15 |
0.0068 |
0.0499 |
288.15 |
0.0237 |
0.0426 |
288.15 |
0.0400 |
0.0384 |
288.15 |
0.0601 |
0.0366 |
288.15 |
0.0728 |
0.0358 |
288.15 |
0.1253 |
0.0344 |
288.15 |
0.1749 |
0.0326 |
288.15 |
0.2503 |
0.0322 |
288.15 |
0.3515 |
0.0312 |
288.15 |
0.4018 |
0.0307 |
288.15 |
0.5038 |
0.0306 |
288.15 |
0.6080 |
0.0302 |
288.15 |
0.7120 |
0.0300 |
288.15 |
0.7503 |
0.0297 |
288.15 |
0.8542 |
0.0293 |
288.15 |
1.0000 |
0.0284 |
293.15 |
0.0000 |
0.0726 |
293.15 |
0.0010 |
0.0614 |
293.15 |
0.0011 |
0.0613 |
293.15 |
0.0013 |
0.0606 |
293.15 |
0.0034 |
0.0534 |
293.15 |
0.0050 |
0.0524 |
293.15 |
0.0068 |
0.0486 |
293.15 |
0.0237 |
0.0419 |
293.15 |
0.0400 |
0.0376 |
293.15 |
0.0601 |
0.0360 |
293.15 |
0.0728 |
0.0351 |
293.15 |
0.1253 |
0.0339 |
293.15 |
0.1749 |
0.0322 |
293.15 |
0.2503 |
0.0318 |
293.15 |
0.3515 |
0.0307 |
293.15 |
0.4018 |
0.0302 |
293.15 |
0.5038 |
0.0302 |
293.15 |
0.6080 |
0.0297 |
293.15 |
0.7120 |
0.0297 |
293.15 |
0.7503 |
0.0293 |
293.15 |
0.8542 |
0.0288 |
293.15 |
1.0000 |
0.0280 |
298.15 |
0.0000 |
0.0718 |
298.15 |
0.0010 |
0.0608 |
298.15 |
0.0011 |
0.0607 |
298.15 |
0.0013 |
0.0599 |
298.15 |
0.0034 |
0.0526 |
298.15 |
0.0050 |
0.0514 |
298.15 |
0.0068 |
0.0474 |
298.15 |
0.0237 |
0.0408 |
298.15 |
0.0400 |
0.0369 |
298.15 |
0.0601 |
0.0352 |
298.15 |
0.0728 |
0.0346 |
298.15 |
0.1253 |
0.0332 |
298.15 |
0.1749 |
0.0316 |
298.15 |
0.2503 |
0.0312 |
298.15 |
0.3515 |
0.0302 |
298.15 |
0.4018 |
0.0297 |
298.15 |
0.5038 |
0.0297 |
298.15 |
0.6080 |
0.0292 |
298.15 |
0.7120 |
0.0291 |
298.15 |
0.7503 |
0.0288 |
298.15 |
0.8542 |
0.0284 |
298.15 |
1.0000 |
0.0276 |
303.15 |
0.0000 |
0.0712 |
303.15 |
0.0010 |
0.0601 |
303.15 |
0.0011 |
0.0600 |
303.15 |
0.0013 |
0.0592 |
303.15 |
0.0034 |
0.0519 |
303.15 |
0.0050 |
0.0505 |
303.15 |
0.0068 |
0.0465 |
303.15 |
0.0237 |
0.0399 |
303.15 |
0.0400 |
0.0360 |
303.15 |
0.0601 |
0.0345 |
303.15 |
0.0728 |
0.0339 |
303.15 |
0.1253 |
0.0325 |
303.15 |
0.1749 |
0.0308 |
303.15 |
0.2503 |
0.0308 |
303.15 |
0.3515 |
0.0297 |
303.15 |
0.4018 |
0.0293 |
303.15 |
0.5038 |
0.0292 |
303.15 |
0.6080 |
0.0288 |
303.15 |
0.7120 |
0.0286 |
303.15 |
0.7503 |
0.0283 |
303.15 |
0.8542 |
0.0279 |
303.15 |
1.0000 |
0.0272 |
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Mass fraction of N,N-Diethyl-2-aminoethanol (1) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
0.0254 |
272.71 |
0.0505 |
272.28 |
0.0754 |
271.84 |
0.1001 |
271.35 |
0.1255 |
270.79 |
0.1505 |
270.21 |
0.1751 |
269.54 |
0.2006 |
268.80 |
0.2254 |
268.01 |
0.2501 |
267.09 |
0.2755 |
266.09 |
0.3002 |
265.14 |
0.3253 |
264.05 |
0.3501 |
263.01 |
0.3752 |
261.80 |
0.4003 |
260.55 |
0.4499 |
257.64 |
0.4999 |
253.91 |
0.5501 |
248.56 |
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Mass fraction of N,N-Diethyl-2-aminoethanol (1) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
0.0254 |
272.71 |
0.0505 |
272.28 |
0.0754 |
271.84 |
0.1001 |
271.35 |
0.1255 |
270.79 |
0.1505 |
270.21 |
0.1751 |
269.54 |
0.2006 |
268.80 |
0.2254 |
268.01 |
0.2501 |
267.09 |
0.2755 |
266.09 |
0.3002 |
265.14 |
0.3253 |
264.05 |
0.3501 |
263.01 |
0.3752 |
261.80 |
0.4003 |
260.55 |
0.4499 |
257.64 |
0.4999 |
253.91 |
0.5501 |
248.56 |
Binary diffusion coefficient, m2/s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of N,N-Diethyl-2-aminoethanol (1) - Liquid |
Binary diffusion coefficient, m2/s - Liquid |
298.15 |
0.0043 |
0.0000 |
298.15 |
0.0143 |
0.0000 |
298.15 |
0.0352 |
0.0000 |
298.15 |
0.0509 |
0.0000 |
298.15 |
0.0512 |
0.0000 |
298.15 |
0.0701 |
0.0000 |
298.15 |
0.0971 |
0.0000 |
298.15 |
0.1004 |
0.0000 |
298.15 |
0.1467 |
0.0000 |
303.15 |
0.0028 |
0.0000 |
303.15 |
0.0052 |
0.0000 |
303.15 |
0.0078 |
0.0000 |
303.15 |
0.0103 |
0.0000 |
303.15 |
0.0128 |
0.0000 |
303.15 |
0.0154 |
0.0000 |
303.15 |
0.0178 |
0.0000 |
303.15 |
0.0203 |
0.0000 |
303.15 |
0.0273 |
0.0000 |
303.15 |
0.0382 |
0.0000 |
303.15 |
0.0502 |
0.0000 |
303.15 |
0.0736 |
0.0000 |
303.15 |
0.0985 |
0.0000 |
303.15 |
0.1247 |
0.0000 |
303.15 |
0.1476 |
0.0000 |
303.15 |
0.1801 |
0.0000 |
Binary diffusion coefficient, m2/s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of N,N-Diethyl-2-aminoethanol (1) - Liquid |
Binary diffusion coefficient, m2/s - Liquid |
298.15 |
0.0043 |
0.0000 |
298.15 |
0.0143 |
0.0000 |
298.15 |
0.0352 |
0.0000 |
298.15 |
0.0509 |
0.0000 |
298.15 |
0.0512 |
0.0000 |
298.15 |
0.0701 |
0.0000 |
298.15 |
0.0971 |
0.0000 |
298.15 |
0.1004 |
0.0000 |
298.15 |
0.1467 |
0.0000 |
303.15 |
0.0028 |
0.0000 |
303.15 |
0.0052 |
0.0000 |
303.15 |
0.0078 |
0.0000 |
303.15 |
0.0103 |
0.0000 |
303.15 |
0.0128 |
0.0000 |
303.15 |
0.0154 |
0.0000 |
303.15 |
0.0178 |
0.0000 |
303.15 |
0.0203 |
0.0000 |
303.15 |
0.0273 |
0.0000 |
303.15 |
0.0382 |
0.0000 |
303.15 |
0.0502 |
0.0000 |
303.15 |
0.0736 |
0.0000 |
303.15 |
0.0985 |
0.0000 |
303.15 |
0.1247 |
0.0000 |
303.15 |
0.1476 |
0.0000 |
303.15 |
0.1801 |
0.0000 |
Sources