Datasets
-
Mass fraction (8)
-
Cp,liquid - Molar heat capacity at constant pressure, J/K/mol (2)
-
η - Viscosity, Pa*s (8)
-
Excess molar enthalpy (molar enthalpy (4)
-
n0 - Refractive index (Na D-line) (2)
-
ρl - Mass density, kg/m3 (18)
-
csound,fluid - Speed of Sound, m/s (12)
-
Tboil - Boiling temperature at pressure P, K (2)
-
λ - Thermal conductivity, W/m/K (2)
-
Binary diffusion coefficient, m2/s (4)
Mass fraction of Ethanol, 2,2'-oxybis- (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Mass fraction of Ethanol, 2,2'-oxybis- (1) - Liquid mixture 1 |
280.25 |
0.9696 |
293.75 |
0.9568 |
302.65 |
0.9536 |
310.55 |
0.9469 |
320.95 |
0.9429 |
329.85 |
0.9376 |
340.00 |
0.9259 |
301.35 |
0.9565 |
Mass fraction of Ethanol, 2,2'-oxybis- (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Mass fraction of Ethanol, 2,2'-oxybis- (1) - Liquid mixture 2 |
280.25 |
0.3192 |
293.75 |
0.3193 |
302.65 |
0.3157 |
310.55 |
0.3158 |
320.95 |
0.3185 |
329.85 |
0.3276 |
340.00 |
0.3494 |
301.35 |
0.3164 |
Mass fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
100 (Liquid mixture 2)
Temperature, K - Liquid mixture 2 |
Mass fraction of Water (2) - Liquid mixture 1 |
293.15 |
0.6783 |
308.15 |
0.6869 |
308.15 |
0.6821 |
293.15 |
0.6770 |
Mass fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
100 (Liquid mixture 2)
Temperature, K - Liquid mixture 2 |
Mass fraction of Water (2) - Liquid mixture 2 |
293.15 |
0.0428 |
308.15 |
0.0542 |
308.15 |
0.0539 |
293.15 |
0.0430 |
Mass fraction of Ethanol, 2,2'-oxybis- (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Mass fraction of Ethanol, 2,2'-oxybis- (1) - Liquid mixture 1 |
280.25 |
0.9696 |
293.75 |
0.9568 |
302.65 |
0.9536 |
310.55 |
0.9469 |
320.95 |
0.9429 |
329.85 |
0.9376 |
340.00 |
0.9259 |
301.35 |
0.9565 |
Mass fraction of Ethanol, 2,2'-oxybis- (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Mass fraction of Ethanol, 2,2'-oxybis- (1) - Liquid mixture 2 |
280.25 |
0.3192 |
293.75 |
0.3193 |
302.65 |
0.3157 |
310.55 |
0.3158 |
320.95 |
0.3185 |
329.85 |
0.3276 |
340.00 |
0.3494 |
301.35 |
0.3164 |
Mass fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
100 (Liquid mixture 2)
Temperature, K - Liquid mixture 2 |
Mass fraction of Water (2) - Liquid mixture 1 |
293.15 |
0.6783 |
308.15 |
0.6869 |
308.15 |
0.6821 |
293.15 |
0.6770 |
Mass fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
100 (Liquid mixture 2)
Temperature, K - Liquid mixture 2 |
Mass fraction of Water (2) - Liquid mixture 2 |
293.15 |
0.0428 |
308.15 |
0.0542 |
308.15 |
0.0539 |
293.15 |
0.0430 |
Molar heat capacity at constant pressure, J/K/mol
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid |
Temperature, K - Liquid |
Molar heat capacity at constant pressure, J/K/mol - Liquid |
0.2000 |
303.15 |
111.80 |
0.2000 |
313.15 |
113.50 |
0.2000 |
323.15 |
115.30 |
0.2000 |
333.15 |
117.40 |
0.2000 |
343.15 |
119.30 |
0.2000 |
353.15 |
121.70 |
0.4000 |
303.15 |
148.70 |
0.4000 |
313.15 |
150.70 |
0.4000 |
323.15 |
153.30 |
0.4000 |
333.15 |
155.90 |
0.4000 |
343.15 |
158.70 |
0.4000 |
353.15 |
161.80 |
0.5000 |
303.15 |
167.60 |
0.5000 |
313.15 |
169.90 |
0.5000 |
323.15 |
172.60 |
0.5000 |
333.15 |
175.50 |
0.5000 |
343.15 |
178.70 |
0.5000 |
353.15 |
182.20 |
0.6000 |
303.15 |
184.50 |
0.6000 |
313.15 |
187.10 |
0.6000 |
323.15 |
190.30 |
0.6000 |
333.15 |
193.60 |
0.6000 |
343.15 |
197.30 |
0.6000 |
353.15 |
201.20 |
0.8000 |
303.15 |
217.90 |
0.8000 |
313.15 |
221.20 |
0.8000 |
323.15 |
225.00 |
0.8000 |
333.15 |
229.10 |
0.8000 |
343.15 |
233.60 |
0.8000 |
353.15 |
238.50 |
Molar heat capacity at constant pressure, J/K/mol
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid |
Temperature, K - Liquid |
Molar heat capacity at constant pressure, J/K/mol - Liquid |
0.2000 |
303.15 |
111.80 |
0.2000 |
313.15 |
113.50 |
0.2000 |
323.15 |
115.30 |
0.2000 |
333.15 |
117.40 |
0.2000 |
343.15 |
119.30 |
0.2000 |
353.15 |
121.70 |
0.4000 |
303.15 |
148.70 |
0.4000 |
313.15 |
150.70 |
0.4000 |
323.15 |
153.30 |
0.4000 |
333.15 |
155.90 |
0.4000 |
343.15 |
158.70 |
0.4000 |
353.15 |
161.80 |
0.5000 |
303.15 |
167.60 |
0.5000 |
313.15 |
169.90 |
0.5000 |
323.15 |
172.60 |
0.5000 |
333.15 |
175.50 |
0.5000 |
343.15 |
178.70 |
0.5000 |
353.15 |
182.20 |
0.6000 |
303.15 |
184.50 |
0.6000 |
313.15 |
187.10 |
0.6000 |
323.15 |
190.30 |
0.6000 |
333.15 |
193.60 |
0.6000 |
343.15 |
197.30 |
0.6000 |
353.15 |
201.20 |
0.8000 |
303.15 |
217.90 |
0.8000 |
313.15 |
221.20 |
0.8000 |
323.15 |
225.00 |
0.8000 |
333.15 |
229.10 |
0.8000 |
343.15 |
233.60 |
0.8000 |
353.15 |
238.50 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
92.3 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid |
Viscosity, Pa*s - Liquid |
293.15 |
0.0490 |
0.0021 |
293.15 |
0.0992 |
0.0036 |
293.15 |
0.1490 |
0.0055 |
293.15 |
0.1998 |
0.0077 |
293.15 |
0.2490 |
0.0100 |
293.15 |
0.2987 |
0.0125 |
293.15 |
0.3501 |
0.0152 |
293.15 |
0.4007 |
0.0177 |
293.15 |
0.4504 |
0.0201 |
293.15 |
0.4973 |
0.0223 |
293.15 |
0.5530 |
0.0247 |
293.15 |
0.5938 |
0.0262 |
293.15 |
0.6514 |
0.0283 |
293.15 |
0.6864 |
0.0295 |
293.15 |
0.7556 |
0.0314 |
293.15 |
0.7999 |
0.0324 |
293.15 |
0.8525 |
0.0335 |
293.15 |
0.9002 |
0.0344 |
293.15 |
0.9554 |
0.0353 |
298.15 |
0.0490 |
0.0017 |
298.15 |
0.0992 |
0.0029 |
298.15 |
0.1490 |
0.0043 |
298.15 |
0.1998 |
0.0060 |
298.15 |
0.2490 |
0.0078 |
298.15 |
0.2987 |
0.0098 |
298.15 |
0.3501 |
0.0118 |
298.15 |
0.4007 |
0.0137 |
298.15 |
0.4504 |
0.0156 |
298.15 |
0.4973 |
0.0172 |
298.15 |
0.5530 |
0.0191 |
298.15 |
0.5938 |
0.0202 |
298.15 |
0.6514 |
0.0219 |
298.15 |
0.6864 |
0.0227 |
298.15 |
0.7556 |
0.0242 |
298.15 |
0.7999 |
0.0249 |
298.15 |
0.8525 |
0.0258 |
298.15 |
0.9002 |
0.0265 |
298.15 |
0.9554 |
0.0272 |
303.15 |
0.0490 |
0.0016 |
303.15 |
0.0992 |
0.0026 |
303.15 |
0.1490 |
0.0038 |
303.15 |
0.1998 |
0.0053 |
303.15 |
0.2490 |
0.0068 |
303.15 |
0.2987 |
0.0083 |
303.15 |
0.3501 |
0.0100 |
303.15 |
0.4007 |
0.0115 |
303.15 |
0.4504 |
0.0130 |
303.15 |
0.4973 |
0.0143 |
303.15 |
0.5530 |
0.0157 |
303.15 |
0.5938 |
0.0166 |
303.15 |
0.6514 |
0.0179 |
303.15 |
0.6864 |
0.0186 |
303.15 |
0.7556 |
0.0197 |
303.15 |
0.7999 |
0.0203 |
303.15 |
0.8525 |
0.0210 |
303.15 |
0.9002 |
0.0216 |
303.15 |
0.9554 |
0.0221 |
308.15 |
0.0490 |
0.0014 |
308.15 |
0.0992 |
0.0023 |
308.15 |
0.1490 |
0.0033 |
308.15 |
0.1998 |
0.0045 |
308.15 |
0.2490 |
0.0058 |
308.15 |
0.2987 |
0.0071 |
308.15 |
0.3501 |
0.0084 |
308.15 |
0.4007 |
0.0096 |
308.15 |
0.4504 |
0.0108 |
308.15 |
0.4973 |
0.0118 |
308.15 |
0.5530 |
0.0129 |
308.15 |
0.5938 |
0.0137 |
308.15 |
0.6514 |
0.0147 |
308.15 |
0.6864 |
0.0152 |
308.15 |
0.7556 |
0.0161 |
308.15 |
0.7999 |
0.0166 |
308.15 |
0.8525 |
0.0171 |
308.15 |
0.9002 |
0.0175 |
308.15 |
0.9554 |
0.0179 |
293.15 |
0.0000 |
0.0011 |
298.15 |
0.0000 |
0.0009 |
303.15 |
0.0000 |
0.0008 |
308.15 |
0.0000 |
0.0008 |
293.15 |
1.0000 |
0.0359 |
298.15 |
1.0000 |
0.0277 |
303.15 |
1.0000 |
0.0225 |
308.15 |
1.0000 |
0.0183 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid |
Temperature, K - Liquid |
Viscosity, Pa*s - Liquid |
0.2500 |
294.25 |
0.0098 |
0.2500 |
313.05 |
0.0049 |
0.2500 |
333.05 |
0.0028 |
0.2500 |
353.15 |
0.0018 |
0.2500 |
384.95 |
0.0010 |
0.2500 |
396.75 |
0.0009 |
0.2500 |
413.25 |
0.0007 |
0.2500 |
430.35 |
0.0006 |
0.2500 |
445.65 |
0.0005 |
0.5000 |
293.45 |
0.0220 |
0.5000 |
312.95 |
0.0096 |
0.5000 |
332.95 |
0.0050 |
0.5000 |
352.95 |
0.0030 |
0.5000 |
382.55 |
0.0017 |
0.5000 |
394.25 |
0.0014 |
0.5000 |
409.35 |
0.0011 |
0.5000 |
428.25 |
0.0009 |
0.5000 |
447.05 |
0.0007 |
0.7500 |
294.05 |
0.0304 |
0.7500 |
313.05 |
0.0133 |
0.7500 |
333.05 |
0.0067 |
0.7500 |
353.05 |
0.0039 |
0.7500 |
385.05 |
0.0020 |
0.7500 |
394.95 |
0.0017 |
0.7500 |
410.95 |
0.0014 |
0.7500 |
428.65 |
0.0010 |
0.7500 |
447.65 |
0.0008 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid |
Viscosity, Pa*s - Liquid |
303.15 |
0.0000 |
0.0008 |
303.15 |
0.0501 |
0.0016 |
303.15 |
0.1016 |
0.0026 |
303.15 |
0.1512 |
0.0038 |
303.15 |
0.2012 |
0.0053 |
303.15 |
0.2477 |
0.0067 |
303.15 |
0.2980 |
0.0083 |
303.15 |
0.3505 |
0.0099 |
303.15 |
0.4483 |
0.0125 |
303.15 |
0.5421 |
0.0151 |
303.15 |
0.6518 |
0.0175 |
303.15 |
0.7525 |
0.0193 |
303.15 |
0.7864 |
0.0199 |
303.15 |
0.8499 |
0.0206 |
303.15 |
0.9005 |
0.0213 |
303.15 |
0.9503 |
0.0217 |
303.15 |
1.0000 |
0.0222 |
308.15 |
0.0000 |
0.0007 |
308.15 |
0.0501 |
0.0014 |
308.15 |
0.1016 |
0.0022 |
308.15 |
0.1512 |
0.0033 |
308.15 |
0.2012 |
0.0044 |
308.15 |
0.2477 |
0.0056 |
308.15 |
0.2980 |
0.0069 |
308.15 |
0.3505 |
0.0082 |
308.15 |
0.4483 |
0.0103 |
308.15 |
0.5421 |
0.0123 |
308.15 |
0.6518 |
0.0141 |
308.15 |
0.7525 |
0.0156 |
308.15 |
0.7864 |
0.0161 |
308.15 |
0.8499 |
0.0167 |
308.15 |
0.9005 |
0.0172 |
308.15 |
0.9503 |
0.0175 |
308.15 |
1.0000 |
0.0179 |
313.15 |
0.0000 |
0.0007 |
313.15 |
0.0501 |
0.0012 |
313.15 |
0.1016 |
0.0020 |
313.15 |
0.1512 |
0.0028 |
313.15 |
0.2012 |
0.0038 |
313.15 |
0.2477 |
0.0047 |
313.15 |
0.2980 |
0.0058 |
313.15 |
0.3505 |
0.0068 |
313.15 |
0.4483 |
0.0085 |
313.15 |
0.5421 |
0.0101 |
313.15 |
0.6518 |
0.0116 |
313.15 |
0.7525 |
0.0128 |
313.15 |
0.7864 |
0.0132 |
313.15 |
0.8499 |
0.0137 |
313.15 |
0.9005 |
0.0141 |
313.15 |
0.9503 |
0.0144 |
313.15 |
1.0000 |
0.0147 |
318.15 |
0.0000 |
0.0006 |
318.15 |
0.0501 |
0.0011 |
318.15 |
0.1016 |
0.0017 |
318.15 |
0.1512 |
0.0025 |
318.15 |
0.2012 |
0.0033 |
318.15 |
0.2477 |
0.0041 |
318.15 |
0.2980 |
0.0050 |
318.15 |
0.3505 |
0.0058 |
318.15 |
0.4483 |
0.0071 |
318.15 |
0.5421 |
0.0085 |
318.15 |
0.6518 |
0.0097 |
318.15 |
0.7525 |
0.0106 |
318.15 |
0.7864 |
0.0110 |
318.15 |
0.8499 |
0.0114 |
318.15 |
0.9005 |
0.0117 |
318.15 |
0.9503 |
0.0119 |
318.15 |
1.0000 |
0.0122 |
323.15 |
0.0000 |
0.0005 |
323.15 |
0.0501 |
0.0010 |
323.15 |
0.1016 |
0.0015 |
323.15 |
0.1512 |
0.0022 |
323.15 |
0.2012 |
0.0028 |
323.15 |
0.2477 |
0.0035 |
323.15 |
0.2980 |
0.0043 |
323.15 |
0.3505 |
0.0049 |
323.15 |
0.4483 |
0.0061 |
323.15 |
0.5421 |
0.0071 |
323.15 |
0.6518 |
0.0081 |
323.15 |
0.7525 |
0.0089 |
323.15 |
0.7864 |
0.0092 |
323.15 |
0.8499 |
0.0095 |
323.15 |
0.9005 |
0.0098 |
323.15 |
0.9503 |
0.0100 |
323.15 |
1.0000 |
0.0102 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid |
Viscosity, Pa*s - Liquid |
293.15 |
0.0000 |
0.0010 |
293.15 |
0.0255 |
0.0014 |
293.15 |
0.0565 |
0.0022 |
293.15 |
0.1027 |
0.0036 |
293.15 |
0.1966 |
0.0075 |
293.15 |
0.3010 |
0.0126 |
293.15 |
0.3989 |
0.0175 |
293.15 |
0.5006 |
0.0222 |
293.15 |
0.6011 |
0.0260 |
293.15 |
0.7003 |
0.0295 |
293.15 |
0.8051 |
0.0323 |
293.15 |
0.8920 |
0.0340 |
293.15 |
1.0000 |
0.0364 |
303.15 |
0.0000 |
0.0008 |
303.15 |
0.0255 |
0.0011 |
303.15 |
0.0565 |
0.0017 |
303.15 |
0.1027 |
0.0026 |
303.15 |
0.1966 |
0.0051 |
303.15 |
0.3010 |
0.0084 |
303.15 |
0.3989 |
0.0114 |
303.15 |
0.5006 |
0.0141 |
303.15 |
0.6011 |
0.0163 |
303.15 |
0.7003 |
0.0185 |
303.15 |
0.8051 |
0.0200 |
303.15 |
0.8920 |
0.0212 |
303.15 |
1.0000 |
0.0221 |
313.15 |
0.0000 |
0.0007 |
313.15 |
0.0255 |
0.0010 |
313.15 |
0.0565 |
0.0013 |
313.15 |
0.1027 |
0.0020 |
313.15 |
0.1966 |
0.0037 |
313.15 |
0.3010 |
0.0058 |
313.15 |
0.3989 |
0.0078 |
313.15 |
0.5006 |
0.0095 |
313.15 |
0.6011 |
0.0109 |
313.15 |
0.7003 |
0.0122 |
313.15 |
0.8051 |
0.0132 |
313.15 |
0.8920 |
0.0139 |
313.15 |
1.0000 |
0.0146 |
323.15 |
0.0000 |
0.0006 |
323.15 |
0.0255 |
0.0008 |
323.15 |
0.0565 |
0.0010 |
323.15 |
0.1027 |
0.0015 |
323.15 |
0.1966 |
0.0028 |
323.15 |
0.3010 |
0.0042 |
323.15 |
0.3989 |
0.0055 |
323.15 |
0.5006 |
0.0067 |
323.15 |
0.6011 |
0.0076 |
323.15 |
0.7003 |
0.0085 |
323.15 |
0.8051 |
0.0091 |
323.15 |
0.8920 |
0.0096 |
323.15 |
1.0000 |
0.0100 |
333.15 |
0.0000 |
0.0005 |
333.15 |
0.0255 |
0.0006 |
333.15 |
0.0565 |
0.0008 |
333.15 |
0.1027 |
0.0012 |
333.15 |
0.1966 |
0.0021 |
333.15 |
0.3010 |
0.0032 |
333.15 |
0.3989 |
0.0041 |
333.15 |
0.5006 |
0.0049 |
333.15 |
0.6011 |
0.0055 |
333.15 |
0.7003 |
0.0061 |
333.15 |
0.8051 |
0.0065 |
333.15 |
0.8920 |
0.0069 |
333.15 |
1.0000 |
0.0072 |
343.15 |
0.0000 |
0.0004 |
343.15 |
0.0255 |
0.0005 |
343.15 |
0.0565 |
0.0007 |
343.15 |
0.1027 |
0.0010 |
343.15 |
0.1966 |
0.0017 |
343.15 |
0.3010 |
0.0025 |
343.15 |
0.3989 |
0.0032 |
343.15 |
0.5006 |
0.0037 |
343.15 |
0.6011 |
0.0042 |
343.15 |
0.7003 |
0.0046 |
343.15 |
0.8051 |
0.0049 |
343.15 |
0.8920 |
0.0051 |
343.15 |
1.0000 |
0.0054 |
353.15 |
0.0000 |
0.0004 |
353.15 |
0.0255 |
0.0005 |
353.15 |
0.0565 |
0.0006 |
353.15 |
0.1027 |
0.0008 |
353.15 |
0.1966 |
0.0014 |
353.15 |
0.3010 |
0.0020 |
353.15 |
0.3989 |
0.0025 |
353.15 |
0.5006 |
0.0029 |
353.15 |
0.6011 |
0.0033 |
353.15 |
0.7003 |
0.0036 |
353.15 |
0.8051 |
0.0038 |
353.15 |
0.8920 |
0.0040 |
353.15 |
1.0000 |
0.0041 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
92.3 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid |
Viscosity, Pa*s - Liquid |
293.15 |
0.0490 |
0.0021 |
293.15 |
0.0992 |
0.0036 |
293.15 |
0.1490 |
0.0055 |
293.15 |
0.1998 |
0.0077 |
293.15 |
0.2490 |
0.0100 |
293.15 |
0.2987 |
0.0125 |
293.15 |
0.3501 |
0.0152 |
293.15 |
0.4007 |
0.0177 |
293.15 |
0.4504 |
0.0201 |
293.15 |
0.4973 |
0.0223 |
293.15 |
0.5530 |
0.0247 |
293.15 |
0.5938 |
0.0262 |
293.15 |
0.6514 |
0.0283 |
293.15 |
0.6864 |
0.0295 |
293.15 |
0.7556 |
0.0314 |
293.15 |
0.7999 |
0.0324 |
293.15 |
0.8525 |
0.0335 |
293.15 |
0.9002 |
0.0344 |
293.15 |
0.9554 |
0.0353 |
298.15 |
0.0490 |
0.0017 |
298.15 |
0.0992 |
0.0029 |
298.15 |
0.1490 |
0.0043 |
298.15 |
0.1998 |
0.0060 |
298.15 |
0.2490 |
0.0078 |
298.15 |
0.2987 |
0.0098 |
298.15 |
0.3501 |
0.0118 |
298.15 |
0.4007 |
0.0137 |
298.15 |
0.4504 |
0.0156 |
298.15 |
0.4973 |
0.0172 |
298.15 |
0.5530 |
0.0191 |
298.15 |
0.5938 |
0.0202 |
298.15 |
0.6514 |
0.0219 |
298.15 |
0.6864 |
0.0227 |
298.15 |
0.7556 |
0.0242 |
298.15 |
0.7999 |
0.0249 |
298.15 |
0.8525 |
0.0258 |
298.15 |
0.9002 |
0.0265 |
298.15 |
0.9554 |
0.0272 |
303.15 |
0.0490 |
0.0016 |
303.15 |
0.0992 |
0.0026 |
303.15 |
0.1490 |
0.0038 |
303.15 |
0.1998 |
0.0053 |
303.15 |
0.2490 |
0.0068 |
303.15 |
0.2987 |
0.0083 |
303.15 |
0.3501 |
0.0100 |
303.15 |
0.4007 |
0.0115 |
303.15 |
0.4504 |
0.0130 |
303.15 |
0.4973 |
0.0143 |
303.15 |
0.5530 |
0.0157 |
303.15 |
0.5938 |
0.0166 |
303.15 |
0.6514 |
0.0179 |
303.15 |
0.6864 |
0.0186 |
303.15 |
0.7556 |
0.0197 |
303.15 |
0.7999 |
0.0203 |
303.15 |
0.8525 |
0.0210 |
303.15 |
0.9002 |
0.0216 |
303.15 |
0.9554 |
0.0221 |
308.15 |
0.0490 |
0.0014 |
308.15 |
0.0992 |
0.0023 |
308.15 |
0.1490 |
0.0033 |
308.15 |
0.1998 |
0.0045 |
308.15 |
0.2490 |
0.0058 |
308.15 |
0.2987 |
0.0071 |
308.15 |
0.3501 |
0.0084 |
308.15 |
0.4007 |
0.0096 |
308.15 |
0.4504 |
0.0108 |
308.15 |
0.4973 |
0.0118 |
308.15 |
0.5530 |
0.0129 |
308.15 |
0.5938 |
0.0137 |
308.15 |
0.6514 |
0.0147 |
308.15 |
0.6864 |
0.0152 |
308.15 |
0.7556 |
0.0161 |
308.15 |
0.7999 |
0.0166 |
308.15 |
0.8525 |
0.0171 |
308.15 |
0.9002 |
0.0175 |
308.15 |
0.9554 |
0.0179 |
293.15 |
0.0000 |
0.0011 |
298.15 |
0.0000 |
0.0009 |
303.15 |
0.0000 |
0.0008 |
308.15 |
0.0000 |
0.0008 |
293.15 |
1.0000 |
0.0359 |
298.15 |
1.0000 |
0.0277 |
303.15 |
1.0000 |
0.0225 |
308.15 |
1.0000 |
0.0183 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid |
Temperature, K - Liquid |
Viscosity, Pa*s - Liquid |
0.2500 |
294.25 |
0.0098 |
0.2500 |
313.05 |
0.0049 |
0.2500 |
333.05 |
0.0028 |
0.2500 |
353.15 |
0.0018 |
0.2500 |
384.95 |
0.0010 |
0.2500 |
396.75 |
0.0009 |
0.2500 |
413.25 |
0.0007 |
0.2500 |
430.35 |
0.0006 |
0.2500 |
445.65 |
0.0005 |
0.5000 |
293.45 |
0.0220 |
0.5000 |
312.95 |
0.0096 |
0.5000 |
332.95 |
0.0050 |
0.5000 |
352.95 |
0.0030 |
0.5000 |
382.55 |
0.0017 |
0.5000 |
394.25 |
0.0014 |
0.5000 |
409.35 |
0.0011 |
0.5000 |
428.25 |
0.0009 |
0.5000 |
447.05 |
0.0007 |
0.7500 |
294.05 |
0.0304 |
0.7500 |
313.05 |
0.0133 |
0.7500 |
333.05 |
0.0067 |
0.7500 |
353.05 |
0.0039 |
0.7500 |
385.05 |
0.0020 |
0.7500 |
394.95 |
0.0017 |
0.7500 |
410.95 |
0.0014 |
0.7500 |
428.65 |
0.0010 |
0.7500 |
447.65 |
0.0008 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid |
Viscosity, Pa*s - Liquid |
303.15 |
0.0000 |
0.0008 |
303.15 |
0.0501 |
0.0016 |
303.15 |
0.1016 |
0.0026 |
303.15 |
0.1512 |
0.0038 |
303.15 |
0.2012 |
0.0053 |
303.15 |
0.2477 |
0.0067 |
303.15 |
0.2980 |
0.0083 |
303.15 |
0.3505 |
0.0099 |
303.15 |
0.4483 |
0.0125 |
303.15 |
0.5421 |
0.0151 |
303.15 |
0.6518 |
0.0175 |
303.15 |
0.7525 |
0.0193 |
303.15 |
0.7864 |
0.0199 |
303.15 |
0.8499 |
0.0206 |
303.15 |
0.9005 |
0.0213 |
303.15 |
0.9503 |
0.0217 |
303.15 |
1.0000 |
0.0222 |
308.15 |
0.0000 |
0.0007 |
308.15 |
0.0501 |
0.0014 |
308.15 |
0.1016 |
0.0022 |
308.15 |
0.1512 |
0.0033 |
308.15 |
0.2012 |
0.0044 |
308.15 |
0.2477 |
0.0056 |
308.15 |
0.2980 |
0.0069 |
308.15 |
0.3505 |
0.0082 |
308.15 |
0.4483 |
0.0103 |
308.15 |
0.5421 |
0.0123 |
308.15 |
0.6518 |
0.0141 |
308.15 |
0.7525 |
0.0156 |
308.15 |
0.7864 |
0.0161 |
308.15 |
0.8499 |
0.0167 |
308.15 |
0.9005 |
0.0172 |
308.15 |
0.9503 |
0.0175 |
308.15 |
1.0000 |
0.0179 |
313.15 |
0.0000 |
0.0007 |
313.15 |
0.0501 |
0.0012 |
313.15 |
0.1016 |
0.0020 |
313.15 |
0.1512 |
0.0028 |
313.15 |
0.2012 |
0.0038 |
313.15 |
0.2477 |
0.0047 |
313.15 |
0.2980 |
0.0058 |
313.15 |
0.3505 |
0.0068 |
313.15 |
0.4483 |
0.0085 |
313.15 |
0.5421 |
0.0101 |
313.15 |
0.6518 |
0.0116 |
313.15 |
0.7525 |
0.0128 |
313.15 |
0.7864 |
0.0132 |
313.15 |
0.8499 |
0.0137 |
313.15 |
0.9005 |
0.0141 |
313.15 |
0.9503 |
0.0144 |
313.15 |
1.0000 |
0.0147 |
318.15 |
0.0000 |
0.0006 |
318.15 |
0.0501 |
0.0011 |
318.15 |
0.1016 |
0.0017 |
318.15 |
0.1512 |
0.0025 |
318.15 |
0.2012 |
0.0033 |
318.15 |
0.2477 |
0.0041 |
318.15 |
0.2980 |
0.0050 |
318.15 |
0.3505 |
0.0058 |
318.15 |
0.4483 |
0.0071 |
318.15 |
0.5421 |
0.0085 |
318.15 |
0.6518 |
0.0097 |
318.15 |
0.7525 |
0.0106 |
318.15 |
0.7864 |
0.0110 |
318.15 |
0.8499 |
0.0114 |
318.15 |
0.9005 |
0.0117 |
318.15 |
0.9503 |
0.0119 |
318.15 |
1.0000 |
0.0122 |
323.15 |
0.0000 |
0.0005 |
323.15 |
0.0501 |
0.0010 |
323.15 |
0.1016 |
0.0015 |
323.15 |
0.1512 |
0.0022 |
323.15 |
0.2012 |
0.0028 |
323.15 |
0.2477 |
0.0035 |
323.15 |
0.2980 |
0.0043 |
323.15 |
0.3505 |
0.0049 |
323.15 |
0.4483 |
0.0061 |
323.15 |
0.5421 |
0.0071 |
323.15 |
0.6518 |
0.0081 |
323.15 |
0.7525 |
0.0089 |
323.15 |
0.7864 |
0.0092 |
323.15 |
0.8499 |
0.0095 |
323.15 |
0.9005 |
0.0098 |
323.15 |
0.9503 |
0.0100 |
323.15 |
1.0000 |
0.0102 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid |
Viscosity, Pa*s - Liquid |
293.15 |
0.0000 |
0.0010 |
293.15 |
0.0255 |
0.0014 |
293.15 |
0.0565 |
0.0022 |
293.15 |
0.1027 |
0.0036 |
293.15 |
0.1966 |
0.0075 |
293.15 |
0.3010 |
0.0126 |
293.15 |
0.3989 |
0.0175 |
293.15 |
0.5006 |
0.0222 |
293.15 |
0.6011 |
0.0260 |
293.15 |
0.7003 |
0.0295 |
293.15 |
0.8051 |
0.0323 |
293.15 |
0.8920 |
0.0340 |
293.15 |
1.0000 |
0.0364 |
303.15 |
0.0000 |
0.0008 |
303.15 |
0.0255 |
0.0011 |
303.15 |
0.0565 |
0.0017 |
303.15 |
0.1027 |
0.0026 |
303.15 |
0.1966 |
0.0051 |
303.15 |
0.3010 |
0.0084 |
303.15 |
0.3989 |
0.0114 |
303.15 |
0.5006 |
0.0141 |
303.15 |
0.6011 |
0.0163 |
303.15 |
0.7003 |
0.0185 |
303.15 |
0.8051 |
0.0200 |
303.15 |
0.8920 |
0.0212 |
303.15 |
1.0000 |
0.0221 |
313.15 |
0.0000 |
0.0007 |
313.15 |
0.0255 |
0.0010 |
313.15 |
0.0565 |
0.0013 |
313.15 |
0.1027 |
0.0020 |
313.15 |
0.1966 |
0.0037 |
313.15 |
0.3010 |
0.0058 |
313.15 |
0.3989 |
0.0078 |
313.15 |
0.5006 |
0.0095 |
313.15 |
0.6011 |
0.0109 |
313.15 |
0.7003 |
0.0122 |
313.15 |
0.8051 |
0.0132 |
313.15 |
0.8920 |
0.0139 |
313.15 |
1.0000 |
0.0146 |
323.15 |
0.0000 |
0.0006 |
323.15 |
0.0255 |
0.0008 |
323.15 |
0.0565 |
0.0010 |
323.15 |
0.1027 |
0.0015 |
323.15 |
0.1966 |
0.0028 |
323.15 |
0.3010 |
0.0042 |
323.15 |
0.3989 |
0.0055 |
323.15 |
0.5006 |
0.0067 |
323.15 |
0.6011 |
0.0076 |
323.15 |
0.7003 |
0.0085 |
323.15 |
0.8051 |
0.0091 |
323.15 |
0.8920 |
0.0096 |
323.15 |
1.0000 |
0.0100 |
333.15 |
0.0000 |
0.0005 |
333.15 |
0.0255 |
0.0006 |
333.15 |
0.0565 |
0.0008 |
333.15 |
0.1027 |
0.0012 |
333.15 |
0.1966 |
0.0021 |
333.15 |
0.3010 |
0.0032 |
333.15 |
0.3989 |
0.0041 |
333.15 |
0.5006 |
0.0049 |
333.15 |
0.6011 |
0.0055 |
333.15 |
0.7003 |
0.0061 |
333.15 |
0.8051 |
0.0065 |
333.15 |
0.8920 |
0.0069 |
333.15 |
1.0000 |
0.0072 |
343.15 |
0.0000 |
0.0004 |
343.15 |
0.0255 |
0.0005 |
343.15 |
0.0565 |
0.0007 |
343.15 |
0.1027 |
0.0010 |
343.15 |
0.1966 |
0.0017 |
343.15 |
0.3010 |
0.0025 |
343.15 |
0.3989 |
0.0032 |
343.15 |
0.5006 |
0.0037 |
343.15 |
0.6011 |
0.0042 |
343.15 |
0.7003 |
0.0046 |
343.15 |
0.8051 |
0.0049 |
343.15 |
0.8920 |
0.0051 |
343.15 |
1.0000 |
0.0054 |
353.15 |
0.0000 |
0.0004 |
353.15 |
0.0255 |
0.0005 |
353.15 |
0.0565 |
0.0006 |
353.15 |
0.1027 |
0.0008 |
353.15 |
0.1966 |
0.0014 |
353.15 |
0.3010 |
0.0020 |
353.15 |
0.3989 |
0.0025 |
353.15 |
0.5006 |
0.0029 |
353.15 |
0.6011 |
0.0033 |
353.15 |
0.7003 |
0.0036 |
353.15 |
0.8051 |
0.0038 |
353.15 |
0.8920 |
0.0040 |
353.15 |
1.0000 |
0.0041 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Mole fraction of Water (2) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.1026 |
-0.2750 |
0.2012 |
-0.5110 |
0.2094 |
-0.5210 |
0.3067 |
-0.7410 |
0.4068 |
-0.9310 |
0.4937 |
-1.039 |
0.5018 |
-1.066 |
0.6003 |
-1.192 |
0.6996 |
-1.245 |
0.7998 |
-1.172 |
0.8999 |
-0.8570 |
0.9002 |
-0.8670 |
0.9498 |
-0.5380 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.2000 |
-1.219 |
0.4010 |
-1.217 |
0.5010 |
-1.149 |
0.8040 |
-0.4630 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Mole fraction of Water (2) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.1026 |
-0.2750 |
0.2012 |
-0.5110 |
0.2094 |
-0.5210 |
0.3067 |
-0.7410 |
0.4068 |
-0.9310 |
0.4937 |
-1.039 |
0.5018 |
-1.066 |
0.6003 |
-1.192 |
0.6996 |
-1.245 |
0.7998 |
-1.172 |
0.8999 |
-0.8570 |
0.9002 |
-0.8670 |
0.9498 |
-0.5380 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.2000 |
-1.219 |
0.4010 |
-1.217 |
0.5010 |
-1.149 |
0.8040 |
-0.4630 |
Refractive index (Na D-line)
[ref]
Operational conditions:
- Temperature, K = 303 (Liquid)
- Pressure, kPa = 100 (Liquid)
Mass fraction of Water (2) - Liquid |
Refractive index (Na D-line) - Liquid |
0.1100 |
1.4341 |
0.2000 |
1.4241 |
0.3000 |
1.4134 |
0.4100 |
1.4011 |
0.5000 |
1.3892 |
0.6000 |
1.3782 |
0.7000 |
1.3662 |
0.8000 |
1.3541 |
0.9000 |
1.3426 |
1.0000 |
1.3318 |
Refractive index (Na D-line)
[ref]
Operational conditions:
- Temperature, K = 303 (Liquid)
- Pressure, kPa = 100 (Liquid)
Mass fraction of Water (2) - Liquid |
Refractive index (Na D-line) - Liquid |
0.1100 |
1.4341 |
0.2000 |
1.4241 |
0.3000 |
1.4134 |
0.4100 |
1.4011 |
0.5000 |
1.3892 |
0.6000 |
1.3782 |
0.7000 |
1.3662 |
0.8000 |
1.3541 |
0.9000 |
1.3426 |
1.0000 |
1.3318 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
92.3 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid |
Mass density, kg/m3 - Liquid |
293.15 |
0.0097 |
1006.17 |
293.15 |
0.0201 |
1013.774 |
293.15 |
0.0297 |
1020.398 |
293.15 |
0.0397 |
1026.981 |
293.15 |
0.0502 |
1033.245 |
293.15 |
0.0591 |
1038.24 |
293.15 |
0.0703 |
1044.159 |
293.15 |
0.0796 |
1048.669 |
293.15 |
0.0897 |
1053.152 |
293.15 |
0.1004 |
1057.714 |
293.15 |
0.1507 |
1074.468 |
293.15 |
0.1996 |
1085.68 |
293.15 |
0.2467 |
1093.589 |
293.15 |
0.2943 |
1098.855 |
293.15 |
0.3511 |
1103.727 |
293.15 |
0.3995 |
1106.647 |
293.15 |
0.4527 |
1109.078 |
293.15 |
0.5008 |
1110.756 |
293.15 |
0.5449 |
1111.946 |
293.15 |
0.5834 |
1112.812 |
293.15 |
0.6482 |
1113.95 |
293.15 |
0.6982 |
1114.602 |
293.15 |
0.7444 |
1115.11 |
293.15 |
0.7962 |
1115.574 |
293.15 |
0.8401 |
1115.893 |
293.15 |
0.8947 |
1116.234 |
293.15 |
0.9092 |
1116.317 |
293.15 |
0.9190 |
1116.369 |
293.15 |
0.9303 |
1116.392 |
293.15 |
0.9393 |
1116.4 |
293.15 |
0.9473 |
1116.498 |
293.15 |
0.9566 |
1116.546 |
293.15 |
0.9694 |
1116.601 |
293.15 |
0.9801 |
1116.648 |
293.15 |
0.9915 |
1116.69 |
298.15 |
0.0097 |
1004.885 |
298.15 |
0.0201 |
1012.33 |
298.15 |
0.0297 |
1018.801 |
298.15 |
0.0397 |
1025.226 |
298.15 |
0.0502 |
1031.33 |
298.15 |
0.0591 |
1036.189 |
298.15 |
0.0703 |
1041.951 |
298.15 |
0.0796 |
1046.341 |
298.15 |
0.0897 |
1050.705 |
298.15 |
0.1004 |
1055.142 |
298.15 |
0.1507 |
1071.485 |
298.15 |
0.1996 |
1082.45 |
298.15 |
0.2467 |
1090.206 |
298.15 |
0.2943 |
1095.375 |
298.15 |
0.3511 |
1100.191 |
298.15 |
0.3995 |
1103.051 |
298.15 |
0.4527 |
1105.496 |
298.15 |
0.5008 |
1107.171 |
298.15 |
0.5449 |
1108.361 |
298.15 |
0.5834 |
1109.228 |
298.15 |
0.6482 |
1110.368 |
298.15 |
0.6982 |
1111.024 |
298.15 |
0.7444 |
1111.536 |
298.15 |
0.7962 |
1112.005 |
298.15 |
0.8401 |
1112.329 |
298.15 |
0.8947 |
1112.673 |
298.15 |
0.9092 |
1112.755 |
298.15 |
0.9190 |
1112.81 |
298.15 |
0.9303 |
1112.845 |
298.15 |
0.9393 |
1112.85 |
298.15 |
0.9473 |
1112.94 |
298.15 |
0.9566 |
1112.989 |
298.15 |
0.9694 |
1113.044 |
298.15 |
0.9801 |
1113.092 |
298.15 |
0.9915 |
1113.135 |
303.15 |
0.0097 |
1003.366 |
303.15 |
0.0201 |
1010.671 |
303.15 |
0.0297 |
1017.004 |
303.15 |
0.0397 |
1023.281 |
303.15 |
0.0502 |
1029.242 |
303.15 |
0.0591 |
1033.98 |
303.15 |
0.0703 |
1039.597 |
303.15 |
0.0796 |
1043.879 |
303.15 |
0.0897 |
1048.134 |
303.15 |
0.1004 |
1052.456 |
303.15 |
0.1507 |
1068.416 |
303.15 |
0.1996 |
1079.151 |
303.15 |
0.2467 |
1086.765 |
303.15 |
0.2943 |
1091.844 |
303.15 |
0.3511 |
1096.608 |
303.15 |
0.3995 |
1099.417 |
303.15 |
0.4527 |
1101.877 |
303.15 |
0.5008 |
1103.557 |
303.15 |
0.5449 |
1104.748 |
303.15 |
0.5834 |
1105.614 |
303.15 |
0.6482 |
1106.76 |
303.15 |
0.6982 |
1107.423 |
303.15 |
0.7444 |
1107.937 |
303.15 |
0.7962 |
1108.413 |
303.15 |
0.8401 |
1108.739 |
303.15 |
0.8947 |
1109.088 |
303.15 |
0.9092 |
1109.172 |
303.15 |
0.9190 |
1109.229 |
303.15 |
0.9303 |
1109.267 |
303.15 |
0.9393 |
1109.277 |
303.15 |
0.9473 |
1109.361 |
303.15 |
0.9566 |
1109.41 |
303.15 |
0.9694 |
1109.467 |
303.15 |
0.9801 |
1109.516 |
303.15 |
0.9915 |
1109.562 |
308.15 |
0.0097 |
1001.634 |
308.15 |
0.0201 |
1008.814 |
308.15 |
0.0297 |
1015.021 |
308.15 |
0.0397 |
1021.167 |
308.15 |
0.0502 |
1026.994 |
308.15 |
0.0591 |
1031.626 |
308.15 |
0.0703 |
1037.108 |
308.15 |
0.0796 |
1041.293 |
308.15 |
0.0897 |
1045.448 |
308.15 |
0.1004 |
1049.659 |
308.15 |
0.1507 |
1065.271 |
308.15 |
0.1996 |
1075.794 |
308.15 |
0.2467 |
1083.272 |
308.15 |
0.2943 |
1088.253 |
308.15 |
0.3511 |
1092.986 |
308.15 |
0.3995 |
1095.833 |
308.15 |
0.4527 |
1098.237 |
308.15 |
0.5008 |
1099.92 |
308.15 |
0.5449 |
1101.11 |
308.15 |
0.5834 |
1101.985 |
308.15 |
0.6482 |
1103.133 |
308.15 |
0.6982 |
1103.802 |
308.15 |
0.7444 |
1104.328 |
308.15 |
0.7962 |
1104.809 |
308.15 |
0.8401 |
1105.138 |
308.15 |
0.8947 |
1105.494 |
308.15 |
0.9092 |
1105.578 |
308.15 |
0.9190 |
1105.636 |
308.15 |
0.9303 |
1105.678 |
308.15 |
0.9393 |
1105.694 |
308.15 |
0.9473 |
1105.769 |
308.15 |
0.9566 |
1105.82 |
308.15 |
0.9694 |
1105.878 |
308.15 |
0.9801 |
1105.926 |
308.15 |
0.9915 |
1105.973 |
293.15 |
0.0000 |
998.429 |
298.15 |
0.0000 |
997.267 |
303.15 |
0.0000 |
995.867 |
308.15 |
0.0000 |
994.252 |
293.15 |
1.0000 |
1116.733 |
298.15 |
1.0000 |
1113.174 |
303.15 |
1.0000 |
1109.599 |
308.15 |
1.0000 |
1106.013 |
293.15 |
0.0490 |
1032.591 |
293.15 |
0.0992 |
1057.143 |
293.15 |
0.1490 |
1074.037 |
293.15 |
0.1998 |
1085.893 |
293.15 |
0.2490 |
1093.806 |
293.15 |
0.2987 |
1099.437 |
293.15 |
0.3501 |
1103.603 |
293.15 |
0.4007 |
1106.626 |
293.15 |
0.4504 |
1108.903 |
293.15 |
0.4973 |
1110.602 |
293.15 |
0.5530 |
1112.185 |
293.15 |
0.5938 |
1113.094 |
293.15 |
0.6514 |
1114.071 |
293.15 |
0.6864 |
1114.522 |
293.15 |
0.7556 |
1115.186 |
293.15 |
0.7999 |
1115.521 |
293.15 |
0.8525 |
1115.894 |
293.15 |
0.9002 |
1116.233 |
293.15 |
0.9554 |
1116.574 |
298.15 |
0.0490 |
1030.669 |
298.15 |
0.0992 |
1054.615 |
298.15 |
0.1490 |
1071.09 |
298.15 |
0.1998 |
1082.664 |
298.15 |
0.2490 |
1090.405 |
298.15 |
0.2987 |
1095.935 |
298.15 |
0.3501 |
1100.047 |
298.15 |
0.4007 |
1103.049 |
298.15 |
0.4504 |
1105.321 |
298.15 |
0.4973 |
1107.021 |
298.15 |
0.5530 |
1108.607 |
298.15 |
0.5938 |
1109.516 |
298.15 |
0.6514 |
1110.493 |
298.15 |
0.6864 |
1110.943 |
298.15 |
0.7556 |
1111.608 |
298.15 |
0.7999 |
1111.947 |
298.15 |
0.8525 |
1112.329 |
298.15 |
0.9002 |
1112.677 |
298.15 |
0.9554 |
1113.023 |
303.15 |
0.0490 |
1028.576 |
303.15 |
0.0992 |
1051.966 |
303.15 |
0.1490 |
1068.055 |
303.15 |
0.1998 |
1079.366 |
303.15 |
0.2490 |
1086.946 |
303.15 |
0.2987 |
1092.382 |
303.15 |
0.3501 |
1096.446 |
303.15 |
0.4007 |
1099.431 |
303.15 |
0.4504 |
1101.701 |
303.15 |
0.4973 |
1103.405 |
303.15 |
0.5530 |
1104.997 |
303.15 |
0.5938 |
1105.91 |
303.15 |
0.6514 |
1106.888 |
303.15 |
0.6864 |
1107.338 |
303.15 |
0.7556 |
1108.005 |
303.15 |
0.7999 |
1108.346 |
303.15 |
0.8525 |
1108.736 |
303.15 |
0.9002 |
1109.094 |
303.15 |
0.9554 |
1109.446 |
308.15 |
0.0490 |
1026.325 |
308.15 |
0.0992 |
1049.205 |
308.15 |
0.1490 |
1064.938 |
308.15 |
0.1998 |
1076.008 |
308.15 |
0.2490 |
1083.444 |
308.15 |
0.2987 |
1088.798 |
308.15 |
0.3501 |
1092.823 |
308.15 |
0.4007 |
1095.796 |
308.15 |
0.4504 |
1098.068 |
308.15 |
0.4973 |
1099.779 |
308.15 |
0.5530 |
1101.377 |
308.15 |
0.5938 |
1102.291 |
308.15 |
0.6514 |
1103.268 |
308.15 |
0.6864 |
1103.717 |
308.15 |
0.7556 |
1104.385 |
308.15 |
0.7999 |
1104.732 |
308.15 |
0.8525 |
1105.132 |
308.15 |
0.9002 |
1105.502 |
308.15 |
0.9554 |
1105.863 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Molality, mol/kg of Ethanol, 2,2'-oxybis- (1) - Liquid |
Mass density, kg/m3 - Liquid |
293.15 |
0.0985 |
999.65 |
293.15 |
0.1974 |
1001.03 |
293.15 |
0.2950 |
1002.36 |
293.15 |
0.4101 |
1003.86 |
293.15 |
0.5006 |
1004.99 |
303.15 |
0.0985 |
997.07 |
303.15 |
0.1974 |
998.39 |
303.15 |
0.2950 |
999.64 |
303.15 |
0.4101 |
1001.05 |
303.15 |
0.5006 |
1002.15 |
293.15 |
0.0000 |
998.21 |
303.15 |
0.0000 |
995.66 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
98.3 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Molality, mol/kg of Ethanol, 2,2'-oxybis- (1) - Liquid |
Mass density, kg/m3 - Liquid |
278.15 |
0.0511 |
1000.743 |
278.15 |
0.1025 |
1001.52 |
278.15 |
0.2049 |
1003.056 |
278.15 |
0.2972 |
1004.427 |
278.15 |
0.4063 |
1006.029 |
283.15 |
0.0511 |
1000.462 |
283.15 |
0.1025 |
1001.222 |
283.15 |
0.2049 |
1002.721 |
283.15 |
0.2972 |
1004.058 |
283.15 |
0.4063 |
1005.619 |
288.15 |
0.0511 |
999.849 |
288.15 |
0.1025 |
1000.593 |
288.15 |
0.2049 |
1002.061 |
288.15 |
0.2972 |
1003.369 |
288.15 |
0.4063 |
1004.895 |
293.15 |
0.0511 |
998.941 |
293.15 |
0.1025 |
999.67 |
293.15 |
0.2049 |
1001.113 |
293.15 |
0.2972 |
1002.394 |
293.15 |
0.4063 |
1003.891 |
298.15 |
0.0511 |
997.772 |
298.15 |
0.1025 |
998.489 |
298.15 |
0.2049 |
999.907 |
298.15 |
0.2972 |
1001.167 |
298.15 |
0.4063 |
1002.636 |
303.15 |
0.0511 |
996.365 |
303.15 |
0.1025 |
997.071 |
303.15 |
0.2049 |
998.466 |
303.15 |
0.2972 |
999.707 |
303.15 |
0.4063 |
1001.152 |
308.15 |
0.0511 |
994.74 |
308.15 |
0.1025 |
995.437 |
308.15 |
0.2049 |
996.813 |
308.15 |
0.2972 |
998.034 |
308.15 |
0.4063 |
999.457 |
313.15 |
0.0511 |
992.916 |
313.15 |
0.1025 |
993.604 |
313.15 |
0.2049 |
994.96 |
313.15 |
0.2972 |
996.164 |
313.15 |
0.4063 |
997.567 |
318.15 |
0.0511 |
990.905 |
318.15 |
0.1025 |
991.585 |
318.15 |
0.2049 |
992.924 |
318.15 |
0.2972 |
994.112 |
318.15 |
0.4063 |
995.495 |
323.15 |
0.0511 |
988.72 |
323.15 |
0.1025 |
989.393 |
323.15 |
0.2049 |
990.716 |
323.15 |
0.2972 |
991.889 |
323.15 |
0.4063 |
993.254 |
328.15 |
0.0511 |
986.371 |
328.15 |
0.1025 |
987.036 |
328.15 |
0.2049 |
988.343 |
328.15 |
0.2972 |
989.503 |
328.15 |
0.4063 |
990.852 |
333.15 |
0.0511 |
983.864 |
333.15 |
0.1025 |
984.525 |
333.15 |
0.2049 |
985.817 |
333.15 |
0.2972 |
986.963 |
333.15 |
0.4063 |
988.296 |
338.15 |
0.0511 |
981.213 |
338.15 |
0.1025 |
981.866 |
338.15 |
0.2049 |
983.145 |
338.15 |
0.2972 |
984.279 |
338.15 |
0.4063 |
985.595 |
343.15 |
0.0511 |
978.42 |
343.15 |
0.1025 |
979.067 |
343.15 |
0.2049 |
980.331 |
343.15 |
0.2972 |
981.454 |
343.15 |
0.4063 |
982.755 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid |
Mass density, kg/m3 - Liquid |
283.15 |
0.9070 |
1123.135 |
288.15 |
0.9070 |
1119.575 |
293.15 |
0.9070 |
1116.018 |
298.15 |
0.9070 |
1112.454 |
303.15 |
0.9070 |
1108.881 |
308.15 |
0.9070 |
1105.295 |
313.15 |
0.9070 |
1101.695 |
323.15 |
0.9070 |
1094.447 |
333.15 |
0.9070 |
1087.119 |
343.15 |
0.9070 |
1079.71 |
283.15 |
0.9589 |
1123.266 |
288.15 |
0.9589 |
1119.71 |
293.15 |
0.9589 |
1116.151 |
298.15 |
0.9589 |
1112.585 |
303.15 |
0.9589 |
1109.016 |
308.15 |
0.9589 |
1105.431 |
313.15 |
0.9589 |
1101.834 |
323.15 |
0.9589 |
1094.595 |
333.15 |
0.9589 |
1087.278 |
343.15 |
0.9589 |
1079.883 |
283.15 |
0.9698 |
1123.273 |
288.15 |
0.9698 |
1119.716 |
293.15 |
0.9698 |
1116.159 |
298.15 |
0.9698 |
1112.594 |
303.15 |
0.9698 |
1109.025 |
308.15 |
0.9698 |
1105.442 |
313.15 |
0.9698 |
1101.843 |
323.15 |
0.9698 |
1094.603 |
333.15 |
0.9698 |
1087.288 |
343.15 |
0.9698 |
1079.897 |
283.15 |
0.9900 |
1123.325 |
288.15 |
0.9900 |
1119.767 |
293.15 |
0.9900 |
1116.211 |
298.15 |
0.9900 |
1112.649 |
303.15 |
0.9900 |
1109.077 |
308.15 |
0.9900 |
1105.496 |
313.15 |
0.9900 |
1101.9 |
323.15 |
0.9900 |
1094.667 |
333.15 |
0.9900 |
1087.359 |
343.15 |
0.9900 |
1079.973 |
283.15 |
0.9901 |
1123.327 |
288.15 |
0.9901 |
1119.771 |
293.15 |
0.9901 |
1116.213 |
298.15 |
0.9901 |
1112.651 |
303.15 |
0.9901 |
1109.081 |
308.15 |
0.9901 |
1105.498 |
313.15 |
0.9901 |
1101.903 |
323.15 |
0.9901 |
1094.668 |
333.15 |
0.9901 |
1087.356 |
343.15 |
0.9901 |
1079.969 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Molality, mol/kg of Ethanol, 2,2'-oxybis- (1) - Liquid |
Mass density, kg/m3 - Liquid |
288.15 |
0.0985 |
1000.689 |
288.15 |
0.1974 |
1002.06 |
288.15 |
0.2950 |
1003.358 |
288.15 |
0.4101 |
1004.837 |
288.15 |
0.5006 |
1005.961 |
288.15 |
0.6001 |
1007.125 |
288.15 |
0.6996 |
1008.278 |
288.15 |
0.7999 |
1009.393 |
298.15 |
0.0985 |
998.458 |
298.15 |
0.1974 |
999.78 |
298.15 |
0.2950 |
1001.026 |
298.15 |
0.4101 |
1002.49 |
298.15 |
0.5006 |
1003.585 |
298.15 |
0.6001 |
1004.735 |
298.15 |
0.6996 |
1005.827 |
298.15 |
0.7999 |
1006.873 |
308.15 |
0.0985 |
995.44 |
308.15 |
0.1974 |
996.778 |
308.15 |
0.2950 |
998.046 |
308.15 |
0.4101 |
999.471 |
308.15 |
0.5006 |
1000.531 |
308.15 |
0.6001 |
1001.676 |
308.15 |
0.6996 |
1002.761 |
308.15 |
0.7999 |
1003.829 |
318.15 |
0.0985 |
991.758 |
318.15 |
0.1974 |
993.102 |
318.15 |
0.2950 |
994.366 |
318.15 |
0.4101 |
995.788 |
318.15 |
0.5006 |
996.853 |
318.15 |
0.6001 |
997.974 |
318.15 |
0.6996 |
999.056 |
318.15 |
0.7999 |
1000.108 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Molality, mol/kg of Ethanol, 2,2'-oxybis- (1) - Liquid |
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
0.0985 |
293.15 |
999.647 |
0.1974 |
293.15 |
1001.031 |
0.2950 |
293.15 |
1002.356 |
0.4101 |
293.15 |
1003.859 |
0.5006 |
293.15 |
1004.993 |
0.0985 |
298.15 |
998.458 |
0.1974 |
298.15 |
999.78 |
0.2950 |
298.15 |
1001.026 |
0.4101 |
298.15 |
1002.49 |
0.5006 |
298.15 |
1003.585 |
0.0985 |
303.15 |
997.071 |
0.1974 |
303.15 |
998.395 |
0.2950 |
303.15 |
999.643 |
0.4101 |
303.15 |
1001.051 |
0.5006 |
303.15 |
1002.146 |
0.0985 |
308.15 |
995.44 |
0.1974 |
308.15 |
996.778 |
0.2950 |
308.15 |
998.046 |
0.4101 |
308.15 |
999.471 |
0.5006 |
308.15 |
1000.531 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid |
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
0.2500 |
294.25 |
1095.0 |
0.2500 |
313.05 |
1081.0 |
0.2500 |
333.05 |
1066.0 |
0.2500 |
353.15 |
1051.0 |
0.2500 |
381.45 |
1027.0 |
0.2500 |
392.75 |
1017.0 |
0.2500 |
409.25 |
1004.0 |
0.2500 |
426.35 |
987.6 |
0.2500 |
441.65 |
973.3 |
0.5000 |
293.45 |
1111.0 |
0.5000 |
312.95 |
1097.0 |
0.5000 |
332.95 |
1082.0 |
0.5000 |
352.95 |
1066.0 |
0.5000 |
380.05 |
1043.0 |
0.5000 |
390.25 |
1035.0 |
0.5000 |
405.35 |
1023.0 |
0.5000 |
424.25 |
1006.0 |
0.5000 |
443.05 |
988.2 |
0.7500 |
294.05 |
1115.0 |
0.7500 |
313.05 |
1101.0 |
0.7500 |
333.05 |
1087.0 |
0.7500 |
353.05 |
1071.0 |
0.7500 |
382.55 |
1048.0 |
0.7500 |
390.95 |
1042.0 |
0.7500 |
406.95 |
1029.0 |
0.7500 |
424.65 |
1014.0 |
0.7500 |
443.65 |
996.3 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid |
Mass density, kg/m3 - Liquid |
303.15 |
0.0000 |
995.6 |
303.15 |
0.0501 |
1028.38 |
303.15 |
0.1016 |
1051.83 |
303.15 |
0.1512 |
1067.99 |
303.15 |
0.2012 |
1078.71 |
303.15 |
0.2477 |
1086.55 |
303.15 |
0.2980 |
1092.27 |
303.15 |
0.3505 |
1096.22 |
303.15 |
0.4483 |
1101.17 |
303.15 |
0.5421 |
1103.74 |
303.15 |
0.6518 |
1106.25 |
303.15 |
0.7525 |
1107.78 |
303.15 |
0.7864 |
1107.94 |
303.15 |
0.8499 |
1108.55 |
303.15 |
0.9005 |
1108.84 |
303.15 |
0.9503 |
1109.66 |
303.15 |
1.0000 |
1109.48 |
308.15 |
0.0000 |
994.12 |
308.15 |
0.0501 |
1026.09 |
308.15 |
0.1016 |
1048.94 |
308.15 |
0.1512 |
1065.34 |
308.15 |
0.2012 |
1075.25 |
308.15 |
0.2477 |
1082.95 |
308.15 |
0.2980 |
1088.52 |
308.15 |
0.3505 |
1092.42 |
308.15 |
0.4483 |
1097.58 |
308.15 |
0.5421 |
1100.11 |
308.15 |
0.6518 |
1102.58 |
308.15 |
0.7525 |
1103.95 |
308.15 |
0.7864 |
1104.26 |
308.15 |
0.8499 |
1104.93 |
308.15 |
0.9005 |
1105.16 |
308.15 |
0.9503 |
1105.58 |
308.15 |
1.0000 |
1105.72 |
313.15 |
0.0000 |
992.25 |
313.15 |
0.0501 |
1023.67 |
313.15 |
0.1016 |
1046.02 |
313.15 |
0.1512 |
1062.04 |
313.15 |
0.2012 |
1071.77 |
313.15 |
0.2477 |
1079.42 |
313.15 |
0.2980 |
1084.97 |
313.15 |
0.3505 |
1088.68 |
313.15 |
0.4483 |
1093.68 |
313.15 |
0.5421 |
1096.37 |
313.15 |
0.6518 |
1098.97 |
313.15 |
0.7525 |
1100.25 |
313.15 |
0.7864 |
1100.56 |
313.15 |
0.8499 |
1101.32 |
313.15 |
0.9005 |
1101.55 |
313.15 |
0.9503 |
1101.98 |
313.15 |
1.0000 |
1102.11 |
318.15 |
0.0000 |
990.3 |
318.15 |
0.0501 |
1021.08 |
318.15 |
0.1016 |
1043.03 |
318.15 |
0.1512 |
1058.72 |
318.15 |
0.2012 |
1068.24 |
318.15 |
0.2477 |
1075.76 |
318.15 |
0.2980 |
1081.58 |
318.15 |
0.3505 |
1084.97 |
318.15 |
0.4483 |
1089.91 |
318.15 |
0.5421 |
1092.91 |
318.15 |
0.6518 |
1095.29 |
318.15 |
0.7525 |
1096.58 |
318.15 |
0.7864 |
1096.89 |
318.15 |
0.8499 |
1097.62 |
318.15 |
0.9005 |
1097.87 |
318.15 |
0.9503 |
1098.33 |
318.15 |
1.0000 |
1098.35 |
323.15 |
0.0000 |
988.1 |
323.15 |
0.0501 |
1018.36 |
323.15 |
0.1016 |
1039.94 |
323.15 |
0.1512 |
1055.2 |
323.15 |
0.2012 |
1064.5 |
323.15 |
0.2477 |
1072.18 |
323.15 |
0.2980 |
1077.47 |
323.15 |
0.3505 |
1081.16 |
323.15 |
0.4483 |
1086.1 |
323.15 |
0.5421 |
1088.98 |
323.15 |
0.6518 |
1091.34 |
323.15 |
0.7525 |
1093.18 |
323.15 |
0.7864 |
1093.37 |
323.15 |
0.8499 |
1093.91 |
323.15 |
0.9005 |
1094.19 |
323.15 |
0.9503 |
1094.55 |
323.15 |
1.0000 |
1094.94 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid |
Mass density, kg/m3 - Liquid |
283.15 |
0.0000 |
999.7 |
283.15 |
0.0255 |
1019.73 |
283.15 |
0.0565 |
1040.15 |
283.15 |
0.1027 |
1063.34 |
283.15 |
0.1966 |
1091.18 |
283.15 |
0.3010 |
1106.34 |
283.15 |
0.3989 |
1113.62 |
283.15 |
0.5006 |
1117.88 |
283.15 |
0.6011 |
1120.39 |
283.15 |
0.7003 |
1121.98 |
283.15 |
0.8051 |
1123.07 |
283.15 |
0.8920 |
1123.64 |
283.15 |
1.0000 |
1124.24 |
288.15 |
0.0000 |
999.1 |
288.15 |
0.0255 |
1018.61 |
288.15 |
0.0565 |
1038.42 |
288.15 |
0.1027 |
1060.91 |
288.15 |
0.1966 |
1088.01 |
288.15 |
0.3010 |
1102.88 |
288.15 |
0.3989 |
1110.06 |
288.15 |
0.5006 |
1114.29 |
288.15 |
0.6011 |
1116.8 |
288.15 |
0.7003 |
1118.39 |
288.15 |
0.8051 |
1119.47 |
288.15 |
0.8920 |
1120.05 |
288.15 |
1.0000 |
1120.65 |
293.15 |
0.0000 |
998.2 |
293.15 |
0.0255 |
1017.27 |
293.15 |
0.0565 |
1036.53 |
293.15 |
0.1027 |
1058.39 |
293.15 |
0.1966 |
1084.81 |
293.15 |
0.3010 |
1099.4 |
293.15 |
0.3989 |
1106.48 |
293.15 |
0.5006 |
1110.68 |
293.15 |
0.6011 |
1113.19 |
293.15 |
0.7003 |
1114.79 |
293.15 |
0.8051 |
1115.87 |
293.15 |
0.8920 |
1116.45 |
293.15 |
1.0000 |
1117.05 |
298.15 |
0.0000 |
997.04 |
298.15 |
0.0255 |
1015.72 |
298.15 |
0.0565 |
1034.5 |
298.15 |
0.1027 |
1055.77 |
298.15 |
0.1966 |
1081.56 |
298.15 |
0.3010 |
1095.89 |
298.15 |
0.3989 |
1102.89 |
298.15 |
0.5006 |
1107.07 |
298.15 |
0.6011 |
1109.59 |
298.15 |
0.7003 |
1111.19 |
298.15 |
0.8051 |
1112.27 |
298.15 |
0.8920 |
1112.86 |
298.15 |
1.0000 |
1113.47 |
303.15 |
0.0000 |
995.55 |
303.15 |
0.0255 |
1013.97 |
303.15 |
0.0565 |
1032.33 |
303.15 |
0.1027 |
1053.07 |
303.15 |
0.1966 |
1078.28 |
303.15 |
0.3010 |
1092.36 |
303.15 |
0.3989 |
1099.29 |
303.15 |
0.5006 |
1103.45 |
303.15 |
0.6011 |
1105.97 |
303.15 |
0.7003 |
1107.58 |
303.15 |
0.8051 |
1108.67 |
303.15 |
0.8920 |
1109.27 |
303.15 |
1.0000 |
1109.88 |
308.15 |
0.0000 |
994.03 |
308.15 |
0.0255 |
1011.83 |
308.15 |
0.0565 |
1030.02 |
308.15 |
0.1027 |
1050.27 |
308.15 |
0.1966 |
1074.94 |
308.15 |
0.3010 |
1088.8 |
308.15 |
0.3989 |
1095.67 |
308.15 |
0.5006 |
1099.82 |
308.15 |
0.6011 |
1102.36 |
308.15 |
0.7003 |
1103.97 |
308.15 |
0.8051 |
1105.06 |
308.15 |
0.8920 |
1105.68 |
308.15 |
1.0000 |
1106.29 |
313.15 |
0.0000 |
992.21 |
313.15 |
0.0255 |
1009.99 |
313.15 |
0.0565 |
1027.57 |
313.15 |
0.1027 |
1047.39 |
313.15 |
0.1966 |
1071.56 |
313.15 |
0.3010 |
1085.22 |
313.15 |
0.3989 |
1092.03 |
313.15 |
0.5006 |
1096.18 |
313.15 |
0.6011 |
1098.73 |
313.15 |
0.7003 |
1100.35 |
313.15 |
0.8051 |
1101.45 |
313.15 |
0.8920 |
1102.09 |
313.15 |
1.0000 |
1102.7 |
318.15 |
0.0000 |
990.21 |
318.15 |
0.0255 |
1007.73 |
318.15 |
0.0565 |
1025.01 |
318.15 |
0.1027 |
1044.41 |
318.15 |
0.1966 |
1068.13 |
318.15 |
0.3010 |
1081.61 |
318.15 |
0.3989 |
1088.37 |
318.15 |
0.5006 |
1092.53 |
318.15 |
0.6011 |
1095.08 |
318.15 |
0.7003 |
1096.71 |
318.15 |
0.8051 |
1097.83 |
318.15 |
0.8920 |
1098.49 |
318.15 |
1.0000 |
1099.11 |
323.15 |
0.0000 |
988.03 |
323.15 |
0.0255 |
1005.37 |
323.15 |
0.0565 |
1022.33 |
323.15 |
0.1027 |
1041.36 |
323.15 |
0.1966 |
1064.65 |
323.15 |
0.3010 |
1077.97 |
323.15 |
0.3989 |
1084.69 |
323.15 |
0.5006 |
1088.85 |
323.15 |
0.6011 |
1091.42 |
323.15 |
0.7003 |
1093.07 |
323.15 |
0.8051 |
1094.21 |
323.15 |
0.8920 |
1094.88 |
323.15 |
1.0000 |
1095.51 |
328.15 |
0.0000 |
985.69 |
328.15 |
0.0255 |
1002.86 |
328.15 |
0.0565 |
1019.53 |
328.15 |
0.1027 |
1038.21 |
328.15 |
0.1966 |
1061.13 |
328.15 |
0.3010 |
1074.29 |
328.15 |
0.3989 |
1080.98 |
328.15 |
0.5006 |
1085.16 |
328.15 |
0.6011 |
1087.74 |
328.15 |
0.7003 |
1089.41 |
328.15 |
0.8051 |
1090.57 |
328.15 |
0.8920 |
1091.26 |
328.15 |
1.0000 |
1091.91 |
333.15 |
0.0000 |
983.19 |
333.15 |
0.0255 |
1000.22 |
333.15 |
0.0565 |
1016.62 |
333.15 |
0.1027 |
1034.99 |
333.15 |
0.1966 |
1057.55 |
333.15 |
0.3010 |
1070.58 |
333.15 |
0.3989 |
1077.25 |
333.15 |
0.5006 |
1081.43 |
333.15 |
0.6011 |
1084.04 |
333.15 |
0.7003 |
1085.74 |
333.15 |
0.8051 |
1086.93 |
333.15 |
0.8920 |
1087.63 |
333.15 |
1.0000 |
1088.3 |
338.15 |
0.0000 |
980.55 |
338.15 |
0.0255 |
997.46 |
338.15 |
0.0565 |
1013.61 |
338.15 |
0.1027 |
1031.68 |
338.15 |
0.1966 |
1053.92 |
338.15 |
0.3010 |
1066.84 |
338.15 |
0.3989 |
1073.49 |
338.15 |
0.5006 |
1077.69 |
338.15 |
0.6011 |
1080.33 |
338.15 |
0.7003 |
1082.06 |
338.15 |
0.8051 |
1083.27 |
338.15 |
0.8920 |
1083.99 |
338.15 |
1.0000 |
1084.68 |
343.15 |
0.0000 |
977.76 |
343.15 |
0.0255 |
994.57 |
343.15 |
0.0565 |
1010.51 |
343.15 |
0.1027 |
1028.29 |
343.15 |
0.1966 |
1050.24 |
343.15 |
0.3010 |
1063.06 |
343.15 |
0.3989 |
1069.69 |
343.15 |
0.5006 |
1073.93 |
343.15 |
0.6011 |
1076.59 |
343.15 |
0.7003 |
1078.36 |
343.15 |
0.8051 |
1079.6 |
343.15 |
0.8920 |
1080.34 |
343.15 |
1.0000 |
1081.05 |
348.15 |
0.0000 |
974.84 |
348.15 |
0.0255 |
991.57 |
348.15 |
0.0565 |
1007.27 |
348.15 |
0.1027 |
1024.84 |
348.15 |
0.1966 |
1046.51 |
348.15 |
0.3010 |
1059.24 |
348.15 |
0.3989 |
1065.88 |
348.15 |
0.5006 |
1070.14 |
348.15 |
0.6011 |
1072.84 |
348.15 |
0.7003 |
1074.63 |
348.15 |
0.8051 |
1075.91 |
348.15 |
0.8920 |
1076.67 |
348.15 |
1.0000 |
1077.4 |
353.15 |
0.0000 |
971.79 |
353.15 |
0.0255 |
988.5 |
353.15 |
0.0565 |
1004.07 |
353.15 |
0.1027 |
1021.3 |
353.15 |
0.1966 |
1042.72 |
353.15 |
0.3010 |
1055.38 |
353.15 |
0.3989 |
1062.02 |
353.15 |
0.5006 |
1066.32 |
353.15 |
0.6011 |
1069.05 |
353.15 |
0.7003 |
1070.89 |
353.15 |
0.8051 |
1072.2 |
353.15 |
0.8920 |
1072.99 |
353.15 |
1.0000 |
1073.74 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
92.3 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid |
Mass density, kg/m3 - Liquid |
293.15 |
0.0097 |
1006.17 |
293.15 |
0.0201 |
1013.774 |
293.15 |
0.0297 |
1020.398 |
293.15 |
0.0397 |
1026.981 |
293.15 |
0.0502 |
1033.245 |
293.15 |
0.0591 |
1038.24 |
293.15 |
0.0703 |
1044.159 |
293.15 |
0.0796 |
1048.669 |
293.15 |
0.0897 |
1053.152 |
293.15 |
0.1004 |
1057.714 |
293.15 |
0.1507 |
1074.468 |
293.15 |
0.1996 |
1085.68 |
293.15 |
0.2467 |
1093.589 |
293.15 |
0.2943 |
1098.855 |
293.15 |
0.3511 |
1103.727 |
293.15 |
0.3995 |
1106.647 |
293.15 |
0.4527 |
1109.078 |
293.15 |
0.5008 |
1110.756 |
293.15 |
0.5449 |
1111.946 |
293.15 |
0.5834 |
1112.812 |
293.15 |
0.6482 |
1113.95 |
293.15 |
0.6982 |
1114.602 |
293.15 |
0.7444 |
1115.11 |
293.15 |
0.7962 |
1115.574 |
293.15 |
0.8401 |
1115.893 |
293.15 |
0.8947 |
1116.234 |
293.15 |
0.9092 |
1116.317 |
293.15 |
0.9190 |
1116.369 |
293.15 |
0.9303 |
1116.392 |
293.15 |
0.9393 |
1116.4 |
293.15 |
0.9473 |
1116.498 |
293.15 |
0.9566 |
1116.546 |
293.15 |
0.9694 |
1116.601 |
293.15 |
0.9801 |
1116.648 |
293.15 |
0.9915 |
1116.69 |
298.15 |
0.0097 |
1004.885 |
298.15 |
0.0201 |
1012.33 |
298.15 |
0.0297 |
1018.801 |
298.15 |
0.0397 |
1025.226 |
298.15 |
0.0502 |
1031.33 |
298.15 |
0.0591 |
1036.189 |
298.15 |
0.0703 |
1041.951 |
298.15 |
0.0796 |
1046.341 |
298.15 |
0.0897 |
1050.705 |
298.15 |
0.1004 |
1055.142 |
298.15 |
0.1507 |
1071.485 |
298.15 |
0.1996 |
1082.45 |
298.15 |
0.2467 |
1090.206 |
298.15 |
0.2943 |
1095.375 |
298.15 |
0.3511 |
1100.191 |
298.15 |
0.3995 |
1103.051 |
298.15 |
0.4527 |
1105.496 |
298.15 |
0.5008 |
1107.171 |
298.15 |
0.5449 |
1108.361 |
298.15 |
0.5834 |
1109.228 |
298.15 |
0.6482 |
1110.368 |
298.15 |
0.6982 |
1111.024 |
298.15 |
0.7444 |
1111.536 |
298.15 |
0.7962 |
1112.005 |
298.15 |
0.8401 |
1112.329 |
298.15 |
0.8947 |
1112.673 |
298.15 |
0.9092 |
1112.755 |
298.15 |
0.9190 |
1112.81 |
298.15 |
0.9303 |
1112.845 |
298.15 |
0.9393 |
1112.85 |
298.15 |
0.9473 |
1112.94 |
298.15 |
0.9566 |
1112.989 |
298.15 |
0.9694 |
1113.044 |
298.15 |
0.9801 |
1113.092 |
298.15 |
0.9915 |
1113.135 |
303.15 |
0.0097 |
1003.366 |
303.15 |
0.0201 |
1010.671 |
303.15 |
0.0297 |
1017.004 |
303.15 |
0.0397 |
1023.281 |
303.15 |
0.0502 |
1029.242 |
303.15 |
0.0591 |
1033.98 |
303.15 |
0.0703 |
1039.597 |
303.15 |
0.0796 |
1043.879 |
303.15 |
0.0897 |
1048.134 |
303.15 |
0.1004 |
1052.456 |
303.15 |
0.1507 |
1068.416 |
303.15 |
0.1996 |
1079.151 |
303.15 |
0.2467 |
1086.765 |
303.15 |
0.2943 |
1091.844 |
303.15 |
0.3511 |
1096.608 |
303.15 |
0.3995 |
1099.417 |
303.15 |
0.4527 |
1101.877 |
303.15 |
0.5008 |
1103.557 |
303.15 |
0.5449 |
1104.748 |
303.15 |
0.5834 |
1105.614 |
303.15 |
0.6482 |
1106.76 |
303.15 |
0.6982 |
1107.423 |
303.15 |
0.7444 |
1107.937 |
303.15 |
0.7962 |
1108.413 |
303.15 |
0.8401 |
1108.739 |
303.15 |
0.8947 |
1109.088 |
303.15 |
0.9092 |
1109.172 |
303.15 |
0.9190 |
1109.229 |
303.15 |
0.9303 |
1109.267 |
303.15 |
0.9393 |
1109.277 |
303.15 |
0.9473 |
1109.361 |
303.15 |
0.9566 |
1109.41 |
303.15 |
0.9694 |
1109.467 |
303.15 |
0.9801 |
1109.516 |
303.15 |
0.9915 |
1109.562 |
308.15 |
0.0097 |
1001.634 |
308.15 |
0.0201 |
1008.814 |
308.15 |
0.0297 |
1015.021 |
308.15 |
0.0397 |
1021.167 |
308.15 |
0.0502 |
1026.994 |
308.15 |
0.0591 |
1031.626 |
308.15 |
0.0703 |
1037.108 |
308.15 |
0.0796 |
1041.293 |
308.15 |
0.0897 |
1045.448 |
308.15 |
0.1004 |
1049.659 |
308.15 |
0.1507 |
1065.271 |
308.15 |
0.1996 |
1075.794 |
308.15 |
0.2467 |
1083.272 |
308.15 |
0.2943 |
1088.253 |
308.15 |
0.3511 |
1092.986 |
308.15 |
0.3995 |
1095.833 |
308.15 |
0.4527 |
1098.237 |
308.15 |
0.5008 |
1099.92 |
308.15 |
0.5449 |
1101.11 |
308.15 |
0.5834 |
1101.985 |
308.15 |
0.6482 |
1103.133 |
308.15 |
0.6982 |
1103.802 |
308.15 |
0.7444 |
1104.328 |
308.15 |
0.7962 |
1104.809 |
308.15 |
0.8401 |
1105.138 |
308.15 |
0.8947 |
1105.494 |
308.15 |
0.9092 |
1105.578 |
308.15 |
0.9190 |
1105.636 |
308.15 |
0.9303 |
1105.678 |
308.15 |
0.9393 |
1105.694 |
308.15 |
0.9473 |
1105.769 |
308.15 |
0.9566 |
1105.82 |
308.15 |
0.9694 |
1105.878 |
308.15 |
0.9801 |
1105.926 |
308.15 |
0.9915 |
1105.973 |
293.15 |
0.0000 |
998.429 |
298.15 |
0.0000 |
997.267 |
303.15 |
0.0000 |
995.867 |
308.15 |
0.0000 |
994.252 |
293.15 |
1.0000 |
1116.733 |
298.15 |
1.0000 |
1113.174 |
303.15 |
1.0000 |
1109.599 |
308.15 |
1.0000 |
1106.013 |
293.15 |
0.0490 |
1032.591 |
293.15 |
0.0992 |
1057.143 |
293.15 |
0.1490 |
1074.037 |
293.15 |
0.1998 |
1085.893 |
293.15 |
0.2490 |
1093.806 |
293.15 |
0.2987 |
1099.437 |
293.15 |
0.3501 |
1103.603 |
293.15 |
0.4007 |
1106.626 |
293.15 |
0.4504 |
1108.903 |
293.15 |
0.4973 |
1110.602 |
293.15 |
0.5530 |
1112.185 |
293.15 |
0.5938 |
1113.094 |
293.15 |
0.6514 |
1114.071 |
293.15 |
0.6864 |
1114.522 |
293.15 |
0.7556 |
1115.186 |
293.15 |
0.7999 |
1115.521 |
293.15 |
0.8525 |
1115.894 |
293.15 |
0.9002 |
1116.233 |
293.15 |
0.9554 |
1116.574 |
298.15 |
0.0490 |
1030.669 |
298.15 |
0.0992 |
1054.615 |
298.15 |
0.1490 |
1071.09 |
298.15 |
0.1998 |
1082.664 |
298.15 |
0.2490 |
1090.405 |
298.15 |
0.2987 |
1095.935 |
298.15 |
0.3501 |
1100.047 |
298.15 |
0.4007 |
1103.049 |
298.15 |
0.4504 |
1105.321 |
298.15 |
0.4973 |
1107.021 |
298.15 |
0.5530 |
1108.607 |
298.15 |
0.5938 |
1109.516 |
298.15 |
0.6514 |
1110.493 |
298.15 |
0.6864 |
1110.943 |
298.15 |
0.7556 |
1111.608 |
298.15 |
0.7999 |
1111.947 |
298.15 |
0.8525 |
1112.329 |
298.15 |
0.9002 |
1112.677 |
298.15 |
0.9554 |
1113.023 |
303.15 |
0.0490 |
1028.576 |
303.15 |
0.0992 |
1051.966 |
303.15 |
0.1490 |
1068.055 |
303.15 |
0.1998 |
1079.366 |
303.15 |
0.2490 |
1086.946 |
303.15 |
0.2987 |
1092.382 |
303.15 |
0.3501 |
1096.446 |
303.15 |
0.4007 |
1099.431 |
303.15 |
0.4504 |
1101.701 |
303.15 |
0.4973 |
1103.405 |
303.15 |
0.5530 |
1104.997 |
303.15 |
0.5938 |
1105.91 |
303.15 |
0.6514 |
1106.888 |
303.15 |
0.6864 |
1107.338 |
303.15 |
0.7556 |
1108.005 |
303.15 |
0.7999 |
1108.346 |
303.15 |
0.8525 |
1108.736 |
303.15 |
0.9002 |
1109.094 |
303.15 |
0.9554 |
1109.446 |
308.15 |
0.0490 |
1026.325 |
308.15 |
0.0992 |
1049.205 |
308.15 |
0.1490 |
1064.938 |
308.15 |
0.1998 |
1076.008 |
308.15 |
0.2490 |
1083.444 |
308.15 |
0.2987 |
1088.798 |
308.15 |
0.3501 |
1092.823 |
308.15 |
0.4007 |
1095.796 |
308.15 |
0.4504 |
1098.068 |
308.15 |
0.4973 |
1099.779 |
308.15 |
0.5530 |
1101.377 |
308.15 |
0.5938 |
1102.291 |
308.15 |
0.6514 |
1103.268 |
308.15 |
0.6864 |
1103.717 |
308.15 |
0.7556 |
1104.385 |
308.15 |
0.7999 |
1104.732 |
308.15 |
0.8525 |
1105.132 |
308.15 |
0.9002 |
1105.502 |
308.15 |
0.9554 |
1105.863 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Molality, mol/kg of Ethanol, 2,2'-oxybis- (1) - Liquid |
Mass density, kg/m3 - Liquid |
293.15 |
0.0985 |
999.65 |
293.15 |
0.1974 |
1001.03 |
293.15 |
0.2950 |
1002.36 |
293.15 |
0.4101 |
1003.86 |
293.15 |
0.5006 |
1004.99 |
303.15 |
0.0985 |
997.07 |
303.15 |
0.1974 |
998.39 |
303.15 |
0.2950 |
999.64 |
303.15 |
0.4101 |
1001.05 |
303.15 |
0.5006 |
1002.15 |
293.15 |
0.0000 |
998.21 |
303.15 |
0.0000 |
995.66 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
98.3 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Molality, mol/kg of Ethanol, 2,2'-oxybis- (1) - Liquid |
Mass density, kg/m3 - Liquid |
278.15 |
0.0511 |
1000.743 |
278.15 |
0.1025 |
1001.52 |
278.15 |
0.2049 |
1003.056 |
278.15 |
0.2972 |
1004.427 |
278.15 |
0.4063 |
1006.029 |
283.15 |
0.0511 |
1000.462 |
283.15 |
0.1025 |
1001.222 |
283.15 |
0.2049 |
1002.721 |
283.15 |
0.2972 |
1004.058 |
283.15 |
0.4063 |
1005.619 |
288.15 |
0.0511 |
999.849 |
288.15 |
0.1025 |
1000.593 |
288.15 |
0.2049 |
1002.061 |
288.15 |
0.2972 |
1003.369 |
288.15 |
0.4063 |
1004.895 |
293.15 |
0.0511 |
998.941 |
293.15 |
0.1025 |
999.67 |
293.15 |
0.2049 |
1001.113 |
293.15 |
0.2972 |
1002.394 |
293.15 |
0.4063 |
1003.891 |
298.15 |
0.0511 |
997.772 |
298.15 |
0.1025 |
998.489 |
298.15 |
0.2049 |
999.907 |
298.15 |
0.2972 |
1001.167 |
298.15 |
0.4063 |
1002.636 |
303.15 |
0.0511 |
996.365 |
303.15 |
0.1025 |
997.071 |
303.15 |
0.2049 |
998.466 |
303.15 |
0.2972 |
999.707 |
303.15 |
0.4063 |
1001.152 |
308.15 |
0.0511 |
994.74 |
308.15 |
0.1025 |
995.437 |
308.15 |
0.2049 |
996.813 |
308.15 |
0.2972 |
998.034 |
308.15 |
0.4063 |
999.457 |
313.15 |
0.0511 |
992.916 |
313.15 |
0.1025 |
993.604 |
313.15 |
0.2049 |
994.96 |
313.15 |
0.2972 |
996.164 |
313.15 |
0.4063 |
997.567 |
318.15 |
0.0511 |
990.905 |
318.15 |
0.1025 |
991.585 |
318.15 |
0.2049 |
992.924 |
318.15 |
0.2972 |
994.112 |
318.15 |
0.4063 |
995.495 |
323.15 |
0.0511 |
988.72 |
323.15 |
0.1025 |
989.393 |
323.15 |
0.2049 |
990.716 |
323.15 |
0.2972 |
991.889 |
323.15 |
0.4063 |
993.254 |
328.15 |
0.0511 |
986.371 |
328.15 |
0.1025 |
987.036 |
328.15 |
0.2049 |
988.343 |
328.15 |
0.2972 |
989.503 |
328.15 |
0.4063 |
990.852 |
333.15 |
0.0511 |
983.864 |
333.15 |
0.1025 |
984.525 |
333.15 |
0.2049 |
985.817 |
333.15 |
0.2972 |
986.963 |
333.15 |
0.4063 |
988.296 |
338.15 |
0.0511 |
981.213 |
338.15 |
0.1025 |
981.866 |
338.15 |
0.2049 |
983.145 |
338.15 |
0.2972 |
984.279 |
338.15 |
0.4063 |
985.595 |
343.15 |
0.0511 |
978.42 |
343.15 |
0.1025 |
979.067 |
343.15 |
0.2049 |
980.331 |
343.15 |
0.2972 |
981.454 |
343.15 |
0.4063 |
982.755 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid |
Mass density, kg/m3 - Liquid |
283.15 |
0.9070 |
1123.135 |
288.15 |
0.9070 |
1119.575 |
293.15 |
0.9070 |
1116.018 |
298.15 |
0.9070 |
1112.454 |
303.15 |
0.9070 |
1108.881 |
308.15 |
0.9070 |
1105.295 |
313.15 |
0.9070 |
1101.695 |
323.15 |
0.9070 |
1094.447 |
333.15 |
0.9070 |
1087.119 |
343.15 |
0.9070 |
1079.71 |
283.15 |
0.9589 |
1123.266 |
288.15 |
0.9589 |
1119.71 |
293.15 |
0.9589 |
1116.151 |
298.15 |
0.9589 |
1112.585 |
303.15 |
0.9589 |
1109.016 |
308.15 |
0.9589 |
1105.431 |
313.15 |
0.9589 |
1101.834 |
323.15 |
0.9589 |
1094.595 |
333.15 |
0.9589 |
1087.278 |
343.15 |
0.9589 |
1079.883 |
283.15 |
0.9698 |
1123.273 |
288.15 |
0.9698 |
1119.716 |
293.15 |
0.9698 |
1116.159 |
298.15 |
0.9698 |
1112.594 |
303.15 |
0.9698 |
1109.025 |
308.15 |
0.9698 |
1105.442 |
313.15 |
0.9698 |
1101.843 |
323.15 |
0.9698 |
1094.603 |
333.15 |
0.9698 |
1087.288 |
343.15 |
0.9698 |
1079.897 |
283.15 |
0.9900 |
1123.325 |
288.15 |
0.9900 |
1119.767 |
293.15 |
0.9900 |
1116.211 |
298.15 |
0.9900 |
1112.649 |
303.15 |
0.9900 |
1109.077 |
308.15 |
0.9900 |
1105.496 |
313.15 |
0.9900 |
1101.9 |
323.15 |
0.9900 |
1094.667 |
333.15 |
0.9900 |
1087.359 |
343.15 |
0.9900 |
1079.973 |
283.15 |
0.9901 |
1123.327 |
288.15 |
0.9901 |
1119.771 |
293.15 |
0.9901 |
1116.213 |
298.15 |
0.9901 |
1112.651 |
303.15 |
0.9901 |
1109.081 |
308.15 |
0.9901 |
1105.498 |
313.15 |
0.9901 |
1101.903 |
323.15 |
0.9901 |
1094.668 |
333.15 |
0.9901 |
1087.356 |
343.15 |
0.9901 |
1079.969 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Molality, mol/kg of Ethanol, 2,2'-oxybis- (1) - Liquid |
Mass density, kg/m3 - Liquid |
288.15 |
0.0985 |
1000.689 |
288.15 |
0.1974 |
1002.06 |
288.15 |
0.2950 |
1003.358 |
288.15 |
0.4101 |
1004.837 |
288.15 |
0.5006 |
1005.961 |
288.15 |
0.6001 |
1007.125 |
288.15 |
0.6996 |
1008.278 |
288.15 |
0.7999 |
1009.393 |
298.15 |
0.0985 |
998.458 |
298.15 |
0.1974 |
999.78 |
298.15 |
0.2950 |
1001.026 |
298.15 |
0.4101 |
1002.49 |
298.15 |
0.5006 |
1003.585 |
298.15 |
0.6001 |
1004.735 |
298.15 |
0.6996 |
1005.827 |
298.15 |
0.7999 |
1006.873 |
308.15 |
0.0985 |
995.44 |
308.15 |
0.1974 |
996.778 |
308.15 |
0.2950 |
998.046 |
308.15 |
0.4101 |
999.471 |
308.15 |
0.5006 |
1000.531 |
308.15 |
0.6001 |
1001.676 |
308.15 |
0.6996 |
1002.761 |
308.15 |
0.7999 |
1003.829 |
318.15 |
0.0985 |
991.758 |
318.15 |
0.1974 |
993.102 |
318.15 |
0.2950 |
994.366 |
318.15 |
0.4101 |
995.788 |
318.15 |
0.5006 |
996.853 |
318.15 |
0.6001 |
997.974 |
318.15 |
0.6996 |
999.056 |
318.15 |
0.7999 |
1000.108 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Molality, mol/kg of Ethanol, 2,2'-oxybis- (1) - Liquid |
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
0.0985 |
293.15 |
999.647 |
0.1974 |
293.15 |
1001.031 |
0.2950 |
293.15 |
1002.356 |
0.4101 |
293.15 |
1003.859 |
0.5006 |
293.15 |
1004.993 |
0.0985 |
298.15 |
998.458 |
0.1974 |
298.15 |
999.78 |
0.2950 |
298.15 |
1001.026 |
0.4101 |
298.15 |
1002.49 |
0.5006 |
298.15 |
1003.585 |
0.0985 |
303.15 |
997.071 |
0.1974 |
303.15 |
998.395 |
0.2950 |
303.15 |
999.643 |
0.4101 |
303.15 |
1001.051 |
0.5006 |
303.15 |
1002.146 |
0.0985 |
308.15 |
995.44 |
0.1974 |
308.15 |
996.778 |
0.2950 |
308.15 |
998.046 |
0.4101 |
308.15 |
999.471 |
0.5006 |
308.15 |
1000.531 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid |
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
0.2500 |
294.25 |
1095.0 |
0.2500 |
313.05 |
1081.0 |
0.2500 |
333.05 |
1066.0 |
0.2500 |
353.15 |
1051.0 |
0.2500 |
381.45 |
1027.0 |
0.2500 |
392.75 |
1017.0 |
0.2500 |
409.25 |
1004.0 |
0.2500 |
426.35 |
987.6 |
0.2500 |
441.65 |
973.3 |
0.5000 |
293.45 |
1111.0 |
0.5000 |
312.95 |
1097.0 |
0.5000 |
332.95 |
1082.0 |
0.5000 |
352.95 |
1066.0 |
0.5000 |
380.05 |
1043.0 |
0.5000 |
390.25 |
1035.0 |
0.5000 |
405.35 |
1023.0 |
0.5000 |
424.25 |
1006.0 |
0.5000 |
443.05 |
988.2 |
0.7500 |
294.05 |
1115.0 |
0.7500 |
313.05 |
1101.0 |
0.7500 |
333.05 |
1087.0 |
0.7500 |
353.05 |
1071.0 |
0.7500 |
382.55 |
1048.0 |
0.7500 |
390.95 |
1042.0 |
0.7500 |
406.95 |
1029.0 |
0.7500 |
424.65 |
1014.0 |
0.7500 |
443.65 |
996.3 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid |
Mass density, kg/m3 - Liquid |
303.15 |
0.0000 |
995.6 |
303.15 |
0.0501 |
1028.38 |
303.15 |
0.1016 |
1051.83 |
303.15 |
0.1512 |
1067.99 |
303.15 |
0.2012 |
1078.71 |
303.15 |
0.2477 |
1086.55 |
303.15 |
0.2980 |
1092.27 |
303.15 |
0.3505 |
1096.22 |
303.15 |
0.4483 |
1101.17 |
303.15 |
0.5421 |
1103.74 |
303.15 |
0.6518 |
1106.25 |
303.15 |
0.7525 |
1107.78 |
303.15 |
0.7864 |
1107.94 |
303.15 |
0.8499 |
1108.55 |
303.15 |
0.9005 |
1108.84 |
303.15 |
0.9503 |
1109.66 |
303.15 |
1.0000 |
1109.48 |
308.15 |
0.0000 |
994.12 |
308.15 |
0.0501 |
1026.09 |
308.15 |
0.1016 |
1048.94 |
308.15 |
0.1512 |
1065.34 |
308.15 |
0.2012 |
1075.25 |
308.15 |
0.2477 |
1082.95 |
308.15 |
0.2980 |
1088.52 |
308.15 |
0.3505 |
1092.42 |
308.15 |
0.4483 |
1097.58 |
308.15 |
0.5421 |
1100.11 |
308.15 |
0.6518 |
1102.58 |
308.15 |
0.7525 |
1103.95 |
308.15 |
0.7864 |
1104.26 |
308.15 |
0.8499 |
1104.93 |
308.15 |
0.9005 |
1105.16 |
308.15 |
0.9503 |
1105.58 |
308.15 |
1.0000 |
1105.72 |
313.15 |
0.0000 |
992.25 |
313.15 |
0.0501 |
1023.67 |
313.15 |
0.1016 |
1046.02 |
313.15 |
0.1512 |
1062.04 |
313.15 |
0.2012 |
1071.77 |
313.15 |
0.2477 |
1079.42 |
313.15 |
0.2980 |
1084.97 |
313.15 |
0.3505 |
1088.68 |
313.15 |
0.4483 |
1093.68 |
313.15 |
0.5421 |
1096.37 |
313.15 |
0.6518 |
1098.97 |
313.15 |
0.7525 |
1100.25 |
313.15 |
0.7864 |
1100.56 |
313.15 |
0.8499 |
1101.32 |
313.15 |
0.9005 |
1101.55 |
313.15 |
0.9503 |
1101.98 |
313.15 |
1.0000 |
1102.11 |
318.15 |
0.0000 |
990.3 |
318.15 |
0.0501 |
1021.08 |
318.15 |
0.1016 |
1043.03 |
318.15 |
0.1512 |
1058.72 |
318.15 |
0.2012 |
1068.24 |
318.15 |
0.2477 |
1075.76 |
318.15 |
0.2980 |
1081.58 |
318.15 |
0.3505 |
1084.97 |
318.15 |
0.4483 |
1089.91 |
318.15 |
0.5421 |
1092.91 |
318.15 |
0.6518 |
1095.29 |
318.15 |
0.7525 |
1096.58 |
318.15 |
0.7864 |
1096.89 |
318.15 |
0.8499 |
1097.62 |
318.15 |
0.9005 |
1097.87 |
318.15 |
0.9503 |
1098.33 |
318.15 |
1.0000 |
1098.35 |
323.15 |
0.0000 |
988.1 |
323.15 |
0.0501 |
1018.36 |
323.15 |
0.1016 |
1039.94 |
323.15 |
0.1512 |
1055.2 |
323.15 |
0.2012 |
1064.5 |
323.15 |
0.2477 |
1072.18 |
323.15 |
0.2980 |
1077.47 |
323.15 |
0.3505 |
1081.16 |
323.15 |
0.4483 |
1086.1 |
323.15 |
0.5421 |
1088.98 |
323.15 |
0.6518 |
1091.34 |
323.15 |
0.7525 |
1093.18 |
323.15 |
0.7864 |
1093.37 |
323.15 |
0.8499 |
1093.91 |
323.15 |
0.9005 |
1094.19 |
323.15 |
0.9503 |
1094.55 |
323.15 |
1.0000 |
1094.94 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid |
Mass density, kg/m3 - Liquid |
283.15 |
0.0000 |
999.7 |
283.15 |
0.0255 |
1019.73 |
283.15 |
0.0565 |
1040.15 |
283.15 |
0.1027 |
1063.34 |
283.15 |
0.1966 |
1091.18 |
283.15 |
0.3010 |
1106.34 |
283.15 |
0.3989 |
1113.62 |
283.15 |
0.5006 |
1117.88 |
283.15 |
0.6011 |
1120.39 |
283.15 |
0.7003 |
1121.98 |
283.15 |
0.8051 |
1123.07 |
283.15 |
0.8920 |
1123.64 |
283.15 |
1.0000 |
1124.24 |
288.15 |
0.0000 |
999.1 |
288.15 |
0.0255 |
1018.61 |
288.15 |
0.0565 |
1038.42 |
288.15 |
0.1027 |
1060.91 |
288.15 |
0.1966 |
1088.01 |
288.15 |
0.3010 |
1102.88 |
288.15 |
0.3989 |
1110.06 |
288.15 |
0.5006 |
1114.29 |
288.15 |
0.6011 |
1116.8 |
288.15 |
0.7003 |
1118.39 |
288.15 |
0.8051 |
1119.47 |
288.15 |
0.8920 |
1120.05 |
288.15 |
1.0000 |
1120.65 |
293.15 |
0.0000 |
998.2 |
293.15 |
0.0255 |
1017.27 |
293.15 |
0.0565 |
1036.53 |
293.15 |
0.1027 |
1058.39 |
293.15 |
0.1966 |
1084.81 |
293.15 |
0.3010 |
1099.4 |
293.15 |
0.3989 |
1106.48 |
293.15 |
0.5006 |
1110.68 |
293.15 |
0.6011 |
1113.19 |
293.15 |
0.7003 |
1114.79 |
293.15 |
0.8051 |
1115.87 |
293.15 |
0.8920 |
1116.45 |
293.15 |
1.0000 |
1117.05 |
298.15 |
0.0000 |
997.04 |
298.15 |
0.0255 |
1015.72 |
298.15 |
0.0565 |
1034.5 |
298.15 |
0.1027 |
1055.77 |
298.15 |
0.1966 |
1081.56 |
298.15 |
0.3010 |
1095.89 |
298.15 |
0.3989 |
1102.89 |
298.15 |
0.5006 |
1107.07 |
298.15 |
0.6011 |
1109.59 |
298.15 |
0.7003 |
1111.19 |
298.15 |
0.8051 |
1112.27 |
298.15 |
0.8920 |
1112.86 |
298.15 |
1.0000 |
1113.47 |
303.15 |
0.0000 |
995.55 |
303.15 |
0.0255 |
1013.97 |
303.15 |
0.0565 |
1032.33 |
303.15 |
0.1027 |
1053.07 |
303.15 |
0.1966 |
1078.28 |
303.15 |
0.3010 |
1092.36 |
303.15 |
0.3989 |
1099.29 |
303.15 |
0.5006 |
1103.45 |
303.15 |
0.6011 |
1105.97 |
303.15 |
0.7003 |
1107.58 |
303.15 |
0.8051 |
1108.67 |
303.15 |
0.8920 |
1109.27 |
303.15 |
1.0000 |
1109.88 |
308.15 |
0.0000 |
994.03 |
308.15 |
0.0255 |
1011.83 |
308.15 |
0.0565 |
1030.02 |
308.15 |
0.1027 |
1050.27 |
308.15 |
0.1966 |
1074.94 |
308.15 |
0.3010 |
1088.8 |
308.15 |
0.3989 |
1095.67 |
308.15 |
0.5006 |
1099.82 |
308.15 |
0.6011 |
1102.36 |
308.15 |
0.7003 |
1103.97 |
308.15 |
0.8051 |
1105.06 |
308.15 |
0.8920 |
1105.68 |
308.15 |
1.0000 |
1106.29 |
313.15 |
0.0000 |
992.21 |
313.15 |
0.0255 |
1009.99 |
313.15 |
0.0565 |
1027.57 |
313.15 |
0.1027 |
1047.39 |
313.15 |
0.1966 |
1071.56 |
313.15 |
0.3010 |
1085.22 |
313.15 |
0.3989 |
1092.03 |
313.15 |
0.5006 |
1096.18 |
313.15 |
0.6011 |
1098.73 |
313.15 |
0.7003 |
1100.35 |
313.15 |
0.8051 |
1101.45 |
313.15 |
0.8920 |
1102.09 |
313.15 |
1.0000 |
1102.7 |
318.15 |
0.0000 |
990.21 |
318.15 |
0.0255 |
1007.73 |
318.15 |
0.0565 |
1025.01 |
318.15 |
0.1027 |
1044.41 |
318.15 |
0.1966 |
1068.13 |
318.15 |
0.3010 |
1081.61 |
318.15 |
0.3989 |
1088.37 |
318.15 |
0.5006 |
1092.53 |
318.15 |
0.6011 |
1095.08 |
318.15 |
0.7003 |
1096.71 |
318.15 |
0.8051 |
1097.83 |
318.15 |
0.8920 |
1098.49 |
318.15 |
1.0000 |
1099.11 |
323.15 |
0.0000 |
988.03 |
323.15 |
0.0255 |
1005.37 |
323.15 |
0.0565 |
1022.33 |
323.15 |
0.1027 |
1041.36 |
323.15 |
0.1966 |
1064.65 |
323.15 |
0.3010 |
1077.97 |
323.15 |
0.3989 |
1084.69 |
323.15 |
0.5006 |
1088.85 |
323.15 |
0.6011 |
1091.42 |
323.15 |
0.7003 |
1093.07 |
323.15 |
0.8051 |
1094.21 |
323.15 |
0.8920 |
1094.88 |
323.15 |
1.0000 |
1095.51 |
328.15 |
0.0000 |
985.69 |
328.15 |
0.0255 |
1002.86 |
328.15 |
0.0565 |
1019.53 |
328.15 |
0.1027 |
1038.21 |
328.15 |
0.1966 |
1061.13 |
328.15 |
0.3010 |
1074.29 |
328.15 |
0.3989 |
1080.98 |
328.15 |
0.5006 |
1085.16 |
328.15 |
0.6011 |
1087.74 |
328.15 |
0.7003 |
1089.41 |
328.15 |
0.8051 |
1090.57 |
328.15 |
0.8920 |
1091.26 |
328.15 |
1.0000 |
1091.91 |
333.15 |
0.0000 |
983.19 |
333.15 |
0.0255 |
1000.22 |
333.15 |
0.0565 |
1016.62 |
333.15 |
0.1027 |
1034.99 |
333.15 |
0.1966 |
1057.55 |
333.15 |
0.3010 |
1070.58 |
333.15 |
0.3989 |
1077.25 |
333.15 |
0.5006 |
1081.43 |
333.15 |
0.6011 |
1084.04 |
333.15 |
0.7003 |
1085.74 |
333.15 |
0.8051 |
1086.93 |
333.15 |
0.8920 |
1087.63 |
333.15 |
1.0000 |
1088.3 |
338.15 |
0.0000 |
980.55 |
338.15 |
0.0255 |
997.46 |
338.15 |
0.0565 |
1013.61 |
338.15 |
0.1027 |
1031.68 |
338.15 |
0.1966 |
1053.92 |
338.15 |
0.3010 |
1066.84 |
338.15 |
0.3989 |
1073.49 |
338.15 |
0.5006 |
1077.69 |
338.15 |
0.6011 |
1080.33 |
338.15 |
0.7003 |
1082.06 |
338.15 |
0.8051 |
1083.27 |
338.15 |
0.8920 |
1083.99 |
338.15 |
1.0000 |
1084.68 |
343.15 |
0.0000 |
977.76 |
343.15 |
0.0255 |
994.57 |
343.15 |
0.0565 |
1010.51 |
343.15 |
0.1027 |
1028.29 |
343.15 |
0.1966 |
1050.24 |
343.15 |
0.3010 |
1063.06 |
343.15 |
0.3989 |
1069.69 |
343.15 |
0.5006 |
1073.93 |
343.15 |
0.6011 |
1076.59 |
343.15 |
0.7003 |
1078.36 |
343.15 |
0.8051 |
1079.6 |
343.15 |
0.8920 |
1080.34 |
343.15 |
1.0000 |
1081.05 |
348.15 |
0.0000 |
974.84 |
348.15 |
0.0255 |
991.57 |
348.15 |
0.0565 |
1007.27 |
348.15 |
0.1027 |
1024.84 |
348.15 |
0.1966 |
1046.51 |
348.15 |
0.3010 |
1059.24 |
348.15 |
0.3989 |
1065.88 |
348.15 |
0.5006 |
1070.14 |
348.15 |
0.6011 |
1072.84 |
348.15 |
0.7003 |
1074.63 |
348.15 |
0.8051 |
1075.91 |
348.15 |
0.8920 |
1076.67 |
348.15 |
1.0000 |
1077.4 |
353.15 |
0.0000 |
971.79 |
353.15 |
0.0255 |
988.5 |
353.15 |
0.0565 |
1004.07 |
353.15 |
0.1027 |
1021.3 |
353.15 |
0.1966 |
1042.72 |
353.15 |
0.3010 |
1055.38 |
353.15 |
0.3989 |
1062.02 |
353.15 |
0.5006 |
1066.32 |
353.15 |
0.6011 |
1069.05 |
353.15 |
0.7003 |
1070.89 |
353.15 |
0.8051 |
1072.2 |
353.15 |
0.8920 |
1072.99 |
353.15 |
1.0000 |
1073.74 |
Speed of sound, m/s
[ref]
Operational conditions:
- Pressure, kPa = 92.3 (Liquid)
- Frequency, MHz = 3 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid |
Speed of sound, m/s - Liquid |
293.15 |
0.0097 |
1511.15 |
293.15 |
0.0201 |
1539.56 |
293.15 |
0.0297 |
1563.59 |
293.15 |
0.0397 |
1586.15 |
293.15 |
0.0502 |
1607.67 |
293.15 |
0.0591 |
1623.95 |
293.15 |
0.0703 |
1642.55 |
293.15 |
0.0796 |
1655.49 |
293.15 |
0.0897 |
1667.88 |
293.15 |
0.1004 |
1679.66 |
293.15 |
0.1507 |
1713.04 |
293.15 |
0.1996 |
1723.89 |
293.15 |
0.2467 |
1723.01 |
293.15 |
0.2943 |
1716.57 |
293.15 |
0.3511 |
1705.08 |
293.15 |
0.3995 |
1694.05 |
293.15 |
0.4527 |
1681.69 |
293.15 |
0.5008 |
1670.71 |
293.15 |
0.5449 |
1661.45 |
293.15 |
0.5834 |
1653.41 |
293.15 |
0.6482 |
1640.67 |
293.15 |
0.6982 |
1632.2 |
293.15 |
0.7444 |
1624.39 |
293.15 |
0.7962 |
1616.66 |
293.15 |
0.8401 |
1610.38 |
293.15 |
0.8947 |
1603.32 |
293.15 |
0.9092 |
1601.45 |
293.15 |
0.9190 |
1600.23 |
293.15 |
0.9303 |
1599.06 |
293.15 |
0.9393 |
1598.01 |
293.15 |
0.9473 |
1597.15 |
293.15 |
0.9566 |
1595.98 |
293.15 |
0.9694 |
1594.59 |
293.15 |
0.9801 |
1593.4 |
293.15 |
0.9915 |
1592.14 |
298.15 |
0.0097 |
1522.97 |
298.15 |
0.0201 |
1549.09 |
298.15 |
0.0297 |
1571.11 |
298.15 |
0.0397 |
1591.7 |
298.15 |
0.0502 |
1611.33 |
298.15 |
0.0591 |
1626.12 |
298.15 |
0.0703 |
1643.04 |
298.15 |
0.0796 |
1654.71 |
298.15 |
0.0897 |
1665.88 |
298.15 |
0.1004 |
1676.48 |
298.15 |
0.1507 |
1705.92 |
298.15 |
0.1996 |
1714.67 |
298.15 |
0.2467 |
1712.57 |
298.15 |
0.2943 |
1705.45 |
298.15 |
0.3511 |
1693.48 |
298.15 |
0.3995 |
1682.2 |
298.15 |
0.4527 |
1669.76 |
298.15 |
0.5008 |
1658.74 |
298.15 |
0.5449 |
1649.42 |
298.15 |
0.5834 |
1641.4 |
298.15 |
0.6482 |
1628.68 |
298.15 |
0.6982 |
1620.25 |
298.15 |
0.7444 |
1612.47 |
298.15 |
0.7962 |
1604.75 |
298.15 |
0.8401 |
1598.51 |
298.15 |
0.8947 |
1591.46 |
298.15 |
0.9092 |
1589.6 |
298.15 |
0.9190 |
1588.38 |
298.15 |
0.9303 |
1587.24 |
298.15 |
0.9393 |
1586.16 |
298.15 |
0.9473 |
1585.29 |
298.15 |
0.9566 |
1584.12 |
298.15 |
0.9694 |
1582.74 |
298.15 |
0.9801 |
1581.55 |
298.15 |
0.9915 |
1580.29 |
303.15 |
0.0097 |
1533.23 |
303.15 |
0.0201 |
1557.23 |
303.15 |
0.0297 |
1577.38 |
303.15 |
0.0397 |
1596.13 |
303.15 |
0.0502 |
1614.02 |
303.15 |
0.0591 |
1627.38 |
303.15 |
0.0703 |
1642.71 |
303.15 |
0.0796 |
1653.19 |
303.15 |
0.0897 |
1663.2 |
303.15 |
0.1004 |
1672.68 |
303.15 |
0.1507 |
1698.47 |
303.15 |
0.1996 |
1705.09 |
303.15 |
0.2467 |
1701.82 |
303.15 |
0.2943 |
1694.07 |
303.15 |
0.3511 |
1681.7 |
303.15 |
0.3995 |
1670.2 |
303.15 |
0.4527 |
1657.65 |
303.15 |
0.5008 |
1646.57 |
303.15 |
0.5449 |
1637.26 |
303.15 |
0.5834 |
1629.22 |
303.15 |
0.6482 |
1616.58 |
303.15 |
0.6982 |
1608.12 |
303.15 |
0.7444 |
1600.43 |
303.15 |
0.7962 |
1592.72 |
303.15 |
0.8401 |
1586.58 |
303.15 |
0.8947 |
1579.52 |
303.15 |
0.9092 |
1577.65 |
303.15 |
0.9190 |
1576.47 |
303.15 |
0.9303 |
1575.31 |
303.15 |
0.9393 |
1574.27 |
303.15 |
0.9473 |
1573.35 |
303.15 |
0.9566 |
1572.17 |
303.15 |
0.9694 |
1570.82 |
303.15 |
0.9801 |
1569.62 |
303.15 |
0.9915 |
1568.35 |
308.15 |
0.0097 |
1541.96 |
308.15 |
0.0201 |
1563.99 |
308.15 |
0.0297 |
1582.41 |
308.15 |
0.0397 |
1599.44 |
308.15 |
0.0502 |
1615.66 |
308.15 |
0.0591 |
1627.75 |
308.15 |
0.0703 |
1641.6 |
308.15 |
0.0796 |
1650.94 |
308.15 |
0.0897 |
1659.89 |
308.15 |
0.1004 |
1668.31 |
308.15 |
0.1507 |
1690.55 |
308.15 |
0.1996 |
1695.23 |
308.15 |
0.2467 |
1690.86 |
308.15 |
0.2943 |
1682.5 |
308.15 |
0.3511 |
1669.71 |
308.15 |
0.3995 |
1658.05 |
308.15 |
0.4527 |
1645.42 |
308.15 |
0.5008 |
1634.33 |
308.15 |
0.5449 |
1625.03 |
308.15 |
0.5834 |
1617.03 |
308.15 |
0.6482 |
1604.4 |
308.15 |
0.6982 |
1596.02 |
308.15 |
0.7444 |
1588.33 |
308.15 |
0.7962 |
1580.66 |
308.15 |
0.8401 |
1574.51 |
308.15 |
0.8947 |
1567.53 |
308.15 |
0.9092 |
1565.66 |
308.15 |
0.9190 |
1564.48 |
308.15 |
0.9303 |
1563.32 |
308.15 |
0.9393 |
1562.29 |
308.15 |
0.9473 |
1561.39 |
308.15 |
0.9566 |
1560.2 |
308.15 |
0.9694 |
1558.86 |
308.15 |
0.9801 |
1557.66 |
308.15 |
0.9915 |
1556.4 |
293.15 |
0.0000 |
1482.78 |
298.15 |
0.0000 |
1496.99 |
303.15 |
0.0000 |
1509.32 |
308.15 |
0.0000 |
1519.89 |
293.15 |
1.0000 |
1591.03 |
298.15 |
1.0000 |
1579.13 |
303.15 |
1.0000 |
1567.21 |
308.15 |
1.0000 |
1555.26 |
Speed of sound, m/s
[ref]
Operational conditions:
- Pressure, kPa = 100 (Liquid)
- Frequency, MHz = 3 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Molality, mol/kg of Ethanol, 2,2'-oxybis- (1) - Liquid |
Speed of sound, m/s - Liquid |
293.15 |
0.0985 |
1487.7 |
293.15 |
0.1974 |
1493.1 |
293.15 |
0.2950 |
1498.1 |
293.15 |
0.4101 |
1504.1 |
293.15 |
0.5006 |
1508.3 |
303.15 |
0.0985 |
1513.1 |
303.15 |
0.1974 |
1517.6 |
303.15 |
0.2950 |
1522.0 |
303.15 |
0.4101 |
1526.9 |
303.15 |
0.5006 |
1530.6 |
293.15 |
0.0000 |
1482.3 |
303.15 |
0.0000 |
1508.5 |
Speed of sound, m/s
[ref]
Operational condition: Pressure, kPa =
98.3 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Molality, mol/kg of Ethanol, 2,2'-oxybis- (1) - Liquid |
Speed of sound, m/s - Liquid |
278.15 |
0.0511 |
1430.06 |
278.15 |
0.1025 |
1433.67 |
278.15 |
0.2049 |
1440.62 |
278.15 |
0.2972 |
1446.92 |
278.15 |
0.4063 |
1454.36 |
283.15 |
0.0511 |
1450.72 |
283.15 |
0.1025 |
1454.05 |
283.15 |
0.2049 |
1460.39 |
283.15 |
0.2972 |
1466.18 |
283.15 |
0.4063 |
1472.97 |
288.15 |
0.0511 |
1469.07 |
288.15 |
0.1025 |
1472.12 |
288.15 |
0.2049 |
1478.02 |
288.15 |
0.2972 |
1483.3 |
288.15 |
0.4063 |
1489.53 |
293.15 |
0.0511 |
1485.2 |
293.15 |
0.1025 |
1488.04 |
293.15 |
0.2049 |
1493.47 |
293.15 |
0.2972 |
1498.43 |
293.15 |
0.4063 |
1504.05 |
298.15 |
0.0511 |
1499.38 |
298.15 |
0.1025 |
1501.98 |
298.15 |
0.2049 |
1507.01 |
298.15 |
0.2972 |
1511.53 |
298.15 |
0.4063 |
1516.73 |
303.15 |
0.0511 |
1511.66 |
303.15 |
0.1025 |
1514.06 |
303.15 |
0.2049 |
1518.71 |
303.15 |
0.2972 |
1522.85 |
303.15 |
0.4063 |
1527.63 |
308.15 |
0.0511 |
1522.21 |
308.15 |
0.1025 |
1524.41 |
308.15 |
0.2049 |
1528.68 |
308.15 |
0.2972 |
1532.49 |
308.15 |
0.4063 |
1536.91 |
313.15 |
0.0511 |
1531.13 |
313.15 |
0.1025 |
1533.15 |
313.15 |
0.2049 |
1537.1 |
313.15 |
0.2972 |
1540.62 |
313.15 |
0.4063 |
1544.69 |
318.15 |
0.0511 |
1538.56 |
318.15 |
0.1025 |
1540.43 |
318.15 |
0.2049 |
1544.07 |
318.15 |
0.2972 |
1547.3 |
318.15 |
0.4063 |
1551.01 |
323.15 |
0.0511 |
1544.58 |
323.15 |
0.1025 |
1546.3 |
323.15 |
0.2049 |
1549.63 |
323.15 |
0.2972 |
1552.58 |
323.15 |
0.4063 |
1555.99 |
328.15 |
0.0511 |
1549.27 |
328.15 |
0.1025 |
1550.84 |
328.15 |
0.2049 |
1553.89 |
328.15 |
0.2972 |
1556.58 |
328.15 |
0.4063 |
1559.7 |
333.15 |
0.0511 |
1552.73 |
333.15 |
0.1025 |
1554.17 |
333.15 |
0.2049 |
1556.94 |
333.15 |
0.2972 |
1559.4 |
333.15 |
0.4063 |
1562.24 |
338.15 |
0.0511 |
1555.04 |
338.15 |
0.1025 |
1556.35 |
338.15 |
0.2049 |
1558.86 |
338.15 |
0.2972 |
1561.09 |
338.15 |
0.4063 |
1563.66 |
343.15 |
0.0511 |
1556.26 |
343.15 |
0.1025 |
1557.44 |
343.15 |
0.2049 |
1559.73 |
343.15 |
0.2972 |
1561.73 |
343.15 |
0.4063 |
1564.05 |
Speed of sound, m/s
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid |
Speed of sound, m/s - Liquid |
283.15 |
0.9070 |
1620.3 |
288.15 |
0.9070 |
1608.0 |
293.15 |
0.9070 |
1595.9 |
298.15 |
0.9070 |
1583.8 |
303.15 |
0.9070 |
1571.7 |
308.15 |
0.9070 |
1559.6 |
313.15 |
0.9070 |
1547.5 |
323.15 |
0.9070 |
1523.4 |
333.15 |
0.9070 |
1499.0 |
343.15 |
0.9070 |
1474.6 |
283.15 |
0.9589 |
1617.8 |
288.15 |
0.9589 |
1605.5 |
293.15 |
0.9589 |
1593.3 |
298.15 |
0.9589 |
1581.0 |
303.15 |
0.9589 |
1569.0 |
308.15 |
0.9589 |
1557.0 |
313.15 |
0.9589 |
1545.0 |
323.15 |
0.9589 |
1520.9 |
333.15 |
0.9589 |
1496.6 |
343.15 |
0.9589 |
1472.2 |
283.15 |
0.9698 |
1617.4 |
288.15 |
0.9698 |
1605.2 |
293.15 |
0.9698 |
1593.0 |
298.15 |
0.9698 |
1580.8 |
303.15 |
0.9698 |
1568.6 |
308.15 |
0.9698 |
1556.6 |
313.15 |
0.9698 |
1544.6 |
323.15 |
0.9698 |
1520.5 |
333.15 |
0.9698 |
1496.2 |
343.15 |
0.9698 |
1471.8 |
283.15 |
0.9900 |
1616.4 |
288.15 |
0.9900 |
1604.1 |
293.15 |
0.9900 |
1591.9 |
298.15 |
0.9900 |
1579.6 |
303.15 |
0.9900 |
1567.5 |
308.15 |
0.9900 |
1555.4 |
313.15 |
0.9900 |
1543.4 |
323.15 |
0.9900 |
1519.3 |
333.15 |
0.9900 |
1495.1 |
343.15 |
0.9900 |
1470.8 |
283.15 |
0.9901 |
1616.5 |
288.15 |
0.9901 |
1604.2 |
293.15 |
0.9901 |
1592.0 |
298.15 |
0.9901 |
1579.8 |
303.15 |
0.9901 |
1567.4 |
308.15 |
0.9901 |
1555.4 |
313.15 |
0.9901 |
1543.3 |
323.15 |
0.9901 |
1519.2 |
333.15 |
0.9901 |
1494.9 |
343.15 |
0.9901 |
1470.5 |
Speed of sound, m/s
[ref]
Operational conditions:
- Pressure, kPa = 100 (Liquid)
- Frequency, MHz = 3 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Molality, mol/kg of Ethanol, 2,2'-oxybis- (1) - Liquid |
Speed of sound, m/s - Liquid |
288.15 |
0.0985 |
1472.11 |
288.15 |
0.1974 |
1478.01 |
288.15 |
0.2950 |
1483.78 |
288.15 |
0.4101 |
1489.36 |
288.15 |
0.5006 |
1494.73 |
288.15 |
0.6001 |
1500.28 |
288.15 |
0.6996 |
1505.69 |
288.15 |
0.7999 |
1510.78 |
298.15 |
0.0985 |
1501.24 |
298.15 |
0.1974 |
1506.01 |
298.15 |
0.2950 |
1510.78 |
298.15 |
0.4101 |
1516.15 |
298.15 |
0.5006 |
1520.34 |
298.15 |
0.6001 |
1527.06 |
298.15 |
0.6996 |
1534.55 |
298.15 |
0.7999 |
1540.32 |
308.15 |
0.0985 |
1523.52 |
308.15 |
0.1974 |
1527.52 |
308.15 |
0.2950 |
1531.47 |
308.15 |
0.4101 |
1536.11 |
308.15 |
0.5006 |
1541.59 |
308.15 |
0.6001 |
1549.18 |
308.15 |
0.6996 |
1556.59 |
308.15 |
0.7999 |
1562.29 |
318.15 |
0.0985 |
1541.59 |
318.15 |
0.1974 |
1547.17 |
318.15 |
0.2950 |
1552.68 |
318.15 |
0.4101 |
1558.07 |
318.15 |
0.5006 |
1563.21 |
318.15 |
0.6001 |
1568.76 |
318.15 |
0.6996 |
1573.92 |
318.15 |
0.7999 |
1579.48 |
Speed of sound, m/s
[ref]
Operational conditions:
- Pressure, kPa = 100 (Liquid)
- Frequency, MHz = 3 (Liquid)
Fixed |
Measured |
Molality, mol/kg of Ethanol, 2,2'-oxybis- (1) - Liquid |
Temperature, K - Liquid |
Speed of sound, m/s - Liquid |
0.0985 |
293.15 |
1487.65 |
0.1974 |
293.15 |
1493.09 |
0.2950 |
293.15 |
1498.14 |
0.4101 |
293.15 |
1504.13 |
0.5006 |
293.15 |
1508.33 |
0.0985 |
298.15 |
1501.24 |
0.1974 |
298.15 |
1506.01 |
0.2950 |
298.15 |
1510.78 |
0.4101 |
298.15 |
1516.15 |
0.5006 |
298.15 |
1520.34 |
0.0985 |
303.15 |
1513.09 |
0.1974 |
303.15 |
1517.58 |
0.2950 |
303.15 |
1521.95 |
0.4101 |
303.15 |
1526.88 |
0.5006 |
303.15 |
1530.64 |
0.0985 |
308.15 |
1523.52 |
0.1974 |
308.15 |
1527.52 |
0.2950 |
308.15 |
1531.47 |
0.4101 |
308.15 |
1536.11 |
0.5006 |
308.15 |
1539.59 |
Speed of sound, m/s
[ref]
Operational conditions:
- Pressure, kPa = 92.3 (Liquid)
- Frequency, MHz = 3 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid |
Speed of sound, m/s - Liquid |
293.15 |
0.0097 |
1511.15 |
293.15 |
0.0201 |
1539.56 |
293.15 |
0.0297 |
1563.59 |
293.15 |
0.0397 |
1586.15 |
293.15 |
0.0502 |
1607.67 |
293.15 |
0.0591 |
1623.95 |
293.15 |
0.0703 |
1642.55 |
293.15 |
0.0796 |
1655.49 |
293.15 |
0.0897 |
1667.88 |
293.15 |
0.1004 |
1679.66 |
293.15 |
0.1507 |
1713.04 |
293.15 |
0.1996 |
1723.89 |
293.15 |
0.2467 |
1723.01 |
293.15 |
0.2943 |
1716.57 |
293.15 |
0.3511 |
1705.08 |
293.15 |
0.3995 |
1694.05 |
293.15 |
0.4527 |
1681.69 |
293.15 |
0.5008 |
1670.71 |
293.15 |
0.5449 |
1661.45 |
293.15 |
0.5834 |
1653.41 |
293.15 |
0.6482 |
1640.67 |
293.15 |
0.6982 |
1632.2 |
293.15 |
0.7444 |
1624.39 |
293.15 |
0.7962 |
1616.66 |
293.15 |
0.8401 |
1610.38 |
293.15 |
0.8947 |
1603.32 |
293.15 |
0.9092 |
1601.45 |
293.15 |
0.9190 |
1600.23 |
293.15 |
0.9303 |
1599.06 |
293.15 |
0.9393 |
1598.01 |
293.15 |
0.9473 |
1597.15 |
293.15 |
0.9566 |
1595.98 |
293.15 |
0.9694 |
1594.59 |
293.15 |
0.9801 |
1593.4 |
293.15 |
0.9915 |
1592.14 |
298.15 |
0.0097 |
1522.97 |
298.15 |
0.0201 |
1549.09 |
298.15 |
0.0297 |
1571.11 |
298.15 |
0.0397 |
1591.7 |
298.15 |
0.0502 |
1611.33 |
298.15 |
0.0591 |
1626.12 |
298.15 |
0.0703 |
1643.04 |
298.15 |
0.0796 |
1654.71 |
298.15 |
0.0897 |
1665.88 |
298.15 |
0.1004 |
1676.48 |
298.15 |
0.1507 |
1705.92 |
298.15 |
0.1996 |
1714.67 |
298.15 |
0.2467 |
1712.57 |
298.15 |
0.2943 |
1705.45 |
298.15 |
0.3511 |
1693.48 |
298.15 |
0.3995 |
1682.2 |
298.15 |
0.4527 |
1669.76 |
298.15 |
0.5008 |
1658.74 |
298.15 |
0.5449 |
1649.42 |
298.15 |
0.5834 |
1641.4 |
298.15 |
0.6482 |
1628.68 |
298.15 |
0.6982 |
1620.25 |
298.15 |
0.7444 |
1612.47 |
298.15 |
0.7962 |
1604.75 |
298.15 |
0.8401 |
1598.51 |
298.15 |
0.8947 |
1591.46 |
298.15 |
0.9092 |
1589.6 |
298.15 |
0.9190 |
1588.38 |
298.15 |
0.9303 |
1587.24 |
298.15 |
0.9393 |
1586.16 |
298.15 |
0.9473 |
1585.29 |
298.15 |
0.9566 |
1584.12 |
298.15 |
0.9694 |
1582.74 |
298.15 |
0.9801 |
1581.55 |
298.15 |
0.9915 |
1580.29 |
303.15 |
0.0097 |
1533.23 |
303.15 |
0.0201 |
1557.23 |
303.15 |
0.0297 |
1577.38 |
303.15 |
0.0397 |
1596.13 |
303.15 |
0.0502 |
1614.02 |
303.15 |
0.0591 |
1627.38 |
303.15 |
0.0703 |
1642.71 |
303.15 |
0.0796 |
1653.19 |
303.15 |
0.0897 |
1663.2 |
303.15 |
0.1004 |
1672.68 |
303.15 |
0.1507 |
1698.47 |
303.15 |
0.1996 |
1705.09 |
303.15 |
0.2467 |
1701.82 |
303.15 |
0.2943 |
1694.07 |
303.15 |
0.3511 |
1681.7 |
303.15 |
0.3995 |
1670.2 |
303.15 |
0.4527 |
1657.65 |
303.15 |
0.5008 |
1646.57 |
303.15 |
0.5449 |
1637.26 |
303.15 |
0.5834 |
1629.22 |
303.15 |
0.6482 |
1616.58 |
303.15 |
0.6982 |
1608.12 |
303.15 |
0.7444 |
1600.43 |
303.15 |
0.7962 |
1592.72 |
303.15 |
0.8401 |
1586.58 |
303.15 |
0.8947 |
1579.52 |
303.15 |
0.9092 |
1577.65 |
303.15 |
0.9190 |
1576.47 |
303.15 |
0.9303 |
1575.31 |
303.15 |
0.9393 |
1574.27 |
303.15 |
0.9473 |
1573.35 |
303.15 |
0.9566 |
1572.17 |
303.15 |
0.9694 |
1570.82 |
303.15 |
0.9801 |
1569.62 |
303.15 |
0.9915 |
1568.35 |
308.15 |
0.0097 |
1541.96 |
308.15 |
0.0201 |
1563.99 |
308.15 |
0.0297 |
1582.41 |
308.15 |
0.0397 |
1599.44 |
308.15 |
0.0502 |
1615.66 |
308.15 |
0.0591 |
1627.75 |
308.15 |
0.0703 |
1641.6 |
308.15 |
0.0796 |
1650.94 |
308.15 |
0.0897 |
1659.89 |
308.15 |
0.1004 |
1668.31 |
308.15 |
0.1507 |
1690.55 |
308.15 |
0.1996 |
1695.23 |
308.15 |
0.2467 |
1690.86 |
308.15 |
0.2943 |
1682.5 |
308.15 |
0.3511 |
1669.71 |
308.15 |
0.3995 |
1658.05 |
308.15 |
0.4527 |
1645.42 |
308.15 |
0.5008 |
1634.33 |
308.15 |
0.5449 |
1625.03 |
308.15 |
0.5834 |
1617.03 |
308.15 |
0.6482 |
1604.4 |
308.15 |
0.6982 |
1596.02 |
308.15 |
0.7444 |
1588.33 |
308.15 |
0.7962 |
1580.66 |
308.15 |
0.8401 |
1574.51 |
308.15 |
0.8947 |
1567.53 |
308.15 |
0.9092 |
1565.66 |
308.15 |
0.9190 |
1564.48 |
308.15 |
0.9303 |
1563.32 |
308.15 |
0.9393 |
1562.29 |
308.15 |
0.9473 |
1561.39 |
308.15 |
0.9566 |
1560.2 |
308.15 |
0.9694 |
1558.86 |
308.15 |
0.9801 |
1557.66 |
308.15 |
0.9915 |
1556.4 |
293.15 |
0.0000 |
1482.78 |
298.15 |
0.0000 |
1496.99 |
303.15 |
0.0000 |
1509.32 |
308.15 |
0.0000 |
1519.89 |
293.15 |
1.0000 |
1591.03 |
298.15 |
1.0000 |
1579.13 |
303.15 |
1.0000 |
1567.21 |
308.15 |
1.0000 |
1555.26 |
Speed of sound, m/s
[ref]
Operational conditions:
- Pressure, kPa = 100 (Liquid)
- Frequency, MHz = 3 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Molality, mol/kg of Ethanol, 2,2'-oxybis- (1) - Liquid |
Speed of sound, m/s - Liquid |
293.15 |
0.0985 |
1487.7 |
293.15 |
0.1974 |
1493.1 |
293.15 |
0.2950 |
1498.1 |
293.15 |
0.4101 |
1504.1 |
293.15 |
0.5006 |
1508.3 |
303.15 |
0.0985 |
1513.1 |
303.15 |
0.1974 |
1517.6 |
303.15 |
0.2950 |
1522.0 |
303.15 |
0.4101 |
1526.9 |
303.15 |
0.5006 |
1530.6 |
293.15 |
0.0000 |
1482.3 |
303.15 |
0.0000 |
1508.5 |
Speed of sound, m/s
[ref]
Operational condition: Pressure, kPa =
98.3 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Molality, mol/kg of Ethanol, 2,2'-oxybis- (1) - Liquid |
Speed of sound, m/s - Liquid |
278.15 |
0.0511 |
1430.06 |
278.15 |
0.1025 |
1433.67 |
278.15 |
0.2049 |
1440.62 |
278.15 |
0.2972 |
1446.92 |
278.15 |
0.4063 |
1454.36 |
283.15 |
0.0511 |
1450.72 |
283.15 |
0.1025 |
1454.05 |
283.15 |
0.2049 |
1460.39 |
283.15 |
0.2972 |
1466.18 |
283.15 |
0.4063 |
1472.97 |
288.15 |
0.0511 |
1469.07 |
288.15 |
0.1025 |
1472.12 |
288.15 |
0.2049 |
1478.02 |
288.15 |
0.2972 |
1483.3 |
288.15 |
0.4063 |
1489.53 |
293.15 |
0.0511 |
1485.2 |
293.15 |
0.1025 |
1488.04 |
293.15 |
0.2049 |
1493.47 |
293.15 |
0.2972 |
1498.43 |
293.15 |
0.4063 |
1504.05 |
298.15 |
0.0511 |
1499.38 |
298.15 |
0.1025 |
1501.98 |
298.15 |
0.2049 |
1507.01 |
298.15 |
0.2972 |
1511.53 |
298.15 |
0.4063 |
1516.73 |
303.15 |
0.0511 |
1511.66 |
303.15 |
0.1025 |
1514.06 |
303.15 |
0.2049 |
1518.71 |
303.15 |
0.2972 |
1522.85 |
303.15 |
0.4063 |
1527.63 |
308.15 |
0.0511 |
1522.21 |
308.15 |
0.1025 |
1524.41 |
308.15 |
0.2049 |
1528.68 |
308.15 |
0.2972 |
1532.49 |
308.15 |
0.4063 |
1536.91 |
313.15 |
0.0511 |
1531.13 |
313.15 |
0.1025 |
1533.15 |
313.15 |
0.2049 |
1537.1 |
313.15 |
0.2972 |
1540.62 |
313.15 |
0.4063 |
1544.69 |
318.15 |
0.0511 |
1538.56 |
318.15 |
0.1025 |
1540.43 |
318.15 |
0.2049 |
1544.07 |
318.15 |
0.2972 |
1547.3 |
318.15 |
0.4063 |
1551.01 |
323.15 |
0.0511 |
1544.58 |
323.15 |
0.1025 |
1546.3 |
323.15 |
0.2049 |
1549.63 |
323.15 |
0.2972 |
1552.58 |
323.15 |
0.4063 |
1555.99 |
328.15 |
0.0511 |
1549.27 |
328.15 |
0.1025 |
1550.84 |
328.15 |
0.2049 |
1553.89 |
328.15 |
0.2972 |
1556.58 |
328.15 |
0.4063 |
1559.7 |
333.15 |
0.0511 |
1552.73 |
333.15 |
0.1025 |
1554.17 |
333.15 |
0.2049 |
1556.94 |
333.15 |
0.2972 |
1559.4 |
333.15 |
0.4063 |
1562.24 |
338.15 |
0.0511 |
1555.04 |
338.15 |
0.1025 |
1556.35 |
338.15 |
0.2049 |
1558.86 |
338.15 |
0.2972 |
1561.09 |
338.15 |
0.4063 |
1563.66 |
343.15 |
0.0511 |
1556.26 |
343.15 |
0.1025 |
1557.44 |
343.15 |
0.2049 |
1559.73 |
343.15 |
0.2972 |
1561.73 |
343.15 |
0.4063 |
1564.05 |
Speed of sound, m/s
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid |
Speed of sound, m/s - Liquid |
283.15 |
0.9070 |
1620.3 |
288.15 |
0.9070 |
1608.0 |
293.15 |
0.9070 |
1595.9 |
298.15 |
0.9070 |
1583.8 |
303.15 |
0.9070 |
1571.7 |
308.15 |
0.9070 |
1559.6 |
313.15 |
0.9070 |
1547.5 |
323.15 |
0.9070 |
1523.4 |
333.15 |
0.9070 |
1499.0 |
343.15 |
0.9070 |
1474.6 |
283.15 |
0.9589 |
1617.8 |
288.15 |
0.9589 |
1605.5 |
293.15 |
0.9589 |
1593.3 |
298.15 |
0.9589 |
1581.0 |
303.15 |
0.9589 |
1569.0 |
308.15 |
0.9589 |
1557.0 |
313.15 |
0.9589 |
1545.0 |
323.15 |
0.9589 |
1520.9 |
333.15 |
0.9589 |
1496.6 |
343.15 |
0.9589 |
1472.2 |
283.15 |
0.9698 |
1617.4 |
288.15 |
0.9698 |
1605.2 |
293.15 |
0.9698 |
1593.0 |
298.15 |
0.9698 |
1580.8 |
303.15 |
0.9698 |
1568.6 |
308.15 |
0.9698 |
1556.6 |
313.15 |
0.9698 |
1544.6 |
323.15 |
0.9698 |
1520.5 |
333.15 |
0.9698 |
1496.2 |
343.15 |
0.9698 |
1471.8 |
283.15 |
0.9900 |
1616.4 |
288.15 |
0.9900 |
1604.1 |
293.15 |
0.9900 |
1591.9 |
298.15 |
0.9900 |
1579.6 |
303.15 |
0.9900 |
1567.5 |
308.15 |
0.9900 |
1555.4 |
313.15 |
0.9900 |
1543.4 |
323.15 |
0.9900 |
1519.3 |
333.15 |
0.9900 |
1495.1 |
343.15 |
0.9900 |
1470.8 |
283.15 |
0.9901 |
1616.5 |
288.15 |
0.9901 |
1604.2 |
293.15 |
0.9901 |
1592.0 |
298.15 |
0.9901 |
1579.8 |
303.15 |
0.9901 |
1567.4 |
308.15 |
0.9901 |
1555.4 |
313.15 |
0.9901 |
1543.3 |
323.15 |
0.9901 |
1519.2 |
333.15 |
0.9901 |
1494.9 |
343.15 |
0.9901 |
1470.5 |
Speed of sound, m/s
[ref]
Operational conditions:
- Pressure, kPa = 100 (Liquid)
- Frequency, MHz = 3 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Molality, mol/kg of Ethanol, 2,2'-oxybis- (1) - Liquid |
Speed of sound, m/s - Liquid |
288.15 |
0.0985 |
1472.11 |
288.15 |
0.1974 |
1478.01 |
288.15 |
0.2950 |
1483.78 |
288.15 |
0.4101 |
1489.36 |
288.15 |
0.5006 |
1494.73 |
288.15 |
0.6001 |
1500.28 |
288.15 |
0.6996 |
1505.69 |
288.15 |
0.7999 |
1510.78 |
298.15 |
0.0985 |
1501.24 |
298.15 |
0.1974 |
1506.01 |
298.15 |
0.2950 |
1510.78 |
298.15 |
0.4101 |
1516.15 |
298.15 |
0.5006 |
1520.34 |
298.15 |
0.6001 |
1527.06 |
298.15 |
0.6996 |
1534.55 |
298.15 |
0.7999 |
1540.32 |
308.15 |
0.0985 |
1523.52 |
308.15 |
0.1974 |
1527.52 |
308.15 |
0.2950 |
1531.47 |
308.15 |
0.4101 |
1536.11 |
308.15 |
0.5006 |
1541.59 |
308.15 |
0.6001 |
1549.18 |
308.15 |
0.6996 |
1556.59 |
308.15 |
0.7999 |
1562.29 |
318.15 |
0.0985 |
1541.59 |
318.15 |
0.1974 |
1547.17 |
318.15 |
0.2950 |
1552.68 |
318.15 |
0.4101 |
1558.07 |
318.15 |
0.5006 |
1563.21 |
318.15 |
0.6001 |
1568.76 |
318.15 |
0.6996 |
1573.92 |
318.15 |
0.7999 |
1579.48 |
Speed of sound, m/s
[ref]
Operational conditions:
- Pressure, kPa = 100 (Liquid)
- Frequency, MHz = 3 (Liquid)
Fixed |
Measured |
Molality, mol/kg of Ethanol, 2,2'-oxybis- (1) - Liquid |
Temperature, K - Liquid |
Speed of sound, m/s - Liquid |
0.0985 |
293.15 |
1487.65 |
0.1974 |
293.15 |
1493.09 |
0.2950 |
293.15 |
1498.14 |
0.4101 |
293.15 |
1504.13 |
0.5006 |
293.15 |
1508.33 |
0.0985 |
298.15 |
1501.24 |
0.1974 |
298.15 |
1506.01 |
0.2950 |
298.15 |
1510.78 |
0.4101 |
298.15 |
1516.15 |
0.5006 |
298.15 |
1520.34 |
0.0985 |
303.15 |
1513.09 |
0.1974 |
303.15 |
1517.58 |
0.2950 |
303.15 |
1521.95 |
0.4101 |
303.15 |
1526.88 |
0.5006 |
303.15 |
1530.64 |
0.0985 |
308.15 |
1523.52 |
0.1974 |
308.15 |
1527.52 |
0.2950 |
308.15 |
1531.47 |
0.4101 |
308.15 |
1536.11 |
0.5006 |
308.15 |
1539.59 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Pressure, kPa - Liquid |
Mole fraction of Water (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
100.00 |
0.9980 |
372.60 |
100.00 |
0.9890 |
373.20 |
100.00 |
0.9790 |
373.72 |
100.00 |
0.9610 |
375.15 |
100.00 |
0.9180 |
376.19 |
100.00 |
0.8900 |
376.71 |
100.00 |
0.8560 |
377.17 |
100.00 |
0.7990 |
380.14 |
100.00 |
0.7750 |
381.31 |
100.00 |
0.7590 |
382.40 |
100.00 |
0.7110 |
383.93 |
100.00 |
0.6960 |
383.68 |
100.00 |
0.6580 |
385.91 |
100.00 |
0.6440 |
387.39 |
100.00 |
0.5620 |
393.37 |
100.00 |
0.4890 |
398.40 |
100.00 |
0.3850 |
409.60 |
100.00 |
0.3210 |
419.09 |
100.00 |
0.2460 |
429.60 |
70.00 |
0.9980 |
362.52 |
70.00 |
0.9800 |
363.73 |
70.00 |
0.9510 |
364.82 |
70.00 |
0.9110 |
365.91 |
70.00 |
0.8740 |
368.25 |
70.00 |
0.8740 |
367.05 |
70.00 |
0.7940 |
369.95 |
70.00 |
0.7190 |
372.60 |
70.00 |
0.6830 |
374.37 |
70.00 |
0.6610 |
376.34 |
70.00 |
0.6600 |
375.52 |
70.00 |
0.6140 |
377.37 |
70.00 |
0.5890 |
379.09 |
70.00 |
0.4960 |
385.08 |
70.00 |
0.3560 |
397.65 |
70.00 |
0.3180 |
402.77 |
70.00 |
0.2590 |
413.67 |
70.00 |
0.1900 |
424.56 |
50.00 |
0.9980 |
353.64 |
50.00 |
0.9640 |
355.40 |
50.00 |
0.9330 |
356.25 |
50.00 |
0.8900 |
358.15 |
50.00 |
0.8630 |
359.28 |
50.00 |
0.7930 |
362.15 |
50.00 |
0.6830 |
364.95 |
50.00 |
0.6570 |
366.30 |
50.00 |
0.6270 |
367.64 |
50.00 |
0.6270 |
367.64 |
50.00 |
0.6090 |
368.57 |
50.00 |
0.5110 |
374.35 |
50.00 |
0.4550 |
378.72 |
50.00 |
0.3630 |
387.50 |
50.00 |
0.3050 |
395.36 |
50.00 |
0.2390 |
403.18 |
50.00 |
0.2270 |
405.63 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Pressure, kPa - Liquid |
Mole fraction of Water (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
100.00 |
0.9980 |
372.60 |
100.00 |
0.9890 |
373.20 |
100.00 |
0.9790 |
373.72 |
100.00 |
0.9610 |
375.15 |
100.00 |
0.9180 |
376.19 |
100.00 |
0.8900 |
376.71 |
100.00 |
0.8560 |
377.17 |
100.00 |
0.7990 |
380.14 |
100.00 |
0.7750 |
381.31 |
100.00 |
0.7590 |
382.40 |
100.00 |
0.7110 |
383.93 |
100.00 |
0.6960 |
383.68 |
100.00 |
0.6580 |
385.91 |
100.00 |
0.6440 |
387.39 |
100.00 |
0.5620 |
393.37 |
100.00 |
0.4890 |
398.40 |
100.00 |
0.3850 |
409.60 |
100.00 |
0.3210 |
419.09 |
100.00 |
0.2460 |
429.60 |
70.00 |
0.9980 |
362.52 |
70.00 |
0.9800 |
363.73 |
70.00 |
0.9510 |
364.82 |
70.00 |
0.9110 |
365.91 |
70.00 |
0.8740 |
368.25 |
70.00 |
0.8740 |
367.05 |
70.00 |
0.7940 |
369.95 |
70.00 |
0.7190 |
372.60 |
70.00 |
0.6830 |
374.37 |
70.00 |
0.6610 |
376.34 |
70.00 |
0.6600 |
375.52 |
70.00 |
0.6140 |
377.37 |
70.00 |
0.5890 |
379.09 |
70.00 |
0.4960 |
385.08 |
70.00 |
0.3560 |
397.65 |
70.00 |
0.3180 |
402.77 |
70.00 |
0.2590 |
413.67 |
70.00 |
0.1900 |
424.56 |
50.00 |
0.9980 |
353.64 |
50.00 |
0.9640 |
355.40 |
50.00 |
0.9330 |
356.25 |
50.00 |
0.8900 |
358.15 |
50.00 |
0.8630 |
359.28 |
50.00 |
0.7930 |
362.15 |
50.00 |
0.6830 |
364.95 |
50.00 |
0.6570 |
366.30 |
50.00 |
0.6270 |
367.64 |
50.00 |
0.6270 |
367.64 |
50.00 |
0.6090 |
368.57 |
50.00 |
0.5110 |
374.35 |
50.00 |
0.4550 |
378.72 |
50.00 |
0.3630 |
387.50 |
50.00 |
0.3050 |
395.36 |
50.00 |
0.2390 |
403.18 |
50.00 |
0.2270 |
405.63 |
Thermal conductivity, W/m/K
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid |
Temperature, K - Liquid |
Thermal conductivity, W/m/K - Liquid |
0.2500 |
294.40 |
0.2910 |
0.2500 |
323.40 |
0.3100 |
0.2500 |
347.40 |
0.3150 |
0.2500 |
373.00 |
0.3220 |
0.2500 |
396.00 |
0.3250 |
0.2500 |
421.50 |
0.3300 |
0.2500 |
447.50 |
0.3280 |
0.5000 |
295.90 |
0.2350 |
0.5000 |
322.10 |
0.2440 |
0.5000 |
347.80 |
0.2490 |
0.5000 |
371.90 |
0.2580 |
0.5000 |
395.60 |
0.2570 |
0.5000 |
422.00 |
0.2560 |
0.5000 |
447.00 |
0.2530 |
0.7500 |
296.40 |
0.2090 |
0.7500 |
323.80 |
0.2130 |
0.7500 |
349.60 |
0.2170 |
0.7500 |
373.20 |
0.2190 |
0.7500 |
396.90 |
0.2170 |
0.7500 |
421.60 |
0.2220 |
0.7500 |
446.80 |
0.2130 |
Thermal conductivity, W/m/K
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid |
Temperature, K - Liquid |
Thermal conductivity, W/m/K - Liquid |
0.2500 |
294.40 |
0.2910 |
0.2500 |
323.40 |
0.3100 |
0.2500 |
347.40 |
0.3150 |
0.2500 |
373.00 |
0.3220 |
0.2500 |
396.00 |
0.3250 |
0.2500 |
421.50 |
0.3300 |
0.2500 |
447.50 |
0.3280 |
0.5000 |
295.90 |
0.2350 |
0.5000 |
322.10 |
0.2440 |
0.5000 |
347.80 |
0.2490 |
0.5000 |
371.90 |
0.2580 |
0.5000 |
395.60 |
0.2570 |
0.5000 |
422.00 |
0.2560 |
0.5000 |
447.00 |
0.2530 |
0.7500 |
296.40 |
0.2090 |
0.7500 |
323.80 |
0.2130 |
0.7500 |
349.60 |
0.2170 |
0.7500 |
373.20 |
0.2190 |
0.7500 |
396.90 |
0.2170 |
0.7500 |
421.60 |
0.2220 |
0.7500 |
446.80 |
0.2130 |
Binary diffusion coefficient, m2/s
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Mole fraction = 0 (Liquid)
Temperature, K - Liquid |
Binary diffusion coefficient, m2/s - Liquid |
303.20 |
0.0000 |
308.20 |
0.0000 |
313.20 |
0.0000 |
318.20 |
0.0000 |
323.20 |
0.0000 |
Binary diffusion coefficient, m2/s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid |
Temperature, K - Liquid |
Binary diffusion coefficient, m2/s - Liquid |
0.2000 |
303.20 |
0.0000 |
0.2000 |
308.20 |
0.0000 |
0.2000 |
313.20 |
0.0000 |
0.2000 |
318.20 |
0.0000 |
0.2000 |
323.20 |
0.0000 |
0.4000 |
303.20 |
0.0000 |
0.4000 |
308.20 |
0.0000 |
0.4000 |
313.20 |
0.0000 |
0.4000 |
318.20 |
0.0000 |
0.4000 |
323.20 |
0.0000 |
0.6000 |
303.20 |
0.0000 |
0.6000 |
308.20 |
0.0000 |
0.6000 |
313.20 |
0.0000 |
0.6000 |
318.20 |
0.0000 |
0.6000 |
323.20 |
0.0000 |
0.8000 |
303.20 |
0.0000 |
0.8000 |
308.20 |
0.0000 |
0.8000 |
313.20 |
0.0000 |
0.8000 |
318.20 |
0.0000 |
0.8000 |
323.20 |
0.0000 |
Binary diffusion coefficient, m2/s
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Mole fraction = 0 (Liquid)
Temperature, K - Liquid |
Binary diffusion coefficient, m2/s - Liquid |
303.20 |
0.0000 |
308.20 |
0.0000 |
313.20 |
0.0000 |
318.20 |
0.0000 |
323.20 |
0.0000 |
Binary diffusion coefficient, m2/s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Mole fraction of Ethanol, 2,2'-oxybis- (1) - Liquid |
Temperature, K - Liquid |
Binary diffusion coefficient, m2/s - Liquid |
0.2000 |
303.20 |
0.0000 |
0.2000 |
308.20 |
0.0000 |
0.2000 |
313.20 |
0.0000 |
0.2000 |
318.20 |
0.0000 |
0.2000 |
323.20 |
0.0000 |
0.4000 |
303.20 |
0.0000 |
0.4000 |
308.20 |
0.0000 |
0.4000 |
313.20 |
0.0000 |
0.4000 |
318.20 |
0.0000 |
0.4000 |
323.20 |
0.0000 |
0.6000 |
303.20 |
0.0000 |
0.6000 |
308.20 |
0.0000 |
0.6000 |
313.20 |
0.0000 |
0.6000 |
318.20 |
0.0000 |
0.6000 |
323.20 |
0.0000 |
0.8000 |
303.20 |
0.0000 |
0.8000 |
308.20 |
0.0000 |
0.8000 |
313.20 |
0.0000 |
0.8000 |
318.20 |
0.0000 |
0.8000 |
323.20 |
0.0000 |
Sources