Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Ethanol, 2-ethoxy- (2) - Liquid | Viscosity, Pa*s - Liquid |
298.15 | 0.0585 | 0.0006 |
298.15 | 0.1533 | 0.0007 |
298.15 | 0.2518 | 0.0008 |
298.15 | 0.3637 | 0.0008 |
298.15 | 0.4521 | 0.0009 |
298.15 | 0.5048 | 0.0010 |
298.15 | 0.5525 | 0.0010 |
298.15 | 0.6521 | 0.0012 |
298.15 | 0.7508 | 0.0013 |
298.15 | 0.8521 | 0.0015 |
298.15 | 0.9547 | 0.0017 |
308.15 | 0.0585 | 0.0005 |
308.15 | 0.1533 | 0.0006 |
308.15 | 0.2518 | 0.0006 |
308.15 | 0.3637 | 0.0007 |
308.15 | 0.4521 | 0.0008 |
308.15 | 0.5048 | 0.0008 |
308.15 | 0.5525 | 0.0008 |
308.15 | 0.6521 | 0.0009 |
308.15 | 0.7508 | 0.0010 |
308.15 | 0.8521 | 0.0012 |
308.15 | 0.9547 | 0.0013 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Ethanol, 2-ethoxy- (2) - Liquid | Viscosity, Pa*s - Liquid |
298.15 | 0.0585 | 0.0006 |
298.15 | 0.1533 | 0.0007 |
298.15 | 0.2518 | 0.0008 |
298.15 | 0.3637 | 0.0008 |
298.15 | 0.4521 | 0.0009 |
298.15 | 0.5048 | 0.0010 |
298.15 | 0.5525 | 0.0010 |
298.15 | 0.6521 | 0.0012 |
298.15 | 0.7508 | 0.0013 |
298.15 | 0.8521 | 0.0015 |
298.15 | 0.9547 | 0.0017 |
308.15 | 0.0585 | 0.0005 |
308.15 | 0.1533 | 0.0006 |
308.15 | 0.2518 | 0.0006 |
308.15 | 0.3637 | 0.0007 |
308.15 | 0.4521 | 0.0008 |
308.15 | 0.5048 | 0.0008 |
308.15 | 0.5525 | 0.0008 |
308.15 | 0.6521 | 0.0009 |
308.15 | 0.7508 | 0.0010 |
308.15 | 0.8521 | 0.0012 |
308.15 | 0.9547 | 0.0013 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Ethanol, 2-ethoxy- (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
308.15 | 0.0263 | 0.2237 |
308.15 | 0.0693 | 0.4218 |
308.15 | 0.0792 | 0.4469 |
308.15 | 0.1159 | 0.5282 |
308.15 | 0.1327 | 0.5592 |
308.15 | 0.1630 | 0.5920 |
308.15 | 0.1866 | 0.6140 |
308.15 | 0.2104 | 0.6236 |
308.15 | 0.2411 | 0.6303 |
308.15 | 0.2961 | 0.6226 |
308.15 | 0.3551 | 0.5843 |
308.15 | 0.4042 | 0.5547 |
308.15 | 0.4786 | 0.4912 |
308.15 | 0.5503 | 0.4243 |
308.15 | 0.6047 | 0.3681 |
308.15 | 0.6669 | 0.3033 |
308.15 | 0.7336 | 0.2326 |
308.15 | 0.7859 | 0.1799 |
308.15 | 0.8653 | 0.1065 |
308.15 | 0.9188 | 0.0647 |
318.15 | 0.0307 | 0.2495 |
318.15 | 0.0615 | 0.4069 |
318.15 | 0.1237 | 0.5819 |
318.15 | 0.1866 | 0.6392 |
318.15 | 0.2502 | 0.6719 |
318.15 | 0.3065 | 0.6622 |
318.15 | 0.3551 | 0.6454 |
318.15 | 0.4042 | 0.6163 |
318.15 | 0.4786 | 0.5535 |
318.15 | 0.5539 | 0.4750 |
318.15 | 0.6047 | 0.4196 |
318.15 | 0.6559 | 0.3613 |
318.15 | 0.7336 | 0.2702 |
318.15 | 0.7859 | 0.2181 |
318.15 | 0.8653 | 0.1302 |
318.15 | 0.9188 | 0.0795 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Ethanol, 2-ethoxy- (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
308.15 | 0.0263 | 0.2237 |
308.15 | 0.0693 | 0.4218 |
308.15 | 0.0792 | 0.4469 |
308.15 | 0.1159 | 0.5282 |
308.15 | 0.1327 | 0.5592 |
308.15 | 0.1630 | 0.5920 |
308.15 | 0.1866 | 0.6140 |
308.15 | 0.2104 | 0.6236 |
308.15 | 0.2411 | 0.6303 |
308.15 | 0.2961 | 0.6226 |
308.15 | 0.3551 | 0.5843 |
308.15 | 0.4042 | 0.5547 |
308.15 | 0.4786 | 0.4912 |
308.15 | 0.5503 | 0.4243 |
308.15 | 0.6047 | 0.3681 |
308.15 | 0.6669 | 0.3033 |
308.15 | 0.7336 | 0.2326 |
308.15 | 0.7859 | 0.1799 |
308.15 | 0.8653 | 0.1065 |
308.15 | 0.9188 | 0.0647 |
318.15 | 0.0307 | 0.2495 |
318.15 | 0.0615 | 0.4069 |
318.15 | 0.1237 | 0.5819 |
318.15 | 0.1866 | 0.6392 |
318.15 | 0.2502 | 0.6719 |
318.15 | 0.3065 | 0.6622 |
318.15 | 0.3551 | 0.6454 |
318.15 | 0.4042 | 0.6163 |
318.15 | 0.4786 | 0.5535 |
318.15 | 0.5539 | 0.4750 |
318.15 | 0.6047 | 0.4196 |
318.15 | 0.6559 | 0.3613 |
318.15 | 0.7336 | 0.2702 |
318.15 | 0.7859 | 0.2181 |
318.15 | 0.8653 | 0.1302 |
318.15 | 0.9188 | 0.0795 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Ethanol, 2-ethoxy- (2) - Liquid | Mass density, kg/m3 - Liquid |
298.15 | 0.0585 | 875.67 |
298.15 | 0.1533 | 879.82 |
298.15 | 0.2518 | 884.9 |
298.15 | 0.3637 | 891.24 |
298.15 | 0.4521 | 896.46 |
298.15 | 0.5048 | 899.57 |
298.15 | 0.5525 | 902.38 |
298.15 | 0.6521 | 908.09 |
298.15 | 0.7508 | 913.45 |
298.15 | 0.8521 | 918.56 |
298.15 | 0.9547 | 923.27 |
303.15 | 0.0585 | 870.69 |
303.15 | 0.1533 | 875.37 |
303.15 | 0.2518 | 880.92 |
303.15 | 0.3637 | 887.65 |
303.15 | 0.4521 | 893.03 |
303.15 | 0.5048 | 896.19 |
303.15 | 0.5525 | 899.0 |
303.15 | 0.6521 | 904.62 |
303.15 | 0.7508 | 909.81 |
303.15 | 0.8521 | 914.71 |
303.15 | 0.9547 | 919.26 |
308.15 | 0.0585 | 865.67 |
308.15 | 0.1533 | 870.76 |
308.15 | 0.2518 | 876.66 |
308.15 | 0.3637 | 883.7 |
308.15 | 0.4521 | 889.27 |
308.15 | 0.5048 | 892.53 |
308.15 | 0.5525 | 895.41 |
308.15 | 0.6521 | 901.17 |
308.15 | 0.7508 | 906.45 |
308.15 | 0.8521 | 911.43 |
308.15 | 0.9547 | 916.04 |
313.15 | 0.0585 | 860.78 |
313.15 | 0.1533 | 865.96 |
313.15 | 0.2518 | 871.86 |
313.15 | 0.3637 | 878.82 |
313.15 | 0.4521 | 884.27 |
313.15 | 0.5048 | 887.44 |
313.15 | 0.5525 | 890.23 |
313.15 | 0.6521 | 895.76 |
313.15 | 0.7508 | 900.8 |
313.15 | 0.8521 | 905.49 |
313.15 | 0.9547 | 909.8 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Ethanol, 2-ethoxy- (2) - Liquid | Mass density, kg/m3 - Liquid |
298.15 | 0.0585 | 875.67 |
298.15 | 0.1533 | 879.82 |
298.15 | 0.2518 | 884.9 |
298.15 | 0.3637 | 891.24 |
298.15 | 0.4521 | 896.46 |
298.15 | 0.5048 | 899.57 |
298.15 | 0.5525 | 902.38 |
298.15 | 0.6521 | 908.09 |
298.15 | 0.7508 | 913.45 |
298.15 | 0.8521 | 918.56 |
298.15 | 0.9547 | 923.27 |
303.15 | 0.0585 | 870.69 |
303.15 | 0.1533 | 875.37 |
303.15 | 0.2518 | 880.92 |
303.15 | 0.3637 | 887.65 |
303.15 | 0.4521 | 893.03 |
303.15 | 0.5048 | 896.19 |
303.15 | 0.5525 | 899.0 |
303.15 | 0.6521 | 904.62 |
303.15 | 0.7508 | 909.81 |
303.15 | 0.8521 | 914.71 |
303.15 | 0.9547 | 919.26 |
308.15 | 0.0585 | 865.67 |
308.15 | 0.1533 | 870.76 |
308.15 | 0.2518 | 876.66 |
308.15 | 0.3637 | 883.7 |
308.15 | 0.4521 | 889.27 |
308.15 | 0.5048 | 892.53 |
308.15 | 0.5525 | 895.41 |
308.15 | 0.6521 | 901.17 |
308.15 | 0.7508 | 906.45 |
308.15 | 0.8521 | 911.43 |
308.15 | 0.9547 | 916.04 |
313.15 | 0.0585 | 860.78 |
313.15 | 0.1533 | 865.96 |
313.15 | 0.2518 | 871.86 |
313.15 | 0.3637 | 878.82 |
313.15 | 0.4521 | 884.27 |
313.15 | 0.5048 | 887.44 |
313.15 | 0.5525 | 890.23 |
313.15 | 0.6521 | 895.76 |
313.15 | 0.7508 | 900.8 |
313.15 | 0.8521 | 905.49 |
313.15 | 0.9547 | 909.8 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Ethanol, 2-ethoxy- (2) - Liquid | Speed of sound, m/s - Liquid |
298.15 | 0.0585 | 1292.0 |
298.15 | 0.1533 | 1285.0 |
298.15 | 0.2518 | 1281.0 |
298.15 | 0.3637 | 1282.0 |
298.15 | 0.4521 | 1285.0 |
298.15 | 0.5048 | 1287.0 |
298.15 | 0.5525 | 1289.0 |
298.15 | 0.6521 | 1294.0 |
298.15 | 0.7508 | 1299.0 |
298.15 | 0.8521 | 1301.0 |
298.15 | 0.9547 | 1300.0 |
308.15 | 0.0585 | 1258.0 |
308.15 | 0.1533 | 1255.0 |
308.15 | 0.2518 | 1252.0 |
308.15 | 0.3637 | 1250.0 |
308.15 | 0.4521 | 1250.0 |
308.15 | 0.5048 | 1250.0 |
308.15 | 0.5525 | 1251.0 |
308.15 | 0.6521 | 1254.0 |
308.15 | 0.7508 | 1257.0 |
308.15 | 0.8521 | 1261.0 |
308.15 | 0.9547 | 1265.0 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Ethanol, 2-ethoxy- (2) - Liquid | Speed of sound, m/s - Liquid |
298.15 | 0.0585 | 1292.0 |
298.15 | 0.1533 | 1285.0 |
298.15 | 0.2518 | 1281.0 |
298.15 | 0.3637 | 1282.0 |
298.15 | 0.4521 | 1285.0 |
298.15 | 0.5048 | 1287.0 |
298.15 | 0.5525 | 1289.0 |
298.15 | 0.6521 | 1294.0 |
298.15 | 0.7508 | 1299.0 |
298.15 | 0.8521 | 1301.0 |
298.15 | 0.9547 | 1300.0 |
308.15 | 0.0585 | 1258.0 |
308.15 | 0.1533 | 1255.0 |
308.15 | 0.2518 | 1252.0 |
308.15 | 0.3637 | 1250.0 |
308.15 | 0.4521 | 1250.0 |
308.15 | 0.5048 | 1250.0 |
308.15 | 0.5525 | 1251.0 |
308.15 | 0.6521 | 1254.0 |
308.15 | 0.7508 | 1257.0 |
308.15 | 0.8521 | 1261.0 |
308.15 | 0.9547 | 1265.0 |