Operational conditions:
Mole fraction of Ethane, 1,2-dibromo- (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0552 | 0.0448 |
0.1177 | 0.0696 |
0.1800 | 0.0864 |
0.2446 | 0.0900 |
0.3072 | 0.0851 |
0.3659 | 0.0750 |
0.4203 | 0.0590 |
0.4702 | 0.0393 |
0.4789 | 0.0275 |
0.5086 | 0.0195 |
0.5255 | 0.0103 |
0.5837 | -0.0105 |
0.6456 | -0.0215 |
0.7119 | -0.0257 |
0.7852 | -0.0281 |
0.8597 | -0.0229 |
0.9321 | -0.0120 |
Operational conditions:
Mole fraction of Ethane, 1,2-dibromo- (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0552 | 0.0448 |
0.1177 | 0.0696 |
0.1800 | 0.0864 |
0.2446 | 0.0900 |
0.3072 | 0.0851 |
0.3659 | 0.0750 |
0.4203 | 0.0590 |
0.4702 | 0.0393 |
0.4789 | 0.0275 |
0.5086 | 0.0195 |
0.5255 | 0.0103 |
0.5837 | -0.0105 |
0.6456 | -0.0215 |
0.7119 | -0.0257 |
0.7852 | -0.0281 |
0.8597 | -0.0229 |
0.9321 | -0.0120 |
Operational conditions:
Mole fraction of Methyl propionate (2) - Liquid | Mass density, kg/m3 - Liquid |
---|---|
0.0544 | 2090.48 |
0.1086 | 2015.14 |
0.1617 | 1942.18 |
0.2130 | 1872.81 |
0.2714 | 1794.99 |
0.3254 | 1724.12 |
0.4447 | 1570.72 |
0.5056 | 1494.18 |
0.5610 | 1425.55 |
0.6166 | 1357.57 |
0.6838 | 1276.41 |
0.7430 | 1205.94 |
0.8086 | 1129.0 |
0.8715 | 1056.36 |
0.9358 | 982.68 |
Operational conditions:
Mole fraction of Methyl propionate (2) - Liquid | Mass density, kg/m3 - Liquid |
---|---|
0.0544 | 2090.48 |
0.1086 | 2015.14 |
0.1617 | 1942.18 |
0.2130 | 1872.81 |
0.2714 | 1794.99 |
0.3254 | 1724.12 |
0.4447 | 1570.72 |
0.5056 | 1494.18 |
0.5610 | 1425.55 |
0.6166 | 1357.57 |
0.6838 | 1276.41 |
0.7430 | 1205.94 |
0.8086 | 1129.0 |
0.8715 | 1056.36 |
0.9358 | 982.68 |