Operational conditions:
Mole fraction of Triethylene glycol (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0313 | -0.1392 |
0.0606 | -0.2409 |
0.0883 | -0.3145 |
0.1143 | -0.3695 |
0.1623 | -0.4341 |
0.2047 | -0.4660 |
0.2792 | -0.4920 |
0.3405 | -0.5019 |
0.4366 | -0.5055 |
0.5376 | -0.5042 |
0.6078 | -0.5001 |
0.6992 | -0.4552 |
0.7560 | -0.4050 |
0.8230 | -0.3311 |
0.8613 | -0.2781 |
0.9029 | -0.2101 |
0.9490 | -0.1000 |
Operational conditions:
Mole fraction of Triethylene glycol (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0313 | -0.1392 |
0.0606 | -0.2409 |
0.0883 | -0.3145 |
0.1143 | -0.3695 |
0.1623 | -0.4341 |
0.2047 | -0.4660 |
0.2792 | -0.4920 |
0.3405 | -0.5019 |
0.4366 | -0.5055 |
0.5376 | -0.5042 |
0.6078 | -0.5001 |
0.6992 | -0.4552 |
0.7560 | -0.4050 |
0.8230 | -0.3311 |
0.8613 | -0.2781 |
0.9029 | -0.2101 |
0.9490 | -0.1000 |
Operational conditions:
Mole fraction of Triethylene glycol (2) - Liquid | Mass density, kg/m3 - Liquid |
---|---|
0.0519 | 1039.48 |
0.1740 | 1051.93 |
0.2411 | 1058.18 |
0.3373 | 1066.69 |
0.4327 | 1074.57 |
0.5295 | 1082.04 |
0.6320 | 1089.43 |
0.7533 | 1097.6 |
0.8256 | 1102.12 |
0.8572 | 1104.07 |
0.9337 | 1108.5 |
0.9610 | 1110.01 |
Operational conditions:
Mole fraction of Triethylene glycol (2) - Liquid | Mass density, kg/m3 - Liquid |
---|---|
0.0519 | 1039.48 |
0.1740 | 1051.93 |
0.2411 | 1058.18 |
0.3373 | 1066.69 |
0.4327 | 1074.57 |
0.5295 | 1082.04 |
0.6320 | 1089.43 |
0.7533 | 1097.6 |
0.8256 | 1102.12 |
0.8572 | 1104.07 |
0.9337 | 1108.5 |
0.9610 | 1110.01 |