Operational conditions:
Fixed | Measured | |
---|---|---|
Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid | Mole fraction of 1-Propanol (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.0270 | 0.0842 | 0.4950 |
0.0547 | 0.1704 | 0.6500 |
0.0551 | 0.0547 | 0.4010 |
0.0648 | 0.0211 | 0.2500 |
0.0756 | 0.2356 | 0.7220 |
0.1007 | 0.3139 | 0.7430 |
0.1008 | 0.1001 | 0.5750 |
0.1158 | 0.3610 | 0.7390 |
0.1291 | 0.4023 | 0.7110 |
0.1342 | 0.0437 | 0.4200 |
0.1480 | 0.1469 | 0.6800 |
0.1506 | 0.4695 | 0.6460 |
0.1596 | 0.4974 | 0.6180 |
0.1772 | 0.5521 | 0.5390 |
0.1871 | 0.1856 | 0.7300 |
0.1892 | 0.5898 | 0.4880 |
0.1999 | 0.6230 | 0.4190 |
0.2010 | 0.0655 | 0.5480 |
0.2089 | 0.6510 | 0.3580 |
0.2200 | 0.6857 | 0.2580 |
0.2274 | 0.2256 | 0.7400 |
0.2283 | 0.7115 | 0.1780 |
0.2358 | 0.7349 | 0.0910 |
0.2689 | 0.0877 | 0.6470 |
0.2975 | 0.2952 | 0.6970 |
0.3213 | 0.1048 | 0.6710 |
0.3234 | 0.3209 | 0.6530 |
0.3511 | 0.3484 | 0.5910 |
0.3730 | 0.1216 | 0.6800 |
0.3780 | 0.3751 | 0.5250 |
0.4044 | 0.4012 | 0.4460 |
0.4160 | 0.1356 | 0.6590 |
0.4289 | 0.4255 | 0.3660 |
0.4474 | 0.4439 | 0.2850 |
0.4664 | 0.1520 | 0.6160 |
0.4678 | 0.4641 | 0.1950 |
0.4862 | 0.4824 | 0.0970 |
0.5149 | 0.1679 | 0.5630 |
0.5551 | 0.1810 | 0.4950 |
0.5913 | 0.1928 | 0.4380 |
0.6369 | 0.2076 | 0.3540 |
0.6669 | 0.2174 | 0.2790 |
0.6977 | 0.2275 | 0.1930 |
0.7301 | 0.2380 | 0.0960 |
Operational conditions:
Fixed | Measured | |
---|---|---|
Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid | Mole fraction of 1-Propanol (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.0270 | 0.0842 | 0.4950 |
0.0547 | 0.1704 | 0.6500 |
0.0551 | 0.0547 | 0.4010 |
0.0648 | 0.0211 | 0.2500 |
0.0756 | 0.2356 | 0.7220 |
0.1007 | 0.3139 | 0.7430 |
0.1008 | 0.1001 | 0.5750 |
0.1158 | 0.3610 | 0.7390 |
0.1291 | 0.4023 | 0.7110 |
0.1342 | 0.0437 | 0.4200 |
0.1480 | 0.1469 | 0.6800 |
0.1506 | 0.4695 | 0.6460 |
0.1596 | 0.4974 | 0.6180 |
0.1772 | 0.5521 | 0.5390 |
0.1871 | 0.1856 | 0.7300 |
0.1892 | 0.5898 | 0.4880 |
0.1999 | 0.6230 | 0.4190 |
0.2010 | 0.0655 | 0.5480 |
0.2089 | 0.6510 | 0.3580 |
0.2200 | 0.6857 | 0.2580 |
0.2274 | 0.2256 | 0.7400 |
0.2283 | 0.7115 | 0.1780 |
0.2358 | 0.7349 | 0.0910 |
0.2689 | 0.0877 | 0.6470 |
0.2975 | 0.2952 | 0.6970 |
0.3213 | 0.1048 | 0.6710 |
0.3234 | 0.3209 | 0.6530 |
0.3511 | 0.3484 | 0.5910 |
0.3730 | 0.1216 | 0.6800 |
0.3780 | 0.3751 | 0.5250 |
0.4044 | 0.4012 | 0.4460 |
0.4160 | 0.1356 | 0.6590 |
0.4289 | 0.4255 | 0.3660 |
0.4474 | 0.4439 | 0.2850 |
0.4664 | 0.1520 | 0.6160 |
0.4678 | 0.4641 | 0.1950 |
0.4862 | 0.4824 | 0.0970 |
0.5149 | 0.1679 | 0.5630 |
0.5551 | 0.1810 | 0.4950 |
0.5913 | 0.1928 | 0.4380 |
0.6369 | 0.2076 | 0.3540 |
0.6669 | 0.2174 | 0.2790 |
0.6977 | 0.2275 | 0.1930 |
0.7301 | 0.2380 | 0.0960 |