Research Article
Reactivity of Phenol Allylation Using Phase-Transfer Catalysis in Ion-Exchange Membrane Reactor
Table 1
Advantages and disadvantages of three reactors.
| | V1 reactor | H1 reactor | H2 reactor |
| Diameter of membrane (cm) | 6.2 | 2.2 | 2.5 | Area of membrane (m2) | | | | Working volume (cm3) | 55 | 35 | 35 | Activation energy (kcal/mole) | 12.11 | 13.12 | 11.69 | Turnover number (s−1) | | | | Recovery rate of phenol in 90 min (ppm/(min m2)) | 13794 | 45263 | 38452 | Pressure drop | △ | △ | ○ | Gravity | × | △ | ○ | Area of membrane | × | ○ | ○ | Apparatus | △ | ○ | ○ | Cost | △ | ○ | ○ | Operating difficulty | △ | ○ | ○ | Reactivity | × | ○ | ○ |
|
|
○ good, △ fair, × poor.
|