Abstract
Pervaporation is a promising option to enhance conversion of reversible condensation reactions, generating water as a byproduct. The present study aims to develop a continuous composite catalytic pervaporation membrane reactor, as integration of reaction and separation offers advantages in terms of process efficiency and compactness. Composite catalytic membranes have been prepared by applying a zeolite coating on top of ceramic hollow fiber silica-membranes. This approach allows independent optimization of the selective and catalytic properties. The performance of the composite catalytic membrane is examined in the esterification reaction between acetic acid and butanol. Additionally, a preliminary large-scale composite membrane reactor evaluation is carried out based on the obtained experimental data (e.g., membrane permeability and catalyst activity). In the pervaporation-assisted esterification reaction, the catalytic membrane is able to couple catalytic activity and water removal. A computational reactor evaluation proved that the outlet conversion for the catalytic pervaporation-assisted esterification reaction exceeds the conversion of a conventional inert pervaporation membrane reactor, with the same loading of catalyst dispersed in the liquid bulk. This shows the potential added value of such a membrane system as compared to more common reactor designs.
Original language | English |
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Pages (from-to) | 9490-9496 |
Number of pages | 7 |
Journal | Industrial and Engineering Chemistry Research |
Volume | 44 |
Issue number | 25 |
Early online date | 9 Jun 2005 |
DOIs | |
Publication status | Published - 1 Dec 2005 |
Externally published | Yes |
Keywords
- n/a OA procedure