A continuous pervaporation membrane reactor for the study of esterification reactions using a composite polymeric/ceramic membrane
β Scribed by Y. Zhu; R.G. Minet; T.T. Tsotsis
- Publisher
- Elsevier Science
- Year
- 1996
- Tongue
- English
- Weight
- 808 KB
- Volume
- 51
- Category
- Article
- ISSN
- 0009-2509
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β¦ Synopsis
The esterification reaction between acetic acid and ethanol was studied in a continuous flow pervaporation membrane reactor utilizing a polymeric/ceramic composite membrane. For a range of experimental conditions reactor conversions were observed which are higher than the corresponding calculated equilibrium values. This is due to the ability of the membrane to remove water, a product of the reaction. A theoretical model has been developed which gives a reasonable fit of the experimental results.
π SIMILAR VOLUMES
## Abstract A simulation of a membrane reactor for the water gas shift reaction is carried out by means of a 1D pseudoβhomogeneous nonisothermal mathematical model. The composite membrane consists of a dense layer of Pd (selective to H~2~) supported over a porous ceramic layer. The effect of temper