## Abstract **BACKGROUND:** Acetals can be considered important bio‐based diesel additives. The production of most of these compounds, from an alcohol and an aldehyde, suffers from low conversion due to thermodynamic limitations. These limitations can be overcome through the removal of the by‐produ
The conceptual design of a continuous pervaporation membrane reactor for the production of 1,1-diethoxy butane
✍ Scribed by Ion Agirre; M. Belén Güemez; Anatolie Motelica; Henk M. van Veen; Jaap F. Vente; Pedro L. Arias
- Book ID
- 111994592
- Publisher
- American Institute of Chemical Engineers
- Year
- 2011
- Tongue
- English
- Weight
- 956 KB
- Volume
- 58
- Category
- Article
- ISSN
- 0001-1541
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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 eq
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