| Article ID | Journal | Published Year | Pages | File Type |
|---|---|---|---|---|
| 10262991 | Chemical Engineering Science | 2006 | 11 Pages |
Abstract
Based on the detailed batch column model, a complete model of a simulated-moving-bed reactor has been implemented and its optimal point of operation for the synthesis of methyl acrylate from acrylic acid has been determined. Particularly when considering the low-operating temperature, we can regard this process as a possible competition for current technologies.
Related Topics
Physical Sciences and Engineering
Chemical Engineering
Chemical Engineering (General)
Authors
Guido Ströhlein, Yolanda Assunção, Nikhil Dube, André Bardow, Marco Mazzotti, Massimo Morbidelli,