Ravindranath, K. ; Mashelkar, R. A. (1982) Modeling of poly(ethylene terephthalate) reactors. II. A continuous transesterification process Journal of Applied Polymer Science, 27 (2). pp. 471-487. ISSN 0021-8995
Full text not available from this repository.
Official URL: http://onlinelibrary.wiley.com/doi/10.1002/app.198...
Related URL: http://dx.doi.org/10.1002/app.1982.070270212
Abstract
A comprehensive mathematical model for a continuous transesterification process has been built so as to enable prediction of the influence of different process and operational variables on productivity and by-product formation. The influence of temperatures and temperature profiles, of residence time and residence time distribution, and also of the number of reactors in series has been investigated. The modeling has been done as close to the industrial practice as possible. Important pragmatic implications from the point of view of operation of continuous transesterification are highlighted.
| Item Type: | Article |
|---|---|
| Source: | Copyright of this article belongs to John Wiley and Sons, Inc. |
| ID Code: | 22137 |
| Deposited On: | 23 Nov 2010 08:16 |
| Last Modified: | 06 Jun 2011 10:36 |
Repository Staff Only: item control page
