Ravindranath, K. ; Mashelkar, R. A. (1982) Modeling of poly (ethylene terephthalate) reactors: 4. A continuous esterification process Polymer Engineering & Science, 22 (10). pp. 610-618. ISSN 0032-3888
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Official URL: http://www3.interscience.wiley.com/journal/1096002...
Related URL: http://dx.doi.org/10.1002/pen.760221005
Abstract
A mathematical model has been developed for the direct, continuous esterification process. Influence of process and operational variables, including temperature distribution, residence time distribution, bis(hydroxyethyl)terephthalate recycle, pressure, and ethylene glycol (EG) to terephthalic acid ratio on the reactor performance have been investigated in a range as close to industrial practice as possible. The variables influencing the amount of EG reflux (which governs the energy economy) and side products (which govern the product quality) have been discussed. This investigation provides an analysis of a continuous, direct esterification process, and the results indicate strategies for optimizing productivity and product quality.
| Item Type: | Article |
|---|---|
| Source: | Copyright of this article belongs to Society of Plastics Engineers. |
| ID Code: | 22114 |
| Deposited On: | 23 Nov 2010 08:21 |
| Last Modified: | 06 Jun 2011 09:36 |
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