## Abstract A comprehensive model for a semibatch ester interchange reactor has been developed with a view to investigate the effect of various process and operational variables on the DMT conversion rate as well as the byβproduct formation. The influence of important variables such as EGβtoβDMT ra
Modeling of semibatch direct esterification reactor for poly(ethylene terephthalate) synthesis
β Scribed by Chang-Kwon Kang; Byoung Chul Lee; Dae Woo Ihm
- Publisher
- John Wiley and Sons
- Year
- 1996
- Tongue
- English
- Weight
- 627 KB
- Volume
- 60
- Category
- Article
- ISSN
- 0021-8995
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β¦ Synopsis
A comprehensive kinetic model for a semibatch direct esterification reactor has been developed. The solid-liquid equilibrium of terephthalic acid was considered in the modeling. Effects of the monomer feed ratio, reaction temperatures, and oligomer addition on the conversion, degree of polymerization, and the formation of diethylene glycol were studied.
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The second stage of batch poly(ethy1ene terephthalate) (PET) reactor with bis(2-hydroxyethyl) terephthalate (BHET) as the feed has been simulated. In this stage, the overall polymerization is not diffusion limited and is known to be a complex reaction. In this work it has been assumed to consist of
A mathematical model for a continuous direct esterification reactor has been developed. The solid-liquid equilibrium of terephthalic acid (TPA) was considered in our modeling, and the characteristic dissolution time, an adjustable parameter, was introduced to account for the mass-transfer effect in
## Abstract The experimental and modeling studies are presented on the melt polycondensation of poly(ethylene terephthalate) by a gas sweeping process. In this process, low molecular weight prepolymer is polymerized to a higher molecular weight polymer in a molten state at ambient pressure as ethyl