Industrial autothermal cationic isobutylene polymerization reactors may present very complex dynamic behavior and difficult operation. A mathemathical model was developed to describe the operation of an autothermal solution industrial reactor, and some possible sources of complex dynamical behavior
The dynamic behavior of continuous polymerization reactors—I: Isothermal solution polymerization in a CSTR
✍ Scribed by Alan D. Schmidt; W.Harmon Ray
- Publisher
- Elsevier Science
- Year
- 1981
- Tongue
- English
- Weight
- 897 KB
- Volume
- 36
- Category
- Article
- ISSN
- 0009-2509
No coin nor oath required. For personal study only.
📜 SIMILAR VOLUMES
## Abstract This work presents results on the problem of robust on‐line diagnosis of abnormal situations in the case of the free‐radical solution polymerization of styrene in a continuous well‐mixed reactor operating under feedback control. The control system is constituted of a model predictive co
This article describes the influence of gel effect in the free radical polymerization of methyl methacrylate. A mathematical model has been developed which tries to predict the performance of batch and continuous polymerization reactors under dynamic and steady-state conditions. The influence of dif
## Abstract The kinetic scheme of nylon‐6 polymerization consists of ring opening, polyaddition, step growth, reaction with monofunctional acids and cyclization. A set of ordinary differential equations (initial value problem) governing the concentrations and moments of the reacting species and the
The mixing rate of the specfal stirrer device warn studied on various scalem with different stirrer diameters and stirrer speeds, scaling-up procedures were developed. A digital simulation model was met up to study the effects of the stirring parameters On the mixing rate. To study polyzerization, t