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Free‐radical polymerizations associated with the trommsdorff effect under semibatch reactor conditions. III. Experimental responses to step changes in initiator concentration
Author(s) -
Dua V.,
Saraf D. N.,
Gupta Santosh K.
Publication year - 1996
Publication title -
journal of applied polymer science
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.575
H-Index - 166
eISSN - 1097-4628
pISSN - 0021-8995
DOI - 10.1002/(sici)1097-4628(19960124)59:4<749::aid-app20>3.0.co;2-j
Subject(s) - radical polymerization , monomer , thermodynamics , polymerization , diffusion , chemistry , polymer chemistry , polymer , process engineering , chemical engineering , materials science , organic chemistry , engineering , physics
The presence of the diffusion‐limited gel or Trommsdorff effect in free‐radical polymerizations poses a challenge for the modelling of these reactors. The available models cannot be applied to industrial reactors because of their inability to account for nonisothermal effects and semibatch operations. Recent models have overcome these limitations. These models have already been validated for step changes in temperature. The validity of these models under semibatch reactor conditions has been established in the present investigation. Experiments have been carried out at constant temperatures (50 and 70 ° C) and a step change in the initiator concentration from about 15.48 to 100 mol/m 3 has been effected during the course of polymerization. Experimental results on monomer conversions and average molecular weights have been found to be in reasonable agreement with model predictions. The present study establishes the applicability of these models for more general semibatch reactor operations, as well as the possibility of model‐based optimal control of industrial reactors. © 1996 John Wiley & Sons, Inc.