The paper discusses the general principles of the kinetics of reactions as carried out in the two main types of continuous process. Comparison is made with the corresponding batch system with regard to the necessary volume of reaction space. It is shown that a correct choice of the type of process can sometimes be used to increase the yield of a reaction. The application of these principles to polymerization is described in outline.
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K. G. Denbigh (1951) studied this question.
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