Use of a new type of apparatus, high-output small-size tubular turbulent reactors of mainly dif- fuser-confuser design, in very fast processes, including polymerization, is considered. The turbulent diffusion coefficient D t and its distribution over the apparatus volume were calculated as functions of the confuser divergence angle α. The calculations were confirmed by experimental data. New reactor designs for a number of processes of large-tonnage polymer production were proposed and put into practice.
Russian Journal of Applied Chemistry – Springer Journals
Published: Oct 13, 2004
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