Abstract
Aspects of the macrokinetics of fast polymerization processes in turbulent flows are considered. The dependences of the yield and molecular characteristics (MM and MMD) of the polymer formed on the geometry of the reaction volume and the parameters of mixing and heat transfer processes (rates of flows, turbulization, boiling, etc.) have been established. It is shown that such reactions call for special methods of investigation and control. A fundamentally new material-, resource- and energy-saving technology has been devised for obtaining isobutylene polymers based on the developed model of fast flow polymerization.
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