FIELD: polymerization processes and synthetic rubber production. SUBSTANCE: catalyst charge is divided into two portions. The first one is charged simultaneously with solvent and styrene, its amount being proportional to moisture content in the two latter. After agitation is terminated, the second portion is charged, its amount being adjusted in dependence of melt index. Reaction temperature is controlled by portion-wise feeding of butadiene into reactor, the butadiene portions being proportionated taking into account optimal polymerization temperature. First portion of butadiene is loaded after styrene polymerization is completed and temperature is lowered to a value appropriate for butadiene polymerization, and the second one after completion of the first portion polymerization and lowering temperature to a maximum value for the beginning of the second portion polymerization. When temperature in reactor reaches 52 C during styrene polymerization, the gate controlling cooling agent access into reactor jacket is fully opened. EFFECT: achieved automation of polymerization process. 1 dwg
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Authors
Dates
1997-07-20—Published
1994-04-08—Filed