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- W2385403716 abstract "Using the results from the experiments of styrene and maleic anhydride copolymerization in 10 L continuous-flow stirred tank reactor,the mathematical model for describing the dependence of the monomer feed rate on monomer conversion and polymerization temperature was successfully set up. This model was applicable in commercial plants with an annual capacity of several thousand tons for predicting polymerization temperature as a function of reactor volume or feed rate. It was concluded that the decrease in polymerization temperature is 5～6 ℃ as the reactor volume increases from 2 m 3 for 5 kt/a plant to 8 6 m 3 for 15 kt/a plant. It was estimated that the decrease in the production loading of the plants from 100% to 40% causes a reduction of 17 ℃ in polymerization temperature." @default.
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- W2385403716 date "2002-01-01" @default.
- W2385403716 modified "2023-09-24" @default.
- W2385403716 title "Relationship of Polymerization Process Parameters in Continuous Bulk Copolymerization of Styrene and Maleic Anhydride" @default.
- W2385403716 hasPublicationYear "2002" @default.
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