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• W1973248935 abstract "Free radical solution polymerization of styrene has been studied using a binary mixture of symmetrical bifunctional initiators in a filled tubular reactor packed with static mixers. Owing to intensive radial mixing induced by the static mixers, a near plug flow pattern was obtained in the reactor with some axial dispersion effect. The axial mass dispersion coefficient was determined from the residence time distribution experiment and a dynamic axial dispersion model has been developed and solved to investigate steady state and transient behavior of the filled tubular reactor. With a solvent volume fraction of 0.3, the monomer conversion up to 70% was obtained without fouling problems in the temperature range 90 to 120°C. The experimental filled tubular reactor was operated under various reaction conditions and a reasonably good agreement between the model and the experimental data was obtained without using any adjustable parameters." @default.
• W1973248935 created "2016-06-24" @default.
• W1973248935 creator A5051009203 @default.
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• W1973248935 date "1996-01-01" @default.
• W1973248935 modified "2023-10-18" @default.
• W1973248935 title "Polymerization of styrene in a continuous filled tubular reactor" @default.
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• W1973248935 doi "https://doi.org/10.1002/pen.10385" @default.
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