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- W2084883197 abstract "Abstract The flow field of a non-Newtonian fluid in a conduit undergoing exothermal chemical reactions is strongly determined by heat and mass transfer processes predominatly via the molecular weight dependence of the fluid properties. The specific example in this study is polymerization of styrene in a steady, laminar flow tubular reactor. Avoiding the region of thermal instability, nonlinear transport and conversion mechanisms leading to characteristically elongated, jet-like velocity profiles are discussed. Specifically, the newly developed distributed parameter model has been used to investigate the coupled effects of strong temperatures, gradients and local polymerization processes on the tubular fluid dynamics. For extreme operational conditions either the highly viscous polymer almost plugs the reactor or most of the incoming monomer solution leaves the tube unreacted." @default.
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- W2084883197 date "1987-01-01" @default.
- W2084883197 modified "2023-09-26" @default.
- W2084883197 title "Fluid dynamics of a tubular polymerizer" @default.
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- W2084883197 doi "https://doi.org/10.1016/0020-7225(87)90110-8" @default.
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