Mass transfer at high Péclet numbers for
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Peter Fedkiw; John Newman
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Article
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1977
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American Institute of Chemical Engineers
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English
⚖ 844 KB
## Abstract An isotropic, homogeneous packed‐bed reactor is modeled as an array of sinusoidal periodically constricted tubes (PCT). The effective asymptotic bed‐Sherwood number has been calculated for mass transfer at large Péclet number with a constant wall concentration and creeping flow hydrodyn