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Heat or mass transfer at low Péclet number for Brinkman and Darcy flow round a sphere

✍ Scribed by Bell, Christopher G.; Byrne, H.M.; Whiteley, J.P.; Waters, S.L.

Book ID
121316607
Publisher
Elsevier Science
Year
2014
Tongue
English
Weight
731 KB
Volume
68
Category
Article
ISSN
0017-9310

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Mass transfer at high Péclet numbers for creeping flow in a packed-bed reactor
✍ Peter Fedkiw; John Newman 📂 Article 📅 1977 🏛 American Institute of Chemical Engineers 🌐 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