A Numerical Study on the Influence of Confining Walls on Drag and Heat Transfer Coefficients in Single‐Particle Lab‐Scale Reactors

Abstract Single‐particle reactors in lab‐scale are a promising technology to gain an in‐depth understanding of the intricate reaction and transport processes that occur in catalyst particles under operando conditions. It is not described whether the effect of the bounding walls in such narrow flow channels influence the processes at the particle. Therefore, this work applies three‐dimensional (3D) computational fluid dynamics (CFD) simulations to analyze the drag coefficient C D alongside the local and average particle Nusselt number Nu p as characteristic local and integral quantities in the range of particle Reynolds numbers 10 ≤ Re p ≤ 10 3 . An equation is derived to correct for the wall effects on C D and Nu p and assist the experimenter in the interpretation of measured results.

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Publication Details

Journal
Chemie Ingenieur Technik
Published
2024-09-26
DOI
https://doi.org/10.1002/cite.202400083
Citations
1
Primary Topic
Heat and Mass Transfer in Porous Media
Type
article
Field-Weighted Citation Impact
0.37

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article

A Numerical Study on the Influence of Confining Walls on Drag and Heat Transfer Coefficients in Single‐Particle Lab‐Scale Reactors

Gregor D. Wehinger, Philipp Reinold, Martin Kutscherauer
1 citations
Chemie Ingenieur Technik
Heat and Mass Transfer in Porous Media
0.37
article

A Numerical Study on the Influence of Confining Walls on Drag and Heat Transfer Coefficients in Single‐Particle Lab‐Scale Reactors

Gregor D. Wehinger, Philipp Reinold, Martin Kutscherauer
article en
1 citations

Abstract

Abstract Single‐particle reactors in lab‐scale are a promising technology to gain an in‐depth understanding of the intricate reaction and transport processes that occur in catalyst particles under operando conditions. It is not described whether the effect of the bounding walls in such narrow flow channels influence the processes at the particle. Therefore, this work applies three‐dimensional (3D) computational fluid dynamics (CFD) simulations to analyze the drag coefficient C D alongside the local and average particle Nusselt number Nu p as characteristic local and integral quantities in the range of particle Reynolds numbers 10 ≤ Re p ≤ 10 3 . An equation is derived to correct for the wall effects on C D and Nu p and assist the experimenter in the interpretation of measured results.

Chemie Ingenieur TechnikVol. 96(12)
Karlsruhe Institute of Technology (DE)
Deutsche Forschungsgemeinschaft
Openalex Percentile: Top 42%
Heat and Mass Transfer in Porous Media
0.37
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A Numerical Study on the Influence of Confining Walls on Drag and Heat Transfer Coefficients in Single‐Particle Lab‐Scale Reactors — Gregor D. Wehinger, Philipp Reinold, et al. · Chemie Ingenieur Technik (2024) | TGRS Research Map | TGRS