Flow through packed bed reactors: 1. Single-phase flow
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Spherical beads are chosen because the homogenization of this microstructure to obtain macroscopic properties is well studied and considered robust.
“We choose spherical beads because the homogenization of this microstructure to obtain macroscopic properties is well studied and considered robust [19, 47, 48].”
From Topology optimisation of adsorption beds for cost-effective direct air capture (2026) · cites this paper as [48]
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- Authors
- Nemec, D., & Levec, J.
- Affiliations
- National Institute of Chemistry (SI)
- University of Ljubljana (SI)
- Corresponding author
- Levec, Janez
- Venue
- Chemical Engineering Science
- Publisher
- Elsevier BV
- Published
- 2005-12
- Volume
- 60
- Issue
- 24
- Pages
- 6947-6957
- ISSN
- 0009-2509 (ISSN-L)
- OpenAlex
- W1995619639
- Cited by
- 338
- References
- 46
- Citations by year
- 2026: 19 · 2025: 22 · 2024: 29 · 2023: 16 · 2022: 27 · 2021: 18 · 2020: 23 · 2019: 16 · 2018: 23 · 2017: 22 · 2016: 23 · 2015: 18 · 2014: 11 · 2013: 16 · 2012: 4
- FWCI
- 6.82
- Type
- journal article
- Language
- en
- Open access
- closed
- Locations
- Chemical Engineering Science (publishedVersion)
- Topics
- Physical Sciences › Engineering › Computational Mechanics › Heat and Mass Transfer in Porous Media
- Physical Sciences › Engineering › Computational Mechanics › Granular flow and fluidized beds
- Physical Sciences › Engineering › Biomedical Engineering › Fluid Dynamics and Mixing
- Keywords
- fixed-bed reactor, trickle bed reactor, pressure drop, single-phase flow, Ergun equation, non-spherical particles, particle shape effects, random close packing, random loose packing, bed porosity, capillary model, wall effects
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