The DOI matches its Crossref record; 43 of the 46 references it cites were found in a registry or an index.
Flow through packed bed reactors: 1. Single-phase flow
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“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]
Citations
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“We choose spherical beads because the homogenization of this microstructure to obtain macroscopic properties is well studied and considered robust [19, 47, 48].”
Vargas, J. D. (2013) · RECERCAT (Consorci de Serveis Universitaris de Catalunya)
Metadata
- 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 › Chemical Engineering › Fluid Flow and Transfer Processes › 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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