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
Cites
Fluid Flow Through Packed Columns
Ergün, Ş. (1952) · Medical Entomology and Zoology · Cited by 6,992
Porous Media: Fluid Transport and Pore Structure
Dullien, F. A. L. (1979) · Cited by 3,995
The Physics of Flow Through Porous Media
Scheidegger, A. E. (1958) · Soil Science · doi:10.1097/00010694-195812000-00015 · Cited by 2,596
Porous Media: Fluid Transport and Pore Structure
Mason, G. (1981) · The Chemical Engineering Journal · doi:10.1016/0300-9467(81)80049-4 · Cited by 2,074
Flow through Porous Media-the Ergun Equation Revisited
MacDonald, I. F., El-Sayed, M., Mow, K., & Dullien, F. A. L. (1979) · Industrial & Engineering Chemistry Fundamentals · doi:10.1021/i160071a001 · Cited by 1,082
Packing of Spheres: Packing of Equal Spheres
Scott, G. D. (1960) · Nature · doi:10.1038/188908a0 · Cited by 835
The physics of flow through porous media
Yager, W. C. (1957) · Journal of the Franklin Institute · doi:10.1016/0016-0032(57)90199-0 · Cited by 603
Comiti, J., & Renaud, M. (1989) · Chemical Engineering Science · doi:10.1016/0009-2509(89)80031-4 · Cited by 545
Moderate-Reynolds-number flows in ordered and random arrays of spheres
Hill, R. J., Koch, D. L., & Ladd, A. J. C. (2001) · Journal of Fluid Mechanics · doi:10.1017/s0022112001005936 · Cited by 494
The first effects of fluid inertia on flows in ordered and random arrays of spheres
Hill, R. J., Koch, D. L., & Ladd, A. J. C. (2001) · Journal of Fluid Mechanics · doi:10.1017/s0022112001005948 · Cited by 422
The influence of confining walls on the pressure drop in packed beds
Eisfeld, B., & Schnitzlein, K. (2001) · Chemical Engineering Science · doi:10.1016/s0009-2509(00)00533-9 · Cited by 384
Fand, R. M., Kim, B. Y. K., Lam, A. C. C., & Phan, R. T. (1987) · Journal of Fluids Engineering · doi:10.1115/1.3242658 · Cited by 296
Einflüsse der Porosität und Korngrößenverteilung im Widerstandsgesetz der Porenströmung
Rumpf, H., & Gupte, A. R. (1971) · Chemie Ingenieur Technik · doi:10.1002/cite.330430610 · Cited by 245
Physical insight into the Ergun and Wen & Yu equations for fluid flow in packed and fluidised beds
Niven, R. K. (2002) · Chemical Engineering Science · doi:10.1016/s0009-2509(01)00371-2 · Cited by 198
Pressure Drop in Packed Beds of Spheres
Hicks, R. E. (1970) · Industrial & Engineering Chemistry Fundamentals · doi:10.1021/i160035a032 · Cited by 189
Rutgers, R. P. G. (1962) · Nature · doi:10.1038/193465a0 · Cited by 188
Zur Berechnung des Druckverlustes einphasig durchströmter Kugel‐ und Zylinderschüttungen
Reichelt, W. (1972) · Chemie Ingenieur Technik · doi:10.1002/cite.330441806 · Cited by 162
Packed bed pressure drop—an extension to higher Reynolds numbers
Tallmadge, J. A. (1970) · AIChE Journal · doi:10.1002/aic.690160639 · Cited by 151
A generalized Blake‐Kozeny equation for multisized spherical particles
MacDonald, M. J., Chu, C. F., Guilloit, P. P., & Ng, K. M. (1991) · AIChE Journal · doi:10.1002/aic.690371016 · Cited by 143
Impact of tube‐to‐particle‐diameter ratio on pressure drop in packed beds
Winterberg, M., & Tsotsas, E. (2000) · AIChE Journal · doi:10.1002/aic.690460519 · Cited by 112
Steady incompressible laminar flow in porous media
Liu, S., Afacan, A., & Masliyah, J. H. (1994) · Chemical Engineering Science · doi:10.1016/0009-2509(94)00168-5 · Cited by 110
Wall effects for the pressure drop in fixed beds
Felice, R. D., & Gibilaro, L. G. (2004) · Chemical Engineering Science · doi:10.1016/j.ces.2004.03.030 · Cited by 105
SINGLE FLUID FLOW IN POROUS MEDIA
Liu, S., & Masliyah, J. H. (1996) · Chemical Engineering Communications · doi:10.1080/00986449608936537 · Cited by 100
The Influence of the Wall on Flow Through Pipes Packed With Spheres
Fand, R. M., & Thinakaran, R. (1990) · Journal of Fluids Engineering · doi:10.1115/1.2909373 · Cited by 95
Iliuta, I., Larachi, F., & Grandjean, B. P. A. (1998) · Industrial & Engineering Chemistry Research · doi:10.1021/ie980394r · Cited by 79
Einfluß des Lückenvolumens auf den Druckverlust in gasdurchströmten Füllkörpersäulen
Sonntag, G. (1960) · Chemie Ingenieur Technik · doi:10.1002/cite.330320502 · Cited by 67
Flow through packed bed reactors: 2. Two-phase concurrent downflow
Nemec, D., & Levec, J. (2005) · Chemical Engineering Science · doi:10.1016/j.ces.2005.05.069 · Cited by 65
Self-citationElucidation of pressure drop in packed-bed systems
Foumeny, E. A., Kulkarni, A., Roshani, S., & Vatani, A. (1996) · Applied Thermal Engineering · doi:10.1016/1359-4311(95)00002-x · Cited by 44
The Influence of Surface Roughness on Resistance to Flow Through Packed Beds
Crawford, C. W., & Plumb, O. A. (1986) · Journal of Fluids Engineering · doi:10.1115/1.3242584 · Cited by 42
Theoretical consideration of permeation resistance of fluid through a particle packed layer
Endo, Y., Chen, D., & Pui, D. Y. H. (2002) · Powder Technology · doi:10.1016/s0032-5910(01)00479-x · Cited by 41
Hydrodynamics of trickling flow in packed beds: Relative permeability concept
Lakota, A., Levec, J., & Carbonell, R. G. (2002) · AIChE Journal · doi:10.1002/aic.690480408 · Cited by 39
Self-citationSingle phase flow modeling in packed beds: discrete cell approach revisited
Jiang, Y., Khadilkar, M. R., Al‐Dahhan, M. H., & Duduković, M. P. (2000) · Chemical Engineering Science · doi:10.1016/s0009-2509(99)00453-4 · Cited by 39
Pressure drop during the flow of a Newtonian fluid through a fixed bed of particles
Dolejš, V., & Machač, I. (1995) · Chemical Engineering and Processing - Process Intensification · doi:10.1016/0255-2701(94)00566-4 · Cited by 29
Process Development and Scale Up: II. Catalyst Design Strategy
Sie, S. T., & Krishna, R. (1998) · Reviews in Chemical Engineering · doi:10.1515/revce.1998.14.3.159 · Cited by 28
Hydroprocessing conditions affect catalyst shape selection
Cooper, B. H., Donnis, B. B. L., & Moyse, B. M. (1986) · Oil & gas journal/Oil and gas journal · Cited by 24
Tukač, V., & Hanika, J. (1992) · Chemical Engineering Science · doi:10.1016/0009-2509(92)87039-s · Cited by 23
Hydrodynamics of pulsing flow in three-phase chemical reactors
Burghardt, A., Bartelmus, G., & Gancarczyk, A. (1999) · Chemical Engineering and Processing - Process Intensification · doi:10.1016/s0255-2701(99)00039-2 · Cited by 21
Limits of applicability of capillary model for pressure drop correlation
Punčochář, M., & Drahoš, J. (2000) · Chemical Engineering Science · doi:10.1016/s0009-2509(00)00025-7 · Cited by 18
Intraparticle diffusion and reaction kinetics as factors in catalyst particle design
Sie, S. T. (1993) · The Chemical Engineering Journal and the Biochemical Engineering Journal · doi:10.1016/0923-0467(93)80002-e · Cited by 17
Gravimetric Method for the Determination of Liquid Holdup in Pressurized Trickle-Bed Reactors
Nemec, D., Berčič, G., & Levec, J. (2001) · Industrial & Engineering Chemistry Research · doi:10.1021/ie010061l · Cited by 15
Self-citationTHE EFFECT OF SURFACE ROUGHNESS ON PRESSURE DROP IN A PACKED BED
JORDI, R. G., Young, B. D., & VLIET, B. M. V. (1990) · Chemical Engineering Communications · doi:10.1080/00986449008940565 · Cited by 11
Worstell, J. H. (1992) · Chemical engineering progress · Cited by 7
PRESSURE DROP IN FLOW OF A NEARLY CRITICAL FLUID THROUGH PACKED BEDS OF SPHERES
Salatino, P., & Massimilla, L. (1990) · Chemical Engineering Communications · doi:10.1080/00986449008911439 · Cited by 4
Research works printed but not linked: 5
- Carman, 1937, Fluid flow through packed beds, Transactions of the Institution of Chemical Engineers, 15, 150
- England, 1970, Dispersion, pressure drop, and chemical reaction in packed beds of cylindrical particles, Transactions of the Institution of Chemical Engineers, 48, 265
- Nemec, D., 2003. Pressure drop and liquid holdup in packed beds with cocurrent two-phase flow at high pressures. Ph.D. Thesis, University of Ljubljana (in English).
- Pahl, M.H., 1975. Über die Kennzeichnung diskret disperser Systeme und die systematische Variation der Einflußgrößen zur Ermittlung eines allgemeingültigeren Widerstands-gesetzes der Porenströmung, Ph.D. Thesis, University of Karlsruhe.
- Wooten, 1998, Dense and sock catalyst loading compared, Oil & Gas Journal October, 12, 66
Cited by
Sorted by citations
Zhong, W., Yu, A., Liu, X., Tong, Z., & Zhang, H. (2016) · Powder Technology · doi:10.1016/j.powtec.2016.07.010 · Cited by 663
Analysis of Flow in Fractal Porous Media
Yu, B. (2008) · Applied Mechanics Reviews · doi:10.1115/1.2955849 · Cited by 527
A review on experience feedback and numerical modeling of packed-bed thermal energy storage systems
Esence, T., Bruch, A., Molina, S., Stutz, B., & Fourmigué, J.-F. (2017) · Solar Energy · doi:10.1016/j.solener.2017.03.032 · Cited by 335
Adiabatic Compressed Air Energy Storage with packed bed thermal energy storage
Barbour, E. R., Mignard, D., Ding, Y., & Li, Y. (2015) · Applied Energy · doi:10.1016/j.apenergy.2015.06.019 · Cited by 279
Allen, K. G., von Backström, T. W., & Kroger, D. G. (2013) · Powder Technology · doi:10.1016/j.powtec.2013.06.022 · Cited by 264
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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