The inhomogeneous MUSIG model for the simulation of polydispersed flows
Integrity signals
Registry
Cites
Statistics
Claims the paper makes
Claims other papers make about this one
Each is checked against this paper’s own text: does it say what the citing paper says it does?
In iMUSIG, the gaseous disperse phase is divided into N phases (groups), each characterized by its velocity field, and the overall bubble size distribution is represented by dividing the bubble diameter range within each velocity group into several size fractions.
“In the inhomogeneous MUSIG model, the gaseous disperse phase is divided into a number N of phases (groups), where each phase is characterized by its velocity field. Moreover, the overall bubble size distribution is represented by dividing the bubble diameter range within each velocity group into several size fractions.”
From Modeling and Simulation of Photobioreactors with Computational Fluid Dynamics—A Comprehensive Review (2022) · cites this paper as [299]
Krepper et al. [299] developed an inhomogeneous multiple size group (iMUSIG) model and implemented it in CFX.
“Therefore, Krepper et al. [299] developed an inhomogeneous multiple size group (iMUSIG) model and they implemented it in CFX ® .”
From Modeling and Simulation of Photobioreactors with Computational Fluid Dynamics—A Comprehensive Review (2022) · cites this paper as [299]
Cites
Some problems in particle technology
Hulburt, H. M., & Katz, S. (1964) · Chemical Engineering Science · doi:10.1016/0009-2509(64)85047-8 · Cited by 1,670 · see citing works
Theoretical model for drop and bubble breakup in turbulent dispersions
Luo, H., & Svendsen, H. F. (1996) · AIChE Journal · doi:10.1002/aic.690420505 · Cited by 1,250 · see citing works
Bubble coalescence and break-up in air-sparged bubble columns
Prince, M. J., & Blanch, H. W. (1990) · AIChE Journal · doi:10.1002/aic.690361004 · Cited by 1,238 · see citing works
Description of aerosol dynamics by the quadrature method of moments
McGraw, R. (1997) · Aerosol Science and Technology · doi:10.1080/02786829708965471 · Cited by 1,128 · see citing works
Struggle with computational bubble dynamics
(1998) · Multiphase Science and Technology · doi:10.1615/multscientechn.v10.i4.40 · Cited by 663 · see citing works
Foundation of the interfacial area transport equation and its closure relations
Kocamustafaogullari, G., & Ishii, M. (1995) · International Journal of Heat and Mass Transfer · doi:10.1016/0017-9310(94)00183-v · Cited by 503 · see citing works
Shape of liquid drops moving in liquid media
Wellek, R. M., Agrawal, A. K., & Skelland, A. H. P. (1966) · AIChE Journal · doi:10.1002/aic.690120506 · Cited by 435 · see citing works
Validation of CFD models for mono- and polydisperse air–water two-phase flows in pipes
Frank, T., Zwart, P. J., Krepper, E., Prasser, H.-M., & Lucas, D. (2008) · Nuclear Engineering and Design · doi:10.1016/j.nucengdes.2007.02.056 · Cited by 237 · see citing works
Self-citationOn the modelling of bubbly flow in vertical pipes
Krepper, E., Lucas, D., & Prasser, H.-M. (2004) · Nuclear Engineering and Design · doi:10.1016/j.nucengdes.2004.09.006 · Cited by 202 · see citing works
Self-citationDevelopment of co-current air–water flow in a vertical pipe
Lucas, D., Krepper, E., & Prasser, H.-M. (2005) · International Journal of Multiphase Flow · doi:10.1016/j.ijmultiphaseflow.2005.07.004 · Cited by 194 · see citing works
Self-citationLucas, D., Krepper, E., & Prasser, H.-M. (2007) · Chemical Engineering Science · doi:10.1016/j.ces.2007.04.035 · Cited by 168 · see citing works
Self-citationThe Rise of Bubbles in a Vertical Shear Flow
Ervin, E. A., & Tryggvason, G. (1997) · Journal of Fluids Engineering · doi:10.1115/1.2819153 · Cited by 152 · see citing works
Tomiyama, A., Sou, A., Žun, I., et al. (1995) · Elsevier eBooks · doi:10.1016/b978-0-444-81811-9.50005-6 · Cited by 147 · see citing works
Prasser, H.-M., Krepper, E., & Lucas, D. (2002) · International Journal of Thermal Sciences · doi:10.1016/s1290-0729(01)01300-x · Cited by 142 · see citing works
Self-citationEvolution of the structure of a gas–liquid two-phase flow in a large vertical pipe
Prasser, H.-M., Beyer, M., Carl, H., Gregor, S., Lucas, D., Pietruske, H., Schütz, P., & Weiß, F.-P. (2007) · Nuclear Engineering and Design · doi:10.1016/j.nucengdes.2007.02.018 · Cited by 132 · see citing works
Self-citationPrediction of radial gas profiles in vertical pipe flow on the basis of bubble size distribution
Lucas, D., Krepper, E., & Prasser, H.-M. (2001) · International Journal of Thermal Sciences · doi:10.1016/s1290-0729(00)01211-4 · Cited by 101 · see citing works
Self-citationInhomogeneous MUSIG Model - a Population Balance Approach for Polydispersed Bubbly Flows
Frank, T., Zwart, P. J., Shi, J., Krepper, E., Lucas, D., & Rohde, U. L. (2005) · Cited by 79 · see citing works
Self-citationVOF‐Simulation of the Lift Force for Single Bubbles in a Simple Shear Flow
Bothe, D., Schmidtke, M., & Warnecke, H.-J. (2006) · Chemical Engineering & Technology · doi:10.1002/ceat.200600168 · Cited by 74 · see citing works
Lucas, D., Krepper, E., & Prasser, H.-M. (2003) · Prace Instytutu Maszyn Przepływowych · Cited by 18 · see citing works
Self-citation
Flagged first, then by citations
Cited by
Sorted by citations
Two-Phase Bubble Columns: A Comprehensive Review
Besagni, G., Inzoli, F., & Ziegenhein, T. (2018) · ChemEngineering · doi:10.3390/chemengineering2020013 · Cited by 190 · see citing works
Modeling and Simulation of Photobioreactors with Computational Fluid Dynamics—A Comprehensive Review
Luzi, G., & McHardy, C. (2022) · Energies · doi:10.3390/en15113966 · Cited by 44 · see citing works
- Authors
- Krepper, E., Lucas, D., Frank, T., Prasser, H.-M., & Zwart, P. J.
- Affiliations
- Helmholtz-Zentrum Dresden-Rossendorf (DE)
- Ansys (Germany) (DE)
- ETH Zurich (CH)
- Corresponding author
- Krepper, Eckhard
- Venue
- Nuclear Engineering and Design
- Publisher
- Elsevier BV
- Published
- 2008-07
- Volume
- 238
- Issue
- 7
- Pages
- 1690-1702
- ISSN
- 0029-5493 (ISSN-L)
- OpenAlex
- W1977704174
- Cited by
- 275
- References
- 19
- Citations by year
- 2026: 12 · 2025: 10 · 2024: 12 · 2023: 22 · 2022: 14 · 2021: 21 · 2020: 13 · 2019: 26 · 2018: 19 · 2017: 20 · 2016: 21 · 2015: 18 · 2014: 12 · 2013: 14 · 2012: 10
- FWCI
- 6.49
- Type
- journal article
- Language
- en
- Open access
- closed
- Locations
- Nuclear Engineering and Design (publishedVersion)
- Funders
- Bundesministerium für Wirtschaft und Technologie
- Topics
- Physical Sciences › Engineering › Biomedical Engineering › Fluid Dynamics and Mixing
- Physical Sciences › Engineering › Aerospace Engineering › Nuclear Engineering Thermal-Hydraulics
- Physical Sciences › Engineering › Ocean Engineering › Particle Dynamics in Fluid Flows
- Keywords
- bubble size distribution, bubble coalescence, bubble fragmentation, lift force, interfacial forces, vertical pipe flow, gas-liquid two-phase flow, CFX
About these checks
Registry, retraction, Cites and statistics results are computed, not judged, with one exception: a printed reference that no index lists is read once by a model before it counts as a citation error. Claims are extracted by a model and kept only when their quote appears verbatim in the text; each cited source is then checked, with a model’s help, for whether it says what the claim relies on. Those verdicts can be wrong — read the claim’s quote and the cited source before relying on one.
Statistics and arithmetic are recomputed, not judged.
Confidence bands are shown only for fields calibrated on our annotated test set. None is calibrated yet, so no band is shown.
What counts as a claim ›How we measure confidence ›How we check this ›
Are you an author, or do you see a problem with this page? Request a review
