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International Journal of Fluid Mechanics Research

Publicou 6 edições por ano

ISSN Imprimir: 2152-5102

ISSN On-line: 2152-5110

The Impact Factor measures the average number of citations received in a particular year by papers published in the journal during the two preceding years. 2017 Journal Citation Reports (Clarivate Analytics, 2018) IF: 1.1 To calculate the five year Impact Factor, citations are counted in 2017 to the previous five years and divided by the source items published in the previous five years. 2017 Journal Citation Reports (Clarivate Analytics, 2018) 5-Year IF: 1.3 The Eigenfactor score, developed by Jevin West and Carl Bergstrom at the University of Washington, is a rating of the total importance of a scientific journal. Journals are rated according to the number of incoming citations, with citations from highly ranked journals weighted to make a larger contribution to the eigenfactor than those from poorly ranked journals. Eigenfactor: 0.0002 The Journal Citation Indicator (JCI) is a single measurement of the field-normalized citation impact of journals in the Web of Science Core Collection across disciplines. The key words here are that the metric is normalized and cross-disciplinary. JCI: 0.33 SJR: 0.256 SNIP: 0.49 CiteScore™:: 2.4 H-Index: 23

Indexed in

Eulerian Modeling of Gas-Solid Flow with Solid Volume Fraction up to 0.1

Volume 42, Edição 4, 2015, pp. 355-373
DOI: 10.1615/InterJFluidMechRes.v42.i4.50
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RESUMO

This paper presents the results related to the CFD simulations using the two-fluid model approach to study the effects of solids volume fraction and gas phase Reynolds number on the pressure drop in a fully developed gas-solid flow. A horizontal pipe of internal diameter 30 mm and length 3 m is considered for this study. The Gidaspow drag model with algebraic granular temperature model is used for the simulations. Numerical results are compared with the bench mark experimental data, and good agreement is found with a maximum deviation of −20 %. The solids volume fractions ranging from 0.01 to 0.1 and gas phase Reynolds numbers ranging from 20000 to 100000 are used in the present study. The numerical results indicate that the magnitude of the pressure drop is higher for higher values of the solids volume fraction and gas phase Reynolds number.

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