{"title":"A Stokes number-dependent filtered drag model for fluidized gas-particle beds with varying material properties","authors":"Yiming Zhao , Shouzheng Yuan , Xiao Chen , Qiang Zhou","doi":"10.1016/j.powtec.2025.120860","DOIUrl":null,"url":null,"abstract":"<div><div>In fluidized bed systems, accurately predicting drag forces is essential for understanding particle-fluid interactions, and the drag force model should be applicable across a wide range of parameters for particles with varying material properties, such as Geldart A, B, and D types. Using fine-grid two-fluid simulation data from periodic sedimentation systems, this study examines the influence of Stokes number <em>St</em>, density ratio <em>DR</em>, dimensionless filter size, and filtered solid volume fraction <span><math><msub><mover><mi>ϕ</mi><mo>¯</mo></mover><mi>s</mi></msub></math></span> on the heterogeneous index <span><math><msub><mi>H</mi><mi>d</mi></msub></math></span>. For the same <em>St</em> but different <em>DR</em>, <span><math><msub><mi>H</mi><mi>d</mi></msub></math></span> decreases as <em>DR</em> increases. Conversely, for the same <em>DR</em> but different <em>St</em>, a critical solid volume fraction <span><math><msub><mover><mi>ϕ</mi><mo>¯</mo></mover><mrow><mi>s</mi><mo>,</mo><mi>c</mi></mrow></msub></math></span> of approximately 0.32 is observed: when <span><math><msub><mover><mi>ϕ</mi><mo>¯</mo></mover><mi>s</mi></msub><mo><</mo><msub><mover><mi>ϕ</mi><mo>¯</mo></mover><mrow><mi>s</mi><mo>,</mo><mi>c</mi></mrow></msub></math></span>, <span><math><msub><mi>H</mi><mi>d</mi></msub></math></span> increases with larger <em>St</em>, while when <span><math><msub><mover><mi>ϕ</mi><mo>¯</mo></mover><mi>s</mi></msub><mo>></mo><msub><mover><mi>ϕ</mi><mo>¯</mo></mover><mrow><mi>s</mi><mo>,</mo><mi>c</mi></mrow></msub></math></span>, <span><math><msub><mi>H</mi><mi>d</mi></msub></math></span> increases with smaller <em>St</em>. Furthermore, <span><math><msub><mi>H</mi><mi>d</mi></msub></math></span> approaches unity at high <em>St</em> (<em>St</em> > 20,000) for Geldart D particles. Based on these findings, a unified filtered drag model was developed by incorporating <em>St</em> to capture the impact of material properties. The proposed model demonstrates favorable performance in <em>a posteriori</em> tests across various fluidized beds.</div></div>","PeriodicalId":407,"journal":{"name":"Powder Technology","volume":"457 ","pages":"Article 120860"},"PeriodicalIF":4.5000,"publicationDate":"2025-03-05","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Powder Technology","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S0032591025002554","RegionNum":2,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q2","JCRName":"ENGINEERING, CHEMICAL","Score":null,"Total":0}
引用次数: 0
Abstract
In fluidized bed systems, accurately predicting drag forces is essential for understanding particle-fluid interactions, and the drag force model should be applicable across a wide range of parameters for particles with varying material properties, such as Geldart A, B, and D types. Using fine-grid two-fluid simulation data from periodic sedimentation systems, this study examines the influence of Stokes number St, density ratio DR, dimensionless filter size, and filtered solid volume fraction on the heterogeneous index . For the same St but different DR, decreases as DR increases. Conversely, for the same DR but different St, a critical solid volume fraction of approximately 0.32 is observed: when , increases with larger St, while when , increases with smaller St. Furthermore, approaches unity at high St (St > 20,000) for Geldart D particles. Based on these findings, a unified filtered drag model was developed by incorporating St to capture the impact of material properties. The proposed model demonstrates favorable performance in a posteriori tests across various fluidized beds.
期刊介绍:
Powder Technology is an International Journal on the Science and Technology of Wet and Dry Particulate Systems. Powder Technology publishes papers on all aspects of the formation of particles and their characterisation and on the study of systems containing particulate solids. No limitation is imposed on the size of the particles, which may range from nanometre scale, as in pigments or aerosols, to that of mined or quarried materials. The following list of topics is not intended to be comprehensive, but rather to indicate typical subjects which fall within the scope of the journal's interests:
Formation and synthesis of particles by precipitation and other methods.
Modification of particles by agglomeration, coating, comminution and attrition.
Characterisation of the size, shape, surface area, pore structure and strength of particles and agglomerates (including the origins and effects of inter particle forces).
Packing, failure, flow and permeability of assemblies of particles.
Particle-particle interactions and suspension rheology.
Handling and processing operations such as slurry flow, fluidization, pneumatic conveying.
Interactions between particles and their environment, including delivery of particulate products to the body.
Applications of particle technology in production of pharmaceuticals, chemicals, foods, pigments, structural, and functional materials and in environmental and energy related matters.
For materials-oriented contributions we are looking for articles revealing the effect of particle/powder characteristics (size, morphology and composition, in that order) on material performance or functionality and, ideally, comparison to any industrial standard.