{"title":"Effect of mixing ratio on flow characteristics of binary particles in a fluidized bed","authors":"Qiuqin Gou , Dongmei Song , Haokun Wu , Shiqi Wen , Guoding Chen","doi":"10.1016/j.powtec.2025.121132","DOIUrl":null,"url":null,"abstract":"<div><div>Understanding the flow characteristics of binary non-spherical particles in a gas-solid spouted bed is important to improve the process design of the equipment. In this paper, the effect of the volume fraction share of spherocylindrical particles versus spherical particles in a binary particle system on the particle fluidization mechanism inside a spouted bed is analyzed by CFD-DEM method. Particle forces, velocities, collisions, mixing, and concentration distribution characteristics were investigated through qualitative and quantitative perspectives, respectively. The results show that with the increase of the volume fraction of spherocylindrical particles in the binary particle system, the drag force of different types of particles increases and the average velocity decreases, which helps to improve the mixing rate of different types of particles, and the rotational velocity of spherocylindrical particles increases and the rotational velocity of spherocylindrical particles decreases, which accelerates the collision frequency of the particles tends to be in a stable state. Increasing the superficial gas velocity helps to increase particle drag force, mixing properties, and rotational velocity. However, the average velocity of the particles does not necessarily increase (e.g., <em>Vol</em> = 25 % and <em>Vol</em> = 50 %). In addition, the spherocylindrical particles contact force is significantly larger than the fluid-particle interaction force, and the values of the forces are, in descending order, particle contact force, pressure gradient force, drag force, virtual mass force, and lift force. Compared with the low bed layer, the particles in the high bed layer are more significantly affected by the gas flow perturbation and the flow is more active.</div></div>","PeriodicalId":407,"journal":{"name":"Powder Technology","volume":"462 ","pages":"Article 121132"},"PeriodicalIF":4.5000,"publicationDate":"2025-05-18","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/S0032591025005273","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
Understanding the flow characteristics of binary non-spherical particles in a gas-solid spouted bed is important to improve the process design of the equipment. In this paper, the effect of the volume fraction share of spherocylindrical particles versus spherical particles in a binary particle system on the particle fluidization mechanism inside a spouted bed is analyzed by CFD-DEM method. Particle forces, velocities, collisions, mixing, and concentration distribution characteristics were investigated through qualitative and quantitative perspectives, respectively. The results show that with the increase of the volume fraction of spherocylindrical particles in the binary particle system, the drag force of different types of particles increases and the average velocity decreases, which helps to improve the mixing rate of different types of particles, and the rotational velocity of spherocylindrical particles increases and the rotational velocity of spherocylindrical particles decreases, which accelerates the collision frequency of the particles tends to be in a stable state. Increasing the superficial gas velocity helps to increase particle drag force, mixing properties, and rotational velocity. However, the average velocity of the particles does not necessarily increase (e.g., Vol = 25 % and Vol = 50 %). In addition, the spherocylindrical particles contact force is significantly larger than the fluid-particle interaction force, and the values of the forces are, in descending order, particle contact force, pressure gradient force, drag force, virtual mass force, and lift force. Compared with the low bed layer, the particles in the high bed layer are more significantly affected by the gas flow perturbation and the flow is more active.
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.