Jinxin Tie , Yibo He , Donghui Shen , Jie Li , Aolin Gu , Runhui Zhang , Xiaoke Ku , Qingsong Zhang , Jizhong Wu
{"title":"用结合多球模型模拟流化床中湿纤维的运动和断裂","authors":"Jinxin Tie , Yibo He , Donghui Shen , Jie Li , Aolin Gu , Runhui Zhang , Xiaoke Ku , Qingsong Zhang , Jizhong Wu","doi":"10.1016/j.partic.2025.09.001","DOIUrl":null,"url":null,"abstract":"<div><div>In the present study, a combined bonded multi-sphere model was developed, validated, and applied to simulate the motion and breakage behavior of wet fibers in a fluidized bed. The effects of particle resolution, bond number, and humidity coefficient (<em>γ</em>) on fiber breakage rate, breakage location, and fragment size distribution were systematically investigated. Results show that increasing particle resolution from 3 to 6 generally reduces fiber breakage. While a higher bond number lowers the probability of breakage. Two different breakage modes are identified under varying <em>γ</em> values: Mode 1, characterized by breakage due to collisions between rapidly falling individual fibers and fiber clusters, and Mode 2, arising from impacts between fiber clusters and the bed bottom. As <em>γ</em> increases within a certain range, the dominant breakage mechanism transitions from Mode 1 to a mixed mode involving both Modes 1 and 2, accompanied by a shift in the primary breakage location from the corner region toward the center region of the bed. All these findings provide valuable insights into the dynamics of wet fiber fluidization and offer guidance for optimizing wet fiber breakage behavior in real applications.</div></div>","PeriodicalId":401,"journal":{"name":"Particuology","volume":"106 ","pages":"Pages 174-185"},"PeriodicalIF":4.3000,"publicationDate":"2025-09-06","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Modeling the motion and breakage of wet fibers in a fluidized bed using a combined bonded multi-sphere model\",\"authors\":\"Jinxin Tie , Yibo He , Donghui Shen , Jie Li , Aolin Gu , Runhui Zhang , Xiaoke Ku , Qingsong Zhang , Jizhong Wu\",\"doi\":\"10.1016/j.partic.2025.09.001\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><div>In the present study, a combined bonded multi-sphere model was developed, validated, and applied to simulate the motion and breakage behavior of wet fibers in a fluidized bed. The effects of particle resolution, bond number, and humidity coefficient (<em>γ</em>) on fiber breakage rate, breakage location, and fragment size distribution were systematically investigated. Results show that increasing particle resolution from 3 to 6 generally reduces fiber breakage. While a higher bond number lowers the probability of breakage. Two different breakage modes are identified under varying <em>γ</em> values: Mode 1, characterized by breakage due to collisions between rapidly falling individual fibers and fiber clusters, and Mode 2, arising from impacts between fiber clusters and the bed bottom. As <em>γ</em> increases within a certain range, the dominant breakage mechanism transitions from Mode 1 to a mixed mode involving both Modes 1 and 2, accompanied by a shift in the primary breakage location from the corner region toward the center region of the bed. All these findings provide valuable insights into the dynamics of wet fiber fluidization and offer guidance for optimizing wet fiber breakage behavior in real applications.</div></div>\",\"PeriodicalId\":401,\"journal\":{\"name\":\"Particuology\",\"volume\":\"106 \",\"pages\":\"Pages 174-185\"},\"PeriodicalIF\":4.3000,\"publicationDate\":\"2025-09-06\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Particuology\",\"FirstCategoryId\":\"88\",\"ListUrlMain\":\"https://www.sciencedirect.com/science/article/pii/S1674200125002342\",\"RegionNum\":2,\"RegionCategory\":\"材料科学\",\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q2\",\"JCRName\":\"ENGINEERING, CHEMICAL\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Particuology","FirstCategoryId":"88","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S1674200125002342","RegionNum":2,"RegionCategory":"材料科学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q2","JCRName":"ENGINEERING, CHEMICAL","Score":null,"Total":0}
Modeling the motion and breakage of wet fibers in a fluidized bed using a combined bonded multi-sphere model
In the present study, a combined bonded multi-sphere model was developed, validated, and applied to simulate the motion and breakage behavior of wet fibers in a fluidized bed. The effects of particle resolution, bond number, and humidity coefficient (γ) on fiber breakage rate, breakage location, and fragment size distribution were systematically investigated. Results show that increasing particle resolution from 3 to 6 generally reduces fiber breakage. While a higher bond number lowers the probability of breakage. Two different breakage modes are identified under varying γ values: Mode 1, characterized by breakage due to collisions between rapidly falling individual fibers and fiber clusters, and Mode 2, arising from impacts between fiber clusters and the bed bottom. As γ increases within a certain range, the dominant breakage mechanism transitions from Mode 1 to a mixed mode involving both Modes 1 and 2, accompanied by a shift in the primary breakage location from the corner region toward the center region of the bed. All these findings provide valuable insights into the dynamics of wet fiber fluidization and offer guidance for optimizing wet fiber breakage behavior in real applications.
期刊介绍:
The word ‘particuology’ was coined to parallel the discipline for the science and technology of particles.
Particuology is an interdisciplinary journal that publishes frontier research articles and critical reviews on the discovery, formulation and engineering of particulate materials, processes and systems. It especially welcomes contributions utilising advanced theoretical, modelling and measurement methods to enable the discovery and creation of new particulate materials, and the manufacturing of functional particulate-based products, such as sensors.
Papers are handled by Thematic Editors who oversee contributions from specific subject fields. These fields are classified into: Particle Synthesis and Modification; Particle Characterization and Measurement; Granular Systems and Bulk Solids Technology; Fluidization and Particle-Fluid Systems; Aerosols; and Applications of Particle Technology.
Key topics concerning the creation and processing of particulates include:
-Modelling and simulation of particle formation, collective behaviour of particles and systems for particle production over a broad spectrum of length scales
-Mining of experimental data for particle synthesis and surface properties to facilitate the creation of new materials and processes
-Particle design and preparation including controlled response and sensing functionalities in formation, delivery systems and biological systems, etc.
-Experimental and computational methods for visualization and analysis of particulate system.
These topics are broadly relevant to the production of materials, pharmaceuticals and food, and to the conversion of energy resources to fuels and protection of the environment.