Investigation on the influence of particle size and porosity on solid phase fluidization and heat transfer in carbon fibre porous media

IF 1.9 4区 工程技术 Q3 ENGINEERING, CHEMICAL Canadian Journal of Chemical Engineering Pub Date : 2024-10-02 DOI:10.1002/cjce.25511
Licheng Wang, Wenwen Zhang, Zhouzhe Yang
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Abstract

In this paper, the 3D pore structure was reconstructed and solid phase fluidization in porous media was investigated. Based on the two fluid model, a computational fluid dynamics (CFD) model of gas–solid fluidization was established and the influence of particle size and porosity were investigated. When porosity was constant, during the fluidization process, the particle velocity and solid concentration standard deviation gradually decreased, and the bed height increased. At the same time, the smaller the particle size was, the smaller the solid concentration standard deviation was, the faster the bed height increased, and the more the particle temperature decreased. Based on the fixed value of particle size, when studying the effect of porosity on fluidization, it was found that with the enhancement of solid-phase fluidization, particle velocity, solid concentration standard deviation, and particle temperature decreased, and bed height increased. Moreover, when porosity was large, particle velocity decreased rapidly, and solid concentration standard deviation reached a smaller minimum value, which took a longer time. Within the same time, the particle temperature also decreased less.

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粒径和孔隙率对碳纤维多孔介质固相流化和传热影响的研究
本文重建了三维孔隙结构,并研究了多孔介质中的固相流化。在双流体模型的基础上,建立了气固流化的计算流体动力学(CFD)模型,并研究了粒度和孔隙率的影响。当孔隙率不变时,在流化过程中,颗粒速度和固体浓度标准偏差逐渐减小,床层高度增加。同时,粒度越小,固体浓度标准偏差越小,床层高度增加越快,颗粒温度降低越多。在固定粒度值的基础上,研究孔隙率对流化的影响时发现,随着固相流化的增强,颗粒速度、固体浓度标准偏差和颗粒温度降低,床层高度增加。此外,当孔隙率较大时,颗粒速度迅速降低,固体浓度标准偏差达到较小的最小值,所需的时间较长。在同一时间内,颗粒温度的降低幅度也较小。
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来源期刊
Canadian Journal of Chemical Engineering
Canadian Journal of Chemical Engineering 工程技术-工程:化工
CiteScore
3.60
自引率
14.30%
发文量
448
审稿时长
3.2 months
期刊介绍: The Canadian Journal of Chemical Engineering (CJChE) publishes original research articles, new theoretical interpretation or experimental findings and critical reviews in the science or industrial practice of chemical and biochemical processes. Preference is given to papers having a clearly indicated scope and applicability in any of the following areas: Fluid mechanics, heat and mass transfer, multiphase flows, separations processes, thermodynamics, process systems engineering, reactors and reaction kinetics, catalysis, interfacial phenomena, electrochemical phenomena, bioengineering, minerals processing and natural products and environmental and energy engineering. Papers that merely describe or present a conventional or routine analysis of existing processes will not be considered.
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