Effects of cylindrical particle structure modification on the flow and heat transfer characteristics in packed beds

被引:0
作者
Bao, Xing [1 ]
Guo, Xueyan [1 ]
机构
[1] School of Energy and Power Engineering, University of Shanghai for Science and Technology, Shanghai
来源
Huagong Xuebao/CIESC Journal | 2025年 / 76卷 / 06期
关键词
cylindrical particle; flow; heat transfer; numerical simulation; packed bed;
D O I
10.11949/0438-1157.20241343
中图分类号
学科分类号
摘要
To investigate the effects of different modified cylindrical particle shapes on the wall effect and flow-heat transfer characteristics in packed beds, computational fluid dynamics (CFD) methods were employed to perform numerical simulations on six types of packed beds filled with particles: unmodified cylindrical particles and modified single-hole cylindrical, 3-hole cylindrical, trilobe, 3-hole trilobe, and 9-hole trilobe particles. The radial and axial porosity distributions, flow characteristics, and flow-heat transfer performance were analyzed. The results show that the cylindrical particles can improve the uniformity of fluid flow by either internal openings or external slots. Internal perforation reduces the proportion of flow near the wall, and the number of perforations has no significant effect on the flow near the wall. However, increasing the number of perforations weakens the uniformity of radial flow distribution while enhancing the uniformity of axial flow distribution. External grooving of cylindrical particles into a Trilobe shape improves the heat transfer coefficient but significantly increases the unit pressure drop. In contrast, internal perforation reduces both the heat transfer coefficient and unit pressure drop. Increasing the number of perforations enhances heat transfer performance but also results in a higher pressure drop. Considering both heat transfer performance and flow resistance, the mixed-modified 9-hole trilobe particles exhibit the highest overall heat transfer efficiency and demonstrate the best comprehensive heat transfer performance. © 2025 Materials China. All rights reserved.
引用
收藏
页码:2603 / 2615
页数:12
相关论文
共 34 条
[1]  
Karthik G M, Buwa V V., Particle-resolved simulations of methane steam reforming in multilayered packed beds, AIChE Journal, 64, 11, pp. 4162-4176, (2018)
[2]  
Wang J Y, Yang J, Sunden B, Et al., Hydraulic and heat transfer characteristics in structured packed beds with methane steam reforming reaction for energy storage, International Communications in Heat and Mass Transfer, 121, (2021)
[3]  
Kim S G, Addad Y, Liu M L, Et al., Computational investigation into heat transfer coefficients of randomly packed pebbles in flowing FLiBe, International Journal of Heat and Mass Transfer, 145, (2019)
[4]  
Wang M H, Bu S S, Zhou B, Et al., Pore-scale simulation on flow and heat transfer characteristics in packed beds with internal heat sources at low Reynolds numbers, International Journal of Heat and Mass Transfer, 213, (2023)
[5]  
Huang Z G, Sun Z G., Simulation of the application of nano-scale phase change microcapsules for thermal storage in structured packed bed, CIESC Journal, 74, 10, pp. 4109-4128, (2023)
[6]  
Li C, Li Q, Ding Y L., Investigation on the thermal performance of a high temperature packed bed thermal energy storage system containing carbonate salt based composite phase change materials, Applied Energy, 247, pp. 374-388, (2019)
[7]  
Guo X Y., CFD modeling of heat transfer in fixed bed reactors, Journal of Chemical Industry and Engineering (China), 59, 8, pp. 1914-1922, (2008)
[8]  
Guo X Y, Chao D H, Chai H S, Et al., CFD analysis of wall effects in packed beds with small tube-to-sphere diameter ratio, CIESC Journal, 63, 1, pp. 103-108, (2012)
[9]  
Dong Y, Sosna B, Korup O, Et al., Investigation of radial heat transfer in a fixed-bed reactor: CFD simulations and profile measurements, Chemical Engineering Journal, 317, pp. 204-214, (2017)
[10]  
Guo X Y, Zhu Z P., CFD based modeling on chemical looping combustion in a packed bed reactor, Chemical Engineering Science, 138, pp. 303-314, (2015)