Solid conduction effects and design criteria in moving bed heat exchangers

被引:29
作者
Almendros-Ibanez, J. A. [1 ,2 ]
Soria-Verdugo, A. [3 ]
Ruiz-Rivas, U. [3 ]
Santana, D. [3 ]
机构
[1] Univ Castilla La Mancha, Escuela Ingenieros Ind, Dpto Mecan Aplicada & Ingn Proyectos, Albacete 02071, Spain
[2] Renewable Energy Res Inst, Sect Solar & Energy Efficiency, Albacete 02071, Spain
[3] Univ Carlos III Madrid, ISE Res Grp, Thermal & Fluid Engn Dept, Madrid 28911, Spain
关键词
Moving bed heat exchanger; Heat transfer; Biot number; Packed bed; HOT GAS FILTRATION; GRANULAR BED; PACKED-BEDS; FLOW; REACTOR; THICKNESS; PROFILES; FILTERS; MODELS; WALL;
D O I
10.1016/j.applthermaleng.2010.12.021
中图分类号
O414.1 [热力学];
学科分类号
摘要
This work presents a theoretical study of the energetic performance of a moving bed heat exchanger (MBHE), which consists of a flow of solid particles moving down that recovers heat from a gas flow percolating the solids in cross-flow. In order to define the solid conduction effects, two solutions for the MBHE energy equations have been studied: an analytical solution considering only convection heat transfer (and neglecting solid conduction) and a numerical solution with the solid conductivity retained in the equations. In a second part, the power requirements of a MBHE (to pump the gas and to raise the down-flowing particles) are confronted with the heat transferred considering the variation of design parameters, such as gas and solids' velocities, solids particle diameter or MBHE dimensions. The numerical results show that solid conductivity reduces the global efficiency of the heat exchanger. Therefore, a selection criterion for the solids can be established, in which their thermal conductivity should be minimized to avoid conduction through the solid phase, but to a limit in order to ensure that temperature differences inside an individual solid particle remain small. Regarding the other energy interactions involved in the system, these are at least one order of magnitude lower than the heat exchanged. Nevertheless, for a proper analysis of the system the efficiency of the devices used to pump the gas and to raise the particles and the relative costs of the different energy forms present in the system should be taken into account. (C) 2010 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1200 / 1207
页数:8
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