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Heat and Mass Transfer in Packed Beds Accompanied by Exothermic/Endothermic Reactions

填充床中伴随放热/吸热反应的传热和传质

基本信息

批准号：
09650246
负责人：
MORI Hideo
金额：
$ 2.18万
依托单位：
KYUSHU UNIVERSITY
依托单位国家：
日本
项目类别：
Grant-in-Aid for Scientific Research (C)
财政年份：
1997
资助国家：
日本
起止时间：
1997 至 1998
项目状态：
已结题

来源：
https://kaken.nii.ac.jp/grant/KAKENHI-PROJECT-09650246/
关键词：
Adsorbent Packed Bed Heat and Mass Transfer Adsorption Zeolite Steam System Silica Gel Adsorbent Heat Exchanger Experiment Numerical Analysis 熱・物質伝達特性吸着反応脱着反応水系吸着式冷凍サイクル

项目摘要

Experiments and numerical analyses were made on heat and mass transfer in thin packed beds of zeolite 13X and silica gel A adsorbing steam. In addition, the effective thermal conductivity was measured for the beds.1. The adsorption rate generally decreases as the bed thickness increases, and it reduces with the decrease of grain size in the zeolite bed where the adsorption rate is high. These reductions are attributed mainly to the resistance to heat conduction within the bed and more or less to the resistance to mass transfer in the interstices of grains especially in the early stage of the adsorption period. There is an optimum bed thickness at which the amount of adsorbed water per unit area of heat transfer surface takes a maximum, because it depends on both the adsorption rate and the amount of packed adsorbent. In the consolidated bed, the adsorption rate is enhanced in the latter half of the adsorption period. The adsorption rates can be expressed by a single non-dimensional equation, irrespective of kinds of adsorbent, grain size, bed thickness and types of bed.2. The effective thermal conductivity of the adsorbent packed bed can be predicted well by both the Hayashi et al.'s model and Bauer-Schlunder model, by considering the particle thermal conductivity rise due to the steam adsorption.3. The adsorption rate in the bed fixed on the side surfaces of a fin can be evaluated by considering the effect of heat conduction within the fin segment.4. Numerical analyses were made on heat and mass transfer in packed beds adsorbing steam, based on a physical model taking account of elemental processes which take place in the bed. Calculations of the adsorption rate were in good agreement with measurements.

对13 X沸石和硅胶A吸附水蒸气的薄层填料床的传热传质进行了实验和数值分析。此外，还测定了床层的有效导热系数.吸附速率一般随床层厚度的增加而减小，在吸附速率较高的沸石床层中，吸附速率随粒径的减小而减小。这些降低主要归因于床层内的热传导阻力，并或多或少地归因于颗粒间隙中的传质阻力，特别是在吸附期的早期阶段。存在一个最佳床层厚度，在该厚度处，单位传热面积的吸附水量最大，因为它取决于吸附速率和填充的吸附剂的量。在固结床中，吸附速率在吸附期的后半段有所提高。吸附速率可以用一个无量纲方程表示，与吸附剂种类、粒径、床层厚度和床层类型无关.吸附剂填充床的有效导热系数可以由Hayashi等人很好地预测。的模型和Bauer-Schlunder模型，通过考虑蒸汽吸附引起的颗粒热导率上升.固定在翅片侧面的吸附床的吸附速率可以通过考虑翅片段内的热传导效应来评估.本文在考虑床层内基本过程的物理模型基础上，对水蒸气吸附填料床的传热传质过程进行了数值分析。吸附速率的计算与测量结果吻合良好。