Wall heat transfer coefficient and effective radial conductivity of ceramic foam catalyst supports

被引:7
|
作者
Turchetti, L. [1 ]
Murmura, M. A. [2 ]
Monteleone, G. [1 ]
Annesini, M. C. [2 ]
机构
[1] ENEA Italian Natl Agcy New Technol, Energy & Sustainable Econ Dev, Via Anguillarese 301, I-00123 Rome, Italy
[2] Sapienza Univ Roma, Dipartimento Ingn Chim Mat Ambiente, Via Eudossiana 18, I-00184 Rome, Italy
来源
CHEMICAL ENGINEERING RESEARCH & DESIGN | 2020年 / 156卷 / 156期
关键词
Solid foam; Wall heat transfer coefficient; Effective conductivity; Pressure drop; Silicon carbide; Alumina; TRANSPORT; MEMBRANE; OPTIMIZATION; PACKINGS; GAS; PD;
D O I
10.1016/j.cherd.2020.01.021
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In this work, different tubular solid-foam packed-beds were experimentally investigated under air flow in order to determine the effective conductivity and wall-to-bed heat transfer coefficient. Several foam types with different material, namely silicon carbide and alumina, and cell density were tested. Foam samples were experimentally studied using different air flow rates and wall temperatures ranging between 200 and 500 degrees C. Axial and radial steady-state temperatures in the bed were experimentally measured and analysed with a two-dimensional, one-equation model. A Chilton-Colburn-type correlation based on the reactor diameter as characteristic dimension was proposed for the wall-to-bed heat transfer coefficient, which proved good to describe the behaviour of all tested foams. Effective radial thermal conductivity and pressure drop in the foams were also characterized. (C) 2020 Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
引用
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页码:146 / 155
页数:10
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