Analysis of catalyst effectiveness in trickle-bed reactors processing volatile or nonvolatile reactants
Analysis of catalyst effectiveness in trickle-bed reactors processing volatile or nonvolatile reactants
复制标题
处理挥发性或非挥发性反应物的滴流床反应器中的催化剂有效性分析
DOI:
10.1016/0009-2509(80)87004-7
复制
发表时间:
1980
影响因子:
4.7
通讯作者:
M. Duduković
中科院分区:
文献类型:
--
作者:
P. Mills;M. Duduković
The problem of diffusion and first-order reaction in catalyst pellets whose exterior surface is partially wetted, as encountered in trickle-bed reactors; is formulated to account for all cases of interest such as gas or liquid limiting reactants, finite or negligible external surface resistance, and volatile or nonvolatile liquids. It is shown that the problem of evaluating catalyst effectiveness for a slab, cylindrical, or spherical shape results in a general dual-series equation which for a given geometry may be reduced to a variety of cases of interest by proper assignment of Biot numbers for dry and wetted surfaces. The catalyst effectiveness factor is given by a simple expression that depends solely on the Thiele modulus and first series coefficient which is found by numerical solution of the dual-series using the method of weighted residuals. A comparison between effectiveness factors predicted by approximate formulas to those given by the more accurate numerical solutions suggests that these former expressions underestimate the catalyst effectiveness and consequently are safe to employ for initial design estimates. The opposite effect of contacting efficiency on catalyst effectiveness for nonvolatile liquid limiting and gas or volatile liquid limiting reactants is illustrated and quantified. Possible pitfalls of employing reaction studies to determine contacting are also discussed.