DETERMINATION OF BOUNDARY CONDITIONS FOR ZERO-ORDER CHEMICAL REACTION INSIDE A SINGLE CATALYST PELLET UNDER TRANSIENT CONDITION

被引:3
作者
Do, D. D. [1 ]
机构
[1] Univ Queensland, Dept Chem Engn, St Lucia, Qld 4067, Australia
关键词
D O I
10.1080/00986448408940110
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The transient boundary condition for a zero-order chemical reaction occurring inside a porous catalyst pellet is determined in this paper by applying a singular perturbation technique to a full transient nonequilibrium adsorption and reaction problem. The reactant exhaustion phenomenon is observed during the transient time course and the reactant-free core interface moves toward the center of the pellet. It was found in this paper that the reactant concentration is zero at the core interface and the slope of the reactant concentration profile at this interface is non-zero, and this non-zero slope of the reactant finally reaches zero when t -> infinity and phi > phi(cri), which is the steady state boundary condition used by many workers in their steady state analysis.
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页码:251 / 265
页数:15
相关论文
共 9 条
[1]  
Aris R., 1975, MATH THEORY DIFFUSIO, VI
[2]  
Bailey J., 1977, BIOCH ENG FUNDAMENTA
[3]  
Cole J. D., 1968, PERTURBATION METHODS
[4]   ON THE ZERO-ORDER CHEMICAL-KINETICS IN A SINGLE CATALYST PELLET [J].
DO, DD .
MATHEMATICAL BIOSCIENCES, 1982, 61 (01) :123-133
[6]   USEFUL REPRESENTATIONS OF SERIES SOLUTIONS FOR TRANSPORT PROBLEMS [J].
DO, DD ;
BAILEY, JE .
CHEMICAL ENGINEERING SCIENCE, 1981, 36 (11) :1811-1818
[7]   CONCENTRATION DISTRIBUTION, EFFECTIVENESS FACTOR, AND REACTANT EXHAUSTION FOR CATALYTIC REACTION WITH VOLUME CHANGE [J].
LIN, K ;
LIH, MM .
AICHE JOURNAL, 1971, 17 (05) :1234-&
[8]  
SATTERFIELD CN, 1971, MASS TRANSFER HETERO
[9]   INFLUENCE OF VOLUME CHANGE ON GAS-PHASE REACTIONS IN POROUS CATALYSTS [J].
WEEKMAN, VW ;
GORRING, RL .
JOURNAL OF CATALYSIS, 1965, 4 (02) :260-&