REACTIVITY, EXPERIMENTAL STRATEGY AND REACTION-RATE DATA EVALUATION IN NONCATALYTIC GAS-SOLID SYSTEMS

被引:5
作者
RODE, H
ORLICKI, D
HLAVACEK, V
机构
[1] Laboratory for Ceramic and Reaction Engineering, Department of Chemical Engineering, State University of New York at Buffalo, Buffalo
关键词
D O I
10.1016/S0009-2509(05)80009-0
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Important aspects of noncatalytic gas-solid reactions including mass transfer and pore structure, heat transfer, chemical reaction kinetics and equilibrium, mechanical stresses, phase change and sintering are briefly reviewed. An improved strategy for the determination of reaction kinetics is formulated, akin to the systematic procedure which exists for catalytic systems. The synthesis of titanium nitride is utilized as a case study. The approach includes the use of nonisothermal data in addition to the traditional isothermal data as a crucial step to obtain data with sufficient orthogonality to allow rigorous evaluation of competing rate laws. Two particle morphologies are tested and experiments are conducted over a wide range of conversion, temperature and heating rate. Four kinetic laws are evaluated by nonlinear optimization using the BET surface area as a measure of reactivity. The logarithmic law provides a surprisingly good fit of the experimental data. The apparent observed activation energy is a function of temperature, conversion and particle size even though the intrinsic activation energy remains constant. This offers an explanation for discrepancies that exist between kinetic parameters obtained in previous investigations.
引用
收藏
页码:4103 / 4120
页数:18
相关论文
共 85 条
[51]   QUANTITATIVE PHASE-ANALYSIS OF SI3N4 BY X-RAY-DIFFRACTION [J].
PIGEON, RG ;
VARMA, A .
JOURNAL OF MATERIALS SCIENCE LETTERS, 1992, 11 (20) :1370-1372
[52]   RATE OF DIFFUSION-CONTROLLED REACTION BETWEEN A GAS AND A POROUS SOLID SPHERE - REACTION OF SO2 WITH CACO3 [J].
PIGFORD, RL ;
SLIGER, G .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1973, 12 (01) :85-91
[53]  
Pilling NB, 1923, J I MET, V29, P529
[54]   STUDY OF GAS SOLID, HETEROGENEOUS, EXOTHERMIC, NONCATALYTIC REACTIONS IN A FLOW REGIME [J].
RAJAIAH, J ;
DANDEKAR, H ;
PUSZYNSKI, J ;
DEGREVE, J ;
HLAVACEK, V .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1988, 27 (03) :513-518
[55]   EFFECT OF SINTERING AND POROSITY CHANGES ON RATES OF GAS-SOLID REACTIONS [J].
RAMACHANDRAN, PA ;
SMITH, JM .
CHEMICAL ENGINEERING JOURNAL AND THE BIOCHEMICAL ENGINEERING JOURNAL, 1977, 14 (02) :137-146
[56]   PERCOLATION CONCEPTS IN MODELING OF GAS SOLID REACTIONS .1. APPLICATION TO CHAR GASIFICATION IN THE KINETIC REGIME [J].
REYES, S ;
JENSEN, KF .
CHEMICAL ENGINEERING SCIENCE, 1986, 41 (02) :333-343
[57]   PERCOLATION CONCEPTS IN MODELING OF GAS SOLID REACTIONS .2. APPLICATION TO CHAR GASIFICATION IN THE DIFFUSION REGIME [J].
REYES, S ;
JENSEN, KF .
CHEMICAL ENGINEERING SCIENCE, 1986, 41 (02) :345-354
[58]   PERCOLATION CONCEPTS IN MODELING OF GAS SOLID REACTIONS .3. APPLICATION TO SULFATION OF CALCINED LIMESTONE [J].
REYES, S ;
JENSEN, KF .
CHEMICAL ENGINEERING SCIENCE, 1987, 42 (03) :565-574
[59]  
RODE H, 1992, COMBUST SCI TECH, V88, P153
[60]  
RODE H, 1994, IN PRESS AICHE J