MODEL FOR COKE OXIDATION FROM CATALYST PELLETS IN INITIAL BURNING PERIOD

被引:15
作者
RAMACHANDRAN, PA [1 ]
RASHID, MH [1 ]
HUGHES, R [1 ]
机构
[1] UNIV SALFORD,DEPT CHEM ENGN,SALFORD M5 4WT,ENGLAND
关键词
D O I
10.1016/0009-2509(75)85070-6
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
引用
收藏
页码:1391 / 1398
页数:8
相关论文
共 11 条
[1]   A DIFFUSE INTERFACE MODEL FOR FLUID-SOLID REACTION [J].
BOWEN, JH ;
CHENG, CK .
CHEMICAL ENGINEERING SCIENCE, 1969, 24 (12) :1829-&
[2]  
CALVELO A, 1970, CHEMICA
[3]   COMPARISON OF KINETIC AND DIFFUSIONAL MODELS FOR SOLID-GAS REACTIONS [J].
ISHIDA, M ;
WEN, CY .
AICHE JOURNAL, 1968, 14 (02) :311-&
[4]   OXIDATION OF COKED SILICA-ALUMINA CATALYST [J].
MASSOTH, FE .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1967, 6 (02) :200-&
[5]  
SAMPATH BS, TO BE PUBLISHED
[6]  
SHETTIGAR UR, 1972, CHEM ENGNG J, V4, P208
[7]   STRUCTURAL MODEL FOR GAS-SOLID REACTIONS WITH A MOVING BOUNDARY .2. EFFECT OF GRAIN SIZE, POROSITY AND TEMPERATURE ON REACTION OF POROUS PELLETS [J].
SZEKELY, J ;
EVANS, JW .
CHEMICAL ENGINEERING SCIENCE, 1971, 26 (11) :1901-&
[8]   A STRUCTURAL MODEL FOR GAS-SOLID REACTIONS WITH A MOVING BOUNDARY [J].
SZEKELY, J ;
EVANS, JW .
CHEMICAL ENGINEERING SCIENCE, 1970, 25 (06) :1091-&
[9]   GAS REACTIONS OF CARBON [J].
WALKER, PL ;
RUSINKO, F ;
AUSTIN, LG .
ADVANCES IN CATALYSIS, 1959, 11 :133-221
[10]  
YAGI S, 1959, SOC CHEM IND JAPAN, V56, P131