NUMERICAL CONSTRUCTION OF BIFURCATION DIAGRAMS FOR NONLINEAR COMPLEX-REACTION NETWORKS IN CATALYTIC REACTORS

被引:3
作者
HELAL, AM [1 ]
ELNASHAIE, SS [1 ]
机构
[1] KING SAUD UNIV,COLL ENGN,DEPT CHEM ENGN,POB 800,RIYADH 11421,SAUDI ARABIA
关键词
D O I
10.1016/0098-1354(90)87038-Q
中图分类号
TP39 [计算机的应用];
学科分类号
081203 ; 0835 ;
摘要
[No abstract available]
引用
收藏
页码:691 / 697
页数:7
相关论文
共 21 条
[1]  
[Anonymous], 1991, FLUID ENG, DOI DOI 10.1016/B978-0-08-050664-7.50009-3
[2]  
Aris R., 1969, ELEMENTARY CHEM REAC
[3]  
BENNETT JM, 1965, NUMER MATH, V7, P217
[4]  
BOCK HJ, 1983, GER CHEM ENG, V6, P57
[5]  
BROYDEN CG, 1965, MATH COMPUT, V19, P577, DOI DOI 10.1090/S0025-5718-1965-0198670-6
[6]   THE EFFECT OF BUBBLE-SIZE VARIATION ON THE PERFORMANCE OF FLUIDIZED-BED REACTORS [J].
BUKUR, DB ;
NASIF, N .
CHEMICAL ENGINEERING SCIENCE, 1985, 40 (10) :1925-1933
[7]   MODELING OF FLUIDIZED-BED REACTORS .2. UNIFORM CATALYST TEMPERATURE AND CONCENTRATION [J].
BUKUR, DB ;
AMUNDSON, NR .
CHEMICAL ENGINEERING SCIENCE, 1975, 30 (08) :847-858
[8]   ANALYSIS OF A MODEL FOR A NONISOTHERMAL CONTINUOUS FLUIDIZED-BED CATALYTIC REACTOR [J].
BUKUR, DB ;
WITTMANN, CV ;
AMUNDSON, NR .
CHEMICAL ENGINEERING SCIENCE, 1974, 29 (05) :1173-1192
[9]  
Cajori Florian, 1980, HIST MATH
[10]   PREDICTION OF PACKED-BED CATALYTIC REACTOR PERFORMANCE FOR A COMPLEX-REACTION (OXIDATION OF ORTHO-XYLENE TO PHTHALIC-ANHYDRIDE) [J].
CHANDRASEKHARAN, K ;
CALDERBANK, PH .
CHEMICAL ENGINEERING SCIENCE, 1979, 34 (11) :1323-1331