DYNAMIC MODELING OF AN INDUSTRIAL FLUID CATALYTIC CRACKING UNIT

被引:7
作者
LOPEZISUNZA, F
机构
[1] Departamento de Ingeniería de Procesos e Hidráulica, Universidad Autónoma Metropolitana - Iztapalapa, México, 09340
关键词
FLUID CATALYTIC CRACKING; PROCESS MODELING; DYNAMIC BEHAVIOR;
D O I
10.1016/S0098-1354(09)80016-1
中图分类号
TP39 [计算机的应用];
学科分类号
081203 ; 0835 ;
摘要
A fluid catalytic cracking unit is described by a dynamic model which considers both reactor and regenerator behaviour and their interaction. A lumped kinetics were used for the cracking reactions and coke deposition which occur in the riser. The regenerator is described by a fluidized moving-bed reactor with recycle, where coke is burned off with air. Simulation studies of the complex interactions between both reactors were performed for changes in the operating variables.
引用
收藏
页码:S139 / S148
页数:10
相关论文
共 18 条
[1]  
BERTEAU F, 1991, COMMUNICATION
[2]   RECENT PROCESS-RELATED AND CATALYST-RELATED DEVELOPMENTS IN FLUID CATALYTIC CRACKING [J].
BISWAS, J ;
MAXWELL, IE .
APPLIED CATALYSIS, 1990, 63 (02) :197-258
[3]  
DeCroocq D., 1984, CATALYTIC CRACKING H
[4]   MULTIPLE STEADY-STATES IN FCC UNIT OPERATIONS [J].
EDWARDS, WM ;
KIM, HN .
CHEMICAL ENGINEERING SCIENCE, 1988, 43 (08) :1825-1830
[5]   DIGITAL-SIMULATION OF INDUSTRIAL FLUID CATALYTIC CRACKING UNITS - BIFURCATION AND ITS IMPLICATIONS [J].
ELSHISHINI, SS ;
ELNASHAIE, SSEH .
CHEMICAL ENGINEERING SCIENCE, 1990, 45 (02) :553-559
[6]  
ENG MT, 1974, ISA T, V13, P232
[7]  
ISCOL L, 1970, 1970 JACC M ATL GA, P602
[8]  
KURIHARA H, 1967, THESIS MIT
[9]   ADVANCED CONTROL PRACTICE IN CHEMICAL PROCESS INDUSTRY - VIEW FROM INDUSTRY [J].
LEE, W ;
WEEKMAN, VW .
AICHE JOURNAL, 1976, 22 (01) :27-38
[10]   NUMBER OF STEADY-STATE OPERATING POINTS AND LOCAL STABILITY OF OPEN-LOOP FLUID CATALYTIC CRACKER [J].
LEE, W ;
KUGELMAN, AM .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1973, 12 (02) :197-204