PILOT-PLANT FOR THE FLUID CATALYTIC CRACKING PROCESS - DETERMINATION OF THE KINETIC-PARAMETERS OF DEACTIVATION OF THE CATALYST

被引：19
作者：
CORELLA, J
FERNANDEZ, A
VIDAL, JM
机构：
来源：
INDUSTRIAL & ENGINEERING CHEMISTRY PRODUCT RESEARCH AND DEVELOPMENT | 1986年 / 25卷 / 04期
关键词：
D O I：
10.1021/i300024a009
中图分类号：
TQ [化学工业];
学科分类号：
0817 ;
摘要：
引用
收藏
页码：554 / 562
页数：9
相关论文
共 27 条
[21]   KINEMATIC MODEL FOR AN ADIABATIC TRANSFER LINE CATALYTIC CRACKING REACTOR [J].
SHAH, YT ;
HULING, GP ;
PARASKOS, JA ;
MCKINNEY, JD .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1977, 16 (01) :89-94
[22]   CARBON FORMATION IN CATALYTIC CRACKING [J].
VOORHIES, A .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1945, 37 (04) :318-322
[23]  
WACHTEL SJ, 1972, OIL GAS J, V70, P104
[24]  
Wagner M. C., 1984, PLANT OPERATION PROG, V3, P222
[25]   A MODEL OF CATALYTIC CRACKING CONVERSION IN FIXED MOVING AND FLUID-BED REACTORS [J].
WEEKMAN, VW .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1968, 7 (01) :90-&
[26]  
WOLLASTON G, 1975, HYDROCARBON PROCESS, V54, P93
[27]   CONVEYABILITY OF MATERIALS OF MIXED PARTICLE SIZE [J].
ZENZ, FA .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1964, 3 (01) :65-&
123