OPTIMUM PARTICLE-SIZE IN A GAS-LIQUID SOLID FLUIDIZED-BED CATALYTIC REACTOR

被引:4
作者
WISECARVER, KD [1 ]
FAN, LS [1 ]
机构
[1] OHIO STATE UNIV,DEPT CHEM ENGN,COLUMBUS,OH 43210
关键词
D O I
10.1016/0009-2509(88)80017-4
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
引用
收藏
页码:2741 / 2750
页数:10
相关论文
共 20 条
[1]   SOLID LIQUID MASS-TRANSFER IN A GAS-LIQUID SOLID FLUIDIZED-BED [J].
ARTERS, DC ;
FAN, LS .
CHEMICAL ENGINEERING SCIENCE, 1986, 41 (01) :107-115
[2]  
Begovich J.M., 1978, FLUIDIZATION, P190
[3]  
BHATIA VK, 1974, P INT S FLUID ITS AP, P380
[4]   CATALYST DEACTIVATION IN THE H-COAL COAL-LIQUEFACTION PROCESS .1. CATALYST RESIDENCE TIME DISTRIBUTION [J].
BICKEL, TC ;
THOMAS, MG .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1982, 21 (03) :377-381
[5]   SOLIDS MIXING IN A GAS-LIQUID-SOLID FLUIDIZED-BED CONTAINING A BINARY MIXTURE OF PARTICLES [J].
FAN, LS ;
CHERN, SH ;
MUROYAMA, K .
AICHE JOURNAL, 1984, 30 (05) :858-860
[6]  
FAN LS, 1988, IN PRESS FLUIDIZATIO
[7]   ON THE STEADY-STATE PERFORMANCE OF CO-CURRENT BUBBLE COLUMN SLURRY REACTORS [J].
GOVINDARAO, VMH ;
CHIDAMBARAM, M .
CHEMICAL ENGINEERING JOURNAL AND THE BIOCHEMICAL ENGINEERING JOURNAL, 1983, 27 (01) :29-36
[8]  
GOVINDRAO VMH, 1975, CHEM ENG J, V9, P229
[9]   HOLDUP AND MASS TRANSFER IN BUBBLE COLUMNS [J].
HUGHMARK, GA .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1967, 6 (02) :218-&
[10]  
Kato Y., 1972, J CHEM ENG JPN, V5, P112