TUBULAR REACTOR DESIGN .1. 2 DIMENSIONAL MODEL

被引:39
作者
AHMED, M [1 ]
FAHIEN, RW [1 ]
机构
[1] UNIV FLORIDA,DEPT CHEM ENGN,GAINESVILLE,FL 32611
关键词
D O I
10.1016/0009-2509(80)85076-7
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
引用
收藏
页码:889 / 895
页数:7
相关论文
共 32 条
[1]  
AHMED M, 1976, THESIS U FLORIDA
[2]  
ARGO WB, 1953, CHEM ENG PROG, V49, P443
[3]  
BADDOUR RF, 1961, CHEM ENG PROGR S SER, V57, P35
[4]  
Beek J, 1962, ADV CHEM ENG, P203, DOI [10.1016/S0065-2377(08)60060-5, DOI 10.1016/S0065-2377(08)60060-5]
[5]   ON ROEL OF TRANSPORT PHENOMENA IN CATALYTIC REACTOR BEHAVIOR DIGITAL SIMULATION OF NAPHTHALENE OXIDATION OVER V205 [J].
CARBERRY, JJ ;
WHITE, D .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1969, 61 (07) :27-&
[6]  
CHASE J, UNPUBLISHED
[7]   MASS TRANSFER AT LOW FLOW RATES IN A PACKED COLUMN [J].
DORWEILER, VP ;
FAHIEN, RW .
AICHE JOURNAL, 1959, 5 (02) :139-144
[8]   MASS TRANSFER IN PACKED BEDS [J].
FAHIEN, RW ;
SMITH, JM .
AICHE JOURNAL, 1955, 1 (01) :28-37
[9]   EQUATION FOR THE VELOCITY PROFILE IN PACKED-COLUMNS [J].
FAHIEN, RW ;
STANKOVIC, IM .
CHEMICAL ENGINEERING SCIENCE, 1979, 34 (11) :1350-1354
[10]  
FAHIEN RW, 1954, THESIS PURDUE U