GAS MIXING CHARACTERISTICS OF A FLUID BED REGENERATOR

被引:25
作者
HANDLOS, AE
KUNSTMAN, RW
SCHISSLER, DO
机构
来源
INDUSTRIAL AND ENGINEERING CHEMISTRY | 1957年 / 49卷 / 01期
关键词
D O I
10.1021/ie50565a019
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
引用
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页码:25 / 30
页数:6
相关论文
共 7 条
[1]  
ASKINS JW, 1951, CHEM ENG PROG, V47, P401
[2]   THE DISTRIBUTION OF RESIDENCE-TIMES IN AN INDUSTRIAL FLUIDISED REACTOR [J].
DANCKWERTS, PV ;
JENKINS, JW ;
PLACE, G .
CHEMICAL ENGINEERING SCIENCE, 1954, 3 (01) :26-35
[3]   CONTINUOUS FLOW SYSTEMS - DISTRIBUTION OF RESIDENCE TIMES [J].
DANCKWERTS, PV .
CHEMICAL ENGINEERING SCIENCE, 1953, 2 (01) :1-13
[4]  
EWALD H, 1952, METHODEN ANDWENDUNGE
[5]   GAS-FLOW PATTERNS IN BEDS OF FLUIDIZED SOLIDS [J].
GILLILAND, ER ;
MASON, EA ;
OLIVER, RC .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1953, 45 (06) :1177-1185
[6]   GAS MIXING IN BEDS OF FLUIDIZED SOLIDS [J].
GILLILAND, ER ;
MASON, EA .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1952, 44 (01) :218-224
[7]   Mass transfer between phases - Role of eddy diffusion [J].
Sherwood, TK ;
Woertz, BB .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1939, 31 :1034-1041