FULLY-DEVELOPED, FORCED CONVECTIVE FLOW THROUGH AN ANNULAR PACKED-SPHERE BED WITH WALL EFFECTS

被引：87

作者：

CHENG, P ^{[1
]}

HSU, CT ^{[1
]}

机构：

[1] TRW,SPACE & TECHNOL GRP,DEPT FLUID MECH,REDONDO BEACH,CA 90278

来源：

INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER | 1986年 / 29卷 / 12期

关键词：

D O I：

10.1016/0017-9310(86)90003-7

中图分类号：

O414.1 [热力学];

学科分类号：

摘要：

引用

页码：1843 / 1853

页数：11

共 19 条

[1] TUBULAR REACTOR DESIGN .1. 2 DIMENSIONAL MODEL [J].

AHMED, M ;

FAHIEN, RW .

CHEMICAL ENGINEERING SCIENCE, 1980, 35 (04) :889-895

[2]

ARNTZ D, 1982, ACS SYM SER, V196, P3

[3] VOID FRACTION DISTRIBUTION IN BEDS OF SPHERES [J].

BENENATI, RF ;

BROSILOW, CB .

AICHE JOURNAL, 1962, 8 (03) :359-361

[4]

BRINKMAN HC, 1947, APPL SCI RES, V1, P27

[5] WALL HEAT-TRANSFER TO CHEMICAL REACTORS [J].

CHAO, RE ;

CABAN, RA ;

IRIZARRY, MM .

CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1973, 51 (01) :67-70

[6]

CHENG P, CHEM ENG SCI

[7]

ERGUN S, 1952, CHEM ENG PROG, V48, P89

[8]

FROMENT GF, 1972, ADV CHEM SER, V109, P1

[9] IGNITION-EXTINCTION PHENOMENA IN A WALL COOLED FIXED-BED REACTOR - EXPERIMENTS AND MODEL-CALCULATIONS INCLUDING RADIAL POROSITY AND VELOCITY DISTRIBUTIONS [J].

KALTHOFF, O ;

VORTMEYER, D .

CHEMICAL ENGINEERING SCIENCE, 1980, 35 (07) :1637-1643

[10] VELOCITY, TEMPERATURE AND CONVERSION PROFILES IN FIXED-BED CATALYTIC REACTORS [J].

LEROU, JJ ;

FROMENT, GF .

CHEMICAL ENGINEERING SCIENCE, 1977, 32 (08) :853-861

← 1 2 →