LIQUID-SOLID MASS-TRANSFER IN PACKED-BEDS WITH DOWNWARD CONCURRENT GAS-LIQUID FLOW

被引：88

作者：

SATTERFIELD, CN

VANEEK, MW

BLISS, GS

机构：

来源：

关键词：

D O I：

10.1002/aic.690240421

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

引用

页码：709 / 717

页数：9

共 23 条

[1] BLISS GS, 1976, THESIS MASS I TECHNO
[2] THE CONTINUOUS PHASE HEAT AND MASS-TRANSFER PROPERTIES OF DISPERSIONS
CALDERBANK, PH
MOOYOUNG, MB
[J]. CHEMICAL ENGINEERING SCIENCE, 1961, 16 (1-2) : 39 - 54
[3] A BOUNDARY-LAYER MODEL OF FLUID-PARTICLE MASS TRANSFER IN FIXED BEDS
CARBERRY, JJ
[J]. AICHE JOURNAL, 1960, 6 (03) : 460 - 463
[4] CHARPENTIER JC, 1971, 2ND C QUELQ APPL CHI
[5] GIANETTO A, 1976, COMMUNICATION SEP
[6] MASS-TRANSFER IN PACKED-BEDS WITH 2-PHASE FLOW
GOTO, S
LEVEC, J
SMITH, JM
[J]. INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1975, 14 (04): : 473 - 478
[7] TRICKLE-BED REACTOR PERFORMANCE .1. HOLDUP AND MASS-TRANSFER EFFECTS
GOTO, S
SMITH, JM
[J]. AICHE JOURNAL, 1975, 21 (04) : 706 - 713
[8] Hirose T., 1974, J CHEM ENG JAPAN, V7, P19
[9] Hirose T., 1976, J CHEM ENG JPN, V9, P220
[10] KREKELS JTC, 1972, COMMUNICATION SEP