PERFORMANCE ANALYSIS OF A FLUIDIZED-BED REACTOR .3. MODIFICATION AND EXTENSION OF CONVENTIONAL 2-PHASE MODELS

被引：22

作者：

CHAVARIE, C ^{[1
]}

GRACE, JR ^{[1
]}

机构：

[1] MCGILL UNIV,DEPT CHEM ENGN,MONTREAL H3C 3G1,QUEBEC,CANADA

来源：

INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS | 1975年 / 14卷 / 02期

关键词：

D O I：

10.1021/i160054a003

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

引用

页码：86 / 91

页数：6

共 27 条

[11] BUBBLING BED MODEL - MODEL FOR FLOW OF GAS THROUGH A FLUIDIZED BED
KUNII, D
LEVENSPIEL, O
[J]. INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1968, 7 (03): : 446 - +
[12] BUBBLING BED MODEL FOR KINETIC PROCESSES IN FLUIDIZED BEDS - GAS-SOLID MASS AND HEAT TRANSFER AND CATALYTIC REACTIONS
KUNII, D
LEVENSPI.O
[J]. INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1968, 7 (04): : 481 - &
[13] KUNII D, 1969, FLUIDIZATION ENGINEE
[14] CONSIDERATION OF VOLUME VARIABILITY IN CALCULATION OF CATALYTIC GAS REACTIONS IN FLUIDIZED-BEDS
LITZ, W
[J]. CHEMIE INGENIEUR TECHNIK, 1973, 45 (06) : 382 - 387
[15] May W.G., 1959, CHEM ENG PROG, V55, P49
[16] MIXING AND CONTACTING MODELS FOR FLUIDIZED BEDS
MIREUR, JP
BISCHOFF, KB
[J]. AICHE JOURNAL, 1967, 13 (05) : 839 - &
[17] Orcutt J.C., 1962, CHEM ENG PROG S SER, V58, P1
[18] PROPERTIES OF BUBBLES IN FLUIDIZED BEDS OF CONDUCTING PARTICLES AS MEASURED BY AN ELECTRORESISTIVITY PROBE
PARK, WH
KANG, WK
CAPES, CE
OSBERG, GL
[J]. CHEMICAL ENGINEERING SCIENCE, 1969, 24 (05) : 851 - &
[19] Partrige B. A., 1966, T I CHEM ENGRS, V44, P335
[20] PYLE DL, 1965, THESIS CAMBRIDGE U