ANALYSIS OF GAS-FLOW IN FLUIDIZED-BED REACTORS

被引：6

作者：

BUKUR, DB

机构：

来源：

INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS | 1978年 / 17卷 / 02期

关键词：

D O I：

10.1021/i160066a009

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

引用

页码：120 / 123

页数：4

共 18 条

[1]

BUKUR D, 1977, CHEMICAL REACTOR THE, P692

[2]

BUKUR DB, 1974, SOME MODEL STUDIES F, P10

[3] PERFORMANCE ANALYSIS OF A FLUIDIZED-BED REACTOR .2. OBSERVED REACTOR BEHAVIOR COMPARED WITH SIMPLE 2-PHASE MODELS [J].

CHAVARIE, C ;

GRACE, JR .

INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1975, 14 (02) :79-86

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

CHAVARIE, C ;

GRACE, JR .

INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1975, 14 (02) :86-91

[5]

DAVIDSON JF, 1963, FLUIDIZED PARTICLES, P100

[6] COUNTERCURRENT BACKMIXING MODEL FOR FLUIDIZED-BED CATALYTIC REACTORS - APPLICABILITY OF SIMPLIFIED SOLUTIONS [J].

FRYER, C ;

POTTER, OE .

INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1972, 11 (03) :338-&

[7]

GRACE JR, 1971, CHEM ENG PROG S SER, V67, P159

[8]

JJ V.D., 1967, P INT S FLUIDIZATION, P334

[9] BUBBLING BED MODEL - MODEL FOR FLOW OF GAS THROUGH A FLUIDIZED BED [J].

KUNII, D ;

LEVENSPIEL, O .

INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1968, 7 (03) :446-+

[10] BUBBLING BED MODEL FOR KINETIC PROCESSES IN FLUIDIZED BEDS - GAS-SOLID MASS AND HEAT TRANSFER AND CATALYTIC REACTIONS [J].

KUNII, D ;

LEVENSPI.O .

INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1968, 7 (04) :481-&

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