EXPERIMENTAL INVESTIGATION OF MODELS FOR FLUIDIZED-BED CATALYTIC REACTORS

被引：81

作者：

FRYER, C ^{[1
]}

POTTER, OE ^{[1
]}

机构：

[1] MONASH UNIV,DEPT CHEM ENGN,CLAYTON 3168,VICTORIA,AUSTRALIA

来源：

AICHE JOURNAL | 1976年 / 22卷 / 01期

关键词：

D O I：

10.1002/aic.690220104

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

引用

页码：38 / 47

页数：10

共 15 条

[1]

Davidson J.F., 1963, FLUIDIZED PARTICLES

[2] BUBBLE SIZE VARIATION IN 2-PHASE MODELS OF FLUIDIZED-BED REACTORS [J].

FRYER, C ;

POTTER, OE .

POWDER TECHNOLOGY, 1972, 6 (06) :317-&

[3] 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-&

[4]

FRYER C, 1974, THESIS MONASH U

[5]

FRYER C, 1974, 1973 C INT FLUID APP, P440

[6]

Harrison D., 1961, TRANS INST CHEM ENG, V39, P409

[7] BUBBLE ASSEMBLAGE MODEL FOR FLUIDIZED BED CATALYTIC REACTORS [J].

KATO, K ;

WEN, CY .

CHEMICAL ENGINEERING SCIENCE, 1969, 24 (08) :1351-&

[8]

KOBAYASHI H, 1966, KAGAKU KOGAKU, V4, P147

[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]

LATHAM R, 1968, BRIT CHEM ENG, V13, P666

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