FLOW PATTERNS AND MASS-TRANSFER RATES IN FLUIDIZED-BED ION-EXCHANGE EQUIPMENT

被引：7

作者：

SLATER, MJ

LUCAS, BH

机构：

[1] UNIV BRADFORD,SCH CHEM ENGN,BRADFORD,YORKSHIRE,ENGLAND

[2] CANADA DEPT ENERGY MINES & RESOURCES,DIV EXTRACTION MET,MINES BRANCH,OTTAWA,ONTARIO,CANADA

来源：

CANADIAN JOURNAL OF CHEMICAL ENGINEERING | 1976年 / 54卷 / 04期

关键词：

D O I：

10.1002/cjce.5450540404

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

引用

页码：264 / 268

页数：5

共 14 条

[1]

BENNETT B, 1969, SOC CHEM IND S ION E, P133

[2] OPERATION AND MODELING OF A PERIODIC, COUNTERCURRENT, SOLID-LIQUID REACTOR [J].

DODDS, R ;

HUDSON, PI ;

KERSHENB.L ;

STREAT, M .

CHEMICAL ENGINEERING SCIENCE, 1973, 28 (06) :1233-1248

[3] COMPUTATIONAL AND EXPERIMENTAL STUDIES ON A MOVING ION EXCHANGE BED [J].

GONDO, S ;

ITAI, M ;

KUSUNOKI, K .

INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1971, 10 (01) :140-&

[4]

GONDO S, 1969, J NUCL SCI TECHNOL-T, V6, P567

[5]

GONDO S, 1967, MEM FAC ENG KYUSHU U, V26, P103

[6]

HAINES A, 1973, JSA I MIN MET

[7]

Helfferich F., 1962, ANGEW CHEM INT EDITI, V1, P440, DOI [10.1002/anie.196204401., DOI 10.1002/ANIE.196204401, 10.1002/anie.196204401]

[8] THEORETICAL INVESTIGATION OF AGITATED ION EXCHANGE BEDS [J].

MARCHELLO, JM ;

DAVIS, MW .

INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1963, 2 (01) :27-&

[9] CONTINUOUS FLOW STIRRED TANK REACTOR SYSTEMS - DEVELOPMENT OF TRANSIENT EQUATIONS [J].

MASON, DR ;

PIRET, EL .

INDUSTRIAL AND ENGINEERING CHEMISTRY, 1950, 42 (05) :817-825

[10]

SELKE WA, 1951, CHEM ENG PROG, V47, P529

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