Bubble size and mass transfer coefficients in dual-impeller agitated reactors

被引：65

作者：

Bouaifi, MI ^{[1
]}

Roustan, M ^{[1
]}

机构：

[1] Inst Natl Sci Appl, Dept Genie Proc Ind, F-31077 Toulouse 4, France

来源：

CANADIAN JOURNAL OF CHEMICAL ENGINEERING | 1998年 / 76卷 / 03期

关键词：

bubble size; interfacial area; mass transfer coefficients; dual-impeller; agitated vessel;

D O I：

10.1002/cjce.5450760307

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

The study relates to the mass transfer and the bubble size in a non standard vessel equipped with various dual-impeller combinations. The effects of the rotational speed, gas flow rate, impeller type and diameter are investigated. The volumetric mass transfer coefficient k(L)a and the bubble size d(bs) were studied. The liquid side mass transfer coefficient k(L) and the volumetric interfacial area a were estimated separately. A comparison has been made with some existing correlations.

引用

页码：390 / 397

页数：8

共 27 条

[1]

BAKKER A, 1991, THESIS DELFT U NETHE

[2]

BOUAIFI M, 1997, P 9 EUR C MIX, P137

[3]

BOUAIFI M, 1997, THESIS INSA TOULOUSE

[4]

Calderbank PH., 1958, T I CHEM ENG-LOND, V36, P443

[5]

CHARLES JM, 1978, THESIS INSA TOULOUSE

[6]

CHIAMPO F, 1994, P 8 INT C MIX CAMBR, P73

[7]

Deckwer W. D., 1992, BUBBLE COLUMN REACTO

[8] COMPREHENSIVE STUDY ON CO2-INTERPHASE MASS-TRANSFER IN VERTICAL COCURRENT AND COUNTERCURRENT GAS-LIQUID FLOW [J].

DECKWER, WD ;

ADLER, I ;

ZAIDI, A .

CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1978, 56 (01) :43-55

[9]

Figueiredo M, 1979, CHEM ENG SCI, V34, P1333, DOI DOI 10.1016/0009-2509(79)80025-1

[10]

Greaves M, 1988, P 6 EUR C MIX PAV IT, P313

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