MASS-TRANSFER IN 2-PHASE AND 3-PHASE FLUIDIZED-BEDS

被引：40

作者：

CHANG, SK ^{[1
]}

KANG, Y ^{[1
]}

KIM, SD ^{[1
]}

机构：

[1] KOREA ADV INST SCI & TECHNOL,DEPT CHEM ENGN,SEOUL 131,SOUTH KOREA

来源：

JOURNAL OF CHEMICAL ENGINEERING OF JAPAN | 1986年 / 19卷 / 06期

关键词：

D O I：

10.1252/jcej.19.524

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

引用

页码：524 / 530

页数：7

共 22 条

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[2]

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[3]

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[4]

DANKWERTS PV, 1951, IND ENGNG CHEM IND E, V43, P1460

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[7] RADIAL DISPERSION CHARACTERISTICS OF 2-PHASE AND 3-PHASE FLUIDIZED-BEDS [J].

KANG, Y ;

KIM, SD .

INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1986, 25 (03) :717-722

[8] INHIBITION OF BUBBLE COALESCENCE BY SOLUTES IN AIR WATER DISPERSIONS [J].

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[9] HOLD-UP AND AXIAL MIXING CHARACTERISTICS OF 2 AND 3 PHASE FLUIDIZED-BEDS [J].

KIM, SD ;

BAKER, CGJ ;

BERGOUGNOU, MA .

CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1972, 50 (06) :695-701

[10] PHASE HOLDUP CHARACTERISTICS OF 3 PHASE FLUIDIZED-BEDS [J].

KIM, SD ;

BAKER, CGJ ;

BERGOUGNOU, MA .

CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1975, 53 (02) :134-139

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