CRITIQUE ON DETERMINATION OF PACKED-BED PARTICLE-TO-FLUID HEAT-TRANSFER COEFFICIENTS FROM STEADY RADIAL HEAT-TRANSFER MEASUREMENTS

被引：8

作者：

WAKAO, N ^{[1
]}

KAGUEI, S ^{[1
]}

NAGAI, H ^{[1
]}

机构：

[1] YOKOHAMA NATL UNIV,DEPT CHEM ENGN,MINAMI KU,YOKOHAMA 233,JAPAN

来源：

CHEMICAL ENGINEERING SCIENCE | 1977年 / 32卷 / 10期

关键词：

D O I：

10.1016/0009-2509(77)80063-8

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

引用

页码：1261 / 1265

页数：5

共 7 条

[1] GAS-PARTICLE HEAT-TRANSFER COEFFICIENTS IN PACKED-BEDS AT LOW REYNOLDS-NUMBERS [J].

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VERKERK, JW ;

VANDENBERG, PJ .

CHEMICAL ENGINEERING SCIENCE, 1975, 30 (09) :1015-1018

[2] HEAT-TRANSFER AND AXIAL DISPERSION IN PACKED-BEDS [J].

GUNN, DJ ;

DESOUZA, JFC .

CHEMICAL ENGINEERING SCIENCE, 1974, 29 (06) :1363-1371

[3] HEAT TRANSFER CHARACTERISTICS OF POROUS ROCKS .2. THERMAL CONDUCTIVITIES OF UNCONSOLIDATED PARTICLES WITH FLOWING FLUIDS [J].

KUNII, D ;

SMITH, JM .

AICHE JOURNAL, 1961, 7 (01) :29-34

[4] GAS-PARTICLE HEAT TRANSFER COEFFICIENTS IN PACKED BEDS AT LOW REYNOLDS NUMBERS [J].

LITTMAN, H ;

BARILE, RG ;

PULSIFER, AH .

INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1968, 7 (04) :554-&

[5] EQUIVALENCE OF ONE-PHASE AND 2-PHASE MODELS FOR HEAT-TRANSFER PROCESSES IN PACKED-BEDS - ONE-DIMENSIONAL THEORY [J].

VORTMEYER, D ;

SCHAEFER, RJ .

CHEMICAL ENGINEERING SCIENCE, 1974, 29 (02) :485-491

[6] EFFECT OF AXIAL FLUID THERMAL DISPERSION COEFFICIENT ON NUSSELT NUMBERS OF DISPERSION-CONCENTRIC MODEL OF PACKED-BEDS AT LOW FLOW-RATES [J].

WAKAO, N ;

KAGUEI, S ;

SHIOZAWA, B .

CHEMICAL ENGINEERING SCIENCE, 1977, 32 (04) :451-454

[7]

Wakao N., 1969, J CHEM ENG, V2, P24

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