THEORETICAL-STUDY OF PRESSURE-DROP FOR NON-NEWTONIAN CREEPING FLOW PAST AN ASSEMBLAGE OF SPHERES

被引：37

作者：

MOHAN, V ^{[1
]}

RAGHURAMAN, J ^{[1
]}

机构：

[1] INDIAN INST TECHNOL,DEPT CHEM ENGN,MADRAS 600 036,INDIA

来源：

AICHE JOURNAL | 1976年 / 22卷 / 02期

关键词：

D O I：

10.1002/aic.690220206

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

引用

页码：259 / 264

页数：6

共 18 条

[1] NON-NEWTONIAN FLOW PAST A SPHERE [J].

ADACHI, K ;

YOSHIOKA, N ;

YAMAMOTO, K .

CHEMICAL ENGINEERING SCIENCE, 1973, 28 (11) :2033-2043

[2]

Carnahan B., 1969, APPL NUMERICAL METHO

[3] POWER-LAW FLOW THROUGH A PACKED TUBE [J].

CHRISTOPHER, RH ;

MIDDLEMAN, S .

INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1965, 4 (04) :422-+

[4] THEORETICAL STUDY OF PRESSURE-DROP AND TRANSPORT IN PACKED-BEDS AT INTERMEDIATE REYNOLDS-NUMBERS [J].

ELKAISSY, MM ;

HOMSY, GM .

INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1973, 12 (01) :82-90

[5] VISCOUS FLOW IN MULTIPARTICLE SYSTEMS - SLOW MOTION OF FLUIDS RELATIVE TO BEDS OF SPHERICAL PARTICLES [J].

HAPPEL, J .

AICHE JOURNAL, 1958, 4 (02) :197-201

[6]

Happel J., 1965, LOW REYNOLDS NUMBER

[7] PRESSURE-DROP DURING FLOW OF STOKESIAN FLUIDS THROUGH GRANULAR BEDS [J].

KEMBLOWSKI, Z ;

MERTI, J .

CHEMICAL ENGINEERING SCIENCE, 1974, 29 (01) :213-223

[8] THE FORCES EXPERIENCED BY RANDOMLY DISTRIBUTED PARELLEL CIRCULAR CYLINDERS OR SPHERES IN A VISCOUS FLOW AT SMALL REYNOLDS NUMBERS [J].

KUWABARA, S .

JOURNAL OF THE PHYSICAL SOCIETY OF JAPAN, 1959, 14 (04) :527-532

[9] VISCOUS FLOW THROUGH PARTICLE ASSEMBLAGES AT INTERMEDIATE REYNOLDS NUMBERS - STEADY-STATE SOLUTIONS FOR FLOW THROUGH ASSEMBLAGES OF SPHERES [J].

LECLAIR, BP ;

HAMIELEC, AE .

INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1968, 7 (04) :542-&

[10]

MANGASRIAN OL, 1972, T ASME B, V94, P364

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