Download Advances in Engineering Fluid Mechanics: Multiphase Reactor by Nicholas P. Cheremisinoff (Eds.) PDF

By Nicholas P. Cheremisinoff (Eds.)

Content material:
Contributors to this volume

, Pages viii-x
About the editor

, Page xi
Preface

, Page xii, Nicholas P. Cheremisinoff
Chapter 1 - The viscosity of liquid hydrocarbons and their mixtures

, Pages 1-23, Stanley I. Sandler, Hasan Orbey
Chapter 2 - Experimental reports for characterization of combining mechanisms

, Pages 25-47, Jin Kuk Kim
Chapter three - actual modeling of axial blending in slugging gas-liquid columns

, Pages 49-65, J.R.F. Guedes de Carvalho, J.B.L.M. Campos, J.A.S. Teixeira
Chapter four - Numerical answer of the permeation, sorption, and desorption cost curves incorporating the dual-mode sorption and delivery model

, Pages 67-78, Keio Toi
Chapter five - Kinematic viscosity and viscous circulation in binary combos containing ethane-1,2-diol

, Pages 79-104, Lorenzo Tassi
Chapter 6 - response of a continuing blend in a effervescent fluidized bed

, Pages 105-117, R. Aris
Chapter 7 - Fluid dynamics of coarse dispersions

, Pages 119-166, Y.A. Buyevich, S.K. Kapbasov
Chapter eight - Combustion of unmarried coal debris in turbulent fluidized beds

, Pages 167-191, Prabir Kumar Halder
Chapter nine - stream of solids and slurries in rotary drums

, Pages 193-253, H.A. Nasr-El-Din, A. Afacan, J.H. Masliyah
Chapter 10 - fuel section hydrodynamics in circulating fluidized mattress risers

, Pages 255-296, Gregory S. endurance, Jamal Chaouki, Franco Berruti
Chapter eleven - Boundary stipulations required for the CFD simulation of flows in stirred tanks

, Pages 297-316, Suzanne M. Kresta
Chapter 12 - function of interfacial shear modelling in predicting balance of stratified two-phase flow

, Pages 317-378, N. Brauner, D. Moalem Maron
Chapter thirteen - Water circulation via helical coils in turbulent condition

, Pages 379-403, Sudip Kumar Das
Chapter 14 - Modeling coalescence of bubble clusters emerging freely in low-viscosity liquids

, Pages 405-429, C.W. Stewart
Chapter 15 - Oxygen move in non-newtonian fluids stirred with a helical ribbon screw impeller

, Pages 431-453, A. Tecante, E. Brito de l. a. Fuente, L. Choplin, P.A. Tanguy
Chapter sixteen - Modeling of the hydrodynamic habit of hugely viscous fluids in stirred tanks built with two-blade impellers

, Pages 455-485, Catherine Xuereb, Mohammed Abid, Bertrand Joël
Chapter 17 - Non-newtonian liquid circulation via globe and gate valves

, Pages 487-505, Sudip Kumar Das
Chapter 18 - comparability of numerical and experimental rheological info of homogeneous non-newtonian suspensions

, Pages 507-524, V. Nassehi
Chapter 19 - focus forcing of isothermal plug-flow reactors for autocatalytic reactions

, Pages 525-538, M. Chidambaram
Chapter 20 - Non-newtonian results in bubble columns

, Pages 539-570, R.P. Chhabra, U.K. Ghosh, Y. Kawase, S.N. Upadhyay
Chapter 21 - reviews in supported titanium catalyst procedure utilizing magnesium dichloride-alcohol adduct

, Pages 571-581, V.K. Gupta, Shashikant, M. Ravindranathan
Chapter 22 - Plasticizing polyesters of dimer acids and 1,4-butanediol

, Pages 583-597, U.D.N. Bajpai, Nivedita
Chapter 23 - Viscoelastic houses of version silicone networks with pendant chains

, Pages 599-614, M.A. Villar, E.M. Vallés
Chapter 24 - Rheology of water-soluble polymers used for greater oil recovery

, Pages 615-668, H.A. Nasr-El-Din, K.C. Taylor
Chapter 25 - Relation of rheological houses of UV-cured movies with glass transition temperatures in line with fox equation

, Pages 669-681, M. Azam Ali, M.A. Kahn, K.M. Irdriss Ali
Chapter 26 - Prediction and calculation of the shear creep habit of amorphous polymers lower than revolutionary actual aging

, Pages 683-709, R.O.E. Greiner, J. Kaschta
Chapter 27 - Die extrusion habit of carbon black-filled block copolymer thermoplastic elastomers

, Pages 711-736, Jin Kuk Kim, Min Hyeon Han
Chapter 28 - Polysulfides

, Pages 737-746, C.P. Tsonis
Chapter 29 - houses and purposes of thermoplastic polyurethane blends

, Pages 747-761, M. Yue, K.S. Chian
Index

, Pages 763-772

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Additional resources for Advances in Engineering Fluid Mechanics: Multiphase Reactor and Polymerization System Hydrodynamics. Advances in Engineering Fluid Mechanics Series

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Dimensional analysis shows that the flow pattern, and, therefore, the dimensionless wake volume, v/D^, and dimensionless wake length, 1/D, may depend on L/D, (g/D^)^^^/v, and pD^g/o. , diameter below about 20 mm) and the dependence on L/D is expected to cease for large enough values of this parameter, when the velocity profile in the film flowing alongside the slug is fully developed. 5. The photographic study revealed that for (gD^)'^^/v < 500 flow in the wake is laminar, whereas for (gD^)'^^/v > 900 it is turbulent.

Unfortunately, no standard method exists because of the difficulty of characterizing particle agglomerates ranging from lOOjitm (easily visible in an optical microscopy) to submicron particulates, which cannot be seen. One must then combine different methods to determine the entire distribution of particulate size. In general, the high magnification size of agglomerates is measured by electron microscopy. Methods used to study morphology are: 1. measurement of the size distribution of agglomerates from optical microscopy; 2.

Recent Researches in Electricity and Magnetium," Oxford University Press, London (1893). 20. , Ann. , 46, p. 809 (1905). 21. , Ann. , 12, p. 161 (1939). 22. Min, K. , Rubber Chem. , 58, p. 1,024 (1985). 23. K. , Nihon Reorogi Gakkaishi, 17, p. 203 (1989). 24. L. , J. AppL of Polym. , 44, p. 59 (1989). 25. D. Dissertation, University of Akron (1989). 26. , J. of AppL Polym. , 50, p. 145 (1992). F. M. S. Teixeira Escola Superior Agraria Instituto Politecnico de Braganga Braganga, Portugal CONTENTS INTRODUCTION, 49 THE WAKES OF SLUGS, 50 Laminar Wakes, 51 Turbulent Wakes, 55 TAYLOR DISPERSION FOR LAMINAR LIQUID FLOW ALONG A TUBE, 57 AXIAL MIXING IN CO-CURRENT FLOW OF GAS AND LIQUID, 58 NOTATION, 64 REFERENCES, 65 INTRODUCTION Mixing of liquid in gas/liquid contactors is a topic of great practical interest to the chemical industry, especially since it may determine product yield in chemical reactors.

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