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By Dimitri Gidaspow

Helpful as a reference for engineers in and as a complicated point textual content for graduate engineering scholars, Multiphase stream and Fluidization takes the reader past the theoretical to illustrate how multiphase circulate equations can be utilized to supply utilized, functional, predictive suggestions to business fluidization difficulties. Written to assist strengthen development within the rising technology of multiphase movement, this book Read more...

summary: precious as a reference for engineers in and as a sophisticated point textual content for graduate engineering scholars, Multiphase circulate and Fluidization takes the reader past the theoretical to illustrate how multiphase circulate equations can be utilized to supply utilized, useful, predictive recommendations to business fluidization difficulties. Written to assist boost development within the rising technology of multiphase movement, this publication starts off with the advance of the conservation legislation and strikes on via kinetic concept, clarifying many actual suggestions (such as particulate viscosity and solids strain) and introducing the recent established variable--the quantity fraction of the dispersed part. routines on the finish of every chapterare supplied for extra learn and lead into functions no longer coated within the textual content itself. Key beneficial properties * Treats fluidization as a department of shipping phenomena * Demonstrates the way to do brief, multidimensional simulation of multiphase procedures * the 1st publication to use kinetic idea to movement of particulates * Is the one e-book to debate numerical balance of multiphase equations and even if such equations are well-posed * Explains the starting place of bubbles and the idea that of serious granular move * offers basically written workouts on the finish of every bankruptcy to facilitate figuring out and extra research

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23) can be rewritten in convective form as follows: m;. su. 78) Convective differentiation of Eq. 78) moving with phase i gives the usual thermodynamic relation shown by Eq. 79), where definitions of temperature and pressure were used: as. -1 au. -', dt i . 79) Multiplication ofEq. 77) gives the expression for the rate of change of entropy: as. -I dp. -'-. -' -P·"\l·E·Y·. 81 ) where all the terms on the right-hand side cancel. Thus, in the absence of heat transfer and energy dissipation, the entropy of the ith phase stays a constant along its own stream line.

1955). Introduction to Thermodynamics of Irreversible Processes. Springfield, Illinois: Charles Thomas. Reldaitis G. , and B. W. Overturf (1983). "Fluidized-Bed Reactor Model with Generalized Particle Balances," AIChE J. 29,813. Slattery, J. C. (1972). Momentum. Energy. and Mass Transfer in Continua. New York: McGraw-Hill Book Co. , and B. Wendroff (1984). J. Compo Phys. 56,363-409. , and D. Gidaspow (1985). "Hydrodynamics of Fluidization: Prediction of Wall to Bed Heat Transfer Coefficients," presented at the 21st ASMFJAIChE Heat Transfer Conference, 1983.

6) and use of the definition of the motion along phase i, represented by d/dt', shows that aEj apj t7 ' + E·v. vp, = m. E·v. 75) can be written as aEj ' -1, Ei dpj mj _ do, mi -+v·EjVi=---i+--EiPi-,-· +-, at Pj dt Pi dt Pj t7 (l. 76) where the left-hand side of Eq. 6) in its conservative form, Eq. 23) can be rewritten in convective form as follows: m;. su. 78) Convective differentiation of Eq. 78) moving with phase i gives the usual thermodynamic relation shown by Eq. 79), where definitions of temperature and pressure were used: as.

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