By Milorad P. Duduković and Patrick L. Mills (Eds.)

ISBN-10: 0841208158

ISBN-13: 9780841208155

ISBN-10: 0841210659

ISBN-13: 9780841210653

content material: Trickling and pulsing transition in cocurrent downflow trickle-bed reactors with designated connection with large-scale columns / D.M. Dimenstein, S.P. Zimmerman, and K.M. Ng --
effect of the reactional approach at the irrigation cost in trickle-bed reactors / P. Ruiz, M. Crine, A. Germain, and G. L'Homme --
A comparability of present types for isothermal trickle-bed reactors : software to a version response procedure / P.L. turbines and M.P. Duduković --
balance of trickle-bed reactors / C.H. Barkelew and B.S. Gambhir --
fuel absorption with complicated chemical reactions : a basic computational scheme for fee calculations / P.A. Ramachandran --
Modeling of gas-liquid continuous-stirred tank reactors (CSTRs) / A.A. Shaikh and A. Varma --
The influence of fuel and liquid velocities and good measurement on reliable suspension in a three-phase bubble column reactor / Barry W. Brian and Paul N. Dyer --
Bubble habit in a slurry bubble column reactor version / D.N. Smith, W. Fuchs, R.J. Lynn, D.H. Smith, and M. Hess --
A two-bubble category version for churn turbulent bubble column slurry reactor / S. Joseph and Y.T. Shah --
Mathematical modeling of cross-flow, sturdy nation electrochemical reactors / P.G. Debenedetti, C.G. Vayenas, I. Yentekakis, and L.L. Hegedus --
Modeling of chemical vapor deposition reactors for the fabrication of microelectronic units / Klavs F. Jensen --
Multicomponent diffusion and response in porous catalysts / Henry W. Haynes, Jr. --
research of fixed-bed catalytic reactor types / S.I. Pereira Duarte and N.O. Lemcoff --
The optimum layout of a reactor for the hydrogenation of butyraldehyde to butanol / J.B. Cropley, L.M. Burgess, and R.A. Loke --
difficulties within the layout of the countercurrent moving-bed catalytic reactor : a geometrical method / Dimitry Altshuller --
Optimization in tubular reactor structures / E.B. Nauman and Ramesh Mallikarjun --
secure layout of cooled tubular reactors for exothermic a number of first order reactions / K.R. Westerterp, K.J. Ptasinsky, and R.R.M. Overtoom --
balance of adiabatic reactors / C.H. Barkelew --
basic deactivation facts from laboratory reactors / Eugene E. Petersen and Michael A. Pacheco --
Poisoning results in temperature-increased fixed-bed reactor operation : a comparability of experimental effects and version simulation / George J. Frycek and J.B. Butt --
Modeling of tubular nonisothermal nonadiabatic packed-bed reactors with catalyst poisoning / Qamardeep S. Bhatia and Vladimir Hlavacèk.

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Extra resources for Chemical and Catalytic Reactor Modeling

Sample text

It is shown that cer­ tain key items, such as i) extent of liquid-solid wetting, ii) presence or absence of stagnant versus actively flowing liquid films on the catalyst surface, and iii) magnitude of mass transport resistances, can a l l have a significant effect on the predicted reactor behavior. The in­ ability of current correlations to predict mass transfer coefficients is demonstrated. Reactions between gases and liquids that are catalyzed by either homogeneous organometallic complexes or heterogeneous catalysts provide the basis for a significant portion of the products manufactured in both chemical and petroleum processing.

The l i q u i d phase was saturated w i t h the gaseous reactant (hydrogen) before being admitted to the r e a c t o r , t h e r e by r e p r e s e n t i n g a s o - c a l l e d " e q u i l i b r i u m " feed. Pure hydrogen was used as the gas phase and maintained at a s u f f i c i e n t l y h i g h flow r a t e that f u r t h e r i n c r e a s e s d i d not a f f e c t the measured α-methylstyrene conversion. 5% Pd c a t a l y s t . 5% Pd c a t a l y s t . These, along with the experimental conversion versus l i q u i d s u p e r f i c i a l v e l o c i t y data, were input t o a computer program f o r data r e d u c t i o n .

ACS Symposium Series; American Chemical Society: Washington, DC, 1984. ch003 38 CHEMICAL AND CATALYTIC REACTOR MODELING t r i c k l e - f l o w r e a c t o r s o f f e r s e v e r a l advantages over s l u r r y operation. However, the design and scale-up of t r i c k l e - b e d r e a c t o r s i s more d i f f i c u l t than s l u r r y r e a c t o r s which seems to be a disadvantage ( 2 ) . Accurate p r e d i c t i o n of t r i c k l e - b e d r e actor performance r e q u i r e s r e l i a b l e methods f o r estimation of such items as i n t r i n s i c r e a c t i o n k i n e t i c s , l i q u i d - g a s flow d i s t r i b u t i o n , l i q u i d - s o l i d contacting e f f e c t i v e n e s s , i n t e r phase and intraphase heat and mass t r a n s f e r , texture of l i q u i d f i l m s , and thermodynamic parameters.

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Chemical and Catalytic Reactor Modeling by Milorad P. Duduković and Patrick L. Mills (Eds.)


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