By James Wei and Christos Georgakis (Eds.)
content material: Chemical response engineering as an highbrow self-discipline / R. Aris --
improvement of the methanol-to-gasoline strategy / J.E. Penick, W. Lee, and J. Maziuk --
Fluidized-bed reactors / P.N. Rowe --
Fluidized-bed coal combustion : controlling parameters / Adel F. Sarofim --
present difficulties in polymerization response engineering / W. Harmon Ray --
blending in chemical reactors / Jacques Villermaux.
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Additional resources for Chemical Reaction Engineering—Plenary Lectures
There was a complete absence of any troublesome "hot spots". In a d d i t i o n , the t r a n s i e n t temperature p r o f i l e s during heat-up and cool-down were a l s o uniform and s t a b l e . With these encouraging r e s u l t s , i t was decided to scale-up the f l u i d - b e d process f u r t h e r . A 100 B/D f l u i d - b e d program has been formulated to demonstrate h o r i z o n t a l scale-up. H o r i z o n t a l Scale-Up of F l u i d Bed. The 100 B/D p i l o t p l a n t w i l l provide a d d i t i o n a l i n f o r m a t i o n f o r design of a commercials c a l e , f l u i d - b e d process.
C. 20036 from C H E M I C A L REACTION 48 Literature Cited 1. Meisel, S. , McCullough, J. , Lechthaler, C. , and Weisz, P. , CHEMTECH, 1976, 6, 86-9. 2. Kokotailo, G. , Lawton, S. , Olson, D. , and Meier, W. , Nature, 1978, 272, 437-8. 3. Chang, C. , and Silvestri, A. , J. , 1977, 47, 249-59. 4. Fitch, F. , 1981. 5. Garwood, W. , "Conversion of C -C Olefins to Higher Olefins Over Synthetic Zeolite ZSM-5," presented at Am. Chem. Soc. , Las Vegas, Nevada, March, 1982. 6. Meisel, S. L. and Weisz, P.
Two-stage fixed-bed MTG. C H E M I C A L R E A C T I O N ENGINEERING 32 Since i n a l a r g e diameter f l u i d bed, bubbles may bypass the c a t a l y s t , elaborate hydrodynamic s t u d i e s are required to scale-up the r e a c t o r i n t e r n a l s to accomplish the complete conversion of methanol. As mentioned e a r l i e r , e s s e n t i a l l y complete conversion of methanol i s a process requirement; otherwise, a c o s t l y d i s t i l l a t i o n step must be added to recover unconverted methanol.