By H. Scott Fogler (Eds.)
content material: Fluidized mattress reactor modeling : an summary / J.R. Grace --
An preliminary price method of the counter-current backmixing version of the fluid mattress / V.K. Jayaraman, B.D. Kulkarni, and L.K. Doraiswamy --
Predictions of fluidized mattress operation below restricting stipulations : response keep watch over and shipping keep an eye on / H.S. Fogler and L.F. Brown --
Simulation of a fluidized mattress reactor for the construction of maleic anhydride / J.L. Jaffrès, W. Ian Patterson, C. Chavarie, and C. Laguérie --
A version for a gas-solid fluidized mattress filter out / Michael H. Peters, Thomas L. Sweeney, and Liang-Shih Fan --
Modeling and simulation of dynamic and steady-state features of shallow fluidized mattress combustors / L.T. Fan and C.C. Chang --
Modeling of fluidized mattress combustion of coal char containing sulfur / A. Rehmat, S.C. Saxena, and R.H. Land --
desktop modeling of fluidized mattress coal gasification reactors / T.R. Blake and P.J. Chen --
research of the habit of warmth and mass move coefficients in gas-solid fluidized mattress structures at low Reynolds numbers / J. Ramírez, M. Ayora, and M. Vizcarra --
Bubble column, an outline / Yatish T. Shah --
entry of hydrodynamic parameters required within the layout and scale-up of bubble column reactors / Wolf-Dieter Deckwer --
a brand new version for warmth move coefficients in bubble columns / Yatish T. Shah, J.B. Joshi, and M.M. Sharma --
Dispersion and hold-up in bubble columns / Richard G. Rice, Jorma M.I. Tupperainen, and Robyn M. Hedge --
Packed mattress reactors, an summary / Arvind Varma --
resolution of packed mattress heat-exchanger versions via orthogonal collocation utilizing piecewise cubic hermite features / A.G. Dixon --
An research of radial circulation packed mattress reactors : how are they diverse? / Hsueh-Chia Chang and Joseph M. Calo --
relocating mattress coal gasifier dynamics utilizing MOC and MOL strategies / Richard Stillman --
mounted mattress reactors with deactivating catalysts / James M. Pommersheim and Ravindra S. Dixit.
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Content material: Fluidized mattress reactor modeling : an summary / J. R. Grace -- An preliminary price method of the counter-current backmixing version of the fluid mattress / V. ok. Jayaraman, B. D. Kulkarni, and L. ok. Doraiswamy -- Predictions of fluidized mattress operation less than proscribing stipulations : response keep watch over and delivery keep watch over / H.
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G. Chem. Eng. (London) 1975, 671-677. Zenz, F. ; Othmer, D. F. " F l u i d i z a t i o n and F l u i d - P a r t i c l e Systems," Reinhold, New York, 1960, pp. 231, 234. van Swaaij, W. P. M. in "Chemical Reaction Engineering Reviews-Houston" (D. Luss and V. W. ), ACS Symposium S e r i e s #72, American Chemical S o c i e t y , Washington, DC, 1979, pp. 193-222. RECEIVED June 3, 1981. ; ACS Symposium Series; American Chemical Society: Washington, DC, 1981. 4 Simulation of a Fluidized Bed Reactor for the Production of Maleic Anhydride J.
Yates, J. G. Chem. Eng. (London) 1975, 671-677. Zenz, F. ; Othmer, D. F. " F l u i d i z a t i o n and F l u i d - P a r t i c l e Systems," Reinhold, New York, 1960, pp. 231, 234. van Swaaij, W. P. M. in "Chemical Reaction Engineering Reviews-Houston" (D. Luss and V. W. ), ACS Symposium S e r i e s #72, American Chemical S o c i e t y , Washington, DC, 1979, pp. 193-222. RECEIVED June 3, 1981. ; ACS Symposium Series; American Chemical Society: Washington, DC, 1981. 4 Simulation of a Fluidized Bed Reactor for the Production of Maleic Anhydride J.
00376) (u -u J o mi 1 (u s in cm/s, and d D O 2 10 ( > in cm) Equations (6) and (2) are used to o b t a i n h, and the b u b b l e - r i s e v e l o c i t y u^, appears in Eq. ( 6 ) . Consequently, we see a p r e d i c a ment has a r i s e n , in that h is needed to c a l c u l a t e d^, which is needed to c a l c u l a t e u^, which in turn is needed to c a l c u l a t e h. To overcome this d i f f i c u l t y , the sequence in F i g u r e 1 is normally adopted. The unexpanded bed height was 39 cm, so the expanded bed height w i l l probably be around 60 cm and the average bubble s i z e w i l l f i r s t be c a l c u l a t e d a t L = h/2 = 30 cm.