Chemical Reaction Engineering—Boston by James Wei, Christos Georgakis

By James Wei, Christos Georgakis

content material: Catalytic air oxidation of propylene to acrolein : modeling in response to facts from an business fixed-bed reactor / D. Arntz, okay. Knapp, G. Prescher, G. Emig, and H. Hofmann --
Simultaneous uncorrelated adjustments of technique variables in a fixed-bed reactor / A. Baiker, M. Bergougnan, and W. Richarz --
Direct aid of iron ore in a moving-bed reactor : analyzed by utilizing the water fuel shift response / R. Hughes and E.K.T. Kam : a simulation of coke burning in a fixed-bed reactor / W.-K. Liaw, J. Villadsen, and R. Jackson --
influence of porosity and speed distribution at the theoretical prediction of fixed-bed chemical reactor functionality : comparability with experimental facts / D. Vortmeyer and R.P. iciness --
a singular technique for picking out the multiplicity good points of multi-reaction platforms / Vemuri Balakotaiah and Dan Luss --
response cost oscillations in the course of the carbon monoxide oxidation response over Pt/[gamma]-Al₂O₃ catalysts : an IR-transmission spectroscopy examine / A.E. Elhaderi and T.T. Tsotsis --
Multiplicity and propagating fronts in adiabatic and nonadiabatic fixed-bed reactors / V. Hlavacek, J. Puszynski, and P. Van Rompay --
pressured composition biking experiments in a fixed-bed ammonia synthesis reactor / A.K. Jain, P.L. Silveston, and R.R. Hudgins --
Dynamic habit of an business scale fixed-bed catalytic reactor / L.S. Kershenbaum and F. Lopez-Isunza --
Modeling advanced response structures in fluidized-bed reactors / Werner Bauer and Joachim Werther --
Runaway in an commercial hydrogenation reactor / Gerhart Eigenberger and Ulrike Wegerle --
Transitions among periodic and chaotic states in a continual stirred reactor / J. Mankin, P. Lamba, and J.L. Hudson --
online estimation of the nation of biochemical reactors / Gregory Stephanopoulos and Ka-Yiu San --
price oscillations in the course of propylene oxide oxidation on silver motion pictures in a continual stirred reactor / Michael Stoukides, Savvas Seimanides, and Costas Vayenas --
Steam reforming of ordinary fuel : intrinsic kinetics, diffusional impacts, and reactor layout / J.C. De Deken, E.F. Devos, and G.F. Froment --
brief kinetics of the Fischer-Tropsch synthesis / E. Ph. Kieffer and H.S. Van Der Baan --
Rival kinetic versions within the oxidation of carbon monoxide over a silver catalyst by means of the brief reaction strategy / Masayoshi Kobayashi --
Mass move and product selectivity in a robotically stirred Fischer-Tropsch slurry reactor / Charles N. Satterfield and George A. Huff, Jr. --
The Fischer-Tropsch synthesis through amorphous Fe₂₀Ni₆₀P₂₀ and Fe₉₀Zr₁₀ catalysts / Akinori Yokoyama, Hiroshi Komiyama, Hakuai Inoue, Tsuyoshi Masumoto, and Hisamichi Kimura --
Modeling zeolite catalyst deactivation via coking and nitrogen compound poisoning / Chen-Chih Lin and William J. Hatcher, Jr. --
price of oxidation of ammonia on platinum wires, ribbons, and gauzes / C.W. Nutt, S. Kapur, and A. Majeed --
Dynamic discernment of catalytic kinetics / Deepak Perti and Robert L. Kabel --
Hydrogenation functionality of clean and deactivated hydrocracking catalysts : cyclohexene hydrogenation / S.R. Pookote, J.S. Dranoff, and J.B. Butt --
non-stop response fuel chromatography : the dehydrogenation of cyclohexane over Pt/[gamma]-Al₂O₃ / Alan W. Wardwell, Robert W. Carr, Jr., and Rutherford Aris --
Catalyst decay in the course of hydrotreatment of a heavy coal oil / Hong Ju Chang, Mayis Seapan, and Billy L. Crynes --
The steady-state permeation version for underground coal gasification / Henry W. Haynes, Jr. --
A pore diffusion version of char gasification with simultaneous sulfur catch / Klavs F. Jensen, William Bartok, and Howard Freund --
Nitric oxide aid through hydrogen and carbon monoxide over char floor : primary kinetics for nitric oxide emission regulate from fluidized-bed combustor of coal / Takehiko Furusawa, Mikio Tsunoda, and Daizo Kunii --
brief simulation of moving-bed coal gasifiers / Wen-Ching Yu, Morton M. Denn, and James Wei --
Simultaneous mass move of hydrogen sulfide and carbon dioxide with complicated chemical response in an aqueous diisopropanolamine answer / P.M.M. Blauwhoff and W.P.M. Van Swaaij --
Hydrodynamics and mass move in pulsing trickle-bed columns / J.R. Blok and A.A.H. Drinkenburg --
The percolation thought : a strong device for a unique method of the layout of trickle-bed reactors and columns / M.D. Crine and G.A. L'Homme --
Trickle-bed reactors : dynamic tracer assessments, response reports, and modeling of reactor functionality / A.A. El-Hisnawi, M.P. Duduković, and P.L. generators --
Exothermic fuel absorption with complicated response : sulfonation and discoloration within the absorption of sulfur trioxide in dodecylbenzene / R. Mann, P. Knysh, and J.C. Allan --
research of chemical and actual strategies in the course of devolatilization of a unmarried, huge particle of wooden / R. Wai Chun Chan and Barbara B. Krieger --
Characterization of nonisobaric diffusion as a result of nonequimolar fluxes in catalyst debris / C. McGreavy and M. Asaeda --
Coke deposition on a advertisement nickel oxide catalyst throughout the steam reforming of methane / Steve Paloumbis and Eugene E. Petersen --
actual features in natural liquid-phase oxidations / T. Sridhar and O.E. Potter --
Structural diversifications as a device to investigate the mechanism of noncatalytic solid-gas reactions / Sevil Ulkutan, Timur Dogu, and Gulsen Dogu --
warmth move in packed reactor tubes appropriate for selective oxidation / T. Wellauer, D.L. Cresswell, and E.J. Newson --
a brand new chemical technique for the research of neighborhood micromixing stipulations in commercial stirred tanks / J.P. Barthole, R. David, and J. Villermaux --
issues of macromixing and micromixing in semi-batch stirred bioreactors / R.K. Bajpai and M. Reuss --
blending, diffusion, and chemical response in one screw extruder / R. Chella and J.M. Ottino --
Mathematical version of low density polyethylene tubular reactor / G. Donati, L. Marini, G. Marziano, C. Mazzaferri, M. Spampinato, and E. Langianni --
The influence of combining on steady-state and balance features of low density polyethylene vessel reactors / C. Georgakis and L. Marini.

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V. -1 10 w 5 [m Is] , T = 571 Κ 0 *C H 2 %0 2 = 0 6 = 0 0 0 0 3 3 3 2 4 9 6 10 u z N T p 8 10 [m/s] Figure 6. Migration speeds as a function of the average gas flow. Key: · , mea­ sured points (IS); , calculation with uniformflow(IS); and , calculation with nonuniform flow. ; ACS Symposium Series; American Chemical Society: Washington, DC, 1982. VORTMEYER AND WINTER Fixed-Bed Chemical Reactor Performance Figure 8. Key is the same as in Figure 6. ; ACS Symposium Series; American Chemical Society: Washington, DC, 1982.

Solution of Differential Equation Models by Polynomial Approximation", Prentice H a l l , New Jersey, 1978. 8. Van den Bosch, B . ; Hellinckx 9. T. Proc. on Comp. Appl. in Chem. 155. 10. Bard, Y. 61. RECEIVED April 27, 1982. ; ACS Symposium Series; American Chemical Society: Washington, DC, 1982. 27 3 Direct Reduction of Iron Ore in a Moving-Bed Reactor: Analyzed by Using the Water Gas Shift Reaction R. HUGHES and Ε . Κ. T. K A M University of Salford, Department of Chemical Engineering, Salford M5 4WT, England A model f o r th d i r e c t r e d u c t i o f iro in a moving bed has f o r the water ga equilibriu u c t i o n by the species H and CO.

5 mm i n diameter i n a packed bed about 1 m deep. 0% oxygen. At the s t a r t of regeneration the c a t a l y s t t y p i c a l l y bears 2% coke by weight. For the present purpose the coke i s t r e a t e d as carbon and the C0 /C0 r a t i o i n the combustion products i s r e l a t e d to temperature as suggested by Arthur [5] and Rossberg [6]. Then the f o l l o w i n 2 1) The accumulation term i s neglected i n the oxygen balance w i t h i n a p e l l e t . 2) The accumulation term i s n e g l e c t e d i n the oxygen balance f o r the f l o w i n g gas.

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