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By Jr. Frank L. Evans

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Extra resources for Equipment Design Handbook for Refineries and Chemical Plants. Volume 2

Sample text

R J (29) where r is the reaction rate. Notice that, although chemical equi librium prevails everywhere in the liquid, r is not zero, Since the reaction takes place at whatever rate is required to maintain chemical equilibrium in the presence of diffusion. b· m "" J (30) J J The coefficient A. , in the absence of diffusion phenomena) does not change the molarity; hence : r A. v. 30 is differentiated twice with respect to x, and Eq's. 32 is not zero; this implies that the molarity is not constant in the liquid phase.

Degaleesan. Transport Phenomena in Liquid Extraction (Tata Mc Graw Hill ~1ieWDe~ 1978). ----r4. Sci. 14 (1961) 161-170). -15. Trambouze. "Extractive Reaction: Batch or continous flow chemical reaction systems. Dilute case" AIChEJl 6 (1960) 394-402. 16. Trambouze,P. Piret "Continous stirred tank reactors". AIChEJl 5 (1959) 384-389. 17. Schonemann,K. Sci. 14 (1961) 193-203. 18. Alper,E-:--rrIntroduction to liquid-liquid systems". , 19"81). 19. A. "Introduction to gas-liquid-solid systems" (Proceedings of NATO ASI on "Mass transfer with chemical reaction in multiphase systems", Turkey, 1981) - 14 20.

4"8". Alper,E. Oeckwer. sci. 36 (1981) 1097-1099. 49. Juvekar. "Fast reactions in slurry reactors". _E_n~ng. S_cJ_~ 50. Davloson. '1recent developments in platinium metal catalyst systems". Chem~ (London) No: 283 (1974) 145-158. -51. Komiyama,H. Smith. "Sulfur dioxide oxidation in slurries of activated carbon. Part II. " AIChEJl 21 (1975) 664-676. 52. A. ) Chemical Engineerin of Gas-Liquid-Solid Catalyst Reactions (Procee lngs 0 an nternatlona symposlum CEBEDOC, [lege, 1979). 53. C. Calimli. "Direct coal liquefaction" (Proceedin2s of NATO ASI on "Mass transfer with chemical reaction in multlphase systems," Turkey, 1981].

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