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Abstract:

A correlation to predict the maximum mass transfer from a liquid fluidized bed to the column wall or to an immersed surface has been proposed on the basis of available data in the literature. In addition, an equation is presented to determine the optimum fluidizing velocity at which the bed should be operated. © 1983, American Chemical Society. All rights reserved.

Registro:

Documento: Artículo
Título:Communications Maximum Mass Transfer to the Wall or Immersed Objects in Liquid Fluidized Beds
Autor:Böhm, U.
Filiación:Departamento de Industrias, Universidad de Buenos, Aires Ciudad Universitaria, 1428 Buenos Aires, Argentina
Palabras clave:CHEMICAL OPERATIONS - Fluidization; MASS TRANSFER
Año:1983
Volumen:22
Número:2
Página de inicio:339
Página de fin:341
DOI: http://dx.doi.org/10.1021/i200021a027
Título revista:Industrial and Engineering Chemistry Process Design and Development
Título revista abreviado:Ind. Eng. Chem. Process. Des. Dev.
ISSN:01964305
Registro:https://bibliotecadigital.exactas.uba.ar/collection/paper/document/paper_01964305_v22_n2_p339_Bohm

Referencias:

  • Carbin, D.C., Qabe, D.R., (1974) Electrochim. Acta, 19, p. 645
  • Carbin, D.C., Qabe, D.R., (1975) J. Appl. Electrochem., 5, p. 129
  • Coeuret, F., Vergnes, F., Le Goff, P., (1969) HouBe Blanche, 3, p. 275
  • Coeuret, F., Le Goff, P., (1976) Electrochim. Acta, 21, p. 195
  • Grewal, N.S., Saxena, S.C., (1981) Ind. Eng. Chem. Process Des. Dev., 20, p. 108
  • Heschel, W., Klose, E., (1971) Chem. Tech. (Leipzig), 23, p. 219
  • Heyde, M., Klocke, H., (1979) J. Chem. Ing. Tech., 51, p. 318
  • Jagannadharaju, G.J.V., Venkata Rao, C., (1965) Indian J. Technol., 3, p. 201
  • Jottrand, R., Grunchard, F., (1962) “The Interaction between Fluids and Particles”, p. 211. , 3rd Congress of the European Federation of Chemical Engineering, Institution of Chemical Engineers: London
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  • King, D.H., (1970) Ph.D. Thesis, , University of Toronto, Ontario, Canada
  • Kreysa, G., Pionteck, S., Heltz, E., (1975) J. Appl. Electrochem., 5, p. 305
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  • Richardson, J.F., Romani, M.N., Shaklrl, K., (1976) J. Chem. Eng. Sci., 31, p. 619
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  • Storck, A., Coeuret, F., (1980) Chem. Eng. J., 20, p. 149
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Citas:

---------- APA ----------
(1983) . Communications Maximum Mass Transfer to the Wall or Immersed Objects in Liquid Fluidized Beds. Industrial and Engineering Chemistry Process Design and Development, 22(2), 339-341.
http://dx.doi.org/10.1021/i200021a027
---------- CHICAGO ----------
Böhm, U. "Communications Maximum Mass Transfer to the Wall or Immersed Objects in Liquid Fluidized Beds" . Industrial and Engineering Chemistry Process Design and Development 22, no. 2 (1983) : 339-341.
http://dx.doi.org/10.1021/i200021a027
---------- MLA ----------
Böhm, U. "Communications Maximum Mass Transfer to the Wall or Immersed Objects in Liquid Fluidized Beds" . Industrial and Engineering Chemistry Process Design and Development, vol. 22, no. 2, 1983, pp. 339-341.
http://dx.doi.org/10.1021/i200021a027
---------- VANCOUVER ----------
Böhm, U. Communications Maximum Mass Transfer to the Wall or Immersed Objects in Liquid Fluidized Beds. Ind. Eng. Chem. Process. Des. Dev. 1983;22(2):339-341.
http://dx.doi.org/10.1021/i200021a027