Abstract:
The local mass transfer rate to tubes immersed in gas‐liquid two‐phase systems was studied using the electrochemical method. It was found that the mass transfer distribution around the tube perimeter is not uniform and depends on the geometry of the system, the properties of the liquid phase and the superficial gas velocity. Taking into account the analogy between heat and mass transfer, these results may be useful in both fields. Copyright © 1994 Canadian Society for Chemical Engineering
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Documento: |
Artículo
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Título: | Local mass transfer for tube banks in two‐phase flow |
Autor: | Giorgio, A.C.D.D.; Cavatorta, O.N.; Böhm, U. |
Filiación: | Universidad Central de Venezuela, Escuela de Ingenieria Quimica, Apartado 51576, Caracas, 1050, Venezuela Departamento de Industrias, Facultad de Ciencias Exactas y Naturales, Universidad de Buenos Aires, Ciudad Universitaria, Buenos Aires, 1428, Argentina
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Palabras clave: | gas‐liquid dispersions; Keywords: local mass transfer; tube banks; Dispersions; Electrolytic analysis; Mass transfer; Tubes (components); Gas liquid dispersions; Local mass transfer; System geometry; Tube banks; Two phase flow; Mass Transfer; Tube Banks; Two-Phase Flow(Gas/Liquid |
Año: | 1994
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Volumen: | 72
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Número: | 1
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Página de inicio: | 50
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Página de fin: | 55
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DOI: |
http://dx.doi.org/10.1002/cjce.5450720108 |
Título revista: | The Canadian Journal of Chemical Engineering
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Título revista abreviado: | Can. J. Chem. Eng.
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ISSN: | 00084034
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Registro: | https://bibliotecadigital.exactas.uba.ar/collection/paper/document/paper_00084034_v72_n1_p50_Giorgio |
Referencias:
- Chiappori de del Giorgio, A., Cavatorta, O.N., Böhm, U., Mass Transfer in Tube Banks with Two‐phase Flow (1993) Can. J. Chem. Eng., 71, pp. 63-67
- Korte, H.J., Steiff, A., Weinspach, P.M., (1985), “Heat Transfer in Bubble Column Reactors”, Proceedings Int. Symposium on Heat Transfer, Tsinghua. China, Vol. 2; Korte, H.J., Steiff, A., Weinspach, P.M., (1986), pp. 61-72. , “A Comparison of Different Heat Exchanger‐installations in Bubble Columns With Respect to Their Heat Transfer Behaviour”, Proceedings Int. Conference on Bioreactor Fluid Dynamics, Cambridge, England; McAdams, W.H., (1954) Heat Transmission, , 3rd, McGraw‐Hill, New York
- Nieva, I.A., Böhm, U., Mass Transfer at Single Cylinders and at Tandem Arrangements of Two Cylinders Normal to the Flow (1979) Lat. Am. J. Heat, Mass Trans., 3, pp. 39-48
- Nieva, I.A., Böhm, U., Mass Transfer at Vertical and Horizontal Arrangements of Cylinders Normal to the Flow (1980) Lat. Am. J. Heat Mass Trans., 4, pp. 109-119
- Nieva, I.A., Böhm, U., Local Mass Transfer for Cross Flow Through Tube Banks of Square In‐line Layout at Intermediate Reynolds Number (1983) Int. J. Heat Mass Trans., 26, pp. 1283-1288
- Nieva, I.A., Böhm, U., Local Mass Transfer for Cross Flow Through Tube Banks: Equilateral Triangular Layout at Intermediate Reynolds Numbers (1985) Int. Commun. Heat Mass Trans., 12, pp. 227-285
- Nieva, I.A., Böohm, U., Mass Transfer in Tube Banks With a Fixed Bed ofInert Particles (1988) Lat. Am. Appl. Res., 18, pp. 59-62
- Nieva, I.A., Böhm, U., Mass Transfer in Tube Bundles With Liquid Fluidized Particles (1989) Can. J. Chem. Eng., 67, pp. 26-31
- Saxena, S.C., Heat Transfer From a Cylinder Probe Immersed in a Bubble Column (1989) Chem. Eng. J., 41, p. 25
- Saxena, S.C., Vadivel, R., Heat Transfer From a Tube Bundle in Bubble Column (1988) Int. Commun. Heat Mass Trans., 15, pp. 657-667
- Selman, J.R., Tobias, C.W., Mass Transfer Measurements by the Limiting Current Technique (1978) Adv. Chem. Eng., 10, pp. 211-324
- Schütz, G., Natural Convection Mass Transfer Measurements on Spheres and Horizontal Cylinders by an Electrochemical Method (1969) Int. J. Heat Mass Trans., 6, pp. 873-879
- Tonini, R.D., Remorino, M.R., Brea, F.M., Determination of Diffusi Coefficients With a Pipe Wall Electrode (1978) Electrochim. Acta, 23, pp. 699-704
- Weder, E., (1967), “Messung des Stoffüfbergangs von einer Flüssigkeit an eine feste Oberfläche mittels einer elektrochemischen Methode”, Ph.D. Thesis, ETH, Zürich, Switzerland
Citas:
---------- APA ----------
Giorgio, A.C.D.D., Cavatorta, O.N. & Böhm, U.
(1994)
. Local mass transfer for tube banks in two‐phase flow. The Canadian Journal of Chemical Engineering, 72(1), 50-55.
http://dx.doi.org/10.1002/cjce.5450720108---------- CHICAGO ----------
Giorgio, A.C.D.D., Cavatorta, O.N., Böhm, U.
"Local mass transfer for tube banks in two‐phase flow"
. The Canadian Journal of Chemical Engineering 72, no. 1
(1994) : 50-55.
http://dx.doi.org/10.1002/cjce.5450720108---------- MLA ----------
Giorgio, A.C.D.D., Cavatorta, O.N., Böhm, U.
"Local mass transfer for tube banks in two‐phase flow"
. The Canadian Journal of Chemical Engineering, vol. 72, no. 1, 1994, pp. 50-55.
http://dx.doi.org/10.1002/cjce.5450720108---------- VANCOUVER ----------
Giorgio, A.C.D.D., Cavatorta, O.N., Böhm, U. Local mass transfer for tube banks in two‐phase flow. Can. J. Chem. Eng. 1994;72(1):50-55.
http://dx.doi.org/10.1002/cjce.5450720108