Abstract:
The fluid dynamic behaviour and the liquid‐solid mass transfer to horizontal cylinders, under bubble induced convection, was investigated. The gas void fraction was measured and overall mass transfer coefficients were determined for single cylinders as well as for banks of tubes with various characteristics. Copyright © 1993 Canadian Society for Chemical Engineering
Registro:
Documento: |
Artículo
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Título: | Mass transfer in tube banks with two‐phase flow |
Autor: | Giorgio, A.C.D.D.; Cavatorta, O.N.; Böhm, U. |
Filiación: | Departamento de Industrias, Facultad de Ciencias Exactas Y Naturales, Universidad de Buenos Aires, Ciudad Universitaria, Buenos Aires, 1428, Argentina Escuela de Ingenienría Química, Universidad Central de Venezuela, Apartado 51576, Caracas, 51576, Venezuela
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Palabras clave: | gas sparging; mass transfer; tube bundles; Fluid dynamics; Heat convection; Mass transfer; Mathematical models; Two phase flow; Bubble induced convection; Gas sparging; Tube banks; Chemical reactors; Bubbles; Convection; Mass Transfer; Two-Phase Flow(Liquid/Solid |
Año: | 1993
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Volumen: | 71
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Número: | 1
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Página de inicio: | 63
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Página de fin: | 67
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DOI: |
http://dx.doi.org/10.1002/cjce.5450710109 |
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_v71_n1_p63_Giorgio |
Referencias:
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- Cavatorta, O.N., Böhm, U., Mass Transfer in Electrolytic Cells With Gas Stirring (1987) J. Appl. Electrochem., 17, pp. 340-346
- Cavatorta, O.N., Böhm, U., Heat and Mass Transfer in Gas Sparging Systems: Empirical Correlations and Theoretical Models (1988) Chem. Eng. Res. Des., 66, pp. 265-274
- Cavatorta, O.N., Böhm, U., Chiappori de del Giorgio, A.M., Mass Transfer in Annular Electrolytic Cells With Gas Stirring (1991) J. Appl. Electrochem., 21, pp. 40-43
- Deckwer, W.D., On the Mechanism of Heat Transfer in Bubble Column Reactors (1980) Chem. Eng. Sci., 35, pp. 1341-1346
- Fair, J.R., Lambright, A.J., Andersen, J.W., Heat Transfer and Gas Hold‐up in a Sparged Contactor (1962) Ind. Eng. Chem. Proc. Des. Dev., 1, pp. 33-36
- Hikita, H., Asai, S., Kikukawa, H., Zaike, T., Ohue, M., Heat Transfer Coefficient in Bubble Columns (1981) Ind. Eng. Chem. Proc. Des. Dev., 20, pp. 540-545
- Kast, W., Analyse des Wärmeübergang in Blasensäulen (1962) Int. J. Heat Mass Transfer, 5, pp. 329-336
- Kölbel, H., Siemes, W., Maas, R., Müller, K., Wärmeübergang an Blasensäulen (1958) Chemie Ingenieur Technik - CIT, 30, pp. 400-404
- Korte, H.J., (1987), “Wärmeübergang in Blasensäulen mit und ohne Ein‐ bauten”, Thesis, Universität Dortmund; Lewis, D.A., Field, R.W., Xavier, A.M., Edwards, D., Heat Transfer in Bubble Columns (1982) Trans. Inst. Chem. Eng., 60, pp. 40-47
- Ruckenstein, E., Smigelschi, O., Heat Transfer to Bubble Beds (1965) Trans. Inst. Chem. Eng., 43, pp. 334-338
- Selman, J.R., Tobias, C.W., Mass Transfer Measurements by the Limiting‐Current Technique (1978) Adv. Chem. Eng., 10, pp. 211-328
- Wendt, R., (1983), “Untersuchungen zum Wärmeübergang an Einzelrohren und querangeströmten Rohrbündelwärmeaustauschern in Blasen‐ säulenreaktoren” Thesis, Universität Dortmund
Citas:
---------- APA ----------
Giorgio, A.C.D.D., Cavatorta, O.N. & Böhm, U.
(1993)
. Mass transfer in tube banks with two‐phase flow. The Canadian Journal of Chemical Engineering, 71(1), 63-67.
http://dx.doi.org/10.1002/cjce.5450710109---------- CHICAGO ----------
Giorgio, A.C.D.D., Cavatorta, O.N., Böhm, U.
"Mass transfer in tube banks with two‐phase flow"
. The Canadian Journal of Chemical Engineering 71, no. 1
(1993) : 63-67.
http://dx.doi.org/10.1002/cjce.5450710109---------- MLA ----------
Giorgio, A.C.D.D., Cavatorta, O.N., Böhm, U.
"Mass transfer in tube banks with two‐phase flow"
. The Canadian Journal of Chemical Engineering, vol. 71, no. 1, 1993, pp. 63-67.
http://dx.doi.org/10.1002/cjce.5450710109---------- VANCOUVER ----------
Giorgio, A.C.D.D., Cavatorta, O.N., Böhm, U. Mass transfer in tube banks with two‐phase flow. Can. J. Chem. Eng. 1993;71(1):63-67.
http://dx.doi.org/10.1002/cjce.5450710109