Experimental results on mass transfer obtained during the constant rate period of the through-circulation drying of packed beds, were analyzed. The results, expressed as / factors, were correlated using a theoretical model for fluid-particle mass transfer in fixed beds. A good agreement was found, which allows us to deduce that a laminar boundary layer exists over the range of Reynolds numbers investigated. © 1972, American Chemical Society. All rights reserved.
Documento: | Artículo |
Título: | Mass Transfer in Through-Circulation Drying of Packed Beds |
Autor: | Chirife, J.; Gardner, R.G. |
Filiación: | Departamento de Industrias, Falcultad de Ciencias Exactas y Naturales, Universidad de Buenos Aires, Argentina Department of Pure and Applied Chemistry, University of Strathclyde, Glasgow, United Kingdom |
Año: | 1972 |
Volumen: | 11 |
Número: | 2 |
Página de inicio: | 312 |
Página de fin: | 313 |
DOI: | http://dx.doi.org/10.1021/i260042a028 |
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_v11_n2_p312_Chirife |