Mass Transfer in Through-Circulation Drying of Packed Beds

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, w...

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Detalles Bibliográficos
Autor principal: Chirife, J.
Otros Autores: Gardner, R.G
Formato: Capítulo de libro
Lenguaje:Inglés
Publicado: 1972
Acceso en línea:Registro en Scopus
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Registro en la Biblioteca Digital
Aporte de:Registro referencial: Solicitar el recurso aquí
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100 1 |a Chirife, J. 
245 1 0 |a Mass Transfer in Through-Circulation Drying of Packed Beds 
260 |c 1972 
270 1 0 |m Chirife, J.; Departamento de Industrias, Falcultad de Ciencias Exactas y Naturales, Universidad de Buenos AiresArgentina 
506 |2 openaire  |e Política editorial 
504 |a Bradshaw, R.D., Myers, J.E., (1963) AIChE J., 9, p. 595 
504 |a Carberry, J.J., (1960) AIChE J., 6, p. 460 
504 |a Chilton, T.H., Colburn, A.P., (1934) Ind. Eng. Chem., 26, p. 1183 
520 3 |a 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.  |l eng 
593 |a Departamento de Industrias, Falcultad de Ciencias Exactas y Naturales, Universidad de Buenos Aires, Argentina 
593 |a Department of Pure and Applied Chemistry, University of Strathclyde, Glasgow, United Kingdom 
700 1 |a Gardner, R.G. 
773 0 |d 1972  |g v. 11  |h pp. 312-313  |k n. 2  |p Ind. Eng. Chem. Process. Des. Dev.  |x 01964305  |w (AR-BaUEN)CENRE-5125  |t Industrial and Engineering Chemistry Process Design and Development 
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