𝔖 Bobbio Scriptorium
✦   LIBER   ✦

Estimation of diffusion parameters in fluidized bed drying

✍ Scribed by C. Srinivasakannan; N. Balasubramanian


Publisher
Elsevier Science
Year
2009
Tongue
English
Weight
286 KB
Volume
20
Category
Article
ISSN
0921-8831

No coin nor oath required. For personal study only.


πŸ“œ SIMILAR VOLUMES


Diffusion model for fluidized-bed drying
✍ M. A. Zoglio; W. H. Streng; J. T. Carstensen πŸ“‚ Article πŸ“… 1975 πŸ› John Wiley and Sons 🌐 English βš– 477 KB

A sucroselactose-starch granulation was used to study particulate motion and attrition in a fluid bed dryer. There is some classification of material in the dryer as drying proceeds; fine particles are dried faster and become less dense, and the less dry but denser large particles show some (althoug

Fluidized bed drying of solids
✍ A. N. Chandran; S. Subba Rao; Y. B. G. Varma πŸ“‚ Article πŸ“… 1990 πŸ› American Institute of Chemical Engineers 🌐 English βš– 724 KB

A kinetic model is d e v e l o p e d for t h e drying of solids in fluidized b e d s , assuming a falling rate period following a constant rate period. Experimental d a t a obtained using b a t c h a n d continuous single a n d spiral fluidized b e d s are satisfactorily m a t c h e d with t h e ass

Drying of solids in vacuum fluidized bed
✍ Bulent Umur Kozanoglu; Juan Antonio Vilchez; Joaquim Casal; Josep Arnaldos πŸ“‚ Article πŸ“… 2002 πŸ› John Wiley and Sons 🌐 English βš– 874 KB

## Abstract A drying process in a fluidized bed under vacuum conditions is experimentally and theoretically studied. A fluidized bed operating in reduced pressure presents a possibility for a better quality of production, with safer process conditions. A mathematical model is developed for the redu

Modelling of Fluidized-bed Drying of Bla
✍ S.J. Temple; A.J.B. van Boxtel πŸ“‚ Article πŸ“… 1999 πŸ› Elsevier Science 🌐 English βš– 224 KB

Notation a air mass #ow, kg/s A air mass, kg c , c constants C N speci"c heat, kJ/kg K h enthalpy #ow, kJ/s H total enthalpy, kJ H T latent heat of evaporation, kJ/kg J evaporation rate, kg H O/kg dm s k drying rate constant, s\ ΒΈbed depth, m m #ow rate of dry matter, kg/s M dry matter mass, kg ΒΉ te