NDLI: Modelling of batch fluidized bed drying of baker yeast for cylindrical pellets

Content Provider	IEEE Xplore Digital Library
Author	Yuzgec, U. Turker, M. Becerikli, Y.
Copyright Year	2004
Description	Author affiliation: Dept. of Electron. & Telecommunciations Eng., Kocaeli Univ., Turkey (Yuzgec, U.)
Abstract	A mathematical model was enveloped to describe the drying process of microorganism pellets in a fluidized bed dryer. The modeling of heat and mass transfer between air and the pellets in fluidized bed dryers is based on application of temperature and diffusion equations inside the pellets. These equations were nonlinear partial differential equation. Robin boundary condition was selected to solve nonlinear differential equations. In this model, the microorganism pellets are assumed to be nonshrinking and homogenous. The material forms were cylindrical geometry. The baker yeast, the microorganism Saccharomyces cerevisiae was used to test the model in this study. The experimental results of the drying process were compared to the mathematical model predictions. As to the results of comparison, this model was shown very good agreement for batch fluidized bed drying of baker yeast.
Starting Page	7
Ending Page	12
File Size	281350
Page Count	6
File Format	PDF
ISBN	0780385993
DOI	10.1109/ICMECH.2004.1364403
Language	English
Publisher	Institute of Electrical and Electronics Engineers, Inc. (IEEE)
Publisher Date	2004-06-05
Publisher Place	Turkey
Access Restriction	Subscribed
Rights Holder	Institute of Electrical and Electronics Engineers, Inc. (IEEE)
Subject Keyword	Fluidization Fungi Microorganisms Mathematical model Nonlinear equations Differential equations Partial differential equations Heat transfer Temperature Boundary conditions
Content Type	Text
Resource Type	Article

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