Improving Three Phase Modeling of Fluidized Bed Dryer

Document Type : Research Article

Authors

1 Department of Mechanical Engineering, Marvdasht Branch, Islamic Azad University, Marvdasht, I.R. IRAN

2 Department of Mechanical Engineering, Hormozgan University, Bandar Abbas, I.R. IRAN

Abstract

Heat transfer phenomena in batch fluidized bed dryer have been studied and analyzed using three phase model including solid phase, interstitial gas phase and bubble phase based on Rizzi model. New correlations of heat transfer coefficient to surrounding and convection heat transfer coefficient between solid and interstitial gas are being proposed. In addition, some modifications have been done according to the state of flow and particle properties.The model was used to study the effects of particle diameter, particle density and input gas temperature on Geldart group D particles. The numerical results of heat transfer such as solid and gas temperature distributions have been compared with the available experimental data and good agreement between them is observed.

Keywords

Main Subjects


[1] Kunni D., Levenspiel O., “Fluidization Engineering” Butterworth-Heinemann, 2nd ed.: 21&143 (1991).
[2]  Yates J.G., “Fundamental of Fluidized Bed Chemical Processes”, Butterworths. London, UK, 4-71 (1983).
[3] Groenewold H., Tsotsas E., A New Model for Fluidized Bed Drying, Drying Technology, 15(6-8): 1687- 1698 (1997).
[4]  Palancz B., A Mathematical Model for Continuous Fluidized Bed, Chemical Engineering Science J., 38(7): 1045- 1059 (1983). 
[5] Wildhagen G.R.S., Calçada L.A., Massarani G., Drying of Porous Particles in Fluidized Beds: Modeling and Experiments, J. of Porous Media, 5(2): 123- 133 (2002).
[6]  Vitor João F.A., Biscaia Jr., Evaristo C., Massarani G., Modeling of Biomass Drying in Fluidized Bed,"International Drying Symposium",B: 1104-1111 (2004).
[7]  Rizzi Jr. A.C., Passos M.L., Freire J.T., Modeling and Simulating the Drying of Grass Seeds (Brachiariabrizantha) in Fluidized Beds: Evaluation of Heat Transfer Coefficient, Chemical Engineering J., 26(03): 545-554 (2009).
[8] Madhiyanon T., Techaprasan A., Soponronnarit S., Mathematical Models Based on Heat Transfer and Coupled Heat and Mass Transfers for Rapid High Temperature Treatment in Fluidized Bed: Application for Grain Heat Disinfestations, International J. of Heat and Mass Transfer, 49: 2277-2290 (2006).
[9] Horio Masayuki, Nonaka Akira, A Generalized Bubble Diameter Correlation for Gas-Solid Fluidized Beds, AIChEJ., 33(11): 1865-1872 (1987).
[10] Pahlavanzadeh H. et al., Estimation of Heat and Mass Tansfer Coefficient in Fluidized Bed Dryers as a Function of Moisture Content, Nashrieh Shimi va Mohandesi Shimi Iran (NSMSI), 27(4): 41-50 (2009).[ In Persian]