Prediction of Minimum Spout Velocity and Moisture Distribution of Ammonium Perchlorate Particles in a Spouted Bed Dryer

Document Type : Research Note

Authors

Department of Chemical Engineering, Amirkabir University of Technology, P.O. Box 15875-4413 Tehran, I.R. IRAN

Abstract

Ammonium perchlorate particles have been dried in a laboratory spouted bed dryer (screen-bottomed type) which is categorized as a fluidized bed dryer. The solid particles obtained in this process of drying were semi-porous and known as the group D of Geldart classification. The variations of moisture content with resident time, the effects of bed height on the pressure drop, and the influence of moisture content on drying rate were investigated. In this project, the air flow rate and the moisture diffusivity were determined. A model to determine the minimum spout velocity and also a model based on the Fick’s law were obtained which predicted the experimental data very well.

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[1] Mathur, K.B. and Gishler, P.E., A technique for contact gases with coarse solid particles, AIChE J., 1, 157 (1955).
[2] Mathur, K.B. and Epstein, N., “Spouted Beds”, Academic press,New York (1974).
[3] Kmiec, A., Hydrodynamics of flows and heat transfer in spouted beds, Chem. Eng. J., 19, 189 (1980).
[4] Sayles, D.C. and Ala, H., Microwave drying of ammonium perchlorate grinding spheres,  US patent, 4, 513 (1985).
[5] Mujumdar, A.S., Recent developments in spouted bed drying, keynote lecture, Transport Process in Porous Media Conference, Saocarlos. S.P., Brazil, (1989)
[6] Olazar, M., San jose, M.J., Aguayo, A.T., Arandes J.M., Pressure drop in conical spouted beds, Chem. Eng. J., 51, 53 (1995).
[7] Davahastin, S., Mujumdar, and Raghavan, G.S., Hydrodynamic characteristics of a rotary jet annular spouted bed, J. Powder Technology, 103, 169 (1999).
[8] Wang, Z.H. and Chen, G., Heat and mass trasfer during low intensity convective drying, Chem. Eng. Sci., 54, 3899 (1999).
[9] Mola, D. and Montazeri, H., Evaporation condensation and coagulation processes, J. Aerosol Sci., 31, 5793 (2000).
[10] Wang, Z.H. and Chen, G., Heat and mass trasfer in batch fluidized bed drying of porous particles,  Chem. Eng. Sci., 55, 1857 (2000).
[11] Kalbasi, M., Mehraban, M.R., The effect of surface water vapour flux on drying of potato, Trans
IChem. Eng., 78, 204 (2000).
[12] Hattori, H., Morimoto, T., Yamaguchi, M., Onez-awa, T. and Avac, C., Drying of porous solid particles in various-shaped spouted bed with a draft-tube,  J.  Chem.  Eng. of  Japan, 34, 1549 (2001).
[13] Wang, Z., Chen, P., Li, H., Wu. C. and Chen,Y., Study on the hydrodynamics of a spouting-moving bed, Ind. Eng. Chem. Res., 40, 4983 (2001).
[14] Davidson,  J. F., Thorpe, R. B.,  Al-Mansouri,  O., Kwaong, H., Peck, M. and Williamson, R., Evaporation of water from air-fluidized porous particles, Chem. Eng. Sci., 56, 6089 (2001).
[15] Kalbasi, M., Heat and moisture transfer model for onion drying, Drying Technology, 21, 1575 (2003)
[16] Perry, R.H. and  W .Green, D., “Perry's Chemical Engineers Handbook”, 5th Ed., McGrow-Hill Book Company, New York (1997).