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In relation to this article, we declare that there is no conflict of interest.
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Received April 26, 2002
Accepted August 27, 2002
articles This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
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Experimental, Statistical and Stochastic Studies of Pressure Fluctuations in a Three-phase Fluidized Bed with a Moderately Large Diameter

Department of Chemical Engineering, Woosuk University, Chonbuk 565-701, Korea 1Department of Chemical Engineering, Korea Advanced Institute of Science and Technology, Daejeon 305-701, Korea
drpark@woosuk.ac.kr
Korean Journal of Chemical Engineering, January 2003, 20(1), 121-127(7), 10.1007/BF02697196
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Abstract

Hydrodynamic properties of bubbling flow through a three-phase fluidized bed with a moderately large diameter have been characterized with statistical and stochastic analyses of a comprehensive set of experimentally measured pressure fluctuations in the bed. The analyses have yielded the fluctuations’ histogram, mean, maximum, minimum, standard deviation, skewness, kurtosis, and power-spectral-density function. As the gas flow rate increased with other operating conditions fixed, the mean and standard deviation increased, the skewness decreased, the distribution of the power-spectral-density function broadened, and the major frequency increased. In contrast, as the liquid flow rate increased, the mean and standard deviation decreased, the skewness and kurtosis increased, the power-spectral-density function narrowed, and the major frequency decreased. The hydrodynamic properties of a three-phase_x000D_ fluidized bed with a moderately large column in terms of pressure fluctuations are strongly affected by the flow rates of both the fluidizing gas and liquid.

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