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In relation to this article, we declare that there is no conflict of interest.
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Received June 9, 2016
Accepted September 5, 2016
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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Bubble characteristics by pressure fluctuation analysis in gas-solid bubbling fluidized beds with or without internal

Department of Chemical Engineering, Sungkyunkwan University, Korea 1Hanwha Chemical R&D Center, Korea 2Department of Energy Engineering, WooSuk University, Korea
dhlee@skku.edu
Korean Journal of Chemical Engineering, February 2017, 34(2), 566-573(8), 10.1007/s11814-016-0255-7
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Abstract

Bubble flow characteristics were investigated in gas-solid bubbling fluidized beds (0.3 m-I.D×2.4m-high) with or without internals by power spectral analysis of absolute pressure fluctuation. Metallurgical grade silicon particles (MG-Si) were used as bed materials. The particle density and mean particle diameter were 2,328 kg/m3 and 154 μm, respectively. Absolute pressure fluctuations were measured simultaneously at two different positions: plenum chamber and beds. Absolute pressure fluctuation in the beds was measured according to the axial bed height in the range of 0.1 to 0.8m. The total sampling time of each data set was 60 s, and the sampling rate was 200Hz. Absolute pressure fluctuation data were converted to a power spectral density (PSD) by a Fast-Fourier transform (FTT) algorithm. The PSD in the beds was separated into coherent and incoherent output power. The bubble size was estimated from the standard deviation of the spectrum of incoherent output power, which occurred due to the bubble flow. The estimated bubble size determined by incoherence component analysis was compared to various empirical correlations to determine the bubble size without internals. The estimated bubble size agreed well with the correlation by Choi et al. [19]. The internals were installed 0.45 m above the distributor. With the installation of the internals, and at the bed height of 0.5m, the bubble diameter was decreased by 77% compared to the bubble without the internal at U0=0.15m/s.

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