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Received July 12, 2009
Accepted November 19, 2009
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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Hydrodynamic characteristics of cold-bed circulating fluidized beds for the methanol to olefins process

Department of Chemical Engineering, SungKyunKwan University, 300 Chunchun, Jangan, Suwon 440-746, Korea 1Department of Chemical Engineering, DanKook University, 126, Yongin 448-701, Korea 2Alternative Chemicals/Fuel Research Centre, Korea Research Institute of Chemical Technology, P.O. Box 107, Yuseong-gu, Daejeon 305-600, Korea
dhlee@skku.edu
Korean Journal of Chemical Engineering, July 2010, 27(4), 1328-1332(5), 10.1007/s11814-010-0187-6
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Abstract

The effects of the riser inlet velocity (2.2-3.9 m/s), seal-pot inlet velocity (2.4-7.1 Umf), aeration flow rate (2.5×10^(-7)-3.7×10^(-6) m3/s) in seal-pot, and solid inventory (0.15-0.2 kg) on the hydrodynamic characteristics of a 9 mm-ID×1.9 m-high cold-bed circulating fluidized bed for methanol to olefins (MTO) process were investigated. FCC (Engelhard; 82.4 μm) particles were used as bed particles. Most of the experimental flow regimes were observed in fast fluidization_x000D_ and pneumatic transport regimes. The axial solid holdup in a riser increased with increasing solid mass flux and solid inventory. Solid mass flux increased proportionally until reaching a maximum value and then decreased with increasing seal-pot inlet velocity. The obtained hydrodynamic characteristics in the cold-bed circulating fluidized beds were compared with previous results.

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