Numerical Simulation of the Flow Characteristics of 35t/h Internally Circulating Fluidized Bed

Author:

Chen Yu Lin1,Wang Qing2,Liu Cong Cong2,Ge Jian Xin2

Affiliation:

1. Jinneng Project Management Co. Ltd

2. Northeast Dianli University

Abstract

The gas-solid flow characteristics of the 35t/h oil shale-combustion circulating fluidized bed boiler (Developed by Wangqing Longteng Energy Development Co., Ltd) was simulated using Eulerian-Eulerian model (EEM), which was based on the kinetic theory of granular. The distribution of particle volume fraction and the distribution of particle velocity revealed the mechanism of the internal recirculation flow of particles in the furnace. The simulation results provided a reference for the flow structure optimization of the inner circulating fluidized bed and the enlargement of the inner circulating fluidized bed boiler.

Publisher

Trans Tech Publications, Ltd.

Reference5 articles.

1. Yuqing Feng , Tim Swenser-Smith. CFD modeling of gas-solid flow in an internally circulating fluidized bed. Powder Technology, 2012, 219, 78-85.

2. Lidong Zhang, Hongpeng Liu, Chunxia Jia. Research related to Chinese oil shale utilization. Chemical Industry and Engineering Progress, 2012, 31(11), 2359-2363.

3. Qing Wang, Xueheng Li. Experimental study on the circulating fluidized bed boiler combined splitter. Thermal Power Generation, 1999, (3), 18-29.

4. Nan Zhang, Jinghai Li. 3D CFD simulation of hydrodynamics of a 150 MWe circulating fluidized bed boiler. Chemical Engineering Journal, 2010, 162(2), 821-828.

5. S.V. Patankar. Heat transfer—a review of 1980 literature. International Journal of Heat and Mass Transfer, 1981, 24(12), 1863-(1902).

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