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首页> 外文期刊>AIChE Journal >3-D Full-Loop Simulation of an Industrial-Scale Circulating Fluidized-Bed Boiler
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3-D Full-Loop Simulation of an Industrial-Scale Circulating Fluidized-Bed Boiler

机译:工业规模循环流化床锅炉的3-D全循环模拟

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摘要

Three-dimensional (3-D) simulations using an Eulerian multiphase model were employed to explore flow behaviors in a full-loop industrial-scale CFB boiler with and without fluidized-bed heat exchanger (FBHE), where three solids phases were employed to roughly represent the polydisperse behavior of particles. First, a simulation of the boiler without FBHE is implemented to evaluate drag models, in terms of pressure profiles, mixing behaviors, radial velocity profiles, etc. Compared to the conventional model, the simulation using the energy-minimization multiscale (EMMS) model successfully predicts the pressure profile of the furnace. Then, such method is used to simulate the boiler with FBHE. The simulation shows that solid inventory in the furnace is underpredicted and reducedwith an increase of the valve opening, probably due to the under evaluated drag for FBHE flows. It is suggested to improve EMMS model which is now based on a single set of operating parameters to match with thefull-loop system.
机译:使用欧拉多相模型进行的三维(3-D)模拟研究了具有和不具有流化床换热器(FBHE)的全回路工业规模CFB锅炉的流动特性,其中采用了三个固相代表颗粒的多分散行为。首先,对不带FBHE的锅炉进行仿真,以评估阻力模型,包括压力分布,混合行为,径向速度分布等。与常规模型相比,使用最小能量多尺度(EMMS)模型进行的仿真成功预测炉子的压力曲线。然后,采用这种方法对FBHE进行锅炉模拟。模拟表明,炉中的固体存量被低估,并随着阀门开度的增加而减少,这可能是由于对FBHE流量的拖曳力评估不足。建议改进EMMS模型,该模型现在基于一组操作参数来与全回路系统匹配。

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