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Modeling study on the impaction and humidification process in desulfurization activation reactor

机译:脱硫活化反应器冲击加湿过程的建模研究

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In a semi-industrial desulfurization activation reactor, the high-CaO coal ash is directly used as desulfurization sorbent and activated by spray water. As a result of the inertial impactions between ash particles and water droplets, concentrated slurry droplets are formed. In order to numerically investigate the process, a new model of particle-flow-passage is deduced to simulate the impaction humidification process between particles and droplets. Computation results show that the spray water flow rate and droplets size have obvious influence on droplets catching efficiency, and the ash particles are caught primarily in the vicinity of the atomizer nozzle. With the models of gas phase turbulence, heat and mass transfer, and chemical reactions being considered, a comprehensive 3D model for FGD process (Flue Gas Desulfurization) is established, and several operation conditions are simulated by the model. The predicted results such as SO2 absorption efficiency and the flue gas temperature at the outlet are in good agreement with experimental results. (C) 2004 Elsevier Ltd. All rights reserved.
机译:在半工业脱硫活化反应器中,高CaO煤灰直接用作脱硫吸附剂并通过喷雾水活化。由于灰分颗粒和水滴之间的惯性碰撞,形成了浓缩的浆滴。为了对这一过程进行数值研究,推导了一种新的颗粒流道模型,以模拟颗粒与液滴之间的冲击加湿过程。计算结果表明,喷雾水的流量和液滴的大小对液滴的捕集效率有明显的影响,灰分主要被捕集在雾化器喷嘴附近。考虑到气相湍流,传热和传质以及化学反应的模型,建立了烟气脱硫(烟气脱硫)的综合3D模型,并模拟了几种运行条件。 SO 2吸收效率和出口烟气温度等预测结果与实验结果吻合良好。 (C)2004 Elsevier Ltd.保留所有权利。

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