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Numerical simulation of bypass evaporation system treating FGD wastewater using high temperature flue gas

机译:用高温烟气处理FGD废水的旁路蒸发系统数值模拟

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摘要

A novel zero-liquid discharge (ZLD) technology for desulfurization wastewater treatment is put forward in this paper. A ZLD reconstruction project performed on 2 x 320 MW desulfurization system was taken as the research object, to study the evaporator structure and the key factors affecting spray evaporation through CFD numerical simulation. The result shows that when the evaporator diameter is 2.4 m, the central density difference and the temperature difference of evaporator outlets are 0 kg/L and 0 degrees C, under this condition, the wall sticking can be avoided effectively, and the uniformity of evaporator's outlet flow field is improved. As for the same amount of wastewater, small atomized particle size, high flue gas flow rate and high flue gas temperature are conducive to complete evaporation, and the optimum atomized particle size is 100-150 mu m, flue gas velocity is 3-4 m/s and flue gas temperature is 250-260 degrees C. In order to reduce adverse impact on the main flue duct, the optimized design scheme that extracting flue gas before and after the air preheater is put forward in the purpose of energy saving.
机译:本文提出了一种用于脱硫废水处理的新型零液排放(ZLD)技术。在2×320 MW脱硫系统上进行了ZLD重建项目作为研究对象,研究蒸发器结构和影响喷雾蒸发的关键因素通过CFD数值模拟。结果表明,当蒸发器直径为2.4μm时,蒸发器出口的中心密度差和蒸发器出口的温度差为0kg / l和0℃,在这种情况下,可以有效地避免壁粘附,以及蒸发器的均匀性出口流场得到改善。至于相同数量的废水,小雾化粒度,高烟气流量和高烟气温度有利于完全蒸发,最佳雾化粒度为100-150μm,烟气速度为3-4米/ s和烟道气温度为250-260℃。为了降低对主烟道管道的不利影响,提取空气预热器前后提取烟气的优化设计方案以节能。

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