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燃煤电厂脱硫废水旁路烟气干燥塔粘壁原因分析

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为解决燃煤电厂脱硫废水旁路烟气干燥塔常遇到的粘壁问题,探讨了干燥塔烟气量、塔径、塔高、烟气分配器流速等参数的复核方法,从设计、设备、运行等方面分析了旁路烟气干燥塔粘壁原因及建议措施,并提出了一种基于单变量控制原则的粘壁风险从小到大的粘壁原因排查方法.以某三十万机组干燥塔为例,该干燥塔烟气量、塔径塔高等参数满足要求,但烟气分配器出口烟气流速过低且旋转过强,雾滴在干燥前被含尘热烟气带到塔壁导致粘壁.通过改造烟气分配器,将内、外导风通道出口流速从10.13 m/s、19.66 m/s提高至19.36 m/s、23.85 m/s,该干燥塔粘壁问题得到了解决.
Analysis of Wall Sticking in Bypass Flue Gas Drying Tower for Desulfurization Wastewater of Coal-fired Power Plant
Wall sticking in bypass flue gas drying tower for desulfurization wastewater of coal-fired power plant is a common problem encountered during operation.This study discusses the review methods for parameters such as the volume of flue gas in the drying tower,tower diameter,tower height,and flow velocity of the flue gas distributor.It analyzes the causes of wall sticking in bypass flue gas drying towers from aspects of design,equipment,and operation,along with proposed measures to address them.Additionally,a method based on the principle of single variable control for troubleshooting wall sticking issues,ranging from low to high risk,is introduced.Taking a 300,000 kW unit's drying tower as an example,the parameters like the volume of flue gas,tower diameter,and tower height met the requirements.However,the flow velocity of the flue gas exiting the distributor was too low and exhibited excessive rotation,leading to droplets being carried to the tower walls by dusty hot flue gas before drying,resulting in wall sticking.By modifying the flue gas distributor to increase the outlet flow velocities of the inner and outer guide channels from 10.13 m/s and 19.66 m/s to 19.36 m/s and 23.85 m/s respectively,the issue of wall sticking in the drying tower was resolved.

bypass flue gas drying towerdesulfurization wastewaterzero emissionwall adhesionash blockage

张威

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浙江浙能科技环保集团股份有限公司,浙江 杭州 311100

旁路烟气干燥塔 脱硫废水 废水零排放 粘壁 堵灰

2024

广东化工
广东省石油化工研究院

广东化工

影响因子:0.288
ISSN:1007-1865
年,卷(期):2024.51(14)