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两相流诱发低温省煤器磨损的分析与应用

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[目的]为解决气-颗粒两相流诱发低低温电除尘器配套的低温省煤器磨损问题,诊断分析其磨损的主要影响因素和原因,进而提出优化措施.[方法]采用计算流体力学-离散相模型-冲蚀磨损预测模型(computational fluid dynamics-discrete phase mode-erosion prediction model,CFD-DPM-EPM)耦合的数值模拟方法,对低温省煤器进行数值模拟分析;构建低温省煤器的基准模型,分析烟气速度、粉尘浓度和烟气速度均匀性对磨损速率的影响;通过比较磨损速率和低温省煤器入口断面速度分布均匀性分别验证数值模型的可靠性和网格的敏感性.[结果]入口烟气速度过大、粉尘浓度过高和烟气速度分布不均都容易诱发省煤器磨损;某电厂2×660 MW机组低低温电除尘器低温省煤器改造后左、右两侧低温省煤器进口断面烟气最大速度分别从21.94、21.12m/s降低到12.97、12.81 m/s,速度偏差系数分别从0.322、0.310降到0.201、0.210,最大磨损速率分别下降75.2%、87.8%.[结论]研究结果可为低温省煤器磨损现象的诊断分析以及磨损优化设计提供参考依据.
Analysis and application of low-temperature economizer erosion induced by two-phase flow
Objective To enhance the dust removal efficiency of electrostatic precipitators,especially for the removal of fine particulate mat-ter like PM2.5,a low-temperature economizer is often integrated into a sub-low-temperature electrostatic precipitator.It's worth noting that the sub-low-temperature electrostatic precipitator is often subjected to wear,ash accumulation,and corrosion during operation,leading to blockages and leaks in the heat exchange tubes.To address the wear problem of low temperature economizer within the low-temperature electrostatic precipitator induced by gas-particle two-phase flow,we diagnosed the causes and proposed optimization measures that can serve as a reference for the design and optimization of similar engineering projects.Methods Computational fluid dynamics and discrete phase model(CFD-DPM)method were employed to capture multi-phase flow details,and an erosion prediction model(EPM)was utilized for wear prediction.The realizable k-e turbulence model was applied to solve the continuous phase,employing the Lagrange method to track the dust particle trajectories and the rebound model for particle-wall collision.The reliability of the numerical model was verified by comparing the wear rates.The sensitivity of the grid was assessed by examining the uniformity of velocity distribution at the inlet section of low-temperature economizer.Results and Discussion In the benchmark model study,it was observed that lower flue gas velocities corresponded to reduced wear rates of the heat exchange tubes,indicating the necessity of a sufficiently large flue section area in the design of a low-temperature economizer.Furthermore,a decrease in dust concentration upstream of the low-temperature economizer correlated with a slower wear rate of the heat exchange tubes,suggesting the importance of implementing pre-collection measures to miti-gate high dust concentrations entering the economizer.The impact of dust particles on the heat exchange tubes and its fins led to decreased velocity and changed direction,resulting in wear conditions in the low-temperature economizer that did not fully corre-spond to the gas distribution.In the engineering application study,flow field distributions before and after reconstruction were compared and analyzed from the following aspects:1)The optimized design of the flue structure and baffles eliminated the eddy zone on the leeward side of individual baffles that existed before the renovation.2)Before the renovation,the flue gas produced a high-velocity jet downstream after passing through the guide plate in the inlet horn of the low-temperature economizer.The maximum flue gas velocities of the first row of the left and right sides of the pseudo-pipe were 21.94 and 21.12 m/s,respec-tively,which were reduced to 12.97 and 12.81 m/s,respectively,after the renovation,effectively reducing the local maximum wear rate of the low-temperature economizer.3)Flow field optimization significantly decreased the relative standard deviation of the first column of the pseudo-pipe section on the left and right sides,with reductions from 0.322 to 0.201 on the left side and from 0.310 to 0.210 on the right side.4)The flow distribution deviation of the low-temperature economizer on the left and right sides was reduced from±2.03% to±1.23% ,showing an improvement.5)The system pressure drop decreased from 791 Pa before renovation to 603 Pa after renovation,indicating that reasonable deflector measures can reduce system resistance.Conclusion 1)The inlet flue gas velocity,velocity distribution uniformity,and dust concentration of low-temperature econo-mizer significantly affected its wear.Higher gas velocity increased dust concentration,and poorer velocity distribution unifor-mity led to more severe wear of a low-temperature economizer.2)Optimization and renovation of a low-temperature economizer in a coal-fired power plant were carried out.This involved replacing the shell and tube type low-temperature economizer with a vacuum heat pipe type,transforming the streamlined flue design and setting streamlined baffles to reduce eddies in the flue and enhance gas velocity.These modifications significantly improved the velocity distribution uniformity at the inlet section of the economizer,which was beneficial for reducing ash accumulation in the flue and lowering the system pressure drop.Compared to pre-renovation,the maximum wear rates of the low-temperature economizer decreased by 75.2% and 87.8% on the left and right sides,respectively,effectively reducing the risk of leakage.3)Performance test results showed that,after the renovation,the flue gas temperature at the outlet of the low-temperature economizer,the side pressure drop of the flue gas,and the particu-late matter concentration of dry flue gas in the standard state at the outlet of the dust collector all met the corresponding design requirements.

two-phase flowlow-temperature economizererosionnumerical simulation

叶兴联

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国家环境保护电力工业烟尘治理工程技术中心,福建龙岩 364000

福建龙净环保股份有限公司环境研究院,福建龙岩 364000

东北大学冶金学院,辽宁沈阳 110819

两相流 低温省煤器 磨损 数值模拟

国家自然科学基金项目福建省自然科学基金杰出青年项目

120720712020J06045

2024

中国粉体技术
中国颗粒学会,济南大学,中国非金属矿工业协会矿物加工利用专业委员会

中国粉体技术

CSTPCD
影响因子:0.469
ISSN:1008-5548
年,卷(期):2024.30(5)
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