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基于NSGA-的脱硫浆液循环泵变频优化控制策略

Variable Frequency Optimization Control Strategy for Desulfurization Slurry Circulation Pumps Based on NSGA-

  • 摘要:
    目的 为应对燃煤机组脱硫系统在低负荷、高硫煤掺烧及环保约束趋严等复杂工况下面临的循环泵能耗高、脱硫剂消耗大及出口SO2浓度波动剧烈等挑战,文章提出一种脱硫浆液循环泵变频控制的多目标协同优化策略,旨在实现脱硫效率、运行成本与环保指标间的优化平衡。
    方法 提出了一种基于NSGA-Ⅱ的钙硫比与液气比协同控制方案。建立了以运行成本(泵组电耗、脱硫剂消耗)最小化、出口SO2浓度波动最小化及排污达标为核心目标的多目标优化模型,通过NSGA-Ⅱ的非支配排序与拥挤度机制,动态优化循环泵变频参数与石灰石浆液流量,生成帕累托最优解集,并基于工程数据验证算法参数。
    结果 工程应用表明:所提方法在升/降负荷及平稳工况下,可实现浆液循环泵出力与浆液消耗的均衡分配。投运后,5台浆液循环泵平均小时功率降低21.7%,年节约电费133.5万元;单位粉耗下降26.7%。
    结论 研究成果有效解决了脱硫系统多变量强耦合与动态工况适应性差的难题,显著降低了运行成本并提升了环保性能,可为燃煤电厂实现经济运行与超低排放的协同增效提供可借鉴的技术路径,对推动湿法烟气脱硫工艺的智能化升级具有重要的工程实践价值。

     

    Abstract:
    Objective To address the challenges in the desulfurization systems of coal-fired power units: such as high energy consumption of circulation pumps, excessive desulfurizing agent usage, and severe fluctuations in outlet SO2 concentration under complex operating conditions like low loads, high-sulfur coal co-firing, and tightening environmental constraints: this paper proposes a multi-objective cooperative optimization strategy for the variable frequency control of slurry circulation pumps. The strategy aims to achieve an optimal balance among desulfurization efficiency, operational costs, and environmental indicators.
    Method A calcium-to-sulfur (Ca/S) ratio and liquid-to-gas (L/G) ratio intelligent cooperative control scheme based on the NSGA-Ⅱ was proposed. A multi-objective optimization model was established to minimize operational costs (pump energy consumption and desulfurizing agent usage), reduce outlet SO2 concentration fluctuations, and ensure emission compliance. Leveraging NSGA-Ⅱ's non-dominated sorting and crowding distance mechanisms, the frequency conversion parameters of recirculation pumps and limestone slurry flow rates were dynamically optimized to generate a Pareto-optimal solution set. Algorithm parameters were validated using engineering data.
    Result Engineering applications demonstrate that the proposed method achieves balanced allocation of slurry circulation pump output and slurry consumption under load-increasing/decreasing and steady-state conditions. After implementation, the average hourly power consumption of five slurry circulation pumps was reduced by 21.7%, yielding annual electricity cost savings of 1.335 million CNY. The unit powder consumption decreased by 26.7%.
    Conclusion The research effectively addresses the challenges of strong multivariable coupling and poor adaptability to dynamic conditions in desulfurization systems, significantly reducing operational costs while enhancing environmental performance. It provides a valuable technical pathway for coal-fired power units to achieve synergistic optimization of economic operation and ultra-low emissions, holding significant engineering value for promoting the intelligent upgrading of the wet flue gas desulfurization process.

     

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