Abstract

The flue gas desulfurization process in coal-fired power plants is energy and resource-intensive but the eco-efficiency of this process has scarcely been considered. Given the fluctuating unit load and complex desulfurization mechanism, optimizing the desulfurization system based on the traditional mechanistic model poses a great challenge. In this regard, the present study optimized the eco-efficiency from the perspective of operating data analysis. We formulated the issue of eco-efficiency improvement into a many-objective optimization problem. Considering the complexity between the system inputs and outputs and to further reduce the computational cost, we constructed a Kriging model and made a comparison between this model and the response surface methodology based on two accuracy metrics. This surrogate model was then incorporated into the NSGA-III algorithm to obtain the Pareto-optimal front. As this Pareto-optimal front provides multiple alternative operating options, we applied the TOPSIS to select the most appropriate alternative set of operating parameters. This approach was validated using the historical operation data from the desulfurization system at a coal-fired power plant in China with a 600 MW unit. The results indicated that the optimization would cause an improvement in the efficiency of desulfurization and energy efficiency but a slight increase in the consumption of limestone slurry. This study attempted to provide an effective operating strategy to enhance the eco-efficiency performance of desulfurization systems.

Highlights

  • The flue gas desulfurization process in coal-fired power plants is energy and resourceintensive but the eco-efficiency of this process has scarcely been considered

  • The results indicated that the optimal solution in the Pareto front was their relative closeness

  • This paper developed a mathematical model for a many-objective optimization of the operating parameters from the perspective of eco-efficiency

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Summary

Introduction

The flue gas desulfurization process in coal-fired power plants is energy and resourceintensive but the eco-efficiency of this process has scarcely been considered. Given the fluctuating unit load and complex desulfurization mechanism, optimizing the desulfurization system based on the traditional mechanistic model poses a great challenge In this regard, the present study optimized the eco-efficiency from the perspective of operating data analysis. Considering the complexity between the system inputs and outputs and to further reduce the computational cost, we constructed a Kriging model and made a comparison between this model and the response surface methodology based on two accuracy metrics This surrogate model was incorporated into the NSGA-III algorithm to obtain the Pareto-optimal front. As this Pareto-optimal front provides multiple alternative operating options, we applied the TOPSIS to select the most appropriate alternative set of operating parameters This approach was validated using the historical operation data from the desulfurization system at a coal-fired power plant in China with a 600 MW unit. The supercritical/ultra‐supercritical technology and clean coal technology have shown remarkable progress and contributed to significant emission reductions in coal‐

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