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首页> 外文期刊>Chemical engineering journal >Optimization of the design, operating conditions, and coupling configuration of combined cycle power plants and CO2 capture processes by minimizing the mitigation cost
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Optimization of the design, operating conditions, and coupling configuration of combined cycle power plants and CO2 capture processes by minimizing the mitigation cost

机译:通过最小化缓解成本,优化组合循环发电厂和CO2捕获过程的设计,操作条件和耦合配置

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摘要

This paper deals with the optimization of the coupling between a natural gas combined cycle (NGCC) plant and a post-combustion CO2 capture process by minimizing the mitigation cost - defined as the ratio between the cost of electric power generation and the amount of CO2 emitted per unit of total net electric power generated - while satisfying the design specifications: electric power generation capacity and CO2 capture level. Three candidate coupling configurations, which differ in the place where the steam is extracted from, are optimized using detailed and rigorous models for both the NGCC and the CO2 capture plants. By comparing the mitigation cost of each configuration, the optimal integration configuration and the corresponding optimal sizes and operating conditions of all process units (steam turbines, gas turbines, heat recovery steam generators HRSGs, absorption and regeneration columns, reboilers and condensers, and pumps) are provided. In the computed optimal solution, the steam required by the CO2 capture plant is extracted from both the steam turbine and the HRSG (evaporator operating at low pressure), and the mitigation cost is 90.88 (sic)/t CO2. The optimal solution is compared with suboptimal solutions corresponding to the other two candidate coupling schemes. These solutions are compared in detail regarding capital investment and operating costs, HRSG configuration, process unit sizes, and operating conditions.
机译:本文通过使减缓成本最小化定义为发电成本与发出的二氧化碳量的减缓成本,优化了天然气联合循环(NGCC)植物和后燃烧二氧化碳捕获过程的耦合。每个单位的总净电力产生 - 同时满足设计规格:发电能力和二氧化碳捕获水平。三种候选耦合配置,其在从蒸汽中提取的地方不同,使用NGCC和CO2捕获植物的详细和严格的模型进行优化。通过比较每个配置的缓解成本,最佳集成配置和所有工艺单元的相应最佳尺寸和操作条件(蒸汽轮机,燃气轮机,热回收蒸汽发生器HRSG,吸收和再生柱,再沸器和冷凝器以及泵)提供。在计算的最佳解决方案中,CO 2捕获工厂所需的蒸汽从蒸汽轮机和HRSG中提取(蒸发器在低压下操作),缓解成本为90.88(SiC)/ T CO 2。将最佳解决方案与对应于其他两个候选耦合方案的次优溶液进行比较。这些解决方案详细介绍了资本投资和运营成本,HRSG配置,工艺单元尺寸和操作条件。

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