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Optimal design of combined cycle power plants with fixed-bed chemical-looping combustion reactors

机译:固定床化学循环燃烧反应器组合循环发电厂的最优设计

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Process intensification options are explored for near-carbon-neutral, natural-gas-fueled combined cycle (CC) power plants, wherein the conventional combustor is replaced by a series of chemical-looping combustion (CLC) reactors. Dynamic modeling and optimization are deployed to design CLC-CC power plants with optimal configuration and performance. The overall plant efficiency is improved by optimizing the CLC reactor design and operation, and modifying the CC plant configuration and design. The optimal CLC-CC power plant has a time-averaged efficiency of 52.52% and CO2 capture efficiency of 96%. The main factor that limits CLC-CC power plant efficiency is the reactor temperature, which is constrained by the oxygen carrier material. CLC exhaust gas temperature during heat removal and gas compressor to gas turbine pressure ratio are the most important operating variables and if properly tuned, CLC-CC power plants can reach high thermodynamic efficiencies. (c) 2018 American Institute of Chemical Engineers AIChE J, 65: e16516 2019
机译:用于近碳中性,天然气加油的组合循环(CC)发电厂探索了工艺强化选项,其中传统的燃烧器被一系列化学环燃烧(CLC)反应器代替。部署动态建模和优化以设计具有最佳配置和性能的CLC-CC发电厂。通过优化CLC反应堆设计和操作来改善整体植物效率,并改变CC工厂配置和设计。最佳CLC-CC发电厂的时间平均效率为52.52%,二氧化碳捕获效率为96%。限制CLC-CC发电厂效率的主要因素是由氧载体材料约束的反应器温度。加热器在散热过程中的废气温度和气体压缩机到燃气轮机压力比是最重要的操作变量,如果适当调整,CLC-CC发电厂可以达到高热力学效率。 (c)2018美国化学工程师研究所Aiche J,65:E16516 2019

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