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集成供冷的燃煤电厂碳捕集、封存系统优化分析

Optimisation analysis of carbon capture and storage coupled with cooling in coal-fired power plants
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摘要 利用碳捕集、封存系统(CCS)减排燃煤电厂CO_(2)是碳中和必经之路,但目前较高的碳捕集、封存成本限制了该技术的发展和应用。针对某300 MW燃煤机组,利用Aspen Plus模拟软件提出并搭建了基于碱金属基干法碳捕集、封存耦合供冷系统,利用凝结水循环进行深度耦合,达到回收CO_(2)压缩封存过程中冷量的目的,有效降低碳捕集成本。在不耦合供冷过程的情况下,通过回收CO_(2)吸附过程释放的反应热,降低碳捕集系统单位耗电量至413.79 kWh/t(以CO_(2)计,下同);此时CO_(2)压缩封存过程能耗仍巨大。为此,在上述碳捕集封存系统进一步耦合供冷机组。通过模拟计算可得集成后新系统降低了CO_(2)压缩程度,此时加压封存过程的单位耗电量降至247.54 kWh/t,降低了2.3%,CO_(2)捕集封存总运行成本进一步降低33.77%。此外,供冷机组的引入还会降低额外投资成本,如通过提高CO_(2)吸附床内的换热温差,减少受热面布置量和吸附剂装载量,从而减少吸附床尺寸,优化效果明显。上述工作为CO_(2)捕集、封存技术推广和应用提供支撑,拓宽了CO_(2)的利用途径。 The use of carbon capture and storage(CCS)system to reduce CO_(2) in coal-fired power plants is one of the necessary paths to carbon neutrality,but the current high cost of CCS has limited the development and application of this technology.For a 300 MW coalfired unit,an alkali metal-based dry carbon capture and storage coupled cooling system was proposed and built using Aspen Plus simula⁃tion software,which used condensate circulation for deep coupling to achieve the purpose of recovering the cold volume in the CO_(2) com⁃pression and storage process and effectively reduce the carbon capture cost.Without coupling the cooling process,the unit power consump⁃tion of the carbon capture system is reduced to 413.79 kWh/t(in terms of CO_(2),the same below)by recovering the reaction heat released from the CO_(2) adsorption process.The energy consumption of the CO_(2) compression and storage process is still significant at this point.For this reason,the carbon capture and storage system described above was further coupled to a refrigeration unit.The simulation calculation shows that the new integrated system reduces the degree of CO_(2) compression and the unit power consumption of the compression storage process is reduced to 247.54 kWh/t,a reduction of 2.3%,resulting in a further 33.77%reduction in the total operating cost of CO_(2) cap⁃ture and storage.In addition,the introduction of cooling units can reduce additional investment cost reductions,such as reducing the amount of heated surface arrangement and adsorbent loading by increasing the heat transfer temperature difference within the CO_(2) adsorp⁃tion bed,and thus reducing the adsorption bed size with obvious optimization effects.Therefore,the above work provides an important sup⁃port for the promotion and application of CO_(2) capture and storage technology,and also broadens the way of CO_(2) utilization.
作者 陈扬 吴烨 刘兴 刘冬 CHEN Yang;WU Ye;LIU Xing;LIU Dong(School of Energy and Power Engineering,Nanjing University of Science and Technology,Nanjing 210094,China;Jiangsu Whale Energy Zero Carbon Technology Co.,Ltd.,Nanjing 210000,China)
出处 《洁净煤技术》 CAS CSCD 北大核心 2023年第4期109-120,共12页 Clean Coal Technology
基金 国家重点研发计划资助项目(2017YFB0603300) 江苏省碳达峰碳中和专项资助项目(BK20220001)。
关键词 燃煤电厂 碳捕集 碱金属基 CO_(2)制冷 Aspen Plus coal-fired power carbon capture alkali metal-based CO_(2)cooling Aspen Plus
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