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Economic assessment of novel amine based CO2 capture technologies integrated in power plants based on European Benchmarking Task Force methodology

机译:基于欧洲基准工作组方法的电厂中基于胺的新型二氧化碳捕集技术的经济评估

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The objective of this paper is to assess the economic advantages of an innovative solvent for CO2 capture on state-of-the-art solvents. The CESAR-1 solvent, which is an aqueous solution of 2-amino-2-methylpropanol (AMP) and piperazine (PZ), is applied both to advanced supercritical pulverised (ASC) coal and natural gas combined cycle (NGCC) power plants with post-combustion CO2 capture units. The methodology includes process model developments using commercial simulation programs, which determine the thermodynamic properties of the selected power plants and the performance of the CO2 capture units. The results show that the techno-economic benefit of CESAR-1 versus MEA is more significant for ASC than that for NGCC due to a higher concentration of CO2 in the flue gas. This follows from the fact that the switch from MEA to CESAR-1 solvents reduces the electricity cost by 4.16 (sic)/MW h in the case of the ASC plant compared to 0.67 (sic)/MW h in connection with the proposed NGCC plant. Based on the above figures, we can conclude that CESAR-1 reduces the cost of CO2 avoided compared to MEA by 6 (sic)/t CO2 and 2 (sic)/t CO2 for the selected ASC and NGCC plants respectively. In view of that, the techno-economics can be improved if the CO2 capture plant is designed to operate using the CESAR-1 absorption technology due to a reduction in the regeneration energy and the solvent recirculation rate (considering its higher CO2 net capacity). However, the variable costs of running the capture plant are higher for the CESAR-1 solvent due to the higher cost of the amines. (C) 2014 Published by Elsevier Ltd.
机译:本文的目的是评估使用最先进的溶剂捕获二氧化碳的创新溶剂的经济优势。 CESAR-1溶剂是2-氨基-2-甲基丙醇(AMP)和哌嗪(PZ)的水溶液,适用于高级超临界粉煤(ASC)和天然气联合循环(NGCC)电厂,燃烧后二氧化碳捕集单元。该方法包括使用商业仿真程序开发过程模型,这些程序确定所选电厂的热力学性质和CO2捕集单元的性能。结果表明,由于烟气中的CO2浓度较高,CESAR-1与MEA相比,ASC的技术经济优势要比NGCC的技术经济优势更大。这是由于以下事实:在ASC电厂中,从MEA转换为CESAR-1溶剂可将电力成本降低4.16(sic)/ MW h,而与拟建NGCC电厂有关的电费成本仅为0.67(sic)/ MW h 。根据以上数据,我们可以得出结论,对于选定的ASC和NGCC工厂而言,与MEA相比,CESAR-1可将避免的CO2成本降低6(sic)/ t CO2和2(sic)/ t CO2。有鉴于此,如果将CO2捕集装置设计为使用CESAR-1吸收技术运行,则由于可再生能量和溶剂再循环率的降低(考虑到其更高的CO2净容量),可以提高技术经济性。但是,由于胺的成本较高,因此对于CESAR-1溶剂,运行捕集装置的可变成本较高。 (C)2014由Elsevier Ltd.出版

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