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Evaluation of efficiency improvements and performance of coal-fired power plants with post-combustion CO2 capture

机译:通过燃烧后二氧化碳捕集来评估燃煤电厂的效率提高和性能

摘要

The power sector needs to be decarbonised by 2050 to meet the global targetfor greenhouse gas emission reduction and prevent climate change. With fossilfuels expected to play a vital role in the future energy portfolio and highefficiency penalties related to mature CO2 capture technologies, this researchaimed at evaluating the efficiency improvements and alternate operating modesof the coal-fired power plants (CFPP) retrofitted with post-combustion CO2capture. To meet this aim, process models of the CFPPs, chilled ammoniaprocess (CAP) and calcium looping (CaL) were developed in Aspen Plus® andbenchmarked against data available in the literature. Also, the process model ofchemical solvent scrubbing using monoethanolamine (MEA) was adapted fromprevious studies. Base-load analysis of the 580 MWel CFPP retrofits revealedthat if novel CAP retrofit configurations were employed, in which a new auxiliarysteam turbine was coupled with the boiler feedwater pump for extracted steampressure control, the net efficiency penalty was 8.7–8.8% points. This was closeto the 9.5% points in the MEA retrofit scenario. Conversely, CaL retrofit resultedin a net efficiency penalty of 6.7–7.9% points, depending on the fuel used inthe calciner. Importantly, when the optimised supercritical CO2 cycle was usedinstead of the steam cycle for heat recovery, this figure was reduced to 5.8%points. Considering part-load operation of the 660 MWel CFPP and uncertaintyin the process model inputs, the most probable net efficiency penalties ofthe CaL and MEA retrofits were 9.5% and 11.5% points, respectively.Importantly, in the CaL retrofit scenarios, the net power output was found to bearound 40% higher than that of the CFPP without CO2 capture and double thanthat for the MEA retrofit scenario. Such performance of the CaL retrofit scenarioled to higher profit than that of the 660 MWel CFPP without CO2 capture,especially if its inherent energy storage capability was utilised. Hence, this studyrevealed that CaL has the potential to significantly reduce the efficiency andeconomic penalties associated with mature CO2 capture technologies.
机译:电力行业需要在2050年前实现脱碳,以实现减少温室气体排放和防止气候变化的全球目标。由于预计化石燃料将在未来的能源组合中发挥至关重要的作用,并伴随着成熟的CO2捕集技术带来的高效率罚款,因此,本研究旨在评估经过燃烧后的CO2捕集改造的燃煤电厂(CFPP)的效率提高和替代运行模式。为了实现这一目标,在AspenPlus®中开发了CFPP,冷氨法(CAP)和钙环化(CaL)的工艺模型,并根据文献中的数据进行了基准测试。此外,从以前的研究中改编了使用单乙醇胺(MEA)进行化学溶剂洗涤的过程模型。 580 MWel CFPP改造的基本负荷分析表明,如果采用新颖的CAP改造配置,其中新的辅助蒸汽轮机与锅炉给水泵配合使用以控制抽汽压力,则净效率损失为8.7–8.8%点。在MEA改造方案中,这一比例接近9.5%。相反,CaL改造导致净效率损失为6.7–7.9%点,具体取决于煅烧炉中使用的燃料。重要的是,当使用优化的超临界CO2循环而不是蒸汽循环进行热回收时,该数字降低到5.8%。考虑到660 MWel CFPP的部分负荷运行以及过程模型输入中的不确定性,CaL和MEA改造的最可能净效率损失分别为9.5%和11.5%点。重要的是,在CaL改造方案中,净功率输出被发现比没有捕集二氧化碳的CFPP高出40%,比MEA改造方案高出一倍。相比不带CO2捕集的660 MWel CFPP,CaL改造的这种性能带来了更高的利润,特别是如果利用了其固有的储能能力。因此,这项研究表明,CaL有潜力显着降低与成熟的CO2捕集技术相关的效率和经济损失。

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    Hanak Dawid Piotr;

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  • 年度 2016
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