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Optimization of MEA based post combustion CO_2 capture process: Flowsheeting and energetic integration

机译:基于MEA的优化优化CO_2捕获过程:流量和精力充沛的集成

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The main limitation of post-combustion CO_2 capture technology is the high energy consumption leading to a power output loss of approximately 25% when coupled with CO_2 compression. Studies to break this limitation follow two main paths: formulation of new solvents and optimization of the process flowsheet. The purpose of this works is to assess the impact of the different flowsheet modifications and power plant integration on the plant performance. CO_2 capture amine plant has been integrated in a gross electrical 1200 MWe supercritical coal-fired power plant; a process optimization study coupled with economical and availability analysis has been performed for each studied case and compared to a reference case: standard amine capture process with 30%wt MEA. The capture plant increases the cost of a new power plant by approximately 70% and the electricity price by 45%. Process flowsheet optimization on the amine capture plant do no significantly increase the specific power plant cost (from 0 to 2%) with CO_2 capture, the additional expenditure are compensated with the plant efficiency gains. The cost of electricity is, also, almost not affected by the flowsheet optimization (from -2.5 to +1.5 %). The best tested configuration allows a reduction of 10% of the cost of avoided CO_2. The addition of a capture plant increases by approximately 1.4%pt the risk of forced outage factor and therefore decreases the whole power plant availability by the same value. The effects of the availability decreases due to the capture plant on CO_2 and electricity prices are negligible. This work shows that these modifications alone are not sufficient to enable an economically feasible carbon capture on coal fired power plant despites a loss of efficiency of approximately 10%pt. The goal of less than 5% pt efficiency losses induced by post combustion carbon capture need a combination of new solvent and optimized process or a totally new breakthrough process.
机译:燃烧后CO_2捕获技术的主要限制是高能耗,导致电源输出损耗约为25%,当加上CO_2压缩时。打破这一限制的研究遵循两个主要路径:制定新的溶剂和过程流程的优化。这项工作的目的是评估不同流程修改和电厂集成对植物性能的影响。 CO_2捕获胺工厂已集成在一家电气1200 MWE超临界燃煤电厂;已经对每个研究的情况进行了与经济性和可用性分析相结合的过程优化研究,并与参考案例进行比较:标准胺捕获过程,具有30%WT MEA。捕获工厂将新电厂的成本提高了大约70%,电价达到45%。工艺流程捕获工厂对胺捕获工厂的优化无明显增加了CO_2捕获的特定发电厂成本(从0到2%),通过工厂效率提升补偿了额外的支出。电力成本也几乎不受流曲优化的影响(从-2.5到+1.5%)。最佳测试配置允许减少避免CO_2成本的10%。捕获工厂的添加增加了大约1.4%PT强制中断因素的风险,因此通过相同的价值降低了整个电厂可用性。由于CO_2的捕获工厂,可用性的影响降低,电价可忽略不计。这项工作表明,尽管损失约10%Pt的效率,但单独的这些修改不能足以使燃煤发电厂的经济上可行的碳捕获。燃烧碳捕获后诱导的PT效率损失不到5%的目的需要新的溶剂和优化过程或完全新的突破过程。

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