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Molten Carbonate Fuel Cells for Retrofitting Postcombustion CO2 Capture in Coal and Natural Gas Power Plants

机译:用于改造煤炭和天然气发电厂的后Combustion CO2捕获的熔融碳酸盐燃料电池

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The state-of-the-art conventional technology for postcombustion capture of CO2 from fossil-fueled power plants is based on chemical solvents, which requires substantial energy consumption for regeneration. A promising alternative, available in the near future, is the application of molten carbonate fuel cells (MCFC) for CO2 separation from postcombustion flue gases. Previous studies related to this technology showed both high efficiency and high carbon capture rates, especially when the fuel cell is thermally integrated in the flue gas path of a natural gas-fired combined cycle or an integrated gasification combined cycle plant. This work compares the application of MCFC-based CO2 separation process to pulverized coal fired steam cycles (PCC) and natural gas combined cycles (NGCC) as a "retrofit" to the original power plant. Mass and energy balances are calculated through detailed models for both power plants, with fuel cell behavior simulated using a 0D model calibrated against manufacturers' specifications and based on experimental measurements, specifically carried out to support this study. The resulting analysis includes a comparison of the energy efficiency and CO2 separation efficiency as well as an economic comparison of the cost of CO2 avoided (CCA) under several economic scenarios. The proposed configurations reveal promising performance, exhibiting very competitive efficiency and economic metrics in comparison with conventional CO2 capture technologies. Application as a MCFC retrofit yields a very limited ( 3%) decrease in efficiency for both power plants (PCC and NGCC), a strong reduction ( 80%) in CO2 emission and a competitive cost for CO2 avoided (25-40 (sic)/ton).
机译:来自化石燃料发电厂的CO2的后期COMBUSTION捕获的最先进的常规技术基于化学溶剂,这需要进行大量的再生能耗。在不久的将来可提供有前途的替代方案,是熔融碳酸盐燃料电池(MCFC)的应用,用于从后传染烟道气体分离。与该技术有关的先前研究表明,高效率和高碳捕获速率,特别是当燃料电池在天然气燃烧的组合循环或集成气化联合循环厂的烟气路径中热集成。该工作比较了基于MCFC的二氧化碳分离过程的应用,将煤燃煤蒸汽循环(PCC)和天然气组合循环(NGCC)作为原始电厂的“改装”。质量和能量余额是通过用于两种发电厂的详细模型来计算的,使用校准制造商规格的0D模型模拟燃料电池行为,并基于实验测量,具体进行,以支持这项研究。得到的分析包括比较能效和CO2分离效率的比较,以及在几种经济场景下避免(CCA)的二氧化碳成本的经济比较。拟议的配置揭示了有希望的性能,与传统二氧化碳捕获技术相比,表现出非常竞争的效率和经济指标。作为MCFC改造的应用产生非常有限(<3%)发电厂(PCC和NGCC)的效率降低,CO 2排放中强烈的减少(& 80%),避免了二氧​​化碳的竞争成本(25- 40(SiC)/吨)。

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