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Pilot Demonstration and Techno-Economic Analysis of Piperazine Solvent with High Temperature Two-Stage Flash for CO_2 Removal from Coal-Fired Flue Gas

机译:高温两级闪蒸脱除哌嗪溶剂从燃煤烟气中脱除CO_2的试验论证和技术经济性分析

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The University of Texas at Austin (UT-Austin) has developed a CO_2 removal technology for coal-fired flue gas based on absorption via concentrated piperazine solvent coupled with high-temperature, two-stage flash regeneration. The technology is being developed with funding from the US DOE National Energy Technology Laboratory's (NETL) Existing Plants Program. Concentrated piperazine offers advantages of faster kinetics, higher capacity, and lower volatility over other amine solvents. Its thermal stability enables regeneration at higher temperature and pressure, thereby lowering compression costs. This paper reports on the demonstration of this technology at 0.1-MW scale at UT-Austin's Separations Research Program(SRP) pilot plantand on results from a techno-economic analysis of the technology. The pilot demonstration evaluated the reliability of the two-stage flash design, the operating conditions required to achieve 90% CO_2 removal, and the energy performance of the technology. The techno-economic analysis estimated costs for installing and operating a full-scale system capable of achieving 90% CO_2 removal.
机译:得克萨斯大学奥斯汀分校(UT-Austin)开发了一种基于CO2的去除技术,该技术基于通过浓哌嗪溶剂的吸收以及高温,两阶段的闪蒸再生来吸收燃煤烟气。该技术是在美国能源部国家能源技术实验室(NETL)现有工厂计划的资助下开发的。与其他胺类溶剂相比,浓缩的哌嗪具有更快的动力学,更高的容量和更低的挥发性的优势。它的热稳定性可以在较高的温度和压力下进行再生,从而降低了压缩成本。本文报告了在UT-奥斯汀的分离研究计划(SRP)中试工厂以0.1兆瓦规模进行的这项技术的示范以及该技术的技术经济分析的结果。试点示范评估了两阶段闪蒸设计的可靠性,实现90%CO_2去除所需的运行条件以及该技术的能源性能。技术经济分析估算了安装和运行能够实现90%CO_2去除的全尺寸系统的成本。

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