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Packed Bed Ca-Cu Looping Process Integrated with a Natural Gas Combined Cycle for Low Emission Power Production

机译:包装床CA-Cu环形过程与天然气组合循环集成,可用于低发射电力生产

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This work investigates the full process design of a natural gas combined cycle integrated with a packed-bed reactor system where a hydrogen rich gas is produced with inherent CO2 capture based of the CaO/CaCO3 and Cu/CuO chemical loops. The different stages of this Ca-Cu process were modelled with a dynamic 1D pseudo-homogeneous model, proposing a novel reactor configuration allowing to achieve carbon capture efficiency close to 90%. Process simulations of the whole power plant resulted in electric efficiencies of around 48%_(LHV) and SPECCA of 4.7 MJ/kg_(CO2).
机译:该工作调查了与填充床反应器系统一体化的天然气组合循环的完整过程设计,其中富含氢气的气体是基于CaO / CaCO3和Cu / Cuo化学回路的固有的CO2捕获。该CA-Cu工艺的不同阶段用动态1D伪均匀模型建模,提出了一种新的反应器配置,允许实现接近90%的碳捕获效率。整个发电厂的工艺模拟导致电效约为48%_(LHV)和4.7mJ / kg_(CO2)的SPECCA。

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