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Thermodynamic analysis of a new chemical looping process for syngas production with simultaneous CO_2 capture and utilization

机译:用于合成气生产并同时捕获和利用CO_2的新化学循环工艺的热力学分析

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摘要

Since typical CO2 capture technologies lack the consideration of a reliable CO2 storage method or integration with CO2 utilization, this study proposes a new chemical looping reforming process for syngas production with simultaneous CO2 capture and utilization. It integrates chemical looping, mixed reforming (i.e. CO2 reforming and partial oxidation) and calcium looping using CO2 carriers (CCs) and oxygen carriers (OCs). This novel process implements energy-efficient operation, attains flexible H-2/CO ratio, and captures CO2 with immediate CO2 conversion. Through thermodynamic screening, Fe- and Cu-based metal/metal oxides and CaO and MnO are identified as the potential OCs and CCs. For process characteristics, almost full CO2 capture is achieved, CH4 conversion rate is over 92.11%, maximum CO2 utilization rate is 99.18%, H-2/CO ratio is close to 2, and energy consumption is reduced by 40.74% and 68.62% compared to that of conventional mixed reforming and trireforming processes, respectively. Steam addition, low pressure and high temperature are benefit to enhance system performance. From experiment results, gas product distribution, solid reactivity and crystalline phases for solid demonstrate the feasibility of this novel process. More importantly, this process provides a new route to achieve integrated CO2 capture and conversion with the clean usages of carbonaceous energy sources.
机译:由于典型的二氧化碳捕集技术缺乏可靠的二氧化碳存储方法或与二氧化碳利用整合的考虑,因此本研究提出了一种新的化学循环重整工艺,用于合成气的生产,同时进行二氧化碳的捕集和利用。它集成了使用CO2载体(CC)和氧载体(OC)的化学循环,混合重整(即CO2重整和部分氧化)和钙循环。这种新颖的工艺实现了节能运行,可实现灵活的H-2 / CO比,并立即将CO2转化为二氧化碳。通过热力学筛选,将铁和铜基金属/金属氧化物以及CaO和MnO鉴定为潜在的OC和CC。就工艺特性而言,几乎可以完全捕获CO2,CH4转化率超过92.11%,最大CO2利用率为99.18%,H-2 / CO比率接近2,能耗分别降低了40.74%和68.62%与传统的混合重整和三重整工艺分别。蒸汽添加,低压和高温有利于增强系统性能。从实验结果来看,气体产物分布,固体反应性和固体结晶相证明了该新方法的可行性。更重要的是,该过程提供了一条新途径,可以利用碳质能源的清洁使用实现综合的CO2捕集和转化。

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