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Experimental Demonstration of a Novel Gas Switching Combustion Reactor for Power Production with Integrated CO2 Capture

机译:一种新型气体开关燃烧反应堆的实验证明,用于二氧化碳捕集二次发电

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摘要

This paper experimentally demonstrates the feasibility of a novel gas switching combustion (GSC) reactor as an alternative to the traditional chemical looping combustion (CLC) process for power production with integrated CO2 capture. Whereas the CLC process circulates an oxygen carrier material between two fluidized bed reactors, where it is exposed to separate fuel and air streams, the GSC concept employs a single dense fluidized bed reactor where the oxygen carrier is periodically exposed to fuel and air streams. A lab-scale GSC reactor was operated autothermally (without any external temperature supply) to continuously convert cold feed gases into hot product gases, which would be suitable for driving a downstream power cycle. A parametric study was carried out to further investigate the behavior of the GSC concept. The reactor achieved a high CO2 capture efficiency (97.2%) and purity (98.2%) even without the use of a purging stage between the oxidation and reduction stages. A small amount of carbon deposition (around 1%) had a slight negative effect on the CO2 capture efficiency. Finally, the operation of a cluster of GSC reactors capable of delivering two steady process streams to downstream process equipment is discussed.
机译:本文通过实验证明了新型气体转换燃烧(GSC)反应器可替代传统的化学循环燃烧(CLC)工艺用于集成CO2捕集发电的可行性。尽管CLC工艺在两个流化床反应器之间循环氧气载体材料,使氧气暴露于分开的燃料和空气流中,但GSC概念采用了单个致密流化床反应器,其中氧气载体周期性地暴露于燃料和空气流中。实验室规模的GSC反应器自动进行热操作(无需任何外部温度供应),以将冷进料气连续转化为热产物气,这将适合于驱动下游功率循环。进行了参数研究,以进一步调查GSC概念的行为。即使在氧化和还原阶段之间不使用吹扫阶段,反应器仍可实现很高的CO2捕集效率(97.2%)和纯度(98.2%)。少量的碳沉积(约1%)对CO2捕集效率有轻微的负面影响。最后,讨论了能够将两个稳定过程物流输送到下游过程设备的GSC反应器簇的操作。

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