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ANALYSIS OF THE THERMOCHEMICAL REDUCTION OF 3D-ORDERED MACROPOROUS CERIA-ZIRCONIA FOR FUEL PRODUCTION APPLICATIONS

机译:燃料生产应用的3D订购大孔二氧化氮氧化锆的热化学减少分析

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In terms of methods to sustainably convert solar energy into useful, transportable fuels, harnessing the sun's heat to make fuel— solar thermochemical fuel production—has great potential to be transformative. Unfortunately, the direct decomposition of the abundant feedstocks H2O and CO2 into either useful fuel, H, or a fuel precursor, CO + H, is not possible due to the extreme temperatures (>2500 °C) required for generation of an acceptable amount of product.This problem can be circumvented by splitting the decomposition into two steps via the use of a cerium oxide (CeO2) catalyst. In the first step, CeO2 is reduced at high temperatures (1100 to 1800 °C) in an inert gas, generating oxygen gas and CeO_(2-δ) (1). The second step is a lower temperature (~500 to 1000 °C) fuel production step, wherein H2O and/or CO2 gas is allowed to flow over Ce0.5. During this step, the CeO_(2-δ) strips oxygen from the H2O and/or CO, producing H2 (2) and/or CO (3). The CeO2 is regenerated for continued cycling. Improvements are needed to achieve efficiencies that will allow the CeO2 cycle to compete with other methods for synthesizing sustainable fuels.
机译:在可持续地将太阳能转化为有用的可运输燃料的方法方面,利用太阳的热量来使燃料 - 太阳能热化学燃料生产 - 具有巨大的变化潜力。遗憾的是,由于产生可接受量的最佳温度(> 2500℃),不可能将丰富的原料H 2 O和CO2直接分解为有用的燃料,H或燃料前体,CO + H是不可能的产品。通过使用氧化铈(CeO 2)催化剂将分解分解成两步,可以避免该问题。在第一步中,CEO2在惰性气体中在高温(1100至1800℃)下减少,产生氧气和CEO_(2-δ)(1)。第二步骤是较低温度(〜500至1000℃)燃料生产步骤,其中使得H 2 O和/或CO 2气体在Ce0.5上流动。在该步骤中,CEO_(2-Δ)从H 2 O和/或CO中带氧,产生H 2(2)和/或CO(3)。 CEO2被再生以继续循环。需要改进以实现将允许CEO2周期与其他方法合成可持续燃料的方法竞争。

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