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Terbium oxide-based solar thermochemical CO(2)splitting cycle: A thermodynamic investigation

机译:基于氧化铽的太阳能热化学CO(2)分裂周期:热力学调查

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A Tb(2)O3/TbO(2)thermochemical CO(2)splitting cycle was thermodynamically scrutinized in this study. Equilibrium and efficiency analysis are the two major sections of this thermodynamic investigation. As a first step of the thermodynamic analysis, the temperatures required for the thermal reduction (TR) of Tb(2)O(3)and the re-oxidation of the TbO(2)via CO(2)splitting (CS) reaction were identified. The equilibrium analysis indicates that the temperature in the range of 2234-2530 K was required for the increase in the percentage TR of Tb(2)O(3)from 5% to 100%. The efficiency analysis was conducted by following a process flow arrangement, which includes a solar reactor, a CS reactor, a CO(2)heater, multiple coolers, and a fuel cell. The obtained results indicate that the eta solar-to-fuel-Tb-CSincreased from 3.4% to 5.6% when the %TR-Tb upsurged from 5% to 25%. A further rise in the %TR-Tb from 25% to 100%, however, resulted in a decrease in the eta solar-to-fuel-Tb-CSfrom 5.6% to 3.5%. By employing 100% heat recuperation, the maximum eta solar-to-fuel-HR-Tb-CS= 9.6% attained at a %TR-Tb equal to 20% (TH= 2296 K). (c) 2020 Society of Chemical Industry and John Wiley & Sons, Ltd.
机译:TB(2)O 3 / TBO(2)热敏CO(2)分裂循环在本研究中热力学审查。均衡和效率分析是这种热力学调查的两个主要部分。作为热力学分析的第一步,Tb(2)O(3)的热还原(Tr)所需的温度和通过CO(2)分裂(CS)反应的TBO(2)的再氧化确定。平衡分析表明,Tb(2)O(3)的百分比Tr增加到2234-2530k范围内的温度为5%至100%。通过以下过程流动装置进行效率分析,该过程流动装置包括太阳能反应器,CS反应器,CO(2)加热器,多个冷却器和燃料电池。所得结果表明,当达到5%至25%的%Tr-TB时,ETA的ETA太阳能 - 燃料-TB-CSIN增加到3.4%至5.6%。然而,从25%至100%的%TR-TB进一步升高导致ETA太阳能 - 燃料 - TB-CSFRom降低5.6%至3.5%。通过采用100%热回收率,最大ETA太阳能 - 燃料-HR-TB-CS = 9.6%以等于20%(Th = 2296 k)的%Tr-Tb。 (c)2020化学工业协会和约翰瓦利和儿子有限公司

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