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• W3013956557 abstract "Abstract 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 increased 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 from 5.6% to 3.5%. By employing 100% heat recuperation, the maximum = 9.6% attained at a %TR‐Tb equal to 20% ( = 2296 K). © 2020 Society of Chemical Industry and John Wiley & Sons, Ltd." @default.
• W3013956557 created "2020-04-03" @default.
• W3013956557 creator A5027288897 @default.
• W3013956557 date "2020-03-23" @default.
• W3013956557 modified "2023-09-25" @default.
• W3013956557 title "Terbium oxide‐based solar thermochemical CO ₂ splitting cycle: A thermodynamic investigation" @default.
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• W3013956557 doi "https://doi.org/10.1002/ghg.1972" @default.
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