Experimental investigation of La0.6Sr0.4FeO3- pellets as oxygen carriers in a counter-current packed-bed reactor for efficient chemical looping CO2 splitting

The application of chemical looping for reverse water gas-shift provides an efficient way for the conversion of CO 2 to CO, enabling the transformation of captured CO 2 into value-added products. For example, by using the produced CO along with renewable H 2 to synthesise liquid fuels. In this study, we applied the concept of a chemical ‘memory’ reactor, employing a perovskite-based oxygen carrier (La 0.6 Sr 0.4 FeO 3- δ , LSF) in a counter-current packed-bed reactor for CO 2 splitting. This approach overcomes the chemical equilibrium limitation and could produce high purity CO. Our work experimentally investigated the performance of LSF pellets as oxygen carriers in a large lab-scale packed-bed reactor with gas switching technology for chemical looping CO 2 splitting. We evaluated the effects of changes in feed time, bed temperatures, and flow rates on CO 2 to CO conversion. Optimal conditions gave over 90 % CO 2 to CO conversion via counter-current flow, compared to 45 % for conventional co-current flow in the same reactor. Higher bed temperatures enhanced the CO 2 to CO conversion. • La 0.6 Sr 0.4 FeO 3- δ pellets were investigated in a reverse-flow chemical looping reactor for CO 2 splitting. • Nearly complete CO 2 to CO conversion can be achieved without thermodynamic limitations. • Effects of changing in bed temperature, feed time, and flow rates on CO 2 conversion have been evaluated. • La 0.6 Sr 0.4 FeO 3- δ pellets exhibits stable performance over CO 2 splitting tests.

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Publication Details

Journal
Journal of CO2 Utilization
Published
2024-09-21
DOI
https://doi.org/10.1016/j.jcou.2024.102935
Citations
13
Primary Topic
Chemical Looping and Thermochemical Processes
Type
article
Field-Weighted Citation Impact
2.40

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article

Experimental investigation of La0.6Sr0.4FeO3- pellets as oxygen carriers in a counter-current packed-bed reactor for efficient chemical looping CO2 splitting

Ian S. Metcalfe, Zuoan Li, Wenting Hu, Yongliang Yan et al.
13 citations
Journal of CO2 Utilization
Chemical Looping and Thermochemical Processes
2.40
article

Experimental investigation of La0.6Sr0.4FeO3- pellets as oxygen carriers in a counter-current packed-bed reactor for efficient chemical looping CO2 splitting

Ian S. Metcalfe, Zuoan Li, Wenting Hu, Yongliang Yan, Yngve Larring, Reinaldo Juan Lee Pereira, Matteo Fella
article en
13 citations

Abstract

The application of chemical looping for reverse water gas-shift provides an efficient way for the conversion of CO 2 to CO, enabling the transformation of captured CO 2 into value-added products. For example, by using the produced CO along with renewable H 2 to synthesise liquid fuels. In this study, we applied the concept of a chemical ‘memory’ reactor, employing a perovskite-based oxygen carrier (La 0.6 Sr 0.4 FeO 3- δ , LSF) in a counter-current packed-bed reactor for CO 2 splitting. This approach overcomes the chemical equilibrium limitation and could produce high purity CO. Our work experimentally investigated the performance of LSF pellets as oxygen carriers in a large lab-scale packed-bed reactor with gas switching technology for chemical looping CO 2 splitting. We evaluated the effects of changes in feed time, bed temperatures, and flow rates on CO 2 to CO conversion. Optimal conditions gave over 90 % CO 2 to CO conversion via counter-current flow, compared to 45 % for conventional co-current flow in the same reactor. Higher bed temperatures enhanced the CO 2 to CO conversion. • La 0.6 Sr 0.4 FeO 3- δ pellets were investigated in a reverse-flow chemical looping reactor for CO 2 splitting. • Nearly complete CO 2 to CO conversion can be achieved without thermodynamic limitations. • Effects of changing in bed temperature, feed time, and flow rates on CO 2 conversion have been evaluated. • La 0.6 Sr 0.4 FeO 3- δ pellets exhibits stable performance over CO 2 splitting tests.

Journal of CO2 UtilizationVol. 88
SINTEF (NO), Newcastle University (GB)
Royal Academy of Engineering, Newcastle University, Norges Forskningsråd
Openalex Percentile: Top 11%
Chemical Looping and Thermochemical Processes
2.40
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