Experimental investigation of La0.6Sr0.4FeO3 -δ pellets as oxygen carriers for chemical-looping applications

Lanthanum Strontium Ferrite (LSF), as an oxygen carrier, is used for chemical looping H 2 production and CO 2 utilization. In this work, the first attempt to upscale and understand the heat and mass transfer using 400 g of LSF pellets in a dynamically operated packed bed reactor is carried out. Experiments were conducted at 650–820 °C and 1–5 bar g , evaluating the pellets' reactor heat management, phase stability, and mechanical integrity over 70 h for the high-temperature redox cycling in chemical looping water-gas shift (CL-WGS) and chemical looping reverse water-gas shift (CL-RWGS) reactions. Key results at the reactor scale indicate a maximum cyclic average H 2 O-to-H 2 conversion of 31%, with a peak oxygen carrier capacity for CL-WGS of 0.38 mmol/g LSF . In the case of CL-RWGS, a peak CO 2 -to-CO conversion of 99.8% was achieved, with an oxygen carrier capacity of 0.57 mmol/g LSF . Reactor heat management for exothermic and endothermic redox reactions showed the ability to maintain a high temperature profile where the heat front lagged the reaction front over a 15 cm reactive bed length. A maximum ΔT of 45 °C and 35 °C were observed during the oxidation of the LSF bed with H 2 O and CO 2 , respectively. In the case of air oxidation, a maximum ΔT of 120 °C indicates that the reaction is more exothermic and can be used to raise the temperature of the bed especially if heat is required to sustain the process. No evidence of material performance degradation was recorded over 70 h of testing, maintaining the pellets' operational cyclability, phase stability, and mechanical integrity. The results demonstrate the robustness of the material, and they are encouraging versus the scalability of LSF for chemical looping applications, into H 2 production and CO 2 utilization processes. a) Ideal cubic ABO 3 perovskite framework (red, B-site; grey, A-site; blue, oxygen) b) Chemical looping water-gas shift cycling gas outlet. • 400 g of LSF tested for WGS and RWGS chemical looping. • Testing campaign in packed bed up to 820 °C and 5 bar. • High LSF stability over 70 h and 35 redox cycles. • Peak CO 2 -to-CO conversion of 51% and H 2 O-to-H 2 conversion of 31%. • Optimum oxygen transfer capacity of 0.95 ± 0.04 mmol O /g LSF at 750 °C.

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Publication Details

Journal
International Journal of Hydrogen Energy
Published
2024-11-13
DOI
https://doi.org/10.1016/j.ijhydene.2024.10.404
Citations
7
Primary Topic
Chemical Looping and Thermochemical Processes
Type
article
Field-Weighted Citation Impact
1.29

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article

Experimental investigation of La0.6Sr0.4FeO3 -δ pellets as oxygen carriers for chemical-looping applications

Christopher de Leeuwe, Ian S. Metcalfe, Wenting Hu, Yongliang Yan et al.
7 citations
International Journal of Hydrogen Energy
Chemical Looping and Thermochemical Processes
1.29
article

Experimental investigation of La0.6Sr0.4FeO3 -δ pellets as oxygen carriers for chemical-looping applications

Christopher de Leeuwe, Ian S. Metcalfe, Wenting Hu, Yongliang Yan, Vincenzo Spallina, Adam Zaidi, Matteo Fella
article en
7 citations

Abstract

Lanthanum Strontium Ferrite (LSF), as an oxygen carrier, is used for chemical looping H 2 production and CO 2 utilization. In this work, the first attempt to upscale and understand the heat and mass transfer using 400 g of LSF pellets in a dynamically operated packed bed reactor is carried out. Experiments were conducted at 650–820 °C and 1–5 bar g , evaluating the pellets' reactor heat management, phase stability, and mechanical integrity over 70 h for the high-temperature redox cycling in chemical looping water-gas shift (CL-WGS) and chemical looping reverse water-gas shift (CL-RWGS) reactions. Key results at the reactor scale indicate a maximum cyclic average H 2 O-to-H 2 conversion of 31%, with a peak oxygen carrier capacity for CL-WGS of 0.38 mmol/g LSF . In the case of CL-RWGS, a peak CO 2 -to-CO conversion of 99.8% was achieved, with an oxygen carrier capacity of 0.57 mmol/g LSF . Reactor heat management for exothermic and endothermic redox reactions showed the ability to maintain a high temperature profile where the heat front lagged the reaction front over a 15 cm reactive bed length. A maximum ΔT of 45 °C and 35 °C were observed during the oxidation of the LSF bed with H 2 O and CO 2 , respectively. In the case of air oxidation, a maximum ΔT of 120 °C indicates that the reaction is more exothermic and can be used to raise the temperature of the bed especially if heat is required to sustain the process. No evidence of material performance degradation was recorded over 70 h of testing, maintaining the pellets' operational cyclability, phase stability, and mechanical integrity. The results demonstrate the robustness of the material, and they are encouraging versus the scalability of LSF for chemical looping applications, into H 2 production and CO 2 utilization processes. a) Ideal cubic ABO 3 perovskite framework (red, B-site; grey, A-site; blue, oxygen) b) Chemical looping water-gas shift cycling gas outlet. • 400 g of LSF tested for WGS and RWGS chemical looping. • Testing campaign in packed bed up to 820 °C and 5 bar. • High LSF stability over 70 h and 35 redox cycles. • Peak CO 2 -to-CO conversion of 51% and H 2 O-to-H 2 conversion of 31%. • Optimum oxygen transfer capacity of 0.95 ± 0.04 mmol O /g LSF at 750 °C.

International Journal of Hydrogen EnergyVol. 94
University of Manchester (GB), Newcastle University (GB)
Royal Academy of Engineering, Newcastle University, Horizon 2020 Framework Programme, Engineering and Physical Sciences Research Council, Horizon 2020
Openalex Percentile: Top 21%
Chemical Looping and Thermochemical Processes
1.29
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