Calcium-LoopingDry Reforming Enhances Biogas Conversionto Syngas with Simultaneous CO<sub>2</sub> Abatement

Conversion of biogas into syngas expands its application scope from fuel for power generation to industrial feedstock for the synthesis of value-added chemicals; however, it is restricted to the limited CH<sub>4</sub> conversion due to the mismatch between CH<sub>4</sub>/CO<sub>2</sub> feeding ratios of biogas and the stoichiometry of the CH<sub>4</sub> dry reforming reaction. Herein, we proposed a novel calcium-looping biogas dry reforming process (CaL-BR) to supplement exogenous CO<sub>2</sub> into biogas in situ by the introduction of a CaO-based carbon-carrying cycle. Using the facilely prepared composite material CaO–Ni/Al<sub>2</sub>O<sub>3</sub>_1 for CaL-BR at 750 °C, the CH<sub>4</sub> conversion was over 65% and 16.4% higher than that of conventional biogas reforming, enabling the syngas yield to reach as high as 136.7 mmol/g. Importantly, the proposed process exhibited superior cyclic stability with a decay in the biogas reforming performance below 3% over 20 CaL-BR cycles under typical biogas CH<sub>4</sub>/CO<sub>2</sub> feeding ratios, which was confirmed to be a consequence of the suppressed sintering of Ni particles and carbon deposition. The proposed CaL-BR process offered a promising option to make the best of the CH<sub>4</sub> resource in biogas with the simultaneous capture and conversion of CO<sub>2</sub>.

Publication Details

Journal
Figshare
Published
2025-03-04
DOI
https://doi.org/10.1021/acssuschemeng.4c09143.s001
Primary Topic
Chemical Looping and Thermochemical Processes
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article
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Calcium-LoopingDry Reforming Enhances Biogas Conversionto Syngas with Simultaneous CO2 Abatement

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Chemical Looping and Thermochemical Processes
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Calcium-LoopingDry Reforming Enhances Biogas Conversionto Syngas with Simultaneous CO2 Abatement

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Abstract

Conversion of biogas into syngas expands its application scope from fuel for power generation to industrial feedstock for the synthesis of value-added chemicals; however, it is restricted to the limited CH<sub>4</sub> conversion due to the mismatch between CH<sub>4</sub>/CO<sub>2</sub> feeding ratios of biogas and the stoichiometry of the CH<sub>4</sub> dry reforming reaction. Herein, we proposed a novel calcium-looping biogas dry reforming process (CaL-BR) to supplement exogenous CO<sub>2</sub> into biogas in situ by the introduction of a CaO-based carbon-carrying cycle. Using the facilely prepared composite material CaO–Ni/Al<sub>2</sub>O<sub>3</sub>_1 for CaL-BR at 750 °C, the CH<sub>4</sub> conversion was over 65% and 16.4% higher than that of conventional biogas reforming, enabling the syngas yield to reach as high as 136.7 mmol/g. Importantly, the proposed process exhibited superior cyclic stability with a decay in the biogas reforming performance below 3% over 20 CaL-BR cycles under typical biogas CH<sub>4</sub>/CO<sub>2</sub> feeding ratios, which was confirmed to be a consequence of the suppressed sintering of Ni particles and carbon deposition. The proposed CaL-BR process offered a promising option to make the best of the CH<sub>4</sub> resource in biogas with the simultaneous capture and conversion of CO<sub>2</sub>.

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Chemical Looping and Thermochemical Processes
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