Ru/K2CO3–MgO catalytic sorbent for integrated CO2 capture and methanation at low temperatures
[Display omitted] •The existence of K2CO3 improved the Ru dispersion in Ru/KMg catal-sorbents.•CO2 capture and methanation temperatures were confirmed.•CO2 capture was conducted in the presence of 10 vol% CO2 and 10 vol% H2O.•The catal-sorbent exhibited a high CH4 yield in integrated CO2 capture and...
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Veröffentlicht in: | Chemical engineering journal (Lausanne, Switzerland : 1996) Switzerland : 1996), 2023-08, Vol.469, p.143772, Article 143772 |
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Sprache: | eng |
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•The existence of K2CO3 improved the Ru dispersion in Ru/KMg catal-sorbents.•CO2 capture and methanation temperatures were confirmed.•CO2 capture was conducted in the presence of 10 vol% CO2 and 10 vol% H2O.•The catal-sorbent exhibited a high CH4 yield in integrated CO2 capture and methanation.•Ru/KMg catal-sorbent exhibited stable CO2 capture capacity and CH4 productivity.
In this study, we have developed a Ru/K2CO3–MgO (Ru/KMg) catal-sorbent for integrated CO2 capture and methanation (ICCM) at low temperatures. The Ru primarily existed as a K2RuO3 phase, which was not observed after reduction at 400 °C. In addition, the crystallite size of Ru0 is smaller than that of Ru/MgO because Ru species as K2RuO3 phase, instead of RuO2, is dispersed well throughout the MgO support material. Here, the CO2 capture and regeneration properties of Ru/KMg catal-sorbents after carbonation at different temperatures (60, 120, 150, and 320 °C) were studied under N2 or H2 conditions, respectively. The optimal carbonation temperature was 150 °C when considering 100% CO2 conversion to CH4. 20 consecutive cycles of ICCM were conducted at 150 °C for carbonation (10 vol% CO2 and 10 vol% H2O) and 320 °C for methanation (90 vol% H2). The results showed stable CH4 productivities of 1.07–1.19 mmol CH4/g with 100% CH4 selectivity and 96.2%–101.3% CH4 yield. |
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ISSN: | 1385-8947 |
DOI: | 10.1016/j.cej.2023.143772 |