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This study demonstrates the feasibility of a once-through CO2 methanation process using a Ru/Al2O3 catalyst, achieving over 98% CO2 conversion and complete CH4 selectivity at atmospheric pressure. The process utilizes two isothermal tubular packed-bed reactors in series, allowing for the production of synthetic natural gas (SNG) that meets purity standards for direct grid injection without extensive purification. The catalyst shows stability over nearly 600 hours with no significant deactivation, highlighti

Author
sayansarkar1375
Language
EN