{"title":"Turning CO2 into an alternative energy source: Study on methanation reaction optimization","authors":"Apisara Supaokit , Vikas Verma , Wei-Cheng Wang , Chia-Lin Chen , Shun-Min Wang , Rusdan Aditya Aji Nugroho , Viet Dung Duong , Hsin-Wei Hsu","doi":"10.1016/j.apcata.2024.120073","DOIUrl":null,"url":null,"abstract":"<div><div>Carbon dioxide (CO<sub>2</sub>) methanation is an effective technology for mitigating CO<sub>2</sub> emissions, major contributor to global warming, by converting CO<sub>2</sub> into methane (CH<sub>4</sub>). This work describes use of CO<sub>2</sub> (feedstock) using molecular hydrogen to produce CH<sub>4</sub> using mono-metallic Ni/γ-Al<sub>2</sub>O<sub>3</sub> catalyst in continuous flow fixed bed downflow reactor. The catalyst was characterized by XRD, SEM, BET, H<sub>2</sub>-TPD, H<sub>2</sub>-TPR, TPO, and Raman techniques. The influence of temperature, gas hourly space velocity (GHSV), pressure, H<sub>2</sub>/feed, nickel content and calcination temperature were studied. Optimal conditions using Taguchi method yielded maximum CH<sub>4</sub> selectivity (100 %) at T = 350 ºC, GHSV = 5000 mL g<sub>cat</sub><sup>−1</sup> h<sup>−1</sup><sub>,</sub> P = 15 bar, and H<sub>2</sub>/feed = 5. Under industrial reduced conditions (300 °C, 4000 mL g<sub>cat</sub><sup>−1</sup> h<sup>−1</sup>, 1 bar, and 4.5), CO<sub>2</sub> conversion improved from 73.67 % to 92.84 % using optimum 15 wt% Ni catalyst and 600 °C calcination temperature. The catalyst maintained ∼90 % CO<sub>2</sub> conversion over 100 h without deactivation.</div></div>","PeriodicalId":243,"journal":{"name":"Applied Catalysis A: General","volume":"691 ","pages":"Article 120073"},"PeriodicalIF":4.7000,"publicationDate":"2025-02-05","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Applied Catalysis A: General","FirstCategoryId":"1","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S0926860X24005180","RegionNum":2,"RegionCategory":"化学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q2","JCRName":"CHEMISTRY, PHYSICAL","Score":null,"Total":0}
引用次数: 0
Abstract
Carbon dioxide (CO2) methanation is an effective technology for mitigating CO2 emissions, major contributor to global warming, by converting CO2 into methane (CH4). This work describes use of CO2 (feedstock) using molecular hydrogen to produce CH4 using mono-metallic Ni/γ-Al2O3 catalyst in continuous flow fixed bed downflow reactor. The catalyst was characterized by XRD, SEM, BET, H2-TPD, H2-TPR, TPO, and Raman techniques. The influence of temperature, gas hourly space velocity (GHSV), pressure, H2/feed, nickel content and calcination temperature were studied. Optimal conditions using Taguchi method yielded maximum CH4 selectivity (100 %) at T = 350 ºC, GHSV = 5000 mL gcat−1 h−1, P = 15 bar, and H2/feed = 5. Under industrial reduced conditions (300 °C, 4000 mL gcat−1 h−1, 1 bar, and 4.5), CO2 conversion improved from 73.67 % to 92.84 % using optimum 15 wt% Ni catalyst and 600 °C calcination temperature. The catalyst maintained ∼90 % CO2 conversion over 100 h without deactivation.
期刊介绍:
Applied Catalysis A: General publishes original papers on all aspects of catalysis of basic and practical interest to chemical scientists in both industrial and academic fields, with an emphasis onnew understanding of catalysts and catalytic reactions, new catalytic materials, new techniques, and new processes, especially those that have potential practical implications.
Papers that report results of a thorough study or optimization of systems or processes that are well understood, widely studied, or minor variations of known ones are discouraged. Authors should include statements in a separate section "Justification for Publication" of how the manuscript fits the scope of the journal in the cover letter to the editors. Submissions without such justification will be rejected without review.