Methanation of carbon dioxide over Ru/Mn/Ce-Al2O3 catalyst: In-depth of surface optimization, regeneration and reactor scale

Converting the CO2 gas via catalytic methanation technology has significant potential application in the power plant industry. Therefore, ceria based catalyst impregnated with Ru/Mn/Al2O3 was developed and from the experimental results, the optimum conditions over potential Ru/Mn/Ce (5:30:65)/Al2O3...

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Main Authors: Toemen, Susilawati, Jamal Mat Rosid, Salmiah, Wan Abu Bakar, Wan Azelee, Ali, Rusmidah, Sulaiman, Siti Fadziana, Hasan, Rahim
Format: Article
Published: Elsevier Ltd 2018
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Online Access:http://eprints.utm.my/id/eprint/84550/
http://dx.doi.org/10.1016/j.renene.2018.04.082
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spelling my.utm.845502020-02-27T03:05:20Z http://eprints.utm.my/id/eprint/84550/ Methanation of carbon dioxide over Ru/Mn/Ce-Al2O3 catalyst: In-depth of surface optimization, regeneration and reactor scale Toemen, Susilawati Jamal Mat Rosid, Salmiah Wan Abu Bakar, Wan Azelee Ali, Rusmidah Sulaiman, Siti Fadziana Hasan, Rahim QD Chemistry Converting the CO2 gas via catalytic methanation technology has significant potential application in the power plant industry. Therefore, ceria based catalyst impregnated with Ru/Mn/Al2O3 was developed and from the experimental results, the optimum conditions over potential Ru/Mn/Ce (5:30:65)/Al2O3 catalyst was achieved with 65 wt% of Ce based loading calcined at 1000 °C gave 97.73% of CO2 conversion with 91.31% of CH4 at 200 °C of reaction temperature. 10 g of the potential catalyst was pre-reduced at 300 °C for 30 min in the presence of H2 gas prior to the start of catalytic testing. The reliability, robustness, reproducibility and regeneration testing of this catalyst were further studied. The catalyst started to deactivate (spent catalyst) at sixth testing with only gave 41.17% CO2 conversion. However, the catalyst can be regenerated in the presence of compressed air at 400 °C for 3 h as it gave 92.85% of CO2 conversion. From the characterization of spent catalyst, the factor for the catalyst deactivation in this reaction was the particle agglomeration due to the loss of RuO2 and Mn2O3 species. When the catalyst was scale-up, the result showed that Ru/Mn/Ce (5:30:65)/Al2O3 catalyst able to convert 60% of CO2 and 50.4% of methane formation at lower reaction temperature of 160 °C. Elsevier Ltd 2018-11 Article PeerReviewed Toemen, Susilawati and Jamal Mat Rosid, Salmiah and Wan Abu Bakar, Wan Azelee and Ali, Rusmidah and Sulaiman, Siti Fadziana and Hasan, Rahim (2018) Methanation of carbon dioxide over Ru/Mn/Ce-Al2O3 catalyst: In-depth of surface optimization, regeneration and reactor scale. Renewable Energy, 127 . pp. 863-870. ISSN 0960-1481 http://dx.doi.org/10.1016/j.renene.2018.04.082
institution Universiti Teknologi Malaysia
building UTM Library
collection Institutional Repository
continent Asia
country Malaysia
content_provider Universiti Teknologi Malaysia
content_source UTM Institutional Repository
url_provider http://eprints.utm.my/
topic QD Chemistry
spellingShingle QD Chemistry
Toemen, Susilawati
Jamal Mat Rosid, Salmiah
Wan Abu Bakar, Wan Azelee
Ali, Rusmidah
Sulaiman, Siti Fadziana
Hasan, Rahim
Methanation of carbon dioxide over Ru/Mn/Ce-Al2O3 catalyst: In-depth of surface optimization, regeneration and reactor scale
description Converting the CO2 gas via catalytic methanation technology has significant potential application in the power plant industry. Therefore, ceria based catalyst impregnated with Ru/Mn/Al2O3 was developed and from the experimental results, the optimum conditions over potential Ru/Mn/Ce (5:30:65)/Al2O3 catalyst was achieved with 65 wt% of Ce based loading calcined at 1000 °C gave 97.73% of CO2 conversion with 91.31% of CH4 at 200 °C of reaction temperature. 10 g of the potential catalyst was pre-reduced at 300 °C for 30 min in the presence of H2 gas prior to the start of catalytic testing. The reliability, robustness, reproducibility and regeneration testing of this catalyst were further studied. The catalyst started to deactivate (spent catalyst) at sixth testing with only gave 41.17% CO2 conversion. However, the catalyst can be regenerated in the presence of compressed air at 400 °C for 3 h as it gave 92.85% of CO2 conversion. From the characterization of spent catalyst, the factor for the catalyst deactivation in this reaction was the particle agglomeration due to the loss of RuO2 and Mn2O3 species. When the catalyst was scale-up, the result showed that Ru/Mn/Ce (5:30:65)/Al2O3 catalyst able to convert 60% of CO2 and 50.4% of methane formation at lower reaction temperature of 160 °C.
format Article
author Toemen, Susilawati
Jamal Mat Rosid, Salmiah
Wan Abu Bakar, Wan Azelee
Ali, Rusmidah
Sulaiman, Siti Fadziana
Hasan, Rahim
author_facet Toemen, Susilawati
Jamal Mat Rosid, Salmiah
Wan Abu Bakar, Wan Azelee
Ali, Rusmidah
Sulaiman, Siti Fadziana
Hasan, Rahim
author_sort Toemen, Susilawati
title Methanation of carbon dioxide over Ru/Mn/Ce-Al2O3 catalyst: In-depth of surface optimization, regeneration and reactor scale
title_short Methanation of carbon dioxide over Ru/Mn/Ce-Al2O3 catalyst: In-depth of surface optimization, regeneration and reactor scale
title_full Methanation of carbon dioxide over Ru/Mn/Ce-Al2O3 catalyst: In-depth of surface optimization, regeneration and reactor scale
title_fullStr Methanation of carbon dioxide over Ru/Mn/Ce-Al2O3 catalyst: In-depth of surface optimization, regeneration and reactor scale
title_full_unstemmed Methanation of carbon dioxide over Ru/Mn/Ce-Al2O3 catalyst: In-depth of surface optimization, regeneration and reactor scale
title_sort methanation of carbon dioxide over ru/mn/ce-al2o3 catalyst: in-depth of surface optimization, regeneration and reactor scale
publisher Elsevier Ltd
publishDate 2018
url http://eprints.utm.my/id/eprint/84550/
http://dx.doi.org/10.1016/j.renene.2018.04.082
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