Catalytic upgrading of sugarcane bagasse pyrolysis vapours over rare earth metal (Ce) loaded HZSM-5: Effect of catalyst to biomass ratio on the organic compounds in pyrolysis oil

The main objective of the current work is to investigate the influence of catalyst to biomass ratio (by weight%) on the catalytic upgrading of sugarcane bagasse derived pyrolysis vapours over cerium (Ce) loaded Hydrogen exchanged Zeolite Socony Mobil-5 (HZSM-5) catalyst via in-situ fixed bed reactor...

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Main Authors: Balasundram, Vekes, Norazana, Ibrahim, Rafiziana, Md. Kasmani, Ruzinah, Isha, Mohd. Kamaruddin, Abd. Hamid, Hasrinah, Hasbullah, Roshafima, Rasit Ali
Format: Article
Language:English
Published: Elsevier Ltd. 2018
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Online Access:http://umpir.ump.edu.my/id/eprint/22972/
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http://umpir.ump.edu.my/id/eprint/22972/1/Catalytic%20upgrading%20of%20sugarcane%20bagasse%20pyrolysis%20vapours%20over%20rare%20earth%20metal%20.pdf
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spelling ump-229722018-12-03T08:55:41Z http://umpir.ump.edu.my/id/eprint/22972/ Catalytic upgrading of sugarcane bagasse pyrolysis vapours over rare earth metal (Ce) loaded HZSM-5: Effect of catalyst to biomass ratio on the organic compounds in pyrolysis oil Balasundram, Vekes Norazana, Ibrahim Rafiziana, Md. Kasmani Ruzinah, Isha Mohd. Kamaruddin, Abd. Hamid Hasrinah, Hasbullah Roshafima, Rasit Ali TP Chemical technology The main objective of the current work is to investigate the influence of catalyst to biomass ratio (by weight%) on the catalytic upgrading of sugarcane bagasse derived pyrolysis vapours over cerium (Ce) loaded Hydrogen exchanged Zeolite Socony Mobil-5 (HZSM-5) catalyst via in-situ fixed bed reactor. The temperature of pyrolysis was kept at 500 °C for all investigated samples. The HZSM-5 catalyst was used as a support with 1 wt% of Ce as promoter loaded via incipient wetness impregnation method. The biomass sample was fixed at 2 g, while the catalyst mass loading was loaded according to the catalyst to biomass ratio which are 0.5:1.0, 1.0:1.0, 1.5:1.0, and 2.0:1.0. For comparison, the non-catalytic and biomass catalytic over HZSM-5 catalyst was also pyrolyzed at the same operating conditions. The results show that the yields of pyrolysis oil and coke were significantly influenced by the use of Ce/HZSM-5 catalyst at various catalyst to biomass ratio than the catalytic pyrolysis over HZSM-5, in which generate higher pyrolysis oil yield (58.0–68.0 wt%) and lower coke yield (2.9–4.1%). The increasing loading of mass in Ce/HZSM-5 catalyst has additional effect with respect to C6–C8 hydrocarbon contents in pyrolysis oil than the catalytic samples over the HZSM-5 catalyst. Among the tested catalyst to biomass ratio, the catalyst to biomass ratio of 1.5:1 has demonstrated to be the potential candidates in the catalytic upgrading of sugarcane bagasse derived oxygenated pyrolysis vapours into higher content of C6–C8 hydrocarbons (2.45%) in pyrolysis oil with lower coke yield (3.2%) over Ce/HZSM-5 catalyst. The bi-functional Ce/HZSM-5 catalyst was more effective in suppressing the coke formation in comparison to HZSM-5 catalyst at all investigated catalyst to biomass ratios and this was attributed to the synergistic effect of Ce on HZSM-5 support. Elsevier Ltd. 2018 Article PeerReviewed pdf en http://umpir.ump.edu.my/id/eprint/22972/1/Catalytic%20upgrading%20of%20sugarcane%20bagasse%20pyrolysis%20vapours%20over%20rare%20earth%20metal%20.pdf Balasundram, Vekes and Norazana, Ibrahim and Rafiziana, Md. Kasmani and Ruzinah, Isha and Mohd. Kamaruddin, Abd. Hamid and Hasrinah, Hasbullah and Roshafima, Rasit Ali (2018) Catalytic upgrading of sugarcane bagasse pyrolysis vapours over rare earth metal (Ce) loaded HZSM-5: Effect of catalyst to biomass ratio on the organic compounds in pyrolysis oil. Applied Energy, 220. pp. 787-799. ISSN 0306-2619 https://doi.org/10.1016/j.apenergy.2018.03.141 DOI: 10.1016/j.apenergy.2018.03.141
repository_type Digital Repository
institution_category Local University
institution Universiti Malaysia Pahang
building UMP Institutional Repository
collection Online Access
language English
topic TP Chemical technology
spellingShingle TP Chemical technology
Balasundram, Vekes
Norazana, Ibrahim
Rafiziana, Md. Kasmani
Ruzinah, Isha
Mohd. Kamaruddin, Abd. Hamid
Hasrinah, Hasbullah
Roshafima, Rasit Ali
Catalytic upgrading of sugarcane bagasse pyrolysis vapours over rare earth metal (Ce) loaded HZSM-5: Effect of catalyst to biomass ratio on the organic compounds in pyrolysis oil
description The main objective of the current work is to investigate the influence of catalyst to biomass ratio (by weight%) on the catalytic upgrading of sugarcane bagasse derived pyrolysis vapours over cerium (Ce) loaded Hydrogen exchanged Zeolite Socony Mobil-5 (HZSM-5) catalyst via in-situ fixed bed reactor. The temperature of pyrolysis was kept at 500 °C for all investigated samples. The HZSM-5 catalyst was used as a support with 1 wt% of Ce as promoter loaded via incipient wetness impregnation method. The biomass sample was fixed at 2 g, while the catalyst mass loading was loaded according to the catalyst to biomass ratio which are 0.5:1.0, 1.0:1.0, 1.5:1.0, and 2.0:1.0. For comparison, the non-catalytic and biomass catalytic over HZSM-5 catalyst was also pyrolyzed at the same operating conditions. The results show that the yields of pyrolysis oil and coke were significantly influenced by the use of Ce/HZSM-5 catalyst at various catalyst to biomass ratio than the catalytic pyrolysis over HZSM-5, in which generate higher pyrolysis oil yield (58.0–68.0 wt%) and lower coke yield (2.9–4.1%). The increasing loading of mass in Ce/HZSM-5 catalyst has additional effect with respect to C6–C8 hydrocarbon contents in pyrolysis oil than the catalytic samples over the HZSM-5 catalyst. Among the tested catalyst to biomass ratio, the catalyst to biomass ratio of 1.5:1 has demonstrated to be the potential candidates in the catalytic upgrading of sugarcane bagasse derived oxygenated pyrolysis vapours into higher content of C6–C8 hydrocarbons (2.45%) in pyrolysis oil with lower coke yield (3.2%) over Ce/HZSM-5 catalyst. The bi-functional Ce/HZSM-5 catalyst was more effective in suppressing the coke formation in comparison to HZSM-5 catalyst at all investigated catalyst to biomass ratios and this was attributed to the synergistic effect of Ce on HZSM-5 support.
format Article
author Balasundram, Vekes
Norazana, Ibrahim
Rafiziana, Md. Kasmani
Ruzinah, Isha
Mohd. Kamaruddin, Abd. Hamid
Hasrinah, Hasbullah
Roshafima, Rasit Ali
author_facet Balasundram, Vekes
Norazana, Ibrahim
Rafiziana, Md. Kasmani
Ruzinah, Isha
Mohd. Kamaruddin, Abd. Hamid
Hasrinah, Hasbullah
Roshafima, Rasit Ali
author_sort Balasundram, Vekes
title Catalytic upgrading of sugarcane bagasse pyrolysis vapours over rare earth metal (Ce) loaded HZSM-5: Effect of catalyst to biomass ratio on the organic compounds in pyrolysis oil
title_short Catalytic upgrading of sugarcane bagasse pyrolysis vapours over rare earth metal (Ce) loaded HZSM-5: Effect of catalyst to biomass ratio on the organic compounds in pyrolysis oil
title_full Catalytic upgrading of sugarcane bagasse pyrolysis vapours over rare earth metal (Ce) loaded HZSM-5: Effect of catalyst to biomass ratio on the organic compounds in pyrolysis oil
title_fullStr Catalytic upgrading of sugarcane bagasse pyrolysis vapours over rare earth metal (Ce) loaded HZSM-5: Effect of catalyst to biomass ratio on the organic compounds in pyrolysis oil
title_full_unstemmed Catalytic upgrading of sugarcane bagasse pyrolysis vapours over rare earth metal (Ce) loaded HZSM-5: Effect of catalyst to biomass ratio on the organic compounds in pyrolysis oil
title_sort catalytic upgrading of sugarcane bagasse pyrolysis vapours over rare earth metal (ce) loaded hzsm-5: effect of catalyst to biomass ratio on the organic compounds in pyrolysis oil
publisher Elsevier Ltd.
publishDate 2018
url http://umpir.ump.edu.my/id/eprint/22972/
http://umpir.ump.edu.my/id/eprint/22972/
http://umpir.ump.edu.my/id/eprint/22972/
http://umpir.ump.edu.my/id/eprint/22972/1/Catalytic%20upgrading%20of%20sugarcane%20bagasse%20pyrolysis%20vapours%20over%20rare%20earth%20metal%20.pdf
first_indexed 2023-09-18T22:34:13Z
last_indexed 2023-09-18T22:34:13Z
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