Preparation of a single metal catalyst loaded on alumina support to refine waste tire pyrolysis oil (WTPO) via catalytic hydrogenation

Improper disposal of industrial waste, particularly non-biodegradable solid waste like waste tires, has long been a significant environmental concern. Despite this, waste tires can be converted to fuel as alternative source through pyrolysis. However, waste tire pyrolysis oil (WTPO) has limitations,...

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Main Authors: Sinurat, S., Hafriz, R.S.R.M., Habib, S.H., Salmiaton, A., Izhar, S., Hamid, M.R.A., Sobri, S., Razali, N.M.
Format: Article
Published: Elsevier 2023
Online Access:http://psasir.upm.edu.my/id/eprint/110206/
https://linkinghub.elsevier.com/retrieve/pii/S0165237023003807
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Institution: Universiti Putra Malaysia
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spelling my.upm.eprints.1102062024-09-04T04:06:55Z http://psasir.upm.edu.my/id/eprint/110206/ Preparation of a single metal catalyst loaded on alumina support to refine waste tire pyrolysis oil (WTPO) via catalytic hydrogenation Sinurat, S. Hafriz, R.S.R.M. Habib, S.H. Salmiaton, A. Izhar, S. Hamid, M.R.A. Sobri, S. Razali, N.M. Improper disposal of industrial waste, particularly non-biodegradable solid waste like waste tires, has long been a significant environmental concern. Despite this, waste tires can be converted to fuel as alternative source through pyrolysis. However, waste tire pyrolysis oil (WTPO) has limitations, such as high sulfur content, making it unsuitable for direct use as a fuel. This research aims to improve the quality of waste tire pyrolysis oil (WTPO) by catalytic hydrogenation. Using modified metal catalysts, including nickel, cobalt, ammonium molybdenum, and alumina as supporting substances. The catalyst was synthesized using the impregnation method and subsequently subjected to calcination. The catalyst performance was evaluated by conducting the hydrogenation reaction. The catalytic hydrogenation reaction results indicate that the catalyst Mo/Al2O3 exhibited the best performance in producing refined oil. The refined oil was desulfurized to a sulfur compound of 0.7 wt at 320 ◦C under the flow rate of the gas of 100 ± 50 cm3/min, which corresponded to a sulfur reduction of 75 compared to the initial feedstock. Interestingly, while the non-catalytic reaction presented the highest performance towards sulfur removal of 80, it was inferior towards the selectivity of benzene, D-limone and p-cymene. Elsevier 2023 Article PeerReviewed Sinurat, S. and Hafriz, R.S.R.M. and Habib, S.H. and Salmiaton, A. and Izhar, S. and Hamid, M.R.A. and Sobri, S. and Razali, N.M. (2023) Preparation of a single metal catalyst loaded on alumina support to refine waste tire pyrolysis oil (WTPO) via catalytic hydrogenation. Journal of Analytical and Applied Pyrolysis, 176. art. no. 106236. pp. 1-15. ISSN 0165-2370; ESSN: 1873-250X https://linkinghub.elsevier.com/retrieve/pii/S0165237023003807 10.1016/j.jaap.2023.106236
institution Universiti Putra Malaysia
building UPM Library
collection Institutional Repository
continent Asia
country Malaysia
content_provider Universiti Putra Malaysia
content_source UPM Institutional Repository
url_provider http://psasir.upm.edu.my/
description Improper disposal of industrial waste, particularly non-biodegradable solid waste like waste tires, has long been a significant environmental concern. Despite this, waste tires can be converted to fuel as alternative source through pyrolysis. However, waste tire pyrolysis oil (WTPO) has limitations, such as high sulfur content, making it unsuitable for direct use as a fuel. This research aims to improve the quality of waste tire pyrolysis oil (WTPO) by catalytic hydrogenation. Using modified metal catalysts, including nickel, cobalt, ammonium molybdenum, and alumina as supporting substances. The catalyst was synthesized using the impregnation method and subsequently subjected to calcination. The catalyst performance was evaluated by conducting the hydrogenation reaction. The catalytic hydrogenation reaction results indicate that the catalyst Mo/Al2O3 exhibited the best performance in producing refined oil. The refined oil was desulfurized to a sulfur compound of 0.7 wt at 320 ◦C under the flow rate of the gas of 100 ± 50 cm3/min, which corresponded to a sulfur reduction of 75 compared to the initial feedstock. Interestingly, while the non-catalytic reaction presented the highest performance towards sulfur removal of 80, it was inferior towards the selectivity of benzene, D-limone and p-cymene.
format Article
author Sinurat, S.
Hafriz, R.S.R.M.
Habib, S.H.
Salmiaton, A.
Izhar, S.
Hamid, M.R.A.
Sobri, S.
Razali, N.M.
spellingShingle Sinurat, S.
Hafriz, R.S.R.M.
Habib, S.H.
Salmiaton, A.
Izhar, S.
Hamid, M.R.A.
Sobri, S.
Razali, N.M.
Preparation of a single metal catalyst loaded on alumina support to refine waste tire pyrolysis oil (WTPO) via catalytic hydrogenation
author_facet Sinurat, S.
Hafriz, R.S.R.M.
Habib, S.H.
Salmiaton, A.
Izhar, S.
Hamid, M.R.A.
Sobri, S.
Razali, N.M.
author_sort Sinurat, S.
title Preparation of a single metal catalyst loaded on alumina support to refine waste tire pyrolysis oil (WTPO) via catalytic hydrogenation
title_short Preparation of a single metal catalyst loaded on alumina support to refine waste tire pyrolysis oil (WTPO) via catalytic hydrogenation
title_full Preparation of a single metal catalyst loaded on alumina support to refine waste tire pyrolysis oil (WTPO) via catalytic hydrogenation
title_fullStr Preparation of a single metal catalyst loaded on alumina support to refine waste tire pyrolysis oil (WTPO) via catalytic hydrogenation
title_full_unstemmed Preparation of a single metal catalyst loaded on alumina support to refine waste tire pyrolysis oil (WTPO) via catalytic hydrogenation
title_sort preparation of a single metal catalyst loaded on alumina support to refine waste tire pyrolysis oil (wtpo) via catalytic hydrogenation
publisher Elsevier
publishDate 2023
url http://psasir.upm.edu.my/id/eprint/110206/
https://linkinghub.elsevier.com/retrieve/pii/S0165237023003807
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