Catalytic activity and coke resistance of gasification slag-supported Ni catalysts during steam reforming of plastic pyrolysis gas

Pyrolysis gas from polyolefinic plastic waste is a hydrocarbon-rich feedstock for sustainable syngas production. The effect of Cr, Mo, and W promoters on the activity of gasification slag-supported Ni catalysts during the reforming of plastic pyrolysis gas was investigated (polyethylene and polyprop...

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Main Authors: Ong, Hang Meng, Veksha, Andrei, Ha, Quan Luu Manh, Huang, Jijiang, Tsakadze, Zviad, Lisak, Grzegorz
Other Authors: School of Civil and Environmental Engineering
Format: Article
Language:English
Published: 2023
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Online Access:https://hdl.handle.net/10356/164599
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Institution: Nanyang Technological University
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spelling sg-ntu-dr.10356-1645992023-03-31T01:59:33Z Catalytic activity and coke resistance of gasification slag-supported Ni catalysts during steam reforming of plastic pyrolysis gas Ong, Hang Meng Veksha, Andrei Ha, Quan Luu Manh Huang, Jijiang Tsakadze, Zviad Lisak, Grzegorz School of Civil and Environmental Engineering Nanyang Environment and Water Research Institute Residues and Resource Reclamation Centre Engineering::Environmental engineering::Waste management Gasification Slag Nickel Catalyst Pyrolysis gas from polyolefinic plastic waste is a hydrocarbon-rich feedstock for sustainable syngas production. The effect of Cr, Mo, and W promoters on the activity of gasification slag-supported Ni catalysts during the reforming of plastic pyrolysis gas was investigated (polyethylene and polypropylene mixed feedstock, Ni:promoter molar ratio = 4.5, 800 °C, steam-To-carbon molar ratio of 7). Based on 3 h reforming tests, all catalysts showed stable conversion efficiency, suggesting that gasification slag from municipal solid waste is a promising replacement material for traditionally used alumina supports. Moreover, the slag demonstrated good thermal stability and potential for catalyst recycling, justifying the economic benefit of valorizing the material. Interestingly, interaction between slags and promoters is evidenced by the formation of CaWO4and CaMoO4phases, which may have an impact on the reforming activity of bimetallic catalysts. Among the studied catalysts, the highest conversion efficiency of hydrocarbon compounds (76%), highest H2(122.65 mmol Lfeed-1) and CO (49.34 mmol Lfeed-1) yields, and lowest coke deposition (0.06 wt %) were demonstrated by the Ni-Mo catalyst. The superior performance of Ni-Mo was accompanied by the growth of carbon nanotubes via a tip-growth mechanism, which was not observed in other catalysts. Spherical carbon nanocages and filamentous carbon nanofibers predominated in coke deposits of Ni, Ni-W, and Ni-Cr. The high syngas production efficiency of Ni-Mo could be attributed to the dispersion of metal by the growing carbon nanotubes providing the reaction sites for reforming and coke gasification reactions. Owing to these properties, Ni catalyst promoted by Mo and loaded on a gasification support has high potential for the syngas production from plastic pyrolysis gas. National Research Foundation (NRF) Public Utilities Board (PUB) This research was supported by the National Research Foundation, Singapore and PUB, Singapore’s National Water Agency under its RIE2025 Urban Solutions and Sustainability (USS) (Water) Centre of Excellence (CoE) Programme, which provides funding to the Nanyang Environment & Water Research Institute (NEWRI) of the Nanyang Technological University, Singapore (NTU). 2023-02-06T05:46:26Z 2023-02-06T05:46:26Z 2022 Journal Article Ong, H. M., Veksha, A., Ha, Q. L. M., Huang, J., Tsakadze, Z. & Lisak, G. (2022). Catalytic activity and coke resistance of gasification slag-supported Ni catalysts during steam reforming of plastic pyrolysis gas. ACS Sustainable Chemistry & Engineering, 10(51), 17167-17176. https://dx.doi.org/10.1021/acssuschemeng.2c04946 2168-0485 https://hdl.handle.net/10356/164599 10.1021/acssuschemeng.2c04946 2-s2.0-85144284387 51 10 17167 17176 en ACS Sustainable Chemistry & Engineering © 2022 American Chemical Society. All rights reserved.
institution Nanyang Technological University
building NTU Library
continent Asia
country Singapore
Singapore
content_provider NTU Library
collection DR-NTU
language English
topic Engineering::Environmental engineering::Waste management
Gasification Slag
Nickel Catalyst
spellingShingle Engineering::Environmental engineering::Waste management
Gasification Slag
Nickel Catalyst
Ong, Hang Meng
Veksha, Andrei
Ha, Quan Luu Manh
Huang, Jijiang
Tsakadze, Zviad
Lisak, Grzegorz
Catalytic activity and coke resistance of gasification slag-supported Ni catalysts during steam reforming of plastic pyrolysis gas
description Pyrolysis gas from polyolefinic plastic waste is a hydrocarbon-rich feedstock for sustainable syngas production. The effect of Cr, Mo, and W promoters on the activity of gasification slag-supported Ni catalysts during the reforming of plastic pyrolysis gas was investigated (polyethylene and polypropylene mixed feedstock, Ni:promoter molar ratio = 4.5, 800 °C, steam-To-carbon molar ratio of 7). Based on 3 h reforming tests, all catalysts showed stable conversion efficiency, suggesting that gasification slag from municipal solid waste is a promising replacement material for traditionally used alumina supports. Moreover, the slag demonstrated good thermal stability and potential for catalyst recycling, justifying the economic benefit of valorizing the material. Interestingly, interaction between slags and promoters is evidenced by the formation of CaWO4and CaMoO4phases, which may have an impact on the reforming activity of bimetallic catalysts. Among the studied catalysts, the highest conversion efficiency of hydrocarbon compounds (76%), highest H2(122.65 mmol Lfeed-1) and CO (49.34 mmol Lfeed-1) yields, and lowest coke deposition (0.06 wt %) were demonstrated by the Ni-Mo catalyst. The superior performance of Ni-Mo was accompanied by the growth of carbon nanotubes via a tip-growth mechanism, which was not observed in other catalysts. Spherical carbon nanocages and filamentous carbon nanofibers predominated in coke deposits of Ni, Ni-W, and Ni-Cr. The high syngas production efficiency of Ni-Mo could be attributed to the dispersion of metal by the growing carbon nanotubes providing the reaction sites for reforming and coke gasification reactions. Owing to these properties, Ni catalyst promoted by Mo and loaded on a gasification support has high potential for the syngas production from plastic pyrolysis gas.
author2 School of Civil and Environmental Engineering
author_facet School of Civil and Environmental Engineering
Ong, Hang Meng
Veksha, Andrei
Ha, Quan Luu Manh
Huang, Jijiang
Tsakadze, Zviad
Lisak, Grzegorz
format Article
author Ong, Hang Meng
Veksha, Andrei
Ha, Quan Luu Manh
Huang, Jijiang
Tsakadze, Zviad
Lisak, Grzegorz
author_sort Ong, Hang Meng
title Catalytic activity and coke resistance of gasification slag-supported Ni catalysts during steam reforming of plastic pyrolysis gas
title_short Catalytic activity and coke resistance of gasification slag-supported Ni catalysts during steam reforming of plastic pyrolysis gas
title_full Catalytic activity and coke resistance of gasification slag-supported Ni catalysts during steam reforming of plastic pyrolysis gas
title_fullStr Catalytic activity and coke resistance of gasification slag-supported Ni catalysts during steam reforming of plastic pyrolysis gas
title_full_unstemmed Catalytic activity and coke resistance of gasification slag-supported Ni catalysts during steam reforming of plastic pyrolysis gas
title_sort catalytic activity and coke resistance of gasification slag-supported ni catalysts during steam reforming of plastic pyrolysis gas
publishDate 2023
url https://hdl.handle.net/10356/164599
_version_ 1762031103025086464