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Effect of Promoters on Steam Reforming of Toluene over a Ni-Based Catalyst Supported on Coal Gangue Ash

[Image: see text] The exploration of high-value-added materials using inorganic solid waste is a very important contribution to sustainable development. Coal gangue ash (CGA) as a solid waste was chosen as catalyst support. Five low-cost catalysts modified by different promoters (Co, Ce, Fe, Mn, and...

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Autores principales: Lu, Min, Xiong, Zuhong, Fang, Kejing, Li, Jiqing, Li, Xi, Li, Tao
Formato: Online Artículo Texto
Lenguaje:English
Publicado: American Chemical Society 2020
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC7581085/
https://www.ncbi.nlm.nih.gov/pubmed/33110961
http://dx.doi.org/10.1021/acsomega.0c01197
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author Lu, Min
Xiong, Zuhong
Fang, Kejing
Li, Jiqing
Li, Xi
Li, Tao
author_facet Lu, Min
Xiong, Zuhong
Fang, Kejing
Li, Jiqing
Li, Xi
Li, Tao
author_sort Lu, Min
collection PubMed
description [Image: see text] The exploration of high-value-added materials using inorganic solid waste is a very important contribution to sustainable development. Coal gangue ash (CGA) as a solid waste was chosen as catalyst support. Five low-cost catalysts modified by different promoters (Co, Ce, Fe, Mn, and Mo) were prepared using a co-impregnation method. The toluene steam reforming tests were carried out at 800 °C under S/C = 2 (steam-to-carbon mole ratio). Catalyst characteristics were evaluated using X-ray diffraction (XRD), the Brunauer–Emmett–Teller (BET) method, temperature-programmed reduction (TPR), and Raman spectroscopy. The results showed that most promoters could interact with a Ni active compound and enhance the toluene conversion and H(2) yield. The Mo-Ni/CGA-1d (1d means the acid pretreatment time) catalyst performed the best catalytic activity, and corresponding toluene conversion and H(2) yield was equal to 92.6 and 62.3%, respectively, and it should be due to the formation of Mo-Ni alloy. Meanwhile, the Mo-Ni/CGA-1d catalyst exhibited higher stability during the runtime of 300 min compared with the Mn-Ni/CGA-1d catalyst, which can be attributed to the formation of the Mo(2)C structure with high-carbon-resistance ability. This is perhaps because the dissociation of CO(2) or H(2)O on the Mo(2)C structure surface is beneficial to the production of free oxygen species, which can accelerate the removal of carbon deposition on the catalyst surface.
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spelling pubmed-75810852020-10-26 Effect of Promoters on Steam Reforming of Toluene over a Ni-Based Catalyst Supported on Coal Gangue Ash Lu, Min Xiong, Zuhong Fang, Kejing Li, Jiqing Li, Xi Li, Tao ACS Omega [Image: see text] The exploration of high-value-added materials using inorganic solid waste is a very important contribution to sustainable development. Coal gangue ash (CGA) as a solid waste was chosen as catalyst support. Five low-cost catalysts modified by different promoters (Co, Ce, Fe, Mn, and Mo) were prepared using a co-impregnation method. The toluene steam reforming tests were carried out at 800 °C under S/C = 2 (steam-to-carbon mole ratio). Catalyst characteristics were evaluated using X-ray diffraction (XRD), the Brunauer–Emmett–Teller (BET) method, temperature-programmed reduction (TPR), and Raman spectroscopy. The results showed that most promoters could interact with a Ni active compound and enhance the toluene conversion and H(2) yield. The Mo-Ni/CGA-1d (1d means the acid pretreatment time) catalyst performed the best catalytic activity, and corresponding toluene conversion and H(2) yield was equal to 92.6 and 62.3%, respectively, and it should be due to the formation of Mo-Ni alloy. Meanwhile, the Mo-Ni/CGA-1d catalyst exhibited higher stability during the runtime of 300 min compared with the Mn-Ni/CGA-1d catalyst, which can be attributed to the formation of the Mo(2)C structure with high-carbon-resistance ability. This is perhaps because the dissociation of CO(2) or H(2)O on the Mo(2)C structure surface is beneficial to the production of free oxygen species, which can accelerate the removal of carbon deposition on the catalyst surface. American Chemical Society 2020-10-09 /pmc/articles/PMC7581085/ /pubmed/33110961 http://dx.doi.org/10.1021/acsomega.0c01197 Text en © 2020 American Chemical Society This is an open access article published under an ACS AuthorChoice License (http://pubs.acs.org/page/policy/authorchoice_termsofuse.html) , which permits copying and redistribution of the article or any adaptations for non-commercial purposes.
spellingShingle Lu, Min
Xiong, Zuhong
Fang, Kejing
Li, Jiqing
Li, Xi
Li, Tao
Effect of Promoters on Steam Reforming of Toluene over a Ni-Based Catalyst Supported on Coal Gangue Ash
title Effect of Promoters on Steam Reforming of Toluene over a Ni-Based Catalyst Supported on Coal Gangue Ash
title_full Effect of Promoters on Steam Reforming of Toluene over a Ni-Based Catalyst Supported on Coal Gangue Ash
title_fullStr Effect of Promoters on Steam Reforming of Toluene over a Ni-Based Catalyst Supported on Coal Gangue Ash
title_full_unstemmed Effect of Promoters on Steam Reforming of Toluene over a Ni-Based Catalyst Supported on Coal Gangue Ash
title_short Effect of Promoters on Steam Reforming of Toluene over a Ni-Based Catalyst Supported on Coal Gangue Ash
title_sort effect of promoters on steam reforming of toluene over a ni-based catalyst supported on coal gangue ash
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC7581085/
https://www.ncbi.nlm.nih.gov/pubmed/33110961
http://dx.doi.org/10.1021/acsomega.0c01197
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