Upcycling plastic waste into syngas: development of gasification slag supported NI catalysts for steam reforming of pyrolysis gas
Upcycling pyrolysis gas from plastics (70 wt% PP, 6 wt% LDPE, and 24 wt% HDPE) was explored using slag supported Ni catalysts without promoters and promoted with Cr, Mo and W (Ni, Ni-Cr, Ni-Mo, and Ni-W). The objective is to understand the promoting effects of Cr, Mo and W on gasification slag su...
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Format: | Thesis-Master by Research |
Language: | English |
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Nanyang Technological University
2022
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Online Access: | https://hdl.handle.net/10356/162342 |
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Institution: | Nanyang Technological University |
Language: | English |
Summary: | Upcycling pyrolysis gas from plastics (70 wt% PP, 6 wt% LDPE, and 24 wt%
HDPE) was explored using slag supported Ni catalysts without promoters and
promoted with Cr, Mo and W (Ni, Ni-Cr, Ni-Mo, and Ni-W). The objective is to
understand the promoting effects of Cr, Mo and W on gasification slag supported Ni
catalysts during steam reforming of mixed hydrocarbon compounds. The catalytic
activity and coke resistance of the promoted Ni catalysts were investigated for
efficient upgrading of plastic pyrolysis gas to syngas. The reforming experiments
were conducted at 800 °C for 3 h with steam-to-carbon molar ratio of 7. Catalyst
characteristics were studied using BET method, TPR, XRD, SEM, CHNS elemental
analysis, and TGA. Gas composition after steam reforming was determined using gas
chromatography. Ni-Mo catalyst had the highest hydrocarbon conversion, hydrogen
yield, and was less prone to coking. The superior catalytic activity observed from the
Ni-Mo catalyst could be attributed to the formation of Ni2Mo3O8 phase, which led to
dispersion and stabilization of active Ni species in the form of metal alloy upon
reduction. The formation of the reducible species on slag supported catalyst suggest
its potential for valorization. The formation of CaMoO4 in Ni-Mo and CaWO4 in Ni-
W could be attributed to the solid reaction of the Mo and W promoters with the slag
during calcination. Different degree coke deposition was observed over the catalysts,
due to the difference in catalytic activity. |
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