Please use this identifier to cite or link to this item: http://dspace.uniten.edu.my/jspui/handle/123456789/6929
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dc.contributor.authorSaad, J.M.
dc.contributor.authorWilliams, P.T.
dc.date.accessioned2018-01-11T08:26:06Z-
dc.date.available2018-01-11T08:26:06Z-
dc.date.issued2016
dc.identifier.urihttp://dspace.uniten.edu.my/jspui/handle/123456789/6929-
dc.description.abstractThe CO2 dry reforming of various types of waste plastics (LDPE, HDPE, PS, PET, and PP) and a simulated mixture of the different waste plastics was investigated over a Ni-Co-Al catalyst using a two-stage reactor. The first stage pyrolyzed the plastics, and the second stage involved catalytic-dry reforming of the product pyrolysis gases with CO2. The introduction of CO2 without a catalyst markedly increased the dry reforming reaction and significantly improved the production of H2/CO synthesis gas (syngas). The introduction of the Ni-Co-Al catalyst further significantly improved the production of syngas. LDPE produced the highest yield of syngas at 154.7 mmolsyngas g-1 plastic from the pyrolysis-catalytic-dry reforming process. The order of syngas production for the different plastics was LDPE < HDPE < PP < PS < PET. The syngas yield from the processing of the simulated waste plastic mixture was 148.6 7 mmolsyngas g-1 plastic which reflected the high content of the linear polyalkene plastics (LDPE, HDPE, PP) in the simulated waste plastic mixture. © 2016 American Chemical Society.
dc.titlePyrolysis-Catalytic-Dry Reforming of Waste Plastics and Mixed Waste Plastics for Syngas Production
item.grantfulltextnone-
item.fulltextNo Fulltext-
Appears in Collections:COE Scholarly Publication
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