Karagoz, SYanik, JUcar, SSaglam, MSong, C2019-10-272019-10-2720030926-860X1873-38750926-860X1873-3875https://doi.org/10.1016/S0926-860X(02)00505-7https://hdl.handle.net/11454/36895In this study, the conversion of HDPE in VGO to fuels was carried out in absence and presence of catalyst. The blend containing 20% HDPE was co-processed in presence of hydrogen at the temperatures of 435 and 450degreesC. Five kinds of metal supported on active carbon catalysts (M-Ac) and acidic catalysts (HZSM-5 and DHC-8) were tested. The product distribution and the quality of liquid product changed depending upon the temperature and the type of catalyst. Among the metal supported active carbon catalyst, Co-Ac showed the highest cracking activity where as Mo-Ac showed the highest hydrodesulfurization activity. Co-Ac had better cracking activity than commercial hydrocracking catalyst (DHC-8). Although HZSM-5 had the best cracking effect in the hydrocracking of HDPE/VGO blend, the liquid product from HZSM-5 contained the highest sulphur. The use of carbon-supported metal catalysts in the co-processing of HDPE with VGO looks promising solution from an environmental viewpoint. (C) 2002 Elsevier Science B.V. All rights reserved.en10.1016/S0926-860X(02)00505-7info:eu-repo/semantics/closedAccessactive carbonhigh density polyethyleneco-processinghydrocrackingHDSCatalytic and thermal degradation of high-density polyethylene in vacuum gas oil over non-acidic and acidic catalystsArticle24215162WOS:000181703500006Q1Q1