4.7 Article

Upgrading model compounds and Scrap Tires Pyrolysis Oil (STPO) on hydrotreating NiMo catalysts with tailored supports

Journal

FUEL
Volume 145, Issue -, Pages 158-169

Publisher

ELSEVIER SCI LTD
DOI: 10.1016/j.fuel.2014.12.055

Keywords

Hydrodesulfurization; Mild hydrocracking; Tire valorization; NiMo catalyst; Diesel

Funding

  1. Ministry of Economy and Competitivity of the Spanish Government (MINECO) [CTQ2010-19623, CTQ2012-35192]
  2. Department of Industry, Trade and Tourism of the Basque Government (SAIOTEK) [SA-2011/00098, SA-2013/00173]
  3. Basque Government research training grant [BFI2010-223]

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The upgrading of Scrap Tire Pyrolysis Oil (STPO) has been studied in order to remove undesired sulfur, nitrogen and unsaturated compounds while improving the properties of its different fractions (naphtha, diesel and gasoil) toward being used as a potential blend in the refinery. The studied catalysts are NiMo supported on 5 porous materials: gamma-Al2O3 (ALM catalyst), SiO2-Al2O3 (ASA), SBA-15 (SBA), MCM-41 (MCM) and an equilibrated FCC catalyst (FCC). The hydrotreating runs have been carried out in a fixed bed reactor at 275-375 degrees C and 65 bar. The catalysts were characterized by ICP-AES, N-2 adsorption-desorption isotherms, H-2 chemisorption, XRD, XPS, TPR and terc-butylamine adsorption-desorption (TPD). A preliminary catalyst screening with a model mixture of representative STPO compounds has been performed for selecting the most active catalysts: ALM, ASA and MCM catalysts ensured the 99.9% removal of sulfur. Secondly and in the hydrotreating of STPO, our results point the suitability of ASA catalyst for obtaining the highest proportion of naphtha (25 wt%) and diesel (57 wt%), ALM catalyst for increasing the yield of paraffins and the cetane number in diesel, and the promising performance of MCM catalyst for facilitating internal mass transfer. (C) 2014 Elsevier Ltd. All rights reserved.

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