Kinetic Modeling of the Hydrotreating and Hydrocracking Stages for Upgrading Scrap Tires Pyrolysis Oil (STPO) toward High-Quality Fuels

Idoia Hita, Andrés T. Aguayo, Martin Olazar, Miren J. Azkoiti, Javier Bilbao, José M. Arandes, Pedro Castano*

*Corresponding author for this work

Research output: Contribution to journalArticlepeer-review

18 Scopus citations

Abstract

The upgrading of scrap tires pyrolysis oil (STPO) has been studied in order to produce high-quality alternative fuels, conceived as the second and third stage of an industrially orientated valorization pathway for tires: pyrolysis, hydrotreating, and hydrocracking. The experiments have been carried out in a fixed-bed reactor under the following experimental conditions: (i) for hydrotreating: NiMo/Al2O3 catalyst; time on stream (TOS), 0-8 h; 300-375 °C; 65 bar; H2:oil ratio, 1000 (v/v); space time, 0-0.5 gcat h gfeed-1; and (ii) for hydrocracking: PtPd/SiO2-Al2O3 catalyst; TOS, 0-6 h; 440-500 °C; 65 bar; space time, 0-0.28 gcat h gfeed-1; H2:oil ratio, 1000 (v/v). From the results, lump-based kinetic models have been established for both stages, considering the reactions of (i) hydrodesulfurization (HDS), (ii) hydrocracking (HC), and (iii) hydrodearomatization (HDA) in each one of them. Catalyst deactivation is insignificant in the hydrotreating stage but important for the hydrocracking stage. Therefore, deactivation has been considered in the corresponding kinetic equations. The computed deactivation constants have allowed for quantifying the contribution of each lump/composition fraction to coke formation.

Original languageEnglish (US)
Pages (from-to)7542-7553
Number of pages12
JournalEnergy and Fuels
Volume29
Issue number11
DOIs
StatePublished - Nov 19 2015

ASJC Scopus subject areas

  • Chemical Engineering(all)
  • Fuel Technology
  • Energy Engineering and Power Technology

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