GORKA ELORDI FORURIA-rekin lankidetzan egindako argitalpenak (30)

2024

  1. Are Rh Catalysts a Suitable Choice for Bio-Oil Reforming? The Case of a Commercial Rh Catalyst in the Combined H2O and CO2 Reforming of Bio-Oil

    Catalysts, Vol. 14, Núm. 9

2020

  1. Lessening coke formation and boosting gasoline yield by incorporating scrap tire pyrolysis oil in the cracking conditions of an FCC unit

    Energy Conversion and Management, Vol. 224

2019

  1. Coke deposition and product distribution in the co-cracking of waste polyolefin derived streams and vacuum gas oil under FCC unit conditions

    Fuel Processing Technology, Vol. 192, pp. 130-139

2018

  1. Energetic Viability of a Polyolefin Pyrolysis Plant

    Energy and Fuels, Vol. 32, Núm. 3, pp. 3751-3759

  2. Energetic viability of a polyolefin pyrolysis plant

    23rd International Congress of Chemical and Process Engineering, CHISA 2018 and 21st Conference on Process Integration, Modelling and Optimisation for Energy Saving and Pollution Reduction, PRES 2018

2014

  1. Identification of the coke deposited on an HZSM-5 zeolite catalyst during the sequenced pyrolysis-cracking of HDPE

    Applied Catalysis B: Environmental, Vol. 148-149, pp. 436-445

  2. Principal component analysis for kinetic scheme proposal in the thermal pyrolysis of waste HDPE plastics

    Chemical Engineering Journal, Vol. 254, pp. 357-364

2013

  1. Cracking of high density polyethylene pyrolysis waxes on HZSM-5 catalysts of different acidity

    Industrial and Engineering Chemistry Research, Vol. 52, Núm. 31, pp. 10637-10645

2012

  1. Characterization of the waxes obtained by the pyrolysis of polyolefin plastics in a conical spouted bed reactor

    Journal of Analytical and Applied Pyrolysis, Vol. 94, pp. 230-237

  2. Effect of the acidity of the HZSM-5 zeolite catalyst on the cracking of high density polyethylene in a conical spouted bed reactor

    Applied Catalysis A: General, Vol. 415-416, pp. 89-95

  3. Imaging the Profiles of Deactivating Species on the Catalyst used for the Cracking of Waste Polyethylene by Combined Microscopies

    ChemCatChem, Vol. 4, Núm. 5, pp. 631-635

  4. Influence of temperature on biomass pyrolysis in a conical spouted bed reactor

    Resources, Conservation and Recycling, Vol. 59, pp. 23-31

  5. Light olefins from HDPE cracking in a two-step thermal and catalytic process

    Chemical Engineering Journal, Vol. 207-208, pp. 27-34

  6. Pathways of coke formation on an MFI catalyst during the cracking of waste polyolefins

    Catalysis Science and Technology, Vol. 2, Núm. 3, pp. 504-508

  7. Polyethylene cracking on a spent FCC catalyst in a conical spouted bed

    Industrial and Engineering Chemistry Research, Vol. 51, Núm. 43, pp. 14008-14017

  8. Production of light olefins from polyethylene in a two-step process: Pyrolysis in a conical spouted bed and downstream high-temperature thermal cracking

    Industrial and Engineering Chemistry Research, Vol. 51, Núm. 43, pp. 13915-13923

2011

  1. Continuous polyolefin cracking on an HZSM-5 zeolite catalyst in a conical spouted bed reactor

    Industrial and Engineering Chemistry Research, Vol. 50, Núm. 10, pp. 6061-6070

  2. Insights into the coke deposited on HZSM-5, Hβ and HY zeolites during the cracking of polyethylene

    Applied Catalysis B: Environmental, Vol. 104, Núm. 1-2, pp. 91-100

  3. Product yields and compositions in the continuous pyrolysis of high-density polyethylene in a conical spouted bed reactor

    Industrial and Engineering Chemistry Research, Vol. 50, Núm. 11, pp. 6650-6659

  4. Role of pore structure in the deactivation of zeolites (HZSM-5, Hβ and HY) by coke in the pyrolysis of polyethylene in a conical spouted bed reactor

    Applied Catalysis B: Environmental, Vol. 102, Núm. 1-2, pp. 224-231