Pedro Castaño Sanchez-rekin lankidetzan egindako argitalpenak (30)

2024

  1. A global methanol-to-hydrocarbons (MTH) model with H-ZSM-5 catalyst acidity descriptors

    Fuel, Vol. 378

  2. Dual-cycle-based lumped kinetic model for methanol-to-aromatics (MTA) reaction over H-ZSM-5 zeolites of different Si/Al ratio

    Fuel, Vol. 361

  3. Improving the dehydrogenation function and stability of Zn-modified ZSM-5 catalyst in methanol-to-aromatics reaction by Ca addition

    Applied Catalysis A: General, Vol. 683

2022

  1. Spectro-kinetics of the methanol to hydrocarbons reaction combining online product analysis with UV–vis and FTIR spectroscopies throughout the space time evolution

    Journal of Catalysis, Vol. 408, pp. 115-127

  2. Streamlining the estimation of kinetic parameters using periodic reaction conditions: The methanol-to-hydrocarbon reaction as a case study

    Chemical Engineering Journal, Vol. 435

2020

  1. A comprehensive approach for designing different configurations of isothermal reactors with fast catalyst deactivation

    Chemical Engineering Journal, Vol. 379

  2. Coke formation and deactivation during catalytic reforming of biomass and waste pyrolysis products: A review

    Renewable and Sustainable Energy Reviews, Vol. 119

2019

  1. On the dynamics and reversibility of the deactivation of a Rh/CeO 2 –ZrO 2 catalyst in raw bio-oil steam reforming

    International Journal of Hydrogen Energy, Vol. 44, Núm. 5, pp. 2620-2632

2018

  1. Coking and sintering progress of a Ni supported catalyst in the steam reforming of biomass pyrolysis volatiles

    Applied Catalysis B: Environmental, Vol. 233, pp. 289-300

  2. Kinetic Model for the Conversion of Chloromethane into Hydrocarbons over a HZSM-5 Zeolite Catalyst

    Industrial and Engineering Chemistry Research, Vol. 57, Núm. 3, pp. 908-919

  3. Mild steamed HZSM-5 zeolite catalysts for enhancing propylene selectivity in the cracking of 1-butene

    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

  4. Oxidative steam reforming of raw bio-oil over supported and bulk Ni catalysts for hydrogen production

    Catalysts, Vol. 8, Núm. 8

  5. Simultaneous modeling of the kinetics for n-pentane cracking and the deactivation of a HZSM-5 based catalyst

    Chemical Engineering Journal, Vol. 331, pp. 818-830

  6. Temperature Programmed Oxidation Coupled with In Situ Techniques Reveal the Nature and Location of Coke Deposited on a Ni/La2O3-αAl2O3 Catalyst in the Steam Reforming of Bio-oil

    ChemCatChem, Vol. 10, Núm. 10, pp. 2311-2321

2017

  1. Deactivation dynamics of a Ni supported catalyst during the steam reforming of volatiles from waste polyethylene pyrolysis

    Applied Catalysis B: Environmental, Vol. 209, pp. 554-565

  2. Role of oxygenates and effect of operating conditions in the deactivation of a Ni supported catalyst during the steam reforming of bio-oil

    Green Chemistry, Vol. 19, Núm. 18, pp. 4315-4333

  3. SAPO-18 and SAPO-34 catalysts for propylene production from the oligomerization-cracking of ethylene or 1-butene

    Applied Catalysis A: General, Vol. 547, pp. 176-182

  4. Selective dealumination of HZSM-5 zeolite boosts propylene by modifying 1-butene cracking pathway

    Applied Catalysis A: General, Vol. 543, pp. 1-9

2016

  1. Correlating compositions of the reaction medium and coke during the steam reforming of bio-oil on a Ni/La2O3-αAl2O3 catalyst

    22nd International Congress of Chemical and Process Engineering, CHISA 2016 and 19th Conference on Process Integration, Modelling and Optimisation for Energy Saving and Pollution Reduction, PRES 2016

2015

  1. Controlling coke deactivation and cracking selectivity of MFI zeolite by H3PO4 or KOH modification

    Applied Catalysis A: General, Vol. 505, pp. 105-115