Publications by the researcher in collaboration with JOSE DEL ROSARIO VALECILLOS DIAZ (22)

2024

  1. Global Vision of the Reaction and Deactivation Routes in the Ethanol Steam Reforming on a Catalyst Derived from a Ni-Al Spinel

    Energy and Fuels, Vol. 38, Núm. 8, pp. 7033-7048

2023

  1. Comparison of the NiAl2O4 derived catalyst deactivation in the steam reforming and sorption enhanced steam reforming of raw bio-oil in packed and fluidized-bed reactors

    Chemical Engineering Journal, Vol. 458

  2. High-Purity Green Hydrogen Production by Bio-oil/Ethanol Mixtures Steam Reforming in Pd-Based Membrane Reactors

    Chemical Engineering Transactions, Vol. 100, pp. 259-264

  3. Sorption enhanced steam reforming (SESR) of raw bio-oil with Ni based catalysts: Effect of sorbent type, catalyst support and sorbent/catalyst mass ratio

    Fuel Processing Technology, Vol. 247

  4. Syngas Production through Dry Reforming of Raw Bio-oil: Effect of CO2/C Ratio

    Chemical Engineering Transactions, Vol. 99, pp. 355-360

  5. Syngas production through combined steam-dry reforming of raw bio-oil over a NiAl2O4 spinel derived catalyst

    Journal of CO2 Utilization, Vol. 78

  6. Thermodynamic study of the CO2 valorization in the combined steam-dry reforming of bio-oil into syngas

    Journal of CO2 Utilization, Vol. 72

2022

  1. Combined effect of bio-oil composition and temperature on the stability of Ni spinel derived catalyst for hydrogen production by steam reforming

    Fuel, Vol. 326

  2. Comparison of Fixed and Fluidized Bed Reactors in the Steam Reforming of Raw Bio-oil with NiAl2O4 Derived Catalyst

    Chemical Engineering Transactions, Vol. 92, pp. 241-246

  3. Hydrogen Production from Ethanol through Steam Reforming on Ni-based Catalysts

    Chemical Engineering Transactions, Vol. 92, pp. 247-252

  4. Stability of a NiAl2O4 Derived Catalyst in the Ethanol Steam Reforming in Reaction-Regeneration Cycles: Effect of Reduction Temperature

    Catalysts, Vol. 12, Núm. 5

  5. Unveiling the deactivation by coke of NiAl2O4 spinel derived catalysts in the bio-oil steam reforming: Role of individual oxygenates

    Fuel, Vol. 321

2021

  1. Coke deactivation and regeneration of HZSM-5 zeolite catalysts in the oligomerization of 1-butene

    Applied Catalysis B: Environmental, Vol. 291

  2. Effect of reaction conditions on the deactivation by coke of a NiAl2O4 spinel derived catalyst in the steam reforming of bio-oil

    Applied Catalysis B: Environmental, Vol. 297

  3. Feasibility of online pre-reforming step with dolomite for improving Ni spinel catalyst stability in the steam reforming of raw bio-oil

    Fuel Processing Technology, Vol. 215

  4. Insights into the reaction routes for H2 formation in the ethanol steam reforming on a catalyst derived from NiAl2O4 spinel

    Energy and Fuels, Vol. 35, Núm. 21, pp. 17197-17211

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

  2. Slowing down the deactivation of H-ZSM-5 zeolite catalyst in the methanol-to-olefin (MTO) reaction by P or Zn modifications

    Catalysis Today, Vol. 348, pp. 243-256

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

  2. Kinetic and Deactivation Differences Among Methanol, Dimethyl Ether and Chloromethane as Stock for Hydrocarbons

    ChemCatChem