M.A. Soria

ORCID: 0000-0003-4694-3680
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About
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Research Areas
  • Catalysts for Methane Reforming
  • Catalytic Processes in Materials Science
  • Catalysis and Hydrodesulfurization Studies
  • Carbon Dioxide Capture Technologies
  • Catalysis and Oxidation Reactions
  • Catalysis for Biomass Conversion
  • Layered Double Hydroxides Synthesis and Applications
  • Electrocatalysts for Energy Conversion
  • Membrane Separation and Gas Transport
  • Carbon dioxide utilization in catalysis
  • Thermal Expansion and Ionic Conductivity
  • Chemical Looping and Thermochemical Processes
  • Industrial Gas Emission Control
  • Thermochemical Biomass Conversion Processes
  • Process Optimization and Integration
  • Nanomaterials for catalytic reactions
  • Edible Oils Quality and Analysis
  • Hybrid Renewable Energy Systems
  • Transition Metal Oxide Nanomaterials
  • Adsorption and Cooling Systems
  • Zeolite Catalysis and Synthesis
  • Advanced oxidation water treatment
  • Subcritical and Supercritical Water Processes
  • Nanoporous metals and alloys
  • Biodiesel Production and Applications

Universidade do Porto
2016-2025

Instituto de Catálisis y Petroleoquímica
2011-2021

Consejo Superior de Investigaciones Científicas
2010-2013

UCLouvain
2007-2013

Biomass gasification produces syngas composed mainly of hydrogen, carbon monoxide, dioxide, methane, water, and higher hydrocarbons, till C4, ethane. The hydrocarbon content can be upgraded into richer hydrogen streams through the steam reforming reaction. This study assessed process at thermodynamic equilibrium five streams, with different compositions, from three biomass sources (Lignin, Miscanthus, Eucalyptus). simulations were performed on Aspen Plus V12 software using Gibbs energy...

10.1016/j.fuproc.2023.107859 article EN cc-by-nc-nd Fuel Processing Technology 2023-06-08

The effect of La/AlZn/AlLa oxide supports on Ni-based catalysts performance was assessed for glycerol steam reforming renewable H2 production. NiAlLaOx showed the best providing a conversion into gaseous products 91 % and yield 5.40 molH2∙molG,in‐1 at 700 °C. Additionally, stability experiments lasting up to 24h were performed 625 °C, having been observed stable behavior with low coke formation. materials physicochemical properties, determined from different techniques (ICP-OES, N2-sorption...

10.1016/j.renene.2024.120076 article EN cc-by-nc Renewable Energy 2024-01-30

Solids with potential application in tyrosol (Ty) removal by photo–Fenton processes have been synthesized using aluminum salt cake as a source. Two series of hydrocalumite layered double hydroxides (LDH) were synthesized: one containing structural Fe3+ (occupying octahedral positions the LDH) and another surface impregnated Fe3+; all solids calcined air at 750 ºC. The characterized powder X–ray diffraction, FT–infrared spectroscopy, thermal analysis, N2 adsorption–desorption isotherms –196...

10.1016/j.jece.2024.112423 article EN cc-by-nc-nd Journal of environmental chemical engineering 2024-03-07

Distillery wastewater (DW) is a byproduct of the wine distillery industry, posing environmental challenges due to its pollutant nature and costly disposal. This study investigates steam reforming as method for treating valorizing DW by removing pollutants while generating renewable hydrogen. Traditional (TR) autothermal (ATR − combining partial oxidation) processes are explored across varying compositions (mix 1–5) derived from lees, pomace, wine. Simulations performed under different...

10.1016/j.enconman.2024.118442 article EN cc-by-nc-nd Energy Conversion and Management 2024-04-25

In this work, in-house synthesized NiMgAl, Ru/NiMgAl, and Ru/SiO2 catalysts a commercial ruthenium-containing material (Ru/Al2O3com.) were tested for CO2 methanation at 250, 300, 350 °C (weight hourly space velocity, WHSV, of 2400 mLN,CO2·g−1·h−1). Materials compared in terms conversion CH4 selectivity. Still, their performances assessed short stability test (24 h) performed °C. All characterized by temperature programmed reduction (TPR), X-ray diffraction (XRD), N2 physisorption −196 °C,...

10.3390/catal9121008 article EN Catalysts 2019-12-01
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