Heterogeneous Catalysis for a Greener Environment

A special issue of Catalysts (ISSN 2073-4344). This special issue belongs to the section "Environmental Catalysis".

Deadline for manuscript submissions: closed (30 September 2025) | Viewed by 592

Special Issue Editors


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Grupo de Catálisis y Procesos de Separación-CyPS, Departamento de Ingeniería Química y de Materiales, Facultad de Ciencias Químicas, Complutense University, Avda Complutense S-N, E-28040 Madrid, Spain
Interests: adsorption processes; heterogeneous catalysis; modeling; nanostructured carbon materials
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Guest Editor
Group of Catalysis and Separation Processes (CyPS), Department of Chemical Engineering and Materials, Complutense University of Madrid, 28040 Madrid, Spain
Interests: photocatalysis; catalyst synthesis and characterization; catalytic wet peroxide oxidation; advanced oxidation processes
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Special Issue Information

Dear Colleagues,

Water scarcity is a critical global challenge affecting over 2 billion people worldwide, with increasing population, industrial growth, and climate change exacerbating the problem. As freshwater resources become increasingly stressed, innovative technological solutions are essential to address this issue. Green heterogeneous catalysts have emerged as a promising water management approach, offering advanced water purification, treatment, and resource conservation methods.

The focus of this Special Issue is to provide a general overview of the main concepts and current advances in the heterogeneous catalysis field, including the use of catalytic processes as alternative treatment methods for aqueous pollutants, such as plastics, pharmaceutical, pesticide compounds, and numerous industrial chemicals, with regard to water remediation. Original research papers and short reviews addressing the synthesis and characterization of new heterogeneous catalysts, influences of different operating parameters and reactor types, reaction kinetics, and mechanisms and identification of intermediates are invited for submission.

Prof. Dr. Juan García Rodríguez
Dr. Silvia Álvarez-Torrellas
Dr. Jaime Carbajo Olleros
Guest Editors

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Keywords

  • catalytic processes
  • advanced oxidation processes
  • wastewater treatment
  • toxic-refractory wastewaters
  • synthesis of catalysts
  • reaction kinetics and mechanisms
  • identification of intermediates
  • low-cost catalysts
  • activity and stability of heterogeneous catalysts

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Published Papers (1 paper)

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Research

14 pages, 1153 KB  
Article
Greener Catalytic Oxidation of Azole Fungicides: Coupling EO–O3 on BDD with Kinetics and Mineralization Targets
by Joaquin R. Dominguez, Teresa González and David Simón-García
Catalysts 2025, 15(12), 1136; https://doi.org/10.3390/catal15121136 - 3 Dec 2025
Viewed by 383
Abstract
This study evaluates the abatement of four common azole fungicides—prochloraz, tebuconazole, tetraconazole, and penconazole—using ozonation (O3), electro-oxidation (EO on boron-doped diamond anode), and their coupling (EO–O3). A central composite design (CCD) with three coded factors—current (A), electrolyte (B), and [...] Read more.
This study evaluates the abatement of four common azole fungicides—prochloraz, tebuconazole, tetraconazole, and penconazole—using ozonation (O3), electro-oxidation (EO on boron-doped diamond anode), and their coupling (EO–O3). A central composite design (CCD) with three coded factors—current (A), electrolyte (B), and ozone concentration in the gas phase (C)—was employed to model three responses: pollutant abatement (%), apparent pseudo-first-order rate constant k (min−1), and TOC removal (%). Quadratic models showed good in-samples (R2 ≈ 0.84–0.86). Ozone and current dominate abatement and kinetics (with curvature in current), while the electrolyte penalizes mineralization and narrows the window for TOC removal. Under optimal conditions, 116 mA (current), 0.992 mM (electrolyte), and 7.09 ppm (ozone concentration), the EO–O3 configuration results in a TOC removal of 33.78%. At a reaction time of 10 min (total abatement of the pollutants), the hybrid EO–O3 configuration exhibits a specific energy consumption (SEC) of 1.825 kWh·m−3. We compare trends with the last decade of literature on ozone-based EAOPs, electro-peroxone variants, and BDD anodic oxidation, and outline practical guidance for its application and scale-up, and model refinement in predictive settings. Full article
(This article belongs to the Special Issue Heterogeneous Catalysis for a Greener Environment)
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