Iron in Catalysis

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

Deadline for manuscript submissions: closed (31 December 2021) | Viewed by 7423

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Laboratory for Chemical Technology, Universiteit Gent, Ghent, Belgium
Interests: catalysis; chemical kinetics; chemical looping
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Guest Editor
Laboratory of Petrochemical Technology, Chemical Engineering Department, Aristotle University of Thessaloniki, 54124 Thessaloniki, Greece
Interests: heterogeneous catalysis; green chemistry; synchrotron radiation; porous solids; nanoparticles; alloys; selective oxidation; biofuels

Special Issue Information

More than 100 years ago, Nobel Prize winner in Literature, Rudyard Kipling, wrote his poem “Cold Iron” with the following refrain: “But Iron - Cold Iron - is master of them all”. Indeed, iron appears in many facets of our lives and has claimed an irreplaceable position. After years of waning interest, more and more scientists are rediscovering iron and finding themselves amazed by its properties. A century later, the refrain of Kipling has not changed except for one word—currently iron is not cold but, rather, a hot research topic in catalysis.

There has been a resurgence of research into iron-containing materials due to their exciting properties, making them ideal for a wide range of applications. A vast number of products can be generated, including hydrogen, plastics, alcohols, pharmaceuticals, feed-stock chemicals, and other materials. Iron-based catalysts or materials can be/have been employed either industrially or at the research level for several processes:

  • Reforming reactions for syngas production;
  • Catalytic oxidation;
  • Water–gas shift reaction;
  • Alkane dehydrogenation reactions (oxidative or not);
  • CO2 utilization processes;
  • The Fischer–Tropsch process.

This Special Issue of Catalysis will be a collaborative effort to combine current catalysis research on iron, including experimental and theoretical perspectives on both heterogeneous and homogeneous catalysts. We welcome contributions from the catalysis community on catalyst characterization, kinetics, reaction mechanism, reactor development, theoretical modeling, and surface science.

Prof. Dr. Vladimir Galvita
Dr. Stavros Theofanidis
Guest Editors

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Keywords

  • Reforming reactions for syngas production
  • Catalytic oxidation
  • Water–gas shift reaction
  • Alkane dehydrogenation reactions (oxidative or not)
  • CO2 utilization processes
  • Fischer–Tropsch process

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Published Papers (2 papers)

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Research

10 pages, 2552 KiB  
Article
Investigation of Co–Fe–Al Catalysts for High-Calorific Synthetic Natural Gas Production: Pilot-Scale Synthesis of Catalysts
by Tae Young Kim, Seong Bin Jo, Jin Hyeok Woo, Jong Heon Lee, Ragupathy Dhanusuraman, Soo Chool Lee and Jae Chang Kim
Catalysts 2021, 11(1), 105; https://doi.org/10.3390/catal11010105 - 13 Jan 2021
Cited by 7 | Viewed by 2109
Abstract
Co–Fe–Al catalysts prepared using coprecipitation at laboratory scale were investigated and extended to pilot scale for high-calorific synthetic natural gas. The Co–Fe–Al catalysts with different metal loadings were analyzed using BET, XRD, H2-TPR, and FT-IR. An increase in the metal loading [...] Read more.
Co–Fe–Al catalysts prepared using coprecipitation at laboratory scale were investigated and extended to pilot scale for high-calorific synthetic natural gas. The Co–Fe–Al catalysts with different metal loadings were analyzed using BET, XRD, H2-TPR, and FT-IR. An increase in the metal loading of the Co–Fe–Al catalysts showed low spinel phase ratio, leading to an improvement in reducibility. Among the catalysts, 40CFAl catalyst prepared at laboratory scale afforded the highest C2–C4 hydrocarbon time yield, and this catalyst was successfully reproduced at the pilot scale. The pelletized catalyst prepared at pilot scale showed high CO conversion (87.6%), high light hydrocarbon selectivity (CH4 59.3% and C2–C4 18.8%), and low byproduct amounts (C5+: 4.1% and CO2: 17.8%) under optimum conditions (space velocity: 4000 mL/g/h, 350 °C, and 20 bar). Full article
(This article belongs to the Special Issue Iron in Catalysis)
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11 pages, 3824 KiB  
Article
Solution Combustion Synthesis of Fe2O3-Based Catalyst for Ammonia Synthesis
by Binxiang Cai, Huazhang Liu and Wenfeng Han
Catalysts 2020, 10(9), 1027; https://doi.org/10.3390/catal10091027 - 7 Sep 2020
Cited by 12 | Viewed by 4500
Abstract
Fe2O3-based catalysts were prepared by solution combustion synthesis (SCS) with metal nitrates (Fe, K, Al, Ca) as the precursors and glycine as the fuel. The activities of catalysts were evaluated in terms of ammonia synthesis reaction rate in a [...] Read more.
Fe2O3-based catalysts were prepared by solution combustion synthesis (SCS) with metal nitrates (Fe, K, Al, Ca) as the precursors and glycine as the fuel. The activities of catalysts were evaluated in terms of ammonia synthesis reaction rate in a fixed bed reactor similar to the industrial reactors. The results indicate that the precursor of catalyst prepared by SCS is Fe2O3 which facilitates the high dispersion of promoters to provide high activity. The catalysts exhibit higher activity for ammonia synthesis than that of traditional catalysts, and the reaction rate reaches 138.5 mmol g−1 h−1. Fe2O3 prepared by SCS could be favorable precursor for ammonia synthesis catalyst. The present study provides a pathway to prepare catalyst for ammonia synthesis. Full article
(This article belongs to the Special Issue Iron in Catalysis)
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