The New Catalytic Processes in Alternative Fuel Production

A special issue of Catalysts (ISSN 2073-4344).

Deadline for manuscript submissions: closed (31 January 2021) | Viewed by 6241

Special Issue Editors


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Guest Editor
Institute of General and Ecological Chemistry, Lodz University of Technology, Zeromskiego 116, 90-924 Lodz, Poland
Interests: heterogeneous catalysis; chromatographic and electrochemical methods in environmental and biomedical applications

E-Mail Website
Guest Editor
Institute of General and Inorganic Chemistry, Lodz University of Technology, Zeromskiego 116, 90-924 Lodz, Poland
Interests: Heterogeneous catalysis, mechanism of chemical reaction, environmental protection, processes of fuel production: Fischer-Tropsch Synthesis, Biodiesel, BioJet

Special Issue Information

Dear Colleagues,

The nonrenewable sources of fossil fuels are running out, and their availability is limited. Moreover, about 98% of pollution emission comes from fossil fuel combustion. Reducing the use of fossil fuels could significantly improve the quality of our environment. This can be achieved by either using less energy or by replacing fossil fuel with renewable fuels. For this reason, alternative sources and processes of alternative fuel production are sought. However, the evaluation of alternative-fuel production should be considered from various aspects; for example, energy efficiency, emissions, technologies, costs, facilities, and so on. The present Special Issue will be focused on all catalytical processes which present new avenues for fuel production. We are seeking both reviews and research papers. Today, people are rediscovering the environmental and economic benefits of making fuel from alternative resources. Among these processes we can include catalytic processes such as Fischer–Tropsch synthesis, which is catalytically converted of syngas into liquid hydrocarbons, biodiesel and green diesel production or Bio-Jet fuel production—processes in which the biomass and vegetable oils are used as a source (substrate) in a wide spectrum of fuel production. In this Special Issue, hydrogen production is also of interest as a future fuel.

Prof. Dr. Jacek Rynkowski
Dr. Karolina Chalupka
Guest Editors

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Keywords

  • Fischer–Tropsch synthesis
  • hydrogen production
  • biodiesel
  • green diesel
  • Bio-Jet fuel production
  • aviation fuel
  • heterogeneous catalysts for fuel production

Published Papers (2 papers)

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Research

27 pages, 3453 KiB  
Article
Effect of Temperature on the Hydrotreatment of Sewage Sludge-Derived Pyrolysis Oil and Behavior of Ni-Based Catalyst
by Maria V. Alekseeva (Bykova), Olga A. Bulavchenko, Andrey A. Saraev, Anna M. Kremneva, Mikhail V. Shashkov, Olesya O. Zaikina, Yuliya K. Gulyaeva, Andrey N. Grachev, Oleg Kikhtyanin, David Kubička and Vadim A. Yakovlev
Catalysts 2020, 10(11), 1273; https://doi.org/10.3390/catal10111273 - 03 Nov 2020
Cited by 9 | Viewed by 2524
Abstract
The high-energy potential of wastewater sewage sludge (SS) produced in large amounts around the world makes it an attractive feedstock for fuels and energy sectors. Thermochemical valorization relying on pyrolysis of SS followed by hydrotreatment of pyrolysis oil (Py-SS) might even allow the [...] Read more.
The high-energy potential of wastewater sewage sludge (SS) produced in large amounts around the world makes it an attractive feedstock for fuels and energy sectors. Thermochemical valorization relying on pyrolysis of SS followed by hydrotreatment of pyrolysis oil (Py-SS) might even allow the integration of SS into existing oil refineries. In the present study, catalytic hydrotreatment of Py-SS was performed over a NiCuMo-P-SiO2 catalyst in a batch reactor at temperatures in the range of 200–390 °C. Due to sulfur presence in the feed, the increasing reaction temperature induced in situ transformation of metallic Ni into Ni3S2 in the catalyst. In contrast, the Ni3P active phase possessed remarkable stability even at the harshest reaction conditions. The oxygen content in the reaction products was decreased by 59%, while up to 52% of N and 89% of S were removed at 390 °C. The content of free fatty acids was greatly reduced by their conversion to n-alkanes, while the larger amount of volatile aromatics was generated from high molecular mass compounds. The quality of oil-derived products greatly changed at elevated temperatures, providing strong evidence of effective upgrading via decarboxy(ny)lation, hydrogenation, and hydrocracking transformations. Full article
(This article belongs to the Special Issue The New Catalytic Processes in Alternative Fuel Production)
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14 pages, 2185 KiB  
Article
High-Loaded Nickel Based Sol–Gel Catalysts for Methylcyclohexane Dehydrogenation
by Yuliya K. Gulyaeva, Maria V. Alekseeva (Bykova), Dmitry Yu. Ermakov, Olga A. Bulavchenko, Olesya O. Zaikina and Vadim A. Yakovlev
Catalysts 2020, 10(10), 1198; https://doi.org/10.3390/catal10101198 - 16 Oct 2020
Cited by 18 | Viewed by 3222
Abstract
Application of liquid organic hydrogen carriers, such as “methylcyclohexane (MCH)–toluene” chemical couple, is one of the promising approaches for hydrogen storage and transportation. In the present study, copper-modified nickel catalysts with high metal loading of 75 wt% were synthesized via heterophase sol–gel technique, [...] Read more.
Application of liquid organic hydrogen carriers, such as “methylcyclohexane (MCH)–toluene” chemical couple, is one of the promising approaches for hydrogen storage and transportation. In the present study, copper-modified nickel catalysts with high metal loading of 75 wt% were synthesized via heterophase sol–gel technique, and investigated in the dehydrogenation of MCH. Two approaches towards the copper introduction were applied. The catalyst samples prepared via wetness impregnation of the nickel sol–gel catalyst are characterized by more effective Ni-Cu interaction compared to those where two metals were introduced simultaneously by the mixing of their solid precursors. As a result, the “impregnated” catalysts revealed higher selectivity towards toluene. The addition of copper up to 30 wt% of total metal content was shown to increase significantly toluene selectivity and yield without a noticeable decrease in MCH conversion. The catalyst with the active component including 80 wt% of Ni and 20 wt% of Cu demonstrated 96% and 89% toluene selectivity at 40% and 80% MCH conversion, respectively. Based on the obtained data, this non-noble catalytic system appears quite promising for the MCH dehydrogenation. Full article
(This article belongs to the Special Issue The New Catalytic Processes in Alternative Fuel Production)
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