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      Effects of Mg, Ca, Sr, and Ba Dopants on the Performance of La 2O 3 Catalysts for the Oxidative Coupling of Methane

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          Abstract

          Oxidative coupling of methane (OCM) is a reaction to directly convert methane into high value-added hydrocarbons (C 2+) such as ethylene and ethane using molecular oxygen and a catalyst. This work investigated lanthanum oxide catalysts for OCM, which were promoted with alkaline-earth metal oxides (Mg, Ca, Sr, and Ba) and prepared by the solution-mixing method. The synthesized catalysts were characterized using X-ray powder diffraction, CO 2-programmed desorption, and X-ray photoelectron spectroscopy. The comparative performance of each promoter showed that promising lanthanum-loaded alkaline-earth metal oxide catalysts were La-Sr and La-Ba. In contrast, the combination of La with Ca or Mg did not lead to a clear improvement of C 2+ yield. The most promising LaSr50 catalyst exhibited the highest C 2+ yield of 17.2%, with a 56.0% C 2+ selectivity and a 30.9% CH 4 conversion. Catalyst characterization indicated that their activity was strongly associated with moderate basic sites and surface-adsorbed oxygen species of O 2 . Moreover, the catalyst was stable over 25 h at a reactor temperature of 700 °C.

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          Synthesis of ethylene via oxidative coupling of methane I. Determination of active catalysts

          G. Keller (1982)
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            Statistical Analysis of Past Catalytic Data on Oxidative Methane Coupling for New Insights into the Composition of High-Performance Catalysts

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              Catalytic Hydrogen Production from Methane: A Review on Recent Progress and Prospect

              Natural gas (Methane) is currently the primary source of catalytic hydrogen production, accounting for three quarters of the annual global dedicated hydrogen production (about 70 M tons). Steam–methane reforming (SMR) is the currently used industrial process for hydrogen production. However, the SMR process suffers with insufficient catalytic activity, low long-term stability, and excessive energy input, mostly due to the handling of large amount of CO2 coproduced. With the demand for anticipated hydrogen production to reach 122.5 M tons in 2024, novel and upgraded catalytic processes are desired for more effective utilization of precious natural resources. In this review, we summarized the major descriptors of catalyst and reaction engineering of the SMR process and compared the SMR process with its derivative technologies, such as dry reforming with CO2 (DRM), partial oxidation with O2, autothermal reforming with H2O and O2. Finally, we discussed the new progresses of methane conversion: direct decomposition to hydrogen and solid carbon and selective oxidation in mild conditions to hydrogen containing liquid organics (i.e., methanol, formic acid, and acetic acid), which serve as alternative hydrogen carriers. We hope this review will help to achieve a whole picture of catalytic hydrogen production from methane.
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                Author and article information

                Journal
                ACS Omega
                ACS Omega
                ao
                acsodf
                ACS Omega
                American Chemical Society
                2470-1343
                04 January 2022
                18 January 2022
                : 7
                : 2
                : 1785-1793
                Affiliations
                []Department of Chemical Engineering, Faculty of Engineering, Kasetsart University , Bangkok 10900, Thailand
                []Center of Excellence on Petrochemical and Materials Technology, Kasetsart University , Bangkok 10900, Thailand
                [§ ]Research Network of NANOTEC−KU on NanoCatalysts and NanoMaterials for Sustainable Energy and Environment, Kasetsart University , Bangkok 10900, Thailand
                []National Nanotechnology Center (NANOTEC), National Science and Technology Development Agency , Thailand Science Park, Khlong Luang, Pathum Thani 12120, Thailand
                []Department of Chemical Engineering, Kwangwoon University , Seoul 01897, Korea
                [# ]Institute of Materials Chemistry, TU Wien , Vienna 1060, Austria
                Author notes
                Author information
                https://orcid.org/0000-0002-4333-337X
                https://orcid.org/0000-0002-4724-0613
                https://orcid.org/0000-0002-4164-9397
                https://orcid.org/0000-0002-8040-1677
                https://orcid.org/0000-0001-8336-6590
                Article
                10.1021/acsomega.1c04738
                8771708
                35071872
                50fecbd7-3a6e-426e-bc20-3e0437c0c6a7
                © 2022 The Authors. Published by American Chemical Society

                Permits the broadest form of re-use including for commercial purposes, provided that author attribution and integrity are maintained ( https://creativecommons.org/licenses/by/4.0/).

                History
                : 30 August 2021
                : 22 December 2021
                Funding
                Funded by: Austrian Science Fund, doi 10.13039/501100002428;
                Award ID: F81-P08
                Funded by: Fundamental Fund, doi NA;
                Award ID: FF(KU)21.65
                Funded by: Center of Excellence on Petrochemical and Materials Technology, doi 10.13039/501100015625;
                Award ID: NA
                Funded by: Ministry of Science and Technology of Thailand, doi 10.13039/501100007275;
                Award ID: NA
                Funded by: National Nanotechnology Center, doi 10.13039/501100007056;
                Award ID: NA
                Funded by: Kasetsart University Research and Development Institute, doi 10.13039/501100005621;
                Award ID: NA
                Funded by: National Research Council of Thailand, doi 10.13039/501100004704;
                Award ID: NRCT5-RSA63002-11
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                ao1c04738
                ao1c04738

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