51
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Yeetsorn R, Tungkamani S, Maiket Y. Fabrication of a Ceramic Foam Catalyst Using Polymer Foam Scrap via the Replica Technique for Dry Reforming. ACS OMEGA 2022; 7:4202-4213. [PMID: 35155913 PMCID: PMC8829922 DOI: 10.1021/acsomega.1c05841] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Grants] [Track Full Text] [Download PDF] [Figures] [Subscribe] [Scholar Register] [Received: 10/18/2021] [Accepted: 01/18/2022] [Indexed: 06/14/2023]
Abstract
Megapores with spherical-like cells connected through windows and high porosities make up catalyst supports in the form of ceramic foams. These characteristics provide significant benefits for catalytic processes that are limited by mass or heat transport. This study focuses on the manufacture of ceramic foam using a polymeric sponge replica process and polymer foams as a template for catalyst supports, which are industrial waste from the packaging sector. To make ceramic foam catalysts, they were dipped in a catalyst solution, followed by a breakdown stage and a sintering process. Experiments focused on determinants that affect the desired characteristics of ceramic foams, such as the types of polymer foams that affect foam morphology, the rheology of catalyst solution that affects catalyst dispersion, and the polymer decomposition rate that affects catalytic performance during dry reforming of the methane process. The cell architectures of polyurethane and polyvinyl alcohol foams are attractive for catalyst support preparation because they have 98-99% porosity and typical cell sizes of 200 and 50 μm, respectively. The polyurethane performance was superior to the performance of polyvinyl alcohol in terms of higher porosity and better catalytic-solution absorption offering high catalyst active areas. The catalyst prepared from concentrated 10 wt % Ni/Al2O3-MgO (10NAM) slurry had the highest surface area (59.18 m2/g) and the highest metal oxide dispersion (5.65%). These results are relevant to the flow behavior of catalyst slurry which plays a key role in coating the catalyst gel on the polymer template. The thermal decomposition rate used to remove the polymer template from the catalyst structure is proportional to the ceramic foam structure (catalyst support structure). The slow decomposition rate bent and fractured foam-cell struts more than the faster rate. On the other hand, achieving good catalyst dispersion on catalyst supports necessitated a high sintering rate. When sintering was adjusted at a high sintering rate, the metal-particle dispersion was relatively high, around 7.44%, and the surface area of ceramic foam catalysts was 64.61 m2/g. Finally, the catalytic behavior toward hydrogen production through the dry reforming of methane using a fixed-bed reactor was evaluated under certain operating conditions.
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Affiliation(s)
- Rungsima Yeetsorn
- The
Sirindhorn International Thai-German Graduate School of Engineering, King Mongkut’s University of Technology North
Bangkok, Bangkok 10800, Thailand
| | - Sabaithip Tungkamani
- Research
and Development Center for Chemical Engineering Unit Operation and
Catalyst Design (RCC), King Mongkut’s
University of Technology North Bangkok, Bangkok 10800, Thailand
| | - Yaowaret Maiket
- Thai-French
Innovation Institute, King Mongkut’s
University of Technology North Bangkok, Bangkok 10800, Thailand
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52
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Mantripragada HC, Veser G. Hydrogen Production via Chemical Looping Dry Reforming of Methane: Process Modeling and Systems Analysis. AIChE J 2022. [DOI: 10.1002/aic.17612] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/08/2022]
Affiliation(s)
- Hari C. Mantripragada
- Department of Chemical and Petroleum Engineering Swanson School of Engineering, University of Pittsburgh Pittsburgh Pennsylvania USA
| | - Götz Veser
- Department of Chemical and Petroleum Engineering Swanson School of Engineering, University of Pittsburgh Pittsburgh Pennsylvania USA
- Center for Energy University of Pittsburgh Pittsburgh Pennsylvania USA
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53
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Alioui O, Badawi M, Erto A, Amin MA, Tirth V, Jeon BH, Islam S, Balsamo M, Virginie M, Ernst B, Benguerba Y. Contribution of DFT to the optimization of Ni-based catalysts for dry reforming of methane: a review. CATALYSIS REVIEWS 2022. [DOI: 10.1080/01614940.2021.2020518] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.5] [Reference Citation Analysis] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 10/19/2022]
Affiliation(s)
- Oualid Alioui
- Laboratoire de génie des procédés chimiques, LGPC, Université Ferhat ABBAS Sétif-1 19000 Sétif, Algeria
| | - Michael Badawi
- Laboratoire de Physique et Chimie Théoriques, UMR CNRS 7019, Université de Lorraine, 54000 Nancy, France
| | - Alessandro Erto
- Dipartimento di Ingegneria Chimica, dei Materiali e Università degli Studi di Napoli, P.leTecchio, 80, 80125, Napoli, Italy
| | - Mohammed A. Amin
- Department of Chemistry, College of Science, Taif University, Taif 21944, Saudi Arabia
| | - Vineet Tirth
- Mechanical Engineering Department, College of Engineering, King Khalid University, Abha 61411, Asir, Kingdom of Saudi Arabia
- Research Center for Advanced Materials Science (RCAMS), King Khalid University Guraiger, Abha, Asir, Kingdom of Saudi Arabia
| | - Byong-Hun Jeon
- Department of Earth Resources and Environmental Engineering, Hanyang University, Seoul, 04763, Republic of Korea
| | - Saiful Islam
- Civil Engineering Department, College of Engineering, King Khalid University, Abha-61411, Asir, Kingdom of Saudi Arabia
| | - Marco Balsamo
- Dipartimento di Scienze Chimiche, Università degli Studi di Napoli Federico II, Complesso Universitario di Monte Sant’Angelo, 80126 Napoli, Italy
| | - Mirella Virginie
- Univ. Lille, CNRS, Centrale Lille, ENSCL, Uni. Artois, UMR 8181 –UCCS – Unité de Catalyse et de Chimie du Solide, F-59000 Lille, France
| | - Barbara Ernst
- Université de Strasbourg, CNRS, IPHC UMR 7178, Laboratoire de Reconnaissance et Procédés de Séparation Moléculaire (RePSeM), ECPM 25 rue Becquerel, Université de Strasbourg, Strasbourg, France
| | - Yacine Benguerba
- Department of Chemistry, College of Science, Taif University, Taif 21944, Saudi Arabia
- Department of process engineering, Faculty of Technology, Ferhat ABBAS Sétif 1 University, 19000 Setif, Algeria
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54
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Agueniou F, Vidal H, Yeste MP, Hernández-Garrido JC, Cauqui MA, Rodríguez-Izquierdo JM, Calvino JJ, Gatica JM. Honeycomb monolithic design to enhance the performance of Ni-based catalysts for dry reforming of methane. Catal Today 2022. [DOI: 10.1016/j.cattod.2020.07.030] [Citation(s) in RCA: 3] [Impact Index Per Article: 1.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/02/2022]
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55
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Torimoto M, Sekine Y. Effects of alloying for steam or dry reforming of methane: a review of recent studies. Catal Sci Technol 2022. [DOI: 10.1039/d2cy00066k] [Citation(s) in RCA: 5] [Impact Index Per Article: 2.5] [Reference Citation Analysis] [Abstract] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/21/2022]
Abstract
A survey on the catalytic nature of Ni-based alloy catalysts in recent years provides a direction for future catalyst development.
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Affiliation(s)
- Maki Torimoto
- Applied Chemistry, Waseda University, 3-4-1, Okubo, Shinjuku, Tokyo 169-8555, Japan
| | - Yasushi Sekine
- Applied Chemistry, Waseda University, 3-4-1, Okubo, Shinjuku, Tokyo 169-8555, Japan
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56
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Wasantwisut S, Xiao Y, Feng P, Gilliard-AbdulAziz KL. The Influence of High-Energy Faceted TiO2 Supports on Co and Co-Ru Catalysts for Dry Methane Reforming. Chem Asian J 2021; 17:e202101253. [PMID: 34936730 DOI: 10.1002/asia.202101253] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Key Words] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Received: 11/03/2021] [Revised: 12/18/2021] [Indexed: 11/09/2022]
Abstract
The reforming of methane from biogas has been proposed as a promising method of CO2 utilization. Co-based catalysts are promising candidates for dry methane reforming. However, the main constraints limiting the large-scale use of Co-based catalysts are deactivation through carbon deposition (coking) and sintering due to weak metal-support interaction. We studied the structure-function properties and catalytic behavior of Co/TiO2 and Co-Ru/TiO2 catalysts using two different types of TiO2 supports, commercial TiO2 and faceted non-stoichiometric rutile TiO2 crystals (TiO2*). The Co and Ru metal particles were deposited on TiO2 supports using a wet-impregnation method with the percentage weight loading of Co and Ru of 5% and 0.5%, respectively. The materials were characterized using SEM, STEM-HAADF, XRD, XPS and BET. The catalytic performance was studied using the CH4:CO2 ratio of 3:2 to mimic the methane-rich biogas composition. Our results indicate that the addition of Ru to Co catalysts supported on TiO2* reduces carbon deposition and influences oxygen mobility. Co and Co-Ru catalysts supported on TiO2* has superior activity with the highest conversion of CO2 and CH4 of 34.7% and 23.5%, respectively. Despite the improved performance, the Co-Ru/TiO2* catalyst has limited stability due to the proliferation of nanoparticle growth and TiOx layers on the surface of the nanoparticles indicating the prevalence of the strong-metal support interaction.
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Affiliation(s)
- Somchate Wasantwisut
- University of California Riverside, Chemical and Environmental Engineering, UNITED STATES
| | - Yuchen Xiao
- University of California Riverside, Chemistry, UNITED STATES
| | - Pingyun Feng
- University of California Riverside, Chemistry, UNITED STATES
| | - Kandis Leslie Gilliard-AbdulAziz
- University of California, Riverside, Chemical and Environmental Engineering, A211 Bourns Hall, 900 University Ave, 92508, Riverside, UNITED STATES
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57
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Andrade Schaffner R, Schwengber CA, Kowalski RL, Assis NSG, Domingues RCPR, Yamamoto CI, Alves HJ. Dry reforming of methane: Effect of different calcination temperatures of
Al
2
O
3
and
Mg‐Al
2
O
3
supports on Ni catalysts. CAN J CHEM ENG 2021. [DOI: 10.1002/cjce.24333] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/09/2022]
Affiliation(s)
- Rodolfo Andrade Schaffner
- Laboratório de Materiais e Energias Renováveis (LABMATER) Universidade Federal do Paraná (UFPR‐Setor Palotina), R. Pioneiro, 2153, Jardim Dallas, 85950‐000 Palotina PR Brazil
| | - Carine Aline Schwengber
- Laboratório de Materiais e Energias Renováveis (LABMATER) Universidade Federal do Paraná (UFPR‐Setor Palotina), R. Pioneiro, 2153, Jardim Dallas, 85950‐000 Palotina PR Brazil
| | - Rafaela Luisa Kowalski
- Laboratório de Materiais e Energias Renováveis (LABMATER) Universidade Federal do Paraná (UFPR‐Setor Palotina), R. Pioneiro, 2153, Jardim Dallas, 85950‐000 Palotina PR Brazil
| | - Natalie Souto Gonçalves Assis
- Laboratório de Materiais e Energias Renováveis (LABMATER) Universidade Federal do Paraná (UFPR‐Setor Palotina), R. Pioneiro, 2153, Jardim Dallas, 85950‐000 Palotina PR Brazil
| | - Roberta Carolina Pelissari Rizzo Domingues
- Laboratório de Adsorventes e Catalisadores (LAdCat) Universidade Tecnológica Federal do Paraná (UTFPR ‐ Campus Curitiba), Av. Sete de Setembro, 3165, Rebouças, 80230‐901 Curitiba PR Brazil
| | - Carlos Itsuo Yamamoto
- Laboratório de Análises de Combustíveis Automotivos (LACAUT) Universidade Federal do Paraná (UFPR‐Centro Politécnico), Jardim das Américas, 81531‐980 Curitiba PR Brazil
| | - Helton José Alves
- Laboratório de Materiais e Energias Renováveis (LABMATER) Universidade Federal do Paraná (UFPR‐Setor Palotina), R. Pioneiro, 2153, Jardim Dallas, 85950‐000 Palotina PR Brazil
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58
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Lyu Y, Xu R, Williams O, Wang Z, Sievers C. Reaction paths of methane activation and oxidation of surface intermediates over NiO on Ceria-Zirconia catalysts studied by In-situ FTIR spectroscopy. J Catal 2021. [DOI: 10.1016/j.jcat.2021.10.004] [Citation(s) in RCA: 5] [Impact Index Per Article: 1.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/24/2022]
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59
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Akansu H, Arbag H, Tasdemir HM, Yasyerli S, Yasyerli N, Dogu G. Nickel-based alumina supported catalysts for dry reforming of biogas in the absence and the presence of H2S: Effect of manganese incorporation. Catal Today 2021. [DOI: 10.1016/j.cattod.2021.12.012] [Citation(s) in RCA: 2] [Impact Index Per Article: 0.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/30/2022]
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60
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Czaplicka N, Rogala A, Wysocka I. Metal (Mo, W, Ti) Carbide Catalysts: Synthesis and Application as Alternative Catalysts for Dry Reforming of Hydrocarbons-A Review. Int J Mol Sci 2021; 22:12337. [PMID: 34830220 PMCID: PMC8617837 DOI: 10.3390/ijms222212337] [Citation(s) in RCA: 4] [Impact Index Per Article: 1.3] [Reference Citation Analysis] [Abstract] [Key Words] [MESH Headings] [Grants] [Track Full Text] [Download PDF] [Figures] [Journal Information] [Subscribe] [Scholar Register] [Received: 10/22/2021] [Revised: 11/08/2021] [Accepted: 11/11/2021] [Indexed: 11/24/2022] Open
Abstract
Dry reforming of hydrocarbons (DRH) is a pro-environmental method for syngas production. It owes its pro-environmental character to the use of carbon dioxide, which is one of the main greenhouse gases. Currently used nickel catalysts on oxide supports suffer from rapid deactivation due to sintering of active metal particles or the deposition of carbon deposits blocking the flow of gases through the reaction tube. In this view, new alternative catalysts are highly sought after. Transition metal carbides (TMCs) can potentially replace traditional nickel catalysts due to their stability and activity in DR processes. The catalytic activity of carbides results from the synthesis-dependent structural properties of carbides. In this respect, this review presents the most important methods of titanium, molybdenum, and tungsten carbide synthesis and the influence of their properties on activity in catalyzing the reaction of methane with carbon dioxide.
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Affiliation(s)
| | | | - Izabela Wysocka
- Department of Process Engineering and Chemical Technology, Faculty of Chemistry, Gdansk University of Technology, Narutowicza 11/12 St., 80-233 Gdansk, Poland; (N.C.); (A.R.)
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61
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Contribution of Oxide Supports in Nickel-Based Catalytic Elimination of Greenhouse Gases and Generation of Syngas. ENERGIES 2021. [DOI: 10.3390/en14217324] [Citation(s) in RCA: 3] [Impact Index Per Article: 1.0] [Reference Citation Analysis] [Abstract] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 12/30/2022]
Abstract
Carbon dioxide and/or dry methane reforming serves as an effective pathway to mitigate these greenhouse gases. This work evaluates different oxide supports including alumina, Y-zeolite and H-ZSM-5 zeolite for the catalysis of dry reforming methane with Nickel (Ni). The composite catalysts were prepared by impregnating the supports with Ni (5%) and followed by calcination. The zeolite supported catalysts exhibited more reducibility and basicity compared to the alumina supported catalysts, this was assessed with temperature programmed reduction using hydrogen and desorption using carbon dioxide. The catalytic activity, in terms of CH4 conversion, indicated that 5 wt% Ni supported on alumina exhibited higher CH4 conversion (80.5%) than when supported on Y-zeolite (71.8%) or H-ZSM-5 (78.5%). In contrast, the H-ZSM-5 catalyst led to higher CO2 conversion (87.3%) than Y-zeolite (68.4%) and alumina (83.9%) supported catalysts. The stability tests for 9 h time-on-stream showed that Ni supported with H-ZSM-5 had less deactivation (just 2%) due to carbon deposition. The characterization of spent catalysts using temperature programmed oxidation (O2-TPO), X-ray diffraction (XRD) and thermo-gravimetric analysis (TGA) revealed that carbon deposition was a main cause of deactivation and that it occurred in the lowest degree on the Ni H-ZSM-5 catalyst.
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62
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Kim KH, You YW, Jeong MH, Jung BG, Im M, Kim YJ, Heo I, Chang TS, Lee JH. Influence of support acidity on CO2 reforming of ethane at high temperature. J CO2 UTIL 2021. [DOI: 10.1016/j.jcou.2021.101713] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/20/2022]
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63
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Franz R, Pinto D, Uslamin EA, Urakawa A, Pidko EA. Impact of Promoter Addition on the Regeneration of Ni/Al
2
O
3
Dry Reforming Catalysts. ChemCatChem 2021. [DOI: 10.1002/cctc.202101080] [Citation(s) in RCA: 2] [Impact Index Per Article: 0.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/06/2022]
Affiliation(s)
- Robert Franz
- Inorganic Systems Engineering Group Chemical Engineering Department Delft University of Technology Van der Maasweg 9 2629 HZ Delft The Netherlands
| | - Donato Pinto
- Catalysis Engineering Chemical Engineering Department Delft University of Technology Van der Maasweg 9 2629 HZ Delft The Netherlands
| | - Evgeny A. Uslamin
- Inorganic Systems Engineering Group Chemical Engineering Department Delft University of Technology Van der Maasweg 9 2629 HZ Delft The Netherlands
- TsyfroCatLab Group University of Tyumen Volodarskogo St.6 625003 Tyumen Russia
| | - Atsushi Urakawa
- Catalysis Engineering Chemical Engineering Department Delft University of Technology Van der Maasweg 9 2629 HZ Delft The Netherlands
| | - Evgeny A. Pidko
- Inorganic Systems Engineering Group Chemical Engineering Department Delft University of Technology Van der Maasweg 9 2629 HZ Delft The Netherlands
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64
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Naikoo GA, Arshad F, Hassan IU, Tabook MA, Pedram MZ, Mustaqeem M, Tabassum H, Ahmed W, Rezakazemi M. Thermocatalytic Hydrogen Production Through Decomposition of Methane-A Review. Front Chem 2021; 9:736801. [PMID: 34765584 PMCID: PMC8576817 DOI: 10.3389/fchem.2021.736801] [Citation(s) in RCA: 6] [Impact Index Per Article: 2.0] [Reference Citation Analysis] [Abstract] [Key Words] [Track Full Text] [Download PDF] [Figures] [Journal Information] [Subscribe] [Scholar Register] [Received: 07/05/2021] [Accepted: 10/06/2021] [Indexed: 11/26/2022] Open
Abstract
Consumption of fossil fuels, especially in transport and energy-dependent sectors, has led to large greenhouse gas production. Hydrogen is an exciting energy source that can serve our energy purposes and decrease toxic waste production. Decomposition of methane yields hydrogen devoid of COx components, thereby aiding as an eco-friendly approach towards large-scale hydrogen production. This review article is focused on hydrogen production through thermocatalytic methane decomposition (TMD) for hydrogen production. The thermodynamics of this approach has been highlighted. Various methods of hydrogen production from fossil fuels and renewable resources were discussed. Methods including steam methane reforming, partial oxidation of methane, auto thermal reforming, direct biomass gasification, thermal water splitting, methane pyrolysis, aqueous reforming, and coal gasification have been reported in this article. A detailed overview of the different types of catalysts available, the reasons behind their deactivation, and their possible regeneration methods were discussed. Finally, we presented the challenges and future perspectives for hydrogen production via TMD. This review concluded that among all catalysts, nickel, ruthenium and platinum-based catalysts show the highest activity and catalytic efficiency and gave carbon-free hydrogen products during the TMD process. However, their rapid deactivation at high temperatures still needs the attention of the scientific community.
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Affiliation(s)
- Gowhar A. Naikoo
- Department of Mathematics and Sciences, College of Arts and Applied Sciences, Dhofar University, Salalah, Oman
| | - Fareeha Arshad
- Department of Biochemistry, Aligarh Muslim University, Aligarh, India
| | | | - Musallam A. Tabook
- Department of Mathematics and Sciences, College of Arts and Applied Sciences, Dhofar University, Salalah, Oman
| | - Mona Z. Pedram
- Mechanical Engineering-Energy Division, K. N. Toosi University of Technology, Tehran, Iran
| | - Mujahid Mustaqeem
- Institute of Physics, Academia Sinica, Taipei, Taiwan
- Department of Chemistry, National Taiwan University, Taipei, Taiwan
| | - Hassina Tabassum
- Department of Chemical and Biological Engineering, State University of New York at Buffalo, Buffalo, NY, United States
| | - Waqar Ahmed
- School of Mathematics and Physics, College of Science, University of Lincoln, Lincoln, United Kingdom
| | - Mashallah Rezakazemi
- School of Mathematics and Physics, College of Science, University of Lincoln, Lincoln, United Kingdom
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65
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66
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Ćwieka K, Czelej K, Colmenares JC, Jabłczyńska K, Werner Ł, Gradoń L. Supported Plasmonic Nanocatalysts for Hydrogen Production by Wet and Dry Photoreforming of Biomass and Biogas Derived Compounds: Recent Progress and Future Perspectives. ChemCatChem 2021. [DOI: 10.1002/cctc.202101006] [Citation(s) in RCA: 6] [Impact Index Per Article: 2.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/11/2022]
Affiliation(s)
- Karol Ćwieka
- Faculty of Chemical and Process Engineering Warsaw University of Technology L. Warynskiego 1 00645 Warsaw Poland
- Faculty of Materials Science and Engineering Warsaw University of Technology Woloska 141 02507 Warsaw Poland
| | - Kamil Czelej
- Department of Complex System Modeling Institute of Theoretical Physics Faculty of Physics University of Warsaw Pasteura 5 02093 Warszawa Poland
| | - Juan Carlos Colmenares
- Institute of Physical Chemistry Polish Academy of Sciences Kasprzaka 44/52 01224 Warsaw Poland
| | - Katarzyna Jabłczyńska
- Faculty of Chemical and Process Engineering Warsaw University of Technology L. Warynskiego 1 00645 Warsaw Poland
| | - Łukasz Werner
- Faculty of Chemical and Process Engineering Warsaw University of Technology L. Warynskiego 1 00645 Warsaw Poland
| | - Leon Gradoń
- Faculty of Chemical and Process Engineering Warsaw University of Technology L. Warynskiego 1 00645 Warsaw Poland
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67
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Highly active and coke resistant Ni/CeZrO2 catalyst prepared by cold plasma decomposition for CO2 reforming of methane. J CO2 UTIL 2021. [DOI: 10.1016/j.jcou.2021.101647] [Citation(s) in RCA: 9] [Impact Index Per Article: 3.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 12/12/2022]
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68
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Wang Y, Wang Y, Li L, Cui C, Liu X, Da. Costa P, Hu C. Syngas Production via CO 2 Reforming of Methane over Aluminum-Promoted NiO-10Al 2O 3-ZrO 2 Catalyst. ACS OMEGA 2021; 6:22383-22394. [PMID: 34497927 PMCID: PMC8412958 DOI: 10.1021/acsomega.1c03174] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Grants] [Track Full Text] [Download PDF] [Figures] [Subscribe] [Scholar Register] [Received: 06/17/2021] [Accepted: 08/09/2021] [Indexed: 06/13/2023]
Abstract
CO2 reforming of methane was studied at medium temperature (700 °C) using a GSHV of 48,000 h-1 over nickel catalysts supported on ZrO2 promoted by alumina. The catalysts were prepared by a one-step synthesis method and characterized by BET, H2-TPR, XRD, XPS, TEM, Raman spectroscopy, and TGA. The NiO-10Al2O3-ZrO2 catalyst exhibited higher catalytic performance in comparison with the NiO-ZrO2 catalyst. The enhancement of catalytic activity in dry reforming could be associated with the alterations in surface properties due to Al promotion. First, the Al promoter could modify the structure of ZrO2, leading to an increase of its pore volume and pore diameter. Second, the NiO-10Al2O3-ZrO2 catalyst exhibited high resistance to sintering. Third, the NiO-10Al2O3-ZrO2 catalyst showed high suppression to the loss of nickel during a long-term catalytic test. Finally, the addition of Al could inhibit the reduction of ZrO2 during the reduction and reaction, endowing further the stability.
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Affiliation(s)
- Ye Wang
- College
of Chemical Engineering, Sichuan University, Chengdu, Sichuan 610065, P. R. China
- Sorbonne
Université, Institut Jean Le Rond d’Alembert,
CNRS, 2 Place de la Gare de Ceinture, Saint-Cyr-L’Ecole 78210, France
| | - Yannan Wang
- Key
Laboratory of Green Chemistry and Technology, Ministry of Education,
College of Chemistry, Sichuan University, Chengdu, Sichuan 610064, P. R. China
| | - Li Li
- Key
Laboratory of Green Chemistry and Technology, Ministry of Education,
College of Chemistry, Sichuan University, Chengdu, Sichuan 610064, P. R. China
| | - Chaojun Cui
- College
of Chemical Engineering, Sichuan University, Chengdu, Sichuan 610065, P. R. China
| | - Xudong Liu
- Key
Laboratory of Green Chemistry and Technology, Ministry of Education,
College of Chemistry, Sichuan University, Chengdu, Sichuan 610064, P. R. China
| | - Patrick Da. Costa
- Sorbonne
Université, Institut Jean Le Rond d’Alembert,
CNRS, 2 Place de la Gare de Ceinture, Saint-Cyr-L’Ecole 78210, France
| | - Changwei Hu
- College
of Chemical Engineering, Sichuan University, Chengdu, Sichuan 610065, P. R. China
- Key
Laboratory of Green Chemistry and Technology, Ministry of Education,
College of Chemistry, Sichuan University, Chengdu, Sichuan 610064, P. R. China
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69
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Yang M, Wang Y, Zhang R, Liu T, Xia L, Chen Z, Fang X, Xu X, Xu J, Wang X. Ni/LaBO3 (B = Al, Cr, Fe) Catalysts for Steam Reforming of Methane (SRM): On the Interaction Between Ni and LaBO3 Perovskites with Differed Fine Structures. CATALYSIS SURVEYS FROM ASIA 2021. [DOI: 10.1007/s10563-021-09343-7] [Citation(s) in RCA: 5] [Impact Index Per Article: 1.7] [Reference Citation Analysis] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 11/28/2022]
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70
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Pantaleo G, Parola VL, Testa ML, Venezia AM. CO 2 Reforming of CH 4 over SiO 2-Supported Ni Catalyst: Effect of Sn as Support and Metal Promoter. Ind Eng Chem Res 2021. [DOI: 10.1021/acs.iecr.1c02193] [Citation(s) in RCA: 6] [Impact Index Per Article: 2.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/28/2022]
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71
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Glotov A, Vutolkina A, Pimerzin A, Vinokurov V, Lvov Y. Clay nanotube-metal core/shell catalysts for hydroprocesses. Chem Soc Rev 2021; 50:9240-9277. [PMID: 34241609 DOI: 10.1039/d1cs00502b] [Citation(s) in RCA: 18] [Impact Index Per Article: 6.0] [Reference Citation Analysis] [Abstract] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 12/16/2022]
Abstract
Catalytic hydroprocesses play a significant role in oil refining and petrochemistry. The tailored design of new metal nanosystems and optimization of their support, composition, and structure is a prospective strategy for enhancing the efficiency of catalysts. Mesoporous support impacts the active component by binding it to the surface, which leads to the formation of tiny highly dispersed catalytic particles stabilized from aggregation and with minimized leaching. The structural and acidic properties of the support are crucial and determine the size and dispersion of the active metal phase. Currently, research efforts are shifted toward the design of nanoscale porous materials, where homogeneous catalysts are displaced by heterogeneous. Ceramic materials, such as 50 nm diameter natural halloysite nanotubes, are of special interest for this. Much attention to halloysite clay is due to its tubular structure with a hollow 10-15 nm diameter internal cavity, textural characteristics, and different chemical compositions of the outer/inner surfaces, allowing selective nanotube modification. Loading halloysite with metal particles or placing them outside the tubes provides stable and efficient mesocatalysts. The low cost of this abundant nanoclay makes it a good choice for the scaled-up architectural design of core-shell catalysts, containing active metal sites (Au, Ag, Pt, Ru, Co, Mo, Fe2O3, CdS, CdZnS, Cu-Ni) located inside or outside the tubular template. These alumosilicate nanotubes are environment-friendly and are available in thousands of tons. Herein, we summarized the advances of halloysite-based composite materials for hydroprocesses, focusing on the selective binding of metal particles. We analyze the tubes' morphology adjustments and size selection, the physicochemical properties of pristine and modified halloysite (e.g., acid-etched or silanized), the methods of metal clusters formation, and their localization. We indicate prospective routes for the architectural design of stable and efficient nanocatalysts based on this safe and natural clay material.
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Affiliation(s)
- Aleksandr Glotov
- Gubkin Russian State University of Oil and Gas (NRU), 65 Leninsky Prospekt, Moscow, 119991, Russia.
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Kim S, Lauterbach J, Sasmaz E. Yolk–Shell Pt-NiCe@SiO 2 Single-Atom-Alloy Catalysts for Low-Temperature Dry Reforming of Methane. ACS Catal 2021. [DOI: 10.1021/acscatal.1c01223] [Citation(s) in RCA: 18] [Impact Index Per Article: 6.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 12/18/2022]
Affiliation(s)
- Sunkyu Kim
- Department of Chemical and Biomolecular Engineering, University of California, Irvine, Irvine, California 92697, United States
| | - Jochen Lauterbach
- Smartstate Center for Strategic Approaches to the Generation of Electricity (SAGE), Department of Chemical Engineering, University of South Carolina, Columbia, South Carolina 29208, United States
| | - Erdem Sasmaz
- Department of Chemical and Biomolecular Engineering, University of California, Irvine, Irvine, California 92697, United States
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74
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Hydrogen Yield from CO2 Reforming of Methane: Impact of La2O3 Doping on Supported Ni Catalysts. ENERGIES 2021. [DOI: 10.3390/en14092412] [Citation(s) in RCA: 3] [Impact Index Per Article: 1.0] [Reference Citation Analysis] [Abstract] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 11/17/2022]
Abstract
Development of a transition metal based catalyst aiming at concomitant high activity and stability attributed to distinguished catalytic characteristics is considered as the bottleneck for dry reforming of methane (DRM). This work highlights the role of modifying zirconia (ZrO2) and alumina (Al2O3) supported nickel based catalysts using lanthanum oxide (La2O3) varying from 0 to 20 wt% during dry reforming of methane. The mesoporous catalysts with improved BET surface areas, improved dispersion, relatively lower reduction temperatures and enhanced surface basicity are identified after La2O3 doping. These factors have influenced the catalytic activity and higher hydrogen yields are found for La2O3 modified catalysts as compared to base catalysts (5 wt% Ni-ZrO2 and 5 wt% Ni-Al2O3). Post-reaction characterizations such as TGA have showed less coke formation over La2O3 modified samples. Raman spectra indicates decreased graphitization for La2O3 catalysts. The 5Ni-10La2O3-ZrO2 catalyst produced 80% hydrogen yields, 25% more than that of 5Ni-ZrO2. 5Ni-15La2O3-Al2O3 gave 84% hydrogen yields, 8% higher than that of 5Ni-Al2O3. Higher CO2 activity improved the surface carbon oxidation rate. From the study, the extent of La2O3 loading is dependent on the type of oxide support.
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Shi C, Wang S, Ge X, Deng S, Chen B, Shen J. A review of different catalytic systems for dry reforming of methane: Conventional catalysis-alone and plasma-catalytic system. J CO2 UTIL 2021. [DOI: 10.1016/j.jcou.2021.101462] [Citation(s) in RCA: 27] [Impact Index Per Article: 9.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 01/18/2023]
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76
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Kweon S, An H, Shin CH, Park MB, Min HK. Nitrided Ni/N-zeolites as efficient catalysts for the dry reforming of methane. J CO2 UTIL 2021. [DOI: 10.1016/j.jcou.2021.101478] [Citation(s) in RCA: 4] [Impact Index Per Article: 1.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/22/2022]
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77
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Martin-del-Campo J, Uceda M, Coulombe S, Kopyscinski J. Plasma-catalytic dry reforming of methane over Ni-supported catalysts in a rotating gliding arc – Spouted bed reactor. J CO2 UTIL 2021. [DOI: 10.1016/j.jcou.2021.101474] [Citation(s) in RCA: 6] [Impact Index Per Article: 2.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/22/2022]
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78
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Abd El-Hafiz DR, Sakr AAE, Ebiad MA. Methane Bi-reforming for direct ethanol production over smart Cu/Mn- ferrite catalysts. RENEWABLE ENERGY 2021; 167:236-247. [DOI: 10.1016/j.renene.2020.11.078] [Citation(s) in RCA: 3] [Impact Index Per Article: 1.0] [Reference Citation Analysis] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 09/02/2023]
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79
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Gerelt-Od B, Kim J, Shin E, Kang H, Kim N, Jo C, Son H, Yoon S. In situ Raman investigation of resting thermal effects on gas emission in charged commercial 18650 lithium ion batteries. J IND ENG CHEM 2021. [DOI: 10.1016/j.jiec.2021.01.039] [Citation(s) in RCA: 4] [Impact Index Per Article: 1.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/28/2022]
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80
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Nickel Phosphide Catalysts as Efficient Systems for CO2 Upgrading via Dry Reforming of Methane. Catalysts 2021. [DOI: 10.3390/catal11040446] [Citation(s) in RCA: 14] [Impact Index Per Article: 4.7] [Reference Citation Analysis] [Abstract] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/16/2022] Open
Abstract
This work establishes the primordial role played by the support’s nature when aimed at the constitution of Ni2P active phases for supported catalysts. Thus, carbon dioxide reforming of methane was studied over three novel Ni2P catalysts supported on Al2O3, CeO2 and SiO2-Al2O3 oxides. The catalytic performance, shown by the catalysts’ series, decreased according to the sequence: Ni2P/Al2O3 > Ni2P/CeO2 > Ni2P/SiO2-Al2O3. The depleted CO2 conversion rates discerned for the Ni2P/SiO2-Al2O3 sample were associated to the high sintering rates, large amounts of coke deposits and lower fractions of Ni2P constituted in the catalyst surface. The strong deactivation issues found for the Ni2P/CeO2 catalyst, which also exhibited small amounts of Ni2P species, were majorly associated to Ni oxidation issues. Along with lower surface areas, oxidation reactions might also affect the catalytic behaviour exhibited by the Ni2P/CeO2 sample. With the highest conversion rate and optimal stabilities, the excellent performance depicted by the Ni2P/Al2O3 catalyst was mostly related to the noticeable larger fractions of Ni2P species established.
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81
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Ugwu A, Zaabout A, Donat F, van Diest G, Albertsen K, Müller C, Amini S. Combined Syngas and Hydrogen Production using Gas Switching Technology. Ind Eng Chem Res 2021; 60:3516-3531. [PMID: 33840889 PMCID: PMC8033639 DOI: 10.1021/acs.iecr.0c04335] [Citation(s) in RCA: 6] [Impact Index Per Article: 2.0] [Reference Citation Analysis] [Abstract] [Track Full Text] [Download PDF] [Figures] [Journal Information] [Subscribe] [Scholar Register] [Received: 09/03/2020] [Revised: 02/18/2021] [Accepted: 02/18/2021] [Indexed: 11/30/2022]
Abstract
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This paper focuses
on the experimental demonstration of a three-stage
GST (gas switching technology) process (fuel, steam/CO2, and air stages) for syngas production from methane in the fuel
stage and H2/CO production in the steam/CO2 stage
using a lanthanum-based oxygen carrier (La0.85Sr0.15Fe0.95Al0.05O3). Experiments were
performed at temperatures between 750–950 °C and pressures
up to 5 bar. The results show that the oxygen carrier exhibits high
selectivity to oxidizing methane to syngas at the fuel stage with
improved process performance with increasing temperature although
carbon deposition could not be avoided. Co-feeding CO2 with
CH4 at the fuel stage reduced carbon deposition significantly,
thus reducing the syngas H2/CO molar ratio from 3.75 to
1 (at CO2/CH4 ratio of 1 at 950 °C and
1 bar). The reduced carbon deposition has maximized the purity of
the H2 produced in the consecutive steam stage thus increasing
the process attractiveness for the combined production of syngas and
pure hydrogen. Interestingly, the cofeeding of CO2 with
CH4 at the fuel stage showed a stable syngas production
over 12 hours continuously and maintained the H2/CO ratio
at almost unity, suggesting that the oxygen carrier was exposed to
simultaneous partial oxidation of CH4 with the lattice
oxygen which was restored instantly by the incoming CO2. Furthermore, the addition of steam to the fuel stage could tune
up the H2/CO ratio beyond 3 without carbon deposition at
H2O/CH4 ratio of 1 at 950 °C and 1 bar;
making the syngas from gas switching partial oxidation suitable for
different downstream processes, for example, gas-to-liquid processes.
The process was also demonstrated at higher pressures with over 70%
fuel conversion achieved at 5 bar and 950 °C.
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Affiliation(s)
- Ambrose Ugwu
- Department of Energy and Process Engineering, Norwegian University of Science and Technology, Trondheim, 7491, Norway
| | | | - Felix Donat
- Laboratory of Energy Science and Engineering, ETH Zürich, Zurich, 8092, Switzerland
| | - Geert van Diest
- Euro Support Advanced Materials B.V, Uden, 5405, The Netherlands
| | - Knuth Albertsen
- Euro Support Advanced Materials B.V, Uden, 5405, The Netherlands
| | - Christoph Müller
- Laboratory of Energy Science and Engineering, ETH Zürich, Zurich, 8092, Switzerland
| | - Shahriar Amini
- Department of Energy and Process Engineering, Norwegian University of Science and Technology, Trondheim, 7491, Norway.,Process Technology Department, SINTEF Industry, Trondheim, 7465, Norway.,Department of Mechanical Engineering, University of Alabama, Tuscaloosa, 35487, United States
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82
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Kuna E, Mrdenovic D, Jönsson-Niedziółka M, Pieta P, Pieta IS. Bimetallic nanocatalysts supported on graphitic carbon nitride for sustainable energy development: the shape-structure-activity relation. NANOSCALE ADVANCES 2021; 3:1342-1351. [PMID: 36132874 PMCID: PMC9416898 DOI: 10.1039/d0na01063d] [Citation(s) in RCA: 7] [Impact Index Per Article: 2.3] [Reference Citation Analysis] [Abstract] [Grants] [Track Full Text] [Download PDF] [Figures] [Subscribe] [Scholar Register] [Received: 12/19/2020] [Revised: 04/06/2021] [Accepted: 01/19/2021] [Indexed: 06/16/2023]
Abstract
The catalytic performance of metal nanoparticles (NPs), including activity, selectivity, and durability, depends on their shape and structure at the molecular level. Consequently, metal NPs of different size and shape, e.g., nanobelts, nanocubes, nanoflakes, and nanowires, demonstrate different reactivity and provide different reaction rates depending on the facet exposed. In this context, the present review aims to summarize the shape-structure-activity relation of metallic nanocatalysts. Moreover, keeping in mind that the application of noble metal catalysts is expensive, we would like to draw the reader's attention to bimetallic nanocatalysts supported on graphitic carbon nitride. One of the advantages of these systems is the possibility to minimize the use of noble metals by introducing another metal either to the parent NPs and/or modifying the support materials. The development and optimization of bimetallic nanocatalysts might provide the new class of materials with superior, tunable performance, thermal stability and reduced costs compared to presently available commercial catalysts. Therefore, further application of these bimetallic composites for sustainable development in energy, green chemicals/fuels and environmental protection will be discussed.
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Affiliation(s)
- Ewelina Kuna
- Institute of Physical Chemistry Polish Academy of Sciences 01-224 Warsaw Poland
| | - Dusan Mrdenovic
- Institute of Physical Chemistry Polish Academy of Sciences 01-224 Warsaw Poland
| | | | - Piotr Pieta
- Institute of Physical Chemistry Polish Academy of Sciences 01-224 Warsaw Poland
| | - Izabela S Pieta
- Institute of Physical Chemistry Polish Academy of Sciences 01-224 Warsaw Poland
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83
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84
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Shahnazi A, Firoozi S. Improving the catalytic performance of LaNiO3 perovskite by manganese substitution via ultrasonic spray pyrolysis for dry reforming of methane. J CO2 UTIL 2021. [DOI: 10.1016/j.jcou.2021.101455] [Citation(s) in RCA: 21] [Impact Index Per Article: 7.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/29/2022]
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85
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Sepiolite-based adsorbents for carbon dioxide capture. POLISH JOURNAL OF CHEMICAL TECHNOLOGY 2021. [DOI: 10.2478/pjct-2021-0001] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.3] [Reference Citation Analysis] [Abstract] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 11/20/2022]
Abstract
Abstract
Sepiolite and the sepiolite-based materials were studied in terms of carbon dioxide adsorption. The pore structure and the surface characterization of the obtained materials were specified based on adsorption-desorption isotherms of nitrogen measured at –196oC and carbon dioxide at 0oC. The specific surface area (SSA) was calculated according to the BET equation. The pore volume was estimated using the DFT method. Pristine sepiolite has shown the following value of SSA and CO2 uptake at 0oC – 105 m2/g and 0.27 mmol/g, respectively. The highest value of these parameters was found for material obtained by KOH activation of mixture sepiolite and molasses (MSEP2) – 676 m2/g and 1.49 mmol/g. Sample MSEP2 also indicated the highest value of total pore volume and micropores volume with a diameter up to 0.8 nm.
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86
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Deactivating and Non-Deactivating Coking Found on Ni-Based Catalysts during Combined Steam-Dry Reforming of Methane. Top Catal 2021. [DOI: 10.1007/s11244-021-01413-4] [Citation(s) in RCA: 2] [Impact Index Per Article: 0.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/22/2022]
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87
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Zhang F, Gutiérrez RA, Lustemberg PG, Liu Z, Rui N, Wu T, Ramírez PJ, Xu W, Idriss H, Ganduglia-Pirovano MV, Senanayake SD, Rodriguez JA. Metal-Support Interactions and C1 Chemistry: Transforming Pt-CeO 2 into a Highly Active and Stable Catalyst for the Conversion of Carbon Dioxide and Methane. ACS Catal 2021; 11:1613-1623. [PMID: 34164226 PMCID: PMC8210818 DOI: 10.1021/acscatal.0c04694] [Citation(s) in RCA: 16] [Impact Index Per Article: 5.3] [Reference Citation Analysis] [Abstract] [Track Full Text] [Download PDF] [Figures] [Journal Information] [Subscribe] [Scholar Register] [Received: 10/28/2020] [Revised: 12/22/2020] [Indexed: 12/21/2022]
Abstract
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There
is an ongoing search for materials which can accomplish the
activation of two dangerous greenhouse gases like carbon dioxide and
methane. In the area of C1 chemistry, the reaction between CO2 and CH4 to produce syngas (CO/H2),
known as methane dry reforming (MDR), is attracting a lot of interest
due to its green nature. On Pt(111), high temperatures must be used
to activate the reactants, leading to a substantial deposition of
carbon which makes this metal surface useless for the MDR process.
In this study, we show that strong metal–support interactions
present in Pt/CeO2(111) and Pt/CeO2 powders
lead to systems which can bind CO2 and CH4 well
at room temperature and are excellent and stable catalysts for the
MDR process at moderate temperature (500 °C). The behavior of
these systems was studied using a combination of in situ/operando methods (AP-XPS, XRD, and XAFS) which pointed to an active Pt-CeO2-x interface. In this interface, the
oxide is far from being a passive spectator. It modifies the chemical
properties of Pt, facilitating improved methane dissociation, and
is directly involved in the adsorption and dissociation of CO2 making the MDR catalytic cycle possible. A comparison of
the benefits gained by the use of an effective metal-oxide interface
and those obtained by plain bimetallic bonding indicates that the
former is much more important when optimizing the C1 chemistry associated
with CO2 and CH4 conversion. The presence of
elements with a different chemical nature at the metal-oxide interface
opens the possibility for truly cooperative interactions in the activation
of C–O and C–H bonds.
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Affiliation(s)
- Feng Zhang
- Department of Materials Science and Chemical Engineering, SUNY at Stony Brook, Stony Brook, New York 11794, United States
| | - Ramón A. Gutiérrez
- Facultad de Ciencias, Universidad Central de Venezuela, Caracas 1020-A, Venezuela
| | - Pablo G. Lustemberg
- Instituto de Física Rosario (IFIR), CONICET-UNR, Bv. 27 de Febrero 210bis, Rosario, Santa Fe S2000EZP, Argentina
- Instituto de Catálisis y Petroleoquímica, CSIC, C/Marie Curie 2, Madrid 28049, Spain
| | - Zongyuan Liu
- Chemistry Division, Brookhaven National Laboratory, Upton, New York 11973, United States
| | - Ning Rui
- Chemistry Division, Brookhaven National Laboratory, Upton, New York 11973, United States
| | - Tianpin Wu
- X-ray Science Division, Advanced Photon Source, Argonne National Laboratory, Argonne, Illinois 60439, United States
| | - Pedro J. Ramírez
- Facultad de Ciencias, Universidad Central de Venezuela, Caracas 1020-A, Venezuela
- Zoneca-CENEX, R&D Laboratories, Alta Vista, Monterrey 64770, México
| | - Wenqian Xu
- X-ray Science Division, Advanced Photon Source, Argonne National Laboratory, Argonne, Illinois 60439, United States
| | - Hicham Idriss
- SABIC Corporate Research & Development (CRD), KAUST, Thuwal 29355, Saudi Arabia
| | | | - Sanjaya D. Senanayake
- Chemistry Division, Brookhaven National Laboratory, Upton, New York 11973, United States
| | - José A. Rodriguez
- Department of Materials Science and Chemical Engineering, SUNY at Stony Brook, Stony Brook, New York 11794, United States
- Chemistry Division, Brookhaven National Laboratory, Upton, New York 11973, United States
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Shamsuddin MR, Asikin-Mijan N, Marliza TS, Miyamoto M, Uemiya S, Yarmo MA, Taufiq-Yap YH. Promoting dry reforming of methane via bifunctional NiO/dolomite catalysts for production of hydrogen-rich syngas. RSC Adv 2021; 11:6667-6681. [PMID: 35423191 PMCID: PMC8694874 DOI: 10.1039/d0ra09246k] [Citation(s) in RCA: 5] [Impact Index Per Article: 1.7] [Reference Citation Analysis] [Abstract] [Grants] [Track Full Text] [Download PDF] [Figures] [Journal Information] [Subscribe] [Scholar Register] [Received: 10/30/2020] [Accepted: 12/22/2020] [Indexed: 11/21/2022] Open
Abstract
Extensive effort has been focused on the advancement of an efficient catalyst for CO2 reforming of CH4 to achieve optimum catalytic activity together with cost-effectiveness and high resistance to catalyst deactivation. In this study, for the first time, a new catalytic support/catalyst system of bifunctional NiO/dolomite has been synthesized by a wet impregnation method using low-cost materials, and it shows unique performance in terms of amphoteric sites and self-reduction properties. The catalysts were loaded into a continuous micro-reactor equipped with an online GC-TCD system. The reaction was carried out with a gas mixture consisting of CH4 and CO2 in the ratio of 1 : 1 flowing 30 ml min-1 at 800 °C for 10 h. The physicochemical properties of the synthesized catalysts were determined by various methods including X-ray diffraction (XRD), N2 adsorption-desorption, H2 temperature-programmed reduction (H2-TPR), temperature-programmed desorption of CO2 (TPD-CO2), and temperature-programmed desorption of NH3 (TPD-NH3). The highest catalytic performance of the DRM reaction was shown by the 10% NiO/dolomite catalyst (CH4 & CO2 conversion, χCH4; χCO2 ∼ 98% and H2 selectivity, S H2 = 75%; H2/CO ∼ 1 : 1 respectively). Bifunctional properties of amphoteric sites on the catalyst and self-reduction behaviour of the NiO/dolomite catalyst improved dry reforming of the CH4 process by enhancing CH4 and CO2 conversion without involving a catalyst reduction step, and the catalyst was constantly active for more than 10 h.
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Affiliation(s)
- Mohd Razali Shamsuddin
- Catalysis Science and Technology Research Centre (PutraCAT), Chemistry Department, Faculty of Science, Universiti Putra Malaysia 43400 UPM Serdang Selangor Malaysia +60 3 89466758 +60 3 89466809
| | - Nurul Asikin-Mijan
- Department of Chemical Science, Faculty of Science and Technology, Universiti Kebangsaan Malaysia 43650 UKM Bangi Selangor Malaysia
| | - Tengku Sharifah Marliza
- Department of Basic Science and Engineering, Faculty of Agriculture and Food Sciences, Universiti Putra Malaysia Bintulu Sarawak Campus 97008 Bintulu Sarawak Malaysia
| | - Manabu Miyamoto
- Department of Chemistry and Biomolecular Science, Faculty of Engineering, Gifu University Japan
| | - Shigeyuki Uemiya
- Department of Chemistry and Biomolecular Science, Faculty of Engineering, Gifu University Japan
| | - Mohd Ambar Yarmo
- Department of Chemical Science, Faculty of Science and Technology, Universiti Kebangsaan Malaysia 43650 UKM Bangi Selangor Malaysia
| | - Yun Hin Taufiq-Yap
- Catalysis Science and Technology Research Centre (PutraCAT), Chemistry Department, Faculty of Science, Universiti Putra Malaysia 43400 UPM Serdang Selangor Malaysia +60 3 89466758 +60 3 89466809
- Faculty of Science and Natural Resources, Universiti Malaysia Sabah Jln UMS 88400 Kota Kinabalu Sabah Malaysia
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89
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Ranjekar AM, Yadav GD. Dry reforming of methane for syngas production: A review and assessment of catalyst development and efficacy. J INDIAN CHEM SOC 2021. [DOI: 10.1016/j.jics.2021.100002] [Citation(s) in RCA: 28] [Impact Index Per Article: 9.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 12/20/2022]
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90
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Jalid F, Haider MA, Alam MI, Khan TS. Mechanistic insights into the dominant reaction route and catalyst deactivation in biogas reforming using ab initio microkinetic modeling. Catal Sci Technol 2021. [DOI: 10.1039/d0cy02155e] [Citation(s) in RCA: 7] [Impact Index Per Article: 2.3] [Reference Citation Analysis] [Abstract] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/21/2022]
Abstract
Co and Ru are proposed as two possible catalyst candidates for the biogas reforming process as these convert most of the CH4 to CO and yield less coke.
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Affiliation(s)
- Fatima Jalid
- Renewable Energy and Chemicals Laboratory
- Department of Chemical Engineering
- Indian Institute of Technology Delhi
- Delhi, 110016
- India
| | - M. Ali Haider
- Renewable Energy and Chemicals Laboratory
- Department of Chemical Engineering
- Indian Institute of Technology Delhi
- Delhi, 110016
- India
| | - Md. Imteyaz Alam
- Renewable Energy and Chemicals Laboratory
- Department of Chemical Engineering
- Indian Institute of Technology Delhi
- Delhi, 110016
- India
| | - Tuhin S. Khan
- Light Stock Processing Division
- CSIR-Indian Institute of Petroleum
- Dehradun
- India
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91
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Yusuf M, Farooqi AS, Keong LK, Hellgardt K, Abdullah B. Contemporary trends in composite Ni-based catalysts for CO2 reforming of methane. Chem Eng Sci 2021. [DOI: 10.1016/j.ces.2020.116072] [Citation(s) in RCA: 62] [Impact Index Per Article: 20.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 12/12/2022]
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92
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Manavi N, Liu B. Molecular mechanisms of methane dry reforming on Co 3Mo 3N catalyst with dual sites. Catal Sci Technol 2021. [DOI: 10.1039/d1cy00271f] [Citation(s) in RCA: 6] [Impact Index Per Article: 2.0] [Reference Citation Analysis] [Abstract] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 12/16/2022]
Abstract
With density functional theory and microkinetic modeling, mechanisms responsible for the promoted dry reforming of methane (DRM) reactivity and coke resistance on the dual-site Co3Mo3N(111) surface are explained.
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Affiliation(s)
- Narges Manavi
- Tim Taylor Department of Chemical Engineering
- Kansas State University
- Manhattan
- USA
| | - Bin Liu
- Tim Taylor Department of Chemical Engineering
- Kansas State University
- Manhattan
- USA
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93
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The Effects of CeO2 and Co Doping on the Properties and the Performance of the Ni/Al2O3-MgO Catalyst for the Combined Steam and CO2 Reforming of Methane Using Ultra-Low Steam to Carbon Ratio. Catalysts 2020. [DOI: 10.3390/catal10121450] [Citation(s) in RCA: 5] [Impact Index Per Article: 1.3] [Reference Citation Analysis] [Abstract] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/16/2022] Open
Abstract
In this paper, the 10 wt% Ni/Al2O3-MgO (10Ni/MA), 5 wt% Ni-5 wt% Ce/Al2O3-MgO (5Ni5Ce/MA), and 5 wt% Ni-5 wt% Co/Al2O3-MgO (5Ni5Co/MA) catalysts were prepared by an impregnation method. The effects of CeO2 and Co doping on the physicochemical properties of the Ni/Al2O3-MgO catalyst were comprehensively studied by N2 adsorption-desorption, X-ray diffraction (XRD), transmission electron microscopy (TEM), H2 temperature programmed reduction (H2-TPR), CO2 temperature programmed reduction (CO2-TPD), and thermogravimetric analysis (TGA). The effects on catalytic performance for the combined steam and CO2 reforming of methane with the low steam-to-carbon ratio (S/C ratio) were evaluated at 620 °C under atmospheric pressure. The appearance of CeO2 and Co enhanced the oxygen species at the surface that decreased the coke deposits from 17% for the Ni/MA catalyst to 11–12% for the 5Ni5Ce/MA and 5Ni5Co/MA catalysts. The oxygen vacancies in the 5Ni5Ce/MA catalyst promoted water activation and dissociation, producing surface oxygen with a relatively high H2/CO ratio (1.6). With the relatively low H2/CO ratio (1.3), the oxygen species at the surface was enhanced by CO2 activation-dissociation via the redox potential in the 5Ni5Co/MA catalyst. The improvement of H2O and CO2 dissociative adsorption allowed the 5Ni5Ce/MA and 5Ni5Co/MA catalysts to resist the carbon formation, requiring only a low amount of steam to be added.
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94
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Abstract
Solid oxide fuel cells can operate with carbonaceous fuels, such as syngas, biogas, and methane, using either internal or external reforming, and they represent a more efficient alternative to internal combustion engines. In this work, we explore, for the first time, an alumina membrane containing straight, highly packed (461,289 cpsi), parallel channels of a few micrometers (21 µm) in diameter as a microreformer. As a model reaction to test the performance of this membrane, the dry reforming of methane was carried out using nickel metal and a composite nickel/ceria as catalysts. The samples with intact microchannels were more resistant to carbon deposition than those with a powdered sample, highlighting the deactivation mitigation effect of the microchannel structure. The coke content in the microchannel membrane was one order of magnitude lower than in the powder catalyst. Overall, this work is a proof of concept on the use of composite alumina membrane as microchannel reactors for high temperature reactions.
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95
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Al Abdulghani AJ, Park JH, Kozlov SM, Kang DC, AlSabban B, Pedireddy S, Aguilar-Tapia A, Ould-Chikh S, Hazemann JL, Basset JM, Cavallo L, Takanabe K. Methane dry reforming on supported cobalt nanoparticles promoted by boron. J Catal 2020. [DOI: 10.1016/j.jcat.2020.09.015] [Citation(s) in RCA: 15] [Impact Index Per Article: 3.8] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/23/2022]
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96
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Abstract
The combined steam/dry reforming of clean biogas (CH4/CO2 = 50/50 v/v) represents an innovative way to produce synthesis gas (CO + H2) using renewable feeds, avoiding to deplete the fossil resources and increase CO2 pollution. The reaction was carried out to optimize the reaction conditions for the production of a syngas with a H2/CO ratio suitable for the production of methanol or fuels without any further upgrading. Ni-Rh/Mg/Al/O catalysts obtained from hydrotalcite-type precursors showed high performances in terms of clean biogas conversion due to the formation of very active and resistant Ni-Rh bimetallic nanoparticles. Through the utilization of a {Ni10Rh(CO)19}{(CH3CH2)4N}3 cluster as a precursor of the active particles, it was possible to promote the Ni-Rh interaction and thus obtain low metal loading catalysts composed by highly dispersed bimetallic nanoparticles supported on the MgO, MgAl2O4 matrix. The optimization of the catalytic formulation improved the size and the distribution of the active sites, leading to a better catalyst activity and stability, with low carbon deposition with time-on-stream.
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97
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Lee S, Lim H. Utilization of CO2 arising from methane steam reforming reaction: Use of CO2 membrane and heterotic reactors. J IND ENG CHEM 2020. [DOI: 10.1016/j.jiec.2020.08.001] [Citation(s) in RCA: 8] [Impact Index Per Article: 2.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/23/2022]
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98
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Shah S, Sayono S, Ynzunza J, Pan R, Xu M, Pan X, Gilliard‐AbdulAziz KL. The effects of stoichiometry on the properties of exsolved
Ni‐Fe
alloy nanoparticles for dry methane reforming. AIChE J 2020. [DOI: 10.1002/aic.17078] [Citation(s) in RCA: 13] [Impact Index Per Article: 3.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 01/13/2023]
Affiliation(s)
- Soham Shah
- Department of Chemical and Environmental Engineering Bourns College of Engineering, University of California Riverside California USA
| | - Samuel Sayono
- Department of Material Science and Engineering Bourns College of Engineering, University of California Riverside California USA
| | - Jenna Ynzunza
- Department of Chemical and Environmental Engineering Bourns College of Engineering, University of California Riverside California USA
| | - Ryan Pan
- Department of Chemical and Environmental Engineering Bourns College of Engineering, University of California Riverside California USA
| | - Mingjie Xu
- Department of Material Science and Engineering University of California Irvine California USA
- Department of Physics and Astronomy University of California Irvine California USA
- Irvine Materials Research Institute (IMRI) University of California Irvine, CA 92697 USA
| | - Xiaoqing Pan
- Department of Material Science and Engineering University of California Irvine California USA
- Department of Physics and Astronomy University of California Irvine California USA
- Irvine Materials Research Institute (IMRI) University of California Irvine, CA 92697 USA
| | - Kandis Leslie Gilliard‐AbdulAziz
- Department of Chemical and Environmental Engineering Bourns College of Engineering, University of California Riverside California USA
- Department of Material Science and Engineering Bourns College of Engineering, University of California Riverside California USA
- Center for Catalysis College of Natural and Agricultural Science. University of California Riverside California USA
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99
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Nickel–Promoted Molybdenum or Tungsten Carbides as Catalysts in Dry Reforming of Methane: Effects of Variation in CH4/CO2 Molar Ratio. Catal Letters 2020. [DOI: 10.1007/s10562-020-03420-8] [Citation(s) in RCA: 5] [Impact Index Per Article: 1.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/23/2022]
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100
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Comparative study of modified Ni catalysts over mesoporous CaO-Al2O3 support for CO2/methane reforming. CATAL COMMUN 2020. [DOI: 10.1016/j.catcom.2020.106100] [Citation(s) in RCA: 17] [Impact Index Per Article: 4.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/19/2022] Open
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