1
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Ingle AA, Ansari SZ, Shende DZ, Wasewar KL, Pandit AB. Progress and prospective of heterogeneous catalysts for H 2O 2 production via anthraquinone process. ENVIRONMENTAL SCIENCE AND POLLUTION RESEARCH INTERNATIONAL 2022; 29:86468-86484. [PMID: 35710969 PMCID: PMC9203146 DOI: 10.1007/s11356-022-21354-z] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Key Words] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 01/04/2022] [Accepted: 06/04/2022] [Indexed: 04/16/2023]
Abstract
This paper reviews the improvement in the field of catalytic hydrogenation of 2-ethylanthraquinone to 2-ethylanthrahydroquinone for the successful production of hydrogen peroxide. Hydrogen peroxide is being used in almost all industrial areas, particularly in the chemical industry and in environmental protection, as the most promising oxidant for cleaner and environmentally safer processes. A variety of hydrogenation catalysts have been introduced for hydrogenation of 2-ethylanthraquinone in the production of hydrogen peroxide via anthraquinone (AQ) process. The aim of the present study is to describe the catalysts used in the hydrogenation of 2-ethylanthraquinone and the reaction mechanism involved with different catalytic systems. The hydrogenation of 2-ethylanthraquinone using metals, alloy, bimetallic composite, and supported metal catalyst with the structural modifications has been incorporated for the production of hydrogen peroxide. The comprehensive comparison reveals that the supported metal catalysts required lesser catalyst amount, produced lower AQ decay, and provided higher catalyst activity and selectivity. Furthermore, the replacement of conventional catalysts by metal and metal alloy-supported catalyst rises as a hydrogenation trend, enhancing by several times the catalytic performance.
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Affiliation(s)
- Anjali A. Ingle
- Advanced Separation and Analytical Laboratory (ASAL), Department of Chemical Engineering, Visvesvaraya National Institute of Technology, Nagpur, Maharashtra 440010 India
| | - Shahid Z. Ansari
- Department of Chemical Engineering, Institute of Chemical Technology (ICT), Mumbai, Maharashtra 400019 India
| | - Diwakar Z. Shende
- Advanced Separation and Analytical Laboratory (ASAL), Department of Chemical Engineering, Visvesvaraya National Institute of Technology, Nagpur, Maharashtra 440010 India
| | - Kailas L. Wasewar
- Advanced Separation and Analytical Laboratory (ASAL), Department of Chemical Engineering, Visvesvaraya National Institute of Technology, Nagpur, Maharashtra 440010 India
| | - Aniruddha B. Pandit
- Department of Chemical Engineering, Institute of Chemical Technology (ICT), Mumbai, Maharashtra 400019 India
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2
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García-Martínez JC, Chávez-Esquivel G, Colín-Luna JA, de los Reyes-Heredia JA. Hydrodesulfurization of 4,6–Dimethyldibenzothiophene on NiMoP/γ–Al 2O 3 catalyst under reactive distillation conditions in a micro trickle bed reactor: solvent and temperature effect. INTERNATIONAL JOURNAL OF CHEMICAL REACTOR ENGINEERING 2022. [DOI: 10.1515/ijcre-2022-0005] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 11/15/2022]
Abstract
Abstract
In this work, the influence of pressure and temperature experimentally applied on reactive distillation (RD) under lower conditions than conventional hydrotreating (HDT) processes, the hydrodesulfurization (HDS) reaction of 4,6–dimethyldibenzothiophene (4,6–DMDBT) molecule and the experimental performance of a down-flow micro trickle bed reactor (micro-TBR) with n–dodecane and decalin were studied. Thermodynamic analyses to evaluate hydrogen solubility in liquid hydrocarbons and evaporation for n–dodecane and decalin as lineal and cyclic representative solvents, respectively, were considered. It was possible to define experimental conditions, producing a small deviation of the plug flow model (PFM) and diminished the gas–liquid (G–L) mass transfer limitation as determined from a reactor model at 2.5 MPa. The axial dispersion model (ADM) and PFM models adjust the experimental data at 2.5 MPa operational pressure and the 4,6–DMDBT conversion obtained was ca. 20–50% using n–dodecane; 1.5 times higher when decalin was using. This behavior was due to the liquid hydrogen fraction of n–dodecane was two times higher than for decalin for all operational pressures. In this sense, the use of n–dodecane as a solvent decreased the mass transfer resistance at the G–L and liquid–solid (L–S) interphases. The internal mass transfer resistance in the G–L interphase not only depends on the diffusivity of the solvent, but it also depends on both, the temperature and hydrogen pressure, finding that the RD conditions with n–dodecane are viable in the treatment of sterically impaired molecules in HDS processes.
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Affiliation(s)
- Julio Cesar García-Martínez
- Departamento de Biofísica , Escuela Nacional de Ciencias Biológicas , IPN. Prolongación de Carpio y Plan de Ayala S/N. Col. Santo Tomás, 11340, Miguel Hidalgo , Ciudad de México , México
| | - Gerardo Chávez-Esquivel
- Departamento de Ciencias Básicas , Universidad Autónoma Metropolitana-Azcapotzalco , Av. San Pablo 180, Colonia Reynosa Tamaulipas, 02200, Azcapotzalco , Ciudad de México , México
- Instituto de Física , Universidad Nacional Autónoma de México. Circuito de la Investigación Científica , Ciudad Universitaria, 04510, Coyoacán , Ciudad de México , México
| | - José Antonio Colín-Luna
- Departamento de Energía , Universidad Autónoma Metropolitana-Azcapotzalco , Av. San Pablo 180, Colonia Reynosa Tamaulipas, 02200, Azcapotzalco , Ciudad de México , México
| | - José Antonio de los Reyes-Heredia
- Departamento de Ingeniería de Procesos e Hidráulica , Universidad Autónoma Metropolitana-Azcapotzalco , Av. San Rafael Atlixco 186, Leyes de Reforma 1 Secc., 09340, Iztapalapa , Ciudad de México , México
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3
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Crole DA, Underhill R, Edwards JK, Shaw G, Freakley SJ, Hutchings GJ, Lewis RJ. The direct synthesis of hydrogen peroxide from H 2 and O 2 using Pd-Ni/TiO 2 catalysts. PHILOSOPHICAL TRANSACTIONS. SERIES A, MATHEMATICAL, PHYSICAL, AND ENGINEERING SCIENCES 2020; 378:20200062. [PMID: 32623987 PMCID: PMC7422896 DOI: 10.1098/rsta.2020.0062] [Citation(s) in RCA: 11] [Impact Index Per Article: 2.8] [Reference Citation Analysis] [Abstract] [Key Words] [Grants] [Track Full Text] [Subscribe] [Scholar Register] [Accepted: 05/05/2020] [Indexed: 06/11/2023]
Abstract
The direct synthesis of hydrogen peroxide (H2O2) from molecular H2 and O2 offers an attractive, decentralized alternative to production compared to the current means of production, the anthraquinone process. Herein we evaluate the performance of a 0.5%Pd-4.5%Ni/TiO2 catalyst in batch and flow reactor systems using water as a solvent at ambient temperature. These reaction conditions are considered challenging for the synthesis of high H2O2 concentrations, with the use of sub-ambient temperatures and alcohol co-solvents typical. Catalytic activity was observed to be stable to prolonged use in multiple batch experiments or in a flow system, with selectivities towards H2O2 of 97% and 85%, respectively. This study was carried out in the absence of halide or acid additives that are typically used to inhibit sequential H2O2 degradation reactions showing that this Pd-Ni catalyst has the potential to produce H2O2 selectively. This article is part of a discussion meeting issue 'Science to enable the circular economy'.
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Affiliation(s)
- David A. Crole
- Cardiff Catalysis Institute, School of Chemistry, Cardiff University, Main Building, Park Place, Cardiff CF10 3AT, UK
| | - Ricci Underhill
- Cardiff Catalysis Institute, School of Chemistry, Cardiff University, Main Building, Park Place, Cardiff CF10 3AT, UK
| | - Jennifer K. Edwards
- Cardiff Catalysis Institute, School of Chemistry, Cardiff University, Main Building, Park Place, Cardiff CF10 3AT, UK
| | - Greg Shaw
- Cardiff Catalysis Institute, School of Chemistry, Cardiff University, Main Building, Park Place, Cardiff CF10 3AT, UK
| | - Simon J. Freakley
- Department of Chemistry, University of Bath, Claverton Down, Bath BA2 7AY, UK
| | - Graham J. Hutchings
- Cardiff Catalysis Institute, School of Chemistry, Cardiff University, Main Building, Park Place, Cardiff CF10 3AT, UK
| | - Richard J. Lewis
- Cardiff Catalysis Institute, School of Chemistry, Cardiff University, Main Building, Park Place, Cardiff CF10 3AT, UK
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4
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Gao G, Tian Y, Gong X, Pan Z, Yang K, Zong B. Advances in the production technology of hydrogen peroxide. CHINESE JOURNAL OF CATALYSIS 2020. [DOI: 10.1016/s1872-2067(20)63562-8] [Citation(s) in RCA: 20] [Impact Index Per Article: 5.0] [Reference Citation Analysis] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 10/24/2022]
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5
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Recent Advances in the Direct Synthesis of Hydrogen Peroxide Using Chemical Catalysis—A Review. Catalysts 2018. [DOI: 10.3390/catal8090379] [Citation(s) in RCA: 62] [Impact Index Per Article: 10.3] [Reference Citation Analysis] [Abstract] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 12/13/2022] Open
Abstract
Hydrogen peroxide is an important chemical of increasing demand in today’s world. Currently, the anthraquinone autoxidation process dominates the industrial production of hydrogen peroxide. Herein, hydrogen and oxygen are reacted indirectly in the presence of quinones to yield hydrogen peroxide. Owing to the complexity and multi-step nature of the process, it is advantageous to replace the process with an easier and straightforward one. The direct synthesis of hydrogen peroxide from its constituent reagents is an effective and clean route to achieve this goal. Factors such as water formation due to thermodynamics, explosion risk, and the stability of the hydrogen peroxide produced hinder the applicability of this process at an industrial level. Currently, the catalysis for the direct synthesis reaction is palladium based and the research into finding an effective and active catalyst has been ongoing for more than a century now. Palladium in its pure form, or alloyed with certain metals, are some of the new generation of catalysts that are extensively researched. Additionally, to prevent the decomposition of hydrogen peroxide to water, the process is stabilized by adding certain promoters such as mineral acids and halides. A major part of today’s research in this field focusses on the reactor and the mode of operation required for synthesizing hydrogen peroxide. The emergence of microreactor technology has helped in setting up this synthesis in a continuous mode, which could possibly replace the anthraquinone process in the near future. This review will focus on the recent findings of the scientific community in terms of reaction engineering, catalyst and reactor design in the direct synthesis of hydrogen peroxide.
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6
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Abdullah GH, Xing Y. Hydrogen Peroxide Generation in Divided-Cell Trickle Bed Electrochemical Reactor. Ind Eng Chem Res 2017. [DOI: 10.1021/acs.iecr.7b02890] [Citation(s) in RCA: 12] [Impact Index Per Article: 1.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/28/2022]
Affiliation(s)
- Ghassan H. Abdullah
- Department of Chemical Engineering, University of Missouri, Columbia, Missouri 65211, United States
| | - Yangchuan Xing
- Department of Chemical Engineering, University of Missouri, Columbia, Missouri 65211, United States
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7
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Gallina G, García-Serna J, Salmi TO, Canu P, Biasi P. Bromide and Acids: A Comprehensive Study on Their Role on the Hydrogen Peroxide Direct Synthesis. Ind Eng Chem Res 2017. [DOI: 10.1021/acs.iecr.7b01989] [Citation(s) in RCA: 24] [Impact Index Per Article: 3.4] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/30/2022]
Affiliation(s)
- Gianluca Gallina
- Johan
Gadolin Process Chemistry Centre, Laboratory of Industrial Chemistry
and Reaction Engineering, Åbo Akademi University, Biskopsgatan
8, Turku, FI-20500, Finland
| | - Juan García-Serna
- High
Pressure Processes Group, Department of Chemical Engineering and Environmental
Technology, University of Valladolid, 47011 Valladolid, Spain
| | - Tapio O. Salmi
- Johan
Gadolin Process Chemistry Centre, Laboratory of Industrial Chemistry
and Reaction Engineering, Åbo Akademi University, Biskopsgatan
8, Turku, FI-20500, Finland
| | - Paolo Canu
- Department
of Industrial Engineering, University of Padova, Via F. Marzolo,
9, Padova, 35131, Italy
| | - Pierdomenico Biasi
- Johan
Gadolin Process Chemistry Centre, Laboratory of Industrial Chemistry
and Reaction Engineering, Åbo Akademi University, Biskopsgatan
8, Turku, FI-20500, Finland
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8
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Crole DA, Freakley SJ, Edwards JK, Hutchings GJ. Direct synthesis of hydrogen peroxide in water at ambient temperature. Proc Math Phys Eng Sci 2016; 472:20160156. [PMID: 27436982 PMCID: PMC4950207 DOI: 10.1098/rspa.2016.0156] [Citation(s) in RCA: 23] [Impact Index Per Article: 2.9] [Reference Citation Analysis] [Abstract] [Key Words] [Grants] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Received: 03/01/2016] [Accepted: 05/26/2016] [Indexed: 11/12/2022] Open
Abstract
The direct synthesis of hydrogen peroxide (H2O2) from hydrogen and oxygen has been studied using an Au-Pd/TiO2 catalyst. The aim of this study is to understand the balance of synthesis and sequential degradation reactions using an aqueous, stabilizer-free solvent at ambient temperature. The effects of the reaction conditions on the productivity of H2O2 formation and the undesirable hydrogenation and decomposition reactions are investigated. Reaction temperature, solvent composition and reaction time have been studied and indicate that when using water as the solvent the H2O2 decomposition reaction is the predominant degradation pathway, which provides new challenges for catalyst design, which has previously focused on minimizing the subsequent hydrogenation reaction. This is of importance for the application of this catalytic approach for water purification.
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Affiliation(s)
| | | | | | - Graham J. Hutchings
- Cardiff Catalysis Institute and School of Chemistry, Main Building, Park Place, Cardiff CF10 3AT, UK
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9
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Sterchele S, Biasi P, Centomo P, Shchukarev A, Kordás K, Rautio AR, Mikkola JP, Salmi T, Canton P, Zecca M. Influence of Metal Precursors and Reduction Protocols on the Chloride-Free Preparation of Catalysts for the Direct Synthesis of Hydrogen Peroxide without Selectivity Enhancers. ChemCatChem 2016. [DOI: 10.1002/cctc.201600021] [Citation(s) in RCA: 6] [Impact Index Per Article: 0.8] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/12/2022]
Affiliation(s)
- Stefano Sterchele
- Dipartimento di Scienze Chimiche; Università degli Studi di Padova; via Marzolo 8 I35131 Padova Italy
- Department of Chemical Engineering, Laboratory of Industrial Chemistry and Reaction Engineering; Johan Gadolin Process Chemistry Centre; Åbo Akademi University; Biskopsgatan 8 FI-20500 Åbo-Turku Finland
| | - Pierdomenico Biasi
- Department of Chemical Engineering, Laboratory of Industrial Chemistry and Reaction Engineering; Johan Gadolin Process Chemistry Centre; Åbo Akademi University; Biskopsgatan 8 FI-20500 Åbo-Turku Finland
- Department of Chemistry; Chemical-Biochemical Centre (KBC), Technical Chemistry; Umeå University; SE-90187 Umeå Sweden
| | - Paolo Centomo
- Dipartimento di Scienze Chimiche; Università degli Studi di Padova; via Marzolo 8 I35131 Padova Italy
| | - Andrey Shchukarev
- Faculty of Technology, Microelectronics and Materials Physics Laboratories; EMPART Research Group of Infotech Oulu; University of Oulu; FI-90014 Oulu Finland
| | - Krisztián Kordás
- Department of Chemistry; Chemical-Biochemical Centre (KBC), Technical Chemistry; Umeå University; SE-90187 Umeå Sweden
- Faculty of Technology, Microelectronics and Materials Physics Laboratories; EMPART Research Group of Infotech Oulu; University of Oulu; FI-90014 Oulu Finland
| | - Anne-Riikka Rautio
- Faculty of Technology, Microelectronics and Materials Physics Laboratories; EMPART Research Group of Infotech Oulu; University of Oulu; FI-90014 Oulu Finland
| | - Jyri-Pekka Mikkola
- Department of Chemical Engineering, Laboratory of Industrial Chemistry and Reaction Engineering; Johan Gadolin Process Chemistry Centre; Åbo Akademi University; Biskopsgatan 8 FI-20500 Åbo-Turku Finland
- Department of Chemistry; Chemical-Biochemical Centre (KBC), Technical Chemistry; Umeå University; SE-90187 Umeå Sweden
| | - Tapio Salmi
- Department of Chemical Engineering, Laboratory of Industrial Chemistry and Reaction Engineering; Johan Gadolin Process Chemistry Centre; Åbo Akademi University; Biskopsgatan 8 FI-20500 Åbo-Turku Finland
| | - Patrizia Canton
- Department of Molecular Sciences and Nanosystems; Università Ca' Foscari di Venezia; via Torino 155/b 30170 Venezia-Mestre Italy
| | - Marco Zecca
- Dipartimento di Scienze Chimiche; Università degli Studi di Padova; via Marzolo 8 I35131 Padova Italy
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10
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Kilpiö T, Russo V, Eränen K, Salmi T. Design and modeling of laboratory scale three-phase fixed bed reactors. PHYSICAL SCIENCES REVIEWS 2016. [DOI: 10.1515/psr-2015-0020] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/15/2022]
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11
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Ao C, Tian P, Ouyang L, Da G, Xu X, Xu J, Han YF. Dispersing Pd nanoparticles on N-doped TiO2: a highly selective catalyst for H2O2 synthesis. Catal Sci Technol 2016. [DOI: 10.1039/c5cy02275d] [Citation(s) in RCA: 27] [Impact Index Per Article: 3.4] [Reference Citation Analysis] [Abstract] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/21/2022]
Abstract
The selectivity of H2O2 synthesis directly from H2 and O2 over Pd/TiO2 catalysts was found to be improved greatly if TiO2 was doped by nitrogen before dispersing Pd nanoparticles.
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Affiliation(s)
- Can Ao
- State Key Laboratory of Chemical Engineering
- East China University of Science and Technology
- Shanghai
- China
| | - Pengfei Tian
- State Key Laboratory of Chemical Engineering
- East China University of Science and Technology
- Shanghai
- China
| | - Like Ouyang
- State Key Laboratory of Chemical Engineering
- East China University of Science and Technology
- Shanghai
- China
| | - Guojin Da
- State Key Laboratory of Chemical Engineering
- East China University of Science and Technology
- Shanghai
- China
| | - Xingyan Xu
- State Key Laboratory of Chemical Engineering
- East China University of Science and Technology
- Shanghai
- China
| | - Jing Xu
- State Key Laboratory of Chemical Engineering
- East China University of Science and Technology
- Shanghai
- China
| | - Yi-Fan Han
- State Key Laboratory of Chemical Engineering
- East China University of Science and Technology
- Shanghai
- China
- Research Center of Heterogeneous Catalysis and Engineering Sciences
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12
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Gemo N, Salmi T, Biasi P. The use of modelling to understand the mechanism of hydrogen peroxide direct synthesis from batch, semibatch and continuous reactor points of view. REACT CHEM ENG 2016. [DOI: 10.1039/c5re00073d] [Citation(s) in RCA: 7] [Impact Index Per Article: 0.9] [Reference Citation Analysis] [Abstract] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/21/2022]
Abstract
Modelling is a powerful tool to understand the mechanism of H2O2 direct synthesis.
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Affiliation(s)
- Nicola Gemo
- Department of Chemical Engineering
- Åbo Akademi University
- Åbo-Turku
- Finland
| | - Tapio Salmi
- Department of Chemical Engineering
- Åbo Akademi University
- Åbo-Turku
- Finland
| | - Pierdomenico Biasi
- Department of Chemical Engineering
- Åbo Akademi University
- Åbo-Turku
- Finland
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13
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Wilson NM, Flaherty DW. Mechanism for the Direct Synthesis of H2O2 on Pd Clusters: Heterolytic Reaction Pathways at the Liquid–Solid Interface. J Am Chem Soc 2015; 138:574-86. [DOI: 10.1021/jacs.5b10669] [Citation(s) in RCA: 180] [Impact Index Per Article: 20.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 12/26/2022]
Affiliation(s)
- Neil M. Wilson
- Department of Chemical and
Biomolecular Engineering University of Illinois Urbana−Champaign, Urbana, Illinois 61801, United States
| | - David W. Flaherty
- Department of Chemical and
Biomolecular Engineering University of Illinois Urbana−Champaign, Urbana, Illinois 61801, United States
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14
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H2O2 direct synthesis under mild conditions on Pd–Au samples: Effect of the morphology and of the composition of the metallic phase. Catal Today 2015. [DOI: 10.1016/j.cattod.2014.01.015] [Citation(s) in RCA: 35] [Impact Index Per Article: 3.9] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/23/2022]
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15
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Product distribution analysis of the hydrogen peroxide direct synthesis in an isothermal batch reactor. Catal Today 2015. [DOI: 10.1016/j.cattod.2014.03.020] [Citation(s) in RCA: 6] [Impact Index Per Article: 0.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/21/2022]
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16
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Huerta I, Biasi P, García-Serna J, Cocero M, Mikkola JP, Salmi T. Effect of low hydrogen to palladium molar ratios in the direct synthesis of H2O2 in water in a trickle bed reactor. Catal Today 2015. [DOI: 10.1016/j.cattod.2014.04.012] [Citation(s) in RCA: 13] [Impact Index Per Article: 1.4] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/25/2022]
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17
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Edwards JK, Freakley SJ, Lewis RJ, Pritchard JC, Hutchings GJ. Advances in the direct synthesis of hydrogen peroxide from hydrogen and oxygen. Catal Today 2015. [DOI: 10.1016/j.cattod.2014.03.011] [Citation(s) in RCA: 152] [Impact Index Per Article: 16.9] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/28/2022]
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18
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Gallina G, Biasi P, García-Serna J, Salmi T, Mikkola JP. Optimized H 2 O 2 production in a trickled bed reactor, using water and methanol enriched with selectivity promoters. Chem Eng Sci 2015. [DOI: 10.1016/j.ces.2014.10.040] [Citation(s) in RCA: 4] [Impact Index Per Article: 0.4] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/24/2022]
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19
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The origin of active sites for direct synthesis of H 2 O 2 on Pd/TiO 2 catalysts: Interfaces of Pd and PdO domains. J Catal 2015. [DOI: 10.1016/j.jcat.2014.10.003] [Citation(s) in RCA: 108] [Impact Index Per Article: 12.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/23/2022]
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20
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Gemo N, Sterchele S, Biasi P, Centomo P, Canu P, Zecca M, Shchukarev A, Kordás K, Salmi TO, Mikkola JP. The influence of catalyst amount and Pd loading on the H2O2 synthesis from hydrogen and oxygen. Catal Sci Technol 2015. [DOI: 10.1039/c5cy00493d] [Citation(s) in RCA: 17] [Impact Index Per Article: 1.9] [Reference Citation Analysis] [Abstract] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/21/2022]
Abstract
Direct synthesis of H2O2: structure sensitivity in H2O2 production and structure insensitivity in the H2O production were proved with a Pd/K2621 catalyst.
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Affiliation(s)
- Nicola Gemo
- Dipartimento di Ingegneria Industriale
- University of Padova
- Padova
- Italy
- Department of Chemical Engineering
| | - Stefano Sterchele
- Department of Chemical Engineering
- Åbo Akademi University
- Åbo-Turku
- Finland
- Dipartimento di Scienze Chimiche
| | - Pierdomenico Biasi
- Department of Chemical Engineering
- Åbo Akademi University
- Åbo-Turku
- Finland
- Department of Chemistry
| | - Paolo Centomo
- Dipartimento di Scienze Chimiche
- University of Padova
- Padova
- Italy
| | - Paolo Canu
- Dipartimento di Ingegneria Industriale
- University of Padova
- Padova
- Italy
| | - Marco Zecca
- Dipartimento di Scienze Chimiche
- University of Padova
- Padova
- Italy
| | | | - Krisztián Kordás
- Microelectronics and Materials Physics Laboratories
- University of Oulu
- FI-90014 Oulu
- Finland
| | - Tapio Olavi Salmi
- Department of Chemical Engineering
- Åbo Akademi University
- Åbo-Turku
- Finland
| | - Jyri-Pekka Mikkola
- Department of Chemical Engineering
- Åbo Akademi University
- Åbo-Turku
- Finland
- Department of Chemistry
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21
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Li J, Yao H, Wang Y, Luo G. One-Step Preparation of Pd-SiO2 Composite Microspheres by the Sol–Gel Process in a Microchannel. Ind Eng Chem Res 2014. [DOI: 10.1021/ie5009458] [Citation(s) in RCA: 14] [Impact Index Per Article: 1.4] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/28/2022]
Affiliation(s)
- Jiahui Li
- State Key
Laboratory of Chemical Engineering, Department of Chemical Engineering, Tsinghua University, Beijing 100084, China
| | - Hongbao Yao
- State Key
Laboratory of Chemical Engineering, Department of Chemical Engineering, Tsinghua University, Beijing 100084, China
| | - Yujun Wang
- State Key
Laboratory of Chemical Engineering, Department of Chemical Engineering, Tsinghua University, Beijing 100084, China
| | - Guangsheng Luo
- State Key
Laboratory of Chemical Engineering, Department of Chemical Engineering, Tsinghua University, Beijing 100084, China
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22
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Biasi P, Menegazzo F, Canu P, Pinna F, Salmi TO. Role of a Functionalized Polymer (K2621) and an Inorganic Material (Sulphated Zirconia) as Supports in Hydrogen Peroxide Direct Synthesis in a Continuous Reactor. Ind Eng Chem Res 2013. [DOI: 10.1021/ie4011782] [Citation(s) in RCA: 11] [Impact Index Per Article: 1.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/30/2022]
Affiliation(s)
- Pierdomenico Biasi
- Laboratory of Industrial
Chemistry
and Reaction Engineering Process Chemistry Centre (PCC), Åbo Akademi, 20500 Åbo/Turku, Finland
| | - Federica Menegazzo
- Department of Molecular Sciences
and Nanosystems, Ca’ Foscari University of Venice and Consorzio INSTM, Dorsoduro 2137, 30123 Venezia,
Italy
| | - Paolo Canu
- Dipartimento di Ingegneria
Industriale, University of Padova, 35131,
Padova, Italy
| | - Francesco Pinna
- Department of Molecular Sciences
and Nanosystems, Ca’ Foscari University of Venice and Consorzio INSTM, Dorsoduro 2137, 30123 Venezia,
Italy
| | - Tapio O. Salmi
- Laboratory of Industrial
Chemistry
and Reaction Engineering Process Chemistry Centre (PCC), Åbo Akademi, 20500 Åbo/Turku, Finland
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23
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Meng YL, Tian SJ, Li SF, Wang BY, Zhang MH. Transesterification of rapeseed oil for biodiesel production in trickle-bed reactors packed with heterogeneous Ca/Al composite oxide-based alkaline catalyst. BIORESOURCE TECHNOLOGY 2013; 136:730-734. [PMID: 23558183 DOI: 10.1016/j.biortech.2013.03.081] [Citation(s) in RCA: 5] [Impact Index Per Article: 0.5] [Reference Citation Analysis] [Abstract] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 12/28/2012] [Revised: 03/11/2013] [Accepted: 03/12/2013] [Indexed: 06/02/2023]
Abstract
A conventional trickle bed reactor and its modified type both packed with Ca/Al composite oxide-based alkaline catalysts were studied for biodiesel production by transesterification of rapeseed oil and methanol. The effects of the methanol usage and oil flow rate on the FAME yield were investigated under the normal pressure and methanol boiling state. The oil flow rate had a significant effect on the FAME yield for the both reactors. The modified trickle bed reactor kept over 94.5% FAME yield under 0.6 mL/min oil flow rate and 91 mL catalyst bed volume, showing a much higher conversion and operational stability than the conventional type. With the modified trickle bed reactor, both transesterification and methanol separation could be performed simultaneously, and glycerin and methyl esters were separated additionally by gravity separation.
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Affiliation(s)
- Yong-Lu Meng
- Key Laboratory for Green Chemical Technology of State Education Ministry, School of Chemical Engineering and Technology, Tianjin University, Tianjin 300072, China
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Gemo N, Biasi P, Canu P, Menegazzo F, Pinna F, Samikannu A, Kordás K, Salmi TO, Mikkola JP. Reactivity Aspects of SBA15-Based Doped Supported Catalysts: H2O2 Direct Synthesis and Disproportionation Reactions. Top Catal 2013. [DOI: 10.1007/s11244-013-0009-2] [Citation(s) in RCA: 19] [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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25
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Kilpiö T, Biasi P, Bittante A, Salmi T, Wärnå J. Modeling of Direct Synthesis of Hydrogen Peroxide in a Packed-Bed Reactor. Ind Eng Chem Res 2012. [DOI: 10.1021/ie301919y] [Citation(s) in RCA: 9] [Impact Index Per Article: 0.8] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/29/2022]
Affiliation(s)
- Teuvo Kilpiö
- Department of Chemical Engineering,
Laboratory of Industrial
Chemistry and Reaction Engineering, Åbo Akademi, Piispankatu 8, Turku/Åbo, FI-20500, Finland
| | - Pierdomenico Biasi
- Department of Chemical Engineering,
Laboratory of Industrial
Chemistry and Reaction Engineering, Åbo Akademi, Piispankatu 8, Turku/Åbo, FI-20500, Finland
| | - Alice Bittante
- Department of Chemical Engineering,
Laboratory of Industrial
Chemistry and Reaction Engineering, Åbo Akademi, Piispankatu 8, Turku/Åbo, FI-20500, Finland
| | - Tapio Salmi
- Department of Chemical Engineering,
Laboratory of Industrial
Chemistry and Reaction Engineering, Åbo Akademi, Piispankatu 8, Turku/Åbo, FI-20500, Finland
| | - Johan Wärnå
- Department of Chemical Engineering,
Laboratory of Industrial
Chemistry and Reaction Engineering, Åbo Akademi, Piispankatu 8, Turku/Åbo, FI-20500, Finland
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26
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Li Y, Feng J, He Y, Evans DG, Li D. Controllable Synthesis, Structure, and Catalytic Activity of Highly Dispersed Pd Catalyst Supported on Whisker-Modified Spherical Alumina. Ind Eng Chem Res 2012. [DOI: 10.1021/ie300385h] [Citation(s) in RCA: 21] [Impact Index Per Article: 1.8] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/29/2022]
Affiliation(s)
- Yang Li
- State Key Laboratory of Chemical Resource Engineering, Beijing University of Chemical Technology, Beijing
100029, China
| | - Junting Feng
- State Key Laboratory of Chemical Resource Engineering, Beijing University of Chemical Technology, Beijing
100029, China
| | - Yufei He
- State Key Laboratory of Chemical Resource Engineering, Beijing University of Chemical Technology, Beijing
100029, China
| | - David G. Evans
- State Key Laboratory of Chemical Resource Engineering, Beijing University of Chemical Technology, Beijing
100029, China
| | - Dianqing Li
- State Key Laboratory of Chemical Resource Engineering, Beijing University of Chemical Technology, Beijing
100029, China
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27
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Kim J, Chung YM, Kang SM, Choi CH, Kim BY, Kwon YT, Kim TJ, Oh SH, Lee CS. Palladium Nanocatalysts Immobilized on Functionalized Resin for the Direct Synthesis of Hydrogen Peroxide from Hydrogen and Oxygen. ACS Catal 2012. [DOI: 10.1021/cs300090h] [Citation(s) in RCA: 52] [Impact Index Per Article: 4.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/29/2022]
Affiliation(s)
- Jongmin Kim
- Department of Chemical Engineering, Chungnam National University, Yuseong-gu, Daejeon 305-764,
Republic of Korea
| | - Young-Min Chung
- Catalyst Lab, Catalyst & Process R&D Centre, SK innovation, Yuseong-gu, Daejeon 305-712, Republic of Korea
| | - Sung-Min Kang
- Department of Chemical Engineering, Chungnam National University, Yuseong-gu, Daejeon 305-764,
Republic of Korea
| | - Chang-Hyung Choi
- Department of Chemical Engineering, Chungnam National University, Yuseong-gu, Daejeon 305-764,
Republic of Korea
| | - Bo-Yeol Kim
- Department of Chemical Engineering, Chungnam National University, Yuseong-gu, Daejeon 305-764,
Republic of Korea
| | - Yong-Tak Kwon
- Catalyst Lab, Catalyst & Process R&D Centre, SK innovation, Yuseong-gu, Daejeon 305-712, Republic of Korea
| | - Tae Jin Kim
- Catalyst Lab, Catalyst & Process R&D Centre, SK innovation, Yuseong-gu, Daejeon 305-712, Republic of Korea
| | - Seung-Hoon Oh
- Catalyst Lab, Catalyst & Process R&D Centre, SK innovation, Yuseong-gu, Daejeon 305-712, Republic of Korea
| | - Chang-Soo Lee
- Department of Chemical Engineering, Chungnam National University, Yuseong-gu, Daejeon 305-764,
Republic of Korea
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Biasi P, Gemo N, Hernández Carucci JR, Eränen K, Canu P, Salmi TO. Kinetics and Mechanism of H2O2 Direct Synthesis over a Pd/C Catalyst in a Batch Reactor. Ind Eng Chem Res 2012. [DOI: 10.1021/ie2021398] [Citation(s) in RCA: 32] [Impact Index Per Article: 2.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/29/2022]
Affiliation(s)
- Pierdomenico Biasi
- Process Chemistry Centre (PCC), Laboratory of Industrial Chemistry and Reaction Engineering Åbo Akademi, Biskopsgatan 8, 20500, Turku, Finland
- Dipartimento di
Ingegneria Industriale, University of Padova, via Marzolo
9, 35131 Padova, Italy
| | - Nicola Gemo
- Process Chemistry Centre (PCC), Laboratory of Industrial Chemistry and Reaction Engineering Åbo Akademi, Biskopsgatan 8, 20500, Turku, Finland
- Dipartimento di
Ingegneria Industriale, University of Padova, via Marzolo
9, 35131 Padova, Italy
| | - José Rafael Hernández Carucci
- Process Chemistry Centre (PCC), Laboratory of Industrial Chemistry and Reaction Engineering Åbo Akademi, Biskopsgatan 8, 20500, Turku, Finland
- BiCHEM Technology BV, High Tech Campus 48-2, 5656 AE, Eindhoven, The Netherlands
| | - Kari Eränen
- Process Chemistry Centre (PCC), Laboratory of Industrial Chemistry and Reaction Engineering Åbo Akademi, Biskopsgatan 8, 20500, Turku, Finland
| | - Paolo Canu
- Dipartimento di
Ingegneria Industriale, University of Padova, via Marzolo
9, 35131 Padova, Italy
| | - Tapio O. Salmi
- Process Chemistry Centre (PCC), Laboratory of Industrial Chemistry and Reaction Engineering Åbo Akademi, Biskopsgatan 8, 20500, Turku, Finland
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29
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Biasi P, Canu P, Menegazzo F, Pinna F, Salmi TO. Direct Synthesis of Hydrogen Peroxide in a Trickle Bed Reactor: Comparison of Pd-Based Catalysts. Ind Eng Chem Res 2012. [DOI: 10.1021/ie202128v] [Citation(s) in RCA: 32] [Impact Index Per Article: 2.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/29/2022]
Affiliation(s)
- Pierdomenico Biasi
- Process Chemistry Centre (PCC),
Laboratory of Industrial Chemistry and Reaction Engineering, Åbo Akademi, Biskopsgatan 8, 20500 Turku/Åbo,
Finland
- Department of Industrial
Engineering, University of Padova, via
Marzolo 9, 35131, Padova,
Italy
| | - Paolo Canu
- Department of Industrial
Engineering, University of Padova, via
Marzolo 9, 35131, Padova,
Italy
| | - Federica Menegazzo
- Department of Molecular
Science
and Nanosystems, Cà Foscari University and “Consorzio INSTM”, 30123, Venezia, Italy
| | - Francesco Pinna
- Department of Molecular
Science
and Nanosystems, Cà Foscari University and “Consorzio INSTM”, 30123, Venezia, Italy
| | - Tapio O. Salmi
- Process Chemistry Centre (PCC),
Laboratory of Industrial Chemistry and Reaction Engineering, Åbo Akademi, Biskopsgatan 8, 20500 Turku/Åbo,
Finland
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30
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Abate S, Perathoner S, Centi G. Performances of Pd Nanoparticles on Different Supports in the Direct Synthesis of H2O2 in CO2-Expanded Methanol. Top Catal 2011. [DOI: 10.1007/s11244-011-9692-z] [Citation(s) in RCA: 14] [Impact Index Per Article: 1.1] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/18/2022]
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