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Chen Y, Chen X, Liu S. Numerical investigations on influence factors in topology optimization for catalytic microreactors. J DISPER SCI TECHNOL 2020. [DOI: 10.1080/01932691.2020.1770609] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/24/2022]
Affiliation(s)
- Yao Chen
- Faculty of Mechanical Engineering and Automation, Liaoning University of Technology, Jinzhou, China
| | - Xueye Chen
- Faculty of Mechanical Engineering and Automation, Liaoning University of Technology, Jinzhou, China
| | - Shufen Liu
- Faculty of Mechanical Engineering and Automation, Liaoning University of Technology, Jinzhou, China
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Pirmoradi M, Janulaitis N, Gulotty RJ, Kastner JR. Continuous Hydrogenation of Aqueous Furfural Using a Metal-Supported Activated Carbon Monolith. ACS OMEGA 2020; 5:7836-7849. [PMID: 32309693 PMCID: PMC7160850 DOI: 10.1021/acsomega.9b04010] [Citation(s) in RCA: 4] [Impact Index Per Article: 1.0] [Reference Citation Analysis] [Abstract] [Track Full Text] [Figures] [Subscribe] [Scholar Register] [Received: 11/25/2019] [Accepted: 03/19/2020] [Indexed: 06/11/2023]
Abstract
Continuous hydrogenation of aqueous furfural (4.5%) was studied using a monolith form (ACM) of an activated carbon Pd catalyst (∼1.2% Pd). A sequential reaction pathway was observed, with ACM achieving high selectivity and space time yields (STYs) for furfuryl alcohol (∼25%, 60-70 g/L-cat/h, 7-15 1/h liquid hourly space velocity, LHSV), 2-methylfuran (∼25%, 45-50 g/L-cat/h, 7-15 1/h LHSV), and tetrahydrofurfuryl alcohol (∼20-60%, 10-50 g/L-cat/h, <7 1/h LHSV). ACM showed a low loss of activity and metal leaching over the course of the reactions and was not limited by H2 external mass transfer resistance. Acetic acid (1%) did not significantly affect furfural conversion and product yields using ACM, suggesting Pd/ACM's potential for conversion of crude furfural. Limited metal leaching combined with high metal dispersion and H2 mass transfer rates in the composite carbon catalyst (ACM) provides possible advantages over granular and powdered forms in continuous processing.
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Affiliation(s)
- Maryam Pirmoradi
- Biochemical
Engineering, College of Engineering Driftmier Engineering Center, The University of Georgia, 597 D.W. Brooks Drive, Athens, Georgia 30602, United States
| | - Nida Janulaitis
- Biochemical
Engineering, College of Engineering Driftmier Engineering Center, The University of Georgia, 597 D.W. Brooks Drive, Athens, Georgia 30602, United States
| | - Robert J. Gulotty
- Applied
Catalysts/Applied Ceramics Inc., 2 Technology Place, Laurens, South Carolina 29360, United States
| | - James R. Kastner
- Biochemical
Engineering, College of Engineering Driftmier Engineering Center, The University of Georgia, 597 D.W. Brooks Drive, Athens, Georgia 30602, United States
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Roy S, Kamalanathan P, Lehner P, Turek T, Al‐Dahhan M. Effect of phase maldistribution on performance of two‐phase catalytic monolith reactor and its comparison with trickle bed reactor. CAN J CHEM ENG 2020. [DOI: 10.1002/cjce.23617] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/07/2022]
Affiliation(s)
- Shaibal Roy
- Chemical Reaction Engineering Laboratory, Department of Energy, Environmental, and Chemical EngineeringWashington University in St. Louis St. Louis Missouri
| | - Premkumar Kamalanathan
- Chemical and Biochemical Engineering DepartmentMissouri University of Science and Technology Rolla Missouri
| | - Peter Lehner
- Bayer Technology Services, Bayer AG Leverkusen Germany
| | - Thomas Turek
- Bayer Technology Services, Bayer AG Leverkusen Germany
| | - Muthanna Al‐Dahhan
- Chemical Reaction Engineering Laboratory, Department of Energy, Environmental, and Chemical EngineeringWashington University in St. Louis St. Louis Missouri
- Chemical and Biochemical Engineering DepartmentMissouri University of Science and Technology Rolla Missouri
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Chen R, Feng H, Zhu X, Liao Q, Ye D, Liu J, Liu M, Chen G, Wang K. Interaction of the Taylor flow behaviors and catalytic reaction inside a gas-liquid-solid microreactor under long-term operation. Chem Eng Sci 2018. [DOI: 10.1016/j.ces.2017.09.049] [Citation(s) in RCA: 15] [Impact Index Per Article: 2.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/18/2022]
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Reichelt E, Jahn M, Lange R. Derivation and Application of a Generalized Correlation for Mass Transfer in Packed Beds. CHEM-ING-TECH 2017. [DOI: 10.1002/cite.201600045] [Citation(s) in RCA: 9] [Impact Index Per Article: 1.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/09/2022]
Affiliation(s)
- Erik Reichelt
- Fraunhofer IKTS, Fraunhofer Institute for Ceramic Technologies and Systems; Winterbergstraße 28 01277 Dresden Germany
- Technische Universität Dresden; Institute of Materials Science; 01062 Dresden Germany
| | - Matthias Jahn
- Fraunhofer IKTS, Fraunhofer Institute for Ceramic Technologies and Systems; Winterbergstraße 28 01277 Dresden Germany
| | - Rüdiger Lange
- Technische Universität Dresden; Institute of Process Engineering and Environmental Technology; 01062 Dresden Germany
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Schubert M, Kost S, Lange R, Salmi T, Haase S, Hampel U. Maldistribution susceptibility of monolith reactors: Case study of glucose hydrogenation performance. AIChE J 2016. [DOI: 10.1002/aic.15334] [Citation(s) in RCA: 17] [Impact Index Per Article: 2.1] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 01/11/2023]
Affiliation(s)
- Markus Schubert
- Helmholtz-Zentrum Dresden-Rossendorf, Institute of Fluid Dynamics; 01314 Dresden Germany
| | - Sebastian Kost
- Helmholtz-Zentrum Dresden-Rossendorf, Institute of Fluid Dynamics; 01314 Dresden Germany
| | - Rüdiger Lange
- Technische Universität Dresden, Chair of Chemical Reaction Engineering and Process Plant; 01062 Dresden Germany
| | - Tapio Salmi
- Åbo Akademi University, Laboratory of Industrial Chemistry and Reaction Engineering, Process Chemistry Centre, Dept. of Chemical Engineering; FI-20500 Åbo/Turku Finland
| | - Stefan Haase
- Technische Universität Dresden, Chair of Chemical Reaction Engineering and Process Plant; 01062 Dresden Germany
- Åbo Akademi University, Laboratory of Industrial Chemistry and Reaction Engineering, Process Chemistry Centre, Dept. of Chemical Engineering; FI-20500 Åbo/Turku Finland
| | - Uwe Hampel
- Helmholtz-Zentrum Dresden-Rossendorf, Institute of Fluid Dynamics; 01314 Dresden Germany
- Technische Universität Dresden, AREVA Endowed Chair of Imaging Techniques in Energy and Process Engineering; 01062 Dresden Germany
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Güttel R, Eisenbeis C, Knochen J, Turek T. Monolithic Honeycombs in Loop Reactor Configuration for Intensification of Multiphase Processes. Chem Eng Technol 2015. [DOI: 10.1002/ceat.201400727] [Citation(s) in RCA: 7] [Impact Index Per Article: 0.8] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/09/2022]
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8
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Yu L, Liu G, Wang Z, Zhou Y, Ye H. A core–shell structured Si–Al@Al2O3 as novel support of Pd catalyst. CATAL COMMUN 2015. [DOI: 10.1016/j.catcom.2015.04.027] [Citation(s) in RCA: 4] [Impact Index Per Article: 0.4] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/23/2022] Open
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9
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Xu M, Liu H, Ji S, Li C. Intensification of Deep Hydrodesulfurization Through a Two-stage Combination of Monolith and Trickle Bed Reactors. Chin J Chem Eng 2014. [DOI: 10.1016/j.cjche.2014.06.012] [Citation(s) in RCA: 8] [Impact Index Per Article: 0.8] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/25/2022]
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Haase S, Langsch R, Bauer T, Lange R. Impact of Spherical Catalyst Particles on Gas-Liquid Flow Regimes in Minichannels with Square Cross Section. CHEM-ING-TECH 2014. [DOI: 10.1002/cite.201300143] [Citation(s) in RCA: 9] [Impact Index Per Article: 0.9] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/06/2022]
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Lange R, Haase S, Bauer T, Langsch R. Modellierung von Gas/Flüssig/Fest-Reaktionen in engen Kanälen für das Regime der Kolbenströmung. CHEM-ING-TECH 2009. [DOI: 10.1002/cite.200900091] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.1] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/10/2022]
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Guettel R, Turek T. Comparison of different reactor types for low temperature Fischer–Tropsch synthesis: A simulation study. Chem Eng Sci 2009. [DOI: 10.1016/j.ces.2008.10.059] [Citation(s) in RCA: 107] [Impact Index Per Article: 7.1] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/30/2022]
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Guettel R, Knochen J, Kunz U, Kassing M, Turek T. Preparation and Catalytic Evaluation of Cobalt-Based Monolithic and Powder Catalysts for Fischer−Tropsch Synthesis. Ind Eng Chem Res 2008. [DOI: 10.1021/ie800377n] [Citation(s) in RCA: 42] [Impact Index Per Article: 2.6] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/28/2022]
Affiliation(s)
- Robert Guettel
- Institute of Chemical Process Engineering, Clausthal University of Technology, Leibnizstrasse 17, 38678 Clausthal-Zellerfeld, Germany
| | - Jens Knochen
- Institute of Chemical Process Engineering, Clausthal University of Technology, Leibnizstrasse 17, 38678 Clausthal-Zellerfeld, Germany
| | - Ulrich Kunz
- Institute of Chemical Process Engineering, Clausthal University of Technology, Leibnizstrasse 17, 38678 Clausthal-Zellerfeld, Germany
| | - Markus Kassing
- Institute of Chemical Process Engineering, Clausthal University of Technology, Leibnizstrasse 17, 38678 Clausthal-Zellerfeld, Germany
| | - Thomas Turek
- Institute of Chemical Process Engineering, Clausthal University of Technology, Leibnizstrasse 17, 38678 Clausthal-Zellerfeld, Germany
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Tsoligkas A, Simmons M, Wood J, Frost C. Kinetic and selectivity studies of gas–liquid reaction under Taylor flow in a circular capillary. Catal Today 2007. [DOI: 10.1016/j.cattod.2007.07.001] [Citation(s) in RCA: 36] [Impact Index Per Article: 2.1] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/26/2022]
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16
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Bauer T, Schubert M, Lange R. Monolithischer Palladium-Trägerkatalysator – Herstellung und technische Verwendung. CHEM-ING-TECH 2006. [DOI: 10.1002/cite.200600062] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/05/2022]
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17
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Bauer T, Schubert M, Lange R, Abiev RS. Intensification of heterogeneous catalytic gas-fluid interactions in reactors with a multichannel monolithic catalyst. RUSS J APPL CHEM+ 2006. [DOI: 10.1134/s107042720607019] [Citation(s) in RCA: 16] [Impact Index Per Article: 0.9] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/23/2022]
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Bauer T, Schubert M, Lange R. Prozessintensivierung heterogen katalysierter Gas/Flüssig-Reaktionen mit Monolithreaktoren. CHEM-ING-TECH 2005. [DOI: 10.1002/cite.200500143] [Citation(s) in RCA: 6] [Impact Index Per Article: 0.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/10/2022]
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