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Shelepova EV, Vedyagin AA. Comparative Analysis of the Dehydrogenation of Hydrocarbons and Alcohols in a Membrane Reactor. KINETICS AND CATALYSIS 2022. [DOI: 10.1134/s0023158422010074] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 11/23/2022]
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Lee G, Easa J, Jin R, Booth A, O'Brien CP. Enhancing the surface sensitivity of in-situ/operando characterization of palladium membranes through polarization modulation and synthesis of optically smooth palladium thin films. J Memb Sci 2021. [DOI: 10.1016/j.memsci.2021.119605] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/16/2022]
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Microstructural Investigation and On-Site Repair of Thin Pd-Ag Alloy Membranes. MEMBRANES 2020; 10:membranes10120384. [PMID: 33266176 PMCID: PMC7760571 DOI: 10.3390/membranes10120384] [Citation(s) in RCA: 6] [Impact Index Per Article: 1.5] [Reference Citation Analysis] [Abstract] [Key Words] [Track Full Text] [Download PDF] [Figures] [Subscribe] [Scholar Register] [Received: 10/19/2020] [Revised: 11/26/2020] [Accepted: 11/26/2020] [Indexed: 11/16/2022]
Abstract
Pd membranes act in an important role in H2 purification and H2 production in membrane reactors. Pd-Ag alloy membranes fabricated by consecutive electroless- and electroplating process on alumina tubes exhibited good stability under stringent heating/cooling cycles at a ramp rate of 10 K/min, imitating practical fast initiation or emergency shutdown conditions. Bilayer Pd-Ag membranes can form dense and uniform alloy after thermal treatment for 24 h at 823 K under H2 atmosphere, despite a porous structure due to the development of liquid-like properties above Tamman temperature to enforce the migrativity. On the contrary, alloying under N2 atmosphere resulted in a Pd-enriched layer. This led to a lower H2 flux but superior thermal stability compared to that alloying under H2 atmosphere. The trilayer approach of electroless-plated Pd, electro-polated Ag and electroless-plated Pd is not suitable to achieve homogeneous Pd-Ag alloys, which, on the other hand, presented the occurrence of a small gap between top Pd layer and middle Ag layer, probably due to insufficient wetting during plating process. An on-site repair treatment in analogous to MOCVD (Metal-organic Chemical Vapor Deposition) process was first proposed to extend the lifetime of Pd-Ag membrane, i.e., by vaporizing, and subsequent decomposition of Ag(OOCC2F5) powders to "preferentially" block the pinholes under vacuum and at working temperature of ca. 473-673 K, which effectively reduced the N2 flux by 57.4% compared to the initial value. The H2 flux, however, declined by 16.7% due to carbon deposition on the membrane surface, which requires further investigation. This approach shows some potential for on-site repair without disassembly or cooling to room temperature.
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Peters TA, Stange M, Bredesen R. Flux-Reducing Tendency of Pd-Based Membranes Employed in Butane Dehydrogenation Processes. MEMBRANES 2020; 10:E291. [PMID: 33081363 PMCID: PMC7650750 DOI: 10.3390/membranes10100291] [Citation(s) in RCA: 2] [Impact Index Per Article: 0.5] [Reference Citation Analysis] [Abstract] [Key Words] [Grants] [Track Full Text] [Download PDF] [Figures] [Subscribe] [Scholar Register] [Received: 09/29/2020] [Revised: 10/12/2020] [Accepted: 10/14/2020] [Indexed: 11/20/2022]
Abstract
We report on the effect of butane and butylene on hydrogen permeation through thin state-of-the-art Pd-Ag alloy membranes. A wide range of operating conditions, such as temperature (200-450 °C) and H2/butylene (or butane) ratio (0.5-3), on the flux-reducing tendency were investigated. In addition, the behavior of membrane performance during prolonged exposure to butylene was evaluated. In the presence of butane, the flux-reducing tendency was found to be limited up to the maximum temperature investigated, 450 °C. Compared to butane, the flux-reducing tendency in the presence of butylene was severe. At 400 °C and 20% butylene, the flux decreases by ~85% after 3 h of exposure but depends on temperature and the H2/butylene ratio. In terms of operating temperature, an optimal performance was found at 250-300 °C with respect to obtaining the highest absolute hydrogen flux in the presence of butylene. At lower temperatures, the competitive adsorption of butylene over hydrogen accounts for a large initial flux penalty.
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Affiliation(s)
- Thijs A. Peters
- SINTEF Industry, P.O. Box 124 Blindern, N-0314 Oslo, Norway; (M.S.); (R.B.)
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Babak VN, Didenko LP, Kvurt YP, Sementsova LA. Studying the Operation of a Membrane Module Based on Palladium Foil at High Temperatures. THEORETICAL FOUNDATIONS OF CHEMICAL ENGINEERING 2018. [DOI: 10.1134/s004057951802001x] [Citation(s) in RCA: 3] [Impact Index Per Article: 0.5] [Reference Citation Analysis] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 11/23/2022]
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Babak VN, Didenko LP, Zakiev SE. Hydrogen transport through a membrane module based on a palladium foil. THEORETICAL FOUNDATIONS OF CHEMICAL ENGINEERING 2013. [DOI: 10.1134/s004057951306002x] [Citation(s) in RCA: 8] [Impact Index Per Article: 0.7] [Reference Citation Analysis] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 11/22/2022]
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Economic feasibility of silica and palladium composite membranes for industrial dehydrogenation reactions. Chem Eng Res Des 2010. [DOI: 10.1016/j.cherd.2010.01.013] [Citation(s) in RCA: 23] [Impact Index Per Article: 1.6] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/20/2022]
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Wu Z, Hatim IM, Kingsbury BF, Gbenedio E, Li K. A novel inorganic hollow fiber membrane reactor for catalytic dehydrogenation of propane. AIChE J 2009. [DOI: 10.1002/aic.11864] [Citation(s) in RCA: 25] [Impact Index Per Article: 1.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/06/2022]
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Babak VN, Babak TB, Zakiev SE, Kholpanov LP. Theoretical study of hydrocarbon dehydrogenation at high temperatures. THEORETICAL FOUNDATIONS OF CHEMICAL ENGINEERING 2009. [DOI: 10.1134/s0040579509010102] [Citation(s) in RCA: 8] [Impact Index Per Article: 0.5] [Reference Citation Analysis] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 11/23/2022]
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Israni SH, Nair BKR, Harold MP. Hydrogen generation and purification in a composite Pd hollow fiber membrane reactor: Experiments and modeling. Catal Today 2009. [DOI: 10.1016/j.cattod.2008.02.020] [Citation(s) in RCA: 40] [Impact Index Per Article: 2.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/22/2022]
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Lee DW, Park SJ, Yu CY, Ihm SK, Lee KH. Study on methanol reforming–inorganic membrane reactors combined with water–gas shift reaction and relationship between membrane performance and methanol conversion. J Memb Sci 2008. [DOI: 10.1016/j.memsci.2007.12.050] [Citation(s) in RCA: 29] [Impact Index Per Article: 1.8] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/22/2022]
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12
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Sadat Rezai SA, Traa Y. Dehydroalkylation of toluene with ethane in a packed-bed membrane reactor with a bifunctional catalyst and a hydrogen-selective membrane. Chem Commun (Camb) 2008:2382-4. [DOI: 10.1039/b800486b] [Citation(s) in RCA: 3] [Impact Index Per Article: 0.2] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/21/2022]
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Lu GQ, Diniz da Costa JC, Duke M, Giessler S, Socolow R, Williams RH, Kreutz T. Inorganic membranes for hydrogen production and purification: A critical review and perspective. J Colloid Interface Sci 2007; 314:589-603. [PMID: 17588594 DOI: 10.1016/j.jcis.2007.05.067] [Citation(s) in RCA: 183] [Impact Index Per Article: 10.8] [Reference Citation Analysis] [Abstract] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Received: 04/01/2007] [Revised: 05/17/2007] [Accepted: 05/21/2007] [Indexed: 11/23/2022]
Abstract
Hydrogen as a high-quality and clean energy carrier has attracted renewed and ever-increasing attention around the world in recent years, mainly due to developments in fuel cells and environmental pressures including climate change issues. In thermochemical processes for hydrogen production from fossil fuels, separation and purification is a critical technology. Where water-gas shift reaction is involved for converting the carbon monoxide to hydrogen, membrane reactors show great promises for shifting the equilibrium. Membranes are also important to the subsequent purification of hydrogen. For hydrogen production and purification, there are generally two classes of membranes both being inorganic: dense phase metal and metal alloys, and porous ceramic membranes. Porous ceramic membranes are normally prepared by sol-gel or hydrothermal methods, and have high stability and durability in high temperature, harsh impurity and hydrothermal environments. In particular, microporous membranes show promises in water gas shift reaction at higher temperatures. In this article, we review the recent advances in both dense phase metal and porous ceramic membranes, and compare their separation properties and performance in membrane reactor systems. The preparation, characterization and permeation of the various membranes will be presented and discussed. We also aim to examine the critical issues in these membranes with respect to the technical and economical advantages and disadvantages. Discussions will also be made on the relevance and importance of membrane technology to the new generation of zero-emission power technologies.
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Affiliation(s)
- G Q Lu
- Australian Research Centre of Excellence for Functional Nanomaterials, School of Engineering and AIBN, The University of Queensland, Brisbane, Qld 4072, Australia.
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Arstad B, Venvik H, Klette H, Walmsley J, Tucho W, Holmestad R, Holmen A, Bredesen R. Studies of self-supported 1.6μm Pd/23wt.% Ag membranes during and after hydrogen production in a catalytic membrane reactor. Catal Today 2006. [DOI: 10.1016/j.cattod.2006.01.041] [Citation(s) in RCA: 26] [Impact Index Per Article: 1.4] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/24/2022]
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Ryi SK, Park JS, Choi SH, Cho SH, Kim SH. Fabrication and characterization of metal porous membrane made of Ni powder for hydrogen separation. Sep Purif Technol 2006. [DOI: 10.1016/j.seppur.2005.06.017] [Citation(s) in RCA: 27] [Impact Index Per Article: 1.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/25/2022]
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Gielens F, Tong H, van Rijn C, Vorstman M, Keurentjes J. Microsystem technology for high-flux hydrogen separation membranes. J Memb Sci 2004. [DOI: 10.1016/j.memsci.2004.06.021] [Citation(s) in RCA: 23] [Impact Index Per Article: 1.2] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/26/2022]
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Keurentjes JTF, Gielens FC, Tong HD, van Rijn CJM, Vorstman MAG. High-Flux Palladium Membranes Based on Microsystem Technology. Ind Eng Chem Res 2004. [DOI: 10.1021/ie0341202] [Citation(s) in RCA: 27] [Impact Index Per Article: 1.4] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/30/2022]
Affiliation(s)
- Jos T. F. Keurentjes
- Process Development Group, Department of Chemical Engineering and Chemistry, Eindhoven University of Technology, P.O. Box 513, 5600 MB Eindhoven, The Netherlands, Mesa+ Research Institute, Transducer Science Technology Group, University of Twente, P.O. Box 217, 7500 AE Enschede, The Netherlands, and Aquamarijn Microfiltration BV, Beatrixlaan 2, 7255 DB Hengelo, The Netherlands
| | - Frank C. Gielens
- Process Development Group, Department of Chemical Engineering and Chemistry, Eindhoven University of Technology, P.O. Box 513, 5600 MB Eindhoven, The Netherlands, Mesa+ Research Institute, Transducer Science Technology Group, University of Twente, P.O. Box 217, 7500 AE Enschede, The Netherlands, and Aquamarijn Microfiltration BV, Beatrixlaan 2, 7255 DB Hengelo, The Netherlands
| | - H. D. Tong
- Process Development Group, Department of Chemical Engineering and Chemistry, Eindhoven University of Technology, P.O. Box 513, 5600 MB Eindhoven, The Netherlands, Mesa+ Research Institute, Transducer Science Technology Group, University of Twente, P.O. Box 217, 7500 AE Enschede, The Netherlands, and Aquamarijn Microfiltration BV, Beatrixlaan 2, 7255 DB Hengelo, The Netherlands
| | - C. J. M. van Rijn
- Process Development Group, Department of Chemical Engineering and Chemistry, Eindhoven University of Technology, P.O. Box 513, 5600 MB Eindhoven, The Netherlands, Mesa+ Research Institute, Transducer Science Technology Group, University of Twente, P.O. Box 217, 7500 AE Enschede, The Netherlands, and Aquamarijn Microfiltration BV, Beatrixlaan 2, 7255 DB Hengelo, The Netherlands
| | - Marius A. G. Vorstman
- Process Development Group, Department of Chemical Engineering and Chemistry, Eindhoven University of Technology, P.O. Box 513, 5600 MB Eindhoven, The Netherlands, Mesa+ Research Institute, Transducer Science Technology Group, University of Twente, P.O. Box 217, 7500 AE Enschede, The Netherlands, and Aquamarijn Microfiltration BV, Beatrixlaan 2, 7255 DB Hengelo, The Netherlands
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Performance of hydrophobic and hydrophilic silica membrane reactors for the water gas shift reaction. Sep Purif Technol 2003. [DOI: 10.1016/s1383-5866(03)00069-8] [Citation(s) in RCA: 100] [Impact Index Per Article: 4.8] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/18/2022]
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Dittmeyer R, Höllein V, Daub K. Membrane reactors for hydrogenation and dehydrogenation processes based on supported palladium. ACTA ACUST UNITED AC 2001. [DOI: 10.1016/s1381-1169(01)00149-2] [Citation(s) in RCA: 320] [Impact Index Per Article: 13.9] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/17/2022]
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Preparation and characterization of palladium composite membranes for hydrogen removal in hydrocarbon dehydrogenation membrane reactors. Catal Today 2001. [DOI: 10.1016/s0920-5861(01)00279-6] [Citation(s) in RCA: 39] [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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Assabumrungrat S, Jhoraleecharnchai W, Praserthdam P, Goto S. Kinetics for Dehydrogenation of Propane on Pt-Sn-K/.GAMMA.-Al2O3 Catalyst. JOURNAL OF CHEMICAL ENGINEERING OF JAPAN 2000. [DOI: 10.1252/jcej.33.529] [Citation(s) in RCA: 12] [Impact Index Per Article: 0.5] [Reference Citation Analysis] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 11/11/2022]
Affiliation(s)
- Suttichai Assabumrungrat
- Petrochemical Engineering Laboratory, Department of Chemical Engineering, Chulalongkorn University
| | - Wiroj Jhoraleecharnchai
- Petrochemical Engineering Laboratory, Department of Chemical Engineering, Chulalongkorn University
| | - Piyasan Praserthdam
- Petrochemical Engineering Laboratory, Department of Chemical Engineering, Chulalongkorn University
| | - Shigeo Goto
- Department of Chemical Engineering, Nagoya University
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