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Journal of Catalysis
Volume 241, Issue 2, 25 July 2006, Pages 235-242
 
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doi:10.1016/j.jcat.2006.04.033    
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Copyright © 2006 Elsevier Inc. All rights reserved.

Ceramic microreactors for on-site hydrogen production

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Christiana, M. Mitchella, D.-P. Kimb and P.J.A. Kenisa, Corresponding Author Contact Information, E-mail The Corresponding Author

aDepartment of Chemical & Biomolecular Engineering, University of Illinois at Urbana-Champaign, 600 S. Mathews Ave., Urbana, IL 61801, USA

bDepartment of Fine Chemical Engineering & Chemistry, Chungnam National University, Daejeon, 305-764, South Korea


Received 19 January 2006; 
revised 6 April 2006; 
accepted 8 April 2006. 
Available online 5 June 2006.

Abstract

This paper describes the synthesis and characterization of ceramic microreactors composed of inverted beaded silicon carbide (SiC) monoliths with interconnected 0.75-, 2.2-, or 7.2-μm pores as catalyst supports, integrated within high-density alumina reactor housings obtained via an optimized gel-casting procedure. Structural characterization revealed that these tailored macroporous SiC porous monoliths are stable at temperatures up to at least 1200 °C, and have surface areas and porosities as high as 7.4×107 m2/m3 and 74%, respectively. Further characterization of the ceramic microreactors using the decomposition of ammonia with Ru as the catalyst at temperatures between 450 and 1000 °C showed that as much as 54 sccm of hydrogen, or 9.8×104 sccm H2 per cm3 of monolith volume, could be obtained from a 36-sccm entering stream of NH3 at >99.9% conversion at temperatures above 700 °C. Moreover, using SiC as a catalyst support appears to increase the catalytic activity of the Ru catalyst, as evidenced by high turnover frequencies.

Keywords: Ceramic microreactor; Silicon carbide; Hydrogen production; Ammonia decomposition; Fuel reforming

Article Outline

1. Introduction
2. Experimental
2.1. Catalyst preparation
2.1.1. High-surface area porous monoliths (catalyst supports) preparation
2.1.2. Catalyst deposition
2.2. Characterization of the porous catalytic monoliths
2.3. Fabrication of high-density alumina structures
2.4. Assembly of integrated ceramic microreactors
2.5. Testing of the assembled ceramic microreactors
2.6. Determination of reaction rate constant
3. Results and discussion
3.1. Characterization of the porous catalytic monoliths
3.2. Characterization of integrated ceramic microreactors: ammonia decomposition
3.2.1. Integrated ceramic microreactor assembly
3.2.2. Ceramic microreactor testing
3.2.3. Reaction kinetics analysis
4. Conclusion
Acknowledgements
References






Corresponding Author Contact InformationCorresponding author. Fax: +1 217 333 5052.

Journal of Catalysis
Volume 241, Issue 2, 25 July 2006, Pages 235-242
 
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