doi:10.1016/j.jcat.2006.04.033
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,
, 
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
Fig. 1. SEM micrographs of fracture profiles of inverted beaded SiC monoliths after heating at 1200 °C for 6 h in air with (a) 7.2 μm pores (inset: an optical micrograph of the whole SiC porous monolith); (b) 2.2 μm pores; and (c) 0.75 μm pores. The black spots are the windows that connect adjacent pores in these close packed structures. The bits of debris are due to cutting of the samples before SEM analysis.
Fig. 2. Polymer removal and sintering temperature sequence used to obtain high-density, nonporous alumina housings and lids. The heating and cooling rates were optimized to avoid cracking and deformation in the final alumina structures.
Fig. 3. (a) Optical and SEM (inset) micrographs of a high-density alumina housing with five microchannels (400 μm×150 μm×1 mm) in negative relief, obtained via gel-casting. Optical micrographs of (b) alumina lid and (c) assembled ceramic microreactor comprised of an alumina housing structure with five SiC porous monoliths (see Fig. 1), an alumina lid, and alumina inlet and outlet tubes.
Fig. 4. NH3 conversion using Ru-coated SiC porous monoliths (volume = 0.55 mm3) as a function of temperature for different NH3 flow rates measured from 450 to 1000 °C. The conversion values were obtained for integrated ceramic microreactors comprised of SiC catalytic monoliths with (a) 7.2 μm pores; (b) 2.2 μm pores; and (c) 0.75 μm pores. All data are fitted with the design equation for first-order kinetics in a PFR, assuming constant temperature and a constant pressure gradient across the reactor. (- - -) indicates the equilibrium conversion of NH3 as a function of temperature.
Fig. 5. Arrhenius plot of integral turnover frequencies for decomposition of NH3 in integrated ceramic microreactors comprised of Ru-covered SiC monoliths with 7.2- and 2.2-μm pores. The lines connecting the data points are added to guide the eye.
Table 1.
Catalyst loading and dispersion data for Ru-covered SiC porous monoliths with pore diameters of 7.2, 2.2, and 0.75 μm
a Surface area-to-volume ratio is not sufficiently large for a reliable analysis.
b Calculated using the Ru dispersion data obtained with CO chemisorption.
Table 2.
Observed first-order reaction rate constants k′ at different temperatures for SiC porous monoliths with pore diameters of 7.2 and 2.2 μm


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