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NAMS 2002 Workshop - ICOM 2008

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Inorganic Membranes II – 5<br />

Thursday July 17, 11:00 AM-11:30 AM, O’ahu/Waialua<br />

Recent Developments on the Preparation and Modeling of Nanoporous<br />

Silicon Carbide Membranes for Gas Separation Applications<br />

R. Mourhatch (Speaker), University of Southern California, Los Angeles, Califorinia, USA -<br />

mourhatc@usc.edu<br />

B. Elyassi, University of Southern California, Los Angeles, Califorinia, USA<br />

F. Chen, University of Southern California, Los Angeles, Califorinia, USA<br />

M. Sahimi, University of Southern California, Los Angeles, Califorinia, USA<br />

T. Tsotsis, University of Southern California, Los Angeles, Califorinia, USA<br />

Silicon carbide (SiC) is a material with very attractive chemical and physical<br />

properties, which have made it a great candidate for membrane applications,<br />

especially those related to gas separation and hydrogen production. The focus of<br />

the present paper is on using two different approaches to prepare asymmetric<br />

nanoporous silicon carbide membranes which are applicable in reactive<br />

separations involving the water-gas shift and methane steam reforming<br />

reactions, where the membrane has to function in the presence of hightemperature<br />

steam. The first approach for the preparation of SiC microporous<br />

membranes, involves the pyrolysis of thin allyl-hydridopolycarbosilane (AHPCS)<br />

films coated, using a combination of slip-casting and dip-coating techniques, on<br />

tubular SiC macroporous supports. Combining slip-casting with dip-coating<br />

significantly improved the reproducibility in preparing high quality membranes.<br />

The membranes were studied for their transport characteristics, and steam<br />

stability. In addition, a novel method, based on the use of sacrificial interlayers,<br />

was also developed for the preparation of nanoporous SiC membranes, which<br />

involves periodic and alternate coatings of polystyrene sacrificial interlayers and<br />

SiC AHPCS layers on the top of slip-casted tubular SiC supports. Membranes<br />

prepared by this technique exhibit single gas ideal separation factors of He and<br />

hydrogen over Ar in the range of (176-420) and (100-200), respectively, with<br />

permeances that are typically two to three times higher than those of SiC<br />

membranes prepared previously by the more conventional techniques.<br />

Preparation of asymmetric nanoporous SiC membranes is also carried out using<br />

chemical-vapor infiltration/chemical-vapor deposition (CVI/CVD) techniques. We<br />

have used macroporous SiC disks and tubes as supports, and tri-isopropylsilane<br />

as the precursor. We have also developed two dynamic models to describe the<br />

preparation and the transport characteristics of the membranes by the CVD/CVI<br />

technique. First, a coarse-grained pore network model was developed for the<br />

membranes, that provides accurate predictions for the ideal selectivities, as well<br />

as the transport of binary gas mixtures. A continuum model of the CVD/CVI<br />

membrane preparation process has also been developed, which is validated by<br />

the results of a comprehensive experimental study. The results of the model

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