Investigation of the Permeability of Pure Gases in Sol-Gel Derived Al 2o 3 Membrane
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BRONZE
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Yes
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Abstract
The preparation, characterization and pure gas permeation of sol-gel derived alumina membranes were investigated in this work. The effects of acid concentration/type and water content on the particle size in the sols and pore size distributions of the unsupported membrane were investigated by N 2 adsorption/desorption isotherms and Dynamic Light Scattering. Increasing the H +/Al 3+ mole ratio from 0.1 to 0.25 caused the hydrodynamic sol particle size and BJH pore size to decrease from 65 to 30 nm and 3.6 to 2.9 nm, respectively. The pore size increased from 2.8 nm to 3 nm upon increasing the calcination temperature from 500 to 600°C. Unsupported membranes were heat treated in the 200 to 1200 °C range for the characterization of the phase structure. Pinhole and crack free alumina membranes about 3 μm (2-layer) in thickness was observed from the SEM pictures with insignificant infiltration. The CO 2 permeability through the double layer γ-Al 2O 3 membrane calcined at 600 °C was 2.25*10 -7 mol/m 2.s.Pa, and had a slight pressure dependence indicating Knudsen Diffusion and Laminar Flow being the effective transport mechanisms. Upon the calcination of a similar 2-layer alumina membrane at 500°C, the CO 2 permeability decreased to 1.51 *10 -8 mol/m 2.s.Pa. without pressure dependence.
Description
Proceedings of the 8th Conference and Exhibition of the European Ceramic Society; Istanbul; Turkey; 29 June 2003 through 3 July 2003
Keywords
Alumina, Ceramic, Gas permeation, Membrane, Sol-Gel, Sol-Gel, Gas permeation, Alumina, Membrane, Ceramic
Fields of Science
02 engineering and technology, 0210 nano-technology, 01 natural sciences, 0104 chemical sciences
Citation
Topuz, B., Çiftçioğlu, M., and Çakıcıoğlu Özkan, S. F. (2004). Investigation of the permeability of pure gases in sol-gel derived Al 2O 3 membrane. Key Engineering Materials, 264-268(I), 399-402. doi:10.4028/www.scientific.net/KEM.264-268.399
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OpenCitations Citation Count
2
Volume
264-268
Issue
I
Start Page
399
End Page
402
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CrossRef : 2
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2
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871
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476
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