Article ID | Journal | Published Year | Pages | File Type |
---|---|---|---|---|
9610384 | Catalysis Today | 2005 | 5 Pages |
Abstract
The first oxygen permeation data of a dense hollow fiber perovskite membrane based on BaCoxFeyZrzO3 â δ are reported. The hollow fiber was prepared by a phase inversion process. Dense fibers were obtained with the following typical geometries: outer diameter, 800-900 μm; inner diameter, 500-600 μm; length, 30 cm. The O2-permeation through the hollow fiber perovskite membrane was studied in a high-temperature gas permeation cell under different operation conditions. The increase of the helium gas flow rate reduces the oxygen partial pressure (pO2) on the core side and a higher oxygen permeation flux is observed. High oxygen flux of 0.73 m3 (O2)/(m2 (membrane) h) was achieved at 850 °C under the operation parameters Fair (shell side) = 150 ml/min and FHe (core side) = 30 ml/min. The oxygen partial pressure dependence of the O2 permeation flux indicated an interplay of both surface reaction and bulk diffusion as rate limiting steps. During 5 days of permeation a high and stable oxygen flux was observed. X-ray diffraction patterns of fresh and spent membranes after the permeation measurements revealed that no degradation after oxygen permeation appears.
Related Topics
Physical Sciences and Engineering
Chemical Engineering
Catalysis
Authors
Cristina Tablet, Gerd Grubert, Haihui Wang, Thomas Schiestel, Michael Schroeder, Bernd Langanke, Jürgen Caro,