A transient TGA study on oxygen permeation properties of perovskite-type ceramic membrane

1998 ◽  
Vol 110 (3-4) ◽  
pp. 209-221 ◽  
Author(s):  
Y Zeng ◽  
Y.S Lin
2009 ◽  
Vol 156 (5) ◽  
pp. E81 ◽  
Author(s):  
Ken Watanabe ◽  
Daisuke Takauchi ◽  
Masayoshi Yuasa ◽  
Tetsuya Kida ◽  
Kengo Shimanoe ◽  
...  

2004 ◽  
Vol 13 (1-3) ◽  
pp. 613-618 ◽  
Author(s):  
H. Takamura ◽  
K. Okumura ◽  
Y. Koshino ◽  
A. Kamegawa ◽  
M. Okada

Ceramics ◽  
2019 ◽  
Vol 2 (2) ◽  
pp. 246-259 ◽  
Author(s):  
Cyril Gaudillere ◽  
Julio Garcia-Fayos ◽  
Jorge Plaza ◽  
José M. Serra

An original asymmetric tubular membrane for oxygen production applications was manufactured in a two-step process. A 3 mol% Y2O3 stabilized ZrO2 (3YSZ) porous tubular support was manufactured by the freeze-casting technique, offering a hierarchical and radial-oriented porosity of about 15 µm in width, separated by fully densified walls of about 2 µm thick, suggesting low pressure drop and boosted gas transport. The external surface of the support was successively dip-coated to get a Ce0.8Gd0.2O2−δ – 5mol%Co (CGO-Co) interlayer of 80 µm in thickness and an outer dense layer of La0.6Sr0.4Co0.2Fe0.8O3−δ (LSCF) with a thickness of 30 µm. The whole tubular membrane presents both uniform geometric characteristics and microstructure all along its length. Chemical reactivity between each layer was studied by coupling X-Ray Diffraction (XRD) analysis and Energy Dispersive X-Ray spectroscopy (EDX) mapping at each step of the manufacturing process. Cation interdiffusion between different phases was discarded, confirming the compatibility of this tri-layer asymmetric ceramic membrane for oxygen production purposes. For the first time, a freeze-cast tubular membrane has been evaluated for oxygen permeation, exhibiting a value of 0.31 ml·min−1·cm−2 at 1000ºC under air and argon as feed and sweep gases, respectively. Finally, under the same conditions and increasing the oxygen partial pressure to get pure oxygen as feed, the oxygen permeation reached 1.07 ml·min−1·cm−2.


2000 ◽  
Vol 164 (1-2) ◽  
pp. 167-176 ◽  
Author(s):  
Zongping Shao ◽  
Guoxing Xiong ◽  
You Cong ◽  
Weishen Yang

Desalination ◽  
2011 ◽  
Vol 270 (1-3) ◽  
pp. 64-75 ◽  
Author(s):  
Ali Ghadimi ◽  
Mohammad Ali Alaee ◽  
Amir Behrouzifar ◽  
Amir Atabak Asadi ◽  
Toraj Mohammadi

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