High-purity oxygen production by a dead-end Ba 0.5Sr 0.5Co 0.8Fe 0.2O 3-δ tube membrane

Publikation: Beitrag in FachzeitschriftArtikelForschungPeer-Review

Autorschaft

  • Fangyi Liang
  • Heqing Jiang
  • Huixia Luo
  • Ralf Kriegel
  • Jürgen Caro

Externe Organisationen

  • Max-Planck-Institut für Kohlenforschung
  • Fraunhofer-Institut für Keramische Technologien und Systeme (IKTS)
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Details

OriginalspracheEnglisch
Seiten (von - bis)95-100
Seitenumfang6
FachzeitschriftCatalysis today
Jahrgang193
Ausgabenummer1
Frühes Online-Datum1 Feb. 2012
PublikationsstatusVeröffentlicht - 15 Okt. 2012

Abstract

High-purity oxygen was produced by dead-end Ba 0.5Sr 0.5Co 0.8Fe 0.2O 3-δ (BSCF) tube membranes which were sealed by a reaction-diffusion sintering process. First, phase stability of BSCF membrane in a pure oxygen atmosphere - as it is present on the permeate side of the membrane - was studied at 750 and 950 °C, respectively. After the identification of stable operation conditions of BSCF membranes, we studied the oxygen permeation at 950 °C using dead-end BSCF tubes (1 cm outer diameter, 1 mm wall thickness) in (i) a pressure-driven process, (ii) a vacuum process, and (iii) combining both techniques. In all cases, a high oxygen purity of almost 100 vol.% can be obtained at operation temperatures ≥ 850 °C. The oxygen permeation flux, the oxygen recovery, and the oxygen ionic conductivity were investigated. It was found that - for the same oxygen partial pressure difference - the oxygen permeation flux in the vacuum process is significantly higher than that in the pressure-driven process at all investigated temperatures. Moreover, in all cases, oxygen permeation and oxygen ionic conductivity can be described by the Wagner theory for bulk diffusion of oxygen ions as rate-limiting step with the logarithmic ratio of the oxygen partial pressures on feed and permeate sides as driving force.

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Zitieren

High-purity oxygen production by a dead-end Ba 0.5Sr 0.5Co 0.8Fe 0.2O 3-δ tube membrane. / Liang, Fangyi; Jiang, Heqing; Luo, Huixia et al.
in: Catalysis today, Jahrgang 193, Nr. 1, 15.10.2012, S. 95-100.

Publikation: Beitrag in FachzeitschriftArtikelForschungPeer-Review

Liang F, Jiang H, Luo H, Kriegel R, Caro J. High-purity oxygen production by a dead-end Ba 0.5Sr 0.5Co 0.8Fe 0.2O 3-δ tube membrane. Catalysis today. 2012 Okt 15;193(1):95-100. Epub 2012 Feb 1. doi: 10.1016/j.cattod.2011.12.016
Liang, Fangyi ; Jiang, Heqing ; Luo, Huixia et al. / High-purity oxygen production by a dead-end Ba 0.5Sr 0.5Co 0.8Fe 0.2O 3-δ tube membrane. in: Catalysis today. 2012 ; Jahrgang 193, Nr. 1. S. 95-100.
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T1 - High-purity oxygen production by a dead-end Ba 0.5Sr 0.5Co 0.8Fe 0.2O 3-δ tube membrane

AU - Liang, Fangyi

AU - Jiang, Heqing

AU - Luo, Huixia

AU - Kriegel, Ralf

AU - Caro, Jürgen

PY - 2012/10/15

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N2 - High-purity oxygen was produced by dead-end Ba 0.5Sr 0.5Co 0.8Fe 0.2O 3-δ (BSCF) tube membranes which were sealed by a reaction-diffusion sintering process. First, phase stability of BSCF membrane in a pure oxygen atmosphere - as it is present on the permeate side of the membrane - was studied at 750 and 950 °C, respectively. After the identification of stable operation conditions of BSCF membranes, we studied the oxygen permeation at 950 °C using dead-end BSCF tubes (1 cm outer diameter, 1 mm wall thickness) in (i) a pressure-driven process, (ii) a vacuum process, and (iii) combining both techniques. In all cases, a high oxygen purity of almost 100 vol.% can be obtained at operation temperatures ≥ 850 °C. The oxygen permeation flux, the oxygen recovery, and the oxygen ionic conductivity were investigated. It was found that - for the same oxygen partial pressure difference - the oxygen permeation flux in the vacuum process is significantly higher than that in the pressure-driven process at all investigated temperatures. Moreover, in all cases, oxygen permeation and oxygen ionic conductivity can be described by the Wagner theory for bulk diffusion of oxygen ions as rate-limiting step with the logarithmic ratio of the oxygen partial pressures on feed and permeate sides as driving force.

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