(SFCTO)was prepared by solid state reaction method.Oxygen permeation flux through this membrane was investigated at operating temperature ranging from 750℃ to 950℃ and different oxygen partial pressure.XRD measurements indicated that the compound was able to form single-phased perovskite structure in which part of Fe was replaced by Cu and Ti.The oxygen desorption and the reducibility of SFCTO powder were characterized by thermogravimetric analysis and temperature programmed reduction analysis
respectively.It was found that SFCTO had good structure stability under low oxygen pressure at high temperature.The addition of Ti increased the reduction temperature of Cu and Fe.Performance tests showed that the oxygen permeation flux through a 1.5 mm thick SFCTO membrane was 0.35-0.96 ml·min
-1
·cm
-2
under air/helium oxygen partial pressure gradient with activation energy of 53.2 kJ·mol
-1
.The methane conversion of 85%
CO selectivity of 90%and comparatively higher oxygen permeation flux of 5 ml·min
-1
·cm
-2
were achieved at 850℃
when a SFCTO membrane reactor loaded with Ni-Ce/Al
2
O
3
catalyst was applied for the partial oxidation of methane to syngas.
Abstract
Dense membrane with the composition of SrFe
0.6
Cu
0.3
Ti
0.1
O
3-δ
(SFCTO) was prepared by solid state reaction method.Oxygen permeation flux through this membrane was investigated at operating temperature ranging from 750℃ to 950℃ and different oxygen partial pressure.XRD measurements indicated that the compound was able to form single-phased perovskite structure in which part of Fe was replaced by Cu and Ti.The oxygen desorption and the reducibility of SFCTO powder were characterized by thermogravimetric analysis and temperature programmed reduction analysis
respectively.It was found that SFCTO had good structure stability under low oxygen pressure at high temperature.The addition of Ti increased the reduction temperature of Cu and Fe.Performance tests showed that the oxygen permeation flux through a 1.5 mm thick SFCTO membrane was 0.35-0.96 ml·min
-1
·cm
-2
under air/helium oxygen partial pressure gradient with activation energy of 53.2 kJ·mol
-1
.The methane conversion of 85%
CO selectivity of 90% and comparatively higher oxygen permeation flux of 5 ml·min
-1
·cm
-2
were achieved at 850℃
when a SFCTO membrane reactor loaded with Ni-Ce/Al
2
O
3
catalyst was applied for the partial oxidation of methane to syngas.
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references
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Catalytic oxidation of methane for methanol production over copper sepiolite: Effect of noble metals
Oxygen vacancies enriched Ni-Co/SiO2@CeO2 redox catalyst for cycling methane partial oxidation and CO2 splitting
A Study of Acetylene Production by Methane Flaming in a Partial Oxidation Reactor
Preparation of anodic catalysts via in situ exsolution of Pt nanoparticles for a methane oxidation enhanced SOEC process
Research progress on the monolithic catalyst for hydrogenation of CO2 to methane
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