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@ARTICLE{Brands:10079,
author = {Brands, K. and Uhlmann, D. and Smart, S. and Bram, M. and
Diniz da Costa, J.C.},
title = {{L}ong-term flue gas exposure effects of silica membranes
on porous steel substrate},
journal = {Journal of membrane science},
volume = {359},
issn = {0376-7388},
address = {New York, NY [u.a.]},
publisher = {Elsevier},
reportid = {PreJuSER-10079},
pages = {110 - 114},
year = {2010},
note = {The project "Nano-structured ceramic and metal supported
membranes for gas separation-METPORE" is funded by the
Bundeswirtschaftsministerium fur Wirtschaft und Technologie
(BMWi), Forderkennzeichen 0327746A. Funding is gratefully
acknowledged. The authors also acknowledge financial support
through the Innovation Funds given by the Queensland
Government (Australia), with further support in Australia
from Tarong Power, Stanwell Corporation and the Australian
Coal Association via the Centre for Low Emissions Technology
(www.clet.net), and in Germany by EnBW, E.ON and RWE. The
authors would like to thank D. Sebold for her help in
characterizing the membranes, F. Hauler, G. Gottlicher
(EnBW) and C. Blessing (EnBW) for experimental support.},
abstract = {In this work we investigate the long-term effects of
exposing an inorganic membrane for 1100 h in a flue gas
stream of a coal power plant. Of particular importance, from
an industrial testing perspective, was the effect of fly ash
deposition, water vapour and acid gases on the integrity of
the membrane made of cobalt silica coated on a substrate of
316L steel, with interlayers of 310S steel,
yttria-stabilized zirconia and gamma-alumina. Subsequent to
the flue gas testing, the membrane was characterized for
single gas permeance, SEM and EDX spectroscopy. Diffusion of
nickel and chromium during sintering was observed at the
interface of the 316L/310S steels, resulting in a reduced
capacity to withstand corrosion in this area. Single gas
permeation testing following flue gas exposure revealed a
maximum permeation of 1.85 x 10(-8) mol m(-2) s(-1) Pa-1 and
2.13 x 10(-8) mol m(-2) s(-1) Pa-1 for helium and hydrogen
respectively, and selectivity of 5.1 and 5.2 for He/N-2 and
H-2/CO2 respectively, was achieved at a pressure difference
of 2 x 10(5) Pa (2 bar) at 200 degrees C. The permeation
behavior of the membrane appeared to be altered as a result
of flue gas exposure with the membrane displaying a reduced
H2 flux in contrast to an unexposed but otherwise identical
membrane which displayed fluxes an order of magnitude higher
than the membrane used in the power plant. This change in
permeation behavior was thought to be the result of
densification of the silica matrix following long-term
exposure to flue gas containing water vapour.
Micro-fractures in the surface of the cobalt silica gas
separation layer were also observed, possibly the result of
expansion due to corrosion. However, bulk diffusion was not
observed suggesting that the layer was not completely
compromised. (C) 2010 Elsevier B.V. All rights reserved.},
keywords = {J (WoSType)},
cin = {IEF-1},
ddc = {570},
cid = {I:(DE-Juel1)VDB809},
pnm = {Rationelle Energieumwandlung},
pid = {G:(DE-Juel1)FUEK402},
shelfmark = {Engineering, Chemical / Polymer Science},
typ = {PUB:(DE-HGF)16},
UT = {WOS:000279953300013},
doi = {10.1016/j.memsci.2010.02.065},
url = {https://juser.fz-juelich.de/record/10079},
}