% IMPORTANT: The following is UTF-8 encoded. This means that in the presence
% of non-ASCII characters, it will not work with BibTeX 0.99 or older.
% Instead, you should use an up-to-date BibTeX implementation like “bibtex8” or
% “biber”.
@ARTICLE{Czyperek:10121,
author = {Czyperek, M. and Zapp, P. and Bouwmeester, H. J. M. and
Modigell, M. and Ebert, K. and Voigt, I. and Meulenberg, W.
A. and Singheiser, L. and Stöver, D.},
title = {{G}as separation membranes for zero-emission fossil power
plants: {MEM}-{BRAIN}},
journal = {Journal of membrane science},
volume = {359},
issn = {0376-7388},
address = {New York, NY [u.a.]},
publisher = {Elsevier},
reportid = {PreJuSER-10121},
year = {2010},
note = {Financial support from the Helmholtz Association of German
Research Centres (Initiative and Networking Fund) through
the MEM-BRAIN Helmholtz Alliance is gratefully
acknowledged.},
abstract = {The objective of the "MEM-BRAIN" project is the development
and integration of ceramic and polymeric gas separation
membranes for zero-emission fossil power plants. This will
be achieved using membranes with a high permeability and
selectivity for either CO2, O-2 or H-2, for the three CO2
capture process routes in power plants, thus enabling CO2 to
be captured with high-purity in a readily condensable form.
For the pre-combustion process, we have developed ceramic
microporous membranes that operate at intermediate
temperatures (<= 400 degrees C) for H-2/CO2 separation. For
the oxyfuel process, we have developed dense ceramic mixed
oxygen ionic-electronic conducting membranes that operate at
800-1000 degrees C for O-2/N-2 separation. The
perovskite-type oxide Ba0.5Sr0.5Co0.8Fe0.2O3-delta
(BSCF5582) was taken as the reference material for this
application. For the post-combustion process, polymeric and
organic/inorganic hybrid membranes have been developed for
CO2/N-2 separation at temperatures up to 200 degrees C. In
addition to the development of membranes, we consider the
integration of the membranes into power plants by modelling
and optimization. Finally, specific technical, economic and
environmental properties of CO2 capture as a component in a
CCS process chain are assessed, analysing the energy supply
system as a whole. (C) 2010 Elsevier B.V. All rights
reserved.},
keywords = {J (WoSType)},
cin = {IEF-STE / IEF-1 / IEF-2 / JARA-ENERGY / JARA-HPC / IEK-STE},
ddc = {570},
cid = {I:(DE-Juel1)VDB815 / I:(DE-Juel1)VDB809 /
I:(DE-Juel1)VDB810 / $I:(DE-82)080011_20140620$ /
$I:(DE-82)080012_20140620$ / I:(DE-Juel1)IEK-STE-20101013},
pnm = {Nachhaltige Entwicklung und Technik / Rationelle
Energieumwandlung},
pid = {G:(DE-Juel1)FUEK408 / G:(DE-Juel1)FUEK402},
shelfmark = {Engineering, Chemical / Polymer Science},
typ = {PUB:(DE-HGF)16},
UT = {WOS:000279953300017},
doi = {10.1016/j.memsci.2010.04.012},
url = {https://juser.fz-juelich.de/record/10121},
}