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@PHDTHESIS{Hauler:15112,
author = {Hauler, Felix},
title = {{H}erstellung und {C}harakterisierung von keramik- und
metallgestützten {M}embranschichten für die
{CO}$_{2}$-{A}btrennung in fossilen {K}raftwerken},
volume = {80},
issn = {1866-1793},
school = {Faktultät für Maschinenba. Ruhr-Universität Bochum},
type = {Dr.},
address = {Jülich},
publisher = {Forschungszentrum Jülich GmbH Zentralbibiothek, Verlag},
reportid = {PreJuSER-15112},
isbn = {978-3-89336-662-0},
series = {Schriften des Forschungszentrums Jülich : Energie $\&$
Umwelt / Energy $\&$ Environment},
pages = {XVIII, 178 S.},
year = {2010},
note = {Record converted from JUWEL: 18.07.2013; Ruhr-Universität
Bochum, Faktultät für Maschinenbau, 2010},
abstract = {The separation of CO$_{2}$ in fossil fuel power plants has
become a very important issue due to the contribution of
this greenhouse gas to global warming. Thin microporous
membranes are promising candidates for separating CO$_{2}$
from gas flow before being exhausted into the atmosphere.
The membrane demands are good permeation and separation
properties and high stability under operation conditions.
Novel sol-gel derived materials composed of
TiO$_{2}$/ZrO$_{2}$ and stabilized SiO$_{2}$ seem to be
promising due to their good chemical stability and
microporous character, especially for the separation of
H$_{2}$ and CO$_{2}$. Metallic substrates should be
preferred as membrane support because they exhibit practical
advantages combining good mechanical stability and the
benefit of facilitated joining. The present thesis deals
with the development of sol-gel derived microporous membrane
layers on ceramic and metallic supports for the separation
of CO$_{2}$. In this context, the optimized preparation of
high-quality membranes with TiO$_{2}$/ZrO$_{2}$ and Ni, Co,
Zr, Ti doped SiO$_{2}$ top layers is presented. These
multilayered membranes consist of a graded pore structure to
provide a smooth transition of the pore size from the
support to the functional layer. Due to the good surface
properties, the ceramic substrates only need one interlayer,
whereas the rough metallic substrates exhibiting larger
pores require a total of three interlayers to obtain an
enhanced surface quality. On both types of supports,
crack-free functional layers with a thickness below 100 nm
were deposited by dip-coating. The unsupported and supported
sol-gel materials used for the top layers were investigated
in terms of structural properties by thermal analysis,
sorption measurements, X-ray diffraction and electron
microscopy. Gas permeation tests with He, H$_{2}$, CO$_{2}$
und N$_{2}$ were carried out to determine the membrane
performance with regard to permeation rates and separation
properties. Ceramic supported stabilized SiO$_{2}$ membranes
exhibit a 100 \% separation of He and H$_{2}$ towards larger
gas molecules such as CO$_{2}$ and N$_{2}$. This occurs when
all the manufacturing steps which include sol preparation
and layer deposition under cleanroom conditions are
optimized. In contrast, the layers are not applicable for
separation of CO$_{2}$ and N$_{2}$ by reason of very low or
no flow rates. The microporous TiO$_{2}$/ZrO$_{2}$
functional layers show a lack of viable permeation and
separation properties suggesting a low pore volume. The
metal supported membranes with SiO$_{2}$ based functional
layer demonstrate a selectivity of H$_{2}$/CO$_{2}$ up to 50
and exhibit a very good separation performance compared to
similar membranes in literature. Ceramic supported SiO$_{2}$
based functional layers prepared by Rapid Thermal Processing
(RTP) with a deposition and calcination time of one hour
were investigated to reduce the membrane production time.
Gas permeation results show a 100 \% separation of H$_{2}$
towards CO$_{2}$ and N$_{2}$ confirming the excellent layer
quality. The results are an important contribution to the
optimized preparation of high-quality microporous membrane
layers exhibiting a high potential for CO$_{2}$ separation
in fossil fuel power plants. The successful layer deposition
on metallic substrates and the significantly reduced heat
treatment time by using RTP are a further step of
development in membrane technology.},
cin = {IEK-1},
ddc = {500},
cid = {I:(DE-Juel1)IEK-1-20101013},
pnm = {Rationelle Energieumwandlung},
pid = {G:(DE-Juel1)FUEK402},
typ = {PUB:(DE-HGF)11 / PUB:(DE-HGF)3},
url = {https://juser.fz-juelich.de/record/15112},
}