Composite Membranes for Hydrogen
Separation
Chendong Zuo*, T. H. Lee, S.E. Dorris, U.
Balachandran, and Meilin Liu*
Energy Technology Division, Argonne National
Laboratory, Argonne, IL 60439
* School of Materials Science and Engineering,
Georgia Institute of Technology
Atlanta, GA 30332
As the demand for hydrogen increases, a practical way of
separating pure hydrogen from a gas mixture (e.g.,
synthesis gas) is becoming more important. Among the
various separation techniques, dense membranes of mixed
ionic-electronic conductors (MIECs) offer a simple way
for obtaining hydrogen from gas streams at high
temperatures. Because an MIEC membrane will transport
both protons and electronic defects, hydrogen separation
can be achieved without electrodes and external circuitry.
Although various perovskite-type oxides have been
reported to have high proton conductivity in a hydrogen-
containing atmosphere, the chemical stability of these
materials under practical conditions is still a concern.[1]
For example, BaCeO
3
-based proton conductors display
the highest conductivity among this class of materials;
however, it is unstable in a CO
2
-containing
atmosphere.[2] In contrast, BaZrO
3
-based proton
conductors have excellent stability but relatively low
proton conductivity.[3] These results suggest that the
solid solution between cerate and zirconate may offer a
good compromise between proton conductivity and
chemical stability.[4,5]
Compounds in the Ba(Ce
x
Zr
0.8-x
)Y
0.2
O
3-α
(0.0≤x≤0.8)
system were synthesized by solid-state reaction from
stoichiometric mixtures. X-ray diffraction analysis
showed that a solid solution was formed over the whole
range of x values. As shown in Figure 1, the total
conductivities of sintered disks, as determined using
impedance spectroscopy, decreased with increasing
zirconium content in wet 4% H
2
/helium gas.
0.90 0.95 1.00 1.05 1.10 1.15 1.20 1.25 1.30
0.01
Conductivity (S/cm)
1000/T (K
-1
)
Ba(Ce
0.7
Zr
0.1
)Y
0.2
O
3
in wet 4% H
2
Ba(Ce
0.6
Zr
0.2
)Y
0.2
O
3
in wet 4% H
2
Ba(Ce
0.5
Zr
0.3
)Y
0.2
O
3
in wet 4% H
2
Ba(Ce
0.4
Zr
0.4
)Y
0.2
O
3
in wet 4% H
2
Figure 1. Total conductivities of Ba(Ce
x
Zr
0.8-x
)Y
0.2
O
3
in
wet 4% H
2
as function of temperature (the humidity was
introduced by passing the gas through a water bubbler at
room temperature).
Because the electronic conductivities of Ba(Ce
x
Zr
0.8-
x
)Y
0.2
O
3-α
are relatively low, composite membranes
consisting of Ni and Ba(Ce
0.6
Zr
0.2
)Y
0.2
O
3
have been
developed for hydrogen separation. As shown in Figure 2,
hydrogen flux increased with temperature from 600 to
900
o
C. The highest flux, 0.09 cm
3
(STP)/min-cm
2
at
900
o
C, was obtained for a membrane of 0.46-mm-thick
when wet 4% H
2
was used as the feed gas. Preliminary
measurements of membrane stability in atmospheres
containing 10% CO
2
showed that this composite (cermet)
membrane is stable up to 50 hours, as shown in Figure 3.
600 650 700 750 800 850 900
0.01
0.02
0.03
0.04
0.05
0.06
0.07
0.08
0.09
0.10
Flux (cm
3
/min-cm
2
)
Temperature (
o
C)
Ba(Ce
0.6
Zr
0.2
)Y
0.2
O
3
/Ni, wet 4% H
2
Figure 2. Hydrogen flux through a composite membrane
consisting of Ni and Ba(Ce
0.6
Zr
0.2
)Y
0.2
O
3
) (0.46 mm
thick) using wet 4% H
2
(balance He) as feed gas.
0 10 20 30 40 50
0.0
0.1
0.2
0.3
0.4
0.5
0.6
Flux (cm
3
/min-cm
2
)
Time (h)
Ba(Ce
0.6
Zr
0.2
)Y
0.2
O
3
/Ni, wet 10% CO
2
Figure 3. Time dependence of hydrogen flux for
composite membrane consisting of Ba(Ce
0.6
Zr
0.2
)Y
0.2
O
3
and Ni (0.46 mm thick) in wet 10% CO
2
(balance H
2
) at
900
o
C.
Acknowledgements
This work was supported by U.S. Department of Energy,
Office of Fossil Energy, National Energy Technology
Laboratory's Gasification Technologies Program, under
Contract W-31-109-Eng-38.
Reference
1. K.D.Kreuer, Solid State Ionics 97, (1997) 1-15.
2. S. V. Bhide and A. V. Virkar, J. Electrochem. Soc.,
146, (1999) 4386-4392.
3. K.D.Kreuer; Solid State Ionics 125, (1999) 285-302.
4. K. Katahira, Y. Kohchi, T. Shimura, H. Iwahara,
Solid State Ionics 138, (2000) 91-98.
5. K. H. Ryu, S. M. Haile, Solid State Ionics 125,
(1999) 355-367.
Abs. 1053, 204th Meeting, © 2003 The Electrochemical Society, Inc.
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