R&D OF HIGH PERFORMANCE SOLID POLYMER ELECTROLYTE WATER ELECTROLYZER IN WE-NET
M.YAMAGUCHI, K.YAGIUCHI, K.OKISAWA
Environment & Energy Laboratory
Fuji Electric Corporate Research and Development,Ltd.
2-2-1,Nagasaka,Yokosuka city
240-01,Japan
ABSTRACT
Commissioned to execute subtask 4, "Development of Hydrogen Production
Technologies" in WE-NET project of NEDO-MITI, we have been developing technologies
for high performance solid polymer electrolyte electrolyzers. In terms of
technical features, our technological approach calls for membrane-electrode
assemblies to be formed by a hot-press method. In this development acitivities,
diverse types of 50cm2 membrane-electrode assemblies have been fabricated by
composing of various iridium oxide powders as anode catalysts and various
ion-exchange membranes. Consequently, we have obtained a electrolyzer with a
membrane-electrode assembly composed of high surface area iridium dioxide (46m2/g)
as anode catalysts and a thin ion-exchange membrane (52mm) which registered
1.59V of cell voltage at a current density of 1A/cm2 at 80degree.
1. INTRODUCTION
In WE-NET project, the performance target of electrolyzers is as follows:
Energy efficiency 80 `90%
Current density 1 `3A/cm2
To achieve this target, we have been developing technologies of manufucturing
membrane-electrode assemblies' which are main components of solid polymer
electrolyte electrolyzers, by a hot-press method. In this method, a catalyst film
is supurposed over an ion-exchange membrane, and is combined with the ion-exchange
membrane by means of hot-pressing. This technique comes with the following
features:
(1)Different types of catalysts, including oxides,can be applied.
(2)Because carrier catalysts can be used, use of noble metal catalysts can be reduced.
(3)Three-dimensional electrode/membrane interface can be achieved.
In the development activities under way, the hot-press method mentioned above was
adopted and diverse types of membrane-electrode assemblies were fabricated by
composing of various iridium dioxide powders as anode catalysts and various
ion-exchange membranes. Based on the results of performance evaluations of those
samples, studies were being conducted to elucidate the composition of materials
in a membrane-electrode assembly with low cell voltage.
2.EXPERIMENT METHOD
Fabrication Method of Membrane-Electrode Assemblies
The membrane-electrode assemblies used for the experiment were manufactured
through the following process shown in Fig.1.
(1)Preparation of catalyst and PTFE mix solution.
(2)Catalyst film formation from the mix solution.
(3)Natural drying
(4)Heat treatment of the catalyst film
(5)Laminating the catalyst film and an ion-exchange membrane, and then hot-pressing.
Membrane-Electrode Assemblies Composed of Various Iridium Dioxide Powder
Iridium dioxide is the best electrocatalyst for anodes. This material is fine
powder prepared by pyrolysis of iridium hydroxide, and the activity as anode
catalysts depends on the temperature of the pyrolysis, because the content of
metal iridium as by-product and the property of specific surface area are changed
by pyrolysis condition. Five iridium oxide powder samples were prepared by
changing pyrolysis temperature in the range of 200`800 degree. As shown in Table 1,
diverse types of 50cm2 membrane-electrode assemblies composed of different iridium
dioxide powders were fabricated.
Membrane-Electrode Assemblies Composed of Various Ion-Exchange Membranes
As shown in 2, diverse types of 50cm2 membrane-electrode assemblies
were fabricated. Those were composed of various ion-exchange membranes with
different thickness and equivalent weight (EW) made of perfluorosulfonic acid by
three chemicals companies.
Performance Measurement of Membrane-Electrode Assemblies
A laboratory cell was built in filter-press type consisting of a membrane
electrode assembly with a support collector and a current collector fitted on both
sides, as can be seen in Fig.2. The support collector was a titanium fiber-sintered
plate, which was platinum-coated. The current collector was a titanium plate with
grooves of 2mm wide 3mm deep mounted in parallel at a pitch of 4mm, which was also
platinum-coated. The membrane-electrode assemblies were placed in the laboratory
cell and their cell voltages were measured at various current densities at 80 degree
using the operating system illustrated in Fig.3.
3.RESULTS AND DISCUSSION
Effect of Varieties of Iridium Dioxide Powders on Cell Performance
As shown in Table 1, the higher the temperature of pyrolysis of iridium
hydroxide is, the larger the specific surface area of iridium dioxide is. Figure
4 shows the results of the experiment indicating the cell voltage vs the current
density of diverse types of membrane-electrode assemblies composed of various
iridium dioxide powders as anode catalysts. As the pyrolyzing temperature of
iridium hydroxide is lowered, the cell voltage of membrane-electrode assemblies
decreased. Consequently, the membrane-electrode assemblies composed of iridium
dioxide powder prepared by pyrolysis at 200degree registered lower cell voltage of
1.61V at 1A/cm2 than the other assemblies. This suggests iridium dioxide powder
having large specific surface area is effective to decrease cell voltage.
Effect of Varieties of Ion-Exchange Membranes on Cell Performance
Figure 5 shows the curves of the cell voltage vs the current density of
diverse types of membrane-electrode assemblies composed of various ion exchange
membranes. Thinner and smaller EW ion-exchange membranes gave lower cell voltage.
No.9 membrane-electrode assembly composed of the ion-exchange membrane of 52 mm
thickness and 1000 EW registered the lowest cell voltage of 1.59V at 1A/cm2.
Durability of Membrane-Electrode Assemblies
Figure 6 shows the cell voltage change with time for 5400hours in No.7
membrane-electrode assembly. The cell registered 1.62 `1.63V of cell voltage and
9 6.8% of current efficiency at 1A/cm2 and 80 degree during the operation. This
suggests the durability of membrane-electrode assemblies fabricated by the
hot-press method is very high.
4.CONCLUSION
Based on the results of performance evaluation of various membrane-electrode
assemblies, we elucidate the membrane-electrode assembly with such low cell
voltage as 1.59V at 1A/cm2 must be composed of iridium dioxide powder prepared
by pyrolysis of iridium hydroxide at 200 degree and ion exchange membranes of about
50 mm thickness. We also verified from the life test experiment that the
durability of membrane-electrode assemblies made by hot-press method is very
high.
Acknowledgement
This work was performed as a R&D program of the New Energy Development
Organization (NEDO) under the WE-NET project of the Agency of Industrial Science
and Technology, MITI.
REFFERENCE
M.Yamaguchi, T.Shinohara, K.Okisawa, International Hydrogen and Clean Energy Symposium, '95,P.205-208(1995)
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