Biryukov G.M., Osina M.A., Bogdanovskaya V.A., Radina
M.V.
National Research University "Moscow Power Engineering
Institute", Russia
INFLUENCE OF CARBONIC CARRIER CHARACTERISTICS ON SUSTAINABILITY OF FUEL CELL
CATHODE CATALYST
Consumption of
electric power is increasing progressively. However, conventional energy
sources in such areas as aviation, space, submarine service, etc. including
decentralized, emergency and standby energy supply are unable to cover
requirements of consumer. Consequently, to develop autonomous energy systems,
or electrochemical energy facility, is required. These facilities consists of
electrochemical generators, system to store and prepare fuel and oxidizer, electric
transducers, system to utilize generated heat. Electrochemical generator includes
as follows: fuel cell (FC) stack, facility to provide fuel and oxidizer, and
withdraw reaction product and heat, automation system to regulate and control
temperature (thermostatic control), power and other parameters of the system [1].
The main part of FC
is a membrane electrode assembly (MEA) that consists of electrolyte, cathode
and anode layers (active layers). Active layer is a suspension (catalytic
“ink”) that covers membrane surface or gas diffusion layer. This catalytic
“ink” generally comprises three components as follows:
·
catalyst with
carbonic carrier: nanoparticles of metal phase coated on dispersive carbon
material;
·
solvent: water diluted spirits;
·
ionomer solution: solid polymer
electrolyte – Nafion that is solved in a mixture of low-molecular aliphatic
alcohols.
Fig. 1 represents principal diagram of hydrogen air FC.
Fig. 1. Principal diagram of the device layout of H2-air FC:
MEA
– membrane electrode assembly; FP – flow plates; НE –
heating elements; CP – clamping plates; FS – fluoroplastic shims; ТC – thermocouples.
One of the critical
issues that prevents to develop and implement FC as a source of current in
various power facilities is a degradation of cathode catalyst [2]. This leads
to decreasing of its electrochemically active surface (determined with a cyclic
voltammogram (CVA)), activity (determined by voltage upon voltage density 0.5
A/cm2 on a discharge characteristic), and degradation of carbonic
carrier (across potential cycling). Method of accelerated stress-testing [3] allows
to determine specifications of degradation processes in FC hydrogen-air.
Fig. 2. CVA of 20 % Pt/CNT
cathode catalyst in the MEA
Fig. 3. Results of accelerated
stress testing of the MEA
1.
Korovin
N.V. Fuel cells and electrochemical facilities. – М.: Publishing House МEI, 2005. – 280 p.
2.
Tarasevich M.R., Korchagin O.V. Rapid diagnostics of characteristics and
stability of fuel cells proton-conducting electrolyte // Russian Journal of Electrochemistry. 2014. V. 50. № 8. P. 737-750.
3.
Kuzov
A.V., Tarasevich M.R., Modestov A.D., Korchagin O.V. Degradation processes in hydrogen-air fuel cell as a
function of the operating and composition of membrane-electrode assemblies // Russian Journal of Electrochemistry.
2016. V. 52. № 7. P. 705-715.