Investigation of the response of separate electrodes in a polymer electrolyte membrane fuel cell without reference electrode
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Abstract
The paper presents electrochemical measurements carried out in a PEMFC with a view to determining the separate kinetics of the electrode reactions. For this purpose, the separate response of one electrode (anode or cathode) was magnified by dilution of the reacting gas, respectively hydrogen and oxygen, and comparison of the experimental data in the form of steady voltage-current variations and impedance spectra. Experiments were carried out at 60 °C and ambient pressure. Water management was thoroughly controlled so that the gases leaving the cell had the same relative humidity in all experiments of one series. Hydrogen oxidation, although rapid, corresponds to overpotentials up to 50 mV at high dilution rates and current densities. Assuming a Tafel–Volmer mechanism, the exchange current density of the anode reaction at the Pt surface is of the order of 1 mA cm−2. The two techniques employed led to Tafel slopes of oxygen reduction ranging from 120 to 150 mV/decade, with an exchange current density near 1 μA cm−2, in good agreement with published data.
Keywords
electrochemical investigation hydrogen oxidation impedance spectroscopy oxygen reduction PEM Fuel cellsAbbreviations
- bT
Tafel coefficient, V/decade
- C
concentration, mol m−3
- D
diffusion coefficient, m2 s−1
- e
electron
- F
Faraday’s constant, 96487 C mol−1
- I
current, A
- i
current density, A m−2 or A cm−2
- iL
limiting current density, A m−2 or A cm−2
- i0
exchange current density, A m−2 or A cm−2
- J
specific flux mol m−2 s−1
- m
partitioning coefficient
- n
number of electrons involved
- P
pressure, Atm
- Q
pseudocapacitance, S cm−2 sα
- R
gas constant, 8.314 J K−1 mol−1
- r
specific resistance, Ω cm2
- T
temperature, K
- Urev
reversible voltage, V
- V
cell voltage, V
- Z
impedance, Ω
Greek letters
- α
exponent of constant phase element
- α
charge transfer coefficient
- γ
ration of effective area over geometrical area
- δ
layer thickness, m
- ɛ
porosity
- η
overpotential, V
- ∞
bulk conditions
Subscripts
- a
anode
- c
cathode
- CPE
constant phase element
- ct
charge transfer
- diff
diffusion
- eff
effective
- L
limiting
- N
Nafion
- ohm
ohmic
- Ox
oxidant
- Red
reductant
- 0
electrode surface
- 1
gas diffusion electrode
- 2
electrode structure
Notes
Acknowledgements
The authors are indebted to Region Lorraine and CNRS for funding facilities – through PACEM “PRI” – and the Ph.D. grant allocated to M.B.
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