پديدآورندگان :
jabbari Zeynab banana@aut.ac.ir Amirkabir University of Technology , Afsham Neda banana@aut.ac.ir Amirkabir University of Technology , Nassernejad Bahram banana@aut.ac.ir Amirkabir University of Technology , Fallah Narges banana@aut.ac.ir Amirkabir University of Technology , Javanbakht Mehran banana@aut.ac.ir Amirkabir University of Technology
كليدواژه :
Carbon paper , Oxidation , CO tolerance , Fuel cell
چكيده فارسي :
The Proton Exchange Membrane Fuel Cells (PEMFCs) and Direct Methanol Fuel Cells (DMFCs)
are considered good alternatives as power generation systems for different kinds of applications
because of their high efficiency in energy conversion and suitability. One of the PEMFC’s
problems appears when using hydrogen obtained from reforming, because it contains CO, which
can strongly compete with H2 for adsorption on Pt surface. This contamination lead to the metal
poisoning and decreases the anode performance. On the other hand the oxidation of methanol
produces CO-type intermediates in the anode of DMFC, which also lead to the Pt metal poisoning
[1]Studies have shown that particle size, exposed crystal faces and oxidation state of carbon
supports are important factors which have influence on specific activity of the Pt electrocatalyst for
CO and methanol oxidation[2]. Unfortunately, the non-treated carbon is often hydrophobic, so
there is particular interest to carry out treatments on the carbon surface to activate it by additional
functional groups. Studies show the effect of electrochemical treatment of GC support [3] and
oxidation of the HOPG substrate on CO and methanol oxidation [4]. But, as we know, these
supports are not real support for fuel cells. In this study, the carbon paper (CP), as electrode
support, is activated by applying anodic and cathodic potential to introduce oxygenated surface
compounds. The Pt was electrodeposited on treated and non-treated electrode and the effect of
treatment for CO tolerance was investigated. To the best of the authors’ knowledge, studies about
the effect of anodic oxidation for CP as a support on Pt electrodeposition is scarcely found in the
literature [5] and there is no research for these oxidation of CP as catalyst support for enhancing
the Pt activity for CO tolerance in fuel cells electrode. 0.25 cm2 CP (TGPH-090;Toray) was used
as the support for electrochemical catalyst preparation. Oxidation on carbon papers were performed
by applying +2V for anodic oxidation and -2 V for cathodic oxidation for 5 min in 0.5M H2SO4
solution. Pt was electrodeposited onto the CP by electrodeposition in an electrolyte solution of
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0.2M H2SO4 +2mM H2PtCl6.6H2O. Single-pulse chronoamperometry electrodepsition by adjusting
potential profile of 0V (1 s) and 1.15 V (600 s) (vs.Ag/AgCl(sat)) was done. Oxidation of carbon
leads to a formation and growth of oxide layer, causing the surface of individual fibers becomes
roughened and more defects appear on the surface which is in accordance with the SEM pictures.
The surface of the cathodic electrode has more defect than anodic electrode that shows the changes
in surface functional groups is different for cathodic and anodic electrooxidation. The oxidized CPs
were characterized by micro-ATR-FTIR for both oxidized electrodes. Primary alcohol, ether,
phenol, carboxylic, quinne and conjugated ketone functional group peaks can be observed. The
strength of these peaks is weaker for anodic electrode which may result from the higher oxidation
of carbon paper during the cathodic oxidation. Indeed, Phenol oraal tertiary alcohol and lactone
peaks only appear after cathodic treatment which shows additional oxygen functional groups on
CP which is prepared by cathodic oxidation. Cyclic voltammetry diagrams of the oxidized CPs
(Fig.1) show the magnitude of the background current is highly sensitive to the electrochemical
treatment and it is small for non-treated CP in compare with oxidized ones, but in the case of the
anodic a high capacitive-like background current is observed. The CV of anodic shows evidence of
surface oxidation due to the presence of one anodic and cathodic peak current is assigned to the
hydroquinone–quinone redox couple (in the ranges0.3–0.4 V ) [6] In cathodic electrode the weak
reduction peak at 0.3–0.4 V together with the results of FTIR and SEM analyses, indicate that
higher oxidation states of carbon were produced. [1]
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On the other hand, more small particles are noticeable when the deposition is performed on anodic
CP(Fig.2). Further, although the metal particles seems bigger on cathodic electrode, uniformly
dispersion of Pt with low agglomeration is visible (Fig.2.c). It seems that it is because of the
different type of oxygen groups and amount of them, which have influence on nucleation and
agglomeration of the particles on treated supports. The higher coulombic charge of the hydrogen
adsorption/desorption zone for oxidized electrodes in Fig.3 is related to an increase in ECSA of the
catalyst due to lower particle size. [1]. The CO oxidation abilities of the electrodes were evaluated
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by CO-stripping experiment (Fig.4). The cathodic electrode has lower onset potential of CO
electro-oxidation (0.44V) and peak potential of CO electro-oxidation (0.59V) than that of anodic
(0.65V) and non-treated electrode (0.70V). These negative shifts show that cathodic electrode has
more effective for CO oxidation in compare with anodic and non-treated electrode. The CV curves
of methanol electrooxidation for electrodes (Fig.5) were consisted of two well-defined peaks at the
forward and backward scans which were related to oxidation of methanol molecules and oxidation
of intermediates, respectively. The ratio of the forward anodic peak current (If) to the backward
anodic peak current (Ib) which can be used to gauge the tolerance exhibit larger ratios of
If/Ib(1.50,1.41) for cathodic and anodic electrodes in compare with non-oxidized electrode. The
onset potential of methanol oxidation occurs at 0.135 V, which is relatively 100 mV negative than
non-treated electrode. Results show that cathodic electrode has more tolerance for intermediate
species in compare with anodic and non-treated electrode. The stability of the electrodes in
methanol was also evaluated by amperometric measurements.(Fig.6).Treated electrodes are more
stable than non-treated one and cathodic electrode was able to maintain the highest current density
and higher stability among all electrodes. We have revealed how the treatment of carbon with
cathodic and anodic oxidizing improves the activity of the electrocatalyst in methanol and CO
electrooxidations on Pt surface. Our results show that in addition to the size of the catalyst the type
of the oxidation and the amount of functional groups and type of them has great effect on the
activity of the electrodes on CO tolerance when the carbon support is oxidizing and oxygenated
functional groups has two ways to effect on catalytic activity: first, by changing the size and metal
dispersion in electrodeposition of Pt on carbon paper. Second, these groups were likely contributing
to methanol and CO electro-oxidations similar to bifunctional mechanism .These additional oxygen
functional groups on cathodic oxidized CP make this electrode more tolerant in compare with other
electrodes in this study.