• No results found

Electrocatalysis of cathodic oxygen reduction by metal phthalocyanines. Part II. Cobalt phthalocyanine as electrocatalyst: a mechanism of oxygen reduction

N/A
N/A
Protected

Academic year: 2021

Share "Electrocatalysis of cathodic oxygen reduction by metal phthalocyanines. Part II. Cobalt phthalocyanine as electrocatalyst: a mechanism of oxygen reduction"

Copied!
15
0
0

Bezig met laden.... (Bekijk nu de volledige tekst)

Hele tekst

(1)

Electrocatalysis of cathodic oxygen reduction by metal

phthalocyanines. Part II. Cobalt phthalocyanine as

electrocatalyst: a mechanism of oxygen reduction

Citation for published version (APA):

Brink, van den, F. T. B. J., Visscher, W., & Barendrecht, E. (1983). Electrocatalysis of cathodic oxygen reduction by metal phthalocyanines. Part II. Cobalt phthalocyanine as electrocatalyst: a mechanism of oxygen reduction. Journal of Electroanalytical Chemistry and Interfacial Electrochemistry, 157(2), 305-318.

https://doi.org/10.1016/S0022-0728(83)80358-1

DOI:

10.1016/S0022-0728(83)80358-1

Document status and date: Published: 01/01/1983 Document Version:

Publisher’s PDF, also known as Version of Record (includes final page, issue and volume numbers) Please check the document version of this publication:

• A submitted manuscript is the version of the article upon submission and before peer-review. There can be important differences between the submitted version and the official published version of record. People interested in the research are advised to contact the author for the final version of the publication, or visit the DOI to the publisher's website.

• The final author version and the galley proof are versions of the publication after peer review.

• The final published version features the final layout of the paper including the volume, issue and page numbers.

Link to publication

General rights

Copyright and moral rights for the publications made accessible in the public portal are retained by the authors and/or other copyright owners and it is a condition of accessing publications that users recognise and abide by the legal requirements associated with these rights.

• Users may download and print one copy of any publication from the public portal for the purpose of private study or research. • You may not further distribute the material or use it for any profit-making activity or commercial gain

• You may freely distribute the URL identifying the publication in the public portal.

If the publication is distributed under the terms of Article 25fa of the Dutch Copyright Act, indicated by the “Taverne” license above, please follow below link for the End User Agreement:

www.tue.nl/taverne

Take down policy

If you believe that this document breaches copyright please contact us at: openaccess@tue.nl

providing details and we will investigate your claim.

(2)

Elsevier Sequoia S.A., Lausanne - Printed in The Netherlands

E L E C T R O C A T A L Y S I S O F C A T H O D I C O X Y G E N R E D U C T I O N B Y M E T A L P H T H A L O C Y A N I N E S *

P A R T II. C O B A L T P H T H A L O C Y A N I N E A S E L E C T R O C A T A L Y S T : A M E C H A N I S M O F O X Y G E N R E D U C T I O N

F. VAN DEN BRINK **, W. VISSCHER and E. BARENDRECHT

Laboratory of Electrochemistry, Eindhoven University of Technology, P.O. Box 513, 5600 MB Eindhoven (The Netherlands)

(Received 1st July 1982; in final form 7th March 1983)

ABSTRACT

On the basis of a detailed description of the kinetics of oxygen reduction in alkaline solution on cobalt phthalocyanine film electrodes, a mechanism of the electrocatalysis of this reaction is proposed. The main features of this mechanism are those of a redox catalysis scheme, where the central metal atom of the electrocatalyst releases an electron to the adsorbed reactant (02 and, at high overpotential, HO 2 ), which is subsequently further reduced to products (HO~- and O H - respectively). The influence of the redox state of the electrocatalyst is explained in terms of a tentative description of the difference of the interaction of the electrocatalytic site with the respective depolarizers 02 and HO~.

The proposed model gives a satisfactory explanation of the observed kinetics of the reactions involved, as well as the observed correlations between electrocatalytic activity and properties such as phtha- locyanine redox potentials.

INTRODUCTION T h e n a t u r e o f t h e i n t e r a c t i o n b e t w e e n m e t a l p o r p h y r i n s a n d o x y g e n h a s b e e n i n v e s t i g a t e d w i d e l y in r e c e n t y e a r s , s i n c e t h e i r a p p l i c a b i l i t y as o x y g e n r e d u c t i o n e l e c t r o c a t a l y s t s w a s r e c o g n i z e d [1]. I n P a r t I [2] w e h a v e s h o w n t h a t c o b a l t p h t h a l o - c y a n i n e ( C o P c ) in a l k a l i n e s o l u t i o n c a t a l y s e s o n l y t h e r e d u c t i o n o f o x y g e n t o h y d r o g e n p e r o x i d e , i.e. in H 2 / O 2 f u e l cells w i t h C o P c o x y g e n e l e c t r o d e s o n l y s o m e 50% o f t h e t h e o r e t i c a l l y a v a i l a b l e p o w e r c a n b e u t i l i z e d . A p a r t f r o m t h e d i s a s t r o u s c o n s e q u e n c e s o f t h e b u i l d - u p o f H 2 0 2 in t h e cell, this will b e a g o o d e n o u g h r e a s o n t o a b a n d o n t h e i d e a o f C o P c as a o x y g e n r e d u c t i o n e l e c t r o c a t a l y s t .

* Part of thesis, Metal phthalocyanines as electrocatalysts for cathodic oxygen reduction, by F. van den Brink, Eindhoven, 1981.

** Present address: Dutch State Mines Central Laboratory, Department of Catalysis, P.O. Box 18, 6160 MD Geleen, The Netherlands.

(3)

We will show in a forthcoming part of this series that on iron phthalocyanine (FePc) electrodes, oxygen is completely reduced to water, in a direct reaction, so that the application of FePc as oxygen electrodes may be a feasible proposition. Then, however, the question remains as to what constitutes the vast difference between the, chemically very similar, compounds FePc and CoPc. To answer this question, it is necessary to have a reliable description of the kinetics and mechanism of oxygen reduction on both electrocatalysts. In this paper we will explain our kinetic results obtained for CoPc electrodes [2] in terms of a detailed mechanism, which gives an insight into the interaction between oxygen and the electrocatalyst molecule. SUMMARY OF KINETIC RESULTS

In Part I [2] we have given an accurate description of the kinetics of oxygen reduction on cobalt phthalocyanine film electrodes in alkaline solution. This descrip- tion, based mainly upon experiments with rotating ring disc electrodes and surface characterization by in situ methods such as cyclic voltammetry and ac impedance spectrometry, reveals the following fundamentals:

(1) On cobaltphthalocyanine (CoPc), oxygen is at low cathodic overpotential (ERH E > 0.3 V), exclusively reduced to hydrogen peroxide. Only at higher over- potential does some further reduction of H202 to H2 O occur, while the direct reduction of 02 to H 2 0 does not occur at all. Furthermore, no chemical decomposi- tion of H202 is detected, so the scheme of 02 reduction reduces to Fig. 1.

(2) d~//d log k~ -- - 4 0 mV in the vicinity of E R H E = 800 mV; below 800 mV the

slope decreases gradually, to reach - o ¢ at 450 mV. The slope 37//d log k 3 is ca. - 180 mV. The order in oxygen of reaction (2) is one.

(3) In the reduction, no O - O bonds are broken.

(4) Surface processes on the CoPc film are detected at 480 mV vs. RHE, both in the absence and presence of oxygen, and at 800 mV vs. R H E only when oxygen is present. All surface phthalocyanine molecules participate in these processes. INTERACTION OF OXYGEN WITH CoPc

The above observations can be partly explained by the assumption that electro- catalysis of oxygen reduction takes place by end-on adsorption of oxygen on the central Co-atom of CoPc, leading to activation of the oxygen molecule. That the central metal atom should be the electrocatalytic site follows, for example, from the correlation between the redox potential of the metal and the electrocatalytic activity

0:_+02 °. k2f._ H202 0 k3_

- H 2 0

(4)

in a series of metal porphyrins and phthalocyanines [3]. This will be treated in more detail below.

The assumption of end-on adsorption is corroborated by the observation that the oxygen-oxygen bond is not ruptured in the reduction 02 ~ H202, by MO consider- ations [4,5] and by the analogy with oxygen binding by natural porphyrins and their synthetic model compounds (e.g. picket fence porfines [6]), which have been shown to bind oxygen end-on.

The beginning of an explanation for the observed phenomena was originally given by Beck [7,8], who proposed a mechanism which he called " r e d o x catalysis". In this mechanism the redox reaction of the central metal atom plays a crucial role. On the basis of similar ideas, we will first propose a detailed mechanism and its accompany- ing kinetic equation for the reduction of oxygen to hydrogen peroxide on CoPc. Further, we will attempt to give a mechanistic description for the reduction of hydrogen peroxide to water.

Reduction of oxygen to hydrogen peroxide

The essential step of the " r e d o x catalysis" mechanism is the adsorption of oxygen at the electrocatalytic site, which is assumed to occur preferentially on the reduced metal atom according to

1

MPc + e - ~ M P c - (1)

followed by an adsorption step

2

M P c - + 02 ~ MPc-O~- (2)

where the charge transfer in the activated complex MPc-O~- may be only partial. The activated oxygen, which has at least some superoxo-character, is reduced further in the next step to hydrogen peroxide,

3

M P c - O 2 + H 2 0 + e - ~ MPc + H O 2 + O H - (3)

and the oxidized electrocatalyst is recycled.

Mechanisms like this are, in the electrochemical literature, usually treated with the concept of a

rate-determining step (rds, which is much slower than the other

steps, so that these are in virtual equilibrium). However, such a concept imposes rather extreme conditions on the relative rates of the steps involved. For example, for the sequence (1)-(3) it can be shown that the ratios of the rate constant of the rds to those of the other steps should be less than 10 -3 for the " r d s " to be truly rate determining. Therefore, it is better to derive the rate equation using the

steady-state

method.

For the sequence (1)-(3) this gives

--

i2/2 F = k~ [(MPc) exp( - a I f~ll ) -- ( M P c - ) exp(1 - a I )f~/l ]

= k2 [O2 ] ( M P c - ) - k_2 ( M P c - O 2 )

(5)

H e r e , i 2 is the current due to the reaction O z ~ H 2 0 2 , k, is the rate constant for the ith reaction *, a i its transfer coefficient and ~i is defined here as ( E - E~). The surface concentrations, denoted by ( ) , can be eliminated from eqn. (4) and expressed as fractions of their sum s, the total number of sites. The overall rate can then be written

- i , / 2 F = k2s[02]/((1 + e x p / ~ h ) ( 1 + ( k _ J k S ) exp a3f~3 )

+ ( k 2 [ O z l / k ~ ) exp et, f n l + ( k 2 [ O 2 ] / k S ) exp a3fa~3) (5) When k~ << k 2 [O2] , k S and for intermediate coverage eqn. (5) reduces to

i2

2 F -- k~s exp - alf~/1 (6)

predicting a Tafel slope of - 60/a I = - 120 mV for a~ = 0.5, and zeroth order in [O2]--so eqn. (6) clearly does not explain our results.

When k 2 [O2] , k_ 2 << k~, kS, the rate equation can be written as

- i 2 / 2 F = k 2 [02 ] s/(1 + exp f~/i ) (7) In this case the correct order in oxygen, viz. one, is predicted, but the Tafel slope will be - 6 0 mV for 7/1 >> 0 and - o0 for 7 h << 0 - - it will never be - 4 0 mV, irrespective of the value of a~, so step (2) is not the rds over the entire potential range. However,

for high overpotential (low E), the infinite Tafel slope indicates that there step (2) can be the rds.

When k S << k~, k 2 [O2] , eqn. (5) becomes

-i2/2F=

k2[O2]k_ 2

k~s

e x p - a 3 f v / 3 / 1 + e x p f n , + k _ 2 ( 8 ) which again predicts first-order dependence on oxygen concentration, and Tafel slopes of - 6 0 / ( 1 + a n ) = - 4 0 mV for 71 >> 0 and - 6 0 / a 3 = - 120 mV for *h << 0 **. Therefore, we may suppose that for low overpotential, where the observed Tafel slope of - 4 0 mV is predicted by eqn. (8), step (3) is the rds.

Of course, other schemes than those similar to ( 0 - ( 3 ) could be considered, which involve no surface reduction step (1). Several of those would give the same potential dependence of the Tafel slope. On the other hand, only a redox catalysis mechanism will be able to explain other experimental observations, such as the correlation of electrocatalytic activity and redox potential [3] (see below).

However, there are two problems with rate eqn. (5). The first is that, although it explains the observed behaviour at low and high overpotential, no values for the rate parameters k_2/k~, k E / k S and k _ E / k ] could be found which explain the inter- mediate potential range. However, as will be shown later, the behaviour in this potential range can be attributed to the simultaneous occurrence of a second sequence or reactions in parallel to reactions (1)-(3).

* Note: the roman k's used here should not be confused with the overall rate constants k2 ~ and k3, for the reductions 02 -~ H202 and H202 ---, H 2 0 [2].

(6)

The second problem is much more serious, since it is linked with the values chosen for E~' and E~'. The surface process occurring at ca. 800 mV only in the presence of oxygen must obviously be connected with reaction ( 3 ) - - s o E~' = 800 mV. However, the other surface process, at 480 mV, is surely not reaction (1). First, eqn. (5) predicts that the Tafel slope be between - 4 0 and - 6 0 mV, as long as E > 480 mV; we have observed, on the other hand, that the Tafel slope is already near infinity for potentials below ca. 700 mV. Therefore, E~' should be near 800 mV. Hence, the surface process found at 800 mV is due to both reactions (1) and (3).

Further, it is a well-known fact that cobalt porfines in general and cobalt phthalocyanine in particular form O2-adducts [9], especially in alkaline aqueous solutions, the most probable structure of these adducts being Co(III)-O2-.

Thus, we conclude from our kinetic measurements that the formal couple M P c / M P c - , used hitherto, is in fact the couple (Co(III)Pc)+/(Co(II)Pc) and that its standard potential lies between, say, 750 and 850 inV. This value should be contrasted with the standard potential of the hexa-aquo C o ( I I I ) / C o ( I I ) couple, 2.66 V vs. R H E - - s o it appears that the ligand environment of Co in a CoPe solid film in alkaline solution shifts the redox potential by some 1.85 V in the cathodic direction. This shift has been postulated on the grounds of our kinetic evidence, but we have not been able to prove, from independent sources, that the reduction indeed occurs at the indicated potential. Unfortunately, neither is such a proof provided in the available literature. There are, however, a number of indications that the reduction of (Co(III)Pc) + may indeed occur at ca. 0.8 V vs. RHE. First, in any solvent the Co-atom is surrounded by four nitrogen ligands in a square planar configuration, with the Co more or less in the plane of the nitrogens. This case can only be studied in non-aqueous solutions (ref. 10 and refs. therein). For the C o ( I I I ) P c / C o ( I I ) P c couple, the average value of the literature data for the standard potential is ca. 0.60 V vs. an aqueous saturated calomel electrode, i.e. ca. 1.67 V vs. R H E at p H = 14. F o r similar compounds, such as tetraphenyl- (1.37 V), etio- (1.35 V) and deutero- porphyrin (1.33 V), somewhat lower values are found [11]. Therefore, N4-chelation decreases the standard potential by at least 1 V. Further, the 4-coordination by Pc leaves the possibility of 5- or 6-coordination by axial ligands. These axial ligands are known to have a profound influence on both the redox properties [12,13] and the ligand exchange rates [9,14] of the complex. In this context especially the basicity and the ~r-acceptor strength of the axial ligands seem to be important [9,13]. By changing the ligand, differences in the M ( I I I ) / M ( I I ) redox potentials of up to 1 V can be brought about.

In the case of solid films, in aqueous alkaline solution, there are a number of candidates for the role of axial ligands. First, there are the meso nitrogen atoms of underlying phthalocyanine molecules (which are absent in porphyrins). These can act as ligands if the film has a rigid layered, roofing-tile structure, which to some extent limits their eapaeibility to act as axial ligands. Further, especially near the surface there is an abundance of H20, O H - and 02, all of which are known to be able to interact with metal phthalocyanines [9]. Therefore, there is a certain similar- ity between the surface region of solid Pc films and solubilized phthalocyanines. For

(7)

the latter, redox potentials ,ascribed to the M(III)/M(II) transition have been reported. For tetrasulphonated CoPc irreversibly adsorbed on pyrolytic graphite E = 0.8 V vs. SCE in 0.05 M H2SO 4 is given [15], corresponding to 1.1 V vs. R H E at p H = 14, assuming that the standard potential shifts by - 6 0 m V / p H unit. In this case, no pH-dependence was reported, but in the case of an irreversibly adsorbed solubilized cobalt porphyrin [16] a redox process has been detected at 1.08 V vs. R H E at pH = 14, showing this pH-dependence. Furthermore, it was shown that, upon addition of imidazole, the redox potential shifts 0.25 V in the cathodic direction. Therefore, the redox processes involved are in fact

C o ( I I I ) P c - O n + n 2 0 + e - ~ C o ( I I ) P c - H 2 0 + O H - and

(Co(III)Pc-Im) ÷ + e - ~ (Co(II)Pc-Im) respectively (Im stands for imidazole).

Finally, for non-solubilized phthalocyanines some values of the redox potential in concentrated (85% and 96%) sulphuric acid have been reported, i.e. in the presence of H 2 0 in a protic medium [7]. Although a direct comparison is hampered by the problem of the definition of pH in this medium, the values reported (0.52-0.56 V vs. aqueous SCE) do not disagree with our findings.

Therefore, the value found in the present communication for the redox potential of the Co(III)Pc/Co(II)Pc couple, which was inferred from our kinetic results, may be regarded as a reasonable one in view of the available literature data.

This leaves, however, the process at 480 mV to be explained. In Part I [2] we concluded that all surface phthalocyanine molecules contribute to this process. Therefore, it must be ascribed to a further reduction of the phthalocyanine molecules to C o P c - - - a species which has been detected spectrophotometrieaUy in CoPc films [17]. In this species the extra electron may or may not be localized on the central metal atom, since for similar compounds [11] in non-aqueous solutions values for the standard potential of the Co(II)/Co(I) couple between 0.3 and 0.6 V are f o u n d - - s o the standard potential in the solid state would hardly be shifted, contrary to that of the Co(III)/Co(II) couple. This lack of influence of complexation (by axial ligands), as found for the Co(III)/Co(II) couple, would indicate that the reduction process is that of the ring structure, rather than of the central Co-atom. However, formally we will write (Co0)Pc)-. The reduced form CoPc- is known to form O2-adducts which are comparable in stability to those of CoPc [9].

Now, however, we have, parallel to the sequence (1)-(3), an analogous mechanism involving adsorption of 02 on CoPc-, which plays a role for E < 480 mV;

4 CoPc + e - ~ CoPc- 5 C o P e - + 0 2 ~ CoPc-O 2 6 C o P c O f + H 2 0 + e - ~ CoPc + H O f + O H -

(9)

(1o)

(11)

(8)

For reaction 4 (eqn. 9) we can estimate the rate from the characteristic frequency found for the surface process at 480 mV, viz. k] >_ 500 s - l [2]. Further, for high overpotential reactions 4 - 6 will be the predominant route since all CoPe molecules will be in the reduced state CoPe- for E << 480 inV. In that potential range we have found a constant value for k2 r, viz. 3.1 × 10 -4 m s -1, so there reaction 5 (eqn. 10) is clearly the rds and we can estimate a value for ks: k 5 s = 3.1 × 10 -4 m s -I and, with

s = 5 X 1 0 - 6 mol m - 2 [2] we find k 5 --- 60 m 3 mol - l s - k Therefore, k 5 << k ] and we

assume reaction 4 to be in equilibrium. Further, the surface process (eqn. 1) is not detected in the frequency range of impedance measurements of 10-103 s - l and the Tafel slope near 800 mV is - 4 0 mV and surely no - 120 mV, which would have been found if reaction 1 (eqn. 1) were rds. Therefore, we conclude that reaction 1 is also in equilibrium. In that case we have for the parallel sequences 1 - 3 and 4 - 6 respectively,

i2(II) k2[O2](CoPc ) - k _ 2 ( C o P c + - O 2 ) = k~(CoPc+-O~ -) exp - a3f'rl 3 (12) 2 F

i2(I) k s [ O 2 ] ( e o P c - ) - k 5 ( C o P c - 0 2 ) = k ~ ( C o P c - O 2 ) e x p - a6fT/6 (13) 2 F

while the concentrations of the various CoPe species are related by

(CoPe +) = e/n, ' (CoPe) = e/n, (14)

(CoPe)

(CoPe-)

(CoPe +) + (CoPe) + (CoPe-) + ( C o P e + - 0 2 ) + ( C o P e - 0 2 ) = s (15)

F r o m eqns. (12)-(15) the rate equation is derived

i 2 = i2(II) + i2(I) (16)

i2(II) = k2[O2]s// + e/n' + e -/n' 1 + k~e_~dn6

2 F k _ 5 +

( k-2 ) k2[02] (17)

X 1 + k~ e-~3/n~ + k~ e-~3/n'

i2(I)2F ks[Oz]s / 1 + e fn4 1 + e fn' + k - 2 + k~e_~fn~

( k__zs_ ) k , [ 0 2 ] } (,8)

x 1-~ k~e_,d,~ + k~e_,dn,

For ~/4 >> 0 (i.e. E >> Eg = 480 mV) eqn. (17) reduces to eqn. (5)with k~ >> k 2 [O2], k~, while i2(I) << iz(II). For ~4 << 0, i2(II) ~ 0 and i2(I) >> i2(II).

Unfortunately, eqns. (16)-(18) contain too many unknown parameters to make an attempt to fit them numerically to the available data for k2 f feasible. However, by trial and error we have succeeded in obtaining a reasonably accurate fit, which is

(9)

shown in Fig. 2. W e conclude that eqns. (16)-(18) give a best a p p r o x i m a t i o n to the observed d a t a u n d e r the following conditions:

(1) Potential: E~' = 0.80 V, E~ = 0.82 V,

E:

= 0.48 V, 0.6 V ~< E6 ° ~< 0.8 V (2) Rate parameters: k 2 / k ~ ~< 1, k 5 / k ~ ~< 1 k 2 / k ~ = 7 , l ~ < k 5 / k ~ 10 (3) A s y m p t o t i c values: k 5 -~ 60 m 3 m o l - 1 s -

l,

k 2 = 0.75 k 5

T h e values given for k 2 [O2]/k ~ and k s / k ~ are u p p e r limits, since a n y value below t h e m gives an equally accurate fit.

T o summarize, b y c o m b i n i n g our data f r o m surface characterization with the kinetic d a t a over the entire potential range investigated (0-0.85 V vs. R H E ) we have b e e n able to p r o p o s e a detailed mechanism. F u r t h e r m o r e , since we have n o t c o n f i n e d ourselves to the c o n c e p t of a rate-determining step, we have been able to give a fairly accurate estimate of all pertinent mechanistic parameters involved.

F r o m the values of the s t a n d a r d potentials, we can calculate the equilibrium constants of the a d s o r p t i o n of o x y g e n and of the superoxide ion, O2-, on cobalt

log (kf2/k5s)

o ,

\

,o

/

!

/

-1.5 [

!

!

[

!

-2.0 ] I i I 20O 4 0 0 I I 1 J I 6 0 0 8 0 0 ERHE/mV

Fig. 2. Rate constant of reduction of oxygen to hydrogen peroxide on CoPc film electrodes vs. potential according to eqn. (16). (O) Measured points; ( ) calculated curve; ( . . . ) eqn. (18); ( . . . ) eqn. (17). For measured points, see ref. 2.

(10)

phthalocyanine. F r o m the sequence

( C o P c + - 0 2 ) CoPc*-O~- ~ C o P c + + O 2 , K o ; ( I I ) = (CoPc+)[O2_ ] 0 2 + H z O + e - ~ O H - + H O 2 , E ° = 0 . 2 6 5 V v s . N H E the standard potential of reaction (3) can be calculated

Ej' = 1.092 + 0.059 p K o ; ( I I ) V vs. R H E (19)

and analogously for that of reaction 6

Eg = 1.092 + 0.059 PKo2 (I) V vs. R H E (20)

at T -- 298 K and p H = 14. F r o m the standard potential of the overall reaction O 2 + H 2 0 + 2 e - ~ H O E + O H - , E ° = - 0 . 0 6 5 V vs. N H E

the standard potentials E~' and E~ can be expressed as functions of the K o ; 's and the equilibrium constants of reactions 2 and 5

Ko~(ii ) _ (CoPe + - O 2 ) ( C o a c - O ~ - ) (CoPe)[Oz] ' Ko2(I) = ( C o P c - ) [ O 2 ] The results are

E~' = 0.432 + 0.059 [ p K % ( I I ) - P K o ~ ( I I )] V vs. R H E (21) E~ = 0 . 4 3 2 + 0 . 0 5 9 [ p K o : ( I ) - p K % ( I ) ] V vs. R H E (22) Application of eqns. (19)-(22) to our case, where

E~' - 0.80 V E~ = 0.82 V /

E,~ = 0.48 V E~' 0.6-0.8 V / vs. R H E

Ko2(II ) = 2.4 × 10 -5 m 3 mol - l K o ~ ( I I ) = 41 m 3 m o l - '

Ko~(I)=3.4×

10 4 - 14 m3 m o l - l

Ko~(I)=2.2×

1 0 5 - 89 m3 mol - '

The large value of the K o i ' s c o m p a r e d to that of the K % ' s gives us an indication why CoPe electrocatalyses oxygen r e d u c t i o n - - the catalyst stabilizes the superoxide ion by the formation of a complex and thus increases its concentration.

The lower values for Ko2(I ) and Ko~(I ) apply when Eft = 0.80 V is taken. Since we do not expect E~ to differ much from Ej', we will henceforth use E~ = 0.8, although we cannot be sure about this value. However, we have found only one peak at about 800 mV in the cyclic v o l t a m m o g r a m of CoPe films in the presence of oxygen, and this could be associated with b o t h reactions 3 and 6. N o w we can calculate some of the rate constants. Assuming that all surface phthalocyanine molecules are active sites, we have s = 5 × 10 -6 tool m -2, so k 5 = 60 m 3 mol - l s -~ and k 2 = 0.75 k5 = 45 m 3 mol - l s -1. Using the Ko2'S, we find k_ 2 = 2 × 1 0 6 S - 1 and

(11)

T A B L E 1

Steps involved in the reduction 0 2 ---, H 2 0 o n CoPc, and their characteristics inferred from observed kinetics and proposed mechanism

Reaction Properties 1. 2. 3. 4. 5. 6. C o + Pc + e - ~ C o P c C o P c + O 2 ~ C o P c + - O 2 C o P c + - 0 2 + H 2 ° + e - ---, C o P c + + H O E + O H - C o P c + - O 2 ~ C o P c + + O~- C o P c + e - ~ C o P c - C o P c - + 0 2 ~ C o P c - O ~ - C o P c - O 2 + H 2 0 + e - ~ C o P c + H O { + O H - C o P c - O { ~ C o P c + O { E~ = 0.80 V, k~ > 103 s - I K o 2 ( I I ) = 2 . 4 × 10 - s m 3 m o l - l; k 2 = 4 5 m 3 m o l - l s - l , k _ 2 = 2 × 106 s -1 E ~ = 0.82 V, k~ = 3 × 1 0 5 s -1 K o ~ (II) = 40 m 3 t o o l - 1 E g = 0.48 V, k ] > 500 s - 1 K o 2 ( I ) = 15 m 3 m o l - J; k 5 = 6 0 m 3 m o 1 - 1 s - I ; k _ 5 = 4 s - l E g = ( 0 . 6 - 0 . 8 ) V, 0.4 s - 1 ~< kS ~< 4 s - l K o ~ ( E ) = 90 m 3 t o o l - 1

k _ 5 = 4 s -1. Since k 2 / k ~ = 7 and 1 ~< k _ 5 / k ~ ~< 10, we have k~ = 3 × 105 s -1 and 0.4 s - ~ ~< k~ ~< 4 s - t. The rate of reaction 1 is not known, but we k n o w that it must be high compared to k 2, k~ must be at least 103 s - i . Finally, we can estimate k ] > 500 s -1, from the characteristic frequency of the associated surface state capacitance. These results have been summarized in Table 1.

T o summarize, we have found that oxygen reduction on CoPc proceeds, depen- dent on potential, on both CoPc, where the metal is supposed to be in its Co(II) state, and o n C o P c - , where the extra electron is most probably delocalized over the Pc-ring ~r-system. On both types of sites, the overall rate is mainly determined by the rate constant for the adsorption of oxygen; only for low overpotentials has the reduction of adsorbed oxygen a rate comparable to that o f the desorption of oxygen. The proposed mechanism is corroborated by:

(1) the fact that both CoPc and C o P c - are k n o w n to form O2-adducts; (2) the presence o f surface processes at + 0.80 and + 0.48 V vs. RHE;

(3) the values found for the Tafel slopes at low, intermediate and high overpoten- tial;

(4) the fact that no O - O bond rupture occurs in the overall reaction.

Reduction of hydrogen peroxide to water

A s stated in the introductory summary, hydrogen peroxide is reduced at CoPc to water only at low potentials. The availability and accuracy of the data on the overall

rate c o n s t a n t k 3 for this reaction are much poorer than those on k f, discussed in the

previous section. For this reason we will not present a detailed mechanism for this reaction. However, using our results, we can make a few observations on the mechanism.

The most important feature is that the reaction starts only at potentials < 0.4 V vs. RHE, while the reversible potential of the couple H O 2 / O H - is 1.69 V vs. RHE.

(12)

Therefore, some reaction with a reversible potential in the range of, say, 0.4-0.6 V must play a role. One possibility would be reduction of H O f to the hydroxyl radical" HO~- + H 2 0 + e - ~ O H - + 2 O H - E ° = 0.575 V vs. R H E

This would mean a mechanism such as

C o P c - + HO~- + H 2 0 ~ C o P c - O H + 2 O H - (23)

C o P c - O H + e - ~ C o P c - O H - (24)

C o P c - O H - ~ CoPc + O H - (25)

CoPc + e - ~ C o P c - (26)

The first step of this mechanism would involve adsorption of H O ; on C o P c - , which is, at 300 mV, the predominant species, and we have shown [2] that this is a fast process c o m p a r e d to the overall rate. Then, charge transfer followed b y O - O bond breaking would have to occur, whereupon the O - - i o n would be protonated very fast. Therefore, if the first step were rate determining, it would have to be because the charge transfer

C o P c - - H O 2 ~ CoPc - O - + O H -

is slow. In that case, however, the rate, i.e. k3, would have to be independent of electrode potential, which is not what we have observed.

The second step (eqn. 24), will be very fast in any case, since its standard potential is 2.811 V vs. R H E [18], and even if this were lowered b y adsorption, the adsorption would have to be extremely strong (AGad s --- - 2 . 5 eV) to account for the low potentials where the overall reaction occurs. Thus, the second step is ruled out as well.

The third step (eqn. 25), as the rds would again lead to a potential-independent rate. Therefore, we conclude that there the fourth step (eqn. 26) must be rds. The rate equation is in that case

-i3/2F

= k~ exp -

a4f~14

(27)

which predicts a Tafel slope b = - 6 0 / a 4 mV. To explain the observed Tafel slope b --- - 180 mV, a 4 would have to be ca. ½. This does not contradict our findings for oxygen reduction, since in the rate equation used there (eqn. 16), a 4 does not appear.

S O , ot 4 = 1 is possible and could indicate that the extra electron is not localized on the central Co-ion, but is delocalized on the rr-ring system.

The value of k~ is known (see Table 1), viz. k ] > 500 s - l, so we know that the (intrinsic) rates of the reactions given in eqns. (23)-(25) should be considerably larger, i.e. > 103 s - i. In principle it is also possible that a mechanism without redox catalysis applies, i.e.

C o P c - + H O ; + H 2 0 + e - ~ C o P c - - O H . + 2 O H - C o P c - - O H • + e - ~ C o P c - + O H -

(13)

slope of - 6 0 / a mV as well. On the other hand, it would not take into account the fact that hydrogen peroxide is a rather strong oxidator, which is likely to oxidize C o P c - , although it is not able to oxidize CoPc. Further, in this mechanism, it is still more difficult to understand a Tafel slope of - 180 mV, i.e. a = ½. However, we are not able to discriminate between the various possibilities. We therefore conclude that, although we cannot be certain, most probably reduction of hydrogen peroxide follows a mechanism where H O E is adsorbed on C o P c - , which is followed by bond breaking. This leaves an adsorbed hydroxyl radical, which is reduced in a fast step to a hydroxyl ion. The rate-determining factor is the availability of C o P c - , where the extra electron is probably delocalized in the ¢r-system of the Pc ring.

In our opinion, a mechanism like this, with bond breaking after the first electron transfer and therefore involving a radical, is the only possibility as long as only one catalytic site is involved in the reaction. A simultaneous two-electron transfer will only be possible if H O 2- interacts with two sites simultaneously. A mechanism like this could predominate on, for example, reduced platinum, but on CoPc films the sites are separated by a distance of the order of the molecular diameter, i.e. 1.2 nm [19], so the hydrogen peroxide molecule is too small to have a two-site interaction. DISCUSSION AND CONCLUSIONS

The mechanism for the reactions involved in oxygen reduction on CoPc can be summarized as follows.

The reduction of oxygen to hydrogen peroxide proceeds by two parallel paths, both of which involve slow adsorption of oxygen on the electrocatalytic site, followed by oxidation of the site by the adsorbed oxygen molecule. For the path which predominates in the low overpotential region, the site is the (central metal atom of the) CoPc-molecule, while the high overpotential path involves the C o P c - monoanion. On the latter species, some reduction of H O f also takes place, by a fast adsorption of H O f , followed by O - O bond cleavage. Here, the rate of reduction of CoPc to C o P c - is limiting.

One may wonder why the rates of adsorption of 0 2 on CoPc and C o P c - are of the same order of magnitude and why, in connection with this, the fast adsorption step of H O 2 on both species, leads to O - O bond rupture and reduction only on the monoanion.

The indifference of the 0 2 adsorption rate to the redox state of the electrocatalyst is a further indication that, in C o P c - , the formal oxidation state of the central metal atom is Co(II) rather than Co(I) and that a reduced ring system, Pc-, prevails. The extra electron on the ring system exerts only a marginal influence on the relative energies of the Co d-orbitals, which play a predominant role in the formation of the adsorption complex between CoPc and 0 2, together with the ~r-orbitals of the oxygen molecule. On the other hand, in H O { the interacting orbitals will have much more of the nature of lone pairs, and therefore a substantially higher energy on an absolute scale. Therefore, we suppose that the more negative charge on the ring system does not produce an alteration of the relative positions of the Co d-orbitals

(14)

(to give a change in 02 adsorption behaviour), but raises them to a level where a better match with the (high-energy) lone pairs of H O 2 gives a more efficient interaction, i.e. not the rate of adsorption but the adsorption energy is changed. We hope to elaborate on this point in a future communication, where we will give our views on the catalytic site-depolarizer interactions in oxygen reduction on phthalo- cyanines.

A second point which needs clarification is that of the standard potential of the reduction process Co(III)Pc ~-Co(II)Pc. Our observations [2] that for low over- potential the Tafel slope for oxygen reduction is - 40 mV and for high overpotential

- o0 forces us to accept that this reduction plays a role in oxygen reduction and that

its standard potential is about 0.8 V - - w h i c h is also the potential where, judging from the available literature data, we would expect it to occur. On the other hand, we have not been able to detect it in our impedance measurements. These were conducted in the frequency range between 10 and 5000 s-1, while from our kinetic results we estimate the rate constant of the reduction process to be at least 10 3 s - 1 - - s o , we have not missed the process because the measurement frequencies were too high.

Therefore, there must be some reason why the C o ( I I I ) / C o ( I I ) transition is not visible in the impedance spectra. Possibly this can be related to the conductivity of the CoPe film. This is seen to be rather low for high electrode potentials, while it has a maximum at about 0.48 V [2]. We believe that, at high potentials, conduction occurs by chains of Co-atoms, linked by oxygen molecules:

... - O - O - C o - O - O - C o - O - O - . . .

Such a condition mechanism would be especially effective near the film surface, since there oxygen can diffuse from the atmosphere or from the electrolyte solution into the film. On the other hand, at low potentials, we have C o P c - , where the extra electron is supposed to be delocalized in the phthalocyanine ~r-system. Such a delocalized electron is expected to increase conductivity considerably, and indeed such an increase is observed.

Now the impedance measurements were performed in deoxygenated solution. Since cathodic polarization is expected to remove oxygen from the film surface, the surface resistance of the film is increased at high potentials. Then, there will be a larger ohmic potential drop in the film surface, so that the C o ( I I I ) / C o ( I I ) transition will virtually be shifted to much more positive potentials and will not be visible in the impedance spectrum.

On the other hand, since at low potential values conduction is mainly by the ~r-system, the conductivity will not be affected by the presence or absence of oxygen, so the C o P c / C o P c - transition will still be visible in the impedance.

A final point which has previously been ignored is the role which is possibly played by the adsorption of O H - - i o n s on the electrocatalytic sites. This is most likely to occur at CoPc+:

( C o a c O H ) C o P c + + O H - ~ C o P c 0 H KOH = ( C o P c + ) [ 0 H _ ]

(15)

T h i s w o u l d m o d i f y o u r k i n e t i c eqns. (5) a n d (16) b y the r e p l a c e m e n t o f the t e r m s e/n~ b y (1 + K o H [ O H - ] ) e fÈ'. T h i s d o e s n o t affect the e q u a t i o n s s e r i o u s l y as l o n g as K o H [ O H - ] << 1. If, however, this c o n d i t i o n d o e s n o t a p p l y , t h e o r d e r of t h e c u r r e n t s in [ O H - ] w o u l d b e - 1. Since w e h a v e n o t v a r i e d the O H - c o n c e n t r a t i o n , we are n o t in a p o s i t i o n to e s t i m a t e KOH. H o w e v e r , an o r d e r - 1 in [ O H - ] has b e e n r e p o r t e d [15].

I n c o n c l u s i o n , we c a n say t h a t we h a v e s a t i s f a c t o r i l y c o m p l e t e d a n d e x p l a i n e d the k i n e t i c d e s c r i p t i o n give p r e v i o u s l y . T h i s was a c c o m p l i s h e d b y the a d o p t i o n o f a " r e d o x c a t a l y s i s " m o d e l , w h i c h e x p l a i n s all a v a i l a b l e d a t a . T h e m a i n f e a t u r e o f this m o d e l is, t h a t the p o l a r i z e r , w h i c h is 0 2 o v e r the e n t i r e p o t e n t i a l r a n g e i n v e s t i g a t e d , a n d H O 2- o n l y a t h i g h o v e r p o t e n t i a l , is a d s o r b e d on the c a t a l y t i c site (the c e n t r a l C o - a t o m o f CoPc), w h i c h s u b s e q u e n t l y releases a n e l e c t r o n to the a d s o r b e d species. T h i s is s u b s e q u e n t l y r e d u c e d to the r e s p e c t i v e p r o d u c t s , w h i c h are d e s o r b e d , a n d r e d u c t i o n o f the site c o m p l e t e s the cycle. S u c h a p r o c e s s is f o u n d to o c c u r b o t h o n C o P c at l o w o v e r p o t e n t i a l , a n d o n C o P c - at h i g h o v e r p o t e n t i a l . T h e d i f f e r e n c e in the e l e c t r o c a t a l y t i c b e h a v i o u r of t h e t w o c a t a l y s t species C o P c a n d C o P c - is t e n t a t i v e l y e x p l a i n e d w i t h r e g a r d to their r e s p e c t i v e e l e c t r o n i c d i s t r i b u t i o n s a n d their i n f l u e n c e u p o n the n a t u r e o f the c a t a l y s t - a d s o r b e n t c o m p l e x . ACKNOWLEDGEMENTS T h e p r e s e n t i n v e s t i g a t i o n s h a v e b e e n c a r r i e d o u t w i t h the s u p p o r t o f the N e t h e r - l a n d s F o u n d a t i o n for C h e m i c a l R e s e a r c h (S.O.N.) a n d w i t h f i n a n c i a l a i d f r o m the N e t h e r l a n d s O r g a n i z a t i o n for the A d v a n c e m e n t o f P u r e R e s e a r c h (Z.W.O.).

REFERENCES

1 F. van den Brink, E. Barendrecht and W. Visscher, Rec. Trav. Chim. Pays Bas, 99 (1980) 253. 2 F. van den Brink, E. Barendrecht and W. Visscher, J. Electroanal. Chem., 157 (1983) 283. 3 J.P. Randin, Electrochim. Acta, 19 (1979) 83.

4 H. Jahnke, M. SchOnborn and G. Zimmermann, Top. Curr. Chem., 61 (1976) 133; H. Metzner (Ed.), Photosynthetic Oxygen Evolution, Academic Press, London, 1977, p. 439.

5 M. Savy, P. Andro, G. Bernard and G. Magner, Electrochim. Acta, 19 (1974) 403. 6 J.P. Collman, Acc. Chem. Res., 10 (1977) 265.

7 F. Beck, Ber. Bunsenges. Phys. Chem., 77 (1973) 353. 8 F. Beck, J. Appl. Electrochem., 7 (1977) 239.

9 B.R. James in D. Dophin (Ed.), The Porphyrins, Vol. 5, Academic Press, New York, 1978 p. 205. 10 J.A.R. van Veen, Thesis, Leiden University, 1980.

i I R.H. Felton in ref. 9, p. 53.

12 D. de Montauzon, R. Poilblanc, P. Lemoine and M. Gross, Electrochim. Acta, 23 (1978) 1247. 13 A.B.P. Lever and J.P. Wilshire, Inorg. Chem., 17 (1978) 1145.

14 R.F. Pasternak and M.A. Cobb, J. Inorg. Nucl. Chem., 35 (1973) 4327. 15 J. Zagal, P. Bindra and E. Yeager, J. Electrochem. So¢., 127 (1980) 1506. 16 R.R. Durand and F.C. Anson, J. l~lectroanal. Chem., 134 (1982) 273.

17 V.E. Kazarimov, M.R. Terasevich, K.A. Radyushkina and V. Andreev, J. Electroanal. Chem., 100 (1979) 225; M.R. Tarasevich, K.A. Radyushkina and S.1. Andruseva, Bioelectrochem. Bioenerg., 4 (1977) 18.

18 J.P. Hoare, GMR 2948 Res. Publ., 1979.

Referenties

GERELATEERDE DOCUMENTEN

However, it should be noted that by reason of the nature of the OSIS operating environment none of the measuring instruments discussed so far, with the exception of the

Ook bleken sommi- ge van de onderzochte genen gelokaliseerd te zijn in gebieden waar, in vergelijking met de andere soort, veel inserties en deleties voorkomen terwijl de aan-

Het gaat er om parameters van gezondheid van het individuele dier te defi- niëren en deze te testen op hun voorspellende waarde waardoor gerichte maatregelen genomen kunnen worden

De expositie, georganiseerd door het Zeeuws Biologisch Museum en de Werk- groep Geologie van het Koninklijk Zeeuws Genootschap der Wetenschappen, zal te bezichtigen zijn tot

Zijn grote voorbeeld is Nietzsche, de `aristocratische' filosoof, die met zijn `ontwaarding van de waarden' het huidige `derde gezicht' mede heeft voortgebracht, maar die zich

Dat zijn eigen ontkenning van ,,de'' waar- heid eveneens een typisch postmodern trekje vertoont, speelt in de literatuur geen rol, want Peeters aarzelt niet de

Voor de VPRO-radio las hij zijn debuutroman De avonden voor en in dezelfde week verscheen Brieven aan mijn lijfarts, 1963-1980, een nieuw deel van het epistolaire feuilleton dat

Following an inductive process, 361 submitted questions were narrowed to 34 questions in seven themes: (1) effective conservation management; (2) detecting and understanding