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Eprints ID : 10005
To link to this article : doi:10.1016/j.electacta.2012.06.080
URL :
http://dx.doi.org/10.1016/j.electacta.2012.06.080
To cite this version : Belhadj Tahar, Noureddine and Savall, André
Effect of electropolymerisation conditions on the permeability of
polyphenol films deposited on a vitreous carbon electrode. (2012)
Electrochimica Acta, vol. 82 . pp. 427-433. ISSN 0013-4686
Any correspondance concerning this service should be sent to the repository
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Effect
of
electropolymerisation
conditions
on
the
permeability
of
polyphenol
films
deposited
on
a
vitreous
carbon
electrode
Noureddine
Belhadj
Tahar
a,
André
Savall
b,∗aInstitutSupérieurdesSciencesAppliquéesetTechnologiedeMahdia,UniversitédeMonastir,Tunisia
bLaboratoiredeGénieChimique,CNRS,UniversitéPaulSabatier,118,RoutedeNarbonne,31062Toulousecedex,France
Keywords: Rotating-diskelectrode Phenolelectropolymerisation Vitreouscarbon Permeability Wastewatertreatment
a
b
s
t
r
a
c
t
Polymericfilmswerepreparedfromalkaline(NaOH)phenolaqueoussolutionsonavitreouscarbon (VC)electrodebypotentiostaticorgalvanostaticelectro-oxidation.Permeationthroughsuchfilmswas studiedbyrotating-diskelectrodeusingtheferricyanideredoxcouple,andbycyclicvoltammetryusing phenateions.TheinfluenceoftheelectropolymerisationcontrollableparameterssuchasNaOHand phe-nolconcentrations,potentialorcurrentapplied,electrosynthesistime,temperatureandhydrodynamic conditions(electroderotation+solutionmagneticstirring)onthepermeabilityofthesepolymericfilms wasexamined.Conditionsfortheremovalofphenolbyelectropolymerisationarediscussedonthebasis ofthepermeabilityofpolyphenolfilmsobtainedbyelectrosynthesis.Permeablefilmswereformedfora concentrationoffreehydroxylanionlargerof0.1M.Anincreaseofthetemperatureto85◦Cfavoursthe
formationofhighlypermeablefilms,thusavoidingelectrodefouling.
1. Introduction
In recent years there hasbeenan increasing interest inthe
developmentofelectrochemicalpolymerisationfortheremoval
ofphenolsfromaqueoussolutions.Themainadvantagein
pro-ceedingbyelectropolymerisationisthelowconsumption ofthe
electricchargecomparedwithelectrochemicalmineralisation[1].
Inthisway,theremovalofphenolsfromaqueoussolutionsby
elec-trochemicalpolymerisationwasconductedongranularactivated
carbon[2],carbonfibre[3],Ta/b–PbO2[1,4]andpolyaniline/glassy
carbonelectrodes[5].Nevertheless,electropolymerisationof
phe-noliccompoundsleadstothedepositionofanon-conductivefilm
that blocksthe electrode activityand preventsfurtherremoval
of phenol [6–11]. Many works have shown that diffusion of
electroactivespeciesthroughpolymericfilmsdependsonthe
elec-tropolymerisationconditionssuchasthemonomerconcentration
[12],thenatureofthesolventused[13],thepHandbackground
electrolyte[14],thedegreeofcross-linkingofthepolymerchains
[15],thenatureoftheelectrode[16],theelectrodepositionmodes
(cyclicvoltammetryandpotentiostaticorgalvanostatic
electroly-sis)[12,17],theappliedpotential[14,18]orcurrent[19]andthe
electropolymerisationtime(filmthickness)[12].
Theaimofourpreviousworks[1,4,20,21]wastofindthe
operat-ingconditionsthatallowelectropolymerisationtoproceedaslong
∗ Correspondingauthor.Tel.:+33561556110;fax:+33561556139. E-mailaddresses:[email protected](N.BelhadjTahar),
[email protected](A.Savall).
asacurrentissuppliedtotheelectrode;thus,thepolymericfilm
inevitablydepositedontheelectrodesurfacemusthavethehighest
permeabilityforphenolmolecules.Themainoperatingconditions
weredescribedinRef.[1].Theelectrochemicalresponseof
phen-ateiononbare VCandpolyphenolfilm-coated VCwasstudied
in 1MNaOH aqueoussolutions [20]. Howeverusing suchhigh
concentrationofNaOHintheprecursorphenolsolutionpenalizes
anyeventualtreatmentbasedontheremovalofphenolsby
elec-tropolymerisation.Theaimofthisworkwastomeasurebyusing
arotating-diskelectrodethepermeabilityforferricyanideanionof
polyphenolfilmsdepositedinalkalinemediumonVCundervarious
electropolymerisationconditions.Inparticularwearelookingfor
theminimalconcentrationofNaOHwhichallowsthecontinuous
formingofafilmofsufficientpermeabilitynottoblockthe
elec-tropolymerisation.Therelativepermeabilityforphenateanionwas
alsoevaluatedbymonitoringchangesincyclicvoltammogramsof
phenolsolutionrecordedonpolyphenolfilm-coatedVCas
com-paredtobareVC.InordertooptimisetheconcentrationofNaOHin
theprecursorphenolsolutionparticularattentionwaspaidtoits
effectonthepermeabilityofthepolyphenolfilm.
2. Experimental
2.1. General
Cyclicand rotating-diskvoltammetryand
chronoamperome-trymeasurementswereperformedusingacomputercontrolled
Eco Chemie Autolab Model 30 (Utrecht, The Netherlands).The
conventionalthree-electrodecellsystemconsistedofbareVCor
polyphenolfilm-covered VC(disk of3mmdiameter,Metrohm)
working electrode, a platinum spiral counter electrode and an
Hg/Hg2Cl2/Cl− (saturated) reference electrode connected tothe
electrolytic solutionby a long Luggin capillary placed nearthe
workingelectrodeandfilledwith0.1MNa2SO4.Allthepotentials
arereportedversustheabovespecifiedreferenceelectrode.Before
eachexperiment,theworkingelectrodewaspolishedtoamirror
with1mmaluminaslurriesonpolishingsheet(3M262XIMPERIAL
LappingFilm)andsubsequentlywashedwithdistilledwater.
2.2. Preparationofpolyphenolfilm-coatedvitreouscarbon
electrode
Polyphenolfilmswerepreparedbyoxidative
electropolymeri-sationperformedeithergalvanostaticallyorpotentiostaticallyonto
thediskofVCelectrode surfacefromphenolaqueoussolutions
containing0.1MNa2SO4andNaOHatvariousconcentrations.
Elec-tropolymerisationwasperformedonafixedelectrodeandwithout
magneticstirringunlessotherwiseinstructed.Thepolyphenol
film-coatedelectrodeswerecopiouslyrinsedwithdistilledwaterand
usedimmediatelyinpermeationexperiments.
2.3. Polyphenolfilmpermeabilitymeasurement
ThepermeabilityPfilm
ferr.ofthepolyphenolfilmforferricyanide
anionwasmeasuredwitha rotating-diskelectrode(RDE)inpH
7phosphate(0.1M)buffersolutioncontaining0.01Mpotassium
ferricyanideat25◦C.ThelimitingcurrentI
Lofthe
electrochemi-calreductionofferricyanideaniononthepolyphenolfilm-covered
RDEcanbedescribedbythefollowingequation[22]:
I−1
L =(nFACsPferr.film) −1
+(0.62nFACsD2/3s −1/6)
−1
ω−1/2 (1)
whereAistheelectrodearea(cm2),C
sistheconcentrationof
fer-ricyanideanioninthesolution(molcm−3),D
sistheferricyanide
diffusioncoefficientinthesolution(cm2s−1),isthekinematic
viscosityofthesolution(cm2s−1),ωistheangularrotationrateof
theelectroderotation(rads−1)andn(=1)andFhavetheirusual
meanings.
Thepermeabilityofthepolyphenolfilmforferricyanideanion
Pferr.film wasobtainedfromtheinterceptsofIL−1 plotsversusω−1/2
atω−1/2=0.ThesolutionpermeabilityforferricyanidePsol.
ferr.was
obtainedfromtheslopesofplots Id versusω1/2 whereIdisthe
limitingcurrentatthebareVCelectrode asdescribed byLevich
[22]:
Id=0.62nFACsD2/3s −1/6ω1/2=nFACsPferr.sol. (2)
Therelativepermeability ofthepolyphenolfilmforphenate
anionPfilm
Ph. wasassessedbysubjectingthepolyphenolfilm-coated
electrodetocyclinginthesamesolutionusedforthefilm
prepa-ration.TherelativepermeabilityforphenateanionPfilm
Ph. ,expressed
asapercentage,isdefinedastheratiooftheoxidationpeak
cur-rentintensityduringthe1stscanatthepolyphenolfilm-coated
electrodeIfilmoverthatatthebareelectrodeIbare[23,24]:
PPh.film=
Ifilm
Ibare
×100 (3)
Inpractice,thepermeabilityofthefilmofpolyphenolfor
fer-ricyanideanionswascalculatedfromvoltammogramsrecordedat
25◦Conbareglassycarbondisk(freshlypolished)andonthisdisk
coveredwiththefilmevenwhenthefilmwaspreparedat85◦C.
However,thepermeabilityofthefilmofpolyphenolforphenate
anionswascalculatedfromvoltammogramsrecordedonbareVC
andonpolyphenolfilm-coatedVCinthesamesolutionandatthe
sametemperatureusedforthepreparationofthefilm.
-800 -600 -400 -200 0 200 400 200 0 -200 -400 -600 -800 E vs. SCE / mV I / µ A (1) (2)
Fig.1. VoltammogramsonaVCrotateddiskof0.01Mpotassiumferricyanidein pH7sodiumphosphate(0.1M)buffersolutionat25◦
C.Scanrate:10mVs−1and ω=5000rpm.(1)BareVC;(2)polyphenolfilmelectrosynthesizedonVC rotating-diskelectrode(ω=1000rpm)byanodicpolarisationat1800mVduring60minin amagneticallystirred0.01Mphenolsolutioncontaining0.1MNaOHand0.1M Na2SO4at85◦C.
3. Resultsanddiscussion
3.1. Generalbehaviourofthebarevitreouscarbonandthe
polyphenolfilm
Fig. 1 shows typical rotating-disk voltammograms for the
reductionof0.01Mpotassium ferricyanidesolutionatbareand
polyphenol film-coated VC electrodes. The film did not affect
thestartingferricyanidereductionpotentialbutthecurrentwas
stronglyattenuated.
3.2. Polyphenolfilmspreparedbypotentiostaticoxidation
Polyphenolfilmswerepreparedbypotentiostaticoxidationin
ordertohighlighttheinfluenceontheirpermeabilityofoxygen
evolutionwhenitoccurssimultaneouslywith
electropolymerisa-tion.
3.2.1. Influenceoftemperature
ValuesoffilmpermeabilityweredeterminedbyplottingIL−1vs.
ω−0.5andextrapolatingtoveryhighrotationrateatω−0.5=0,where
masstransportistotallyfilmlimited.Fig.2representsplotsofIL−1vs.
ω−0.5forbareandpolymermodifiedVCelectrodes.Table1shows
30000 32000 34000 36000 VC/polyphenol (30 mM) VC/polyphenol (50 mM) (3) (4) 0 1000 2000 3000 4000 ϖ− 1/2 / (rad s-1)-1/2 ϖ− 1/2 / (rad s-1 )-1/2
(I
li m .)
-1/ A
-1(I
li m .)
-1/ A
-1 VC/polyphenol (10 mM) bare VC (2) (1) 0.00 0.02 0.04 0.06 0.08 0.10 0.00 0.02 0.04 0.06 0.08 0.10Fig.2.ReciprocalLevichplotsoflimitingreductioncurrentsforpermeationof ferri-cyanideanionthroughfilmsofpolyphenolonaVCrotateddisk.Scanrate:10mVs−1. Polyphenolfilmswerepreparedat85◦
Conarotating-diskelectrode(ω=1000rpm) byanodicpolarisationat1800mVduring30mininamagneticallystirred0.1M NaOHand0.1MNa2SO4aqueoussolutionwithphenolconcentrations:0Mcurve (1)(bareVC);0.01Mcurve(2);0.03Mcurve(3)and0.05Mcurve(4).
Table1
Relationshipsbetweentemperatureandthepermeabilityforferricyanideanion ofthepolyphenolfilmPfilm
ferr.electrosynthesizedonvitreouscarbonelectrode dur-ing30minatvariousappliedpotentialsEfrom0.01Mphenolaqueoussolution containing1MNaOHand0.1MNa2SO4.
T/◦C 25 85 Evs.SCE/mV 500 900 1200 500 600 700 Pfilm ferr.×10 4 /cms−1 0 5 221 0 1961 3349
therelationshipsbetweenthetemperatureandthepermeability
ofthepolyphenolfilmselectrosynthesizedonVCduring30min
atvariousappliedpotentialsfrom0.01Mphenolaqueoussolution
containing1MNaOHand0.1MNa2SO4.Polyphenolfilmsprepared
atpotentialslessthan500mVwerenotatallpermeableatboth25
and85◦C.Above500mV,thepermeabilityincreasedsubstantially
at85◦Cwhilepolyphenolfilmsremainedalmostimpermeableuntil
900mVat25◦C.
The raising of permeability with temperature and applied
potential(Table1)mayresultfromanincrease inthe
polyphe-nolfilmgrowthrate;thediameteranddensityoftheporesinthe
filmareexpectedtostronglyincreasewiththefilmgrowthrate.On
thecontrary,afilmgrownslowlyismorecompactanddensewith
lessandnarrowerpores[15].Insummary,thelargerpermeability
valueswereobtainedathightemperature,whichallowstheuseof
lowerpotentials.
3.2.2. InfluenceofNaOHconcentration
Fig.3showscyclicvoltammogramsrecordedonbareVC
elec-trodeat85◦Cin0.01Mphenolaqueoussolutioncontaining0.1M
Na2SO4andNaOHatdifferentconcentrations.Decreasingthe
con-centrationofNaOHfrom1to0.01Mhadnoeffectonthepeak
potentialbut noticeablydiminishedthe peakcurrent ofphenol
oxidationindicatingthattheelectrodepassivationwasmoreand
morepronounced.Notethatfor0.01MNaOHtheresponseof
phe-nol(practicallypresentasphenate)isexpressedasawave(curve
3).
Table2showstherelationshipsbetweenthepermeabilityfor
ferricyanide anion and theconcentration of NaOHused during
thepolyphenolfilmpreparationatvariousappliedpotentials.For
NaOHconcentrationof1M,polyphenolfilmspreparedatpotentials
below500mVarenotatallpermeablewhiletheonesprepared
atpotentialhigherthan600mVwerehighlypermeable.Inthese
conditions,comparisonbetweenvaluesofPfilm
ferr.(Table2)andP
sol. ferr.
(Fig.4)showsthatphenoloxidationratewaslimitedbythelow
membranepermeabilityofpolyphenolfilmspreparedatpotentials
lowerthan500mV.Onthecontrary,theoxidationratewaslimited
bythesolutionforfilmspreparedatpotentialshigherthan600mV.
Table2showsthatpolyphenolfilmswithhighpermeabilityto
fer-ricyanideanionwerepreparedatincreasingpotentialsastheNaOH
concentrationdecreasedfrom1to0.01M.Ontheotherhand,very
lowpermeabilityvalueswereobservedevenathighapplied
poten-tialsforNaOHconcentrationslessthan0.1M.Theseresultsarein
0 50 100 150 200 250 900 700 500 300 100 -100 -300 E vs. SCE / mV I / µ A (1) (2) (3)
Fig.3.Effectofsodiumhydroxideconcentrationoncyclicvoltammograms(1st cycles).recordedonbareVCelectrodein0.01Mphenolaqueoussolution contain-ing0.1MNa2SO4andNaOHataconcentrationof1M(curve1),0.1M(curve2)and 0.01M(curve3).Scanrate:100mVs−1andT=85◦
C.
Fig.4. Variationofthesolutionpermeabilityforferricyanideanionasafunctionof theelectroderotationrate.
agreementwithcyclicvoltammogramspresentedinFig.3ifwe
considerthatthepeakcurrentofphenoloxidationdecreasedas
thepermeabilityofthepolyphenolfilmdiminished.
CyclicvoltammogramspresentedinFig.5showthatnophenol
oxidationpeakwasobservedforNaOHconcentrationslessthan
0.1M(curves1and2)indicatingthatundertheseconditionsthe
polyphenolfilmswereimpermeabletophenateanion.Therelative
permeabilityPfilm
Ph. forphenateanionofthepolymerfilmprepared
in0.1MNaOHwasevaluated,accordingtoEq.(3),fromcurve2
inFig.3and curve3inFig.5.Pfilm
Ph. isequal to184%;this value,
higherthan100%,suggeststhatthefilmpermeabilityfor
phen-ateanionisgovernedbythepreferentialpartitioningoftheprobe
intothepolyphenolfilmduetostrongerinteractions(electrostatic,
hydrophobic,etc.)inthefilmthaninthesolution[24].
Phenolisaweakacid(pKa=9.9)andataninitialconcentration
of0.01MitsreactionwithNaOHinitiallyat1M,0.1M,0.05Mor
0.01MleadstoequilibriumconcentrationsoffreeOH−respectively
equalto0.99M,0.09M,0.04Mand0.00M.Consequently,at
rel-ativelyhighNaOHinitialconcentration(1Mand0.1M)thereis
enoughfreeOH−toinstantaneouslyneutralizetheacidityarising
attheelectrodesurfacefromwaterdischargeoccurringin
paral-lelwithpolyphenolelectrosynthesis.Ontheotherhand,withlow
NaOHconcentrations(0.05and0.01M)thefreeOH−
concentra-tionistooweaktoneutralizethetotalityofprotonsproducedat
thesurfaceoftheanodewhentheappliedpotentialincreases.
Fur-thermore,thelowvaluesofpermeabilityobservedwiththelower
NaOHconcentrations(0.05and0.01M),evenforexperiments
per-formedundermagneticstirringand withtherotatingelectrode
(ω=1000rpm),indicatethathighacidityremainedattheelectrode
surface(Table2).
From Table2,one can concludethat at 0.01Mphenol
con-centrationandrelativelyhighNaOHconcentration(0.1and1M),
thepermeability for ferricyanideanion increases as the
poten-tialappliedincreases.However,atlowNaOHconcentration(0.01
and 0.05M), the permeability remains almost nil even at very
highapplied potential. Therefore, we think that the key factor
influencingthepermeabilityofthepolyphenolfilmsisthe
concen-trationoffree OH−in thesolution:[OH−]
sol.=[NaOH]−[PhOH];
0 500 1000 1500 900 700 500 300 100 -100 E vs. SCE / mV I / µ A 0.01 M 0.05 M 0.1 M (3) (1) (2)
Fig.5.Measurementsofpolyphenolfilmpermeabilityforphenateion.Scanrate: 100mVs−1.Thepolyphenolfilmswerepreparedbyanodicpolarisationat1800mV for30minat85◦
Cin0.01Mphenolaqueoussolutionscontaining0.1MNa2SO4and NaOHat0.01M(curve1),0.05M(curve2)and0.1M(curve3).
Table2
RelationshipsbetweentheNaOHconcentrationin0.01Mphenolaqueoussolutioncontaining0.1MNa2SO4at85◦CandthepermeabilityforferricyanideanionPfilm ferr.ofthe polyphenolfilmelectrosynthesizedduring30minonavitreouscarbonelectrodeatdifferentappliedpotentials.
Hydrodynamicconditions Fixedelectrodeandwithoutmagneticstirring Electroderotationrateof1000rpm andundermagneticstirring
[NaOH]/M 1 0.1 0.05 0.01 Evs.SCE/mV 400 500 600 700 700 1300 1500 1800 1800 2500 1800 2500 Pfilm ferr.×10 4/cms−1 0 0 1961 3349 0 0 9 925 5 5 3 3 0 50 100 150 200 900 700 500 300 100 -100 -300 E vs. SCE / mV
I /
µ
A
(2)(A)
(1) 0 1 2 3 900 700 500 300 100 -100 -300 E vs. SCE / mVI / mA
(2)(B)
(1)Fig.6. Cyclicvoltammograms(firstcycles)of0.05Mphenolsolutioncontaining0.1MNa2SO4andNaOHat0.1M(curve1)and0.15M(curve2)at85◦
Con(A)bareVC(B) VCelectrodescoveredbypolyphenolfilms.Scanrate:100mVs−1.Polyphenolfilmswereelectrosynthesizedat85◦
Conarotateddisk(1000rpm)VCelectrodeatanapplied potentialof1800mVinamagneticallystirred0.05Mphenolsolutioncontaining0.1MNa2SO4andNaOHat0.1M(curve1)and0.15M(curve2).
the present results show that the concentration of free OH−
should be preferably higher than 0.1M to prepare
polyphe-nol films with noteworthy permeability values to ferricyanide
anion.Indeed,polyphenolfilmpreparedbyanodicpolarisationat
1800mV for30minin 0.05Mphenolsolution containing0.1M
NaOH([OH−]
sol.=0.05M)and0.1MNa2SO4 at85◦C wasnot at
allpermeableforferricyanideanionwhereastheonepreparedin
thesameconditionsexceptthatNaOHconcentrationwas0.15M
([OH−]
sol.=0.1M)hadapermeabilityequalto149×10−4cms−1.
Fig.6(AandB)showscyclicvoltammograms(firstcycles)recorded
at85◦Crespectivelyonbareandpolyphenolfilm-coatedVC
elec-trodesin0.05Mphenolsolutioncontaining0.1MNa2SO4and0.1M
NaOH(curve 1)or0.15MNaOH(curve 2).Curve 1in Fig.6(B)
exhibitsa weakly defined peak for phenoloxidation indicating
averylowpermeabilityofthecorrespondingpolyphenolfilmto
phenateanion.Alarge,butbetterdefinedpeakwasobservedfor
0.15MNaOH(curve2inFig.6(B))indicatingthatunderthese
condi-tionstheoxidationprocessoccurredwithoutinhibitionandthatthe
polyphenolfilmwashighlypermeabletophenateanion.Itshould
beemphasizedthatthephenoloxidationpeakonpolyphenol
film-coated electrodes (Fig. 6(B)) is moved toward higher potential
valuesascomparedtothatonbareVCelectrode(Fig.6(A)).
Theseresultshaveshownthattheremovalofphenolby
elec-tropolymerisationispossiblebyapplyingahigherpotentialasthe
NaOHconcentrationdecreases.
3.2.3. Influenceofphenolconcentration
The effect of phenol concentration on the permeability of
polyphenol films prepared at 85◦C on a VC rotating disk
(ω=1000rpm) was studied by potentiostatic polarisation at
1800mV during 30min in magnetically stirred 0.01, 0.03 and
0.05Mphenolaqueoussolutionscontaining0.1MNaOHand0.1M
Na2SO4. Potentiostatic I–t curves (not shown) reveals that the
limiting current at the stationary state fell dramatically when
phenolconcentrationincreasedfrom0.01to0.03M.Cyclic
voltam-mograms (not shown) recorded on polyphenol film-coated VC
electrodesinthesamesolutionsshowthat nophenoloxidation
peakwasobservedfor0.03Mand0.05Mphenolconcentrations;
theelectrochemicalresponseofphenolisexpressedasawavewhat
preventstocalculatetherelativepermeabilityforphenateanion
(almostimpermeable);for0.01Mphenolconcentration,the
rela-tivepermeabilityisequalto143%.Theseresultsaswellasthose
presentedinSection3.2.2forfilmsrespectivelypreparedinNaOH
0.1Mand0.15Mmaybeexplainedintermofadecreaseinthe
concentrationoffreeOH− astheconcentrationofphenolinthe
solutionrises.Inparticular,thedecreaseoftheabilityofthe
solu-tiontoopposechanges inpHwhen protonsare formedonthe
electrodesurfaceduringwaterdischargecanexplaintheoriginof
thepermeabilityfall[21](seeSection3.3.1). 3.2.4. Influenceofelectrolysistime
Polyphenolfilmsweresynthesizedonarotating(ω=1000rpm)
VCelectrodebyanodicpolarisationat1800mVforvarious
elec-tropolymerisationtimes (30–120min) in a magneticallystirred
0.01Mphenolsolutioncontaining0.1MNaOHand0.1MNa2SO4
at85◦C.ResultspresentedinTable3revealthatthepermeability
decreased substantially with increasing the
electropolymerisa-tion time; similar results were obtained by Wang et al. [12].
Thisbehaviourisinterpretedintermofanincreasein
polyphe-nolfilmthicknesswithincreasingelectropolymerisationtime;the
polyphenolfilmthicknessvariesbetween10and100nm
depend-ingontheelectropolymerisationconditions[25].Fig.7(A)shows
thatcyclicvoltammogramsoftheferricyanideanionare
charac-terizedbyirreversiblewavesfor60and120minelectrosynthesis
timeswhilemuchmorereversiblepeakswereobservedforonly
30min.Valuesoftherelativepermeabilityforphenateanion,
cal-culatedfromcurves(2)and (3)inFig.7(B),wereequalto155%
and 142% respectively for 60 and 120min indicating that the
polyphenolfilm permeability for phenateanion isindependent
of electrosynthesis times.Electropolymerisation can thus occur
onpre-existingpolymerlayerobtainedbyelectrolysisofphenol
0.01Minalkaline(0.1MNaOH)solution.Thistechniquecouldbe
usedasawaytoremovephenolsinceundertheseconditions
elec-tropolymerisationproceedsaslongasacurrentisappliedtothe
electrode.
Table3
Relationshipsbetween theelectropolymerisation time in magnetically stirred 0.01Mphenolaqueoussolutioncontaining0.1MNaOHand0.1MNa2SO4at85◦
C andthepermeabilityPfilm
ferr.oftheresultingpolyphenolfilmforferricyanideanion. Electrosynthesistime/min 30 60 120 Pfilm
ferr.×10
Fig.7.Measurementsofpolyphenolfilmpermeabilityfor(A)ferricyanideand(B)phenateions.Scanrate:(A)500mVs−1and(B)100mVs−1.Thepolyphenolfilmswere preparedbyanodicpolarisationonarotating(ω=1000rpm)VCelectrodeat1800mVforvariouselectrolysistimesin0.01Mphenolaqueoussolutioncontaining0.1MNaOH and0.1MNa2SO4at85◦
C.Electrolysistime:30min(curve1);60min(curve2)and120min(curve3).
3.3. Polyphenolfilmspreparedbygalvanostaticoxidation
In practice, a treatment of phenolic compounds based on
electropolymerisationshouldbeconductedgalvanostatically;as
a consequence an increase of the potential is expected during
theelectropolymerisation.Therefore,theappliedcurrentmustbe
determinedbytakingintoaccountthetransportpropertiesofthe
polymericfilm.
3.3.1. Influenceofappliedcurrent
Fig. 8(A) exhibits galvanostatic E–t curves recorded during
polyphenolfilmselectrosynthesisonarotating(ω=1000rpm)VC
electrode at various applied currents in a magnetically stirred
0.05Mphenolaqueoussolutioncontaining0.15MNaOHand0.1M
Na2SO4at85◦C;differentelectrosynthesistimeswerechosenin
suchawaythatthesameelectriccharge(Q=3600mC)waspassed
inordertopreparepolyphenolfilmshavingmoreorlessthesame
thickness.GalvanostaticE–t curves presentedin Fig.8(A)show
thattheelectrodepotentialremainedconstantataround1300mV
duringthefirststageofthepolyphenolfilmelectrosynthesis.The
lengthofthisstepdecreasedwhenappliedcurrentincreased;then
the potentialrose rapidly until it reacheda plateau at around
2000mV.Table4showsthatthepermeabilityofthefilmfor
fer-ricyanideaniondropsfrom107×10−4cms−1 to2×10−4cms−1
byincreasingfrom1to3mAthecurrentappliedduringthefilm
electrosynthesis.Thiscurrentdependencyofthepermeabilityis
in agreementwithcyclic voltammogramsof ferricyanide anion
recorded on polyphenol film-coated VC electrodes depicted in
Fig.8(B)inthatthereductionpeakcurrentdecreasedasthe
cur-rentappliedincreasedintherange1–3mA.Fig.8(CandD)shows
cyclicvoltammogramsof0.05Mphenolaqueoussolution
contain-ing0.15MNaOHand0.1MNa2SO4recordedat85◦Conpolyphenol
film-coatedVCelectrodes.CyclicvoltammogramsinFig.8(D)show
thatthephenoloxidationpeakrecordedonpolyphenolfilm-coated
electrodesislargertothatonbareelectrodeanddisplacedtomore
positivepotentials(curve2inFig.6(A)).
Table4 shows that when the appliedcurrent increases one
observesadecreaseofthepermeabilityofthefilmtowardthe
ferri-cyanideanionwhiletherelativepermeabilityofthesamefilmwith
regardtothephenolincreases.Thecurrentintensityeffectonthe
polyphenolfilmpermeabilitycanbeexplainedbythedischargeof
Table4
Relationshipsbetweenthe current Iapplied during theelectrosynthesis of a polyphenolfilmdepositedonarotating(ω=1000rpm)vitreouscarbonelectrode inamagneticallystirred0.05Mphenolaqueoussolutioncontaining0.15MNaOH and0.1MNa2SO4at85◦
CandthepermeabilityPfilm
ferr.forferricyanideanionandP film ph. forphenol. I/mA 1 1.5 2 3 Electrosynthesistime/min 60 40 30 20 Pfilm ferr.×10 4/cms−1 107 45 29 2 Pfilm ph. (%) 176 233 399 1115
waterwhichissourceofprotons.ThecurrentIappliedduringfilms
electrosynthesiscanbeexpressedasfollows:
I=IPh.+IH
2O (4)
whereIPh.andIH2Oarethepartialcurrentsforrespectivelyphenol
andwaterelectro-oxidation.IPh.canbeevaluatedbythefollowing
equation: IPh.=nFAkPh[Ph]sol. considering thatthe concentration
ofphenolattheelectrodesurfacewasequaltozerobecausethe
appliedcurrent Iwasmuchhigher thanthelimiting currentof
phenoloxidation.Indeed,fortheexampleofFig.8,thelimiting
cur-rentofphenoloxidation(duringelectrosynthesisofthefilms)was
equaltoaround0.35mAforn=1,A=0.0707cm2,k
Ph.=10−5ms−1
and[Ph.]sol.=0.05M.Thus,asIincreased(from1to3mA),the
par-tialcurrentofwaterdischargeIH2Orose,producinganincreasein
oxygenevolutionandtheoutputofprotons.Theconcentrationof
protons[H+]
ele.attheelectrodesurfacecanbecorrelatedtoIH2O
by:IH2O=nFAkH+[H
−
]ele.consideringthatthebulkconcentration
ofprotons[H+
]sol.wasequaltozeroduetohydrodynamic
condi-tions(electroderotation,ω=1000rpmplusmagneticstirring)and
therelativelyhighconcentrationoffreehydroxideioninthe
solu-tion([OH−
]sol.=0.1M).Thus, concentrations [H+]ele.,calculated
forn=1 andkH+=10−5ms−1,wereequal toaround0.1Mand
0.4MrespectivelyforIequalto1or3mA.Theseresultsshowthat
forI=3mA,theconcentrationofprotonsattheelectrodesurface
([H+
]ele.=0.4M)wasfourtimeshigherthanthatoffreehydroxide
ionin thesolution([OH−H+]sol.=0.1M).Asa result,the
elec-trode/solutioninterfaceremainedacidthoughelectrosynthesisof
the polyphenolfilm was performed withan electrode rotation
rateof1000rpmandundermagneticstirring.Ifweassumethat
polyphenolfilmspreparedherehadthesamethickness,thedrop
ofpermeabilityforferricyanideanion(Table4)canbeexplainedby
astrongeracidityattheelectrodesurfaceduringpolyphenolfilm
electrosynthesisasIincreased.
Thecontradictorybetweentheincreaseintheapparent
per-meability forphenol(%) Pfilm
Ph. andthedramatic decreaseof the
permeabilityforferricyanideanionPfilm
ferr.whentheappliedcurrent
increases(Table4)canbeinterpretedintermofachangeinthe
microstructureofthepolyphenolfilm.Wethinkthat increasing
theappliedcurrentandthereforetheconcomitantoxygen
evolu-tionincreasesthedensityofsmallpores(permeableforphenate
andnotforferricyanideanion)tothedetrimentofthatoflargeones
(permeableforbothphenateandferricyanideanions).Accordingto
Rothwelletal.’ssuggestion[18]weintendtostudythesefilmsby
scanningelectronmicroscopytounderstandtheseeffects.
Fortheremovalofphenolbyelectropolymerisationthe
oper-atingconditionsshouldfavourahighpermeabilityofthefilmfor
phenateanion.ComparisonbetweenvaluesofPferr.film(Table4)and Psol.
ferr.(P
sol.
ferr.=45×10
−4cms−1forω=1000rpm;Fig.4)showsthat
therateofferricyanidereductionwaslimitedbythemembrane
permeabilityforpolyphenolfilmspreparedatcurrentshigherthan
2mA whereas it wasunder solution transport control for
-200 -150 -100 -50 0 800 600 400 200 0 -200 -400 -600 E vs. SCE / mV 1 mA 3 mA 2 mA 1.5 mA (1) (4) (3) (2) (1) (2) (3) (4)
(B)
0 100 200 300 400 900 700 500 300 100 -100 -300 E vs. SCE / mV (1) (2)(C)
bare vitreous carbon
0 500 1000 1500 2000 900 700 500 300 100 -100 -300 E vs. SCE / mV I / μ A I / μ A I / μ A (4) (3)
(D)
0 500 1000 1500 2000 2500 70 60 50 40 30 20 10 0 Time / min E vs. SCE / mV I = 1 mA I = 1.5 mA I = 2 mA I = 3 mA(A)
(4) (3) (2) (1)Fig.8.(A)GalvanostaticE–tcurvesrecordedduringpolyphenolfilmselectrosynthesisonarotating(ω=1000rpm)VCelectrodeatvariousappliedcurrentsinamagnetically stirred0.05Mphenolaqueoussolutioncontaining0.15MNaOHand0.1MNa2SO4at85◦
C.Appliedcurrent:(1)1mAfor60min,(2)1.5mAfor40min,(3)2mAfor30minand (4)3mAfor20min.(B–D)Measurementsofpolyphenolfilmpermeabilityfor(B)ferricyanideand(CandD)phenateions.Scanrate:(B)500mVs−1and(CandD)100mVs−1.
performedatanappliedcurrentslightlyhigherthanthelimiting
currentofphenoloxidationshouldallowtheremovalofphenol.
3.3.2. Influenceofelectroderotationandmagneticstirring
GalvanostaticE–tcurveswererecordedat85◦ConaVC
elec-trodeat an applied current of 2mA in 0.05Mphenol aqueous
solutioncontaining0.15MNaOHand0.1MNa2SO4;curveswere
registeredeitherinaquiescentsolutionorforanelectrode
rota-tion rate of 1000rpm and a magnetic stirring. The E–t curves
havethesameshapeexceptthatthepotentialplateauat2000mV
wasreachedrightfromthebeginninginthecaseofpolyphenol
filmelectrosynthesizedinaquietsolution.Thepermeability for
ferricyanideanion dropped from29×10−4cms−1 (Table 4) for
polyphenolfilm electrosynthesizedon a rotatingelectrode and
undermagneticstirringtozerointhecaseofafixedelectrodeand
unstirredphenolsolution.AsinSection3.2.1,theseresultsmay
beinterpretedassuminganaccumulationofhighconcentrationof
protonsH+attheelectrodesurfacewhichblocksthepermeability
ofthepolyphenolfilmelectrosynthesizedonafixedelectrodein
unstirredsolution[21].
4. Conclusions
Thisworkdemonstrates thatthepermeability ofpolyphenol
filmsdepositedbyelectrochemicalpolymerisationonavitreous
carbon electrode depends strongly on the composition of the
startingphenol solution,temperature,appliedpotential or
cur-rent,electrosynthesistimeandhydrodynamicconditions.Wehave
shownthattheconcentrationoffreeOH−inthestartingphenol
solution([OH−]
sol.=[NaOH]−[PhOH])mustbehigherthanaround
0.1Mtopreparepolyphenolfilmspermeabletobothferricyanide
andphenateanions;thiswasverifiedbyvaryingNaOH
concen-trationforthesameconcentrationofphenolandviceversa;the
relativelyhighfreeOH−concentrationwasnecessaryto
instanta-neouslyneutralizetheacidity,attheelectrodesurface,arisingfrom
theconcomitantoxygenevolutionoccurringduringthepolyphenol
filmelectrosynthesis.Electrochemicalpolymerisationconductedat
hightemperature(85◦C)yieldshighpermeablepolyphenolfilms
atlowappliedpotentials.Nevertheless,polyphenolfilmsthathave
suitablepermeability weresynthesized atlow temperature but
athighappliedpotential.Fortheremovalofphenolfrom
waste-water by electropolymerisation,it would be bettertouse high
temperatureandlowpotentialinordertominimizetheparasitic
reactionofoxygenevolutionwhichaffectsthecurrentyield.We
havealsoshownthatpolyphenolfilmspreparedat1800mVfrom
0.01Mphenoland0.1MNaOHhavelowpermeability,especially
whenelectrolysistimeincreases;thiswasinterpretedintermof
anincreaseinthepolyphenolfilmthickness.Theapparent
perme-abilityofpolyphenolfilmspreparedgalvanostaticallyfrom0.05M
phenoland0.15MNaOHat85◦Cincreasedforphenateanionas
theappliedcurrentincreased.Theseresultscouldbeinterpreted
interms of(1)theincreasein thelocalacidityattheelectrode
surfaceand(2)anincreaseinthedensityofsmallpores
(perme-ableforphenateandnotforferricyanideanion)tothedetrimentof
largepores(permeableforbothphenateandferricyanideanions)
withincreasingtheconcomitantoxygenevolution.Itwasshown
thatpolyphenolfilmspreparedonarotatingelectrodeandastirred
solutionweremorepermeablethanthosesynthesizedonafixed
electrodeandanunstirredsolution.
References
[1]N.BelhadjTahar,A.Savall,ElectrochimicaActa54(2009)4809.
[2]M.Gattrell,B.MacDougall,JournaloftheElectrochemicalSociety146(1999) 3335.
[3]H.Kuramitz,M.Matsushita,S.Tanaka,WaterResearch38(2004)2331. [4]N.BelhadjTahar,R.Abdelhedi,A.Savall,JournalofAppliedElectrochemistry
39(2009)663.
[5]Y.Zhang,Q.Li,H.Cui,J.Zhai,ElectrochimicaActa55(2010)7219. [6]X-Y.Li,Y-H.Cui,Y-J.Feng,Z-M.Xie,J-D.Gu,WaterResearch39(2005)1972. [7]J.Wang,M.Jiang,F.Lu,JournalofElectroanalyticalChemistry444(1998)127. [8]P.I.Iotov,S.V.Kalcheva,JournalofElectroanalyticalChemistry442(1998)19. [9]J-L.Boudenne,O.Cerclier,P.Bianco,JournaloftheElectrochemicalSociety145
(1998)2763.
[10]G.Mengoli,M.M.Musiani,ElectrochimicaActa31(1986)201.
[11]Ch.Comninellis,C.Pulgarin,JournalofAppliedElectrochemistry21(1991)703. [12] J.Wang,S-P.Chen,M.S.Lin,JournalofElectroanalyticalChemistry273(1989)
231.
[13]R.L.McCarley,JournalofElectrochemicalSociety137(1990)218C. [14]I.Losito,F.Palmisano,P.G.Zambonin,AnalyticalChemistry75(2003)4988. [15]R.L.McCarley,E.A.Irene,R.W.Murray,JournalofPhysicalChemistry95(1991)
2492.
[16]A.Witkowski,M.S.Freund,A.Brajter-Toth,AnalyticalChemistry63(1991)622. [17] M.D.Imisides,R.John,P.J.Riley,G.G.Wallace,Electroanalysis3(1991)879. [18] S.A.Rothwell,C.P.McMahon,R.D.O’Neeill,ElectrochimicaActa55(2010)1051.
[19]P.Gros,T.Gibson,A.Bergel,M.Comtat,JournalofElectroanalyticalChemistry 437(1997)125.
[20]N.BelhadjTahar,A.Savall,ElectrochimicaActa55(2009)465.
[21]N.BelhadjTahar,A.Savall,JournalofAppliedElectrochemistry41(2011) 983.
[22]V.G.Levich,PhysicochemicalHydrodynamics,Prentice-Hall,EnglewoodCliffs, NJ,1962.
[23]J.Cruz,M.Kawasaki,W.Gorski,AnalyticalChemistry72(2000)680. [24] C.A.Martinez-Huitle,C.CarlesiJara,M.Cerro-Lopez,M.A.Quiroz,Canadian
JournalofAnalyticalSciencesandSpectroscopy54(2009)53.
[25]R.Lapuente,F.Cases,P.Garcés,E.Morallon,J.L.Vasquez,Journalof Electroan-alyticalChemistry451(1998)163.