Availableonlineat
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www.sciencedirect.com
www.e-ache.com HormigónyAcero2018;69(S1):43–51 www.elsevierciencia.com/hya
Application
of
combined
electrochemical
treatments
to
reinforced
concrete:
Electrochemical
chloride
extraction
plus
cathodic
protection
Aplicación
de
tratamientos
electroquímicos
combinados
al
hormigón
armado:
extracción
electroquímica
de
cloruros
más
protección
catódica
Miguel
Ángel
Climent
a,∗,
Jesús
Carmona
b,
Pedro
Garcés
aaDr.enCienciasQuímicas,Catedrático,DepartamentodeIngenieríaCivil,UniversidaddeAlicante,Alicante,Spain bDr.IngenierodeCaminos,ProfesorAyudanteDoctor,DepartamentodeIngenieríaCivil,UniversidaddeAlicante,Alicante,Spain
Received11December2017;accepted17May2018 Availableonline14July2018
Abstract
Ithasbeenstudiedthepossibilityofusingagraphite–cementpasteanodeforcombinedtreatmentsofelectrochemicalchlorideextractionplus
cathodicprotectiononreinforced concreteelements.These treatmentswouldbeinterestingincases ofstructuresheavilycontaminated with
chloridesandcontinuouslyexposedtoaharshchlorideenvironment.Ithasbeenshownthat,intheexperimentalconditionsofthiswork,theanode
isnotdamagedduringtheelectrochemicalchlorideextractionstep.Theapplicationofapreviouschlorideextractionstepallowsworkingwitha
lowercurrentdensityatthecathodicprotectionstep,whichreducestheriskofdamagesoftheanodicsystem.Achloridebarriereffectparameter
hasbeendefined,basedonthereductionofthechlorideuptakebyconcrete,duetocathodicprotectionaction,referredtothechlorideuptakeof
thereference(nottreated)specimens.Thevaluesofthechloridebarriereffectparameterfoundinthisworkareabout20%.
©2018Asociaci´onEspa˜noladeIngenier´ıaEstructural(ACHE).PublishedbyElsevierEspa˜na,S.L.U.Allrightsreserved.
Keywords:Steelreinforcedconcrete;Corrosion;Electrochemicalchlorideextraction;Cathodicprotection;Cathodicprevention
Resumen
Sehaestudiadolaposibilidaddeutilizarunánododepastadegrafito-cementoparatratamientoscombinadosdeextracciónelectroquímicade
clorurosyproteccióncatódicadeelementosdehormigónarmado.Dichostratamientosseríaninteresantesencasosdeestructurascontaminadas
conclorurosypermanentementeexpuestasaunambientesalinoagresivo.Sehademostradoque,enlascondicionesdeestetrabajo,elánodono
resultada˜nadodurantelaetapadeextraccióndecloruros.Laaplicacióndeunaetapapreviadeextraccióndeclorurospermiteaplicarlaprotección
catódicaconunadensidaddecorrientemenor,hechoquereduceelriesgodeda˜nosdelsistemaanódico.Sehadefinidounparámetrodeefecto
barreradecloruros,basadoenlareduccióndelapenetracióndecloruros,debidaalaproteccióncatódica,referidaalapenetracióndeclorurosde
referencia(sinproteccióncatódica).Losvaloresdedichoparámetroencontradosenestetrabajosondel20%,aproximadamente.
©2018Asociaci´onEspa˜noladeIngenier´ıaEstructural(ACHE).PublicadoporElsevierEspa˜na,S.L.U.Todoslosderechosreservados.
Palabrasclave: Hormigónarmado;Corrosión;Extracciónelectroquímicadecloruros;Proteccióncatódica;Prevencióncatódica
1. Introduction
Severalelectrochemicaltechniques havebeensuccessfully usedtotheprotectionandremediationofsteelcorrosionin
rein-∗Correspondingauthor.
E-mailaddress:ma.climent@ua.es(M.Á.Climent).
forced concretestructures. Allthese techniquesare based on theloweringoftheelectricpotentialofsteel[1–7].Thiseffect canbe obtained bothbyconnectiontoaless noble metal,as incathodicprotection(CP)bysacrificialanodes,orby connec-tiontothenegativepoleofanelectricdirectcurrentsource,as inCPbyimpressedcurrent[8–12].Thetechniquescanalsobe classifiedinpermanentandtemporary techniques.Permanent
https://doi.org/10.1016/j.hya.2018.05.003
techniquesareCP,whoseaimistostopthesteelreinforcement corrosion,anditsvariantcalledcathodicprevention(CPre), fol-lowingPedeferrietal.[9,11].TheobjectiveofCPreistoprevent theinitiationofsteelcorrosioninnewstructures.Ontheother hand,temporary techniques are thoseintended tochange the prevailing corrosion conditions of the structures by lowering its chloride content, such in electrochemicalchloride extrac-tion(ECE)[13–18],orbyincreasingthepHofconcrete,such inelectrochemicalrealkalization(ER)[19,20].Inthisworkwe concentrateonapplicationsofthetechniquesaimedtoprevent theonsetofcorrosion(CPre),improvetheprevailingconditions (ECE)orstopthecorrosionofsteelreinforcement(CP),dueto chloridecontaminationofconcrete,excludingsacrificialanode applications.
Alltheelectrochemicaltechniqueshaveincommonthe reac-tionsatthesurfaceofsteel,thecathode,i.e.oxygenreductionto producehydroxideions(thebasisofER),andeventual hydro-gen gas evolution if negative enough potentials are reached. Hydrogen production is considered as a potentially harmful process, dueto the possibility of hydrogen embrittlement of highstrength steels [5,6].Besides to thesereactions the sys-tembenefitsalsofromeffectsduetomigrationofionsinduced bytheelectricfield:hydroxide(OH−)andchloride(Cl−)ions movefromcathodetotheexternalanode. Thislattereffectis thebasisofECE.Thepermanenttechniques,i.e.CPreandCP canbeconsideredasmoresophisticatedinthesensethatthey needtoguaranteethemaintenance(CPre),orthenew forma-tion andmaintenance(CP), of the passivatinglayer onsteel, bymaintaining the potentialof steel belowthe pitting poten-tial imposed by the presence of a certain Cl− concentration in the concrete’s inner pore solution [9–12]. These electro-chemical conditions induce a reduction of the ratio of the concentrations of chloride andhydroxideions, [Cl−]/[OH−], near the steel. A non-negligible contribution to the mainte-nanceofthepassivatinglayercomesfromtheso-calledchloride barriereffectactinginCPreandCPapplicationsonsteel rein-forcedstructurespermanentlyexposedtoanaggressivechloride environment[9,11].
The operation conditions of the abovementioned electro-chemicaltechniquesdifferineachcase.CPandCpre,applied toreinforced concrete,needusingapermanentlyfixedanode, whichisusuallyanembeddedmetallicwiremesh,typicallya titaniummeshactivatedwithmixedmetaloxides,ortheyuse conductive coatings or overlays, such as conductive cemen-titious overlays [21–24]. CPtypically applies current density values between 5 and 20mA/m2, while CPre needs only 1–3mA/m2. Nevertheless, in the case of CP the actual cur-rentdensityneededtoeffectivelyprotectthesteelishigherthe higheristheCl−contentofconcrete.ThesuccessofCPorCPre dependsgreatlyonanoptimumdesignoftheanodicsystem,able toprovideanadequatecurrentdistributiononthesteel reinforce-ment[9].ECE,asatemporarytechniqueaimedtoreducetheCl− contentofconcrete,usesexternalanodesandelectrolytes[25], althoughit hasbeendemonstratedthataconductive cementi-tious anodic overlay can also be used as the anode for ECE
[26,27,28,29].ThetypicalcurrentdensityforECEapplications onreinforcedconcreteelementsisintherange1–5A/m2,while
thetotalelectricchargepassedisusuallybetween1×106and 5×106C/m2.Fromanelectrochemicalpointofviewthe cur-rentdensityshouldbedefinedasreferredtoelectrodesurface, i.e. the surface ofthe steel cathode. However,in engineering fieldapplicationsitissometimesdifficulttoknowthesteel rein-forcementarea.So,manytimesthecurrentdensityisreferredto exposedconcretesurface,which,inthecaseofanodicoverlay systemsisequaltotheanodearea.
InthecaseofCPacriticalpointofconcernisthepossibilityof malfunctionoftheanodicsystem,duetotheacidityproducedby theelectrochemicalreactionsattheanode,whichcanimpairthe contactbetweentheembeddedconductingmaterialoftheanode andthesurroundingcementpaste.Thisriskincreaseswhenthe appliedcurrentdensityishigherthan20mA/m2[21].
The Departmentof CivilEngineering of the University of Alicantehasbeenconductingresearchontheuseofconductive cementpastes(CCP),basedonmixesofcementwithdifferent carbonaceousmaterials,asanodiccoatingsforapplicationsof electrochemicaltechniquesonreinforcedconcrete[24,26–31]. Oneofthemostappealingpossibilitiesofferedbythese perma-nentanodicoverlaysisthepossibilityofcombinedsuccessive treatments ofECEplusCP,withoutchangingtheanode.This combination of treatments may be convenient in the case of structuresheavilycontaminatedwithCl−ions,whosechloride environmental load is expected tobe maintained highin the future, forinstancethecaseofreinforcedconcreteexposedto de-icingchloridesalts,oraharshmarineenvironment.Inthese casesitmaybedeemednecessarytofirstreducetheCl−content ofconcretebyapplyingECE,andlatermaintainthesteel pro-tectedbyapermanentCPtreatment,withouttheneedtoapplya toohighCPcurrentdensity,thusreducingtheriskofmalfunction oftheanodeduetotheacidityproducedatitssurface.
2. Methodology
Table1
Nomenclatureofspecimensforapplicationoftheelectrochemicaltechniques.
Studiedtechniques Initial%Cl−inconcrete Referencesample Treatedsample
CP 2 R(noelectrochemicaltreatment) A(CPtreated)
CPre 0 P(noelectrochemicaltreatment) B(CPretreated)
ECE+CP 2 ER(treatedonlywithECE) EA(ECE+CPtreated)
ECE+CPre 2 EB(ECE+CPretreated)
Figure1.Sketchofreinforcementofsamplesandconnectionofthecathodicsystem(steelreinforcement). Adaptedfrom[24].
ontotheconcreteoranodicoverlaysurface,inordertosimulate thecontinuedchloridecontaminationduetoexposuretoavery aggressiveenvironmentasmentionedabove.
2.1. Reinforcedconcretespecimens
Thespecimenswereprism-shapedreinforcedconcrete ele-ments, with a dimension of 18×18×8cm3, which were reinforced by agrid 16×16cm2 composedof six steel bars (5mmdiameter)weldedsymmetricallyformingsquaresof5cm side,and placed 2cm under the anode, Fig.1.The concrete dosagewasasshowninTable2.Twomixeswereprepared:one withoutaddedchloride for preparing the specimens intended for pure cathodic prevention (CPre) treatments, and another mixcontaining2%Cl−relativetocementmassforthe speci-mensusedincathodicprotection(CP)applicationsorcombined treatments (ECE+CP) and (ECE+CPre), see Table 1. Once the formworkwasremoved, thespecimens were moist-cured at95–98%relativehumidity(RH)for28days.The
character-Table2
Concretedosageforpreparationofthetestspecimens.
Material Dosage
PortlandcementCEMI42.5R 250kg/m3
w/cratio 0.65
Limestoneaggregatemax.size 12mm
1890kg/m3
Superplasticizer 2.50kg/m3
NaCl Nilor3.3%(2%Cl−
relativetocementmass)
istics of the hardenedconcretewere as follows: compressive strength37.8N/mm2[32],porosity11.1%[33],andbulkdensity 2.38T/m3[34].
Fig. 1 also shows the system used for connecting the reinforcement(cathodesystem)tothenegativepoleofthe elec-tric powersource, through plastic isolated copperconnectors screwedtotherebar.
2.2. Commonexperimentaldetailsoftheelectrochemical tests
Figure2. Sketchofspecimenassembly. Adaptedfrom[24].
theratiobetweenthesurfaceofconcretecoveredbytheanodic overlayandthetotalsurfaceofthesteelbarswas1.7,Fig.2.All current densityandelectric chargedensityvalues reportedin thisworkarerelativetosurfaceofconcrete,(equaltotheanode surface),exceptotherwisestated.
Theresistivityofthe graphite–cementpastewasmeasured through the four-probemethod.To thisend, pastespecimens werecastin4×4×16cm3moulds,andmoist-curedat95–98% RH during 14 days. The experimental details of the mea-surementscanbefoundelsewhere[35].Theaverageobtained resistivitywas1.5m.
Themeasurementsofsteelcorrosionpotential(Ecorr)andall thesingleelectrodepotentials,wereperformedusingAg–AgCl referenceelectrodes.Theseelectrodeswerehousedinrespective holesdrilled fromthe exposedsurface of the concrete speci-men(that bearing thegraphite–cement anode)tothe vicinity oftherebar,Fig.2.Forthispurpose,theholesweresheathed withaplastictube,andfilledwithaKOH0.2Maqueous solu-tion,tryingtoapproachthephysical-chemicalconditionsofthe concrete’sinnerporesolution.
In thisway ninespecimens were prepared,seven of them with salt in the mixing water and two without it. Two of thesaltedspecimens wereusedonlyfordetermining the effi-ciencyoftheECEprocess.Concretecoreswereextractedfrom them,andtheir chloride contentprofiles weredetermined, in one casebefore and in the other caseafter ECE. Thesetwo specimens were discarded after coring.The seven remaining specimenswereintendedforthetestscorrespondingtoCP,CPre, and the combined treatments (ECE+CP) and (ECE+CPre), seeTable1.
TheECEefficiencieswerecalculatedasthepercentagesof reduction of the initial chloride content. Obtainingthe chlo-ride content profiles before and after the ECE trials allowed calculatingthelocalandoverallefficiencies.Attheendofthe 24weeksof exposuretoasevereCl−load,i.e.thefirstphase of CP andCPretreatments,see Section2.4,chloride content profileswere obtained from all the reinforced concrete spec-imens. The Cl− profileswere measuredfollowingessentially RILEM recommended procedures [36]. Cylindrical concrete cores,95mmdiameterand20mmheight(uptotherebardepth),
wereextracted.Fromthesecores,concretedustsampleswere obtainedbygrindingthin(2mmthick)successiveparallellayers totheexposedsurface[36].Inthisway10concretedust sam-ples weregainedfromeachcore, thusallowingthe obtention ofsufficientlydetailedchloridecontentprofiles.The determina-tionofthesamples’acidsolublechloridecontentswascarried outbypotentiometrictitration[37,38].Allthechloridecontent valuesareexpressedinthisworkas%Cl−relativetocement mass.
2.3. ECEtreatments
Fourofthespecimensmadewithsalinemixingwaterwere subjected toECE.Forthispurpose,thespecimenswere elec-tricallyconnectedinseriesbypairstoadirectcurrentsource. The relevant parameters of the ECEtreatments are shownin
Table3.Alowchargedensitywasapplied,only1.5MC/m2 rel-ativetoconcretesurface(2.6MC/m2relativetosteelsurface). Thecurrentsourcefeedingvoltage(Efeed)wascontrolledata levelbelow40Vduringtheprocesses,forsafetyreasons.Itwas necessary inthis respect tointerrupt the current passage two times (twopausesof 24h eachone)alongthe treatment.The wholeprocesseswereperformedinsideafumehoodto elimi-natethechlorine,Cl2(g),producedbyelectrochemicaloxidation of the Cl− ionsextracted from the concrete. When the ECE processeswerefinished,thepHvaluesoftheelectrolyteswere measuredinordertochecktheacidifyingeffectcausedbythe electrochemicalanodicreactions.
2.4. ApplicationofCP,CPreandthecombinedtreatments ECE+CPandECE+CPre
Thissectiondescribesthedetailsoftheexperimentscarried outtodemonstratetheapplicabilityoftheGCPanodesfor com-binedprotectivetreatmentsofECE+CPandECE+CPre,please refertoTable1.
Table3
SummaryofECEdata.
ECE.SpecimenswithGCPasanode. Electrolyte:dammeddistilledwater
Initial%Cl− 2%relativetocementmass
Currentdensity 2A/m2ofconcreteexposedsurface(3.4A/m2ofsteelsurface)
InitialΔEfeed 16–24V FinalΔEfeed 23–22V
Electricchargedensity 1.5MC/m2ofconcreteexposedsurface(2.6MC/m2ofsteelsurface)
handtheapplicationofCPrewith2mA/m2ofcurrentdensity (relativetoconcretesurface)toasamplepreviouslyECEtreated (EBinTable1)andtoanothermanufacturedwithoutsaltandnot ECEtreated(BinTable1).Thevaluesofthecurrentdensities relativetothesteelbarssurfaceare25.5mA/m2and3.4mA/m2 fortheCPandCpretreatments,respectively.Thedirectcurrent sourcewasprogrammedtomaintainaconstantcurrentdensity alongthe wholeprocesses. Eachapplicationhasits reference samplewithouttreatmentofCPorCPretocomparetheresults. Thereferencesampleforthespecimenssubjectedtocombined treatments(EAforECE+CP,andEBforECE+CPre)isER.R isthereferenceforA,andPisthereferenceforB.
TheapplicationofCPandCPreconsistedoftwophases: Phase1.First24weeks.TheaforementionedtreatmentsCP andCPrewerecontinuouslyappliedduringthefirst13weeks. Then,thecurrentwasswitchedofffor4weeksandafterthat, treatmentswereresumedtotheend.Chloridecontaminationwas continuouslyapplied,evenduringtheswitchoffperiods.
While applying the CP and CPre treatments some elec-trochemical parameters were measured. During the current passingperiodsthefeedingvoltageofeachspecimen,Efeed, wasobtainedas thepotential differencebetweencathode and anode; andthe individual anodicand cathodic potentials,Ea andEc,respectively,weremeasuredagainstthereference elec-trode Ag–AgCl. Finally, in order to check the efficiency of CPandCPreasmaintainersof protectionconditions ofsteel, the “100mV decay” criterion was used, as is specified in ISO12696:2012[39].Thiscriterionhasbeenalsoextensively employedforthispurposebyseveralresearchers[21,40].The methodconsistsinobtainingthe4hpotentialdecay(Edecay), thatisthedifferencebetweenEc4h(thevalueofEc4hafterthe currentswitchoff),andtheinstant-offcathodicpotentialEcio, whichinthiscasewasmeasured1safterthecurrentswitchoff. Theminimumvalueofthe4hdepolarizationmustbe100mV foranadequatecorrosionprotectionofsteel[39].Thevaluesof Ecioweremonitoredwithanautomaticdataloggerabletoobtain andrecord500measurementsin6s,afterthecurrentswitchoff. Once the 24 weeks processes were fulfilled, cores were extractedfromallspecimensofTable1,andtheirrespectiveCl− contentprofileswereobtained.Thiswasdonewiththepurpose ofevaluatingtheneteffectoftheelectrochemicaltreatmentson theCl−ionuptakebythereinforcedconcretespecimensduring thecontinuedexposuretoaveryaggressiveenvironment.
Phase2.Attheendof Phase1 itwasobservedthatallthe specimens had lost the steel protection condition, evidenced by Edecay values lower than 100mV. Then, it was decided tostartthissecond phasewiththeobjectiveof recoveringthe
protectionconditionsofsteelbyadjustingthecurrentdensityof theCPtreatments.Theprocedurewastoincreaseprogressively the current density during 4 weeks, starting with a value of 20mA/m2,untilobtainingtheprotectionconditions.
3. Resultsanddiscussion
3.1. ApplicationofECE
Four of the reinforced concrete specimens weresubjected toan ECEtreatment beforestarting thefirst phaseof theCP andCPretreatments,see Section2.3.Oncefinished the ECE processwiththesettledparameters,Cl− contentprofileswere obtained,correspondingtothestatesbeforeandaftertheECE treatment. ThelocalECE efficiencies,understood as percent-ageofCl−contentremoved,areplottedinFig.3.Theaverage of removedCl− was51%of theinitialcontent,i.e. the resid-ualCl− contentof concreteafterECEwasapproximately1% referredtocementmass.Thisindicatesagoodperformanceof the ECEprocessapplied onaconventionalordinaryPortland cement concrete with the GCP anodic overlay system, for a relativelylowchargedensityof1.5×106C/m2relativeto con-cretesurface.Thisresultcanbecomparedtothe41%efficiency obtainedforaverysimilarreinforcedconcreteelement,withthe sameinitialamountofCl−,subjecttoanECEtreatment,using aTi–RuO2 meshanode,andpassingatotalchargedensityof 1MC/m2relativetoconcretesurface[26].
ThepHvaluesdeterminedfortheelectrolytes,aftertheECE experiments,wereintherange5–5.5.Thismeansthattheacidity
0 20 40 60 80
0 2 4
0 4 8 12 16
Ef
fi
c
ie
nc
y(
%
)
Depth (mm) Efficiency
Initial content of chlorides
Final content of chlorides
Cl
- co
n
ten
t (
%
r
e
la
ti
ve t
o
cemen
t
ma
ss)
Figure3.ChlorideconcentrationprofilesbeforeECE(initial)andafterECE (final),andlocalefficienciesoftheextractionprocess.ECEdetails:current density:2A/m2,chargedensity:1.5MC/m2,bothrelatedtoexposedconcrete surface.
-100 100 300 500 700 900
0 5 10 15 20 25
Δ
Edec
a
y
(m
V)
Time (weeks of treatment) B
A
EB
100 mV EA
Figure4.EvolutionofΔEdecayduringtheCPorCPretreatments.A:CP;B: CPre;EA:ECE+CP;EB:ECE+CPre.AllofthemsubjectedtoCl− contam-inationduringthe24weeks.Theelectrochemicaltreatmentswereinterrupted betweenweek13andweek17.
Adaptedfrom[24].
oftheelectrolyteshadincreasedslightly,(theinitialelectrolyte wasdistilledwater).Thisacidifyingeffectmaybeduetoseveral ofthe electrochemicalanodicreactions,namelytheoxidation ofhydroxideionsorwatertoO2(g) andthe oxidationof car-bontoCO2(g).Itispossiblethatthealkaline characterofthe graphite–cementpasteanodemayhavereducedtheacidity pro-ducedbythoseelectrochemicalprocesses.Itisworthnotingthat nosharpincreaseofthefeedingvoltagewasobservedduringthe ECEtreatments.Thissuggeststhatnoimportantdamageofthe GCPoverlayhasbeenproducedduringECE[21],eventhough thesetrialsareperformedwithahighcurrentdensityof2A/m2. WemustrecallthattheECEtrialsareperformedunder continu-ousliquidpondingoftheanode,anditsdurationisshort,about eightdays.
3.2. FirstphaseofCPandCPretreatments
Inthissectionwedescribetheresultsoftestscarriedoutto investigatetheperformanceoftheGCPanodesduring protec-tiveelectrochemicaltreatmentstoreinforcedconcreteelements affected by steel corrosion due to chloride contamination, such are CP, CPreand combined treatments of ECE+CP or ECE+CPre,seeTable1.
ToverifytheeffectivenessofCPandCPretreatmentsfor pro-tectingsteelfromcorrosion,the“100mVdecay”criterion[39]
wasused,asstatedinSection2.4.Fig.4 showstheevolution oftheEdecayvaluesforthespecimensinTable1,duringthe 24weeksexperiments.TheEdecay valuesoftheAspecimen, treatedonly withCP, practically never reached the threshold valueof100mV.Itseemsthata15mA/m2currentdensitywas notsufficienttoprovideprotectiontosteelinsuchharsh condi-tions:initialCl−contentof2%plusthecontinuedsaltingregime (65mlNaCl0.5Mweeklysprayedontotheanodicoverlay sur-face).RegardingtheEAspecimen(ECE+CP),theprotection conditionsof steelwerekeptduring11weeksbecause ofthe currentcirculation,despiteexternalCl−loading.Cathodic pro-tectionof15mA/m2currentdensity,relativetoconcretesurface, wasabletokeepprotectiveconditionsforthesteelreinforcement iftheinitialCl−contentofthespecimenwasabout1%(EA).
0 2 4 6
0 5 10 15 20
C
lori
de c
o
n
ten
t
(%
r
el
a
tiv
e to
c
em
en
t
mass)
Depth (mm)
%Cl-ER
%Cl-EA
%Cl-EB
Figure5.ProfilesofCl−contentinspecimenstreatedpreviouslywithECEand afterwithCP(EA),withECEandafterCPre(EB),andinthereferencesample onlytreatedwithECE(ER),allofthemsubjectedtoCl−contaminationprocess, afterECEandfirstphaseofCPorCPre(24weeks).
Adaptedfrom[24].
In the caseofthe specimen withinitialCl− contentof about 2%(A),ahighercurrentdensitywouldbeneededforreaching theprotectionconditions[9,11].Theseobservationscorroborate themainhypothesisofthepresentresearch,i.e.incasesof rein-forcedconcretestructureswithahighCl−contaminationsubject toveryharshchlorideenvironments,itwouldbeadvantageous toapplysuccessivelyaninitialECEtreatmenttoreducetheCl− content,andthenmaintainprotectiveconditionstosteelthrough acontinuousCPtreatmentwithouttheneedofusingatoohigh CP currentdensity,whichcouldeventuallyimpairthe perfor-manceoftheanodicsystem[21].Thesecombinedtreatments, ECE+CP,wouldbemoreconvenientlyimplementedwiththe CCPcoatings,sincethesameanodecanservebothfortheECE andfortheCPtreatments.
RegardingtheCPretreatedspecimens(cathodiccurrent den-sity2mA/m2relativetoconcretesurface),specimenBshowed
ΔEdecayvalueshigherthan100mVuptothecurrentswitchoff at13thweek, confirmingthecapacityofcontinuouslyapplied CPretreatmentstokeepsteelprotectionconditionsfor an ini-tially Cl− freereinforced concrete, despiteextensiveexternal Cl− load[9,11,41,42]. Onthe other handsuch alow current densityisunabletoprotectsteelifconcreteispreviously contam-inatedatalevelofabout1%relativetocementmass,andsteel hasstartedtocorrode,asshownforspecimenEB(ECE+CPre) inFig.4.
AttheendofPhase1allthereinforcedconcretespecimens hadreached avery highdegreeof Cl−contamination, ascan beappreciatedinTable4.Nevertheless,somecomparisonscan be doneonthebehaviour ofthedifferentcases. Forinstance,
Table4
Finalaveragedchloridecontents(expressedin%Cl−relativetocementmass)attheendofthe24weeksofexposuretoasevereCl−load(firstphaseofCPand CPretreatments).
Specimen InitialCl−content (%ref.cem.mass)
Electrochemicaltreatmentprevious tothe24weeksfirstphase
Electrochemicaltreatmentduring the24weeksfirstphase
FinalaveragedaCl−
content(%ref.cem.mass)
P 0 – – 4.93
R 2 – – 6.08
ER 2 ECE – 4.26
A 2 – CP 5.39
B 0 – CPre 3.94
EA 2 ECE CP 3.41
EB 2 ECE CPre 3.42
a ThefinalCl−contentwascalculatedasthemeanvalueofthosefoundintheCl−contentprofiledeterminedthroughtheconcretecoverzone(20mmwidth).
(Cl−BEP),whichisdefinedhereasthepercentageofreduction oftheCl−uptakebyconcrete,duetoCPorCPreactions,referred totheCl−uptakeofthereference,(nottreated)specimens,see Eq.(1).
Cl−BEP=(Cl
−UptakebyReference)−(Cl−UptakebyTreatedSpecimen)
(Cl−UptakebyReference) ∗100 (1)
Table 5 shows the net values of the Cl− barrier effect parameterfoundforthespecimenstestedinthiswork,putting in evidence that this parameter reaches values of about 20%intheexperimentalconditionsofthiswork.
3.3. SecondphaseofCPtreatments
Giventhatafterthe24weeksoftreatmentsofPhase1, includ-ing rest periods between the 13th and 17th weeks, the steel reinforcementsinallconcretespecimens hadcompletely lost theirprotectionconditions,andhavingbeendemonstratedthat aCPof15mA/m2wasunabletorestoretheprotective condi-tions(Fig.4),thePhase2wasstarted.TheexternalCl−loadwas discontinuedsinceallthespecimenshadreachedveryhighCl− contents,seeTable4.Intheseconditions,CPwasappliedwith highercurrentdensities.Thequestionwasifitwouldbepossible torecovertheprotectionconditionsofsteelbyincreasingthe cur-rentdensitytotheappropriatevalue.Inthebeginningofthislast phase,thecurrentdensitywassetat20mA/m2.After4weeks inoperation the thresholdvalue of 100mV ΔEdecay was not reached,i.e.theprotectionconditionswerenotobtained,Fig.6. Neithersuccesswasobtainedinasecondattemptat25mA/m2 (datanotshowninFig.6).Finally,athirdstepof40mA/m2was set.Inthiscase,after4weeks,theruleof100mVofΔEdecay wasachievedforEA,AandBspecimens.
Table5
Valuesofthechloridebarriereffectparameterforthetestedspecimens.
Specimen Treatmentof specimen
Reference Treatmentof reference
Cl−BEP (%)
A CP R None 17.0
B CPre P None 21.0
EA ECE+CP ER ECE 26.0
EB ECE+CPre ER ECE 25.7
-100 -50 0 50 100 150 200 250
0 2 4 6 8
Δ
Ede
c
a
y
(mV)
Time (weeks of CP phase 2)
20 mA/m² 40 mA/m²
B
EA
EB 100mV
A
Figure6.EvolutionofΔEdecayduringPhase2ofCP.Firststepof4weekswith 20mA/m2ofcurrentdensity,andthirdstepwith40mA/m2.SpecimensA,B, EAandEB.
Adaptedfrom[24].
Moreover,protectionconditionswereverifiedwiththe mea-surementof depolarization potential difference values7 days after switch off [39]. In fact, more than150mV of ΔEdecay wasreached after7days (209mVforEA,211mVforAand 153mVforB).ThisefficiencyofCPissimilartothatobtained byotherresearchers[40,43].However,thiswasnotthecasefor EB.After4weekswithacathodiccurrentdensityof40mA/m2 the protection conditions were not recovered for this latter specimen.
4. Conclusions
Theresultsofthisworkpointoutthatitispossibletousea graphite–cementpaste, overlaidonthesurfaceofareinforced concreteelement,astheanodeforsuccessivetreatmentsof elec-trochemicalchlorideextraction,toreducethechloridecontent, andthencathodicprotectiontomaintainprotectiveconditions forthesteelreinforcement.Thefollowingaspectscanbe empha-sized,namely:
• The chloridebarriereffectparameter(Cl− BEP)is defined asthepercentageofreductionoftheCl−uptakebyconcrete, duetoCPorCPreactions,referredtotheCl−uptakeofthe reference(nottreated)specimens.Thisparameterallows eval-uatingthemagnitudeofthechloridebarriereffectduetothe application of CP or CPre toreinforced concreteelements continuouslyexposedtoaharshchlorideenvironment.The foundvaluesof thisparameter,bothforsimpleCP orCPre trialsandforthecombinedtreatmentsofECE+CP,areabout 20%,intheexperimentalconditionsofthiswork.
• Acathodiccurrentdensityof2mA/m2,typicalofCPre appli-cations,isunabletoprotectsteelafteranECEtreatment.
• Itispossibletorecoverprotectiveconditionsagainstcorrosion of steel reinforcementinconcretebyapplying acombined treatmentofECEfollowedbyacontinuousCPtreatment.The currentdensityvalueoftheCPstepmustbesetattheproper value,accordingtotheresidualchloridecontentinconcrete. TheneededCPcurrentdensityvaluewillbelowerthanifthe ECE wasnot applied,thusreducing the riskof damage of theanode. Inthissense theGCPoverlaysonconcretemay showanadvantageousversatility,overothertypesofanodic systems,sincethesameanodeisusedonthetwostepsofthe combinedtreatment.
Acknowledgements
ThisresearchwasfundedbytheSpanishAgenciaEstatalde Investigación(AEI),andFondoEuropeodeDesarrolloRegional (FEDER) through project BIA2016-80982-R. We acknowl-edge also funding from the Spanish Ministerio de Ciencia e Innovación (MAT2009-10866), and Generalitat Valenciana (PROMETEO/2013/035).
Theauthorswouldliketodedicatethisworktohonourour masterandfriendProf.CarmenAndradePérdrix,whosuggested ourresearchgroupundertakingresearchontheapplicationof electrochemicaltechniquestoreinforcedconcretestructures.
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