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1、SECRETARIATUSEHeadershouldbeblank.SECRETARIATUSEFootershouldbeblankELECTROCHEMICALBEHAVIOFHOTROLLED304STAINLESSSTEELDURINGCHEMICALPICKLINGINHClBASEDELECTROLYTESLILianFu1CAENENPeter1VANTRAPPENJoost1CELISJeanPierre21.UGINE
2、ALZBelgiumNV(Arcelgroup)Swinnenwijerweg5B3600GenkBelgium2DepartmentMTMKatholiekeUniversiteitLeuvenKasteelparkArenberg44B3001LeuvenBelgiumAbstract:Themechanismkiicsofchemicalpicklingofhotrolled304stainlesssteeloxidizedath
3、ightemperatureswasinvestigatedinHClbasedelectrolyteswithweightlosscrosionpotentialEISmeasurements.CrosionproductswereacterizedwithSEMEDXXPS.ThemechanismofchemicalpicklinginHClbasedelectrolytesisassociatedwithanodicbright
4、ening.Ahighlyionicallyconductivecrosionproductlayercoveringthebrightenedsurfaceensuresahighcrosionrateoftheunderlyingstainlesssteel.TheadditionofferricionstoHClbasedelectrolytessignificantlyenhancesthecrosionrate.Ontheco
5、ntrarytheinfluenceofHClbecomeslessimptantbecausehighlyconcentratedresultinginabrighteningofthestainlesssteelsurface.Theeffectofferrousionsonthecrosionrateisnegligible.Thegetransferresistanceofhotrolledstainlesssteeldecre
6、aseswithpicklingtimeduetotheprogressiveremovalofoxidelayers.Keywds:304stainlesssteelpicklingHClbasedelectrolytesoxidelayercrosionpotentialelectrochemicalimpedancespectroscopy(EIS)anodicbrightening0.IntroductionThepicklin
7、gofstainlesssteelscommonlyincludesthermalmechanicalelectrochemicalchemicaltreatments[12].Thethermaltreatmentsoftensthemetalreleasesthewkhardeninginducesaunifmgrainstructureeliminatessurfacedefects[3].Duringthatprocessing
8、anoxidelayerachromiumdepletedsublayeraregenerallyfmedonstainlesssteels.SubsequentmechanicalelectrochemicalchemicaltreatmentsareappliedfremovingtheoxidelayerthechromiumdepletedmonchemicalpicklinginmixedHFHNO3acidsiseffect
9、ivebutnowadaystheuseofsuchHNO3containingmixedacidsisrestrictedfenvironmentalconcerns[146].Alternativeprocessesaresinglemultistepproceduresinoxidizingacidse.g.HFHClH2SO4.AmongtheseacidsH2SO4[79]HCl[910]aresolelyusedfthepi
10、cklingofmildsteels.Ironoxideseffectivelydissolveinsuchacidsthebasematerialremainsalmostunaffected.Howevertheseacidsalonecanhardlyremoveoxidelayersonstainlesssteelsbecausetheseoxidelayersarecompactquiteinsoluble.Meoverbes
11、idestheoxidelayersthechromiumdepletedsublayerhasalsotoberemoved.Indeedthatsublayerhasalowercrosionresistanceincomparisontothebulkstainlesssteel.Oxidizingagentssuchasferricionsdissolvethechromiumdepletedlayerinsequencethe
12、oxidelayersareundercut[1112].InoxidizingHFmixedHFH2SO4electrolytesintergranularcrosiontakesplace[13]thepicklingisusuallyinsufficientduetoanactivetopassivetransitionofthestainlesssteel[12].Byusingatwosuccessivesteppicklin
13、ginHClHFelectrolytesasurfacefinishfreeofoxidescaleswithalimitedintergranularcrosionwaspreviouslyachieved[1113].SECRETARIATUSEHeadershouldbeblank.SECRETARIATUSEFootershouldbeblankthreeelectrodeswereimmersedindeionizedwate
14、rf30min.Thentheelectrodeswereimmersedinthetestelectrolyteelectrochemicalmeasurementswerestarted.Sincethesurfaceofoxidizedstainlesssteelsamplesevolvesduringpicklingduetotheprogressiveremovaloftheoxidelayersthechromiumdepl
15、etedlayerEISmeasurementscannotbeperfmedoverabroadrangeoffrequencies.TherefedynamicEISmeasurementswereperfmedataconstantfrequencyedbetween20Hz2kHz.Theperturbationpotentialamplitudewas10mV.2.Results2.1.PicklingkiicsinHClba
16、sedelectrolytesTheevolutionwithimmersiontimeofweightlosscrosionpotentialofoxidized304stainlesssteelisdependentonHClferricionconcentrations(Figures12).Theweightlossineachelectrolyteincreaseslinearlywithimmersiontime(Figur
17、es1a2a)exceptduringtheinitialstagewhereaparabolicregimewasnoticed(seeinsetinFig.1a).Theparabolicregimeisribedtothesimultaneousremovaloftheoxidelayersthedissolutionofunderlyingmetalwhereasthesubsequentlinearregimeisrelate
18、dtometaldissolution[11].Thatlinearrelationindicatesaunifmcrosionthatisconfirmedbytheconstantcrosionpotentialafteracertainimmersiontime(Figures1b2b).Meoverthelinearincreaseinweightlosstheconstantcrosionpotentialindicateth
19、atthe304stainlesssteelishighlyreactiveintheHClbasedelectrolytesusedthattheactivetopassivetransitionnoticedinHFH2SO4electrolytes[12]doesnottakeplace.050100150200250300350400012345670102030400.00.20.40.60.80.54MFe30.27MFe2
20、(a)Weightloss(mgcm2)Immersiontime(s)HClcontent0.69M2.74M5.49M6.86M0501001502002503003504000.320.280.240.200.160.12(b)0.54MFe30.27MFe2Crosionpotential(V.vs.AgAgCl)Immersiontime(s)0.69MHCl2.74MHCl5.49MHCl6.86MHClFig.1Effec
21、tofHClconcentrationon(a)weightloss(b)crosionpotentialofoxidized304stainlesssteelinelectrolytescontaining0.54Mferricions0.27Mferrousions.Insetof(a)showstheweightlossattheinitialstage.Theweightlossappearstobealmostindepend
22、entoftheHClconcentrationwithintheacidcontentused(Fig.1a)whereasasignificantdependenceontheferricioncontentisnoticed(Fig.2a).Chlidesbehaveasdepassivatstohinderthepassivationofstainlesssteel[21]thustolowerthecrosionpotenti
23、al(Fig.1b).HoweversincetheweightlossisalmostindependentofHClcontent(Fig.1a)itseemsthatthechlidesusedinthisstudyarepresentatsufficientleveltodepassivatethewholesurface.Incontrastferricionsactaselectronacceptsincreasethecr
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