Maurizio
Carotenuto
a,
Giovanni
Libralato
b,∗,
Hatice
Gürses
a,
Antonietta
Siciliano
b,
Luigi
Rizzo
c,
Marco
Guida
b,
Giusy
Lofrano
daDipartimentodiChimicaeBiologia“AdolfoZambelli”,Università,degliStudidiSalerno,viaGiovanniPaoloII132,84084,Fisciano,SA,Italy bDepartmentofBiology,UniversityofNaplesFedericoII,ComplessoUniversitariodiMonteS.Angelo,ViaCinthiaed.7,80126,Naples,Italy cDepartmentofCivilEngineering,UniversityofSalerno,viaGiovanniPaoloII132,84084,Fisciano,SA,Italy
dCentroServiziMetrologicieTecnologiciAvanzati(CeSMA),UniversityofNaplesFedericoII
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r
t
i
c
l
e
i
n
f
o
Articlehistory:Received17December2018
Receivedinrevisedform28January2019 Accepted30January2019
Availableonline3February2019 Keywords:
Nonylphenolethoxylates Wastewater
Advancedoxidationprocesses Radicalscavengers
Ecotoxicology
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Nonylphenolethoxylated(NPEOs)nonionicsurfactantshavebeenincreasinglyusedindifferent indus-trial,commercialanddomesticapplications.Unfortunately,theyareclassifiedasendocrinedisrupting chemicals(andalsoconsideredascontaminantsofemergingconcern)havingadverseeffectsonanimal andhumanreproduction.Thetreatmentofnonylphenol-decaethoxylated(NP-10)viaH2O2/UV-C
pro-cessatdifferentreactiontimes(5,10,20,40,80min)andH2O2concentrationswasinvestigated.After
80mintreatmenttheremovalratesofNP-10solution(initialconcentration100mg/L)indeionizedwater were88%,97%and98%for10,20and100mg/LofH2O2respectively.Thesameexperimentalconditions
wereappliedtorealwastewaterspikedwith100mg/LofNP-10showingthefollowingremovalrates: 84%,98%and99%,respectively.ThepossiblecontributionofdifferentradicalstoNP-10degradationby H2O2/UV-Ctreatmentwasinvestigatedbyevaluatingtheeffectofdifferentradicalscavengers(namely
NO3−,NaCl,Na2SO4,Na2CO3,KH2PO4andphatalate).Toxicitydata(Aliivibriofischeri,Raphidocelis
sub-capitataandDaphniamagna)ontreatedsolutionsandwastewaterhighlightedthepresenceofresidual toxicityinallsamplesevidencingthatnocompletemineralizationoccurred.
©2019InstitutionofChemicalEngineers.PublishedbyElsevierB.V.Allrightsreserved.
1. Introduction
Nonylphenol ethoxylates (NPEOs) are surface active agents
(surfactants)thatarepartofthebroadercategoryofsurfactants
knownasalkylphenolethoxylates(APEs).Dependingonthedegree
ofethoxylation,NPEOspresentoctanol-waterpartitioning
coeffi-cients(logKow)rangingfrom4.20to4.50changingitssuitability
for the specific use, generally, at relatively low cost (Mcleese
etal.,1981;Ciabattietal.,2009).Thesecharacteristicsmakethem
suitablefordifferentindustrial,commercialanddomestic
applica-tionsinsurfacecleaner,lubricant,shampoo,anddetergents(CEPA,
1999).NPEOscanreachfromtenstohundredsofmg/Linindustrial
effluents(ZhouandZhang,2017;Chokweetal.,2017).
∗ Correspondingauthorat:DepartmentofBiology,UniversityofNaplesFederico II,ComplessoUniversitariodiMonteS.Angelo,ViaCinthiaed.7,80126,Naples,Italy.
E-mailaddresses:mcarotenuto@unisa.it(M.Carotenuto),
giovanni.libralato@unina.it(G.Libralato),gurses.hatice90@gmail.com(H.Gürses), antonietta.siciliano@unina.it(A.Siciliano),l.rizzo@unisa.it(L.Rizzo),
marguida@unina.it(M.Guida),glofrano@unisa.it(G.Lofrano).
Althoughthe toxicity ofNPEOs varies,rangingfrom
moder-atelytoxictotoxictofishandaquaticorganismsonanacutebasis
and increasingas thelengthoftheethoxylatechain(molecular
weight)decreases,agrowingconcernisposedbytheirby-products,
mainly nonylphenol (NP), because of theirpotential estrogenic
effecttotheaquaticbiota(Chenetal.,2007).Accordingto
NP-10safetydatasheetandPAN-Pesticedatabase(2019),onlyacute
toxicityeffectsareavailablesuggestinglow-mediumtoxicity
lev-els,neverthelessitspotentialactivityasendocrinedisruptor(i.e.
variousbacteriamedianeffectconcentration(EC50)>1000mg/L;
EC50=17mg/LforScenedesmusquadricaudaand15mg/LforLemna
minor; lethal median concentration (LC50)=9.3–21.4mg/L and
20.9mg/LforDaphniamagnaandGammaruspulex(48h),
respec-tively;fishLC50=3.8-7.7mg/LforPimephalespromelas(96h)and
16.4mg/LforPoeciliareticulata(48h)).
NPisapriorityhazardoussubstance(PHS)undertheEU’sWater
FrameworkDirective(WFD)andisconsideredanemergingorganic
pollutantthatmimicsthenaturalhormone17-estradiol
interfer-ingwithorganisms’reproduction(LeeandLee,1996;Soléetal.,
2000;Reisetal.,2014).InviewofNPEO’stoxicity,theEuropean
UnionunderDirectiveNo.,2003/53/ECprohibitedtheuseofNPand
https://doi.org/10.1016/j.psep.2019.01.030
Fig.1.a)Verticalreactorconfiguraton;b)Horizontalreactorconfiguration.
NPEO’sandrecommendedtheirreplacementwithcostlyalcohol
ethoxylates.Currently,manufacturerswithintheEUcannot
pro-ducetextilesorclothingcontainingNPorNPEO,butthisdoesnot
meanthattheycanbefoundinwastewatergeneratedfromthe
wash-offofextra-UEmanufacturedclothes(Lofranoetal.,2016a,b).
TheEU 2004ban onmanufactureof textiles and clothing
con-tainingNP(EOs)ledtoafallinNPinUKwaterbodies,butupto
20%oftheNPlevelsfoundinUKwaterbodiescomesfrom
wash-offfromimportedtextilesandclothing(UKEnvironmentAgency,
2013).
Moreover,NPstilloccursintheaquaticenvironmentwith
con-centrationsvaryingwidelyinsurfacewaterfromtensofng/L(Brix
etal.,2010)todozensofmg/L(Pengetal.,2008).Duetolowcostand
higefficiency,NPEOarestillinuseindevelopingcountrieswhere
significantlyhighconcentrations(uptosometensofmg/L)are
detectedintheeffluentofindustrialwastewatertreatmentplants
(WTPs)(Maoetal.,2012).Theyarebeingdischargedcontinuously
intotheenvironmentandthusapropermanagementofsuchkind
ofwastewateris urgentlyrequired.Unfortunately,conventional
biological(such asactivatedsludge)processes arenot effective
inthetreatmentofsohigh(tensofmg/L)NPEOconcentrations,
thereforeasuitableadditionaltreatmentisnecessarytoimprove
theirreduction/removal.Accordingly,variousprocesseshavebeen
investigatedsuchasozonation(Lenzetal.,2004;Ledakowiczetal.,
2005),adsorption(Fanetal.,2011)andadvancedoxidation
pro-cesses(AOPs).AmongAOPs,dfferentmethodshavebeenstudied
inNPEOdegradation,namelygammaradiation/H2O2(Abbasetal.,
2015),UVC/H2O2,photo-Fenton(Karcietal.,2013),(S2O28−
)/UV-C(Olmez-Hancietal.,2013),heterogeneousFenton-likeprocess (Shahbazietal.,2014),heterogeneousphotocatalysis,
eletrochem-icaloxidation andphoto-assisted electrochemicaloxidation (Da
Silvaetal.,2015).However,althoughAOPsareknowntoaffect
water/wastewatertoxicity(Rizzo,2011;Lofranoetal.,2017),only
infewcasesthefinaleffluentwascheckedforresidual
ecotoxic-ity(Lenzetal.,2004;Ledakowiczetal.,2005;Karcietal.,2013;da Silvaetal.,2015),and,frequently,onlyonebiologicalmodelwas
usedlimitingdatainterpretationforecologicalriskassessmentof
NPEOs(Karcietal.,2013).
AmongstAOPs,H2O2/UV-Cisa well-establishedprocess,not
sensiblyaffectedbypH(Parsons,2004).
Inthepresent study,thedegradationofthenonionic
surfac-tantTergitolTMtypeNP-10(CASnumber:127087-87-0),usedin
cleanersanddetergents,paperandtextileprocessing,paintsand
coatings,agrochemicalsandmetalworkingfluidwasinvestigated
byusingH2O2/UV-Cprocess.Experimentswerecarriedoutintwo
reactorconfigurationstoevaluatetheeffectofi)deionizedwater
andspikedrealwastewater,ii)scavengers(CO3−andphtalates)
andintereferringsubstances(NO3−andSO4−).Theecotoxicityof
untreatedandtreatedsampleswasinvestigatedconsideringa
bat-teryoftoxicitytests(Aliivibriofischeri,Raphidocelissubcapitata,and
Daphniamagna).
2. Materialsandmethods
2.1. Chemicalsandanalyticaltechniques
TergitolTMtypeNP-10(C
35H64O11)waspurchasedfrom
Sigma-Aldrich(USA).Theformulationwasacolourlessandhighlywater
soluble.Ultrapurewater(UW)(Milli-Q®systemElix10,Merck
Mil-lipore,Billarica,MA,USA)wasusedforpreparationoftestsolutions.
AstocksolutionofH2O2 (30%w/w;SigmaAldrich,St.Louis,MO,
USA,)wasused.
A high-performance liquid chromatography (HPLC) system
equippedwitha module pump(Thermo SpectraSystem P2000)
and an UV–vis detector (Thermo SpectraSystem) was used for
TergitolTMdetermination.TergitolTMseparationwasachievedby
HypersilODSC18(150mm×4.6mm,5mparticlesizeThermo
FisherScientific,Waltham,MA,USA)reversedphasecolumnusing
amobilephaseofmethanol:water(90:10,v/v) ataflowrateof
1.0mL/min.Injectionvolume,absorbancewavelength,excitation
andemissionwavelengthsweresetat30L,275nm,230nmand
310nm, respectively. TergitolTM concentration was determined
accordingtothecalculationofpeakareasbyexternalcalibration.
Thelimitofdetectionwasidentifiedassignal-to-noiseratio(S/N)
equalto0.050mg/L.
Wastewater, originate from a municipal wastewater
treat-mentplant(WWTP),locatedinCampaniaregion(Italy)receiving
wastewater collected from urban households, agro-industries,
zootechnicalactivities,hospicesandotherfacilities.TheWWTPhad
anaveragecapacityof300,000p.e.,andanaverageflowrate
rang-ingof45,000m3d−1.Thetreatmentprocessincludes:i)Mechanical
pre-treatment (screening and pumping stations, grit and oil
removal);ii)Rainwatersection(primarysedimentationand
aer-atedstorage);iii)Secondarytreatment(nitrification-denitrification
andfinalsettling);andiv)Tertiarytreatment(gravityfiltrationon
sand),anddisinfectionwithperaceticacid.Wastewatersamples
werecharacterisedforbiologicaloxygendemand(BOD5),
chemi-caloxygendemand(COD),totalsuspendedsolids(TSS),nitrogen
asammonia(N-NH3),nitrate(NO3−),andnitrite(NO2−),andtotal
phosphorus(TotalP)accordingtoAPHA(2012).
2.2. Experimentalset-up
H2O2/UV-Cadvancedoxidationexperimentsincludedtwo
con-figurations:a)UV-Clamp,encasedinaquartztube,axiallycentered
respecttothereactorandimmersedintothesolution(vertical
con-figuration,VC);b)UV-Clamphorizontallypositioned10cmabove
trations(10,20,100mg/L)andreactiontimes(5,10,20,40,80min)
lookingforthebestoperativeconditionsofH2O2/UV-Cprocessin
deionizedwater(DW),comparingVCandHCconfigurationsforthe
degradationofTergitolTMconcentration(100mg/L).TheH
2O2
/UV-C process wascarried out atroom temperature(25±2◦C) and
naturalsolutionpH(5.5).Controlexperimentswerealsoconducted
toobserveTergitolTMdegradationintheabsenceofeitherUV-Cor
H2O2.
Thesecondexperimentalscenarioincludedtheserialaddition
totestingsolutionofcompoundsusuallyworkingasscavengers
ofhydroxyl radicals: (NaCl (1000mg/LCl–); Na2CO3 (300mg/L
CO32–), KH2PO4 (10mg/L PO43), NaNO3 (50 and 500mg/LNO3),
852mg/Lofphthalate(correspondingto1000mgO2/LofCOD)as
wellasinterferingsubstancesNa2SO4(500mg/LSO42–),inorderto
evaluatetheirpotentialeffects.
In the third experimental scenario, real wastewater (WW)
taken from a wastewater treatment plant (BOD5=18mg/L;
COD=48.5mg/L;TSS=46mg/L;N-NH3=1.42;N-NO3−=0.25mg/L;
N-NO2-=3.34mg/L;totalP=1.23mg/L)wasspikedwith100mg/L
TergitolTMevaluatingtheinfluenceofmatrixonthebehaviourof
theprocess.
Analysiswascarriedoutatleastinduplicateandreportedas
meanandsemi-dispersion.
Afterwithdrawalofthesamples,theresidualH2O2was
imme-diately quenched with few mL of catalase at 0.1g/L to allow
subsequenttoxicityanalysis.
2.4. Ecotoxicity
ToxicitytestswithA.fischeri,R.subcapitata,andD.magnawere
carriedoutontreated(100mg/LofTergitolTMindeionizedwater
andrealwastewaterspikedwith100mg/lofTergitolTMafter80min
ofphoto-oxidationtreatment)anduntreatedwastewatersamples
TergitolTM.Accordingtoqualityassuranceandqualitycontrol
pro-cedures,bioassaysincludedtheassessmentofnegativeandpositive
controlsaccordingtothecorrespondingstandardmethod.In
par-ticular,theacutebioluminescenceinhibitionassaywascarriedout
usingA.fischeri(NRRL-B-11177)accordingtoISO(2007).The
lumi-nescencewasmeasuredwitha Microtox® analyser(Model500,
AZUREnvironmental)after5and15minat15◦C.Testswerecarried
outintriplicate.DatawereanalysedwithMicrotoxOmnisoftware
andtheresultexpressedaspercentageofbioluminescence
inhibi-tion.
The chronic growth inhibition test with R. subcapitata was
carriedoutaccordingtoISO(2012).Cultureswerekeptin
Erlen-meyer flasks. The initial inoculum contained 104 cell/mL. The
specificgrowthinhibitionratewascalculatedconsidering6
repli-catesexposedat20±1◦Cfor72hundercontinuousillumination
(6000lx).Effectdatawereexpressedaspercentageofgrowth
inhi-bition.
Newborndaphnids(<24hold)wereexposedtosample
accord-ingtotheISO6341method.Daphnidsweregrownat 20±1◦C
revealedsignificantdifferencesamongtreatments,post-hoctests
werecarriedoutwithTukey’stest.Statisticalanalyseswere
per-formedusing Microsoft® Excel 2013/XLSTAT©-Pro(Version 7.2,
2003,Addinsoft,Inc.,Brooklyn,NY,USA).
Finally, toxicity datawere integrated accordingto Persoone
etal. (2003)and Lofranoet al.(2016a,b). Thehazard
classifica-tionsystemisbothbasedonPEorTU50includesaClassIforPE
b20%(score0)(orTU50<0.4),ClassIIfor20%≤PEb50%(score
1)(or0.4<TU50<1),ClassIIIfor50%≤PEb100%(score2)(or
1<TU50<10),ClassIVwhenPE=100%inatleastonetest(score
3)(10<TU50<100)andaClassVwhenPE=100%inallbioassays
(score4)(TU50>100).Finally,theintegratedclassweightscorewas
determinedbyaveragingthevaluescorrespondingtoeach
micro-biotestclassnormalisedtothemostsensitiveorganism(highest
score).
3. Resultsanddiscussion
3.1. Kineticstudies
ExperimentsonTergitolTMat100mg/Lcarriedoutunderdark
(100mg/LofH2O2)provedthattheuseofH2O2appliedalonedid
notallowanyreduction inNP-10concentration(Fig.2a,b).
Pre-liminarymeasurementsofUVabsorbancespectra(200–400nm)
ofuntreatedTergitolTMindicatedtwodistinctabsorbancebands<
300nm:i)apeakat224nmandii)anotherpeakat275nm
charac-teristicofmanyphenoliccompounds(Kimetal.,2005),evidencing
thatTergitolTM absorbslightintheUV C region.Thephotolysis
of100mg/Lof TergitolTM resultedin 20%and30%removal
effi-ciencyafter80mininHCandVC,respectively(Fig.2a,b).InKarci
etal.(2013),theUV Cphotolysisof100mg/LNP-10wasevaluated
ina3250mL-capacity,horizontallypositionedandbatch-operated
cylindricalphotoreactorwiththeUV Clightsource(40Wlamp,
1.4×10−5 EinsteinL−1 s−1at253.7nm)locatedinthecenterof
thephotoreactorina quartzsleeve.Accordingtotheirresultsa
removalrateof92%wasobtainedafter120min,evidencingthat
theefficiencywasstronglyaffectedbylamppower,geometryand
reactiontime.
Chen etal. (2007)evaluated thephotolysis of200mg/L
NP-10usinga125Whigh-pressuremercurylampwiththeprimary
wavelength of 365nm; an absorbance peak at 270nm
corre-sponding to the broken benzene ring was observed after 6h
irradiation.
H2O2/UV-CprocessresultedinaTergitolTMremovalof87,90
and 99%in VCconfiguration after80mintreatment, whereas a
removalof79,87and95%wasachievedinHCconfigurationafter
thesametreatmenttime,with10,20and100mg/LofH2O2,
respec-tively.
The rather poor NP-10 removal kinetics (k
NP-10=0.046±0.0007min−1)andefficienciesobtainedviaphotolyisis
concentra-Fig.2.KineticcurvesofTergitolTM(initialconcentration100mg/L)underdifferent processes:a)verticalconfiguration;b)horizontalconfiguration.
Table1
Kineticconstants±standarddeviationsforTergitolTMdegradationbyH
2O2/UV-Cin VCandHCconfigurations,respectively.
H2O2dose(mg/L) kVC(min−1) kHC(min−1)
10 0.024±0.002 0.024±0.003
20 0.051±0.003 0.030±0.003
100 0.150±0.007 0.074±0.008
tioninaccordancewiththefindingsofKarcietal.(2013)which
reportedthat thehighest NP-10removal ratecoefficient(k
NP-10=0.59±0.030min−1)wasachievedwithH2O2/UV-Cprocessat
aH2O2concentrationof340mgL−1
AsshowninTable1,TergitolTMabatementratesincreasedupon
increasingtheinitialH2O2 concentrationsfrom10 to100mg/L,
showingkineticconstantshigherinVCcomparedtoHC,except
ataninitialoxidantconcentrationof20mg/L.Thepositiveeffect
ofincreasingH2O2concentrationshasalreadybeenevidencedin
formerrelatedstudies(Arslan-Alaton,2010)andwasattributedto
theenhancedHO•production.
Inthepresentstudyafter20minofphotoxidationwith100mg/L
ofH2O2theremovalof100mg/LNP-10inVCandHCsetupreactor
was89%and82%,respectively.
3.2. Intereferingcompounds
Under the operating conditions described above (100mg/L
TergitolTMand100mg/LH
2O2),noneoftheintereferingsubstances
Fig.3.Effectsof:a)phatlatesandb)nitrateonphotoxidationrateofTergitolTMin VCreactor,overthetime.
(NaCl, Na2CO3, KH2PO4, Na2SO4) showeda significanteffect at
theinvestigatedconcentrations,butphthalatesandonlypartially
nitrate.Asmatteroffact,17%ofremovalofTergitolTMwasachieved
after80minofphotoxidationinpresenceof852mg/Lofphthalate
(Fig.3a).
The irradiation of nitrate-rich water leads to nitrite
forma-tionwithareactionquantumyielddependentontheexcitation
wavelength,temperature,pHandnitrateconcentration(Mackand
Bolton,1999).Photolysisofnitrateandnitriteresultsinthe
forma-tionofreactivespeciessuchasthe·OHradicalbutalsoNO·,NO2·,
ONOO·.AsshowninFig.3b,theremovalkineticsslightlyimproved
byincreasingthenitrateconcentration.
ItispossiblyduetotheOHradicalproductionfromtheNO3−
absorptionofUVaccordingtothefollowingreaction:
NO−3+h+H+→·NO2+·OH
Assumingthatthemolarratiobetweennitrateandhydroxyl
radicalswas1:6.6and1:0.65for50mg/Land500mg/Lofnitrate
respectively,itcanbestatedthatinthefirstcasethereisaslight
scanvengereffectofnitrate,whereasinthesecondonethereis
acontributionofradicalnitritetotheoxidationreactionatshort
time.
Unlikeofourresults,thepresenceofnitrate(5mg/L)affected
removal of bisphenol A (BPA) in previous experiments with
UV/H2O2(Parketal.,2014).However,itworthtonoticethatthe
Fig.4.a)Comparisonbetweenphotoxidationremovalof100mg/LTergitolTMfrom DWandWWinVCandHCreactoratthedifferentvaluesofH2O2concentrations; b)comparisonbetweenphotoxidationkineticcurvesof100mg/LofTergitolTMfrom DWandWW,inVCreactor.DashedlinesarethecurvefitforDWsampleswhereas dotlinesarethecurvefitofWWsamples.
1:23and1:46correspondingto150mg/land300mg/lofhydrogen
peroxiderespectively.
3.3. Realwastewater
Accordingtotheresultsachieved withdeionized water,the
removalofTergitolTMinVCreactorwashighercomparedtoHC
reactorinrealwastewaterforalltheH2O2concentrations(Fig.4a).
Therefore,thekineticstudyfortheevaluationoftheinfluenceof
thewatermatrixwascarriedonlyinVC.Asexpectedthe
kinet-ics contant in DW (0.0184±0.0013min−1, 0.024±0.004min−1,
0.072±0.004min−1 for 10, 20 and 100mgL−1 of H2O2
respec-tively) were higher than in WW (0.0096±0.0003min−1,
0.0156±0.0011min−1, 0.045±0.002min−1 for 10, 20 and
100mgL−1ofH2O2respectively).ByincreasingtheH2O2
concen-tration from10 to 100mg/L, after 80min of photoxidationthe
TergitolTMremovalwasabout76.97%,85.76%,99.69%and53.43%,
71.31%, 97.28% in DWand WW, respectively. After50min,the
treatmentwith100mg/lofH2O2carriedoutinDWachievedabout
97% ofTergitolTM removal,30minmore of photoxidationwere
requiredtoachievethesamevalueofTergitolTMremovalinWW.
Fig.5. Toxicity(asTU50)ofTergitolTMsolutions(100mg/L)treatedwithUV-C (VC)atthreeincreasingconcentrationsofH2O2(NP-10=0mg/L;C-10=10mg/L; C-20=20mg/L;andC-100=100mg/L)assessedconsideringA=A.fischeri,B=R. sub-capitata,andC=D.magna;datawithdifferentletters(a–b)aresignificantlydifferent (Tukey’s,p<0.05).
3.4. Ecotoxicologytests
3.4.1. Deionizedwater-basedsolutions
ToxicitydataonDW-basedsolutionsspikedwith100mg/Lof
NP-10andafter80minofphotoxidationtreatmentwithUV-C(VC)
atincreasingH2O2concentrations(NP-10=0mg/L;C-10=10mg/L;
C-20=20mg/L;andC-100=100mg/L)weresummarizedinFig.5
(A–C).Resultsshowedspecies-specificeffectswithincreasinglevel
oftoxicitydisplayedbyR.subcapitata<A.fischeri<D.magna.
Bac-teria(Fig.5A)didnotshowanysignificanttoxicityremovalafter
C-20andC-100,andaslighttoxicityincreaseafterC-10.Microalgae
(Fig.5B)presentedrelativelylowtoxicityeffectswithasignificant
reductionoftoxicityfrom31%(TergitolTM)to1%(C-10),while
toxi-cityincreasedinC-20(8%)andC-100(39%).InthecaseofD.magna
(Fig.5C),thetoxicitywassignificantlyhighercomparedtoFig.5A
andB,especiallyafterC-100treatment.Nosignificantreduction
oftoxicitywasdetectedafterTergitolTMtreatment,nevertheless
itwassignificantlyremoved(>90%).AccordingtoLofranoetal.
(2016a,b)andPersooneetal.(2003),toxicitydatawereintegrated.
Samplesweredeemedaspresentingbetween“slightacute
toxi-city”and“acutetoxicity”withahazardclassificationscoreof1.3
Fig.6.Toxicityeffects(as%ofeffect)ofwastewatersamplesspikedwith100mg/L ofNP-10andtreatedwithUV-CatthreeincreasingconcentrationsofH2O2 (C-10=10mg/L;C-20=20mg/L;andC-100=100mg/L)assessedconsideringA=A. fischeri,B=R.subcapitata,andC=D.magna;datawithdifferentletters(a–b)are significantlydifferent(Tukey’s,p<0.05).
Resultsstatedthat TergitolTM mineralizationwasnot complete,
andby-productscanstillexertanadverseeffectontarget
biolog-icalmodels.Similarly,itwasobservedinKarcietal.(2013)were
acutetheH2O2/UV-Cprocessultimatelyresultedinahigheracute
inhibitoryeffect(27%inhibition)thantheoriginalNP-10solution.
3.4.2. Wastewaterbasedexperiments
ToxicitydataonrealWWspikedwith100mg/LofTergitolTMand
after80minofphotoxidationtreatmentUV-C(atincreasingH2O2
concentrations (NP-10=0mg/L; C-10=10mg/L; C-20=20mg/L;
andC-100=100mg/L)inVCreactor,after80min,were
summa-rizedinFig.6(A–C)expressedaspercentageofeffect.Thetoxicity
ofwastewaterperse,beforespiking,induceda12%,10%and15%
effectinA.fischeri,R.subcapitataandD.magna,respectively.These
backgrounddatawereusedtonormalizethevaluesreportedin
Fig.6(A–C).AfterthephotoxidationtreatmentinpresenceofH2O2
increasingconcentrations,toxicityvalueswereonlyslightlyhigher
thaninDW(Fig.5)forA.fischeri(Fig.6A)andR.subcapitata(Fig.6B),
whiletoxicityinD.magna(Fig.6C)wasreducedespeciallyfor
C-10andC20,whileresidualtoxicitycanbedetectedforC-100(i.e.
thetoxicityinFig.6wasexpressedas%ofeffectandnotasTU50
likeinFig.5).Inallcases,thebestperformancewasobtainedwith
10mg/LofH2O2.AccordingtoLofranoetal.(2016a,Lofranoetal.,
2016bandPersooneetal.(2003),toxicity datawereintegrated.
Samplesweredeemedaspresentingbetween“acutetoxicity”and
“highacutetoxicity”withahazardclassificationscoreof2.7(2(A.
fischeri)+3(R.subcapitata)+3(D.magna)]/3(D.magna)).
4. Conclusions
Promisingremovalefficiency(upto99%)wasobservedafter
UV-C/H2O2 processconsideringtheverticalconfigurationofthe
reactorafter80minofreactiontimeofTergitolTM spiked
deion-izedwater.Similarly,inTergitolTMspikedwastewaters,theremoval
efficiencywasupto96%afterUV-C/H2O2processconsideringthe
verticalconfigurationofthereactorafter80min.InbothTergitolTM
spikeddeionizedwaterandrealwastewater,theefficiencyof
post-treatmenttoxicityreduction/removalremainedpoor,mainlydue
toreactionby-productsevidencingmedium-highlevelsofresidual
toxicity.Thus,furtherresearchisneededtooptimizethetreatment
processschemetoimprovethefinalecotoxicologicalqualityofthe
effluent.
Thecharacterizationofthedegradationproductscouldhelpto
theestimationoftheircontributiontotheoveralltoxicity.Ifthe
degradationproductsofTergitolwouldbebiodegradables,a
subse-quentbiologicaltreatmentstepcouldbeintegratedfortheremoval
of organicmatterand residualtoxicity after80min-H2O2/UV-C
treatment.
References
Abbas,W.,Bokhari,T.H.,Bhatti,I.A.,Iqbal,M.,2015.Degradationstudyofdisperse redF3BSbygammaradiation/H2O2.AsianJ.Chem.27(1),282.
APHA,2012.In:Rice,E.W.,Baird,R.B.,Eaton,A.D.,Clesceri,L.S.(Eds.),Water Envi-ronmentFederation,StandardMethods,2012.,editors.AmericanPublicHealth Association,AmericanWaterWorksAssociation.
Arslan-Alaton,I.,Akin,A.,Olmez-Hanci,T.,2010.Anoptimizationandmodeling approachforH2O2/UV-Coxidationofacommercialnon-ionictextilesurfactant
usingcentralcompositedesign.J.Chem.Technol.Biotechnol.85,493–501. Brix,R.,Postigo,C.,González,S.,Villagrasa,M.,Navarro,A.,Kuster,M.,deAlda,
M.J.,Barceló,D.,2010.Analysisandoccurrenceofalkylphenoliccompoundsand estrogensinaEuropeanriverbasinandanevaluationoftheirimportanceas prioritypollutants.Anal.Bioanal.Chem.396(3),1301–1309.
CEPA—CanadaEnvironmantalProtectionAct,1999.PrioritySubstancesList Assess-mentReport-NonylphenolandItsEthoxylates.EnvironmentCanada,Health Canada.
Chen,C.Y.,Wen,T.Y.,Wang,G.S.,Cheng,H.W.,Lin,Y.H.,Lien,G.W.,2007. Determin-ingestrogenicsteroidsinTaipeiwatersandremovalindrinkingwatertreatment usinghigh-flowsolid-phaseextractionandliquidchromatography/tandem massspectrometry.Sci.TotalEnviron.378(3),352–365.
Chokwe,T.B.,Okonkwo,J.O.,Sibali,L.L.,2017.Distribution,exposurepathways, sourcesandtoxicityofnonylphenolandnonylphenolethoxylatesinthe envi-ronment.WaterSa43,529–542.
Ciabatti,I.,Cesaro,F.,Faralli,L.,Fatarella,E.,Tognotti,F.,2009.Demonstrationofa treatmentsystemforpurificationandreuseoflaundrywastewater.Desalination 245,451–459.
daSilva,S.W.,Klauck,C.R.,Siqueira,M.A.,Bernardes,A.M.,2015.Degradationof thecommercialsurfactantnonylphenolethoxylatebyadvancedoxidation pro-cesses.J.Hazard.Mater.282,241–248.
DIRECTIVE2003/53/ECOFTHEEUROPEANPARLIAMENTANDOFTHECOUNCILof 18June2003amendingforthe26thtimeCouncilDirective76/769/EECrelating torestrictionsonthemarketinganduseofcertaindangeroussubstancesand preparations(nonylphenol,nonylphenolethoxylateandcement).
Fan,J.,Yang,W.B.,Li,A.M.,2011.Adsorptionofphenol,bisphenolAand nonylphe-nolethoxylatesontohypercrosslinkedandaminatedadsorbents.React.Funct. Polym.71,994–1000.
Hatchard,C.G.,Parker,C.A.,1956.Anewsensitivechemicalactinometer-II. Potas-siumferrioxalateasastandardchemicalactinometer.Proc.R.Soc.Lond.A235 (1203),518–536.
Karci,A.,Arslan-Alaton,I.,Bekbolet,M.,2013.Oxidationofnonylphenolethoxylates inaqueoussolutionbyUV-Cphotolysis,H2O2/UV-C,Fentonandphoto-Fenton
processes:aretheseprocessestoxicologicallysafe?WaterSci.Technol.68(8), 1801.
processesforantibioticremoval:areview.Curr.Org.Chem.21,1–14. Mack,J.,Bolton,J.R.,1999.Photochemistryofnitriteandnitrateinaqueoussolution:
areview.J.Photochem.Photobiol.A:Chem.128(1-3),1–13.
Mcleese,D.W.,Zitko,V.,Sergeant,D.B.,Burridge,L.,Metcalf,C.D.,1981.Lethalityand accumulationofalkylphenolsinaquaticfauna.Chemosphere10,723–730. Olmez-Hanci,I.,Arslan-Alaton,B.,2013.GencBisphenolAtreatmentbythehot
persulfateprocess:oxidationproductsandacutetoxicity.J.Hazard.Mater.263, 283–290.
Park,C.G.,Choi,E.S.,Jeon,H.W.,Lee,J.H.,Sung,B.W.,Cho,Y.H.,Ko,K.B.,2014.Effectof nitrateonthedegradationofbisphenolAbyUV/H2O2andozone/H2O2oxidation
inaqueoussolution.Desalin.WaterTreat.52(4-6),797–804.
Solé,M.,Castillo,M.J.L.D.,Porte,M.C.,Pedersen,K.L.,Barceló,D.,2000.Estro-genicity determinationinsewagetreatmentplantsandsurfacewatersfromthe Catalo-nianArea(NESpain).Environ.Sci.Technol.34,5076–5083.
UKEnvironmentAgency,2013.NonylphenolEthoxylates(NPE)inImportedTextiles. ReportVersion1.
Zhou,R.,Zhang,W.,2017.Treatmentofthehighconcentrationnonylphenol ethoxy-lates(NPEOs)wastewaterbyFentonoxidationprocess.Am.J.Analyt.Chem.8 (01),72.