HAL Id: hal-00835632
https://hal.archives-ouvertes.fr/hal-00835632
Submitted on 19 Jun 2013
HAL is a multi-disciplinary open access
archive for the deposit and dissemination of
sci-entific research documents, whether they are
pub-lished or not. The documents may come from
teaching and research institutions in France or
abroad, or from public or private research centers.
L’archive ouverte pluridisciplinaire HAL, est
destinée au dépôt et à la diffusion de documents
scientifiques de niveau recherche, publiés ou non,
émanant des établissements d’enseignement et de
recherche français ou étrangers, des laboratoires
publics ou privés.
Preparation of aqueous dispersion of thermoplastic
sizing agent for carbon fiber by emulsion/solvent
evaporation
Isabelle Giraud, Sophie Franceschi-Messant, Emile Perez, Colette Lacabanne,
Eric Dantras
To cite this version:
Isabelle Giraud, Sophie Franceschi-Messant, Emile Perez, Colette Lacabanne, Eric Dantras.
Prepara-tion of aqueous dispersion of thermoplastic sizing agent for carbon fiber by emulsion/solvent
evapo-ration. Applied Surface Science, Elsevier, 2013, vol. 266, pp. 94-99. �10.1016/j.apsusc.2012.11.098�.
�hal-00835632�
Any correspondence concerning this service should be sent to the repository administrator:
staff-oatao@inp-toulouse.fr
DOI:10.1016/j.apsusc.2012.11.098
Official URL:
http://dx.doi.org/10.1016/j.apsusc.2012.11.098
This is an author-deposited version published in:
http://oatao.univ-toulouse.fr/
Eprints ID: 8782
To cite this version:
Giraud, Isabelle and Franceschi-Messant, Sophie and Perez, Emile and
Lacabanne, Colette and Dantras, Eric Preparation of aqueous dispersion of
thermoplastic sizing agent for carbon fiber by emulsion/solvent evaporation.
(2013) Applied Surface Science, vol. 266 . pp. 94-99. ISSN 0169-4332
O
pen
A
rchive
T
oulouse
A
rchive
O
uverte (
OATAO
)
OATAO is an open access repository that collects the work of Toulouse researchers and
makes it freely available over the web where possible.
Preparation
of
aqueous
dispersion
of
thermoplastic
sizing
agent
for
carbon
fiber
by
emulsion/solvent
evaporation
Isabelle
Giraud
a,
Sophie
Franceschi-Messant
a,
Emile
Perez
a,∗,
Colette
Lacabanne
b,
Eric
Dantras
b aLaboratoiredesI.M.R.C.P.,UMR5623CNRS,UniversitéPaulSabatier,31062ToulouseCedex09,FrancebLaboratoiredePhysiquedesPolymères,CIRIMAT,InstitutCARNOT,UniversitéPaulSabatier,31062ToulouseCedex09,France
Keywords: Sizing Carbonfibers Composites Thermoplasticpolymer Aqueousdispersion Emulsion/solventevaporation
a
b
s
t
r
a
c
t
Inthiswork,differentsizingagentaqueousdispersionsbasedonpolyetherimide(PEI)wereelaboratedin ordertoimprovetheinterfacebetweencarbonfibersandathermoplasticmatrix(PEEK).Thedispersions wereobtainedbytheemulsion/solventevaporationtechnique.Tooptimizethestabilityandthefilm formationonthefibers,twosurfactantsweretestedatdifferentconcentrations,withdifferent concen-trationsofPEI.Thedispersionsobtainedwerecharacterizedbydynamiclightscattering(DLS)andthe stabilityevaluatedbyanalyticalcentrifugation(LUMiFuge).Theselecteddispersionsweretestedforfilm formationabilitybyscanningelectronmicroscopy(SEM),andthesizingperformancewasassessedby observationofthefiber/matrixinterfacebySEM.TheresultsrevealedthatanaqueousdispersionofPEI, stabilizedbysodiumdodecylsulfateasthesurfactant,ledtoverystablesizingagentaqueousdispersion withidealfilmformationandbetterinterfaceadhesion.
1. Introduction
Carbonfiberiswidelyusedasareinforcingmaterialin com-posites,especiallyinadvancedcomposites[1,2].Ascarbonfibers arebrittle,manyproblems,suchasfilamentbreakageandfluffing, ariseduetomechanicalfrictionduringthemanufacturingprocess
[3–5].Therefore,carbonfibersaregenerallysizedorcoatedbya sizinglayeronthesurface,whichisusuallyobtainedfroma solu-tionoremulsionconsistingofpolymericcomponents[6,7].Sizing easesfiberhandlingandcanalsoprovideacouplingagentforthe fiber/matrixbond [8–11]. Thenatureof thesizingis oftenkept secretbymanufacturersofcarbonfibers.However,sizingischosen accordingtothenatureofthematrixandisgenerallyapre-polymer orpolymer.Mostofthecompositesaremadefromepoxyresin,and sizingagentsareoftenofthesamenature[5,12–14].Thisisa prob-lemwhenthematrixisahigh-temperaturethermoplasticpolymer sincethedegradationtemperatureofthistypeofsizingisaround 250◦C [15]. For polyimides, PEEK and other high-temperature
thermoplastic polymers,thefunctional groups provided bythe traditionalepoxy-compatiblesizingdonotreactchemicallywith thesepolymersandweakinterfacialshearstrengthsresult[16]. Moreover,forcompositesmoldedwithpolyimidesorPEEK,high processingtemperaturesduringmanufactureandcontinuoususe
∗ Correspondingauthor.
E-mailaddress:perez@chimie.ups-tlse.fr(E.Perez).
inhigh-temperatureenvironmentsdegradetheepoxysizingand, consequently,weakenthefiber/matrixinterface,producingvoids anddelaminations[17–19].Alloftheseobservationsunderlinethe importanceofhavingsizingthatissuitableforhigh-temperature thermoplasticmatrices.Fromapracticalpointofview,thesizing formulationshouldbeeasytouse,non-toxicandenvironmentally friendly.Inthispaper,wereportthefirstexampleofpreparation anaqueousdispersionofathermoplasticsizingagentforcarbon fiberbyemulsion/solventevaporation.
2. Experimental 2.1. Materials
ThepolyetherimidePEI(Ultem1000)wasobtainedfromSabic®.
Thesodiumdodecylsulfate(SDS)andthechloroformwere pro-videdbySigma–Aldrich,thebenzalkoniumchloride(BC)wasfrom Fluka (C12 60%, C14 40%). The AS4 carbon fiber tow, provided
byHexcel,wastreatedunsizedandcontained12,000fibers.The polyetheretherketone(PEEK)providedbyVictrexwasa 100mm thickfilm.TheremoldingagentwasCIREX041WBfromSICOMIN. 2.2. PreparationofPEIdispersionsbyemulsion/evaporation
In order to reduce thetoxicity and to respect the environ-ment,organicsolventsmustbeavoidedinthefinalsizingagent formulation.Forthesereasons,wedecidedtoelaborateaqueous
Fig.1.Schematicrepresentationofthepharmaceuticalemulsification/evaporationprocess.
dispersions.Thesecanbemadebyavarietyofmethods[20–23]
leading,attheend,tostablehydrophobicparticlesinwater.The preparationprocessdescribedherewaslargelyinspiredby emul-sion/solventevaporation,anencapsulationtechniqueusedinthe pharmaceuticalindustrytoprepareaqueousdispersionsof poly-mernanoparticlesormicrospheres.
Emulsion/solvent evaporation involves a two-step process (Fig.1):theemulsificationofa polymersolutioncontainingthe encapsulatedsubstance,followedbyparticlehardeningthrough solventevaporationandpolymerprecipitation.Duringthewater emulsification, the polymer in solution in the volatile, water-immisciblesolventisbrokenintomicrodropletsbytheshearstress producedbyeitherahomogenizerorasonicatorinthepresenceof asurface-activeagentuntilthepolymerprecipitates[24–27].
Thismethodwasusedtoprepareastableaqueousdispersionof PEIasthesizingagent.Weusedtwodifferentsurfactants,sodium dodecylsulfate(SDS)andbenzalkoniumchloride(BC)atdifferent concentrations(0.3%,0.5%and1wt%).Thefinalconcentrationsof PEIwere0.1%,0.3%,0.5%and1wt%.ThePEIdispersionat0.5wt%ina 0.5wt%surfactantsolutionwaspreparedasfollows.Ina5-mLflask, 0.1005gofPEIwasdissolvedin2mLofchloroform.Thissolution waspouredintoanotherflaskcontaining20mLofthesurfactant solution.Themixturewasemulsifiedbyultrasoundshearing(Vibra Cell,BioblockScientific600W,20Hz).Theshearinglasted5minat power4.Awaterbathwasusedtomaintainthesolutionatroom temperature.Then,magneticstirringoftheemulsionat1200rpm for12hallowedtotalevaporationofthechloroform.
2.3. CharacterizationofPEIdispersions 2.3.1. Particlesizeanalysis
Dynamiclightscattering(DLS)wasperformedusingaMalvern InstrumentsNanoZSwithaHe–Nelaser(633nm)atascattering angleof173◦andat25±1◦C.Thehydrodynamicmeandiameterof
thenanoparticleswasdeterminedusingthesoftwareprovidedby MalvernInstruments.TheContinmodelwasappliedtoobtainsize data.Alltheauto-correlationfunctionfitswerecheckedandfound tobeinaccordancewiththeexperimentaldata.Fivemeasurements weremadeoneachsamplewithanaccuracyofabout2nm. 2.3.2. Evaluationofstabilityusinganalyticalcentrifugation
Aseparationanalyzer(LUMiFuge,L.U.M.Berlin,Germany)was usedtodeterminetheseparationbehaviorofdispersionsunderthe influenceofvariouscentrifugalforces(5–1000×g).Thisapparatus isbasedona low-speedcentrifugecombinedwithan optoelec-tronicmeasuringsystemthatrecordsthelighttransmissionover theentire sample cuvette (Fig. 2). The cuvettes containingthe
suspensionare positioned in thehorizontal planeon therotor ofthecentrifuge.Duringcentrifugationalightsourcepositioned abovetherotoremitsradiation(near-infrared)ontothesample. TransmittedlightisdetectedbyaCCDlinesensorbelowtherotor planeandisanalyzedbyamicrocontroller,whichgeneratesa light-transmissionprofileof thesampleareafor everymeasurement step.
This technique is very appropriate for the study and opti-mizationofverystableaqueousdispersions.Thecentrifugalforce acceleratesthedestabilizationofthedispersionandrapidly deter-minestheshelflifeofthedispersion[28].Moreover,thepossibility ofstudying8samplesatthesametimeenablesdifferent formu-lationstobecomparedimmediately[29,30].Thedispersionsare naturallystableover6monthssowechosetosimulate3yearsof aging.Thedataacquisitioncorrespondedto255profilesrecorded everyeverysecondsat4000rpm.Thetemperaturewas20◦C.
2.4. Sizingtreatmentofcarbonfiberandcompositepreparation 2.4.1. Sizingofcarbonfiber
Differentmethodscanbeusedtosizecarbonfibers,such as electrodeposition[31,32]orelectropolymerization[33,34],butthe mostcommonisbathcoating.Wetestedthesizingatlaboratory scaleso,inthiscase,themostsuitabletechniquewastospraythe dispersiondirectlyontothefibersurface.Anunsizedfibertowwas strainedbyaweighttokeepitvertical,allowinguniformspraying ofthesizingatthefibersurface(Fig.3).Aftersizing,thefiberswere driedatroomtemperature.
Fig.3. Schematicrepresentationofthesizingprocess.
2.4.2. Compositepreparation
WealsopreparedPEEK/unidirectionalcarbonfibersamplesat laboratoryscale.Thesampleswerepreparedbyhotpress mold-ing.ThepressusedwasaCarver4128CEequippedwithheating plates.Theprocessingtookplaceinseveralsteps.Thesamplewas firstprepared,thenmoldedinthehotpressandfinallycooledand remolded.Inordertokeepallthecarbonfibersinthesame direc-tionduringthedifferentsteps,thestrandsofcarbonfiberwere insertedinafoldedPEEKfilm(Fig.4).
The sample was then placed in an aluminum mold previ-ouslycoatedwiththeremoldingagent.Thenthemoldwasplaced betweenthetwoplates,previouslyheatedto400◦C,andkeptin
contactfor15mintoallowthePEEKtomeltuniformly.6MPaof pressurewasthenappliedfor30stoletthePEEKimpregnatethe fibers.Finally,thesamplewasaircooledandremoldedatroom temperature.Thefinalsamplecontained30wt%ofcarbonfibers. 2.5. CharacterizationofPEIfilmsandcomposite
2.5.1. Scanningelectronmicroscopy(SEM)analysis
Thedifferentsampleswereexaminedusingascanningelectron microscope(JEOLJSM6700F)withanacceleratingvoltageof5kV. Thefilmsobtainedafternaturaldryingatroomtemperaturewere mountedonaluminumstubsand sputtercoatedwithgold.The compositeswerefreezefracturedinordertoobservetherupture faces.
3. Resultsanddiscussion 3.1. Sizingagentformulation 3.1.1. Stabilitystudy
We selected PEIas thesizing agent becauseit is a thermo-plastic polymer with high heat resistance [35], miscible with polyetheretherketone(PEEK)[36],andsolubleinchlorinated sol-ventslikechloroform.Severalfactorsinfluencethestabilityofthe dispersion,suchasthenatureandtheamountofsurfactant. Usu-ally,thechoiceofsurfactantdependsonthenatureoftheparticles and,in particular,theirsurface charge.SincePEIhasnospecial charge,thesurfactantcanbeanionicorcationic.Itisalsoimportant
Fig.4. Schemeofthesamplepreparation.
Fig.5.Influenceofthenatureandconcentrationofthesurfactantonthemean particlediameter([PEI]=0.5wt%).
todeterminetherightquantityofsurfactanttomaintainastable dispersion.PEIconcentrationisalsoanimportantparameter.The emulsion/evaporationmethodisnotsuitableforthepreparation ofconcentrateddispersionsbut,inthecaseofsizing,thisisnota limitationbecausetheconcentrationofpolymerdoesnotexceed 1wt%[37,38].
First,westudiedtheinfluenceofthenatureandthe concentra-tionofthesurfactant,andalsotheinfluenceofthePEIconcentration onthecharacteristicsofthesizingdispersions.
Thefirstparametertobeconsideredwastheparticlesizeas itiswellknownthatthesmallertheparticlesare,themore sta-blethedispersionwillbe.Dynamiclightscatteringmeasurements (DLS)wereperformedonallthedispersions.Theinfluenceofthe surfactantonthemeandiameterofparticlescanbeseeninFig.5.
Themeandiametersoftheparticleswerelessthan100nmand favored stabledispersions.The natureofthesurfactantdidnot haveasignificanteffectontheparticlesizeeventhoughthe par-ticlesseemedsmallerwiththeBCsurfactant.Ontheotherhand, thediametersvariednoticeablywiththesurfactantconcentration. Thehighertheconcentrationwas,thesmallerweretheparticles. Atlowconcentration,therewasnotenoughsurfactantto main-tainsmalldropletsofchloroformandthisdeterminedthefinalsize oftheparticles.Althoughthesmallestparticleswereobtainedfor 1wt%,theconcentrationof0.5%waspreferredinordertominimize theamountofsurfactantinthefinalformulation.
Thesamestudywasperformedtoobservetheinfluenceofthe PEIconcentration(Fig.6).Theparticlesizeincreasedquitelinearly withtheconcentrationforbothsurfactantsbutthemean diam-eterremainedunder 100nm.This resultwasrelated toseveral factors.Thefirstwastheratiobetweentheconcentrationof surfac-tantandtheamountofchloroformphasecontainingthedissolved PEI[23].Thesecondwastheviscosityoftheorganicphase[23].
Fig.7.EffectofthePEIconcentrationontheclarificationkineticsfordispersionsat0.3%BC.
IncreasingthePEIconcentrationinchloroformincreasedthe vis-cosityofthesolution.Giventhattheshearforceswerealwaysthe same,whentheconcentrationofPEIwastoohigh,therewasnot sufficientenoughavailabletocreatesmalldropletsofchloroform. Theparticlesizeforthelowestconcentrationswasverysmall, lead-ing,inprinciple, tothemoststable dispersions.However,for a sizingformulation,thedispersionsmusthaveaminimumof0.5% or1wt%ofPEI.
An interesting stability analysis consisted in determining a destabilization velocity by accelerating the gravitation by cen-trifugation. This kind of analysis could be performed withthe “LUMiFuge”apparatus.Thistechniqueissuitabletooptimizevery stabledispersions(stableformorethan6months).
Fromtheprofiles,anintegraltransmissionwascalculatedasa functionoftime.Forinstance,theinfluenceofthePEIconcentration onthestabilitycanbehighlightedimmediately(Fig.7).
Fromthisgraph,aclarificationvelocity,correspondingtothe slopeofthefirstlinearpartofthecurves,wascalculatedbythe “SEPView”software.Thesteepertheslope,themoreunstablethe dispersion.Theclarificationvelocitywascalculatedforthedifferent dispersionsandcomparedsoastohighlighttheeffectofdifferent parameters.
AsshowninFig.8,thenatureofthesurfactantdidnothavea significantinfluenceonthevelocity,exceptfor0.1wt%PEIsolution, whereBCwaslessefficient.Consideringthesurfactant concentra-tion,itseemsthat,from0.5wt%,thestabilityreachesaplateau.This resultindicatesthatitisnotnecessarytousemorethan0.5wt% surfactantsolutionstoincreasethestability.
As expected, the PEI concentration had a major impact on thedispersionstability (Fig.9).Theclarificationvelocitytripled between0.5%and1wt%.Althoughtheshelflifecannotbe deter-mineddirectly from theclarification velocity, the real stability
Fig.8. Influenceofthenatureandconcentrationofthesurfactantontheclarification velocity([PEI]=0.5wt%).
periodextrapolatedfromthedatawasestimatedtobearound6 monthsforthe1%PEIdispersion.
Consideringtheaboveresults,boththetestedsurfactantswere usable.However,benzalkoniumchloridemightbemoreinteresting becauseofitsantimicrobialandlowfoamingproperties. Concern-ingthedifferentconcentrations,agoodcompromiseseemstobe 0.5wt%ofsurfactantand0.5wt%ofPEI.
3.1.2. Filmformation
Forsizing,thecoating,andconsequentlytheformationofafilm, isaveryimportantproperty.Alltheaqueousdispersionsprepared wereabletoformfilmsafterwaterevaporation.Toensurethe qual-ityofthefilm,twochosendispersionswereobservedbySEM.One wasmadewithSDSandtheotherwithBC,andbothcontained 0.5wt%ofsurfactantand0.5wt%ofPEI.
ThesurfaceaspectofthePEIfilmobtainedwithSDSwasvery homogeneous(Fig.10).Thecrackswereduetouncontrolled evapo-ration.Thisparameterwillneedtobetakenintoaccountforfurther applications.Themagnificationofthisfilmshowspartiallyfused PEIparticles(Fig.11).Thisobservationistypicaloflatexfilm for-mation,andisidealforahomogeneouscoating.
ThePEIfilmformedbytheBCdispersionwasverydifferent.
Fig.12isanSEMobservationofthisfilmshowingaheterogeneous surface.Themagnificationshowsthat,infact,theparticlesformed agglomeratesbutdidnotfuse(Fig.13).Thedifferenceinfilm forma-tioncouldbeexplainedbytheabilityofthesurfactanttobedrained outoftheevaporatingfilm[39–41].Wehavetoconsiderthe affin-ityofthesurfactantwiththesurfaceofthePEIparticlestoexplain thisbehavior.Itseemsthat,comparedtoBC,SDShasalower affin-itywiththesurfaceoftheparticlesandismainlydrainedoutofthe film,leadingtothefusionoftheunprotectedparticlesandfinally toahomogeneousfilm.
Fig.9. InfluenceofthePEIconcentrationontheclarificationvelocity ([surfac-tant]=0.5wt%).
Fig.10.SEMobservationofthefilmfromtheSDSdispersion.
Fig.11.MagnificationofFig.10.
Fig.12.SEMobservationofthefilmfromtheBCdispersion.
Fig.13.MagnificationofFig.12.
Consideringthesefilmformationresults,thebestdispersions forasizingapplicationseemtobethoseobtainedwithSDSasthe surfactant.Itisveryimportanttoobtainahomogeneouscoatingon thecarbonfibers.
3.2. Sizingevaluation
Theaimofthisstudywastoelaborateastableaqueous disper-sionusableasathermoplasticsizingformulationforcarbonfibers. Thesizing hasvariousroles,suchasfacilitating thehandlingof fibersandimprovingtheinteractionsbetweenthematrixandthe fibers.
Toevaluatetheeffectofthisnewsizing,PEEK/carbonfiber com-positesweremade;onewithunsizedcarbonfibersandanother withPEIsizedcarbonfibers.Thechosensizingwastheaqueous dispersionwith0.5wt%ofPEIand0.5wt%ofSDS.Thebestwayto highlighttheinfluenceofthesizingwastoobservethefiber/matrix interface.Forthatpurpose,thecompositeswerefreezefractured transversallyandobservedbyscanningelectronmicroscopy.
Fig.14correspondstoanunsizedcarbonfibercompositeand,as wecansee,therearevoidsandnointeractionsbetweenthePEEK matrixandthecarbonfibers.Incontrast,theinterfacebetweenthe
Fig.15. PEIsizedcarbonfibercomposite.
compositeandthePEIsizedcarbonfibersiscontinuous(Fig.15). Inthiscase,thereisarealbondbetweenthePEEKandthecarbon fibers.Theseobservationsconfirmnotonlythatthesizingremains duringthecompositeprocessingbutalsothatthematrixandthe carbonfibersareconnectedbythesizingagent.
4. Conclusions
Theanalysesperformedonthedifferentaqueousdispersions revealedthatthequantityofparticleswasasignificantfactorfor stability.TheparticlesizeincreasedgreatlywiththePEI concentra-tion,whichtendedtodecreasethestabilityofthedispersion.The LUMiFugestudyconfirmedthisresult.ThebestPEIconcentration obtainable bytheemulsion/evaporation technique was0.5wt%. Thedispersions werestable1 yearat 0.5wt%,nevertheless the dispersionat1wt%remainedstablefor3months.Concerningthe natureofthesurfactant,benzalkoniumandSDSallowedstable dis-persionstobeobtained.Nevertheless,thebenzalkoniumdispersion didnotformahomogeneousfilmandsowasnotsuitablefor a sizingapplication.Incontrast,withSDSdispersion,thefilmwas reallyuniformandweobservedacoalescencephenomenon typi-caloflatexfilmformation.Theconcentrationofthesurfactantalso hadaninfluenceontheparticlesizeandstability,and0.3%wasnot enoughtoobtainagooddispersion.Thegaininstabilityobtained at1%didnotjustifytheuseofsuchaconcentrationconsidering thattherewasonly0.5wt%ofPEI.Sothebestconcentrationof surfactantwas0.5wt%.
Consideringalltheresults,thechosendispersionforsizingwas 0.5%PEIand0.5%SDS.Theefficiencyofthisnewsizingagent aque-ousdispersionwasappreciatedthroughSEMobservations,which showedacontinuousinterfacebetweenthecarbonfibersandthe PEEKmatrix.
Acknowledgements
WethankMrJ.M.Bergerat,AIRBUSIndustry,ToulouseFrance, for useful discussions and advice. The financial support of FUI INMAT2andAIRBUSisgratefullyacknowledged.WealsothankMr D.KemmishandMrA.WoodfromVictrexInc.,fortheirinsightful commentsandfruitfuldiscussions.
References
[1] P.Morgan,CarbonFibersandTheirComposites,CRCPressTaylor&Francis Group,NewYork,2005.
[2] D.D.L.Chung,CarbonFiberComposites,Butterworth-Heinemann,Newton, 1994.
[3] B.Fernandez,A.Arbelaiz,A.Valea,F.Mujika,I.Mondragon,PolymerComposites 25(2004)319–330.
[4]W.Chen,Y.Yu,P.Li,C.Wang,T.Zhou,X.Yang,CompositesScienceand Tech-nology67(2007)2261–2270.
[5] A.Paipetis,C.Galiotis,CompositesPartA:AppliedScienceandManufacturing 27(1996)755–767.
[6] N.Dilsiz,J.P.Wightman,Carbon37(1999)1105–1114. [7] R.B.Guan,Y.G.Yang,J.T.Zheng,Fibercomposites1(2002)23. [8] T.Q.Li,M.Q.Zhang,H.M.Zeng,Polymer40(1999)4307–4313.
[9] S.-L.Gao,J.-K.Kim,CompositesPartA:AppliedScienceandManufacturing32 (2001)775–785.
[10]L.T.Drzal,M.J.Rich,M.F.Koenig,P.F.Lloyd,TheJournalofAdhesion16(1983) 133–152.
[11]Z.Dai,F.Shi,B.Zhang,M.Li,Z.Zhang,AppliedSurfaceScience257(2011) 6980–6985.
[12] Z.Dai,B.Zhang,F.Shi,M.Li,Z.Zhang,Y.GU,AppliedSurfaceScience257(2011) 8457–8461.
[13]P.Ren,G.Liang,Z.Zhang,PolymerComposites27(2006)591–598.
[14]V.S.Mironov,M.Park,J.Kim,S.H.Lim,C.R.Choe,JournalofMaterialsScience Letters20(2001),1211–1211.
[15]A.Bledzki,E.Fabrycy,A.Kwasek,JournalofThermalAnalysisandCalorimetry 29(1984)989–994.
[16]D.M.Blackketter,D.Upadhyaya,T.R.King,J.A.King,PolymerComposites14 (1993)430–436.
[17]T.K. O’Brien, Journal of Reinforced Plastics and Composites 7 (1988) 341–359.
[18]P.Davies,W.J.Cantwell,H.H.Kausch,JournalofMaterialsScienceLetters9 (1990)1349–1350.
[19]A.Todoroki,H.Kobayashi,CompositesScience andTechnology52(1994) 551–559.
[20]S.Freitas,H.P.Merkle,B.Gander,JournalofControlledRelease102(2005) 313–332.
[21]C.Zhang,G.Zhang,V.Ji,H.Liao,S.Costil,C.Coddet,ProgressinOrganicCoatings 66(2009)248–253.
[22]P.R.Nepal,M.-K.Chun,H.-K.Choi,InternationalJournalofPharmaceutics341 (2007)85–90.
[23] M.Li,O.Rouaud,D.Poncelet,InternationalJournalofPharmaceutics363(2008) 26–39.
[24]T.R.Tice,R.M.Gilley,JournalofControlledRelease2(1985)343–352. [25] K.S.Soppimath,T.M.Aminabhavi,A.R.Kulkarni,W.E.Rudzinski,Journalof
Con-trolledRelease70(2001)1–20.
[26]S. Freiberg, X.X. Zhu,International Journal of Pharmaceutics 282 (2004) 1–18.
[27] Z.ElBahri,J.-L.Taverdet,JournalofAppliedPolymerScience103 (2007) 2742–2751.
[28]M.Kuentz,D.Röthlisberger,EuropeanJournalofPharmaceuticsand Biophar-maceutics56(2003)355–361.
[29] T.Sobische,H.Heb,H.Niebelschütz,U.Schmidt,ColloidsandSurfacesA: PhysicochemicalandEngineeringAspects162(2000)1–14.
[30]T.Sobische,D.Lerche,ColloidsandSurfacesA:Physicochemicaland Engineer-ingAspects331(2008).
[31]A.Bismarck,A.F.Lee,A.S.Sarac,E.Schulz,K.Wilson,CompositesScienceand Technology65(2005)1564–1573.
[32]A.S.Sarac,E.A.Parlak,E.Sernath,T.Cakir,JournalofAppliedPolymerScience 104(2007)238–246.
[33] B.Lin,R.Sureshkumar,J.L.Kardos,ChemicalEngineeringScience56(2001) 6563–6575.
[34]C.Dalmolin,S.C.Canobre,S.R.Biaggio,R.C.Rocha-Filho,N.Bocchi,Journalof ElectroanalyticalChemistry578(2005)9–15.
[35]R.Torrecillas,A.Baudry,J.Dufray,B.Mortaigne,PolymerDegradationand Sta-bility54(1996)267–274.
[36]G.Crevecoeur,G.Groeninckx,Macromolecules24(1991)1190–1195. [37]R.L.Zhang,Y.D.Huang,L.Liu,Y.R.Tang,D.Su,L.W.Xu,AppliedSurfaceScience
257(2011)3519–3523.
[38]D.D.L. Chung,CarbonFiberComposites,Butterworth-Heinemann,Newton, 1994,pp.91–93.
[39]E.Kientz,Y.Holl,ColloidsandSurfacesA:PhysicochemicalandEngineering Aspects78(1993)255–270.
[40] J.Mallégol,J.-P.Gorce,O.Dupont,C.Jeynes,P.J.McDonald,J.L.Keddie,Langmuir 18(2002)4478–4487.
[41]A.Tzitzinou,P.M.Jenneson,A.S.Clough,J.L.Keddie,J.R.Lu,P.Zhdan,K.E. Treacher,R.Satguru,ProgressinOrganicCoatings35(1999)89–99.