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Publisher’s version / Version de l'éditeur:

Macromolecules, 23, 1, pp. 338-345, 1990-01-01

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Spherulitic growth rates and coalescence phenomena in

polypropylene/polyethylene-based ionomer blends

Caldas, V.; Brown, G. Ronald; Willis, J. M.

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1990, 23,

Spherulitic Growth

Rates

and

Coalescence

Phenomena

in

Polypropylene/Polyethylene-Based Ionomer

Blends

V. Caldas and G.R.

Brown*

Department ofChemistry,Polymer McGill,McGill University,801 SherbrookeStreet West, Montreal, Quebec,CanadaH3A-2K6

J, M. Willis

Industrial Materials ResearchInstitute, NationalResearch Council ofCanada, Boucherville, Quebec, CanadaJ4B-6Y4. ReceivedDecember19,1988;

RevisedManuscriptReceivedMay23, 1989

ABSTRACT: Theisothermalradialgrowth ratesofspherulitesofpolypropyleneinblendswithan essen-tiallynoncrystallizable ionomer havebeendetermined by photomicroscopy. Blendscontaining 5and 10

wt % ionomer, crystallizedfromthe melt,havea grainyappearance duetoionomerentrapmentandshow

an increasednucleationdensityas compared topure polypropylene. At large supercooling,theseblends

also show depressedradialgrowth rates, whichare attributedtoa significant dissipation ofenergy by the

crystallizingfrontto affect the rejectionoftheionomer domains. Upon repeatedcrystallization ofagiven

sample,an increasein theradialgrowth ratewith melt timeisobservedinitiallygiving rise toa maximum,

withgeneral behaviorthatisdependent upon the blendcomposition and thecrystallizationtemperature. Beyondthis maximum thespherulitic growth rate decreasesuponfurther crystallization. Theobserved effectson thespherulitic radialgrowth rateswithrespect to repeatedcrystallization are attributedtothe

coalescenceofthe ionomer dispersedphase. Thisisconsistentwith aconcomitantincreaseintheaverage

domainsize.

Introduction

The blending ofpolymerstoproduce alloyswith prop-ertiesselected for given applicationsis an area of poly-mer sciencethatispresentlyreceivinggreatattention.1"3 Blending is not only economically viable but is also a

versatile wayofmakingnew materialshavingawide range

ofproperties.

For polymerblendsin whichone ofthe componentsis

crystallizable, thepresenceofthe secondcomponentcan strongly affect the crystallizationprocess. Both the

crys-tallizationkineticsandthe finalcrystal morphologycan

beverydifferentfromthat ofthepurecrystallizing

com-ponent. As reviewedrecently by Martuscelli,4such changes have been found not onlyin blendsofcompatible

poly-mers butalsoinblendsofimmiscibleor partially misci-ble polymers.

Inarecentstudy, Willisetal.5demonstrated the

abil-ity

ofapolyethylene-based ionomer toenhancethe

com-patibility

of polyolefin/polyamideblends. The

morphol-ogyoftheternary polyolefin /ionomer /polyamideblends

was significantly dependent upon ionomer concentra-tion. Infact, for fixedprocessingconditions, the size of thedispersedphasewas reducedbyasmuchasfour times

dueto theadditionofaslittleas0.5% ionomer byweight.

From the physicochemicalstudiesofthebinary blend of

the ionomerwith polyamide,6specific interactions in the form of hydrogen bonding between the blend compo-nentswere demonstrated. Suchinteractionswere absent in the polypropylene or polyethylene/ionomer blends. Moreover, the ionomerseverely impedesthe

crystalliza-tion ofthepolyamidebutenhancesthenucleationofthe

polyolefins,particularly in thecase of polypropylene. Thepresentinvestigationconcerns the effectofa

poly-ethylene-based ionomeron theradialgrowth ratesof

spher-ulitesofpolypropylene. In the lastfew years many

stu-dies7"14 have been done on the effect ofelastomers on

the crystallization kinetics ofpolypropylene. However,

*Authorto whom correspondence shouldbeaddressed.

0024-9297/90/2223-0338$02.50/0

to theknowledgeofthe authors, thereare no reportsof

studies ofthe effect ofan essentially noncrystallizable ionomer on the radial growth rates of spherulites of a crystallizable polymer.

The main goal of this work is to study the effect of

composition,crystallization temperature,and melt resi-dencetimeon the spherulitic growthratesof

polypropy-lene in binary polypropylene/ionomer blends. A study

ofthecrystallizationofblendscan ultimatelyyield

infor-mationconcerning the interactionsatthe interface between

the polymers in the blend. The effectofcrystallization

on the rate ofcoalescenceofdispersedionomerphaseis alsoconsidered. Thus, theresults presentedin thispaper

willcontribute to the understandingoftheeffectiveness

of the ionomer at enhancing the

compatibility

of

polyolefin/polyamideblends.

Experimental

Section

Materials. The polymers used were polypropylene

(Pro-Fax6501)originallyobtainedinpowderform from Himontand

Surlyn9020from DuPont. The polypropylene (PP) resinwith 0.1% of Irganox 1076 antioxidant was subsequently

com-pounded with a Werner and Pfleiderer (ZSK30) twin-screw

extruderand converted toapelletform. The ionomeric resin

(Du Pont, Surlyn 9020) is a randomterpolymerconsisting of approximately80% ofpolyethylene, 10% of methacrylicacid, approximately70% neutralized withzinc, and10% of isobutyl acrylate. Somepropertiesoftheseresinsare giveninTable I. Priorto blending, the resinswere dried undervacuum at95°C for 24h.

Preparation of the Polypropylene/Ionomer Blends. Blends having 5%, 10%, 20%, and50% byweightofionomer

were prepared according to thefollowingprocedure: The

res-inswere meltblendedina Brabender chamber,initiallysetat 250°C, usingrollerbladesthatare recommendedforhighshear applications. The resinswere allowed to mixat 50rpm under

a constant nitrogenflowfor5min. Themeltwas thenrapidly

transferredtoa mold and placedinahydraulicpressunder2.5

MPa ofpressureuntilthe samplecooledtoroom temperature.

Theresultantmolded sampleswere cutinto specimenshaving dimensionsofroughly1 X0.5X0.5cm. Thin films(5-10Mm)

©1990American Chemical Society

(3)

Macromolecules, Vol. 23, No. 1, 1990 Polypropylene/Polyethylene-Based Ionomer Blends 339 0.40

I

o at o 0.35 0.30

TIMEINTHE MELT (min)

Figure 1. Reproducibility oftheradialgrowth ratesfor

poly-propylene at 124 °C.

TableI

GeneralProperties of PolypropyleneandSurlyn

meltindex, density, torque(250°C), melting

resin g/10 min g/mL N/m point,°C

PP 4.0 0.905 8.6 165

Surlyn 1.0 0.965 14.3 62

were then cut fromthese specimensusingaReichert Jung

Super-cut2050microtome.

Isothermal CrystallizationProcedure. ALeitz Wetzlar optical polarizing microscope fitted with a MettlerFP52 hot

stage was used to observe isothermal crystallization at 100x

magnification. The hotstagecouldbeheldataconstant tem-perature to ±0.3 °C byaMettlerFP5temperature control unit. For the microscope study, microtomedfilmswere placed on amicroscope slideglassand meltedon ahotplate while

apply-ing pressureon the cover glass. The thicknessofthemelted

filmwas fixedbya 12-#mialuminumspacerbetween thecover

glassand the microscope slide. Filmthicknessofthe orderof

12-15 nm were obtained andused in the microscope study. The followingprocedurewas usedto view isothermal crys-tallization: Thesampleswere meltedon thehotstageat200°C for 10minto remove crystallinity. Different distributions of

spheruliteswere observedinsuccessivecrystallizations, indicat-ingthat the melt residencetime as well as melt temperature was sufficientto remove residualcrystallinity. Thehot stage

was thensettoan intermediatetemperatureof135°C, and the samplewas allowed tocome totemperatureequilibrium,which

took approximately2min. Whentemperatureequilibriumwas

achieved, the hot-stagecontrolwas settothe desired crystalli-zation temperature, andequilibriumwas achievedrapidly(<30 s). Photomicrographswere takenofthe growing spherulites at

appropriate timeintervals, depending on the rateof crystalli-zation.

Radial GrowthRateMeasurements. The isothermalradial growthrates,G= dr/dt(r= radiusofthe

spherulites, t= time),

were determined by measuring the sizesofthe spherulitesas seen in the photomicrographsas afunction oftime. Theradii

ofthesespheruliteswere measuredwithasemiautomatic

digi-tizer, describedelsewhere.15

The radius ofeach spherulite was taken as the average of 15-20 individual radii. From the average radii, plotted as a

function of time, theradial growth rateofthespherulitewas

determinedastheslopeoftheresultingstraightline. Foreach composition andcrystallizationtemperature, theaverageradial growth rate was determined from at leastfour radial growth rate measurements. The experimental error in these growth

rates was determinedto be lessthan 5%.

Results and Discussion

Crystallization

of Polypropylene. When polypro-pylene is crystallized from themelt in the temperature

rangeof118-126 °C,the predominant spherulitic

appear-ance observedmicroscopically istype I, as classified by

Padden and Keith.16 The various results presented in

this investigation will mainly concern this morphology.

CRYSTALLIZATIONTEMPERATURE(°C)

Figure2. Radial growth rate dependenceofpolypropylene and the 50% PP/50% ionomer blend on crystallization

tempera-ture,for amelt time of10min.

Asecondtypeofspheruliticappearance(type

III),

intro-duced later in the paper, is shown tobehave somewhat

differentlyfrom thefirst.

Intheregionof15-60 ^m, theradii ofthe

polypropy-lene spherulites crystallized from the melt increase

lin-earlywithtime. To verify the reproducibilityoftheradial growthrates,a sample ofpolypropylene was repeatedly

melted, for 10 min, and crystallized. As shown in Fig-ure 1, at 124 °C theradial growth rates fluctuate about 0.335/um/s andare withinapproximately±0.02^m/sof

eachother.

Thedependence ofthe radial growth rateof

polypro-pylenespheruliteson the crystallization temperatureshown

in Figure2 is inaccordance with that predicted by the

Fischer-Turnbullequation17

G =

G0expj-A£D*/kT]

expj-A$*//jTj

(1)

where, the term exp(-AED*/kT\isreferredtoasthe

trans-portterm andexp{-A$*/&Tj, as the nucleation term, G isthe growthrate ofpolymers, Gais the preexponential

term, AEB* is the free energy of activation for move-ment across theembryo-meltinterface, A$* is the min-imumfree energyrequiredfortheformationofanucleus

of criticalsize, k isthe Boltzmann constant,andTisthe crystallization temperature. For crystallizationabovethe

optimum crystallization temperature, the growth rate is

controlled by the nucleation process so that the activa-tionfree energy isnegative and theexpectedinverse depen-dence ofthe radial growth rate on the temperature is observed.

Crystallization

of

Polypropylene/Ionomer

Blends.The effectofcomposition on theradial growth

rates of the polypropylene spherulites obtained for the blendsthathave beenheldinthemelt at200 °Cfor 10

minisshowninFigure3. Asmall depressionofthegrowth rate is seen at low ionomer content and low

tempera-tures. Athighertemperatures,consequently much slower

crystallization, the growth rate is essentially

indepen-dentoftheionomerconcentration.

As shownin Figure 2,theradial growthratesobtained

for the polypropylene (PP) spherulites in the50% PP/ 50% ionomer blend are identical, within experimental

error, to those obtained for pure polypropylene. This

generalpatternhasalso been observed byMartuscelliet

al.14,18 forthe spherulitic growthofpolypropylene with ethylene/propylene/diene terpolymer (EPDM).

How-ever,the growthratesofisotacticpolypropylene inblends

with othertypes ofrubbersshoweda significant

depen-denceon compositionandcrystallizationtemperature,18 whichwas attributed to partial miscibility.

(4)

23, ° 118"C • 120*C i °_ • 0 10 10 20 30 40 50 50 PERCENT IONOMER

Figure3. Composition andcrystallizationtemperature

depen-denceoftheradial growthratesin polypropylene/ionomerblends.

It hasbeendemonstrated thatthepresenceof foreign

inclusionsinthemelt,asin thecase ofimmiscibleblends, can disturb the crystallizingfront.4,14,18 Ifthereare

inter-facial interactions between the blend components, the growing crystal front must do work against the

dis-persedphasein the melt. Inthecase ofaone-phasemelt, some energyisrequired to effect the rejection ofthe sec-ond component from the crystallizing polymer. In the

case ofa two-phase melt,where thesecond component

hastaken theform of droplikedomains, energymustalso bedissipated for therejection, engulfment,and/or defor-mationofthe secondcomponent.

These energy dissipations constitute energy barriers

which influence the growth rateofthe spherulites in the

melt. Bartczak,Galeski, andMartuscelli19 modified the

classical Fischer-Turnbull equation to account for the

energy dissipations which result during the

crystalliza-tion of a polymer in the presence ofnoncrystallizable, sphericaldomains. The modified equation is

G =

G0exp|-AED*/kT) exp{-A$*/fcT) X

expHEj

+E2 + E3+ E4+ E5)/kT) (2) whereE1 istheenergydissipated by the crystal to effect the rejection ofthe second component into interlamel-larregions,E2 istheenergydissipated by thespherulite

front to effect the rejection ofdroplike domains inthe

melt,E3 is the kineticenergy required to overcome the

inertia of the drops, £4 is the energy required to form

new interfaces between the spherulite and drop when

engulfmentoccurs, and£5istheenergydissipatedwhen the engulfed dropsare deformed by thecrystallizing front. The equationsthatdescribethe growth rate, takinginto

account these energy dissipations, derived byBartczak

et al.,19are summarized inTable II.

The crystallization of polymer blends whose compo-nents havephaseseparatedinthe meltisinfluencedboth

by thesizeofthe dispersed phase and theinterfacial

ener-gies. The drivingforcefor therejection,engulfment,and/ or deformationprocessesliesin thedifferenceofthe

inter-facial free energy betweenthe crystallizingfrontand

inclu-sions, 7„s, and the interfacial free energy between the meltana inclusions, 7pl:20-22

AE=

7ps

-TPi (3)

ForAF< 0,the dispersed domainsinthemeltare more

likelyto beengulfed than rejected by the growingfront.

However, when AE > 0, the situation is more

compli-cated. At slowrates of crystallization, the domains are

TableII

Growth RateExpressions for Spherulites in an

IncompatiblePolymer-PolymerSystem

description expression11 rejection ofthe ^ G1 G: dispersedphase G= i+EJRT,~

3p^y^R'

1+ 2Pmr*RTc

engulfment ofthe G= Gj exp{E3/i?Tc|

dispersedphase = Gjexp|-(3c^mAF/(pmrRTc)j deformationofthe G= Gtexp\EJRTc\ dispersed phase = G[ exp{-C/(*)(3cMm7pa/(p„rRTc)\ a

Gj istheundisturbed growthrate;pmisthemolecularweight

ofthe repetitive unit;c isthevolumeconcentrationof the second

componentinthe blend;ymisthe viscosity ofthematrix; R'isthe

temporary radius ofthespherulite;pmisthedensity of the matrix;

ristheradiusoftheionomer domains; U(k)isadeformation

func-tion;R isthegas constant; and Tc isthecrystallization tempera-ture.

pushed alongby the growingfront,while at higherrates

theyare simplyengulfed.

At

some intermediaterate,the domains maybepushedfor shortdistances before being engulfedby the crystallizing front. Engulfment occurs

whentheviscoushindrancecausedby the motion ofthe

domainsoverwhelmsthe forcesofrepulsion. This implies

a critical rate at which the pushing of the domains no

longeroccurs and engulfment takes precedence. Using

these arguments,foragiven AE,there must beacritical

domainsizesuchthat, ataconstant growth rate,domains

ofthis size or larger are simply engulfed and no longer

pushedby the growingfront. Engulfmentoccurs above

thiscriticalsize because the hydrodynamicforceis

pro-portionalto the domain size while the repulsive forces

are determined by factorssuchas the shapeofthe

inter-facebehindtheparticle.19 Thecriticalsizeitselfis

depen-denton thesystem, i.e., on the interfacial energies,

vis-cosities, and heatconductivities.

In this study, only marginal differences in the radial growthrates of polypropylene spherulites resulted from

theadditionofionomer. This is asexpected for immis-cible blendswithminimal interfacialinteractions. Indeed, the freeze-fractured surfaceofacompression-molded sam-pleof80%PP/20%.ionomer blend(Figure4),asobserved

by scanning electron microscopy,6 showsthe ionomeric

phaseas sphericaldomains embeddedin the

polypropy-lene matrix with very little adhesion between the two phases. Onthis basis,it isunlikely thatthereis

signifi-cant adhesion between the phases in the melt, indicat-ing that AEis approximately equal to zero or positive.

Thus, the relative extent of rejectionandengulfment of

the ionomer domainswill be determined by the rate of crystallization andthe sizeofthedispersedphase.

At lowionomerconcentrationsandlowcrystallization temperatures, significant energy dissipation must be involvedinrejectionofthedomainsasthe spherulitegrows. This energy loss retardsthe radial growthofthe spher-ulites, as seen in Figure 3. Therefore, the radial growth rate is depressed as compared to that ofpure

polypro-pylene.

The binaryblends alsoconsistentlyshowagreater

pri-mary nucleation density than pure polypropylene at all compositions andcrystallization temperatures(Figure5).

(5)

poly-Macromolecules, Vol. 23, No. 1, 1990 Polypropylene/Polyethylene-Based Ionomer Blends 341

Figure 4. SEM photomicrographofthe freeze-fractured

sur-face of the compression-molded sample ofthe 80% PP/20% ionomerblend6as obtained from the Brabendermixing cham-ber, The ionomericphaseisseen asthe spherical entities.

40

min

50

min

60

min

70

min

Figure6. Photomicrographsillustratingthecoalescenceof the ionomer domainsas aresultofrepeatedmelting(10-min period)

and crystallization for the 95% PP/5% ionomer blend, at a

crystallizationtemperatureof124°C.

Figure5. Nucleation density, after10min melttime,as a

func-tion ofthe percent ionomer in the blend,atdifferent crystalli-zation temperatures.

propylene spherulites,as suggestedpreviouslyby Willis

et al.6 based on DSC observations. This effect is most pronounced for the 95% PP/5% ionomer blend,

possi-bly reflecting thesmallerionomerdomain size and con-comitantly larger surface area available for nucleation.

Asimilarsynergistic effect uponnucleationwas observed

by Martuscelliet al.18for

iPP/PIB

blends. The effect,

as wellasthe observed reductioninthegrowthrate,was attributedto thepreferentialdissolutionofimperfect

crys-tals (molecular fractionation). It is possible that these processesare alsoresponsibleforthe observations shown

in Figure5 for the polypropylene/ionomerblends.

Effect of Coalescence on the Growth Rate. The overall morphology of the blends containing 5% iono-mer,as viewedwithoutcross polarizers atatemperature of124 °C, is illustrated in Figure6. It shows the

pres-ence ofthe ionomer phase as approximately spherical

domains embeddedinthepolypropylenespherulites. Ini-tially, a linear increase in the average domain size with

melting timeisobserved,forthosedomainsof sufficient

sizeto bedetected microscopically,withachangeinslope

at approximately45 min as seen in Figure 7. By

com-parison,forthe50% PP/50% ionomer blend, the domains

are much larger andasimplelinearincreaseinthe

aver-agesizewith melting timeisobserved,as seen in Figure

8. It should be noted that, in the 50% PP/50%

iono-Figure 7. Increase in the size ofthe ionomer domains with repeated melting (10-min period) and crystallization, for the 95% PP/5% ionomer blend, at a crystallization temperature

of124°C. Thetimeindicatesthe cumulativemelttime.

Figure 8. Increase in thesize of the ionomer domains with repeated melting (10-min period) and crystallization, for the 50% PP/50% ionomer blend,ata crystallizationtemperature

of124 °C.

mer blend, the measured diametershaveextended beyond the thicknessofthefilm. Thus, the domainsare no longer sphericalas inthe 95% PP/5% ionomerblend buthave

takentheform ofdisks. If volumes,rather than diame-ters, are plotted as a function of melt time, calculated forspheresin Figure7 and disksin Figure8, then

iden-tical trends are observed. The important point is that

thesizeincreaseswithmelt time,regardlessoftheshape

(6)

DOMAIN SIZE (pm)

Figure 9. Ionomer domainsize distribution inthe 95% PP/

5%ionomer blend and 80% PP/20% ionomerblend obtained fromcryogenicallyfracturedsurfaces.

is much greater for thisblend than for that containing

5% ionomer.

The increase in ionomer domainsize could be due to either or both oftwo factors, namely, phase separation during the time spent in the melt and/or rejection (or

pushingofthe domains)duringrepeatedcrystallization.

AsshowninFigure7,for the95%PP/5% ionomerblend, the average size of the ionomer domains increases

rap-idly until thefourthcrystallization. Uponfurther

crys-tallization,therate ofincreasein theaveragesizeofthe

domains isdiminished. Thissuggeststhat,at the point

wherethechange in slope occurs,thereis adepletion in

thenumberofdomainsofradiuslessthan acriticalsize.

Ionomerdomainsofradiuslessthan the criticalsize are

beingrejected bythe crystallizing

front

andas a conse-quence are coalescing. Therefore, coalescencenot only isoccurring while thepolypropyleneisin the meltphase

butalsoisinducedbycrystallization. Inthecase ofthe

50% PP/50% ionomer blend, wheredomains are larger than thecritical size,coalescence occurs predominantly

in the melt. This was confirmed by separate

experi-ments that showed increases in domain size with melt

time when the crystallization steps were omitted, also shown in Figure8 (filledsquare).

The

initial

size distribution in the ionomer phase in theblendswas determined from cryogenically fractured

surfacesobserved using scanning electron microscopy and isshowninFigure9.6 Thesizedistributions afterrepeated

crystallizations at124°C as determinedusing

photomi-croscopyare shownin Figure 10. Thesharpdrop-offin thenumberofdomainsforthefirst crystallization

(Fig-ure 10) probably reflectslimitations in detection at the magnificationlevelused. It isevidentthat

initially

it is

predominantly the smaller domains(lessthan1pm)that are beingrejectedby the crystallizingfrontand

coalesc-ing into the larger ones. In the case of the 50% PP/ 50% ionomer blend (Figure 8), the size ofthe domains iswell abovethat critical size. Even though some iono-mer maybepresentwithin interlamellarregions, which may give rise to some rejection, domain size increase is

occurringpredominantly as a resultofcoalescence dur-ing the timethat the polypropyleneis in the melt.

As mentioned before, it is predicted that the radial growthrates of spherulites in phase-separated polymer

blendscan beinfluenced by thesizeofthe dispersed

par-ticles. Estimateswere madeoftheeffectofdomainsize

on energy terms Ely Z?3, and E4, using the equations of

Bartczakand co-workers19 shownin TableII, forthePP/ ionomerblends. Theresults, assuming AF= 1

erg/cm2

and

7^

= 1

erg/cm2,forthe95% PP/5% ionomerblend

at aspheruliticradialsizeof30 pm anda growthrate of

Macromolecules, 23,

Figure 10. Ionomer domainsizedistributionin the95% PP/ 5% ionomer blend attotal melttimesof(a) 20min, (b)40min,

(c) 50min, and (d)80minandacrystallizationtemperatureof

124 °C. The melt times correspondto repeated melting and crystallizationat 10-minintervals.

0 2 4 6 8 10

RADIUS (pm)

Figure 11. Estimated energies ofrejection, engulfment, and deformationforthe 95% PP/5% ionomerblendas a function

ofionomer domainsizeatacrystallizationtemperatureof118 °C.

0.92pm/s,are shownin Figure 11for the crystallization

temperatureof118°C. Itshouldbenotedthatthe inter-facialfree energieswere choseninaccordancewithresults

previouslyreported for polypropylene/polyethylene23 at

140°C. The viscosityofthe blend at the crystallization

temperaturewas estimatedfrommeasuredviscositiesat higher temperatures (~200°C)24andlowshearrate (17 s-1) assuming Newtonianflow andusing the conceptof

activation energyfrom the Arrhenius equation. These

equationspredict that, at small domainsize,theenergy

of rejectionhasa considerable influenceon the

spheru-litic

growth rate. Theenergies due to deformation and occlusion make much smallercontributions to thetotal

energydissipation. Increasing the interfacialfree energy betweenthe polymersinthe blendhasthe effectof

increas-ing the energy of deformation and engulfment.

How-ever, for reasonable changes (AFand7p8 from0.1 to 10

erg/cm2), these energies remain much smallerthan the

energyofrejection. As the ionomerdomainsize increases,

thetotal ofthese energiesdecreasesin magnitudeuntil,

for domain size greater than4 pm, they are essentially negligible.

Theinclusionofthese energy terms ineq2allowsthe predictionofthegrowth rate atacertainionomerdomain

size. As shown in Figure 12for the crystallization

tem-perature of118°C,an increaseintheradial growthrate

(7)

Macromolecules, Vol. 23, No. 1,1990

RADIUS(Atm)

Figure 12. Theoretical growthrate dependenceon the

iono-mer domainsizeasestimatedforthe95%PP/5%ionomer blend ata crystallization temperature of118°C.

Figure13. Growthrate dependenceof the95% PP/5%

ion-omer blendwithrepeatedmelting(10-min period) and crystal-lization atvariouscrystallizationtemperatures.

sizeleading toward thegrowth rateofthe pure polymer

at the same temperature. Abovea certain domain size (4 Mm), where theenergy ofrejectionis essentially

neg-ligible, the growth rateofthe crystallizing polymerisno

longer affected by the presence of the second

compo-nent.

The effect of domain size on the growth rate ofthe

polypropylene spherulites can be observed

experimen-tallywhen blends containing5% and 10% ionomer are repeatedly meltedfor10minandcrystallized. Asshown

inFigures13and14, an initialincreasein the radial growth

rate is observed,followed bya decrease when the

sam-ple has been crystallized several times. This gives rise toa maximum growthrate whichisdependentupon the blend composition and the crystallization temperature.

It isinterestingto notethatif themaximumradial growth

rates, ratherthan the values for 10 min, are plotted in Figure3,the growthratesare essentiallyindependentof ionomer concentration at all temperatures. When the

50% PP/50% ionomer blend is repeatedly crystallized,

Polypropylene/Polyethylene-Based Ionomer Blends 343

TIME IN THE MELT (min)

Figure14. Growthrate dependenceofthe 90%PP/10%

ion-omer blendwithrepeatedmelting(10-min period) and crystal-lizationat variouscrystallizationtemperatures.

Figure15. Growthrate dependenceofthe 50% PP/50%

ion-omer blendwithrepeatedmelting(10-min period) and

crystal-lizationata crystallization temperature of124°C.

onlyadecrease in the radial growth rate is observed,as

shownin Figure 15.

The

initial

increaseinthe growth rate (Figures13and 14) ismainlyduetothe rejectionofthe smaller ionomer domains(lessthan thecriticalsize)into interspherulitic regions. Since thesizeofthe domains in the95%

PP/

5% ionomerblendis

initially

muchsmallerthanthat of

the90%PP/10% ionomer blendasdemonstratedin

Fig-ure 9, the growing front requires more energy to effect

theirrejection. Consequently, the initial growth rate is reduced by a greater extent than in the 90% PP/10%

ionomer blend.

Through coalescenceduring crystallization and melt-ing, thedomains increase insizesuch thata significant

fraction is above that critical size. During subsequent

crystallization, the growing front dissipatesless energy

in rejecting these domains, due to their largersize, and

a radialgrowth rate increase is observed leadingto the

maximum. As mentioned previously, themaximumgrowth rate corresponds closely to theradial growthrateobtained

for pure polypropylene at the same temperature. Fur-thermore, atatemperatureof124°C, themaximumgrowth

rate for the95% PP/5% ionomer blend occurs at

rela-tivelythesame timeas thechangein slope observedfor the domain size increase with meltingtime (Figure 7).

(8)

Macromolecules, 23,

This strongly supportsthe ideathatrejectionofthe

ion-omer domains affects thecoalescencemechanism,which inturn directlyaffectstheradial growthrateofthe

poly-propylenespherulites.

The speed of the crystallizing front, at any constant small domain size, also influences the perturbation

observed inthe growth rate of the spherulites. At high crystallizationtemperatures, where thegrowthrateis

rel-ativelyslow, lessenergyisdissipated to effectthe

rejec-tionoftheionomer domains. Asaresult, theinitialgrowth

rate is not decreased, with respect to pure

polypropy-lene, tothe extent that it isfor a samplethatis crystal-lized at lower temperatures.

Althoughthe increasesintheradial growthrateswith

melt time, observed at short timesforthesamples con-taining 5% and 10% ionomer, are in accordance with

the equationsderived byBartczak,the maximum inthe

growth rates and subsequent decreases are not consis-tent withthetheoretical predictions. Two explanations

can be offered: (1) Viscosity increases with melt time.

Since the transportterm in the classical Fischer-Turn-bullequationcan bedescribedin terms oftheWLF

equa-tion, increases in viscosity after several crystallizations would be expected to decrease the radial growth rate. However,an increasein viscosity aftercoalescenceof ion-omericdomainsseems rather unlikely. Furthermore,the direct verificationofsuchan effectisverydifficult,since

it requiresameasurement oftheviscosity ofthe matrix

polymer in the blend, andthis is not a trivial task. (2)

Limited miscibility oflowmolecular weight fractions of

ionomer inthe polypropylene wouldseem tooffera

bet-ter explanation. Increasingquantitiesofthisfraction of

ionomerduringrepeatedmelting would result ina

dimin-ished radial growth rate. Oncethe effects ofrejection/

engulfment/deformationbecomenegligible and thegrowth ratehasreacheditsmaximum,thisionomer, presentwithin

thepolypropylene, wouldberesponsiblefor theobserved

hindranceto crystallization. Therefore, throughout the

crystallization study, there is competition between the influencesofphase sizeandtheinfluenceoflimited

sol-ubilityon thegrowthrate. Theprocess isnotofa

sequen-tial nature but a direct competition until such time as

the domainsare large enough thattheyno longerplaya

role in thecrystallizationprocess (Figure 15).

Crystallization

Behavior of the TypeIII

Spheru-lite. The complex crystalline structure of

polypropy-lenemanifestsitself not only at the crystal lattice level

butalso at the level ofthe polarizingmicroscope where

avariety of spherulitetypes havebeenclassified bytheir

appearance incrossed polarizedfields.16

Inthetemperaturerangeof118-126°C,asecond

spher-ulitic morphology, appearing highly luminous amidst darker spherulites,was noted andcan beseen in Figure 16. The grainystructure observedin this photographis due to the ionomer trapped within the polypropylene spherulites. This spheruliticappearance was classified astypeIII byPaddenand Keith.16 It was latershown25"26

thatthis spheruliticmorphology crystallizeswiththe hex-agonal,fJ,crystal structure whilethe predominant form (type I,inthis study) crystallizeswiththemonoclinic, a, structure. It has also been found16,25,27 that once type

III spherulitesnucleate,theirrate ofradial growthis

20-70% fasterthan that oftype I.

During this study,thetype III spheruliteswere found

to behavesimilarlyto thepredominantspherulitic form

with respect to physical interactions with the ionomer domains. In Figure 17, a plot ofthe growth rate as a function oftime in the melt shows a very rapid initial

100 pm

Figure 16. Type III spherulitic morphology (bright) amidst the muchdarker typeIas observedforthe90% PP/10%

ion-omer blend atacrystallizationtemperature of120°C.

Figure 17. Growth rate dependenceofthe typeIII spherulite

withrepeatedmelting (10-min period) andcrystallizationin the 90% PP/10% ionomerblend ata crystallization temperature

of120°C.

radial growthrate increase,followedbyadecreasetoward

longertotalmelttimes. However, whenthis plotis

com-pared tothatoftypeIatthesame compositionand tem-perature (Figure 13), the depression of the growth rate atashort melting time isfoundto bemuch larger. The radial growth rateofthetypeIII spherulitesis30%greater

thanthat ofthe typeI spheruliteat the same

crystalli-zationtemperature(120°C)andisconsistentwith obser-vations previously reported byNortonandKeller.27 There-fore, themore significantdepressionoftheinitial growth

rate is due to the larger quantity ofenergy required to

effectthe rejectionofthe ionomerdomains.

Conclusion

The spherulitic growth of polypropylene in binary

polypropylene/ionomerblends isdisturbed to a certain

extent by the presence of the ionomer component inthe

melt. Infact, for the blendthat contains5% ionomer, a smalldepressionoftheradial growthrate is observedat

a temperature where the crystallization proceeds rap-idly. Thisdepressionis dueto energydissipated by the growingpolypropylenespherulitic front in rejecting the ionomerdomains. The dispersed ionomeris alsofound

to actas a nucleation site forthe polypropylene spheru-lites. Thenucleation effectismore pronounced at lower ionomer contents possibly due to the smaller ionomer domains beingmore efficient nucleationsites due to the

(9)

Macromolecules 1990, 23, 345-348 345 Coalescenceoftheionomer domainsoccurs duringthe

time spent in the viscous melt. However, the coarsen-ing ofthe dispersed ionomer appears to be accelerated when the sample is repeatedly melted and crystallized.

This suggeststhat acrystallization-induced type of

coa-lescence is also occurring. A combination ofthese two effectsresultsinalinearincreaseofthedomainsizewith

time as a sample is repeatedly melted for 10 min and

crystallized. Thiscoalescencephenomenonaswellasthe

“speed”ofthecrystallizingfrontisshowntohavean effect

on the radial growth rate ofthe polypropylene

spheru-lites. A radial growthrate depressionoccurs as the

spher-ulite is rejecting the second component, the effective-ness ofwhichisdependenton the crystallization

temper-ature. Maximum growth ratesare observed atthepoint

wherethe rejectionofthe dispersed domainsisata min-imum or the size ofthe dispersed phase is well above

that criticalsizerequired for rejection. Oncethe domain

size is greater than the critical size, coalescence occurs predominantly in the melt. Afterthis point, the radial growth rate decreases as the ionomer domain size is increased. This radial growth ratedecreasebeyondthat

maximum cannot be explained using the equations for rejection, engulfment, and deformation.

Future workwillinvolvestudiesoftheinfluenceofthe

chemical characteristics ofthe ionomer (such as func-tionalities, neutralization,etc.)on the crystallizationand coalescence phenomenaof

polypropylene/polyethylene-basedionomerblends. Bymodifying thechemical struc-ture ofthe ionomer, the interfacial free energy between

the matrix polymer and the dispersed phase will be changed, which would yieldmore informationaboutthe

importance of interfacial energieson the crystallization kinetics ofan immiscible blend.

Acknowledgment. Wesincerely appreciate the assis-tance ofF. Hamelin preparation oftheblends and Dr.

B. D. Favis,

IMRI,

andProf. A. Eisenberg, Department

ofChemistry,McGillUniversity, forseveralfruitful dis-cussions. Financial support from the Natural Sciences

andEngineeringResearch CouncilofCanada(NSERC)

and the Quebec Government (Fonds FCAR) is

grate-fully

acknowledged.

RegistryNo. Pro-Fax6501, 25085-53-4;Surlyn 9020,61843-71-8.

References and Notes

(1) Utracki, L. A. Polyblends-87\ NRC/IMRI Symposium

Pro-ceedings,1987.

(2) Robeson,L. M. Polym.Eng. Sci. 1984,24, 587.

(3) Shaw,M.T. Polym.Eng. Sci. 1982,22, 115.

(4) Martuscelli,E.Polym.Eng. Sci. 1984,24, 563.

(5) Willis,J.M.;Favis B. D.Polym.Eng. Sci. 1988,28,1416.

(6) Willis,J.M.;Caldas,V.;Favis, B. D.4th Annual Polymer

Pro-cessingSocietyMeeting, Orlando, FL, May 1988,submitted toPolymer.

(7) Martuscelli,E.;Silvestre,C.;Abate,G.Polymer1982,23, 23. (8) Kumbhoni, K. Polym.Prog. 1974,3.

(9) Spenadel,L. J. Appl. Polym.Sci. 1972,16,2375.

(10) Karger-Kocsis, J.; Kallo, A.;Szufner, A.; Bordor,G.; Senyei,

Zs.Polymer1979,20, 37.

(11) Danesi,S.;Porter,R. S.Polymer1978,19,448.

(12) Ermilowa, G. A.; Ragozina, I. A.; Leont'eva, N. M. Plast.

Massy1969, 5, 52.

(13) Friedrich, K.Prog.Colloid Polym.Sci.1949,64, 103. (14) Martuscelli,E.Polym.Eng. Sci. 1984,24, 563.

(15) Favis, B.D.;ChalifouxJ. P.; Van Gheluwe P. Tech.Pap.-Soc.

Plast.Eng. 1987, 33, 1326.

(16) Padden,F. J.;Keith, H.D.J.Appl.Phys. 1959,30, 1479.

(17) Turnbull,D.; Fischer, J.C.J. Chem. Phys. 1949,17,71. (18) Martuscelli, E.; Silvestre, C.;Bianchi, L. Polymer 1983, 24,

1458.

(19) Bartczak, Z.; Galeski, A.; Martuscelli, E. Polym. Eng. Sci.

1984, 24, 1155.

(20) Omenyi,S.N.;Neumann, A. W.;Lespinard,G.M.; Smith,R.

P.J. Appl.Phys. 1981,52, 789.

(21) Smith,R. P.J. Appl.Phys. 1981,52, 796.

(22) Omenyi,S.N.;Neumann, A. W.J. Appl.Phys. 1976,47,3956.

(23) Oda,Y.;Hata T. Prepr. Annu. Meeting HighPolym.Soc.Jpn.

1968,May,267.

(24) Kamal, M.R.;LePoutre,P.PersonalCommunication,

Depart-mentofChemical Engineering,McGillUniversity.

(25) Keith, H. D.;Padden, F.D.;Walter,N. M.; Wyckoff, M.W. J.Appl.Phys. 1959,30, 1485.

(26) Padden,F.D.;Keith,H. D. J.Appl.Phys.1973,44, 1217.

(27) Norton,D. R.;Keller,A.Polymer 1985,26, 704.

Notes

Variable-Temperature

FT-IR Studies of Organic Carbonate

Solutions

J.A.KINGJR.*AND PETERJ. CODELLA

GeneralElectric Corporate Research and Development, P.O. Box8, Schenectady, New York12301.

ReceivedFebruary 15, 1989;

RevisedManuscriptReceivedJune15, 1989

Introduction

Although the intermolecular structure ofamorphous BisphenolApolycarbonate(BPAPC)isill-defined,a

num-berofsmaller, well-characterized BPA-based carbonate

systems have been examined extensively.1 These past effortshave beenoriented towardunderstanding how

vari-ationsinfundamental conformationandstructural

pack-ingat the molecular level are manifested in the

macro-scopicpropertiesofthesematerials. Suchintra-and inter-molecular interactions in BPAPC analogues have been

studied by a variety oftechniques (principally, NMR,

X-ray spectroscopy, and quantum mechanical

calcula-tions). Todate,no experimental workhasbeenreported on BPAPC usinglow-temperature solutionIR methods. Thispaper summarizesour observationsofboth

mono-meric and polycarbonate solutions using

variable-temperature infrared spectral analysis (VT-IR). These

Figure

Figure 1. Reproducibility of the radial growth rates for poly- poly-propylene at 124 °C.
Figure 3. Composition and crystallization temperature depen- depen-dence of the radial growth rates in polypropylene/ionomer blends.
Figure 4. SEM photomicrograph of the freeze-fractured sur- sur-face of the compression-molded sample of the 80% PP/20%
Figure 9. Ionomer domain size distribution in the 95% PP/
+3

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