WILLIS CARL L (US)
MUYLDERMANS XAVIER (CN)
BENING ROBERT C (US)
WILLIS CARL L (US)
MUYLDERMANS XAVIER (CN)
US4232137A | 1980-11-04 | |||
US4427837A | 1984-01-24 | |||
US4614768A | 1986-09-30 | |||
US4717749A | 1988-01-05 | |||
US5057583A | 1991-10-15 | |||
US6806317B2 | 2004-10-19 | |||
US20030065099A1 | 2003-04-03 | |||
US20050197464A1 | 2005-09-08 |
CLAIMS
What ss claimed is; I . λ pfoce&s for the pvspaolkm of block copolymers comprising; a, adding an alphas iky! -vmy!- aromatic BKϊsirøs? to an ioert solvent b adding a polytx^ήzmrm modifier wherek the polymerixaiiou modifier is <fctftyl-ftlhes:, ortho-dimethoxy^bcrsiaic or ch^thssxy-props*^ c. adding an anionic polymertifation kuiurior wlterrirs tUt- suitattor is. n-b-utyi- h^hκ;nu s-hittyRϋltium or i-lmξyi-Uihϊum; d adding mo^vmyl-sxomatie monomer continuously and cop&lymeώing said
2. The process of claim 1 whereu? the moaovm>1--arc5!tUi0c monomer is added
■ς oimsuou&ly aikr αnsssi of inϋisuoB for more than I S minsnes asd. f>reforabiy for X? myites Oϊ more u?s to £-0 mioutes.
2S
.>. '
Hk"
4. ' The pRxxtss of nxiy of claims 1 to 2 wherem the polymerization modi f5sr k diethoxy- propane m an amount from 4K^ ι® 1000 ppm.
5. The process of any of claio^ I b> I wlien-in tk& polymers xaiioo nigdifei- Is ortlio-
Cs, The pmcefts of any of clairas 1 to 5 whemrs the
?. The proces.^ of iϊrsy ofclairns I Io 6 wktrcis) lhe con version of aipluwi&y1-vinyi~ srϊHϊ!Stκ-
S. Tho procttβs of arsy of claims 1 to 7 further comprising addilicssi of a coupling ^gsnt after polymers iat ion of tbe living clastomer fefoεlc to fbαtϊ a coupled block CLφoI>tτs«r ^ " be-reh^ tba s.oup ) ing agent is tetraaietboxy sifee > fetπ^ihoxy ≤slane or ^πstbyi- r.rϊmeϋκ>κy silnnc.
^. I h-e process of any of cJaims I Ks ? furihsr comprising steps sub&e<μseϊH to step fj whiefdB adiliisooal a!pha-a!kyKvbyl-aκ>maύc &πd
10 ,
Tfc proee^s of any ofckdmx ! ιu * •
$ wbsrein tlse alpbs-alkyl-Yiuyl-sromaiic mαnotucr is &!|>ha^rneLhyl-styτen«, the nionov iayl-aκ>πιatic nxjrjomer is st.we.oe ;'ual tbe eosjegatcd ώ '
ene is 1 ,
1 i . The process of any of cbims 1 to 10 funhe? eompnsmg seleedve hydrogenaticm whesoir: ai !eα« 90 mo!% of ihe dosibS^ hotsds in tbe c!astom<τic bi^ck arc hydrogeuaiod and ks& tliarj 10 mo\% of she dob]>le boi-sds in the glassy Nock a ? e bvdropenated
, λ H lock copolymer made by the pκκs@s o£d;«m ! having at least oπ« glus^y block consisting of incm<yvmyl~ aromatic asx!
GO si us gated dieses, whtrem the .
peak molecular weight of die gS&xsy block is frorr? 2,1K)O to 30,000 g/mol, preferably from 5,000 to 30,0OU g/rsesL and the »esk ϊrsokeϊskr weigh! oCtfe dastoroenc block is from 20,000 Lo 300,(K)O g%#l, the amount of the alassv block i% from IVt \Q 40 ^=1% cm the basiβ of the iot&l block copϋivmer m^δs arui she glass tr;u^tio« tesφeJSiwt,; of lhs glassy bkxrk is from OO to I4O°C\ prelerablv (wra 130 iυ IWW , The block copolyro^r oCclakn 12 Whcrsin the block cø|X>!>T5ier .is coupled k&vmg ϊkύ geoers! tbnnula (A^8.H>-X where λ in a glassy block s«d B is an ek^omerte bl«rk, τi is from 2 1& 6 tmά X h ϊhe residue of a coupling agent a.o<i ^iieresn the coupling a^cat 1« tφitaϊTssϊhoxy sifeue, tetra^rhexy si! arse or methyi-trimetiioxy Ml^e, , The block copolymer of atsy of claims
3(1 the glass. ts"&n§kk>0 temperature of the gkssy block is from 120 Io 140 : X.\ preferably irom IλO to 14*F " 'C\ &n<k b. κrι ole-fm polymer or copolymer,
17, The
IS 1 The eUtstomenc eompij&siiosi of S5iv of claims 16 to I / wherein ^c block αvpolymcf btis a ^tiieral formula (A-Sj^X where λ is a glassy block, B is an elssiomsric block, X kv tf:e re&kiue of a coupling agem ar^l ts is frora 2 to Cs, ihe |>s^k ϊϊsotecukr weight iA ' ύ\c block λ is !n;;?rs 5,000 to 30,0(Kl g.'mok asκl the amotirss oCtilock A is §o.m H) io 40 \v't% ots (he basis of s.hc ofiism block coρolysner τυass.
J9, The compo?iiioa oC aay of claims claim Ui to IS ikfhes
20. The d&«m*neπc composiUon of say of daims 16 to 19 ^vhcreio the alphs-alkykvmyls aroivistjc monomer sβ
2 L The cJs'stomeπt: compositi*,m cl " any of elaϊms 16 10 20 wheϊe;π block B *s hydmg&r^ted where s§: ka^ * ) (*% of εhe coryu^alfed <loiihte bxsnds have hce^ reclined.
22 A, selectively
h, tbs eUstomerk block is a block of at least one polymerized conjugated diene lisvitxg a vinyl content rrom betws&o. 20 to §5%; c. subsequent k* bγdroge«atkuϊ frosn 0 io shout l*Vh> of the srene double bo.tκis sτ5 the gk^y h&κU have bssrs reduced and at leasi ψj% of the conjugated double bosds m tht; elastomers block have been reduced; d. each glassy febck has & peak trco&eybir wdght from 2,000 Io 50 v
0 r
)0 g'Oio u preferably &onα 5,01 ^ Io 20.0QCK and each &is,vk> rsieπc block lia« a peak mo k-suisf weight
23. The selectively hydrogenMed
24. Ilie βeiectivgly fo>xirøy&oate<i ela&tomsrie block copolymer of elaim 22 whcreiss ihe block eopolyjrϊ<3ϊ hss the gsrse^l linear stπscUsre A - B or λ - B - C where A and C a& gUs.sy blocks smi B ss an L.Jasιomeric block,
25. The selectively
26 An arlkJe |
SIGH TEMPERATURE BLOCK Cβf s 0t¥ME!$S AMI PROCESS FOR MλKJN€
he .
Ths& hivsuiion relates ϊo isovcl pol^mαn^uon processes to prepare alpha-methyl- stymie (aMS) / stvraiε ϋ '
S) coμoiymws and blo-ek copolymer comprising the ssrne io which high eom-Tfskjm of &MS art.- achieved. The invention also relates i& &ϊ8&t&tnvήc block copolymers comprising aMS J 1
S hi oeics having high ul;ss,s Sxamilion temperatures. The invention further r&lsu.s to compcursds
Om? well kiiown p^bkm su?weiated wύh aMS polymers is their low cdHog ;
en>peraiϋre (
Tc). The cεslbg iempennute is tbe ξemperamre above whsch a polymer can spoMan£*jQsiy
λ-s second problem,
axp&sisive recycle openusorux Also. in black copolymer! zatkπi e.ffsekmt eatmimptkirs <A the aMS monome? can prevent eomammatiori of noo-ghssy bbel;$ -with, the high Tg ^KtS,
Block copolymers have previously been prepared comprising aMS^ '
S esxib locks as lauglu m GB Fsfenl 1,264,741. The polymerization was coMueied to syntheske blocks having * andoml;y uisfcibut'ed cosTsoπomtTs, ?hs ^) assy sndhteeks of ihes« block copolymer comprised a majority of mMS aικi hetweeβ IO ami 40 md\% of sfyrene moiwrπer.
Tapered hlock copch^er$ eorstsmmg aMS liave be^ii Uωght m US PMSΏJ 4 V 42TJ1> 1 The process taught thcreisi suffered from coriYtTβkms of kss thsn 10% of the aMS monoϊTisrr. T ' ^us.. large ^cesees of aMS monomer vv«ϊ'§ reqaheu to iricorpyust^ modest imiouBls In the fkml pcsiymcr, Reeuvery of £he uBpdym^ri^ed aMS moτκ;n$cr presents a sigm flcasit practical problem,
F :
ul!y hy<1rog®naϊed styreωe/aMS-Xlieae block eopolysners have bettsi taugh?. in IJS Parent Application 2005/006.1UV^, §m&ll rnioimis o.rp<. *
Iή.r co-soivent were wtili;?e<.1 hi order to
' Thsre .yet. exists a nee<] to? a proex*? ; ϊo eopolymcrke a.MS ■ ■ ' ' mor^winyl-aromaiic i^onorøers which can he corseted ;*t praeucul |K5!y3i"ssπ.?αtk>u ^mperatKres and which ?ιeine\es high coϋvsi^iou of ?h%? aJVfS s^oπomer Such ;'i pmcess will allow the coϊsstrucϋon of block copulyme^ h;mng high Tg glassy bkci<s and s^eh blosk copolymers will b& ^e ( b ^ m makisjg high sendee? tempemnsre mhbcr e<.>mpoιm<b. The prs&ent :rϊvenϋθ5i is dire ted k> suc-b a process, high Tg bkκ\k copol>^ers aad rαbber cwrsjKJunda made from them.
In OTS e
polymeo-ki chain esids is from 50ft So 2500 ppm and wherem the amount of alpha - metbyksϊymnit is from 25 to 50 m»!% OB ihe basis of the fciUil amount of ^yrene and alpha-in^hyl-^tyts-se: adding $ p«!yniεrø.&tιø« modifier, ;κkkng an stύotύc
ITS a further embodsmem the mv«^tκsn is ;s selectively hydrogemned elascomeric biock cop-ohm^ conipαsuig M least one gbs^y block asd a? leasi one efeton-scnc block wherein the ^las^y h\ :
,κk \s n copolymer of MI ylpha-alkyl-Yinyl-ammsπtr and morøvmyl- urwϊi&Uc oκ>oov?>e.fs and whttre ih«? mobr ratio of alpha- alky I -vinyl -arorυauc «\o«oo^er to αsonoviuyl^ϊromaiic nvaπomer is from 1$>1S to SO/SO, the d&stαmsrric biock i^ a bbck of at lcaxi one polymerized coηϊrsgs!t;d cik-Ti«- having a vinyl coistøα Ik* sn tetweeα 20 to 85Vs>, srώsequem to- hydxogsn&tton irut^ 0 u> aboαl 10% o£ tb-e ^e^e double bonds in the glassy block Imve been reduced UJKI at tesst Ot^i oi '
tbt; conjugated double bonds have been ?£-dit«ed, each glassy block ba& ts peak
copolymer mass * and th*c glass transition temper&lure oftbes gi&ssy block ss from 120 to 14ø°C.
Figure I h a GPC chrυrnatogr&m of inventive polymer 5 from Example U.
IMsliiiiJltiiiiiitlMMAfJiiitiilM
The process of the *
present uweatkssi is a unique polymen&atiεm process
M ψ&rtitiύ&r, the inventive process is αtϊhzed to synthesize therøiopkstic block copoϊyTners having high glass tr&usitioa teβperatαre fTg) glassy blocks. As used teτi.α iv
themx>ptetk; bfock copoly^ner" Is defined as a block copolymer having &t Wyst θϊ>fe elass-y bk>ck geiieisHy ρolyme?ized katn alpBϋ-a!i^1-viay|~aroorødc and monovioyK aroin&dc nujnoBiers waύ ui least
As defined herein, a high Tf value means having a glass transition tesmpeϊiMure greater than 100 C
C. Typically, Myn-nie polymer*, inc. lisdrng :«yτeme bJoek copolymers hsiVβ s gfossy block Tg value approaching !Cs(I 1
C. Che ob|ett td '
thc present mveniion is io construct bUxk ecsp-tdyraers having gl&ssy blo-cks comprising ;dphsκsil;yl"viriyl" aromatk . ■
' vhwl arornaiie ecφolYrøtsf blocks, having a giuss tr&srssuoft temperature g.rs;der ih&& thϋt s "
^«o!Uπ« m a. JϊKϊSIO vinyl- sfornstk homopolyr^er block. For hisijmce,
The mosomtxs liδcd in tfe
eycJooetaoe.. all of which ;ire rehniveϋy no^-pofe Other suitable solvents will be knows to OωC skilled in ihe an and can be sdoet&d to perform ϋffoetjvdy m & given set of process conditions, with temperature being one of the major factors taken isto consideration.
Anionic polymerisation initiators in tbe pre^nt invent JOB include, for exssτspk% alkyi lithium compounds arxi other organofkrshini compounds such as s4ustylHthknn, si~ binyfiiiMnm, t-h-utyllithn-ms, ■
iϊnyUϊthium ami fee like, iactudiag <^ .in.it i stars such as fee di-^ee-hutyi Hlhunn adtfees: of «>dnsoρropeϊϊyl beniHtαis, Other such di-irsiti&tors i«~e di?slv>sed m U. S Pat Nd. 6,4^2,469. Of ihe varknss polynierhϊauor; kiitlatorβ, s~ bi5i>lϊuhium is
Another effect of ifw
1Ώ ihc -process of the
would be achieved, ft has fee?;?! discovered that use oi a ;s©m$ »
b&teh ϋs-Mmon of crøioτio?nm ■
w/hs-jre all <■£ the &MS aod ooty a fraction of the styrrøs: ss added at ths beguiling of Ihe copolymers^ ; on h orst way to ^ebieve unsform ciistfibolkms and high iiMS conversions. The remskmg fbseten of styreae monomer required for completion
In !fe fully
Ths glass imnsύkm temperatm'e of a p&lymsr ϊs often
is efficiently eopolyraeti^ed while termhiatioji: k mmhnked Preferably, ikv £sψύyιrs.ύήz'λUCiiι k conducted at a ternrλ^yre from 35 to 50 0 C,
It js impoitaϊU to raamtaύs a hign cfmcfcriiraHon <ή living eals rø < sitemap Iy a high UtIi iiun couceMrsuon, This ss done by o.>nOireu.m; the eopoiymenz&tioB at high so Ms eυrus^ts, In the presem wernion- ^ solkfe eontem "' r^esns fe iaiiύ 5ViSSS of monomers to be polymerized or eoρø1ymcri?ώd expanses as & percctitsge of the tuUU lϊn^ss of mon.θ!mτs, solvents snd modiϋers. The preferred soikfe cosnent i& from 20 to 50 V λ ϊ%. The mαrt ! prcfen-^l s«hds content ss y<i κι 45 wrt-b &nd ϊBost preferred is frøm .>5 κ> 45 \vt%. Under these conditions the ccsLC&atfation of Isvuig polym r-lsthsum ehaiπ end is trorn 500 to 250(5 ppm (0 QOB - 0A)4 rϊuτκ>l/g). The snost preferred eoncentr&tion of living pol>tneτ-lithium chain ends is from 1000 to 25(K) ppm (Oisits - 0.04 rømol/g)
The Islhuim coucc^tratior^ xs aha effected by Lh<? molecular weight of ξhe polymers, λU other conditions bεirsg equal lower molec lar weight polyξBers ryquire
As used heresn, Lhe ierm iv
m<-5lscutaf wdghm "1
refers tα ihe true mαkc^kr weight tn g'Vuol of Ow pclymcr or block of ihe copolymer. The molecular weights refoτec.1 to in tbis sptjϊsikaUosi a?:fl eU':im<; e *
m be measured Wstb ge! p«rm*-siifm cbmreato^rapbv i€ j
PC) using polystyrene calibration standards, sach a^ ^ eone sccordmg to ASTM 3536. CiPl "
is a svα11--k;χwn
wte! the xtyr\?n^ e<mu>nt of the poijtner ami the vmyi eorstenf of the diene segments are known. The detecso? tssed is preferably a combination ults-aviolet s?κ1 rcfmerive mitex άetec&st. The mokxniax weighs sxpressed herein ^re measured at ihe peak of ^ he QFC ϊ?ace, convert to trtse molecular weights, ssxi are commonly referred iø as " " "p^&k mok* * ui;u ' wεs glu^ ' ,
Tl k 5rarx>rtfmi to ^nilke a 8αpøl>τn£rkaH<m modifier. TIm moάύiϋϊ <
im\m to improve the <?fβo icnc> of nicorpor;.uion of the rϋτπf*nonters dumif copolymer! gabion. Tvpicsi ct>ρo1ym?.-r5/adort modi6er; mdyde, for example,, pokr modille^ s^ch as dimethyl ether, diethyl ether, etbyj
Copolymer blocks of aVph>?i&:y!-vi&!yi~&romaik and monovisyl^rofaatk m»nom*:rs can k- used us construct
The dteπBopiastJc block wpolymers of the pres&ns invention can be ϊ^pres^tsd by, Inn sucv,
and n refrce^enes the average norssber of e«s.ιpk;l A - B arms. The ari>:>!.rm of ihe glassy block in the. thermoplastic block copolymer is from K ) to <& ' ) wt% basis, the total block copolymer mass, in this range the block copolymer exhibits thermoplastic elastomer
hi ihe general formula for a coupled polymer, CA - B)n.%, si is from 2 to abom 3ft, preferably iτom about 2 κ> about I S and most preferably from 2 π> 6 WIKII n k 2 the block eespiilymer has a linear configuration When n is greater than 2 the block s;opc<iymcr may be referred to &s radial, branched or *?&?\ Ths coupling reaction may be conduct*;! Io link
A sanely
I i
carboxylic aesεh, including diroethyt &dipate and the like, and er>6?ddk£d oUs*.. Preferred are ktta-aikoxysskffi^ such as t&ita-stho^yssh^e (I EOS l ask! tetra-mefexysdane, aikyi- ixuitkoxydhnes -such ss methyhiximsthoxy sparse (MTMS), alipbsaic diostsrs saoh as ekmslhyl a<jφκte «nd diethyl &dipate, ami digiycklyϊ aromatic erx»;y compounds such as digfyeκlyi ethers ckrivifsg from the reacuαn of his-p-lwol A and epichiorohydrin. When subsequent hydrogensfion or selective hj'd.rogeuafioB ix ύesir^l the coupling ag^tt should be cbαsoR such thm ; ; my residual ^nreacted toxψisng fsgt^fs, coupling :igeut reskkses incorporated hito tlie polpncr diam or by-products of ϋlis coupling reaction do not isterfcrc witl^ thi* hydrogeπatioω.
Iu Ae ombodimoni of &c pj-εscat
In the embodiment ol '
ikfc preset invention where m>s<oup!od l> '
kx-k copolyn^cTs are produced, the polymerisation is stoppyci by addilKsr *
of a tsmunating agent. Anionic
Hydro^enaύ5n eaiϊ ho carts sd otst via any Qϊ the several hydnjgenauoa or ^!erJs%'e hydrogen&Lioπ processes kmiwo in the prior art For c^^i^ple, sueh hydre>gu:aa <
*ft hfϊ& beesi ac4.'£jr?ψhs ;
hed ^siag ir.eihads such as those taught in, for srx^roplc, U ,
S Patent 3395,942 ;
3,634,549; 3,6?0 S
054;
ssmafek
Hydro^enaiion can be earned out snckf s.^cb comlUioαβ tnaf at least Jϊboui 90 percent of tbe. eoβj ' ugaUh! iliene double bctsids have been reduced ^ s^d between ^e^o and 10 percent of the δxo-πiatic do>uhk bonds hav« beea reduced. F^s-fsrrsd rsmges ^re at feast about s ^5 percent of the ccsjugaied. die^e double hoticfe yeduesd, &nά more prcfembly ahoy* 8 >8 psrcc^t of the i-αnjugϋted dk«e double bonds arc reduced. Aiterπstively, h is pos^ϊbk to h>i1?ogemue the polymer such Ou* aromaύc missiursfbn is slso rtHlutre-d beyoϊui tbe 1 C ) percent level n'Jt-nUOBed shove. Such exhaustne hydrog&nation is usαaiϊy achieved at higher temperatures, hi ik&i ea;-,e, the double bonds oi ' botl^ the conjugated <kene ^nd aronsatjc u^iks may be reduced by 90 p&reeni or more
In one embodiment of ihe presenl inveots^n a block poiyruer conipϊisjϊϊg at least αne gla&sy
ednieof/vmyl &eeu*te f EV Au copolymers, «hγkτιf.vvby! alcohol ( EV OH) copolymers, eϊhylene'cyclic okfits copolymers,
The claslomeαc block copdymssre of 4 he present
The ekstomenc block copolymers oi the
In oris lbrlher aspect ol the p?ese?u invontiαn. &n siticle contprisl«g s.he hsgh Tg bioek copolymer caa be roude 5π ihe IOπB of a £ύm. sheet midii-layer laminate. eo;^irs*, baud,
The iollowiBg exaπspk^ am provided as iHuj>tτa!iotsa of the present iπve^non. They are not meurst u ;
fi g
limiting, hoi πnher as enahling HU^trations of Hie fee &
i mode of She invention. 1 he
I S
dcterm.med using gd permeation ehrornattsgϊ&phy tGP€) The composήiion of ihe copolymers wss measured issin^ '' U NMR. The Tg values were measured using dilteremisd scanning eabrimetry ( DSC), SOJϊK? of fc tern*? ?a\mά m shs examples are defined hi I ' sbk- A.
lahie A.
In the following ex angles <tϊid data Uibies the poiymers of the mvendou are «U£ft£fic&!$y $rsoh ' e.sie<I The comparative pαhym«τ$ axe ideotifkd with a "C 1 prefix.
Exsmpk I
Copolymer glassy blocks ofaKIS ami styreoe wets synthesized in th.?c absence of a polymsn&it k>B mod; lkr m a 11. ^amless steel smtoeUwe. €yclohmsns; mtd the &MS were 8<lde<1 to she reaciok In this example no poiymerkaikxn modified %va≤ &£«?! lύ the Cβtse of ϊ«iv^bsteh sty?eue vopol ym α^stion (polynκτs C i . C"2 ami €3} ih@ hϋJch portM^rs of the snresie nKmoaier v.^^ al^o added. See-lπnyl lithium JiS tbe?? sάύzά io iniimt^ φi ή
ytv& ή
z&ύon. The remaining sϊwsrm; munoaiKT was sdd«d ;n a cou&tant rάic over a sp&cifssd ρrograi« lϊme, ussn^ a hi^h pressure syringe Dump. The examples of the mvcntion were
T? ,
hk> ! sii^ws the result? of aMS ■ ■
siyrene eopolymerfeatioris conductsd ^t 5ts*-« solk '
is Suitably high &MS conversioαs cfrom 67 to ?li%) were obϊanied hi polyrners L 2 aiϊd 3 * "
hich ^ '
ere eo duetesl usώo^? a batch charge of «t>τenc tno^ot^er at the onseε of
Example Il
Oφohπjsr gks^y hlocks othiMS mύ styreuε* were sw^hexk<ed according to the proee^ of
No fraction of tf;s rfyrsnε monomer was prcstait In the rcaetbn m.Lκmro at the onset of coρo!ynuϊriaatk.»n. Table 2 shows the result of RMS ' styrem? copolymers >ta dons conducted ai high solids contents {%<>%} mά with 0 % diethyl ether as |>dymcnjatioϊ$ modifier. TKs- poivroers had aλ>lS conversions tbosft 48 to §7% aτκ< reselling Ig values fϊom 128 to !40°C. Narrow mπiec alar weight distnbuiiems of the-
ExampJe Hi
Copolymer glassy blocks of aMS and s?yrene were synthesized act-ordiαg io tht process of Example II sit v&πous yoli^s contents. Di&tln-I ^ther at *.s \vβ-« was u&c<f &s a poK-TϊK.'nzmion modifier. 1 he sty ft ^. numoaier w^g Mdαl continuously ovaj a 6 ' ύ tn-soiste period Tbe coρ6Kτne!-5/.<iiion« wersr conduced at 50 ;V C ' fable 3 showώ the results of the &.MS / &tyτ$ne cαpoly^enzu^oos. Cojxϊhϊtϊsήzaikss ai solids, conrenis from 20 io 5*3 w!% snd molecular weights less ύrnn 20,CK>0 g'mo) gave iahium concentrations liorvi 9<H> us 300 rapm. A? 0u\se conditions high aMS eonvenio^s wersr achieved. For the polders tn^de at 30 to 50% solid? she aJMS corsversioa was 85% or greater. The ronultiαg T^ value of the eopolysners %va? from 120 to L^V " -f;,
Exars"ip!e IV
Copolymer glassy blocks of aMS and slyxcne xvere syntlisdzed accordmg ?o ihe pme&ss of Ii x amp k- Il at various po!yiυ€iizsk>a modifier levels. The eøixih/rneriEMkm ie;nperattir& was 50 "
C< Table 4
Copolymer glassy blocks of
i t t
dsmetbtsxy bewens? (ODMB ) , The chelating modelers gave copolymers having high &y S conversion &nά low molecular weight p-ohxfepes'sjty.
Example Vl
Copolymer gla&sy bbelg (vfaMS ami slyrene were
E^an^ple VII
DiHock coj:x>!)^ers having a gl&s&y block of &M '
S ;uκi ^tyreBe a»d &n sl&shmi&ic block of U - bufadsene were syulbe-siied aecordmg to the me&oii of Esarepls II with ϊha foVi.f.nvi.ng exeepdons. All of lhe ex;ιraplss were perιbrtτ<e<! us-iπg continuous iκk!UHiτ; of &i>ταie mo^os^er. ftere was no styrene aύύ^ά to the reaerk>α mixture- prior to smlktkrt As: lhe completion ofths glassy block eopofymem&Uon, butsdk^e >vas a <
MesJ ia a smgie batch charge, T^b^c 7 shows ihe s:esuifs tor th« (aMS / s,tyre?whbu&dieoe diblock copolymers. Comparative polymers C 7 ;s.rul CR were xtyrene4χ^udi&ne at block
Example VlIl
Xi
Trihløek copolymers having a gkise> block of &MS and stymie mύ m thmonmήc block of ! .3 - bufedlaie ^vore 3ynth&s.&s?od ^ccordmg to the method of E >: ample H with the folknvirsg eκf.epuom. The iπblocks were
Polymers 32 a.od 3? * •
£« sek^ively hydrogc^at&d Io a residual dieite
having a -siyr^nG ersdhloek eositem of 2ts.6 wrU, a $tyrer *
£ end block paak: molecular weigh* of ^ 0,000 and 3. vmyl content before hulrogen ;nk.ni of 50%. C buip&r&UYs- polymer Cl 1 is a coovcαtioπδl styr£r:& ~etb>1sπe- ;
b<Uyku£'§i.ymi£ block copolymer having a sryrene emiblock contest of S '
O
The cαmp*mn<is
Tfibic 9 sho-ws ihα ctvmpϋimά ihrnmlMαyns, snd \ht res is king physical propetikϊs. The faults &how exce-lleof higii tcnipitnjlure properties of ^e ϊnveafivc: compoiuni rdsrh'e to compounds cαnέairsitig converitiojϊ&l SHBS i>kκk copolymers. While
:k' S .
prog hrne unDu sMS 8tø .s' ; sxsjvmsr Modifier FFM Md EMiJ.
DEP 600 50 1 9% 44%
15 OOMδ 150 30 1138) 9.4% vv .'CJ 35 DEP 50 30 10.4% 41? 36 OEP 30 44 J 10.6% 580 1 SV eo% 16 DEP 70 107,100 11.?% 302 39% 56%
' Coπcsπtraϋ of af^S, which is calc
Tsblc 6. tc|t $ys tgUMS theα preg MpK uops t ^MS &M§ nUB sopdy iwi;&i i£ CGfiV
&o% S^ % 50% 50 60 14.910 2, s% 89% 00% so% 53% 50% SCs 3ø 15,560 3. 1 % SS% i>0%
1 ? ^>\.' ,'v 4() 30 VK 13ø 6, 6% ??% 46%
5 Coric«in?rats©o of 3i|>ha~m-e?hy1 siyreπe in St/a^S €αpolymβf (%wt) based OR the convers?ofi of aMS % whsch *s cslςulated Dy assuming ^hsf sny aMS ijifsww ^^ ss wA delected as residual h%$ > polym&n;
Tabic 9.
> ■ ?