Thermal stability of polydivinylbenzene and of copolymers ... · mal stability of these copolymers...

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------ -- -- JOURNAL OF RESEARCH of the National Bureau of Standards-A. Physics and Chemistry V ol. 65A, N o.3, May- June 1961 Thermal Stability of Polydivinylbenzene and of Copoly- mers of Styrene With Divinylbenzene and With Tri- vinylbenzene l Sidney Straus and Samuel L. Madorsky (J anuary 18, 1961) Samp les of poly di vinylbenz ene (PDVB) a nd of copolymers of styrene with di vi nyl- benzene (DVB) a nd wi th trivinylbenzene (TVE) werc pyrolyz ed in a vacuum in t he tem- p erat ur e range of 346 to 450 °C. Th e vol at il e products were coll ect ed in . two fraction s: A h ea vy fraction volat il e at t he te mp erat ur e of pyro lysIs and a lI ght fr act lOn vol at Il e at roo m te mp e rat ur e. Mass sp ect rometer analysis of the light fr act i on sh owed that for the copolymer co n tain in g 2 percent DVB the yicld of sty renc monome r is s omewhat great cr t ha n for the pur c poly st yr ene. On p yro lysis, of copolymers co nta ining 25 perc e nt of DVE or of TVB yield reduced a mount s of s ty rene monomer; tho e conta ining abo ut50 percc nt of DVB do not y ield any s tv re ne monom cr. R ates of ther mal d egradaLi o n of PDVB an d of t he copolymers were studied in the temperaLure range of 33 0 to 390 ° C; the activat ion energies calcul ate d on the ba sis of rates were 53, 54, 58, 58, 61 , a nd 65 kca l/mole for t be copolymers co n ta ining 2 percent DVB, 25 percent DVB, 48 percent DVB, 56 percent DVB, 25 per ce nt TVB, and for PDVB, resp ect ively. 1. Introduction Polystyrene was found to decompose thermall y in a vacuum [1] 2 or in a neutral atmos phere [ 2, 3] at temperatures below 500 °C by a mechanism con- sisting of random scissions of C-C bonds, fo llowed by unzipping at the resulting free-r adical chain ends to yield monomers and multiples of strucLural unit s of an average mol ecular weight of about 264. Under these conditions co mpl ete vol atiliz ation of the sampl e takes place, fo r ex ample, at 400 °C in a bout 30 min. of heaLing. On the other h and , pol ytrivinylbenze ne (P TVB ) [3], when pyrolyzed und er similar conditions, does not yield any ap pr eciable amo unts of eith er styrene or of trivinylbenzene monomers. ] nstead, the vol atil e d egra d aLion products co nsist of a frac- tion co nt aining a small amo unt of hydrogen and sat ur ate d and unsat ur ated hydrocarbon fragments h av ing from 1 to 11 carbons; a less vol at ile fr action consists of l arger fragment s having an average molec- ular weight of 372; a nd the residue co nsists of a car bonaceous m aterial. The mechanism of degradation of this highly cross linked PTVB polymer is assumed to be as follows: When a C- C bond in the shor t connecting links be- tween the phenyl groups breaks, two r eactions are possible: (a) A transfer of hydrogen may take place at the site of br eak so that one end becomes sat u- rated and the other ul1saturfttrd, and (b) the two ends become free radicals. In the l atter case the fr ee radicals do not unzip to form monomers because of Lhe cross linkages that hold the phenyl groups at other points. Instead , the fr ee radicals ab str act hy- This res careh was s upport ed by the U ni ted States Air Force under delivery order No. (33-616)58-8. monitored by Materials Cent ral Directorate of Ad vanccd Systems Technology. Wri ght Air Development Div isioll. . 2 Fi gur es in brackets indicate the literature references at the end of thIS paper. 58540 2- 61- -8 drogen from Lhe surrounding medium and become saL ura ted. As the numb er of s uch SClSSlOn s 111- creases !ragmen ts of various size", whi ch m. ay or mfty nht conta in phenyl gro up s, split off from the chain , abstr act sonee h ydrogen from LiLe resid ne, and va pori ze . Th e residue in the m eantime becomes carbonized in th e process through lo ss of h y dr ogen. Int ermediat e b et ween these two extremes are co- polymers of styrene with di vinylbenzene ( DVB ) or with (TVB ). An in vesti gat ion of the thermal b ehavior of such co polymers was ca,rried out by '\ iVill slow and Matreyek [4] in nitro gen at atmos- pheri c pressure, at tempera.tures up to abo ut 550 0 0. Th ey were in ter es ted primarily in the rel ative mal stabili ty of these copolymers tmd in the n at ure of the residu es, and therefore did not s tudy the vola. tile productions of degradat ion. . . The prese n t st udy was und ertaken to 0 btam .m- form at ion on the mechanism of thermal degrad atiOn of these copolymers through analysis of the vol at ile products of degradation. A st udy was also mad e of the degra dation of polydivinylb enzene ( PDVB). Th e prese nt work, as in the case of most of our work on thermal degrad at ion of pol :ymer s, was cft l'ned out in a vacuum. In addition to investigat ion of the nature of the volatile degrad at ion produ cts, the rates an d ac tivation energies of degrad ation were also de- termined. Allowing for the differences in the ex- perimental co ndition s, our results are in fairly good agreement with those of Winslow and M atreyek. 2. Materials Th e co pol ymers 3 consi ste d of polystyrene co n- ta ining the followin g amo unt s, in weight percent, of 3 'I ' he au thors are in debted to F. H. Win slow of Bell T elephone Laboratories for s uppl ylng them wiLb sampl es of these copolymers. 243

Transcript of Thermal stability of polydivinylbenzene and of copolymers ... · mal stability of these copolymers...

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    JOURNAL OF RESEARCH of the Nationa l Bureau of Standards-A. Physics and Chemistry Vol. 65A, No.3, May- June 1961

    Thermal Stability of Polydivinylbenzene and of Copoly-mers of Styrene With Divinylbenzene and With Tri-vinylbenzene l

    Sidney Straus and Samuel L. Madorsky

    (J anuary 18, 1961)

    Samples of polydi vinylbenzene (PDVB) a nd of copolymers of styrene with divi nyl-benzene (DVB) a nd wi th t riviny lbenzene (TVE) werc pyrolyzed in a vacuum in t he tem-p erature range of 346 to 450 °C. The volatil e products were collected in . two fraction s: A heavy fraction volat ile at t he temperature of pyrolysIs and a lIght fractlOn volatIl e at room temperature. Mass spect rometer analys is of t he light fraction showed t hat for t he copolymer co ntain ing 2 p ercent DVB t he yicld of sty renc monomer is somewhat g reatc r t ha n for the purc polystyrene. On pyrolys is, of copoly mers co ntaining 25 percent of DVE or of TVB yield r edu ced amounts of styrene monomer ; t ho e containing about50 perccnt of DVB do not y ield any stvrene monom cr. R ates of t hermal degradaLion of PDVB an d of t he copoly mers were st udi ed in t he temperaLu re r a nge of 330 to 390 °C; the activation energi es calculated on t he basis of th c~e rates were 53, 54, 58, 58, 61 , a nd 65 kcal/ mole for t be copoly mers co ntainin g 2 percent DVB, 25 percent DVB, 48 p ercent DVB, 56 p ercent DVB, 25 perce nt TVB, and for PDVB, resp ectively.

    1. Introduction

    Polystyrene was found to decompose thermally in a vacuum [1] 2 or in a neutral atmosphere [2, 3] at temperatures below 500 °C by a mechanism con-sisting of random scissions of C-C bonds, followed by unzipping at the resulting free-radical chain ends to yield monomers and mul tiples of strucLural units of an average molecular weight of about 264. Under these conditions complete volatilization of t he sample takes place, for example, at 400 °C in about 30 min. of heaLing. On the other hand, polytrivinylbenzene (PTVB ) [3], when pyrolyzed under similar conditions, does not yield any appreciable amo unts of either styrene or of trivinylbenzene monomers. ] nstead, the volatile degradaLion products consist of a frac-tion containing a small amount of hydrogen and saturated and unsaturated hydrocarbon fragments having from 1 to 11 carbons; a less volatile fraction consists of larger fragments having an average molec-ular weight of 372; and the residue consists of a carbonaceous m aterial.

    The mechanism of degradation of this highly cross linked PTVB polymer is assumed to be as follows: When a C- C bond in the short connecting links be-tween the phenyl groups breaks, two reactions are possible: (a) A transfer of hydrogen may take place at the site of break so that one end becomes satu-rated and the other ul1saturfttrd , and (b) the two ends become free radicals. In the latter case the free radicals do not unzip to form monomers because of Lhe cross linkages that hold the phenyl groups at other points. Instead, the free radicals abstract hy-

    This res careh was supported by the U ni ted States Air Force under delivery order No. (33-616)58-8. monitored by M aterials Central Directorate of Ad vanccd Systems Technology. Wright Air D evelo pment Divisioll. .

    2 Figures in brackets indicate the literature references at the end of thIS paper.

    585402- 61- -8

    drogen from Lhe surrounding medium and become saLurated . As the number of such SClSSlOns 111-creases !ragmen ts of various size", which m.ay or mfty nht contain phenyl groups, spli t off from the chain, abstract sonee hydrogen from LiLe resid ne, and vaporize. The residue in the meantime becomes carbonized in the process thro ugh loss of hydrogen.

    Intermediate between these two extremes are co-polymers of styrene with di vinylbenzene (DVB) or with Lrivin~'lb e n ze n e (TVB). An investigation of the thermal behavior of such copolymers was ca,rri ed out by '\iVillslow and Matreyek [4] in nitrogen at atmos-pheric pressure, at tempera.tures up to abo ut 550 00. They were in teres ted primarily in the relative ther~ mal stability of these copolymers tmd in the nature of the residues, and therefore did no t s tudy the vola. tile productions of degradation. . .

    The presen t study was undertaken to 0 btam .m-formation on the mechanism of thermal degradatiOn of these copolymers through analysis of the volatile products of degradation. A study was also made of the degradation of polydivinylbenzene (PDVB). The present work, as in the case of most of our oth~r work on thermal degradation of pol:ymers, was cftl'ned out in a vacuum. In addition to investigation of the nature of the volatile degradation products, the rates and activation energies of degradation were also de-termined. Allowing for the differences in the ex-perimental conditions, our results are in fairly good agreemen t with those of Winslow and M atreyek .

    2. Materials The copolymers 3 consisted of polystyrene con-

    taining the followin g amounts, in weight percent, of 3 'I' he au thors are in debted to F. H . Winslow of Bell T elephone Laboratories

    for supply lng them wiLb sa mples of these copolymers.

    243

  • DVB or TVB: 2 per cen t DVB, 25 per cent DVB , 48 per cent DVB, 56 percent DVB, and 25 per cent TVB. The PDVB was prepared by heating a pure grade of DVB monomer in an evacuated and sealed 6-mm Pyrex tube in an oven at 80 to 90 °C for 6 weeks. The tube was then opened, and tbe polymer , which was in the form of a rod, was heated fur ther for 1 Ill' in an evacuated ch amber at 120 °C. A loss of 8 percent, presumably monomer , took place during tbis heating s tep, bu t no addi tional loss occurred on fur ther beating at this temperature.

    3. Experimental Procedures

    3 .1. Pyrolysis

    The experimen tal procedure used in th e pyrolysis of PDVB and of the copolymers was the same as tha t used earlier in the pyrolysis of PTVB and other polym ers [3]. Appara tus No. II described in ref-erence [3] was used. Samples weighing 15 to 30 mg were heated in a vacuum by quickly moving a preheated furn ace into position surrounding th e sample for pyrolysis. Dura tion of hea ting was a 5-min period to heat up the sample from room tem-pera ture to the temperature of pyrolysis, followed by a 30-min period a t th e pyrolysis temperature. Fluctua tion of the fin al tempera ture was ± 2 00. The residues were weighed , and th e volatile produ cts were collec ted and fraction ated. The followin g volatilized products were ob tained : (a) A waxlike fraction design a ted as V"yr, vola tile at the tempera-tUTe of pyrolysis, but not a t room temperature, which consi s ted of large molecular fragm en ts de-posited in the appara tus just beyond the ho t zone; (b ) a ligh t frac tion, V25 , vola tile at room tempera-ture, collected in liquid-nitrogen-cooled trap ; and (c) a gaseous fra ction, V -190, no t condensable at the tempera ture of liquid nitrogen.

    Fractions V"yr and V25 were weighed, and the amoun t of V - 190 was determined from pressure, volum e, and chemical composition da ta. Frac-tions V25 and V -190 were an alyzed in the mass spec-trometer. Frac tion V - 190 "vas very small, less than about 0.1 percent by weigh t, and was found to con-sist primarily of CO. This is similar to the r esults obtained previously [1] in t he case of polystyrene.

    The relative thermal stabilities of PDVB and of copolymers of styrene with DVB and with TVB ar e shown in figure 1. Curves for polys tyrene and PTVB, included in this figure for comparison, arc b ased on data obtained previously [3,5]. As can be seen from this figure, a styrene-DVB copolymer con taining only a small p ercen tage of DVB has a thermal stability not much different from that of t he s tyr ene homopolymer. The copolym er con-taining 25 p ercen t of DVB shows an increase in s tability over tha t of pol~Ts tyrene . Still greater quantities of DVB in the copolym ers prodl~ce further increases in the therm al stability, but at about 50 percent of DVB, s tability reaches a maximum and is abou t equal to that of PDVB homopolym er. Poly-trivinylbenzene has a much higher thermal stability

    than the PDVB, and it r equires only 25 percent of TVB in the styrene-TVB copolymer to equal t he th ermal stabili ty of PDVB.

    The amounts of vola t ilized products from th e pyrolysis experiments on PDVB and the copolymers are given in table 1. The V25 fractions from a number of experiments on the copolymers wer e analyzed in the mass spectrometer, and the resul ts are shown in table 2. The mass sp ectrograph for fraction V25 from PDVB was very complex and could no t b e interpreted completely . The r esul ts are therefore no t indica ted in t he table. However , there was a defini te indication of the presence of considerable amounts of toluene, benzene, s tyrene, and xylene.

    100 .--,----,-,-----,----,-..,---,-----,--,------,-----,--,------,-----,--,------,

    90

    80

    :0 10 ~ ¥i! 60 ~

    ~ 50

    ~ 40

    '" ~ l O 10

    10 , , ,

    llO

    , , , ,

    , , , ,

    l 50 llO 190

    .£::0 56 % OV8 .-::;- POLYOIVI NYL6EHIE HE

    LI,.'-=:::""'-='L.:....'..:'-o 15 % TV8

    POlYTRIVI H Yl 6E~~ ~/////

    J' '''''''' ''-//

    "",,,,,"'"

    410 TE .PERIIURE ' C

    430 450 490

    F I GUR E 1. R elative thermal stabi li ty of polydivinylbenzene and polytrivinylbenzene, and their copolymen with styrene.

    T A BLE 1. P yrolysis oj polydivinylbenzene and of copolymel's oj styrene with divinylbenzene and with trivinylbenzene •

    Fractions, based on 'I'empcr- Volat ili· volatil ization

    !\Iater ial ature zation

    Vpyl' V 25

    ------------' C % % %

    2% DVlL . _____________________ { 346 16 0 42. I 57.9 355 32. 2 42. 7 57.3 3n 70.6 47.2 52.8 390 98.3 48. 1 5J. 9

    25% D\·8 ___ ____________________ { 36 t 20.7 43.0 57. 0

    II 375 54.2 49. 7 50. 3 386 n9 49.1 50.9 400 94.5 52. 1 47.9

    ! 370 18.6 PO. 5 19.5 390 3 1. 1 87.4 12 6

    III 48% DV B ___ __ ____ ______________ 401 64.6 94 9 5. I 420 87.5 96. 0 4.0 443 90.7 95.0 5. 0

    56% D\-B _. __ ___ . ___________ . __ . ! 370 14.4 64. 0 36.0 387 28.4 77. 4 22.6 I V 400 50. 1 82.9 17.1 425 87.3 93.2 6.8 450 91. 6 91. 8 8.2

    25% 'I' \ ·B ___ _ • ________ . _________ ! 372 17.3 69. 0 31. 0 388 41.1 63.6 36.4 V 400 65.6 7i.8 22.2 420 81. 4 79. 9 20. 1 450 82.0 83. 7 16.3

    Polyd h·inylbenzene __ . _______ . __ { 385 24. 0 54.4 45. 6

    VI 400 53.8 67. 1 32.9 420 79. 8 71. I 28.9 450 84 . 7 81. 0 19.0

    a. Duration of heating in each eXDcrim ent was 30 min, preceded by 5 min 0 preheating.

    244

  • TAB I ~E 2. AT ass spectrometer analysis of volatile products fTom pyrol ysis of copolymers of styrene WW1 divinylben zene and trivinylben zene

    Copoly mer 2 % DVB 25 % DVB 48 % DVB 56 0 DVB 25 % TVB

    T emperature, °C 34·6 390 386 400 370 390 443 400 450 400 'J20

    Component wt . % wt. %

    C3H O_ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ O. 8 _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ O. 8 O. 4 C4H O_ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ O. 6 _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ ____ ___ _____ ______ - _ - _ - - - - - - - -C5H lO _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ O. 7 O. 6 _______________ _ C5HI2 _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ 3. 0 2. 7 ____ ____ _______ _ coHo_ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ O. 4 l. 5 O. 5 ___________________________ __ . _ _ _ _ _ _ _ _ _ O. 4 O. 4 C6H 14 __ - _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ O. 8 _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ - _ _ _ _ _ _ _ - _ - - - _ - - - - - - - - - - - - - - - - - - - - - - - - - - - - -C7HS_____ _ _____ 0.6 1. 4 2.8 2.7 ________ ________ ________ ____ ___ _ _____ 2.7 3. 0 CsH s--------- ___ 51. 7 49.8 39.9 34.8 ________ ________ _____ ___ _____ ___ ________ 16.2 14. 4 CsH 10 _ _ _ _ _ _ _ _ _ _ _ 2. 0 _ _ _ _ _ _ _ _ O. 9 1. 4 _ _ _ _ _ _ _ _ O. 5 O. 6 1. 3 1. 4 1.0 1. 2 Cglh _ _ _ _ _ _ _ _ _ _ _ _ O. 7 1. 7 1. 0 O. 4 O. 4 O. 5 O. 4 ___ ____ _ 0.9 --- - --- -C9H I2 _________ 2.1 0.7 0.8 0. 7 0.8 0.6 _______________ _ 0.9 0.9 C 1oH I2 ______ ___ _______ ___ _____ 4. 8 9.2 7. (j 2.0 _______ ------- -6.7 o 5 C1oH I4 ______ _ _ 0.8 1. 0 J. 1 8. 9 2. 9 0.6 1. 7 O. 5 --- - ----Others " __ ________ 0 0.3 0.2 0.8 0. 3 0.4 0.7 2.2 1. 8 O. 4 O. 5

    -- -

    Total of V 25 _ -- 57. 9 51. 9 50. 9 V py , _____________ 42. 1 48. 1 49. 1

    47. 9 52. 1

    )9.5 80. 5

    ]2. 6 87. 4

    5. 0 95. 0

    17. I 82. 9

    8. 2 22. 2 20. I 91. 8 77.8 79. 9

    TotaL _____ - - - 100. 0 100.O 100. 0 100.0 100.0 100. 0 100.0 100.0 lOO.O 100. 0 100. 0

    • Compo nents ill amO lln ( ~ of 0.3 perccnt or Jess are no t shown indi v idually ill this tablc.

    There was olso il group of peaks in the nlaSS-rfl ngo of 112 to 118, corresponding to a co mpound CgH ,o .

    In the 2 percent-DVB copoly mcr the yield of t he styrene monom er , CgH s, is slighLly greater t han in the case of 100 pcrcent polystyrene , which was previously found to be about 40 wei gh t percen t of the totHl volatilized part [1, 5]. The yield of monomer de-creases with the i.ncrease of DVn conten t in the copolYlller ami disappears altogether wilen the contenL of DVB is up to flbouL 50 percenL. There i.s, howeve l', consi.derable monOJll(' j" content in lhe volatiles from t ll C 25 perccnt-TVB eopolymcr.

    3.2. Rates

    Rates of Lhermal degradation of the styrene co-polymers and of PDVB were measured in a vacuum by a gravimetric method, which makes use of a very sensitive tungsten spring balance having a sensi-tivity of about 570 micrograms per millimeter of displacement. The apparatus and experimentfll procedure have been described in detail in an earlier publication [6]. Samples were limited to about 5 mg and were heated in a platinum crucible.

    Cumulative p er'cen tages of volatilization for the copolymers an.d for PDVB are shown plotted in figures 2, 4, 6, 8, 10, and 12. These curves of per-centage loss versus tim e were used in calculating th e data for the rate curves, which arc shown plotted in terms of percentage loss per minute as a fun ction of cumulative percentHge vohltilization in figUl"es 3, 5, 7, 9, 11, and 13.4 In calcul ating the activation

    • In fi gure 13 thc se parate pOints are sho\\"n. T11e calculated ratcs at 390°C arc rat her high, an d the calcul ated points show a good deal of scattcring.

    energies of t he poly mer degl"

  • 100

    90

    80

    ::0 70

    3 1" 60

    ~ 50 '" 40 i 30

    10

    10

    FIGU RE 2.

    1.1

    o

    ~ 1.0

    340'

    330'

    100 115 150 175 100 115 150 115 300 TliE fROi STIRT Of EXPERI MENT,m ln

    Thermal degradation of copolymer 98 percent styrene-2 percent divinylbenzene.

    360'

    355'

    0.1 ------------------~

    10 20 30 40 50 60 10 80 90 PE RCENTAGE Of SAiPLE VOL ATlLlZEO

    FIG U RE 3 . Rates of volatilization of copolymer, 98 percent styrene-2 percent divinylbenzene.

    90 369'

    80

    10 -

    3 60 1"

    ~ 50

    ~ 40

    I 30 20 10

    250 300 Tl i E fROM SIAR T Of EIPERI ME!!, min

    FIGURE 4. Thermal degradation of copolymer, 75 percent styrene-25 percent divinylbenzene.

    1.0

    0

    1 0.8 %

    ~ 0.6

    ".

    ::0 0.4 ~ ~ ~

    ~ 01

    0 0 10

    FIGURE 5.

    369 '

    36 0'

    10 30 40 50 60 10 80 PERCENTACE Of SAMPLE VOLATlLlZEO

    Rates of volatilization of copolymer, 75 percent styrene- 25 percent divinylben zene.

    90 r--,--,-,--,--,--,-,--,--,--,-,--,--,,--,

    80 390' 380'

    10 370~

    300 350 TINE fR OM START Of EXPERliENT, min

    FIGURE 6. Thermal degradation of copolymer, 52 percent styrene- 48 percent divinylbenzene.

    1.0

    390'

    .~ 0.8

    ~

    ~ 0.6

    " ~ 380'

    ~ 04 ~ 370'

    ~ 0.2 -0

    0 10 20 30 40 50 60 70 80 PERCE NTAGE Of SAi PLE VOLAIIL1IEO

    FIGU RE 7. Rates of volatilization of copolymer, 52 percent styrene-48 percent divinylbenzene.

    246

  • 90 .---~--'----r---r---'----r---~--'----r---,---,~--,

    80 190' l80'

    370'

    115 150 175 lOO

    7INE fRON S7ART Of EXPERINEN7 , min

    FIGURE 8. Thermal degradation of copolymer, 44 percent styrene-56 percent divinylbenzene.

    190'

    .~ 0.8

    ~ 0.6

    l80'

    ~ 0.1 370 '

    10 10 30 40 50 60 70 80 PERCENTAGE Of SAMPLE VOLA71l1ZEO

    FI GURE 9. Rates of volatilization of copolymer, 44 peTcenl styrene--56 percent divin ytbenzene.

    80

    ~ 70

    ~ 60

    :5 40

    ~ lO ::: 10

    15 50 75 100 125 150 175 100 115 150 175 300 TI ME fRON START Of EXPERIMENT, min

    FIGURE: 10. Thermal degmdation oj copolymer, 75 percent styrene-25 percent tTivinylben zene.

    190' 1.1

    l80'

    ~

    ~ 0.6

    l 70'

    0.1-~

    O L-~~ __ ~~-L~L-~~~ __ ~~~ __ ~~~~ o 10 10 lO 40 50 60 70 80

    PERCENTACE Of SANPLE VOL ATILIZEO

    FIGURE 11. Rates oj volati li zation of copolymer, 75 percent styrene-25 percent trivinylbenzene.

    247

    80

    70

    ~60 = ~ 50 x 370' ;;; 40 :5

    IlO

    40 80 110 160 100 140 180 310 360 400 440 480

    TI ME fROM STAR 7 Of EXPERIMENT , min

    FIGURE 12. 'Thermal degmdation of polydivinylbenzene.

    1. 0 ,.---,.---,---,.---,.---,---,---.,.---,

    .~ 0.8 390'

    o

    o :0;0.6 o ..

    l80' o

    ~ O.l 370'

    ~l60'

    o Lo----~~--~1~0----~lO~--~470 -----7,50~--~6~0 ----~70~--~80 PE RCEN TACE Of SAMPLE VOLA7IlIZED

    FIGURE 13. Rates of volati lization oj polydivinylbenzene.

    -- _. -- --. --------

  • TEMPERATURE 'c 390 380 lIO 360 330

    +0.1

    -0.1

    ~ -0.4

    " " -0.6 ~

    -0.8

    - 1.0

    - 1.1 1.50 1.51 1.54 1. 56 1.58 1.60 1.61 1.64 1.66

    + X 10J FIGUlm 14. Activation energy cW'vesfor the thermal degradation

    of polydivinylben zene and of copolymers of styrene with divinylbenzene and with irivinylbenzene:

    I . styrene-2 percent DVE, n , s t y rcne-25 percent DVE, III, styrcne-48 percent DVB,

    IV, styrene- 56 percent DVB, V, s tyrene-25 percent TVB, VI, polydivi:nylbenzene.

    trivinylbenzenc can b e visualized as follows: In polystyrene, cleavage of t.he chain ordinanly takes place at the weakest. bonds, which are the C- C bonds in i3-posit.ion t o t h e double bonds in the phen.vl groups- in this case the ones in the main chain .

    cleavage, type 1 cleavage, ype 2

    The cleavflgc can be or two types. Type 1 result s in the format ion of one saturated and one unsatul'-ated end ; and type 2 results in 2 free radicals, which proceed to unzip to give monomer, dimer, and trimer [1]. The monomer appears together wi th other small fr agments in ['raction V25, while the dimer , trimer , etc., appeal' in fraction Vp yr . On the addi-tion of a small amount of a crosslinking agent , such as 2 percent divinylbenzene, the unzipping to give dimer and trimer is somewhat blocked by t he short-ening of the free chain b etween cross ljnks, and more of t.he monomer appears at the expense of the mul-t.iple units. However, with a further increase of cross links in th e chain by t h e addition of DVB or TVB, the formation of monomer uni ts is blocked.

    The yield of monomer falls off for the copolymer contaming 25 percent DVB, and even more for the copolymer containing 25 percent TVB. ItVhen the amoun t of the cross linking agent is still further increased , as in t he case of copolymers containing 50 percent or more of DVB, no monomer appears among the volatile produ cts.

    There were no signs of carbonization of the degra-dation residues from. copolymers with 2 or 25 percent of DVB . However, in the case of the copolymers containing higher percentages of DVB , 25 percent TVB, 01' of polydivinylbenzene, the volatilization curves begin to level off at abou t 80 to 90 percent loss (fig. 1), and carbonization of the residue takes place. The polytrivinylbenzened volatilization curve

    T A BLE 3. Rates of thermal degradation of polymeTS of divinyl-benzene and tl'ivin ylben zene and of their copolymers with styrene

    M aterial Tem- Rate Activat ion perature energy a

    ° C %/min kcal/rnole

    I 2% DVB ___________________________ ! 330 0.19 I 340 .39 349 .74 53 355 1. 05 360 1. 39 II 25% DVB ____ _______ ______ _____ ____ {

    350 0.27 } 360 0.52 54 369 1. 00 III 48% DyB __________________________ { 370 0.23 } 380 .45 58 390 .88 n - 56% D \ ·B ____ ____ ____ ______________ { 370 .24 } 380 .48 58 390 . 93

    \- 25% 'l'\-B_. __ ______ __ _______________ { 360 .29

    } 370 .70 61 380 1. 32 390 (b)

    VI Polyd i'·inylbeDzene _________________ { 3fiO 0. 08

    } 370 . 19 65 380 . 44 390 .86

    VII Polytrivin ylbenzene _______ __ _______ { 394 . 03

    } 420 .28 73 430 .59 440 1. 22

    a Act ivation energies for copolymers I , II, III, IV, find for homopolymer VI were calculated on the basis of maxim um rates; th ose for copolymer V and for homopolymer VII, on the basis of initial rates.

    b Degradation rate at this temperature was too rast to obtain an accurate extrapolated init ial rate.

    T A BLE 4. Activation enel'gies based on mtes of degradation a 35 pel'cent and 50 percent volatilization

    ==================~=======T=======

    DVB in Percentage Activation copolymer degradat ion energy

    % % kcal/mole

    I 2 { 35 50 50 50 n 25 { 35 56 50 56

    III 48 • 50 63 I V 56 a 50 58

    a I n t he case of copolymers containin g 48 percent and 56 percent DVB, t he maximu ms in figures 7 and 9, respectively, appeal' at percentages of volatilization higher t llan 35; t here fore t he rates at 35 p ercent yolatilization werc not used iJ calculating activation energies.

    begins to level off at abou t 53 percen t loss, and the residue shows considerable carbonization.

    5. References

    [1] S. L. lVJ adorsky a nd S. Straus, J . R esearch K BS 40, 417 (1948) RP1886.

    [2] H . Staudinger and A. Steinhofer, Ann. 517, 35 (1935). [3] S. L. Madorsky and S. Straus, J . Resear ch KBS 63A

    261 (1959). [4] F. H . Winslow and 'Xl. Matreyek, J . Polym er Sci. 23

    315 (1956). [5] S. Straus and S. L . YIadorsky, J . Research N BS 50, 165

    (1953) RP2'105. [6] S. L . Madorsky, J . Polymer Sci. 9, 133 (1952). [7] S. L . Ma dorsky, J. Research N BS 62, 219 (1959) RP2957

    (Paper 65A3- 108

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