Thermal Degradation of Polyacrylonitrile, Polybutadiene...

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Journal of Research of the National Bureau of Standa rds Vo!' 61, No.2, August 1958 Researc h Paper 2888 Thermal Degradation of Polyacrylonitrile, Polybutadiene, and Copolymers of Butadiene With Acrylonitrile and Styrene 1 Sidney St raus and Samuel 1. Madorsky Polybutadiene and a copolymer consist ing of 76.5 perc ent butadiene and 23 .5 p erce nt of styrene were inv est i gated as to t he rates of t heir the rmal degradat ion . Th e ra tes for po lybu tadiene indi cate d an act iv:ttion energy of 60 kilocalories per mole. Th e copolym er had very high initial rate s of degradation, followed by a rapid cirop, so t h at it not possib le to obta in a reliab le act i vat ion energy. Pol ya crylonitri le a nd a copolymer consisting of 31 percent of acrylonitrile a nd 69 percent of bu ta di ene were inve st i gate d with rega rd to the n ature and di stri bu t ion of vol at ile products, as well as to t he rates of their thermal degradation. Th e rat es were very high in itially, but dropp ed rap idly 50 that it was not possible to determine accurately the act i vation energy. Th p, acrylonitrile-butad iene copolymrr showed a rlecomposition pattern similar to that of po lybutadiene. Here, too, the acL i vat ion ene rgy could !lot be rl ec!uced accurate ly fr om the rate curves. Comparat i\O e thermal in terllls of temperatu re, at which half of the polymer sa mple is e vapora ted in 35 m inu tes of heating , is as follows: -!07°C for polybutad ienc, 374°C for SB ll , 36+° C for polysty rene, 360° C f or NEll, and3JG o C for polyac rylon itrile. 1. Intr oduction Th e copolymcrs, styrene-bu tadiene (GR- S) and acrylonitrile-butadiene (niLrile rubb er ), curr en tly designated in the technical l it cratur e as SBR and NBR , respectivel.\', rcpresent two of the more im- portant synt h et ic rubbers. This pap er describes tbe results of an invest igat ion of the relative thermal stabili ty and of the products of degra dation obtained when these rubb ers are pyrolyzed in a vacuum. A similar description is given of the thermal behavior of a nd polybu tad iene. D etails of the m et hod employed in this investi ga- tion ha ve been described pr eviously [1 - 5].2 T he method consists of t wo parts. In the fir st p art, a sample weighing 25 to 50 mg is heat ed in a vacuum, fir st for 5 min dUTin g a heating-up period, then for 30 min at a constant temperature; the r esidue is w eigh ed, and the volatile products fractionat ed. Th e fractions are then weigh ed and analyzed in the ma ss spectromet er or tested for average molecular weight by a micro cryoscopic m ethod. In the sec ond part , a 4 to 5 mg sample in a pl atinum crucible suspended from a very sensitive tungsten spring balance [3] is h eated in a vacuum, and th e rate of loss of weight of the sample is observed at int ervals. Th e activation energy of degradation is calcul ated from the initial rates by using the Arrhenius equat ion. 2. Ther mal De gr adation of Polybutadie ne and SBR A study of th e relativ e tbermal stabili ty of poly- butadiene and the copolymer SBR, and of yields and chemical nature of the products r es ulting from pyrolysis of these two ma terial s, ha s been report ed previously [2,4]. Pol ybutadiene was found to be 1 Presented before the 132d Meetlng of the American Chemical Society, New York, N. Y., September 7- 12, 1957. , Figures in brackets indicate the literature referen ces at the end of this paper. more stable than the copolymer. Tb e ratios of small molecul ar fragments to large ones were 14 :84 for poly- bu ta diene and 12 : 88 for SBR. In this inv es ti gat ion a st udy was made of ra tes of thermal degradation of these two s ubs Lan ces the loss-of-weight m ethod , using a very sensitive tungst en sp ring balance enclosed in a vacuum [3]. Samp lcs of poly butadi ene and of SBR (76 .5% of butadiene and 23.5 % of weighing about 5 mg, were used. Th e materia ls were pr ep ared b.\' purifying commercial products usin g a m et hod whiclt h as been described previously [2]. R esult s of rate st udi es for polybu tadiene arc shown in fi gure 1. About 12 to 16 percent of the s amples was vaporized at zero time; th is vaporizaLioll Loo k place dur ing the approxima lel.\' 15 min he ating-up period. Zero time in these ex periments W itS reckoned from the moment the sampl e had reached the operat- 100 ,--.--r--,-----,,---,--,----.-.,--,.--,- ,- -,.--, 2.0 1.6 w OJ o iii w a: 1. 2 t5 ;:: z w u a: w lL 040 . 80. W lL 0 ;:: 0 z w 0 U ...J 520 .4 0. o 0 o 80 160 240 320 400 460 TIME FROM START OF EXPERIMENT , MINUTES F IGURB 1. Th ermal degradation of poly butadiene. Solid lines represent percentage volatilization versus time and dashed lines represent logaritbm of percentage residue versus time. 77

Transcript of Thermal Degradation of Polyacrylonitrile, Polybutadiene...

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Journal of Research of the National Bureau of Standa rds Vo!' 61, No.2, August 1958 Research Paper 2888

Thermal Degradation of Polyacrylonitrile, Polybutadiene, and Copolymers of Butadiene With Acrylonitrile

and Styrene 1

Sidney Straus and Samuel 1. Madorsky Polybutadiene and a co poly mer consisting of 76.5 percent butadiene and 23 .5 percent

of styrene were investigated as to t he rates of t heir t hermal degradation . The ra tes for polybu tadiene indicated an act iv:ttion energy of 60 kilocalories per mole. The copolym er had very high init ial rates of degradation, followed by a rapid cirop, so t hat it wa~ not possible to obtain a reliab le activation energy.

Polyacrylonitrile and a copolymer consisting of 31 percent of acrylonitrile a nd 69 percent of butadiene were investigated with regard to t he nature and distribu t ion of volat ile products, as well as to t he rates of t he ir thermal degradation. The rates were very high in it ially, but dropped rapidly 50 t hat it was not possible to determine accurately t he activation energy. Thp, acrylonitrile-butadiene copolym r r s howed a rlecomposit ion pattern s imila r to t hat of polybutadiene. Here, too, t he acLivat ion energy could !lot be rlec!uced accurate ly from the rate curves. Comparati\Oe thermal ~tab ili ty in te rllls of temperatu re, at which half of the polymer sample is evaporated in 35 m inu tes of heating, is as follows: -!07°C for polybutadienc, 374°C for SBll, 36+° C for polystyrene, 360° C for NEll, and3JGo C for polyacr ylon itrile.

1. Introduction

The copolymcrs, styrene-bu tadiene (GR- S) and acr ylonitrile-butadiene (niLrile rubber ), curren tly designated in the technical litcrature as SBR and NBR, respectivel.\' , rcpresent two of the more im­portant synthetic rubbers. This paper describes tbe results of an investigation of the relative thermal stability and of the products of degradation obtained when these rubbers are pyrolyzed in a vacuum. A similar description is given of the thermal behavior of polyacr~Tlonitrile and polybutadiene.

D etails of t he method employed in this investiga­tion have been described previously [1- 5].2 T he method consists of two parts. In the first part, a sample weighing 25 to 50 mg is heated in a vacuum, first for 5 min dUTing a heating-up period, t hen for 30 min at a constant temperature; the residue is weighed, and the volatile products fractionated. The fractions are then weighed and analyzed in the mass spectrometer or tested for average molecular weight by a micro cryoscopic m ethod. I n the second part, a 4 to 5 mg sample in a platinum crucible suspended from a very sensitive tungsten spring balance [3] is heated in a vacuum, and the rate of loss of weight of the sample is observed at intervals. The activation energy of degradation is calculated from the initial rates by using the Arrhenius equation.

2. Thermal Degradation of Polybutadiene and SBR

A study of th e relative tbermal stabili ty of poly­butadiene and the copolymer SBR, and of yields and chemical nature of the products resul ting from pyrolysis of these two materials, has been reported previously [2,4]. Polybutadiene was found to be

1 Presented before the 132d Meetlng of the American Chemical Society, New York, N . Y., September 7- 12, 1957.

, Figures in brackets indicate the literature references at the end of this paper.

more stable than the copolymer. Tbe ratios of small molecular fragments to large ones were 14 :84 for poly­bu tadiene and 12 :88 for SBR.

In this inves tigation a study was made of ra tes of thermal degradation of these two subs Lances b.\~ the loss-of-weight method, using a very sensitive tungsten spring balance enclosed in a vacuum [3]. Samplcs of poly butadiene and of SBR (76.5% of butadiene and 23.5 % of st~Tene), weighing about 5 mg, were used. Th e materials were prepared b.\' purifying commercial products using a method whiclt has been described previously [2].

R esults of rate studies for polybu tadiene arc shown in figure 1. About 12 to 16 percen t of the samples was vaporized at zero time ; this vaporizaLio ll Loo k place during the approxima lel.\' 15 min hea ting-up period. Zero time in these experime nts W itS reckon ed from the moment t he sample had reached t he operat-

100 ,--.--r--,-----,,---,--,----.-.,--,.--,-,--,.--, 2.0

1.6 w OJ o iii w a:

1. 2 t5 ;:: z w u a: w lL

040 . 80.

W lL ~ 0 ;:: 0 z ~ w 0 U ...J

520 .4 0.

o 0 o 80 160 240 320 400 460

TIME FROM START OF EXPERIMENT , MINUTES

F IGURB 1. Thermal degradation of poly butadiene. Solid lines represent percentage volatilization versus time and dashed lines

represent logaritbm of percentage residue versus time.

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ing temperature. The fact that the logarithm of percentage residue versus time curves deviate only sligh tly from straight lines indicates that the reaction involved in the thermal degradation of polybutadiene approaches first order.

In figure 2 rate of volatilization is plotted versus amount volatilized. The apparent initial rates are obtained by extrapolating the straight parts of the rate curves to the ordinate. These rates, in percent­age of sample per minute, are 0.21, 0.31 , 0.42, and 0.63 for temperatures 380°, 385°, 390°, and 395° C, respectively . On plotting logarithm of the initial rates versus t he inverse of absolute temperature, a straight line is ob tained, whose slope indicates an activation energy of 62 kcal/mole.

Percentage volatilization of SBR versus time is shown plotted in figure 3 (solid lines). H ere again there is considerable loss of weight during the heating up period. Plots of logarithm of percentage residue versus amount volatilized (dashed lines) deviate considerably from straight lines. The reaction involved in the thermal degradation of SBR appears to be more complicated than that for polybutadiene and the reaction is far from first order. R ate of volatilizat ion versus amount volatilized is shown in figure 4. The rates, very high initially, drop rapidly with extent of volatilization. It is not possible to determine with any accuracy the activa­tion en ergy from these rate curves.

10 20 30 40 50 60 70 80 AMOUNT VOLATILIZED ,PERCENT

FIGURE 2. Rates of volatilization oj polybllladiene.

90

1.6w :::> Q

Ul W a:

r.2~ <! >­Z W u

5 .8a.

"­o o ~ o

• 4..J

o 80 120 160 200 240 280

TIME FROM START OF EXPERIMENT, MINUTES

FIGURE 3. Thermal degradation of SEll. Solid lines represent percentage volatilization versus time and clashed Jines

represent logarithm of percentage residue versus time.

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I.O,-----,----,---------,---,-------r--,----,

w S.8 z ~ a: w a. w.6 ..J a. ::;

'" Ul

"­° .4

10 20 30 40 50 60 70 AMOUNT VOLATILIZED, PERCENT

FIGURE 4. Rates of volatilization of SEll.

3. Thermal Degradation of Polyacrylonitrile and NBR

The polyacrylonitrile 3 of high purity and in the form of a fine white powder , had a number-average molecular weight of about 40,000. The NBR rubber was Goodrich H ycar 1042 consisting of about 30 percent of acrylonitrile and 70 percent of buta­diene. The rubber was extracted for 24 hI' with ethanol-toluene azeotrope in order to remove im­purities. It was then kept in a vacuum at 60 to 70° C for 5 hr. The purified material analyzed 8.2 per­cent of nitrogen, which corresponds to 31 percent of acrylonitrile. Specimens of polyacrylonitrile and NBR were heated prior to pyrolysis, in a vacuum at 110° C to a co nstant weight.

R esults of pyrolysis are shown in table l. Frac­tion V _ 1904 represented less than 0.1 percent of the total volatilized and is not shown in this table. As in the case of many other polymers the ratio V25 : Vp yr

remained constant t lll'oughout the temperature range. On the average, this ratio is 12 : 88 in the case of polyacl'ylonitrile, and 14: 86 in the case of NBR. In the latter case, in calculating the average ratio, results of experiment 1 were excluded, because vola­tilizat ion was only 9 percent.

As seen from table 1, volatilization of polyacry­lonitrile stabilizes at about 70 to 73 percent. T his is in agreement with the work of K ern and Fernow [6], who found that dry distillation of this material was accompanied by carbonization of the residue. A possible explanation of this stabilization, as given by M cCartney [7] and Houtz [8], is the formation, along the chain, of ring structures involving nitrogen from the CN groups. NBR, which con tains only 31 per­cent of acrylonitrile, does not show any stabilization through the entire temperature range .

Fractions Vpyr from polyacrylonitrile and NBR had a tan waxlike appearance. They were not readily solu ble in ordinary organic solvents, including

3 The anthors are indebted to O. A. Sperati of the Polychcmicals D epartment, E. 1. duPont de Nemours & 00., for supplying them with this polymer, which is LIsen in the production of orIon fiber.

, For definition of fractions sec footnote to tahle 1.

-~~--------

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TABf"E 1. P yrolysis of polyacrylonarile and NBR

fl Volatile fractions a

based on tota l vola· Experiment number T empera· VolaWiza· t ilized

L ................... . . . 2 ..•............••..•.•. 3 ...................... . 4 ..•.•........•••••••... 5 .•.••...•...•.•...•.•.• 6 __ •• __________________ _ 7 ______ ______ __ • _______ _ 8. _________ ____________ _ 9. ____ ________________ _ _ 10 _____________________ _ 11 ___________________ __ _ 12 __ ______ _____________ _ 13 __ _____ ______________ _ 14 ___________ __________ _

A ' ·crage. ______________ _

1. _____________________ _ 2 ___ _________________ _ 3 _____ ______________ __ _ 4 __________________ ___ _ 5 ______________________ _

Avg (2 to 5 inc1.) ___ __ _

tnre tbn 1-----.----1

POLYACRYLONrTHILE

°C 250 250 250 2i5 300 325 325 325 32.> 350 350 400 425 455

310 3.,0 3G5 380 400

NHH

% 21. 5 20.7 18.0 34.9 46.6 53.4 52.3 49.7 50.6 57.7 57.9 67.7 70.2 72.8

9. 1 29.4 G~ .. 1 80. () 95.0

% 86.3 89.1 89.0 88.0 86. 3 88.4 886 87.4 88.8 88.7 87.8 90.1 87.2 883

88.1

71 0 8 1. 5 87.8 8~ . 7 84.8

85.5

% 13.7 10. 9 11. 0 12.0 13.7 11. 6 11. 4 12.6 11.2 11. 3 12.2 9.9

J2.8 11. 7

11.9

26.0 15.5 12.2 J5 3 15.2

] I. 5

The main constituents in V25 are HON, acryloni­trile, and vinylacetonitrile. The composition of V25

seems to depend on the time interval elapsing beLween pyrolysis and analysis. This suggests t.he possibility that some of the component, parLicularly HON and acrylonitrile, react and become non­volatile on standing and, as a result, the remain ing volatile constituents become accentuated in the analysis . This could explain why Houtz [8] r e­ported that pyrolysis at 400 0 0 yielded only a trace of HON. On the otber hand, Hideo Nagao and co­workers [9] reported the evolution of a considerable amount of HON when polyacrylonitrile was heated at temperatures from 200 0 Lo 3500 0 in an aLmos­phere of air or niLrogen. Burlant and Parsons [10] found ammonia as one of the decomposition products from pyrolysis of polyacrylonitrile. We could no t find ammonia in the volatiles.

Results of mass spectromeLer analy is of V25 from NBR are shown in table 3. Two of Lbe analyses were made shorLly after the fractions were collecLed and kept at Lhe temperature of liquid N 2, a third one alter an interval of 3 days at room temperature, and a fourth one aILer an interval of 8 days at the same LemperaLure. All the anal~Tses were similar and the average results are shown in Lable 3. The results

a T he following \'olatilc rractions were collected: V pyr , \'olatile at tbe Irmpera­tnro of pyrolysis, bu t not at 25° C; \ .", ,·o latile at 25° C, hUL not at -J90°. In the case of othcr polymers it was usually found necessary to separate t his frac- T A B IJE 3. jlJass-speclrometer analysis of I '25 from 7Jyrolysis oj tion into two parts to facilitate m ass spectrometer a nalysis. H ero it was fo und nitrile ,·ubber unnecessary to do so; \' -10., ,·olatile at -1900 c.

pyridine. Average molecular weight by tbe micro­cryoscopic method in diphenylamine was 330 ± 9 for polyacrylonitrile and 401 ±3 for NBR.

Fraction V -190 from pyrolysis of polyacrylonitrile was analyzed in the mass spectrometer. This frac­tion consisted of hydrogen. Tb e Y -190 fra cLion from NBR was too small for analysis.

Fraction V25 from pyroly is of pol.raerylollitril e when first collecLed was a milky-whiLe liquid. The color of th e liquid changed arLer standing, firsL Lo tan and tb en to brown . ResulLs of mass spec­trometer analysis of Lhjs fracLion arc shown in table 2. V25 fractions LhaL collecLed in experiments 1, 4, 5, 11, 13, and 14 were analyzed within 1 to 2 hours after they were collected . The Lime interval between collection and analysis was 1 day for ex­periments 2 and 7, and 1 week for experiments 3 and 8.

Formula. of component I A " cl'agc of , 4 analyses

(' ,H , ________ . ________ _ (' , ll . _____________________ _ C,11 , . ______________________ _

~ :~::- :~~:~:::~~~:~:::~~J C,ll". ____________________ , C,II, __________________ _ C,ll, _____________________ _ c,u,, _______________________ _ C SITI 2 _____________ . _______ _ C,J[,. _______________________ _ C.ll, _______________________ _ C, H ,. _______________________ _ C 6U I2 _______________________ _

C, to C" inc1ush·e __________ _

TotaL ____________________ _

. 1 role % Y. I 4.7 3.0 2. [)

H . l

8. :l 3. 3 2.5 9. I 4.8

1.6 .!.:l 6. () 5. 4 2.7

17.6

100.0 J

TABLE 2. 11fass-Sp ectrometer analysis of Y25 from pyrolysis of polyacrylonilrile

Time intrrval betwecn end of cxperiment and analysis

Component 1 to 2 homs 1 day 1 week ------------.,----- ,---,----1----;----1---,----1 Expt. l' Expt.4 Expt.5 Expt. 11 Expt.13 Expt. 14 Expt.2 Expt. 7 Expt.3 Expt. 8

1--------------------------------------------M ole % Mole % }.Iole %

H ydrogen cyanide ______________ ~4 22 16 Aerylonitrile _________________ 36 45 49 Vinylacetonitrile ___ ___ . _ ------ 30 30 32 Pyrrole __ . _______ --- -------- 3 3 Aeetonitrilc ____________________ Butyronitrile __________________ Propionitrile _____ ______________

TotaL _______________________ 100 100 100

u Expcriment numbers are the same as those giwn in table 1.

470~83-58--2

JIoie % }.fole % ,l8 66 10 7 13 13

3 6 2 4 8

100 100

79

Mole % 63

6 12

10 3 6

100

j\Iole % ;lIole % AIole % j\Iole % 28

88 63 86 59 12 11

100

9

100 100

19

100

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resemble those obtained previously for butadiene and SBR (formerly GR- S) [2]. It is rather surprising that none of the products characteristic of polyacryl­onitrile pyrolysis showed up in these analyses, al­though two of the analyses were made shortly after the fractions were prepared and were kept in liquid N2 until the time of analysis. It is likely that in the presence of unsaturated fragments resulting from pyrolysis of the butadiene in the copolymer, the hydrogen cyanide, acrylonitrile, and vinylacetoni­trile, polymerize more rapidly than in their absence, and therefore do not show up in the analysis of the acrylonitrile-butadiene copolymer.

A comparison of thermal stabilities of the various polymers and copolymers discussed in this paper, and also of polystyrene, is shown in figure 5. The curves for polyacrylonitrile and NBR are based on data in table 1, and those for polystyrene, SBR, and polybu tadiene were taken from figure 1 of reference [4]. The temperature, Th DC, at which the sample loses half of its weight by vaporization in 35 min, can serve as a basis of comparison of thermal stability of polymers.

R esults of rate studies in the tungsten spring bal­ance are shown for polyacrylonitrile in figures 6 and 7. In figure 6, percentage of volatilization is plotted versus time from start of experiment. At lower tem-

10 0'---r--.~-.---'---'---'---'---'---'---'--,

.... ~ 8 0 u 0: UJ

":.6 0 z o [i N4 0 :::; [i 620 >

:' ~R / ,,'

POLYSTYREN/' ••••• _. _,.:-0:_/_' -~~ " ' ,:

,,/POlYBUTADIENE

240 280 320 360 4 00 440 TEMPERATURE, DEGREES CENTI GRADE

FIGU RE 5. Relative th er'mal stabi li ty of polymers and copolymers.

Ourv es fo r polystyrene, SBR, and polybutadiene were taken from figure 4 of reference [4] . 1' he T . values are as follows: 4070 0 for polybutad ienc, 3740 0 for STIR, 3640 0 for polystyrene, 3600 0 for NBR, and 3160 0 for polyacrylonitrile.

5o ,-----,-----,-----,------,-----,-----,------

~ 30 ,. " V> .. o

"' 20 '" ~ z "' u

'" "' Q. 10

=====~~-----o------------o2 800

_---0---------<> 2 60 ·

_---<>-----0-----0 2 50 •

°0L-~==~---4~0----~60~--~8~0 ----~10=0~---1~20~--~,40 FROM STAR T OF EXPE RIMENT, MINUTE S

FIGURE 6. Thermal degradati on of polyacrylonitrile.

L_

2 .0 UJ .... :::> z

1.8 ::1 0: W "- 1.6 w --' "-:;;

1.4 <t Ul

lL 0

w 1.2 <.?

~ Z W U 0: W "-Z .8 0 i= <t N .6 o=! .... <t --' .4 0 > lL 0

280 0 W .... <t 0:

10 30

AMOUNT VOLAT ILIZED, PERCEN T

FIGURE 7. Rates of volatilization of polyacrylonitrile.

peratures, a considerable ini tiation period is ob­served . Beyond this period volatilization proceeds rapidly, but soon drops to a very small value, indi­cating stabilization of the r esidue. At higher tem­peratures t he initiation period terminates during tho 15-min heating-up period and the curves show stabil­ization of the polymer soon after the sample reaches the operating temperature. These facts can be ob­served more easily in figure 7, where rate of volatili­zation in percent of the original sample per minute is plotted against percentage volatilization. It is not possible to estimate with any degree of accuracy the initial rates or the activation energy based on any of the rates sho\"11 in figure 7.

80

Results of rate studies for NBR are shown plotted in figure 8, where percentage volatilization is plotted

50r---------,---------,---------,---------,

040 w N :::;

~ --' o > 30 w --' Q.

~ <t If)

lL 0 20 w (9

~ z w .U a:

~Ior

50 100 150 200 TIME FROM START OF EXPERIMENT, MINUTES

FIGU RE 8. Thermal degradation of NER.

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versus time from star t of experiment, and in figure 9, where Tate of volatilization in percen t of original sam­ple pel' minute is plotted versus percen tage volatili­zation. The two sets of curves Tesemble closely those for SBR shown above (figs. 3 and 4), and no defini te conclusion as to initial rates and activation energy can be based on these curves.

0 .8 ~------Y------r------r----r-----,

~ 0 .7 :::> z ~ a: w "- 0.6 w -' "-:;; <l if)

"-- 0.5 o w

'" <t f---

i5 0.4 u a: w "-z ~ 0_ 3 <t N ::;

~ c5 0 _2 > "-­o w

~ 0 .1

°OL----ILO---~2~O--~3~0~--~4~0---~50

AMOUNT VOLATILIZED, PERCENT

FIGURE 9. Rates of volatili zation of NER.

4. Discussion

The main constituents of the light volatile fraction V 25 obtained in the pyrolysis of polyacrylonitrile, are hydrogen cyanide, acryloni trile, and vinylacetoni­trile. The hydrogen cyanide most likely forms by spli tting-off the chain in the same manner as CH3COOH in the pyrolysis of polyvinyl acetate [11], H Cl in tbe pyrolysis of polyvinyl chloride [12], and HF in the pyrolysis of hydroAuoroethylene polymeTs [13].

II IT n II J[ IT c C C C IT C C

~IV-I III"?/H"g/II\ .. 6N CN I 6N

" n/ ""c/ u" / IT" ··-c C +HCN

6N 6N (1)

Formation of monomer can be visualized as follows. A random scission of a C- C bond in the chain re­sults in two free radical ends.

81

H H C c· "H/U"II/ 1I J[ ]I

C C +c= c I I I II ON CN CN

H H C C

II II IT/ IT" rI/Il" C= C+·C C I II I I eN Gl. ON (2)

Thi s is followed by an unzipping reaction yielding monomers, as shown in eq (2).

FormaLion of vinylacetoni trile could be explained if we assume fl, h ead- Lo-head arrangement at some posiLions in the chain, as shown in eq (3).

2 free radicals + c rr2= C IT-CIT~CN (3)

This formation involves 2 C- C scissions in the eha.in , followed by a hydrogen Lransfer from position 1 Lo position 2.

The pyrolysis eUl'ves for polyacryloniLrile (fi g. 5) as well as the raLe curves (figs. 6 and 7) show stabili­zation dur in g pyrolysis. This is charac terisLic of polym ers in which the loss of side groups from a.d jacent carbons of the chain r esults in conjugated double bonds in the chain, since these double bonds tend to enhance the thermal sLability of Lhe chain. Polyvinyl chlorid e [12] and polyviJ1~TlideJ1e fluoride [13] may be cited a.s examples of a behavior similar to that of polyacrylonitrile.

5 . References [1] S. L. Madorsky and S. Straus, J . R esearch NBS !l0, 417

(1948) RP1886. [2] S. L. Madorsky, S_ Straus, D. Thompson, and L . William­

soo, J. Research N BS !l2, 499 (1949) RP1989. [3] S. L. Madorsky, J . Polymer Sci. 9, 133 (1952); 11, 491

(1953) . [4] S. Straus and S. L . Madorsky, J. R esearch rBS 50,

165 (1953) RP2405. [5] S. Straus and S. L. Madorsky, Ind. Eng. Chem. !lS, 1212

(1956) . [6] W. K ern and H. Fernow, J . prakt. Chem. 160, 281

(1942); Rubber Chem. and T echnol. 17,356 (1944) . [7] J . McCartney, Poi.vmer degradation mechanisms, N BS

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