Neoprene GN, Hycar OR-15, and Perbunan 26

(23) Mark, H., in “Der feste Korper” p. 103, S. Hirzel, Leipzig, 1938. (24) Mark, H., “Physical Chemistry of High Polymeric Systems”,. (25) Me...
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INDUSTRIAL A N D E N G I N E E R I N G CHEMISTRY

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(20) Kern, W., Ber., 68, 1439 (1935). (21) Kraemer, E. O., IND.ENQ.CHEM., 30, 1200 (1938). (22) Kraemer, E. O., and Lansing, W. D . , J Am. C k e n . Soc., 57. 1389 (1935). (23) Mark, H . , in “Der feste Korper” p . 103, S. Hirzel, Leipzig, 1938. (24) Mark, H., “Physical Chemistry of High Polymeric Systems”, p. 235 ff., New York, Interscience Publishers, 1940. (25) Mead, D. J., and Fuoss, R . M . , J . Am. Chem. SOC.,64, 277 (1942).

(26) Ostwald, W-, Kolloid-Z., 49, 60 (1929). (27) Schulz, G. V., 2.physik. Chem., B30, 379 (1935).

Vol. 35, No. 9

(28) Schulz, G . V., and Blaschke, F , J. prakt, C h e w , 158, 130 (1941). (29) Schulz, V., and Dinglinger, A , , Zbid., 158, 136 (1941). (30) Staudinger, H . , “Die hochmolekularen organischen Verbindungen”, Berlin, J. Springer, 1932. ( 3 t ) Staudinger, H., and Fisrher, K.’, J . prakt. Chem., 157, 19 (1940). (32) Zbid., 157, 158 (1941). (33) Staudinger, H . , and Schneiders, J., Ann.,541, 151 (1939).

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PRESENCEU before the Division of Rubber Chemistry at the 102th Meeting of the AVERICANC ~ E W X CSocrnry, AL Detroit, Mich Communication 920 from Kodak Research Laboratories.

Neoprene GN, Hycar OR-15, and Perbunan 26 S. M.MARTIN, JR., AND A. E. LAURENCE Thiokol Corporation, T r e n t o n , N. J. The properties of Thiokol FA blends w i t h which will not adversely affect HE use of blends of the N~~~~~~~ GN,H ~0 ~ ~~ 1 and 5 ~, perbunan , ~ the rate of cure of Thiokol FA. various synthetic rubbers Thus, in the Hycar OR-15 in the Of 26 have been studied. Thiokol FA is comand perbunan 26 compounds, stocks is increasing. The purPatible with these synthetics in Proporb e n z o t h i a z y l disulfide and pose is to get better processing stocks, to obtain specific proptions, but properties of the blends do not DPG ( d i p h e n y l g u a n i d i n e ) erties in the cured composition, show a change zuhich i s proportional to the were used for acceleration. amount of each synthetic i n the stock f o r Formulas of the base stocks and to extend the supply of and a summary of their physxny one that might be momenall properties measured. Consequently, ical characteristics are shown trtrily short. Thiokol FA1 is being successfully used in since a number Of the Properties Of the in Table I. The stocks were combination with other synblende do not vary as a linear function of mill-blended so that the crude the composition, i t was necessary to estabsynthetic content of each blend thetic rubbers. I n some of lish trends f o r blends of each of the several w&s that shown in Table 11. the stocks Thiokol FA is the I n the discussion all mention predominant phase; synthetics. Data of a basic nature are of blends refers to the crude some other synthetic is the principal constituent of the Presented which should Prove useful even synthetic content and not to rubber phase and Thiokol FA though any speci& property can be modiparts of compounded stock. .lied to s o m e entent by cornpounding variaThe ~ t o c k blended s easily in all is used to impart specific properties to the compound. tions. proportions. I n all cases the Thiokol FA stock was first millThe purpose of this study warmed by six passes through was to obtain basic information on the properties of Thiokol FA blends with Neoprene GN, Hycar OR-15, and Perbunan 26. It is felt that the data will show general characteristics which prevail in blends even ,though any specific property can be varied within certain TABLE I. J?oR?lrUr..\s OF BASS STOCKS limits by formulation changes. 100 .. .. Ttiiokol F.1 Neoprene O N .. i6o .. A typical FA stock of 70 durometer hardness was selected .. 100 Hycar OR-15 for one part of each series of blends. The other portion was Perbunan 26 .. 100 10 5 8 9 Zinc oxide made up of typical compounds of Neoprene GN, Hycar ORSemireinforcing black 60 50 50 60 0.5 1 1 1 Stearic acid 15, and Perbunan 26. These latter stocks had the same 0.3 .. 1 1 Benzothiatyl disulfide hardness as the Thiokol FA conipound but contained no exDiphenylguanidine 0.1 .. 0.2 Phenyl-a-naph thylamine . . 2 . . tractable plasticizers; the latter were purposely omitted to Extra light calcined magnesia .. 4 .. .. .. 1 . 5 1 .6 simplify the interpretation of the data. Sulfur When stocks are being compounded for blending with Physical Properties of Sheets Cured 60 Min. at 298’ F. Thiokol FA, it is important that accelerators be selected Tensile lb./sq. in. 1290 2820 3000 2760

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1 The trade name “Thiokol” used throughout thin article is registered in the U. 8. Patent O5ce.

Elongaiion, %

410

430

450

I

310

September, 1943

INDUSTRIAL AND ENGINEERING CHEMiSTRY

dered from these blends 318 sunininrized in T a b l e 111. T h e Neoprene GN stock8 :and all ita blends with Thiokol FA weie smooth. T h e Hycni. O R nnd Perbunan stocks were tough ;mI gave wavy or rough slicets 011 calendering. Kith &:%T the roughncss disappeared in the 40 ThiokolMl Hycar blend. With Perbunan 3 smaller amount of Thiokol gave 3 smootli sheet. In

w

20 13 5

The diffusion was measured by puttiiig i 4 ml. of fuel in a half-pint Muson jar

equipped s i t h B Kem top. A disk cut from sheets 0.062 inch thick (cured 40 nrinutes a t 298' F.) was insertod into the top, replacing the regular metal rlisk of the Kern top. The jars were stoved in an inverted position in a eonstbnttemperature rooin (80° F.) with free circulation of air across the surface of the disk and were weighed on a balance sensitive to 0.02 gram. Diffusion through the straight Thiokol FA stock is fairly low and increases slightly on addition of small amounb of another synthetic. Blends containing more than u)per cent Neoprene GN and Perbunan show rapid increase in diffusion u.8 the proportion of either of these synthetics in the blends is raised. With Hycar OR the same general characteristics prevail, but diffusion losses are lower than for Seoprene GN and Perbunan blends.

e4

60

the other e.ttrrn,r.

4a

20

10

0

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Vol. 35, No. 9

INDUSTRIAL AND ENGINEERING CHEMISTRY TENSILE STRENGTH

Figure 3 also shows tensile strength curves for the 60minute press cure at 298" F. for the various stocks. The tensile strength wa3 determined according to A. S. T. M. proce-

2

I

8

6

4

give better processing stocks than straight Thiokol. Here again it is sometimes better to sacrifice slightly in solvent resistance to gain better vorking characteristics even though the tensile strength of the blend is not materially increased

4

8

Figure 1. Diffusion of 813 Fuel through Thiokol FA Blends with Thiokol FA, Hycar OR, and Perbunan

dure (2) for testing vulcanized rubber. The volume swell of the stocks increases more rapidly with addition of other synthetics to Thiokol FA than does tensile strength. At the same time the tensile strength of the other synthetics decreases to a greater extent with the addition of Thiokol FA than does volume swell. However, it may sometimes be advantageous to sacrifice tensile strength to gain better working characteristics even though the volume swell is only slightly improved through blending. On the other hand, 10 to 20 per cent of the other synthetic rubbers blended with Thiokol FA

TABLE IV. TEARRESISTANCE DATA Cure at 298" F., Min.

90

80

Parts Thiokol FA 60 40 20

10

0

10

Parts Other Synthetic 20 40 60 80

90

100

FA-Neoprene GN Blends 221 350 244 211 316 253 264 210 181 277 199 205

368 353 300

370 323 296

314

340

330

Thiokol FA-Hycar OR-15 Blends 258 351 308 269 246 253 295 301 305 328 311 309 262 285 295 335 340 270

360

247 186 181

100 0

20 40

60

Av. 20

40 60

301 286 290 292

Thiokol 299 305 269

_ _ _ _ - - - 291

_

Av. 20 40 60 Av.

303 280 277 278

278

311

238

207

_

299

277

Thiokol FA-Perbunan 243 224 203 298 262 254 240 243 228

260

218

243

228

281

284 227

_

-

303

290

205

26 Blends 222 208 238 181 189 171

195 165 155

193 173

-

-

-

167 -

216

187

172

174

over that of the original Thiokol compound. It should be pointed out that Neoprene GN-Thiokol FA blends do not cure satisfactorily in open steam. Both the Thiokol FA and the Neoprene GN stocks alone cure well under the same conditions. TEAR RESISTANCE

Tear was determined on five strips at each cure and all values falling with 20 per cent of the highest value were averaged (3). Data were obtained on three separate stock mixes, and tear values for the three mixes checked one another within 20 per cent. Table I V summarizes tear resistance of all stocks; and for the purpose of establishing trends, tear values for the three cures were averaged. Blends of Thjokol FA-Neoprene GN show a decided dip in tear in the middle of the range. Small additions of Neoprene GN to Thiokol FA or of Thiokol FA to Neoprene GN do not affect the tear of either control stock. The reason for the low tear values in the middle of the range is not immediately apparent. It is possible that some constituent present in the crudes may exert this undesirable effect. Since the dip appears in repeated tests, it. signifies an actual trend. The tear resistance of Hycar OR shows great improvement with small additions of Thiokol FA, and the average tear across the whole range of the Thiokol FA-Hycar OR blends is comparatively high. This improvement in tear resistance of the Hycar OR stock by the addition of Thiokol FA has been demonstrated on a number of mixes. Such blends offer possibilities for obtaining better tear-resisting Hycar compounds. Blends of Thiokol FA and Perbunan show practically a linear increase as the amount of Thiokol FA increases beyond 10 parts.

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September, 1943

INDUSTRIAL AND ENGINEERING CHEMISTRY

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Figure 3. Swell (in 813 Fuel) and Tensile Strength of Thiokol FA Blends with Neoprene GN, Hycar OR, and Perbunan (Cured 60 Minutes at 298' F.)

COMPRESSION SET

Tables V and VI summarize data on the resilience and compression set of the various stocks. Under momentary distortion as measured by rebound, Thiokol FA shows a relatively high degree of recovery. However, under sustained compression it tends toward high set. Compression set measurements were run by A. S. T. M. method B (1) under constant deflection using plugs ll/sinches in diameter and '/s inch thick. A compression of 25 per cent w a ~uaed and the test assembly was aged 22 hours at 158' F.

990 TABLB

'Thioh,J Syn- Cure at PiasF.4. thetic, 298' F., ticity I'nrts Parts Min. Index

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Vol. 35, No. 9

INDUSTRIAL AND ENGINEERING CHEMISTRY

0

20 40

0 118

VI.

PROPERTIES' O F

THIOKOL FA BLEKDSWITH HYCAR OR15

Raw Modulus Stock at 300% T e n d c , Shore Corn- Lupke X;!onga- Hard- preasion ReAviaElonga- Elonga- Lb./ tion, 'i/a tion Sq. In. tion, ness Set bound tion gas 490

60

66.5 1005 1130

1050 1315 1340

. 4 S D WITH PERBUNAN

Volume Swell 813fuel

Acetone

T'hiokol FA-Hy car OR-15 Blends 660 66 1.0 100 47.5 1.0 490 70 100 46.5 420 72 100 44.0 1.5

11.0 10.0 8.3

20.8

Ethyl acetate

20.0 20,8

70 Hr. at 212' F. in Circa Light Process Oil HardCClb Swell nebs

23.0 20.0 18.5

38.0 36.0 33.0

-6.0 -6.9 -6.0

z2

38 0 33.0 36.0

-7.5 -2.0 -1.5

70 72 76

74 / I

90

10

20 40 60

0 122

4.50

565 930 1090

960 1265 1380

660 530 460

69 71 72

100 100 io0

36.5 36.5 35.5

1.0 1.5 1.5

12 3 11.0 11.0

Ci0.2 48.2

42 0 32.0 30 5

80

20

20 40 60

0 126

1100

,535 865 1030

875 1255 1420

780 640 530

68 70 71

100 100 100

31.5 31.5 32.0

1.0 1.0 1 6

12.5 12.6 12.5

122.2 107.2 83.7

57,o 44.5 -10 o

38.5 35.0 33.0

-4.0 -0.3 -0.3

70 73 74

GO

40

20 40 60

0 136

1200c

460 775 935

945 1400 1560

970 710 650

66 69 71

100 Y7.5 96.5

26 0 26.5 27.0

1.0 1.0 1.0

18.0 18.0 10.5

329,o 197. 0

76.0 66.0

96.0

39.0 36.5 36.0

-2.0 -2.0 -0.3

70 70 70

40

GO

20 40 60

0 148

lZOO+

500 775 945

1235 1860 1985

980 780 680

ti9

66

95.2 86.2 84.5

22.5 23.5 25 0

2.0 1.5 1.5

23.0 21.5 21.5

339.0 281.5 220.8

111.5 132.0 01 0

39.0 40.0 38.0

2.0 3.5 4 0

68 69 70

20 40 60

0.167

675 1045 1270

2120 2550 2630

69

79 6 67.6 60.1

20.0 20.5 21.0

1.5 2.0 1.5

26.0 27.0 25.0

413.3 300.1 259.9

145.5 127.0 105 0

44.0 42.0 42.0

5.0 5.5 5.5

67

b8

, 630

20 40

0.162

1200f

1010 1440 1885

2760 2770 2620

740 560 430

66 69 70

58.2 54.9 42.9

18.0 19.0 18.5

1.5 1.5 1.5

29.5 27 5 24.0

369.9 259.9 220.Y

146 123.5 107.0

40.5 39.0 38.0

5.5 6.5 8.5

66 69 70

20 40 60

0.158

1200f

1400 1930 1250

3060 2940 3050

620 470 440

67 69 70

31.6 23.1 17.7

16.5 15.5 14.6

1.5 2.0 1.5

30.5 29.5 30.5

254.7 18Y . 3 167.2

142 116 107.0

42.0 39.0 38.0

8.0 8.5 7.0

79

20 40 60

0.117

345

485 936 1140

835 1160 1265

Thiokol FA-Perbunan Blends 67 100 47.5 70 100 47.5 370 72 100 46.0

1.5 1.5 1.5

10.0 11.0 10.0

21 21 20

23.0 20.0 18.0

38.0 37.0 33.0

-5.5 -6.0 -7.0

20

0 122

325

485 Y 50 1190

800 1265 1405

680 4Y2 420

65 71 72

100 100 100

43.0 42.5 40.0

2.0 1.5 1.5

17.0

50 46 34

46.0 35.0 30.5

48.5 44.0 41.0

-4.0

14 5

-0.3 0

70 75

100 100 100

41 41 40+

2.5 2.5 2.5

20.5 21.5 17.0

76

59 50

64.5 47.5 41.5

60.0 48.5 47.5

-2.5 -3.0 +0.3

6G 70 74

64 ti5

20

10

80 90

1200f

60 0

100

100

0

90

10

40 ti0

0.5

660 500

li.O

240.9

67 70

68 69

73 74 76 il

20

0 144

390

510 895 1145

810 1200 1400

G60 480 410

66 70 72

20 40 60

0 174

410

385 890 1135

885 1175 1420

580 440 410

67 70 71

92.8 93.1 91.4

40 40 40.5

5.5 4.0 5.0

35.0 80.5 29.0

115 106

Y!,

106.5 81.0 70.5

77.0 68.0 66.5

5.0 5.5 5.0

20

0 189

YO0

1270 1465

1336 1770 1905

480 450 420

66 B9 70

84.5 72.8 72.6

40 41 41

7.5 6.0 6.5

40.0 35.0 32.0

134 122 112

114.5 102.0 90.5

84.0 17.5 (2.5

8.0 7.5 8.5

05

1450 1950

2145 2460 2405

400 4OO

68

1100

A50

09 70

62.8 48.6 41.7

41 42 41.4

10.0 10.0 10.0

44.5 41.5 41,s

i. 42 118 109

121.0 102.0 91.5

89.0 75.0 74.0

13.5 13.5 13.5

65 66 67

345

1980 2420 2480

2600 2620 2600

410 330 320

69 70 71

49.4 37.3 32.6

41.5 42.0 41.5

11.0 10.0 10.0

46.5 44.0 44.0

112 109 107

119.5 99.0 98.0

81.0 77.5 74.5

11.0 12. c5 13.6

07

260 20 0 236 40 60 See Table V for explanatory notes.

2280 2760 2740

2500 2800 2820

330 310 310

69

24.7 14.0 12.1

39.0 40.0 41.6

11.0 12.0 10.5

51.5 48.5 46.5

118 112

118.0 121.5 103.0

89.0 83.0 83.0,

18.5 18.:

ti9 ti!,

20.3

7U

80

20

(io

40

4il

60

40 60

40

375

00

10

IO

0

'1

880 700

70

i5.0

80

90

100

20 40 60

0 213

20 40 60

0 220

106

70

71

(50" C.). Resilience or percentage 1,eboundwas measured 011 the Lupke resiliometer ( 4 ) . The compression set of Thiokol FA is improved by blendiiig with the other synthetic rubbers. The amount required t o effect a noticeable change varies with the different synthetics. In a great many applications this high permanent set does not detract from serviceability. JVhere greater resistance to set is required, it can be obtained by the use of blends n.ithout sacrificing too much in solvent resistance. Thiokol FA is not generally recoinmended where resistance t o caoinpre$sioii set is a primary consideration in use.

11'

65

63 ti4

cib ti9

A summary of the low teinperature characteristics of thebe blends is shown in Table VII. The flexibility was-determined by mounting strips 4 X X l/la inch on sticks 3/4 x d / 4 inch in cross section, aging in dry air a t the temperatures shown, and pinching the samples with a gloved hand. This method gives a good qualitative index of the rate of stiffening of each sto&. OTHER PROPERTIES

FREEZE RESISTANCE

Tables V and VI include supplementary data on various properties for a series of cures. These data are included to give as complete a picture as possible of the properties of the blends.

In stocks containing no plasticizers, Thiokol F A shows better low temperature flexibility than Neoprene GK, Hycar OR-15, or Perbunan 26. The low temperature flexibility of Hycar OR-15 and Perbunan 26 is improved by blending n-it,h Thiokol FA.

PROCESSING. The addition of Thiokol FA to Hycar and Perbunan improves processing. Smce Xeoprene GN requires no additive to get smooth running stocks, no marked improvement was noticed in processing through the use of

SUMMARY

September, 1943

INDUSTRIAL AND ENGINEERING CHEMISTRY

l h d s . Tbe addition uf Seoi>reiir, Ilyesr, or l'erbunnn to Thiokol gives 3 tougher uncured stork wliich is an sdv:i.nt:igv for many processing operiltions.

gasoline I)IFFCRION. The diffusion of ari~~~~atin-blendeil tlirnogli blends of Thiokol FA :and other synthetics, esi,ressod in gmms per square inch per day, does not increase I i n e d y i r i t h the percentage composition of the blends. h a l l :uimints of the ot.her synthetics added to Tliiokol do not iiirreiw the diusion as much as if the increAse were linear.

Likewise, the addition of smaller anrounts of Thiokol to the otlw synthetics does not lover the diihsion 8 s muclr i ~ fwould i he expected from a linear relation. SWX,L IN SOLVENTS. For blen& of Thiokol FA and Xeoiiiene GN, the linear relation holds for percentage swell i i r 818 fuel, acetone, ethyl acetate, :and mrhon tetrachloride at T i m 1 1 temperature and Circo light process oil at 212" F. The volume swell of Thiokol-Hymr 11lmdsin 818 fuel and cirboo tetrachloride, nt room temperst.iire and in Circa light oil :it 212" F., increases linearly as the percentage of Hycar is increased. In acetone and ethyl acetate the percentage swell incresses linearly with increase in Hycar content until tlie 80 Hycar-20 Thiokol proportion is reached, where tiic s ~ e lholds l constant or perhaps deci.e;t*ea. This is probnbly tliw to the state of cure of the Hycm The vohime swell of Thiokol-P liaewly with increased percentages of Perbunan in 813 fuel at rooni temperature snd Circa tight oil itt ZIZa F. The rolume swell of these blends in aeetorre, ethyl acetate, ami carbon t.etiachloride does not follow a linear relation. The i'ereentzge swell of the hle~iilsis greater than would be experteil if the relation were linear. It should be pointed out that in tile ca8e of Neoprene Gii Tliiokol FA blends, whert: the s>~ell reletion is practically linrsr in all solvents, the difference in volume swell for different cures on any one blend is relatively smI1. In the case of the Elycar OR and Perbuiiau blends with Thiokol FA where tlir reistion is not linear, there i s n relatively large difference i i i tho volume swell between different.cures of the same blend. This leads to the belief that, in blends which swell more then would be expected, that one phme hw not reached a good state of cum. TENSILESTRENOTE. The tensile strength of the blends du uot change linearly with the coinposition. In all eases the tensile st.rength was lower than ~vouldlie expeeted from thc trnsile strength of the stocks blendwl. FREEZE REBISTANCE. The freeze rcsiatance of the blends l)ears practically a linear relation tu the Composition and the freeze resistance of the synthetic blended. TEARRESISTANCE.In Neopreni: GN-Thiokol FA blends the tear resistance decrease8 with the addition of Thiokol to eoprene and with the addition of Neoprene to Thiokol. he curve goes through minimurn in blends that are apivoximntely 50 per cent. Neoprene :wI 50 per cent Thiokol

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