CA1037195A - Thermoplastic elastomeric copolymers and terpolymers of tetrafluoroethylene and propylene and method of making the same - Google Patents

Abstract

ABSTRACT OF THE DISCLOSURE
Thermoplastic elastomeric copolymers of tetrafluoroethylene and propylene and terpoly-mers of tetrafluoroethylene, propylene and a cure site monomer are disclosed which have a substantially uniform composition, i. e., a substantially uniform molar ratio of monomeric units and a relatively high molar ratio of tetra-fluoroethylene units to propylene units within the range 1.0:0.11 to 1.0-0.54. The combination of high molar ratio of tetrafluoroethylene/propy-lene units, substantially uniform composition and good elastomeric properties is achieved by using a hybrid batch/continuous process wherein a reactor is initially charged with a mixture of tetrafluoro-ethylene, propylene and, optionally, a cure site monomer having a TFE/propylene molar ratio substan-tially higher than that of the polymer to be pro-duced, i.e., in the range 1.0:0.01 to 1.0:0.087.
The polymerization reaction is then initiated and a mixture of the same monomers is fed to the reac-tor at such a rate and in such proportions as to maintain the molar ratio of the unreacted monomers substantially the same as that in the initial charge to the reactor.

Description

~037~9S
The invention relates to a novel process for preparing thermoplastic elastomeric copolymers of tetrafluoroethylene and propylene, as well as terpolymers of tetraflurorethylene, propy-lene and copolymerizable cure site monomers, having a relatively high molar ratio of tetrafluoroethylene to propylene and a sub-stantially uniform composition. Because of the fact that the process of the invention produces polymers of relatively uniform composition, it is possible to produce thereby novel copolymers which exhibit elastomeric properties at higher molar ratios of tetrafluoroethylene to propylene units than has heretofore been possible.
~uring the past decade elastomers processible by thermo-plastic techniques have become of increasing commercial signifi-cance. They are being used in market areas which require some of their rather unique properties combined w~th the improved economics resulting from the simplified high speed processing techniques characteristic of the plastics industry. These thermo-plastic elastomers are useful in a variety of applications.
The thermoplastic elastomers of the prior art generally achieved their physical and chemical properties through a so-called "hard"
segment which can be characterized as a thermally labile physical crosslink which softens and flows under shear upon heating~ yet recovers its structure upon cooling. Thus the hard segment is ~03719~
analogous to the chemical cross-link of the thermosetting rubbers.
Examples of this type of thermoplastic elastomer are the styrene-isoprene or styrene-butadiene type of block copolymer. More re-cently, efforts to produce thermoplastic elastomers have concen-trated on copolymers of tetrafluoroethylene and various unsaturated monomers to take advantage of the known heat and chemical resistance of tetrafluoroethylene.
Copolymers of tetrafluoroethylene with ethylenically unsaturated monomers are known, and are disclosed, for example, in U.S. Patent No. 2~468,664 (~anford et al) granted to E~I.du Pont de Nemours ~ Company on April 26~ 1949 and British Patent No. 594,249 granted to Imperial Chemical Industries Limited on November 6, 1945.
The specific copolymers exemplified in these patents and the pro-perties disclosed indicate that when about one-half or more of the units present are derived from tetrafluoroethylene, the resultant copolymers are tough, non-resilient, high melting plastics. These patents also teach that when the tetrafluoroethylene units do not predominate, the resulting copolymers are low melting thermoplastic resins. It has been reported in the Journal of Polymer Science, Vol. 2, pages 2235-2243 (1964) that a copolymer of tetrafluoro-ethylene and propylene wherein the units derived from tetrafluoro-ethylene predominate exhibits a "rubber-like" character. However, this publication does not specifically define rubberlike as applied to such copolymers to include thermoplastic elastomers. Moreover, as shown in Figure 7 at page 2240 of the Journal of Polymer Science article, the copolymers of tetrafluoroethylene and propylene disclosed therein contain a maximum of about 60 mole percent of units derived from tetrafluoro-ethylene, whereas the tetrafluoroethylene-propylene copolymers of the present invention contain aminimum of 65 mole percent, de-sirably 65 to 90 mole percent, of units derived from tetrafluoro-ethylene. Hence, the copolymers of the present invention are outside of the scope of the disclosure in the ~ournal of Polymer Science article.
More recently, elastomers based on copolymers and ter-polymers of tetrafluoroethylene and certain olefinic compounds have been disclosed and claimed in U. S. Patent No. 3,467,635 (Brasen et al) granted to E. I. du Pont de Nemours ~ Company on September 16, 1969. This patent discloses that poly~ers of tetra-fluoroethylene with such olefins as ethylene, propylene, butylene and isobutylene~ as well as a cure site monomer, if desired are or may be converted to elastomers. More specifically, this patent teaches that polymers which are convertible to elastomers contain tetrafluoroethylene units and olefin units in a molar ratio of about 1:0.6 to 1:1.2. This indicates that the copolymers of tetrafluoro-ethylene and propylene contain a maximum of about 62.5 mole percent ; 20 of units derived from tetrafluoroethylene. The above-cited patent further teaches that the molar ratio referred to above must be observed in order to obtain polymers of tetrafluoroethylene and olefins which exhibit elastomer characteristics and that polymers containing higher ratios of tetrafluoroethylene to olefin are not elastomeric.
It has now been surprisingly and unexpectedly discovered that by using the novel process of the present invention it is I 1~2049-A
.

1~37195 possible to prepare copolymers of tetrafluoroethylene and propy-lene, as well as terpolymers of tetrafluoroethylene, propylene and a cure site monomer, containing a minimum of about 65 mole percent tetrafluoroethylene units and which exhibit elastomeric characteristics when cured, and even in some cases, in the gum or uncured state. Thus the copolymers and terpolymers of the present invention are distinctly different from the copolymers and terpolymers of the prior art. Moreover, the elastomers of the prior art have been found to be deficient in several respects, e.g " elasticity, processability and/or chemical resistance. The thermoplastic elastomers of the present invention have been found to exhibit satisfactory elastic and processing characteristics, as well as good chemical and heat resistance. Thus, for example, they can be used in the manufacture of heat and solvent resistant flexible tubing and hose or wire coatings. The thermoplastic elastomers can also be used in the manufacture of gaskets, O-rings, and other seals7 or for diaphragms or components of fluid-handling equipment such as pumps, compressors, hydraulic systems, dry-cleaning machinery and the like.
The term "elastomer" as used in the present specification and claims refers to a material which, when stretched to twice its length at room temperature, held for one minute and then released retracts to less than 1,5 times its original length within one minute. This definition corresponds essentially to the definition of a rubber in ASTM Standards, Part 28 D1566 (1973). The amount by which the material fails to retract to its original length when subjected to this test is referred to below as "permanent set"
and is expressed as a percentage of the original length.

- 1037~95 Accordingly it is an object of the present invention to provide new thermoplastic Plastomers having a high weight propor-tion of fluorine. It is another object of the invention to provide new thermoplastic elastomers based on copolymers of tetrafluoro-ethylene and propylene, and optionally cure site monomers, whichcontain high mole percentages of tetrafluoroethylene units, i.e., at least 65 mole percent tetrafluoroethylene units. It is a still further object of the invention to provide polymers having such a high content of tetrafluoroethylene units, which polymers are curable to elastomers having improved elasticity, processability and chemical resistance. It is a still further object of the invention to provide a novel process whereby such polymers can be prepared. Other objects of the invention will be apparent to those skilled in the art from the detailed description of a number of embodiments of the invention given below.
As conducive to a clearer understanding of the present invention, it may be pointed out that in the copolymerization of tetrafluoroethylene and propylene, as well as in the terpolymeriza-tion of tetrafluoroethylene, propylene and a cure site monomer, in most cases the monomers do not enter the copolymer in the same mole ratio as they are present in the monomer mixture. In this regard, the literature indicates that the best available values of the re-activity ratios for TFE and propylene are OoOl and 0.1, respectively These values indicate a high alternating tendency of the monomers, i.e., a polymer radical ending in a TFE unit will preferentially add a propylene monomer unit and conversely. Thus when a mixture containing a major amount (mole fraction) of TFE and a minor amount 1'~204'3-~

of propylene is polymerized, the copolymer will usually contain less TFE than the monomer mixtureO For example, if a monomer mixture containing 60 mole percent of TFE and 40 mole percent of propylene is charged to the reactor, the average composition of 5 the product may contain of the order of 55 mole percent of TFE
units~ As the TFE cont~nt of the monomer mixture charged to the reactor is increased, the difference between the TFE content of the feed and the TFE content of the product increases. Moreover, the TFE content of the intially formed copolymer is substan-tially below the average TFE content of the product formed ata conversion of say 10% to 15%o Thus a batch polymerization of tetrafluoroethylene and propylene produces a product which is of non-uniform composition, i.e., the TFE/propylene ratio o the copolymer formed increases substantially during the course 15 of the reaction. The non-uniform copolymers thus produced have inferior elastomer~ic properties.
A similar effect is obtained when a conventional con-tinuous process is employed. The copolymer initially formed has a TFE unit content substantially below that of the TFE content of the feed mixture. As the reaction proceeds, the TFE concentra-tion of the reaction mixture increases relative to the propylene concentration thereof and copolymer chains are produced having increased proportions of T~E units. The final product obtained in such a continuous process may have an average ratio of TFE/propy-lene units approaching or equal to the TFE/propylene ratio of the feed mixture, but the product will still have a non-uniform composition.
Applicant has found that copolymers of tetrafluoroethyler.e and propylene, as well as terpolymers of tetrafluoroethylene, propy-lene and cure site units, of substantially uniform composition,a high fluorine content and improved elastomeric properties oan be obtained by using a novel hybrid batch/continuous process.
In accordance with applicant's process a polymerization reactor is initially charged with a mixture o tetrafluoroethylene and propylene, which may or may not contain a cure site monomer, and wherein the ratio of TFE/propylene is of the order of 1:0.01 to 1:0.087. The polymerization is then initiated and thereafter the reactor is fed, continuously or incrementally, with a monomer mixture having a TFE/propylene ràtio within the range 1:0.11 to 1:0.54, preferably 1:0.25 to 1:0.43 and substantially equal to the TFE/propylene ratio in the polymer initially formed in the reactor. The feed mixture is introduced into the reactor at such a rate as to maintain the pressure within the reactor substantially constant to cause the monomers within the reactor to be replenished at approximately the same rate as they are consumed within the reactor. As shown in the Examples given below, the polymers thus i produced have a substantially uniform composition, a TFE/propylene molar ratio in the range 1.0:0.11 to 1.0:0.54 and improved elasto-- meric properties.
In the case of copolymers of tetrafluoroethylene and propylene, the copolymers contain from 65 to 90 mole percent , . .
1037~9S
TFE units. The preferred copolymers contain from 70 to 80 mole percent TFE units, since such copolymers provide a good balance of physical and chemical properties and processing characteristics.
The thermoplastic copolymers are useful as such for some application or, as indicated in some of the Examples given below, they may be cross-linked to yield products having impro~ed elastomeric proper-ties O
The terpolymers of the invention may contain 0 to 10 molepercent, based on the total amount of monomeric units, of cure site units and like the copolymers desirably have a TFE/propylene unit ratio of 1.0:0.11 to 100:~.54. The preferred terpolymers have a TFE/propylene unit ratio of 1.0:0.25 to 1.0:0.43.
Monomers which are copolymerizable with tetrafluoro-; ethylene and propylene to provide cure site ~nits are known in the art and in general one or more of any of these known curesite monomers can be used in preparing the polymers of the present invention which contain such cure site units. Such cure site units are disclosed, for example, in U. S. Patent 3,467,635 and the patents cited therein. As is known in the art, the cure site units are commonly olefinically unsaturated organic compounds having functional groups such as carboxyl, halogen, epoxy or non-polymerizable olefinic groups through which the polymer can be cured in known manner. Typical cure site monomers are chloroethyl-vinyl ether, divinyl carbitol, vinyl chloroacetate, allyl chloro-acetate, allyl glycidyl ether, and chloroethylacrylate.
In accordance with a preferred embodiment of the presentprocess, the polymers of the invention are prepared by an emulsion polymerization utilizing a redox initiator system. A suitable reactor, e.g., a horizontally or vertically stirred reactor or 10371~5 closed autoclave is charged with an inert liquid medium, buffer, emulsifier, catalyst and reducing agent. As described above, the reactor is then charged with a monomer mixture have a suffi-ciently high concentration of tetrafluoroethylene to produce an S initial polymer with the desired TFE/propylene unit ratio. The proportions of monomers required to ?roduce an initial polymer of a given desired composition can be determined by a preliminary test at a low conversion. The polymerization is carried out at a temperature of 5C. to 120C., preferably 40C. to 80C., and at a pressure of 100 p.s.i.g. to 1000 p.s.i.g., preferably 250 to 350 p.s.i.g.
The polymerization is initiated by introduction of a suitable initiator into the reactor. When polymerization has started as indicated by a small pressure drop, a monomer feed mixture, having a composition corresponding substantially to that of the polymer initially formed within the reactor, is fed to the reactor continously or incrementally whenever a small pressure drop of say 10 to 15 p.s.i.g. occurs in the reactor. In this way the monomers within the reactor are replenished at approximately the same rate as that at which they are consumed, thereby maintaining an essentially constant monomer composition and pressure in the reactor and producing a polymer of uniform composition. The poly-merization reaction is terminated by venting the unreacted monomers, and the copolymer product is discharged and isolated using known methodsO

192~49-~

1~37i95 In the emulsion or suspension polymerization used to produce the polymers of the present invention, conventional free-radical initiators, such as, for example, peroxides, azo compounds, metal and ammonium persulfates, permanganates, or peroxydiphosphates may be used as initiatorsO When an azo com-pound is employed, a water-soluble azonitrile is suitable, such as, for example, 4-tert-butylazo-4-cyanovaleric acid. Water-soluble organic peroxides, eOg., disuccinic acid peroxides can also conveniently be employed. The preferred initiators in the practice of the present invention are the alkali metal and ammonium persulfates. Water, lower alkanols, e.g., tertiary butyl alcohol, and trichlorotrifluoroethane may be employed as inert media, the latter in conjunction with organic soluble initiators, such as azo-bis-isobutyronitrile, benzoyl peroxide or tert-butyl peroxypivalate and tert-butyl peroxide. Deionized, deoxygenated water is the preferred medium. Emulsifiers which can advantageously be employed are the fluorocarbon or chlor-fluorocarbon carboxylic acids or sulfonic acids or their alkali metal or ammonium salts or alkali metal or ammonium aliphatic alcohol sulfates. A preferred emulsifier in the present invention is ammonium perfluoro-n-octanoate. A buffer such as an alkali metal or ammonium hydroxide, carbonate, or phosphate may be used.
Reducing agents which may conveniently be employed are the alkali metal sulfites or bisulfites. A preferred reducing agent is sodium sulfite. Other ingredients may optionally be employed;

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1~37195 such as, for example, a modifier or chain transfer agent, e.g., hydrogen, a hydrocarbon or hydrocarbon derivative, an aliphatic or aromatic mercaptan, a primary, secondary or tertiary alcohol or a halog~nated aliphatic or aromatic compound, a thickener, 5 suspending agent, or protective colloid, such as polyvinyl alcohol or a polymer or copolymer of acrylic acid or maleic anhydride or their alkali metal or ammonium salts.
In order to point out more fully the nature of the present invention, the following Examples are given to illustrate 10 applicant's novel process for making the copolymers and terpoly-mers of the invention and the novel properties of the products thus obtained.
Example _l Terpolymer of tetrafluoroethylene, propylene and 15 2-chlorovinyl ethyl ether in a molar ratio of 1.0/0.4/0.03 A stirred stainless steel reactor of 86 liter capacity was charged with 2860 g of tetrafluoroethylene, 96 g of propylene, 20.9 g of 2-chloroethyl vinyl ether, 64.5 liters of deionized water~ 127.3 g of ammonium perfluorooctanoate, 19309 g of anhy-20 drous sodium carbonate, and 38.4 g of sodium sulfite. Thus theintial monomer ratio of tetrafluoroethylene (TFE), propylene (Pr), and 2-chloroethyl vinyl ether (CEVE), in mole percentages, was 92.0/7.4/0.6. Polymerization was initiated at 65C. and 20 atm.
gauge pressure by injecting a solution of 38.3 g of ammonium 25 persulfate in 420 ml of water. The partial pressures of ~he gaseous monomers were maintained essentially constant by continuousl 192~49-~

feeding a mixture of TFE and propylene, 70.2/29.8 by mole, until a total of 12020 g of that gas mixture had been chargedO During the same time period (12.8 hours), 387 g of CEVE was continuously pumped into the reactor at such a rate as to maintain the feed composition of TFE, propylene, and CEVE at 68.5/29.1/2.4 by mole.
An additional 20 g of ammonium persulfate and 10 g of sodium sulfite (total) were charged, in four equal increments, as 5%
aqueous solutions, over the reaction period. When the polymer content of the latex had reached 705%, another 129.3 g of ammonium perfluorooctanoate was added as a solution in 400 ml of water.
Samples of latex were withdrawn periodically, and the composition of the isolated terpolymer was calculated from its carbon and chlorine analyses.
The results as set orth below showed excellent uniformity in the composition of the product, i.e., very narrow composition distribution.
Sample NoO I II III
Time, hrs. 207 9.1 12.8 % Solids 3.3 11.0 15.6 % C 33.26 33.32 33.26 % H 1.98 1.88 1.68 % Cl 1.04 1.01 0.89 Mol % TFE 69.7 69.6 69.8 Mol % Prop~lene 27.8 28.0 28.1 Mol % CEVE 205 204 2.1 ~2 . .

It should also be noted that the polymer analyses were close to the monomer feed composition. In other words, although the composition of the terpolymer produced was quite different from the composition of monomer present in the reactor, both the monomer and polymer compositions were maintained essentially constant at all times by replenishing the monomers at the same rate and in the same molar ratio as they were consumed. Periodic monitoring of the gas phase composition by gas chromatography con-firmed that the monomeric TFE content remained essentially constant at 92-95 mol %. At the final solids content of 15.6%, the polymer yield was 12350 g. The rubbery product was compounded with 20 p.h.r.
(20 parts per hundred parts of rubber) of medium thermal carbon black (STERLING MT , G.L. Cabot, Inc.), 5 p.h.r. of dibasic lead phosphite (DYPHOS , NL Industries Inc.), 1 p.h.r. of stearic acid, and 1.3 p.h.r. of hexamethylenediamine carbamate (DIAK No. 1, E.I. du Pont de Nemours & Co.). Sheets were pressed out for 30 min.
at 170C., compression plugs for 45 min. at 170 C. This was followed by a stepwise postcure in an air oven for 4 hours at 200-400F. and then 24 hours at 400 F. (204C.). Physical properties of the cured rubber were as follows: Shore A hardness 80, 100% modulus 1115 p.s.i.
tensile at break 2655 p.s.i., elongation 135 %, permanent set after 100% extension 19%, permanent set at break 24%, compression set 41%
after 22 hours at 400 F. Solvent swell (volume increase after im-mersion for one week) was determined to be as follows: Methanol (ambient temperature), 0%; Methyl ethyl ketone (ambient temperature), 43%; Tetrachloroethylene (ambient temperature), 15%; SKYDROL 500 A
(Isooctyl dipheny] phosphate, a fire resistant hydraulic fluid manu-factured by Monsanto Chemical Co.; 250 F.), 15%; ASTM Oil No. 3 (250 F.), 2%.

*Trademark -Exam~e 2 ~03719S
Terpolymer of tetrafluoroethylene, propylene and2-chloro~thyl vinyl ether in 2 molar ratio of 69.5/28.4/2.1 Another run was carried out substantially as in Example 1.
The mole ratio of the gaseous monomers in the reactor, as monitored by gas chromatography, was maintained at a steady-state value of about 94.6/5.4 with respect to tetrafluoroethylene and propylene.
The feed mixture was maintained at a mole ratio of 69.2/28.3/2.5 with respect to TFE, propylene and 2-chloroethyl vinyl ether, and the average (cumulative) terpolymer composition was 69.5/28.4/2.1 by mole. Samples were taken periodically of the latex and of the gas phase. Analytical results were as follows:
Sample No. I II III
Time, hrs. 1.4 t.l 12.3 % Solids in Latex lo9 9~5 14~0 Mol % TFE 68.8 68.7 69.5 Mol % Propylene 28.2 2808 28.4 Mol % CEVE 300 2.5 2.1 Gas Samples Mol % TFE 94.58 94~ 67 94~ 62 Mol fO Propylene 5.42 5.33 5.38 These data again demonstrate remarkable constancy of monomer and terpolymer compositions over the duration o the experimentS and thus assure excellcnt product uniformity.

~ 1')204')-A
-. . ;

Example 3~ ~0~195 Terpolymer oE tetrafluoroethylene, propylene and ..
~ 2-chloroeth 1 vin l ether at a mole ratio of 1.0/0.466/0.042 .Y ~
A terpolymer containing 66.4 mol % TFE, 30.9 mol %
propylene, and 2.8 mol % 2-chloroethyl vinyl ether was prepared in a manner similar to that described in Example l, except that the initial mole ratio of TFE, propylene and CEVE in the reactor was 90.9/8.6/0.5 and the subsequent feed ratio was 66.4/31.1/2.5.
The reaction was carried out at a temperature of 152F. and a ~ressure of about 330 p~s~iog~ for approximately twelve hours.
Initiator solutions containing a total of 45.9 g of sodium sulfite and 53.3 g of ammonium persulfate were injec~ed over that period.
Samples of the latex were withdrawn periodically and analyzed until the final solids content of 15.4% had been reached. The results of the analyses were as follows:
Sample No. I II III
Time, hrs. 2,35 7.4 11.7 % Solids 2.25 9.0 15.4 Mol % TFE 67.8 65.6 66.4 Mol % Propylene 29.7 31.9 31.0 Mol % CEVE 2.5 2.5 2.6 The final product was compounded with 20 p.h.r. of STERLING MT, 5 p oh .r. of DYPHOS, 1.p.hOrO of stearic acid, and 1.3 p.h.r. of DIAK No. 1 and cured as in Example 1. Physical properties were as follows: Tensile strength, 2200 p o s ~
Elongation, 240 %; 100% Modulus, 560 p~s~io; Shore A hardness, 73;

. . 1~;
,.

1'32049-~

~ 3719S
Permanent set after 100 % extension, 7 %; Compression set after 22 hours at 400Y., 26 %, Solvent swell (volume increase after immersion for one week~ was determined to be as follows: Butyl acetate (ambient temperature), 83 %; Tetrachloroethylene (ambient temperature), 27 %; SKYDROL 500 A (Isooctyl diphenyl phosphate, a fire resistant hydraulic fluid manufactured by Monsanto Chemi-cal Co.; 300F.), 31 %; ASTM Oil No. 3 (300Fo)~ 15 %~
Example 4 Terpolymer of tetrafluoroethylene, propylene and

2-chloroethyl vinyl ether at a molar ratio of 1.0/0 43/0.03 A terpolymer containing 68.5 mol % TFE, 29.4 mol %
propylene, and 2.1 mol % 2-chloroethyl vinyl ether was prepared similarly as described in Example~l, except that the initial mole ra~io of TFE, propylene and CEVE in the reactor was 93.2/6.35/0.45 and the subsequent feed ratio was 68.0/29.5/2.5.
The reaction was carried out at a temperature of 152Fo and a pressure of about 290 p.s.i.go for 14 hours. Initiator solutions containing a total of 48.4 g of sodium sulfite and 5803 g of ammonium persulfate were injected over that period. Samples of the latex were withdrawn periodically and analyzed until the final solids content of 15 % had been reachedO The results of the analyses were as follows:
Sample No. I II III
Time, hrs. 2.4 7.3 14.0 % Solids 1075 8.4 15.0 Mol % TFE 68.5 69.0 68.5 Mol % Propylene 29.7 28.9 29.4 Mol % CEVE 1.8 2.1 2.1 ~6 ~ 192049-A

The final product was compounded with 20 p.hOr. of STERLING MT, 5 pOh.r. of DYPI~OS, 1 p.h.r. of stearic acid, and 1.3 p.h.r. of DIAK No. 1 and cured as in Example 1. Physical properties were as follows: Tensile strength, 2185 p.s.i.;
Elongation, 220 %; 100% Modulus, 700 p.s.i.; Shore A hardness, 75;
Compression set after 22 hours at 400F., 29 %; Permanent set after 100 % extension, 8 %. Solvent swell (volume increase after immersion for one week) was determined to be as follows: Butyl acetate (ambient temperature), 66 %; Tetrachloroethylene (ambient temperature), 21 %, SKYDROL 500 A (Isooctyl diphenyl phosphate, a fire resistant hydraulic fluid manufactured by Monsanto Chemical Co.; 300F.), 26 %; ASTM Oil No. 3 (300F.), 13 %.
Example 5 Terpolymer of tetrafluoroethylene, propylene and 2-chloroethyl vinYl ether at a molar ratio o~ loO/0~32/0~58 .. . . . . . _ A terpolymer containing 72.7 mol % TFE, 23.1 mol % propy-lene, and 4.2 mol % 2-chloroethyl vinyl ether was prepared in a manner similar to that described in Example 1, except that the initial mole ratio of TFE, propylene and CEVE in the reactor was 94~1/4~9/1~0 and the subsequent feed ratio was 69~5/25~5/5~0~
The reaction was carried out at a temperature of 151Fo and a pressure of about 305-325 p.s.i.g~ for 10~5 hours. Initiator solutions containing a total of 63~4 g of sodium sulfite and 88.3 g of ammonîum persulfate were injected over that period. Samples of the latex were withdrawn periodically and analyzed until the ~7 1~2~49-A
. ,-~
1037~9S
inal solids content of 17 % had been reached. The results of the analyses were as follows:

¦ Sample No. I II III
Time, hrs. 1 0 3.6 9 6 % Solids 3 8 9.6 17 0 Mol ~/O TFE 74.2 74.8 7205 Mol % Propylene 21.6 21.9 23.4 Mol % CEVE 4.2 3.3 4.1 ¦ The final product was compounded witll 5 p.h.rO of DYPHOS
! and 1 p.h.rO of DIAK No. 1. Flexible sheets were pressed out at 350F. for 30 minutes and postcured for 24 hours at up to 200C.
(392F.). Physical properties were as follows: Tensile strength, 2110 p.s.i.; Elongation, 170 %; 100% Modulus, 1060 p.s.i.;
Permanent set after lO0 % extension, 9 %.
Solvent swell (volume increase after immersion for one week) was determined to be as follows: Ethyl acetate (ambient temperature), 73 %; Tetrachloroethylene (ambient temperature), 20 %; SKYDROL 500 A (Isooctyl diphenyl phosphate, a fire resistant hydraulic fluid manufactured by Monsanto Chemical CoO; 250F.), 19 %
Example 6 Copolymer of tetrafluoroethylene and propylene in a molar ratio of 76/24 .. . . _ _ A twenty-liter horizontal autoclave was charged with 15 liters o deionized water, 75 grams of ammonium perfluorooctanoate, 75 grams of sodium hydroxide, and 3 g. of sodium sulfi~e. The reactor was evacuated, purged with nitrogen, and re-evacuated.

1~2~4~-~
, ~

Then 458 g. of tetrafluorocthylene and 8 g. of propylene was charged, and the reactor was heated to 60C. Then a solution of 6 g. of ammonium persulfate in 100 ml~ of water was injected.
The polymerization was carried out at a pressure of 240-250 p.s.i.g. An essentially constant pressure and monomer composi-tion was maintained by feeding a mixture of TFE and propylene, 75l25 by mole, whenever a pressure drop of 10 p.s.i. had occurred.
The monomer composition was monitored by gas chromatography, using a column packed with a styrene-divinyl benzene resin (PORAPAK Q).
The rate of reaction was determined from the rate of pressure drop in the reactor and weight loss of the monomer reservoir. After ~.75 hrsO, when 1,600 g. of the 75/25 TFE/propylene gas mixture had been fed, the reaction was terminated by venting the unreacted monomer and discharging the polymer dispersion. The rubbery product was coagulated, washed and dried. The yield was 1,653 g. of co-polymer, which was analyzed to contain 31.4% carbon and 1.5%
hydrogen. Thus the product contained about 88~/o TFE by weight, or 76 mol % TFE. The material could be compounded on a rubber mill.
Samples of the gum stock were pressed out into sheets at 175-250C.
and 8,000 lbs. pressure or extruded at 250-325C. through a screw-type extruderO Physical properties and resistance to solvents, fuels, lubricants, and hydraulic fluids of this Example and Examples 7 and 8 are shown in Table I below. A specimen immersed in 90% nitric acid for 4 weeks showed no signs of deterioration.
The preparation was repeated, except that the pressure was ~ Tratl~JnA~K

,. , 19~049-A

325-335 p.s.i.g. at 60C~ ~ and the reactiDn time was 4~5 hrs.
The product (l,542 g. yield) was found to contain about 75 mol %
tetrafluoroethylene (i.e., 87% by weight) and 26 mol % propylene (13% by weight) from the following elemental analysis: Carbon, S 31~90%; Hydrogen, l.93V/o; Fluorine, 66~09~/o~
Example 7 Copolymer of tetrafluoroethylene and propylene in a molar ratio of 69/31 Another copolymerization was carried out substantially as in Example 3, except that the initial monomer charge consisted of 456 g~ TFE and lO g. propylene, and l,400 g. of a 65/35 mixture (by mole) of TFE and propylene was fed incrementally over a period of 6~75 hrs. at 55-60C. and 270-280 p~s~i~g~ The product was 1~527 g~ of a rubbery copolymer containing about 69 mol % TFE.
15 Properties of the product of this Example are compiled in Table I below.
Example 8 Copolymer of o~r1f1uoroethylene and propy-l-e-ne in a molar ratio of 83/17 Another copolymerization was carried out substantially as in Example 6, except that the initial monomer charge consisted of approximately 466 g. TFE and 4 g. propylene, and l,600 g. of an ; 80/20 mixture (by mole) of TFE and propylene was fed incrementally over a period of 4. 8 hours at 60-65C. and 300-310 p.s.i.g. l`he product was l,5ll g. of a tough rubbery copolymer containing about 83 mole % TFE. Properties are given in Table I belowO

:

192()~9-~

103719~;
Table I
"Gum Stock Properties o~ TFE-Propylene CopolYmers (Unc~
Example NoO 6 7 3 TFE Content, mole % 76 69 83 Tensile Strength,psi. 1590 860 2030 Elongation, % 360 490 230 100% Modulus, psi650 150 1275 ~ Duro (Shore A) 91 63 92 :., Solvent Swell (Volume Increase) Acetone(7 days, 77Fo) 24 35 9 Toluene(7 days, 77F.) 14 14 0 ESSO EXTRA(7 days, 77F.) 13 12 0 Tetrachloroethylene (7 days, 77F.) 11 22 -2 Butyl Acetate(7 days, 77F.) 24 60 3 : 15 Styrene (7 days, 77F.) -- 6 --ASTM Oil #3 (7 days, 300 F.) -- -16 --SKYDROL 500A (7 days, 300Fo) 0 -17 --(Isooctyl diphenyl phosphate) By comparison, an uncured 51/49 TFE/propylene copolymer had the following physical properties (gum stock):
Tensile Strength, psi 430 Elongation, ~/O 670 Duro (Shore A) 53 100% Modulus, psi 140 Tfa~narl~ 2 1 .

1 '3 ' ', Copolymers containing about 50 mol ~/O of propylene swelled approximately 50-60% in toluene or high-octane fuel (ESSO EXTRA) and over 70% in tetrachloroethylene within 24 hours. Some speci-mens disintegrated completely on prolonged immersion in solvents, particularly acetone or ethyl acetate. All 50/50 copolymers were completely soluble in a mixture of acetone and CC12FCClF2 (50/50 b.v.), whereas most of the polymers of higher TFE content could no~ be dissolved.
Examples 9 to 11 Copolymers of tetrafluoroethylene and propylene in molar ratios of 69/31 76/24 83/17 , These Examples illustrate the heat resistance of the copolymers of the present invention. Ln these Examples, samples of TFE/propylene copolymers containing 69, 76 and 83 mole percent TFE, respectively, were prepared in accordance with the procedure described in Example 6 and aged at 400F. for a period of up to 6 months to determine the effect of heat aging on the physical properties of the copolymers. Test results are shown in Table II.

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Examples 12-13 1037195 Copolymers of tetrafluoroethylene and propYlene in molar ratios of 69/31 and 76/24 These Examples illustrate the electrical properties of the thermoplastic elastomers of the pre~ent invention. In these Examples, copolymers of TFE/propylene containing 69 mole % and 76 mole % of tetrafluoroethylene, respectively, prepared as indicated in Examples 6 and 7, were tested for electrical proper-ties. Test results were as follows:
Example No. _ l Copolymer TFE/Propylene (Mole % ratio) 69/31 76/24 Dissipation Factor (1 mc) 0.0346 0.0367 Dielectric Constant (1 mc) 2.25 2.44 Arc Resistance, Seconds 82,6 124 Dielectric Strength (volts/mil) 243 280 Volume Resistivity (ohm-cm) 1.6 x 1014 2.9 x 1014 Surface Resistivity (ohm) 1.6 x 1014 1.6 ~ 10 The above data indicate that the copolymers of the present invention exhibit satisfactory electrical properties.
Example 14 Copolymer of tetrafluoroethylene and propylene in a molar ratio of 76/24 A stirred stainless steel reactor of 86 liter capacity was charged to 75 % of its volume with deionized water (64.5 1) containing about 0.5 p~p.h. of technical grade ammonium perfluoro-octanoate (3M Erand Fluorochemical Surfactant FC-126, Minnesota Mining & Mfg. Co.; 319 g) and 0.5 p.p.h. of sodium hydroxide 192U4~

1037~9S
(319 g). The reactor was sealed, flushed with nitrogen, evacuated, and then pressurized with a gas mixture containing 99.0 mol % of tetra~luoroethylene and 1.0 mol % of propylene, to approximately 300 p.s.i.g. at 145F. Polymerization was initiated by injecting 31.4 g of ammonium persulfate and 31.1 g of sodium sulite as separate, approximately 6 % aqueous solutions. As the polymeriza-tion proceeded, the pressure in the reactor was maintained essen-tially constant by continuously feeding a gas mixture containing ; 76 mol % TFE and 24 mol % propylene until the polymer solids content of the latex was about 22 %. The feed composit~ n of 76/24 by mole was chosen so as to replenish each of the monomers in the reactor at approximately the same rate and in the same mole ratio as they were being consumed, since separate experi-f ments had established that the 99/1 monomer mixture originally charged would produce a copolymer with an initial composition of about 76/24. The product was isolated by coagulation of the latex, filtering, washing and drying. Analysis indicated a copoly-mer composition of 76.5 mol % TFE and 23.5 mol % propylene. The thermoplastic, rubbery material appeared to be highly homogeneous.
This material was blended with another batch of material made in a similar run and the blend was molded to produce prac-tically colorless, transparent, flexible sheets by subjecting it to a pressure of 700 p.s.i. at 325F. for 15 minutes. Some specimens from these sheets were tested in the original form;
i.e., not crosslinked. The remainder of the sheets were exposed ~3jt~

to gamma-radiation from a cobalt-60 source for 7.5 hours, at an average dose rate of about 2.2 megarads per hour, at ambient temperature, in a nitrogen atmosphere. Properties before and after irradiation are tabulated below.
The irradiated polymer showed significantly improved modulus retention, dimensional stability, elastic recovery, and compression-set resistance at elevated temperatures (up to about 400F.). It also offered greatly improved resistance to stress cracking in hot oil; e.g., ASTM Oil No. 3 at 250 F.
Original Irradiated Tensile strength, p.s.i. 2400 2470 Elongation, % 395 275 Hardness, Shore A 95 97 100% Modulus, p.s.i. 890 1045 200% Modulus, p.s.i. 1125 1450 300% Modulus, p.s.i. 1675 ---Permanent set after 100% extension, % 43 48 Permanent set after break, % 310 180 Compression set after 22 hrs. at 250 F.87 27 Solvent Swell (Volume increase after one week at room temperature, %) Butyl Acetate 8 9 Toluene 4 2 Tetrachloroethylene 4 . , 1'32049-A
.. . .

1037~9S
Propert~es after heat aging in air for one week at 450F~ -Tensile strength, p.s.i.2790 2280 Elongation, % 425 285 . 100% Modulus, p.s.i. 760 995 200% Modulus, p.s.i. 925 1350 300~h Modulus, p.s.i. 1405 ~~~
Permanent set after break, % 400 200 Example 15 Copolymer of tetrafluoroethylene and propylene in a molar ratio of 1.0/0.397 A copolymer containing 71.6 mol % TFE and 28~4 mol %
¦ propylene was prepared in a manner similar to that described in Example 11, except that a mixture of TFE and propylene, about 70/30 by mole, was continuously fed to a reactor which had initially been charged with TFE and propylene in a mole ratio of slightly under 99/1. The copolymer was pressed into sheets, which were then exposed to gamma-radiation from a co~alt-60 source at dosages of 5 and 17 megarads, respectively. Properties were as follows:
. Ori~inal Irradiated Irradiated ' (5 Mr) (17 Mr) Tensile strength, p.s.i.1355 1820 2005 Elongation, Z 440 400 280 Hardness, Shore A 86 87 88 1 100% Modulus, p.s.i. 370 390 540 200% Modulus, p.s~i. 475 540 9O0 300% Modulus, p.s.i. 725 890 --400% Modulus, p.s.i. 1200 1820 --Permanent set*, % 12 13 7 ~After 100% extension, measured within one minute after release 1~371'~S

Example 16 Terpolymer of Tetrafluoroethylene, ~ropylene and diethylene glycol divinyl ether at a molar ratio_ f 1.0/0.41/0.044 . _ A twenty-llter reactor was charged with 420 g of tetra-fluoroethylene, 4.0 g of propylene, and 45 g of diethylene glycol divinyl ether, representing an initial monomer mole ratio of 91.7/2.1/6.2, in an emulsion system containing 30 g of ammonium perfluorooctanoate and 45 g of sodium carbonate in 15 1 of de-ionized water. The reactor was heated to 60C. and 7.5 g of sodium sulfite and 15 g of ammonium persulfate were injected, as separate solutions, in 50 ml of water each. As the polymerization progressed 1700 g of a gas mixture containing about 1400 g of tetrafluoroethy-lene and 300 g of propylene was fed continuously over a 3.5-hour period, and two more increments of 45 g each of diethylène glycol divinyl ether were added during that time. The overall mole ratio of the monomers charged was 69.0/27.8/3.2. Coagulation of the latex yielded 181S g of polymer. Analysis of the product was con-sistent with an approximate composition of 69 mol % TFE, 28 mol %
propylene, and 3 mol % of diethylene glycol divinyl ether; calc.
34.50 % C, 2.46 % H, 61.36 % F, and 1.68 % 0; found 34.46 % C, 2.15% H, and 60.10 % F. A tough, flexible, partially crosslinked sheet was prepared by subjecting the material to hydraulic pres-sure for 30 minutes at 100C. The Shore A hardness was 97, the tensile strength 1145 p.s.i., the elongation 90 %, and the permanent set at break 32 %.
~' 1~2049-A
. . .

Example_17 Copolymerization of tetrafluoroethylene, propylene and dieth lene 1 col divin 1 ether at a monomer mole ratio of 92/5/3 . ~ . ~. _ Y
~ A terpolymer was prepared in a manner similar to tha~
described in Example 16, except that the initial composition of the monomer mixture in the reactor was 92 mol % TFE, 5 mol %
propylene and 3 mol % diethylene glycol divinyl ether and a gaseous mixture of 68 mol % TFE and 32 mol % propylene was fed continuouslyO Analysis indicated that the copolymer contained approximately 69 mol % TFE (33.85 % C, 2.80 % H, and 64.12 % F).
The rubbery polymer was milled with 30 p.h.r. of medium thermal carbon black, 2 p.h.r. of m-phenylene dimaleimide, and 4 p.h.r.
of 45 % 2,5-di(tert-butylperoxy)hexane, press-cured for 30 minutes at 180-185C., and postcured stepwise for 6 hours at 50~C. to 15 204Co followed by 24 hours at 204C~ The cured elastomer had the following physical properties: Tensile strength, 1560 p.s.i.;
Elongation, 200 %; 100% Modulus, 1180 pos.i., Shore A hardness, 81;
Permanent set at break, 40 %; Compression set after 22 hours at 300F. 65 %. Solvent swell (volume increase after one week at room temperature) was found to be as follows: Acetone, 23 %;
Toluene, 14 %; High-octane gasoline (EXXON EXTRA), 5 %; Tetra-, ... ..
chloroethylene, 8 %; Butyl acetate, 26 %.

Example 18 Terpolymer of tetrafluoroethylene, propylcne and vinyl chloroacetate .
A twenty-liter autoclave was charged with 528 g of tetra-fluoroethylene, 4.75 g of propylene and 20 g of vinyl chloroacetate ~ ~rA~ 2 9 ~ 4~-~
' ~ 037195 in an emulsion system containing 15 1 of deionized water, 30 g of ammonium perfluorooctanoate, and 30 g o tribasic sodium phosphate dodecahydrate. The initial monomer ratio in tlle reactor was 95.0/2.0/3.0 by mole. Polymerization was initiated at 60C. and 300 p.s.i.g. by injecting 9 g of sodium sulfite and 18 g of ammonium persulfate in 100 ml of water each. As the reaction proceeded, the pressure was maintained at 300 p.s~i.g.
by continuously feeding a mixture of TFE and propylene, 71/29 by mole. When 300 g of that mixture had been fed, another 12 g of vinyl chloroacetate was add;ed, followed by continuous feed of another 300 g of the TFE/propylene mixture. Then the unreacted gaseous monomers were discharged, and 646 g of polymer was isolated by coagulation of the latex. Analysis showed the product to con-tain 77.3 mol % TFE, 22.5 mol % propylene, and 0.2 mol % vinyl chloroacetate. 11~e tough nlbbery polymer was compounded and cured with 1.3 p.h.r. of hexamethylenediamine carbamate and 5 p.h.r. of dibasic lead phosphite~ The tensile strength was 1170 p~S~io~
the elongation at break 345 %, and the Shore A hardness, 90.
Example l9 Copolymer of tetraEluoroethylene and propylene in a molar ratio of l,0/0.26 ... ...
A copolymer containing 79.l mol % of tetrafluoroethylene and 20.9 mol % of propylene was prepared substantially as described in Example 14, except that after the initial monomer charge of 99.0 mol % of TFE and 1.0 mol % propylene a mixture of about ~'~2()/~ A

.
~037195 77 mol % TFE and 23 mol % propylene was used for the continuous feed. The polymerization was carried out at a temperature of 142-148F. and a pressure of about 305-315 p.s.i.g. At the end of nine hours, a dispersion containing 15.6 % polymer was obtained.
5 The isolated product was pressed into flexible sheets having a tensile strength of 2620 p o S ~ an elongation at break of 400 %, a Shore A hardness of 89, a 100% modulus of 530 p.s.i., and a pennanent set value after 100 % extension of 40 %.
Example 20 Copolymer of tetrafluoroethylene and propylene at a molar ratio of 1.0/0.325 A twenty-liter autoclave was charged with 15 1 of de-ionized water, 75 g of ammonium perfluorooctanoate, 75 g of sodium hydroxide, and 3 g of sodium sulfite. The reactor was sealed, 15 purged with nitrogen and evacuated. It was then pressurized to 40 p.s.i.g. at ambient temperature with a mixture of TFE and propylene, 73/27 by mole. 400 g of pure, inhibitor-free TFE was i~ then added to bring the TFE/propylene mole ratio in the reactor to about 95.5/4.5 and the reactor heated to about 60C. Polymeriza-20 tion was initiated by injecting a solution of 6 g ammonium per-sulfate in 100 ml of water. As the reaction proceeded, a mixture of TFE and propylene, 73/27 by mole, was fed in a semi-continuous manner so as to maintain the reaction pressure at 310-325 p.s.i.g..
During a period of 4.8 hours, 1600 g of that gas mixture was 25 charged. After releasing the pressure, the latex was discharged and coagulated, yielding 1396 g of a copolymer containing about 75.5 mol % TFE and 24.5 mol % propylene (elemental analysis:

L'J2~49-~

:103719S
31.37 % C, 1.65 % H, and 64~63 % F). Flexible sheets pressed from this product had the following properties: Tensile strength, 1820 p.s.i.; Elon~ation, 410 %; Shore A hardness, 86; 100% Modulus, 460 p.s.i.; Pennanent set after 100 % exten-sion, 24 %. Solvent swell (volume increase after immersion forone week): Acetone, 17 %; Butyl acetate, 21 %; Tetrachloroethy-lene, 8 %; Hig~l-octane gasoline (EXXON EXTI~A), 8 %; Toluene, 8 %.
From the foregoing discussion and Examples it should be evident that applicant has disclosed a novel process for making a novel group of thenmoplastic elastomeric polymer which, because of their relatively high fluorine content exhibit improvedsolvent resistance, and because of their more nearly unifonn composition in tenms of TFE/propylene molar ratio exhibit improved elasto-meric propertiesO It is, of course, to be understood that the foregoing Examples are intended to be illustrative only and that numerous changes in the ingredients, proportions and conditions disclosed can be made without departing from the spirit of the , invention as defined in the appended claimsO

Claims (14)

1. A thermoplastic elastomer consisting essentially of a copolymer of tetrafluoroethylene and propylene having a substan-tially uniform molar ratio of tetrafluoroethylene units to propy-lene units and having a molar ratio of tetrafluoroethylene units to propylene units of from 1.0:0.11 to 1.0:0.54.

2. A thermoplastic elastomer according to claim 1 having a molar ratio of tetrafluoroethylene units to propylene units of 1.0:0.25 to 1.0:0.43.

3. A curable elastomer consisting essentially of a terpolymer of tetrafluoroethylene, propylene and a cure site monomer having a substantially uniform molar ratio of units derived from the three monomers, a molar ratio of tetrafluoroethy-lene units to propylene units of from 1.0:0.11 to 1.0:0.54 and from 0 to 10 mole percent, based on the total terpolymer, of cure site units.

4. A curable elastomer according to claim 3 having a molar ratio of tetrafluoroethylene units to propylene units of 1.0:0.25 to 1.0:0.43.

5. The cured elastomer of claim 1.

6. The cured elastomer of claim 3.

7. A process for making a thermoplastic elastomer con-sisting essentially of a copolymer of tetrafluoroethylene and pro-pylene having a molar ratio of tetrafluoroethylene units to propy-lene units of from 1.0:0.11 to 1.0:0.54 comprising the steps of (a) charging a reactor with a solution containing an inert liquid medium, emulsifier, buffer, catalyst and reducing agent, (b) charging to said reactor solution a monomer mix-ture of tetrafluoroethylene and propylene in a molar ratio of 1.0:0.01 to 1.0:0.087, (c) adding an initiator to said reactor solution and maintaining the reaction mixture at a temperature of 5° to 120°C.
and a pressure of 100 to 1,000 p.s.i.g., thereby initiating co-polymerization of said monomers to produce a copolymer having a molar ratio of tetrafluoroethylene units to propylene units greater than 1.0:0-54, (d) thereafter continually feeding to said reactor a monomer mixture of tetrafluoroethylene and propylene having a molar ratio of tetrafluoroethylene units to propylene units that is substantially the same as the ratio of tetrafluoroethylene units to propylene units in the initially formed copolymer within the reactor and at a feed rate to maintain the reactor pressure substantially constant to cause the monomers within the reactor to be replenished at approximately the same rate as they are consumed in the polymerization reactor and thereby produce a copolymer having a substantially uniform composition in the reactor and (e) terminating the reaction by venting the unreacted monomer and discharging the reaction product.

8. A process for making a curable elastomer consist-ing essentially of a terpolymer of tetrafluoroethylene, propylene and a cure site monomer, said elastomer having a molar ratio of tetrafluoroethylene units to propylene units of from 1,0:0 11 to 1,0:0.54 and from 0 to 5 mole percent of units derived from said cure site monomer comprising the steps of (a) charging a reactor with a solution containing an inert liquid medium, emulsifier, buffer, catalyst and reducing agent, (b) charging to said reactor solution a monomer mixture of tetrafluoroethylene, propylene and 0 to 5 mole percent of said cure site monomer, the molar ratio of tetrafluoroethylene to propylene being 1.0:0.01 to 1.0:0.087, (c) adding an initiator to said reactor solution and maintaining the reaction mixture at a temperature of 5° to 120°C.
and a pressure of 100 to 1,000 p.s.i.g., thereby initiating co-polymerization of said monomers to produce a copolymer having a molar ratio of tetrafluoroethylene units to propylene units greater than 1.0:0.54, (d) thereafter continually feeding to said reactor a monomer mixture of tetrafluoroethylene, propylene and cure site units in a molar ratio that is substantially the same as the ratio of tetrafluoroethylene, propylene and cure site units in the ini-tially formed polymer within the reactor and at a feed rate to maintain the reactor pressure substantially constant to cause the monomers within the reactor to be replenished at approximately the same rate as they are consumed in the polymerization reaction and thereby produce a copolymer having a substantially uniform compo-sition in the reactor, and (e) terminating the reaction by venting the unreacted monomer and discharging the reaction product.

9. The process as claimed in claim 7 wherein the reac-tion temperature is from 40°C. to 80°C.

10. The process as claimed in claim 8 wherein the reaction temperature is from 40°C. to 80°C.

11. The process as claimed in claim 7 wherein the reaction pressure is from 250 to 350 p.s.i.g.

12. The process as claimed in claim 8 wherein the reaction pressure is from 250 to 350 p.s.i.g.

13. A cross-linkable elastomer consisting essentially of a copolymer of tetrafluoroethylene and propylene having a substantially uniform molar ratio of tetrafluoroethylene units to propylene units and having a molar ratio of tetrafluoroethylene units to propylene units of from 1.0:0.11 to 1.0:0.54.

14. A cross-linkable elastomer according to claim 13 having a molar ratio of tetrafluoroethylene units to propylene units of 1.0:0.25 to 1.0:0.43.