The present invention relates to polyarylene sulphide compositions.

5„ Polyarylene sulphides have properties which make them suitable for use in various situations, for example as plain bearing linings, However, they also possess properties which make their preparation and ^• application inconvenient and frequently difficult.

10. Available techniques involve the use of toxic chemicals or techniques involving what is essentially powder fusion. The powder fusion techniques limit the roles in which polyarylene sulphides can be used and involve slow processes of low productivity.

15. One of the properties of polyarylene sulphides which limits their use is their high viscosities in the molten state. This renders the distribution of the material difficult in the extreme and makes it difficult therefore to establish a bond between the

20. polyarylene sulphide and another material. One known method of forming a bond between the polyarylene sulphide and another material is to apply the poly¬ arylene sulphide powder to the other material as level and evenly as possible, and then to melt, cure and

25. cross-link the powder. Water based dispersions of PPS are also known but this is just another form of applying powder since this is what remains after the water has been evaporated.

However, as stated above, using polyarylene

50. sulphide powder involves considerable manufacturing

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difficulties. Polyphenylene sulphide takes a long time to cure and crosslink particularly when the powder layer is relatively thick. Also since the molten powder has a high viscosity and generally does not flow or wet a surface very well, this results in voids and ccnsec ently a poor bond between the polyphenylene sulphide and the other material which bond may fail when under load.

It is also difficult to achieve a precision thickness of polyarylene sulphide which is di ensionally stable and even more difficult to produce a very thin _: cured layer.

It is an object of the present invention to provide polyarylene sulphide in a workable form in order to minimise the above difficulties in its use .

The present invention is based o the discovery that benzyl benzoate has a solvent action on polyphenylene sulphide.

According to the present invention a composition o matter comprises polyarylene sulphide intimately admixed with an aryl ester of an aryl alcohol the ester being in the liquid phase, and the resin being in solution ar.d/cr in suspension therein.

Thus the mixture may be a two phase mixture of a resin or a resin rich phase comprising polyarylene sulphide and a solvent or a solvent rich phase cornerising an aryl ester of an aryl alcohol preferably benzyl benzoate; alternatively, the resin may be in solution in the solvent.

The resin chase mav further include other resins

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besides polyarylene sulphide in either a major or minor proportion based on the polyarylene sulphide. Such other resins may include polytetrafluoroethylene, polyimides and polysulphones. The resin phase may also

5. include fillers, pigments, dyes, surface active addi¬ tives, stabilizers, cross linking agents, coating aids such as. silica or titanium oxide powders, and bases to enhance .bonding.

The solvent phase may include or comprise mixtures

10. of aryl esters of aryl alcohols, for example one or more of benzyl benzoate, benzyl phthalate, benzyl iosphtha- late, and benzyl terephthalate, and other materials acting as diluents or extenders or viscosity reducers for the active ^' solvent and having no non-solvent action

15. such as to prevent the blend having the necessary plasti ciser or solvent action for the resin phase as the case may be.

The solvent phase may also include co-solvents whic whilst having no significant solvent action on their own

20. enhance the solvent action of the benzyl benzoate.

The solvent phase may also include other solvents for polyphenylene sulphide and when the resin phase includes other resins, solvents for such other resins even if these are not solvents for polyphenylene sulphid

25. though in this case they are preferably iscible with benzyl benzoate to form a single solvent phase.

The compositions of the invention may extend from slurries of polyphenylen sulphide plasticized or not by benzyl benzoate in liquid vehicles

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which contain benzyl benzoate the benzyl benzoate either being in the polyphenylene sulphide or in the liquid vehicle or in both, to pastes of polyphenylene sulphide plasticized or not with benzyl benzoate suspended or

5. dissolved in benzyl benzoate or benzyl benzoate containing vehicles or spreadable, dippable or sprayable solutions of polyphenylene sulphide in benzyl benzoate or benzyl benzoate containing solvents.

The polyarylene sulphide resin that can be used in

10. ^~ tb.e present invention may be a polymer made by the method disclosed in USP 3354129 but in general can be represented as a polymer including a recurring unit of the formula

in which the ring A may be substituted.

One such form of substitution may be represented by the formula

in which: X represents a fluorine, chlorine, bromine or iodine atom, preferably chlorine or bromine, and Y represents 25. a hydrogen atom,

0 0 O R 0 - , - (R) ₂ , -C-OR, -C-OM, -C-N(R) ₂ , - -C-R ₂ , -0-R', -S-R', -SO^H or -SO.M groups in which:

R represents a hydrogen atom, an al yl, cycloalkyl, 30. aryl,_aralkyl, or alkaryl group containing 1 to 12 carbon atoms and in which:

K represents an alkali metal atom of a sodium or potassium atom and in which: p is 0 to 4 and q is 2 to 4.

Polypher.Yler.e sulphide ir. which the repeat unit can be represented by the formula

is prezerrec.

The polyarylene sulphides may be partially oxidized

10 , or may have a branched cr cross linked structure though ncn-crcεs linked polymers or ones having a low degree of cross linking and thus relatively lew I-./vv. are preferred e.g. those having y.. ^~ > ^~ . s in the range 17,500

-c 5000. More cene: ily polyarylene sulphides having

15 a ng ?c :he range 280 C to 300 C are preferred

A_so matεriais πεvmg intrinsic viscosities m chloronapthaler.e at 260 C of at least 0.1, e.g. 0.1 to C3 especially 0.13 to 0.25 are preferred.

Polyphenylene sulphide has a solubility parameter o

20. 8.5 to 9.5. ϋncured F?S sold under the Trade Mark Ryton VI has a melt flow index of lOOOg/ in. by the .American Society Test Method (A5TK, D123S). Using the same test, part cured PPS sold under the Trade Marks Ryton P2 and ? have melt flow indices of 300 and 125g/min. respectively

25. In those compositions including PPS in particulate form the particle size may be in the range 10-200 microns and use of Dcwder of such r-ar icle size is convenient as a sta¬ ins Ooir " . for τne nrenarat; >n of single phase

, - (_ :* ^* .--

.-cuncs i cr use m τm'

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present invention may- -b rep-resented by the- formula

where. X, Y, and Z represent a hydrogen atom or a halogen atom e.g. -a chlorine atom.

The most preferred compound is Compound I, when 10. X, Y, W and Z are all hydrogen. A less preferred compound is Compound I. when W or Z is chlorie and X, Y and Z or W are hydroge ₃ namely benzyl monochlorobenzoaτe. Benzyl benzoate has the _. following properties:- melting point 18-20°C 15. boiling point 320°C solubility parameter 9L.3

Other solvent compounds which may be used in the present invention may comprise phenyl benzoate, ci- phenyi phthalate, di-benzyl ether, benzole anhydride and 20. di-phenyl sulphone.

Using a composition according to the invention a preferred method of curing the polyarylene sulphide comprises mixing polyarylene sulphide with an aryl ester of an aryl alcohol, arranging true conditions affecting 25. the mixture so that the components form a single continuous liquid phase, and subsequently evaporating the ester, and at leas-t partly curing the polyarylene sulphide simultaneously to leave the polyarylene sulphide in an at least partly cured state. 30. Preferably the polyarylene. sulphide is. polyphenylene

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sulphide aid preferably the eater is benzyl benzoate.

Thus, the ester may he in the liquid state so that the mixture may be a paste or slurry of resin in the. ester or may be a solution of the resin in ester, and the

5. components, are preferably* h ated until they form one continuous liquid phas.e.. ^' . The. liquid may be cooled at this, stage for-example in order to promote precipitation of the resin in the. form of fine, crystals in the ester. This step is ^* -not absolutely ne.ces*sary in all cases

10. but may be advantageous ^* for example if it is desired to store the formulation for any length of time.

Preferably:the nature of the ester and the resin are such that when the mixture is heated the resin and ester form a single phase and as the ester evaporates,

15. the resin undergoes curing. Preferably the ester does not evaporate completely until the resin is almost completely cured. Preferably a minimum of ester is employed since this may be lest in evaporation.

The method according to the invention may therefore

20. render it possible to produce a cured polyarylene sulphide in the form of a thin film having a thickness hitherto thought to be unobtainable for example as low as from

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1 to 4 x 10 m, for example 3 x 10 m.

Various methods may be employed in applying the 25. mixture prior to curing. In the case of a paste or wet powder this may be applied for example by wet spraying e.g. by an aerosol or spreading while in the case of slurries and solutions ^* these may be applied by wet spray¬ ing or by painting or the article to which the resin is 30. to be applied may be. dipped into the mixture.

The invention also, extends to the use of the ester in welding togethex* surfaces* of the resin. By applying the eater to two res.in surfaces- to be joined together and holding these together at a suitable pressure and 5. temperature, an effective bond -may be achieved.

The invention may be carried into practice in various ways and will Be illustrated in the following specific*• examples. All percentages _^ in the following examples are by weight.

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Examples 1 to 13 are ex-amples of mixtures in accordance with the invention which are applied to an aluminium alloy backing in order to .coat the backing with .polyphenylene sulphide. Example 19 is an example

5. of solvent welding. EXAMPLE 1

8% uncured polyphenylene sulphide sold under the Trade Mark Ryton VI was mixed ^' with 9 % benzyl benzoate. • The mixture was heated to a temperature in the range

10. 250° to 290°C by which time the polyphenylene sulphide had dissolved in the benzyl benzoate. The backing, at ambient temperature, was immersed for 0.5 seconds and withdrawn. A coating of solution had adhered to the backing. The coated backing was transferred to an air

15. circulatory oven and maintained at a temperature between 300°. and 3 0°C for five minutes. The temperature was then increased to a temperature between 370° and 3S0°C for a further 15 minutes after which time the benzyl benzoate had evaporated and the polyphenylene sulphide

20. was fully cured. The layer of polyphenylene sulphide produced was approximately 0.001 cm in thickness. EXAMPLE 2

30% uncured polyphenylene sulphide were dissolved in a solution comprising 10% diphenyl phthalate and 60%

25. benzyl benzoate and held at a temperature between 250° and 290°C. The backing was immersed in the solution for 2 minutes thus allowing the backing and solution to reach _. a- thermal equilibrium. The backing, with an adherent coating of solution, was transferred to an

30. oven and heated to a temperature between 300° and 3 0°C

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for five minutes and then to a temperature between 370° and 380°C for a further 15 minutes. A coating similar to that obtained in Example 1 was obtained. EXAMPLE 3

5. A suspension of uncured polyphenylene sulphide was prepared by mixing 30% polyphenylene sulphide with 10% diphenyl phthalate and 60% benzyl benzoate, heating the mixture to a temperature between 250° and 290°C in order to dissolve the polyphenylene sulphide, and subsequently

10. cooling the solution to a room temperature while maintaining a vigorous agitation. A fine cloudy gelatinous suspension of polyphenylene sulphide was thus formed. The suspension was sprayed on to two backings, one of which was at room temperature and .the

15. other of which was heated to about 250°C. The sprayed backings were transferred to an oven where they were held at a temperature between 300° and 3 0°C for five minutes and then held at a temperature between 370° and 380°C for a further 15 minutes. An adherent

20. coating of polyphenylene sulphide 0.001 cm thick was produced on each. EXAMPLE 4

A water-based slurry was produced by ball milling together for 24 hours 30% uncured polyphenylene sulphide

25. 49% saturated calcium hydroxide solution, 1% of a non- ionic surfactant (as sold under the Trade Mark Triton X 100) and 20% diphenyl sulphone. This slurry was used to spray coat two backings as described in Example 3 above and similar coatings were -obtained.

EXAMPLE 5

A backing, at room temperature, was sprayed with a solution comprising 10% phenyl benzoate in 90% benzyl benzoate until the surface sprayed was fully wet but

5. not dripping. The wetted surface was sprayed electro¬ statically with a powder mixture of 99% polyphenylene sulphide and 1% calcium hydroxide. The backing was placed ^" in an oven and heated to a temperature of between 300° and 3 0°C for 5 minutes followed by being

10. heated to a temperature between 370° and 380°C for a further 15 minutes. As in the previous examples a satisfactory thin coating was obtained. EXAMPLE 6

This was carried out in the same way as Example 5

15. but with diphenyl phthalate replacing phenyl benzoate. Similar results were obtained as those of Example 5. EXAMPLE 7

This was carried out in the same way as Example 4 but the calcium hydroxide solution was replaced with an

20. aqueous suspension of polytetrafluoroethylene comprising between 15 and 30% polytetrafluoroethylene. Similar results were obtained to those of Example 4. EXAMPLE 8

The following ingredients were mixed intimately

25. in a high speed mixer: 70% uncured polyphenylene sulphide 20% diphenyl sulphone, 9% diphenyl phthalate and 1% calcium hydroxide. The mixture was electros ^t atically sprayed on to a backing, ^' at room temperature. The backing was placed in an oven where it was heated to

30. a temperature between 300° and 310°C, held at that

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temperature for 5 minutes and subsequently raised to a temperature between 370° and 380°C for 15 minutes. An adherent coating of polyphenylene sulphide was obtained having a thickness of 0.001 cm approximately.

5. EXAMPLE 9

This was carried out in the same way as Example 8 except_ that the backing was at a temperature between 350° and 370°C prior to its being sprayed with the mixture. Similar results were obtained to those of

10. Examole 8

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EXAMPLE 10

This was carried out in the same way as example 1 but with the uncured polyphenylene sulphide replaced 5. ^" by 99% part cured polyphenylene sulphide (sold under the Trade Mark Ry- ^' .on P2) and 1% calcium hydroxide powder.. Similar results were obtained to these obtained in example 1 but it was found that the curing time was shorter than in exam le 1.

10.

EXAMPLE 11

This was carried out in the same way as example 2 but an uncured polyphenylene sulphide was replaced by a

15. mixture of 99% part cured polyphenylene sulphide arid 1% calcium hydroxide, and the diphenyl phthalate/ enzyl benzoate mixture was replε-ced by benzyl benzoate alone. Similar results were obtained to those of example 2 but it was found that the curing time was shorter than in

20. example 2.

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This was carried out in the same way as example 3 25. but the uncured polyphenylene sulphide was replaced by a mixture of 99% part cured polyphenylene sulphide and 1% calcium hydroxide, and the diphenyl phthallate/ benzyl benzoate mixture was replaced by benzyl benzoate alone. ^" Similar r-suits were obtained to these in example 30. 3 but_it was found that the curing time was shorter than in example 3.

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EXAMPLE 13.

This was carried out in the same way as example 4 but the uncured polyphenylene sulphide was replaced 5, entirely by part cured polyphenylene sulphide.

Similar results were obtained to those obtained in example 4 but it was found that "the curing time was shorter than in example 4.

10. EXAMPLE 14

This v/as carried out in the same way as example 5 but the uncured polyphenylene sulphide was replaced entirely by part cured polyphenylene sulphide. 15. Similar results were obtained to those obtained in example 5 but it was found that the curing time was shorter than in example 5.

EXAMPLE 15

20.

This was carried out in the same way as example 6 but the uncured polyphenylene sulphide v/as replaced entirely by part cured polyphenylene sulphide. Similar results were obtained to those obtained in 25. example 6 but it was found that the curing time was shorter than in example 6.

EXAMPLE 16

30. This was carried out in the same way as example 7

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but the uncured polyphenylene sulphide was replaced by a mixture of 99% part cured polyphenylene sulphide and % calcium hydroxide. Similar results were obtained to those obtained in Example 7 but it was found that

5. the curing time was shorter than in Example 7. EXAMPLE 17

This was carried out in the same way as Example 8 but the ^' uncured polyphenylene sulphide was replaced entirely by part cured polyphenylene sulphide. Similar

10. results were obtained to those obtained in Example 8 but it was found that the curing time was shorter than in Example 8. EXAMPLE 18

This was carried out in the same way as Example 9

15. but the uncured polyphenylene sulphide was replaced entirely by part cured polyphenylene sulphide. Similar results were obtained to those obtained in Example 9 but it was found that the curing time was shorter than in Example 9.

20. EXAMPLE 19

Two blocks of injection moulded polyphenylene sulphide were bonded together by wetting each mating surface with benzyl benzoate and then clamping together under a pressure of 100 psi, 6.9 x 10 5 N/m2 and heating

25. for 10 minutes at 300°C.

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