PARTICLES

Abstract: The invention provides electroconductive particles comprising a styrene copolymer core and an external gold coating, characterised in that as said copolymer core is used a styrene copolymer comprising less than 50 wt. % styrene residues.

Description: Particles The present invention relates to electroconductive particles, in particular gold-coated polymer microbeads, and to a process for their preparation. The use of electroconductive particles to achieve an anisotropic electrical connection between electronic components has been described in EP-A-265212 (Japan Synthetic Rubber) and in JP-B-5/19241 (Sumitomo Chemical) . Metal coated polymer beads, distributed in an adhesive matrix are disposed between the component surfaces and serve to provide an electrical connection between those surfaces . In JP-B-5/19241, gold, silver, copper, nickel and aluminium are said to be suitable electroconductive coatings and the polymer is stated to be a styrene copolymer, e.g. with an acrylic acid ester, a methacrylic acid ester, an unsaturated carboxylic acid, a nitrile or a diene . The copolymer must however contain styrene as its principal component and no more than 30 wt. % of the polymer can derive from another ethylenically unsaturated monomer. In the Examples a divinyl benzene : styrene (4:96 wt . ratio) polymer particle is either acid treated, treated with colloidal palladium chloride and then plated with silver or is coated with silver by vacuum vapour deposition. EP-A-265212 describes the use of polystyrene, styrene/divinylbenzene/methacrylic acid (65:35:5 by weight), methyl methacrylate/divinylbenzene (50:50), and styrene/divinyl benzene/sodium styrene sulphonate (65:30:5) polymer particles. The surfaces of the particles were chemically etched, treated with colloidal palladium chloride and then plated with nickel or copper. Subsequent gold plating of such nickel plated styrene/divinyl benzene/sodium styrene sulphonate particles was also described and the resulting particles displayed the best results in terms of anisotropic conductivity. Indeed Sumitomo refer to gold plating as being especially preferred for obtaining a good stable and long lasting electrical connection. The electroconductive particles are substantially spherical having an average particle diameter in the micrometer range, e.g. 1 to 50 μm. Gold plated polymer microspheres of this type are available commercially from Sekisui. In application and subsequent use as electrical connectors, the electroconductive microparticles undergo mechanical and thermal stresses and for optimum performance the coatings should be substantially blemish free. Where inert gold coatings are used, to avoid contamination any underlying non-gold metal coating should not be exposed. However when gold-plated polymer microspheres produced as described above are examined by electron microscopy, it may clearly be seen that many of the gold surfaces are blemished and incomplete. We have now found that improved gold-plated styrene copolymer microspheres may be produced by using a styrene copolymer in which styrene is a minor component and/or which incorporates a functionalised comonomer and is palladinated by reaction with a solution of a palladium compound. Thus viewed from one aspect the invention provides electroconductive particles comprising a styrene copolymer core and an external gold coating, characterised in that as said copolymer core is used a styrene copolymer comprising less than 50 wt. % styrene residues . Viewed from a further aspect the invention also provides electroconductive particles comprising a styrene copolymer core and an external gold coating, characterised in that as said copolymer core is used a styrene copolymer produced using styrene and a functionalized comonomer and subsequently palladinated by reaction with a solution of a palladium compound. Preferably the polymer core in the particles of the invention comprises less than 50 wt. % styrene residues and comprises residues of a functionalized comonomer. By "functionalized" it is meant that the comonomer contains reactive chemical groups that are not transformed into a non-reactive form by the polymerization reaction. Typically such groups will be pendant from the polymer backbone of the resultant copolymer. Exemplary functional groups include amine, thiol, hydroxyl , amide, ester and oxyacid groups, e.g. carboxyl, sulphonic, phosphoric and phosphonic groups. Preferred functional groups for the ready-to-palladinate particles include groups capable of coordinating palladium, e.g. amino, carboxyl, hydroxyl and sulphonic groups, especially amino groups. The functional groups in the palladium treated particles need not be the same as in the comonomer used in the polymerization reaction, ie. they may be modified after the copolymer is prepared, e.g. by reaction with a bifunctional agent which serves to introduce the desired functional group. By way of example this may be achieved by reaction of a styrene :divinylbenzene : glycidylmethylmethacrylate copolymer with an aminating agent such as ethylene diamine . The styrene content of the styrene copolymer is preferably 0.5 to 98.5 wt %, e.g. 20 to 95 wt . %, more preferably 10 to 75 wt. %, e.g. 25 to 70 wt. % . Where the styrene content is below 50 wt. %, it is preferably 20 to 49 wt. %, e.g. 25 to 45 wt . %, particularly 30 to 45 wt. %. Where the styrene polymer is crosslinked, the most commonly used cross-linking comonomer is divinylbenzene (DVB) . As used, however, DVB generally contains a relatively high proportion (about 20, 35 or 45% wt) of the monoethylenically unsaturated, styrene analog ethylvinylbenzene (EVB) , and the styrene content of the polymer may be considered to be the sum of the styrene and the EVB. The comonomers used with styrene to produce the polymer cores of the particles of the invention may be any comonomers capable of copolymerization with styrene. These will generally be compounds which are mono- or multiply ethylenically unsaturated; examples include acrylic acid esters (e.g. methyl, ethyl, butyl, glycidyl, etc. acrylate), methacrylate acid esters (e.g. methyl, ethyl , ' butyl , glycidyl, etc. methacrylates) , acrylic acid, methacrylic acid, acrylonitrile, methacrylonitrile, α-methyl styrene, vinyl toluene, vinyl chloride, vinyl acetate, vinyl propionate etc. Acrylic and methacrylic acids and especially esters, and mixtures of two or more thereof are preferred. Other multiply ethylenically unsaturated monomers may be used to achieve a degree of crosslinking, e.g. dienes such as butadiene, divinyl benzene, trimethylolpropane acrylate or polyethylene glycol diacrylate, especially divinyl benzene. The proportion of multiply ethylenically unsaturated monomer used will depend on the resilience required of the polymer cores in use but their residues will generally make up from 2 to 30 wt . %, more preferably 5 to 20 wt. %, especially about 10 wt. % of the polymer. The proportion of the functionalized comonomer (e.g. an acrylate or methacrylate ester) will preferably be such that their residues make up 5 to 99.5 wt . %, e.g. 10 to 75 wt. %, more preferably 15 to 70 wt . %, especially 55 to 65 wt . % (e.g. 5 to 60 wt . %, for example 10 to 50 wt %) . Particularly satisfactory results have been obtained with a styrene content of 25- 35 wt %, a DVB content of 7 to 13 wt % and a methacrylate content of 55 to 65 wt %, and metal -plated particles having a core of such a polymer form a further aspect of the invention. Particularly suitable copolymers include styrene: divinyl benzene : glycidyl methacrylate and styrene: divinyl benzene : glycidyl methacrylate :butyl methacrylate which may subsequently be aminated by treatment with ethylene diamine. The polymer particles are preferably substantially spherical and also substantially monodisperse . Thus the particle size distributions have a coefficient of variation CV of 20% or less, preferably 12% or less, more preferably 5% or less, still more preferably 3% or less, e.g. 1.5 to 2.5%. CV is determined in percent by the formula (standard deviation/mean) x 100 where mean is the mean particle diameter and standard deviation is the standard deviation in particle size. CV is normally calculated by fitting a monomodal distribution curve to the detected particle size distribution. Thus some particles below or above mode size may be discounted in the calculation which may for example be based on about 90%, or more preferably about 98%, of the total detectable particle number. CV is often determined on a Coulter LS 130 particle analyser. Mode particle size for the polymer core in the particles of the invention is preferably 0.5 to 500 μm, more preferably 1 to 250 μm, still more preferably 1 to 50 μm, yet more preferably 1.5 to 20 μm, especially 2 to 12 μm, more especially 3 to 10 μm. Such substantially spherical and substantially monodisperse polymer particles may be produced by the technique described in US-A-4336173 , WO93/02112 (Sinvent) , JP-A-86/215602 , JP-A-86/215603 and JP-A- 86/215604. As may be seen from the attached Figures, the use of low styrene content styrene copolymers can result in gold-plated microspheres which have a more "furry" surface than those produced with higher styrene contents. This surprising effect results in lesser agglomeration of the particles and may also enable a better electrical contact to be made when the microspheres are sandwiched between electrical component surfaces . As may also be seen from the attached Figures, the use of styrene copolymers which carry functional groups and are palladinated using a solution (rather than colloid) of a palladium compound results in coatings with fewer defects. Where "furry" particles are desired, the functional monomer (e.g. methacrylate) content should generally be increased for smaller particle sizes, e.g. 40 wt. % for 7 to 10 μm particles rising almost to 100 wt . % for particles below 4.5 μm. Gold coating of the styrene copolymer particles may be achieved as described by Sumitomo (supra) and Japan Synthetic Rubber (supra) , the contents of which are hereby incorporated by reference. However gold coating is preferably achieved by a multistep process which forms a further aspect of the invention. According to this aspect the invention provides a process for the production of gold-plated polymer particles, said process comprising: (i) palladinating functional groups in functional group containing styrene copolymer particles by contacting said particles with a solution of a palladium compound; (ii) metal plating the palladinated particles with a metal having a standard electrode potential (E Θ ) less than that of gold (1.42 V) , in the presence of a reducing agent; and (iii) gold-plating the metal plated particles, advantageously to a gold thickness of 50 to 600 A, e.g. 100 to 400 A or 50 to 200 A, preferably about 400 A. Conveniently the metal used in step (ii) is one having a standard electrode potential of from -1.0V to + 1.0V, e.g. zinc, iron, nickel, tin, lead, copper, chromium or silver. Nickel is especially preferred and the discussion and Examples below focus on the use of nickel. (For standard electrode potentials see for example CRC Handbook of Chemistry and Physics, 70th Edition, 1989, pages D151 et seq) . In the process of the invention, palladination may be achieved with any soluble palladium compound generally using water or another protic solvent. One exemplary complex is ammonium tetrachloro palladate. Advantageously an activator, e.g. dimethylaminoborane (DMAB) is also used. The palladination step is conveniently effected at elevated temperature, e.g. 50 to 70°C, especially about 60°C, and generally may be affected for 10 to 60 minutes, e.g. about 20 minutes. The palladinated particles may then be nickel plated, or plated with other substrate metal coatings, using conventional electroless plating techniques, e.g. using a solution of a nickel compound (e.g. nickel chloride, nickel sulphate, etc., preferably nickel chloride) and a reducing agent (e.g. DMAB, hydrazine or hypophosphite) . Ammonia may be used to achieve a pH of 10.5 to 11.0, optimally 10.8. Generally this electroless plating may be effected at or near ambient temperature and may be effected for about 20 minutes to 1 hour, e.g. 30 minutes. The resulting metal (e.g. nickel) coating is advantageously at least 200 A thick, preferably 300-1000 A, e.g. about 400 A or more preferably about 600 A. In this metal plating step, it is especially preferable to use DMAB as the reducing agent since this gives particularly good metal coating of the polymer particles. During the metal-plating of the palladinated particles, it is especially preferred to disperse in the plating solution a stabilizer, e.g. an non-ionic surfactant (e.g. a Pluronic) , a polyelectrolyte, a polymer (e.g. a polyelectrolyte), a silane, silicon or most preferably an inorganic oxide particulate, more particularly silica. Finely divided silica, e.g. having particle sizes of 3 to 50 nm, more particularly 5 to 15 nm, are especially preferred. Examples of suitable silicas include Cabosil, Aerosil 972 and, especially Aerosil 200 (available from Degussa, a 7 nm particle size hydrophilic silica) . Such silicas may conveniently be used at concentrations of 0.05 to 5 g/L, especially 0.1 to 2 g/L. The subsequent gold-plating step may again be effected using conventional gold-plating techniques, e.g. using potassium gold cyanide. This plating is preferably effected at elevated temperature, e.g. 70 to 90°C, especially 80°C, and may be effected for example for 20 minutes to 1 hour, e.g. 30 minutes. A "Gold Bath" Aureus from Shipley may conveniently be used. As with the initial metal coating of palladinated particles, it is especially preferred to use a stabilizer in the gold plating solution. For this purpose, the same stabilizers as mentioned above may be used, especially silicas. Following gold coating, it is also preferred to treat the gold plated particles with a stabilizer to reduce any tendency to agglomerate. In this regard, the preferred stabilizers are thiol stabilizers, especially thiols with hydroxyl, carboxyl, silane or sulphonic acid functionalities, most especially C 2 _ 25 , especially C 3 _ 20 , more especially C 5 _ 12 , e.g. C 6 , thiols with hydroxyl functionalities, e.g. thiododecanol or more especially thiohexanol . In such thiols, the carbon backbone is preferably linear and ,ω substituted. Especially preferably, the gold plated particles are treated with the thiol stabilizer, e.g. mercaptohexan-1-ol, for 10 to 100 minutes, e.g. 25 to 35 minutes from ambient temperature at about 60°C. The amount of thiol used is conveniently 4xl0 "7 to 4xl0 "5 mole/g particles (on a dry solids basis) , particularly 10 -6 to 10 "5 mole/g, more particularly 2.5 to 5xl0 " mole/g. The gold-plated particles may then bs formulated together with an adhesive to produce an electroconductive adhesive. Adhesives as described in Japan Synthetic Rubber (supra) , EP-B-413161 and US-A- 5162087 may be used, e.g. radiation-curable or thermosetting resins. Such electroconductive adhesive compositions form a further aspect of the present invention. Viewed from this aspect the invention provides an electroconductive adhesive composition comprising an. adhesive matrix material with disposed therein electroconductive particles, characterised in that said particles comprise electroconductive particles according to the invention or produced by the process of the invention. The adhesive compositions of the invention may be used to connect electronic components, as described in EP-A-265212, EP-B-413161 and US-A-5162087 for example. For example, the adhesive composition may be cast into films which are then laid between the components to be electrically connected. Typically such films may be 5- 35 μm, preferably 5-20 μm, more preferably 10-15 μm, e.g. about 10 μm, thick. Thus viewed from a further aspect the invention provides the use of the adhesive composition of the invention for providing an electrical connection (e.g. an isotropic or more preferably anisotropic connection) between electronic components. Alternatively, the gold plated particles may be provided with an external (external to the gold layer that is) coating of an inorganic or organic material, preferably an electrical insulator, e.g. as described in US-A-5162087. In this way the use of the particles as anisotropic conductors is further facilitated. Such further coated particles and adhesive compositions containing them form a further aspect of the invention. Thus for example the gold-plated particles may be provided with a thin, frangible coating of an insulator polymer, preferably one having a thickness of a few nm, e.g. 5-20 nm. In this way, a larger number of particles can be added to the adhesive since in-plane conduction is prevented. As mentioned above, the palladinated particles may if desired be metal-coated with other metals than nickel, e.g. silver, copper, zinc, tin, etc. and such metal-coated particles (which may if desired subsequently be gold-plated) form a further aspect of the invention. The gold- or other metal-plated particles of the invention may be used for purposes other than providing electrical connections. Thus for example they may be used in almost any of the currently existing uses for gold and gold-plated microbeads, e.g. in medical diagnostic assays, in gene therapy. Likewise they may be used in antibacterial, antifungal, anticorrosion, and antistatic applications, in paints, in polymer products (e.g. sheets, plates, moulded articles, etc.), in electromagnetic field shielding, in flooring products, etc. The particles may be formulated for such use in a conventional manner, e.g. by mixing with polymer moulding powder, by addition to adhesive compositions, by mixing with a paint base, etc. Such products and uses form further aspects of the invention. Viewed from one such aspect the invention provides a formed polymer product (e.g. a moulded article, a sheet, etc.) characterised in that metal-plated (i.e. plated with gold, nickel or other metals) polymer particles according to the invention are dispersed in the polymer. Viewed from another such aspect the invention provides a coating composition (e.g. a paint) comprising a liquid carrier with dispersed therein metal-plated polymer particles according to the invention. Patent and other publications referred to herein are hereby incorporated by reference. The invention will now be described further with reference to the following non-limiting Examples and the accompanying drawings, in which: Figures 1 to 9 are scanning electron micrographs of gold-plated or nickel plated styrene polymer microparticles . In the Examples below where DVB is used as a crosslinking comonomer, the percentage DVB is the value for DVB itself - the EVB contaminant is included in the value given for the styrene (ST) monomer. In these Examples the EVB content of the DVB used was 35% wt . Thus for example 10% DVB, 30% ST means 10% DVB, 5.4% EVB and 24.6% pure styrene. Example 1 Preparation of gold-plated low styrene content styrene copolymer particles using particles with a reactive group conditioned surface. Starting particles In this Example, 5 μm styrene copolymer particles (60% glycidyl methacrylate: 10% DVB: 30% ST) produced by the method of US-A-4336173 and subsequently treated with ethylene diamine were used. Activation Part 1 - In a 2L reactor an aqueous solution containing 50g 10 wt% of the particles was heated to 60°C. While stirring at 200 rpm, a solution of 200 ml 0.05 wt% ammonium tetrachloro pallade was charged and the mixture reacted for 25 minutes. The mixture was decanted and the particles were left to settle. The particles were washed with water until the wash water was clear. Part 2 - In a 2L reactor the palladium activated particles were heated to 60°C. While stirring at 200 rpm, a solution of 400 ml 10% borane dimethylamine complex was charged and the mixture reacted for 15 minutes. The activated particles were washed on a nutch, using an amount of washing water twice the reaction volume. Nickel plating In a 10L reactor a nickel-solution was prepared by mixing 8L water, 2L PVP-solution containing 50g/L K-30, 200g tetra sodium pyrophosphate, 75g nickel -chloride and 60 ml ammonia. The mixture was stirred until dissolved at a temperature of 22.5±2°C. 50g activated particles were charged. While stirring at 300 rpm a solution of 250 ml 10% borane dimethylamine complex was charged and the mixture reacted for 30 minutes. The mixture was decanted and the particles were left to settle. The particles were washed with water until the wash water was clear. Gold plating In a 10L reactor a gold-solution was prepared by mixing 6L water, 4.5L AREUS 7950 from Shipley, and 70g potassium gold cyanide. The bath was heated to 75+5°C. While stirring at 300 rpm 50g nickel plated particles were charged and the mixture reacted for 35 minutes. The mixture was decanted and the particles were left to settle. The particles were washed with water until the wash water was clear and then with methanol . The particles were dried at 50°C for 12 hours. Example 1 may be repeated using 200 μm styrene copolymer particles (30% glycidyl methacrylate: 30% butyl methacrylate: 10% DVB: 30% ST) prepared by the process of US-A-4336173 and subsequently treated with ethylene diamine . Example 2 Preparation of gold-plated low styrene content styrene copolymer particles. Starting particles In this Example 5 μm styrene copolymer particles (45% ST:2% DVB: 53% glycidyl methacrylate) are used. Etching In a 2L reactor IL chrome sulphuric acid from Merck is heated to 65°C. While stirring at 400 rpm, 50g dry particles is charged and the mixture reacted for 10 minutes. The particles are washed on a nutch, using an amount of washing water twice the reaction volume. Neutralising In a 2L reactor an aqueous solution containing lOg sodium pyrosulfite is stirred at 400 rpm at room temperature, 50g etched particles are charged and the mixture reacted for 15 minutes. The particles are washed on a nutch, using an amount of washing water twice the reaction volume. Conditioning In a 2L reactor IL 0.5% DODUPRINT 218 from Doduco in water is heated to 25°C. While stirring at 400 rpm, 50g etched particles are charged and the mixture reacted for 10 minutes. The particles are washed on a nutch, using an amount of washing water half the reaction volume. Activation In a 2L reactor IL LeaRonald SMT Catalyst, from LeaRonald which consists of palladium-chloride, is heated to 30°C. While stirring 50g particles is charged and the mixture reacted for 10 minutes. The particles are washed on a nutch, using an amount of washing water twice the reaction volume. Nickel plating In a 10L reactor a nickel -solution is prepared by mixing 8L water, 2L PVP-solution containing 50g/L K-30, 200g tetra sodium pyrophosphate, 75g nickel -chloride and 60 mL 28% ammonia. The mixture is stirred until dissolved at a temperature of 22.5±2°C. 50g activated particles is charged. While stirring at 300 rpm a solution of 250 ml 10% borane dimethylamine complex is charged and the mixture reacted for 30 minutes. The mixture is decanted and the particles are left to settle. The particles are washed with water until the wash water is clear. Gold plating In a 10L reactor a gold-solution is prepared by mixing 6L water, 4.5L AREUS 7950 from Shipley, and 70g potassium gold cyanide. The bath is heated to 75±5°C. While stirring at 300 rpm 50g nickel plated particles are charged and the mixture reacted for 35 minutes. The mixture is decanted and the particles are left to settle. The particles are washed with water until the wash water is clear and then with methanol. The particles are dried at 50 °C for 12 hours. Example 3 Preparation of gold-plated high styrene content styrene copolymer particles using particles with a reactive group conditioned surface. Example 1 is repeated but using particles of 70% ST: 10% DVB: 20% glycidyl methacrylate which have been treated with ethylene diamine. Example 4 Preparation of gold-plated low styrene content styrene copolymer particles using particles with a reactive group conditioned surface. Starting particles In this Example, 4 μm styrene copolymer particles (30% glycidyl methacrylate: 30% butyl methacrylate : 10% DVB: 30% ST) produced by the method of US-A-4336173 and subsequently treated with ethylene diamine were used. Activation Part 1 - In a 2L reactor 50 mL of an aqueous dispersion containing 50g of the particles was heated to 60°C. While stirring at 200 rpm, a solution of 600 ml 0.05 wt% ammonium tetrachloro pallade was charged and the mixture reacted for 25 minutes. The mixture was decanted and the particles were left to settle. The particles were washed with water until the wash water was clear. Part 2 - In a 2L reactor the palladium activated particles were heated to 60°C. While stirring at 200 rpm, a solution of 75 ml 10% borane dimethylamine complex in water was charged and the mixture reacted for 15 minutes. The activated particles were washed on a nutch, using an amount of washing water twice the reaction volume. Nickel plating In a 15L reactor a nickel -solution was prepared by mixing 8L water, 2L of a polyvinylpyrrolidone solution containing 50g of polyvinylpyrrolidone K-30 (from Fluka) per litre water, 200g tetra sodium pyrophosphate decahydrate, lOOg nickel -chloride hexahydrate, 60 ml 25% ammonia solution and IL of a silica dispersion containing lOg Aerosil 200 (from Degussa) in water. The mixture was stirred at a temperature of 22.5±2°C until all ingredients (except the silica) had dissolved. 50g activated particles were charged. While stirring at 300 rpm a solution of 250 ml 10% borane dimethylamine complex in water was charged and the mixture reacted for 30 minutes. The dispersion was decanted and the particles were left to settle. The particles were washed with water until the wash water was visually clear. Gold plating In a 15L reactor a gold-solution was prepared by mixing 6L water, 4.5L AREUS 7950 from Shipley, 45g potassium gold cyanide and IL of a silica dispersion containing 2.5g Aerosil 200 in water. The bath was heated to 75±5°C. While stirring at 300 rpm a dispersion of 50g nickel plated particles in IL water was charged and the mixture reacted for 35 minutes. The mixture was decanted and the particles were left to settle. The particles were washed with water until the wash water was visually clear. The gold plated particles were then charged into a 3L reactor, heated to 60°C+5°C and 25 μL mercaptohexan-1-ol was charged. The mixture was reacted for 30 minutes, cooled and then washed with methanol. The particles were dried at 50°C for 12 hours. Example 4 may be repeated using 200 μm styrene copolymer particles (30% glycidyl methacrylate: 30% butyl methacrylate: 10% DVB: 30% ST) prepared by the process of US-A-4336173 and subsequently treated with ethylene diamine . Example 5 Preparation of gold-plated low styrene content styrene copolymer particles. Starting particles In this Example 10 μm styrene copolymer particles (98% ST: 2% DVB) are used. Etching In a 2L reactor IL chrome sulphuric acid from Merck is heated to 65°C. While stirring at 400 rpm, 50g dry particles is charged and the mixture reacted for 10 minutes. The particles are washed on a nutch, using an amount of washing water twice the reaction volume. Neutralising In a 2L reactor an aqueous solution containing lOg sodium pyrosulfite is stirred at 400 rpm at room temperature, 50g etched particles are charged and the mixture reacted for 15 minutes. The particles are washed on a nutch, using an amount of washing water twice the reaction volume. Conditioning In a 2L reactor IL 0.5% DODUPRINT 218 from Doduco in water is heated to 25°C. While stirring at 400 rpm, 50g etched particles are charged and the mixture reacted for 10 minutes. The particles are washed on a nutch, using an amount of washing water half the reaction volume. Activation In a 2L reactor IL LeaRonald SMT Catalyst, from LeaRonald which consists of palladium-chloride, is heated to 30°C. While stirring 50g particles is charged and the mixture reacted for 10 minutes. The particles are washed on a nutch, using an amount of washing water twice the reaction volume. Nickel and gold plating This was effected as in Example 4. Example 6 Electron micrography Scanning electron micrographs of the following gold- plated polymer microspheres appear in the accompanying Figures : Figure 1: 11.5 μm particles commercially available from Sekisui Figure 2: 10 μm 98% ST, 2% DVB gold-plated particles Figures 3a and 3b: 10 μm 98% ST, 2% DVB gold-plated particles Figures 4a and 4b: 10 μm 70% ST, 10% DVB, 20% glycidyl methacrylate gold-plated particles according to Example 3 Figures 5a and 5b: 10 μm 50% ST, 10% divinylbenzene, 40% glycidyl methacrylate gold- plated particles prepared analogously to Example 1 Figure 6: 4 μm 30% glycidyl methacrylate, 30% butyl methacrylate, 10% divinyl benzene, 30% ST gold-plated particles according to Example 4 Figure 7: 4 μm 30% glycidyl methacrylate, 30% butyl methacrylate, 10% divinyl benzene, 30% ST nickel-plated particles according to Example 4 (surfaces show silica stabilizer particles) Figure 8: 4 μm 30% glycidyl methacrylate, 30% butyl methacrylate, 10% divinyl benzene, 30% ST gold-plated particles prepared according to Example 4 but without use of silica stabilizer Figures 9a and 9b gold plated particles of Figure 1 (11.5 μm) and Example 4 (however of 10.6 μm rather than 4 μm diameter) following heating to 150°C and application of pressure; the particles of Figure 1 broke at a pressure of about 700 mg/particle while those of Figure 6 withstood pressures of up to 1100 mg/particle.

Claims: Claims : 1. Electroconductive particles comprising a styrene copolymer core and an external gold coating, characterised in that as said copolymer core is used a styrene copolymer comprising less than 50 wt. % styrene residues . 2. Particles as claimed in claim 1 wherein the copolymer core has a styrene content of 25 to 45 wt %. 3. Electroconductive particles comprising a styrene copolymer core and an external gold coating, characterised in that as said copolymer core is used a styrene copolymer produced using styrene and a functionalized comonomer and subsequently palladinated by reaction with a solution of a palladium compound. 4. Particles as claimed in claim 3 wherein the copolymer core has a styrene content of 0.5 to 98.5 wt 5. Particles as claimed in claim 3 wherein the copolymer core is as defined in either one of claims 1 and 2. 6. Particles as claimed in any one of claims 1 to 4 having a nickel coating interior to said gold coating. 7. Particles as claimed in claim 6 wherein said nickel coating has a thickness of 200 to 1000 A. 8. Particles as claimed in any one of claims 1 to 7 wherein said gold coating has a thickness of 50 to 600 A. 9. Particles as claimed in any one of claims 1 to 8 wherein at least one acrylic or methacrylic acid ester is a comonomer for said copolymer. 10. Particles as claimed in any one of claims 1 to 9 wherein the gold coating is surface treated with a thiol. 11. Particles as claimed in any one of claims 1 to 10 having a mode particle diameter of 0.5 to 500 μm. 12. Non-electroconductive particles comprising electroconductive particles as claimed in any one of claims 1 to 11 coated with a non-conductive coating. 13. A process for the production of gold-plated polymer particles, said process comprising: (i) palladinating functional groups in functional group containing styrene copolymer particles by contacting said particles with a solution of a palladium compound; (ii) metal-plating the palladinated particles with a metal having a standard electrode potential less than that of gold in the presence of a reducing agent; and (iii) gold-plating the metal-plated particles. 14. A process as claimed in claim 13 wherein the palladinated particles are nickel plated. 15. A process as claimed in either of claims 13 and 14 wherein metal and gold plating is effected in an aqueous solution containing dispersed particulate silica. 16. A process as claimed in claim 15 wherein said silica has a particle size of about 5 to 15 nm. 17. A process as claimed in any one of claims 13 to 16 wherein the resulting gold-plated particles are treated with a thiol . 18. A process as claimed in claim 17 wherein said thiol is a thioalkanol . 19. An electroconductive adhesive composition comprising an adhesive matrix material with disposed therein electroconductive particles, characterised in that said particles comprise electroconductive particles according to any one of claims 1 to 11, particles as claimed in claim 12 or electrocoaductive particles or produced by a process as claimed in any one of claims 13 to 18. 20. The use of an adhesive composition as claimed in claim 19 for providing an electrical connection between electronic components. 21. Use as claimed in claim 20 for providing an anisotropic electrical connection between electronic components . 22. Metal-plated polymer particles produced by a process comprising: (i) palladinating functional groups in functional group containing styrene copolymer particles by contacting said particles with a solution of a palladium compound; and (ii) metal-plating the palladinated particles in the presence of a reducing agent . 23. The use of particulate silica having a particle size in the range 5 to 15 nm as a stabilizer in metal- plating of palladinated polymer particles. 24. The use of particulate silica having a particle size in the range 5 to 15 nm as a stabilizer in gold- plating of metal-plated polymer particles. 25. A formed polymer product characterized in that particles as claimed in any one of claims 1 to 12 and 22 are dispersed in the polymer. 26. A coating composition comprising a liquid carrier with dispersed therein particles as claimed in any one of claims 1 to ' 12 and 22 dispersed in the polymer.

Inventors: BERGE ARVID TRYGVE, MOLTEBERG ASTRID EVENROED, BERGE, ARVID, TRYGVE, MOLTEBERG, ASTRID, EVENROED
Applicants: BERGE ARVID TRYGVE, DYNO SPECIALTY POLYMERS AS, MOLTEBERG ASTRID EVENROED, BERGE, ARVID, TRYGVE, MOLTEBERG, ASTRID, EVENROED
Application year: 1999
Main classification: H01B1
IPC codes: B22F1, C08F220, C08J3, C08J5, C08K3, C08L33, C08L101, C09J9, H01B1, H01B13, H01L21, H01R11, H05K3