A method for preparing a vinyl polymer-polyolefine composite

Abstract: A method for preparing a polyolefine-vinyl polymer composite, in which 10-200 parts of weight of vinyl monomer and 0.01-4.0 parts of weight, based on 100 parts of weight of vinyl monomer, of a free radical polymerization initiator are impregnated into 100 parts of weight6 of polyolefine particles by blending these at a temperature of 20-130°C in the absence of water whilst maintaining the particle structure of the polyolefine and in which method 80-1000 parts of weight, based on 100 parts by weight of polyolefine are vinyl monomer, of suspension water as well as stabilizing agent, are added to the polyolefine and vinyl monomer before the temperature of the water suspension is increased to polymerize the vinyl monomer, characterized in that the suspension water and stabilizing agent are added when 50-99% of the monomer has been absorbed in the polyolefine particles.

Description: The invention relates to a method for preparing a vinyl polymer -polyolefine composite, in which 10-200 parts of weight of vinyl monomer and 0.01-4.0 parts of weight, based on 100 parts of weight of vinyl monomer, of a free radical polymerization initiator are impregnated in 100 parts of weight of polyolefine particles by slowly blending these at a temperature of 20-130°C without water by maintaining the particle structure of the polyolefine and in which method 80-1000 parts of weight of suspension water are added, based on 100 parts of weight of polyolefine + vinyl monomer, as well as a stabilizing agent, before the temperature of the water suspension is increased for polymerizing the vinyl monomer The present invention relates to a new way of preparing a polyolefine composite, which can be applied to be used as such and processed into various articles, e.g. as foamed plastic, as compatibilisator, or as a component in semiconducting layers on electric cables. The composite is comprised of a polyolefine and a vinyl polymer, and the invention relates to the preparation of this composite by polymerizing the vinyl monomer inside the polyolefine particles. For improving rigidity, dimensional stability, adhesion properties against other polymers and materials, printability and the like of polyolefines, which are to be worked into various articles or which are to be foamed into foamed plastic, attempts have been made to blend the polyolefine with some vinyl polymer. Because different polymers often are incompatible with each other, it has however appeared to be difficult to achieve homogeneous blends with an attractive apprearance and good physical properties. For avoiding these problems, attempts have been made to polymerize the vinyl monomer inside the polyolefine particles. Basically two different methods of polymerizing the vinyl monomer in situ in the polyolefine particles have been suggested, and both methods are based on the fact that the vinyl monomer is allowed to diffuse into the polyolefine particles, after which the polymerization of the vinyl monomer occurs. The greatest difference between the two methods is the way, in which the vinyl monomer is allowed to diffuse into the polyolefine particles. In the West German patent DE 29 07 662 is described the polymerization of styrene in situ in several different polyolefines. In this method, styrene is added slowly into a water suspension containing polyolefine particles at an elevated temperature. This means that impregnation and polymerization of the styrene occur simultaneously with the result that the polymerization tends to occur more in the surface regions of the polyolefine particles, which results in that the polystyrene is concentrated on the surface layer of the polyolefine particles. In the US patent 4.412.938 is described the polymerization of styrene in situ in an ethylene vinyl acetate copolymer. In this method, all styrene is added at a time into a water suspension containing ethylene vinyl acetate copolymer particles. The styrene is added at so low a temperature that no polymerization occurs. Only after all styrene or most of the styrene has diffused into the ethylene vinyl acetate copolymer particles, the temperature is increased and the polymerization starts. A disadvantage of this method is that it takes several hours before the styrene has diffused into the ethylene vinyl acetate copolymer particles. The method is in other words time-consuming. In this patent is described the preparation of a polyolefine - vinyl polymer composite by means of a method, which avoids the problems and disadvantages related to above-mentioned preparation methods. However, the method maintains the advantages of the above-mentioned methods, which advantages are that a homogenous blend of the polyolefine and the vinyl polymer is obtained and that the polymerization product is obtained in a particle form. The inventive method is mainly characterized in that the suspension water and stabilizing agent are added when 50-99% of the amount of the monomer has been absorbed into the polyolefine particles. The preferred embodiments of the invention are given in the subclaims. After the 100 parts of weight of polyolefine particles have been blended with 10-200 parts of weight of vinyl monomer and 0,01-4 parts of weight, based on 100 parts of weight of monomer, of a free radical initiator, the blend is agitated slowly at so low a temperature that no decomposition of the initiator and no polymerization occur, but the temperature is yet so high that the polyolefine particles are impregnated with the monomer. The impregnation is carried out without water until 50-99% of the amount of the monomer has been absorbed in the polyolefine particles whereafter the whole amount of the suspension water and stabilizing agent is added. After that the impregnation continues a short time in the suspension stage to complete the absorption of the monomer in the polyolefine particles. In this method for preparing a polyolefine - vinyl polymer composite, the absorption of the polyolefine may thus be divided into two steps. In the first step the impregnation of 50-99% of the vinyl monomer occurs in the absence of water. In the second step the impregnation of the rest of the monomer occurs in the presence of the suspension water. This means that the monomer, to be able to penetrate into the polyolefine particles, during the first impregnation step does not have to be transported through any water phase, which means that the whole impregnation is faster than in the method described in the US patent 4,412,938 in which the suspension water is present during the whole impregnation. During the impregnation, the polyolefine particles partly swell depending on how much vinyl monomer has been added, but the particle form of the polyolefine is still maintained. In Neste Oy's patent application FI 894461 (EP 418861) is described a method for preparing a polyolefine - vinyl polymer composite, in which method the whole impregnation, the impregnation of 100% of the vinyl monomer into the polyolefine particles occurs in the absense of water. In comparison with the application FI 894461, the present method has two advantages. Firstly, the power demand of the agitator motor is lower, since the suspension water is added in the second step of the impregnation. Hereby the peak power demand is avoided which otherwise is existing in the end of the impregnation when the whole monomer amount has been absorbed in the polyolefine particles. Secondly there is no risk for the particle to decompose in the end of the impregnation as the suspension water is present. In the patent application FI 904586 (EP 476960) of Neste Oy there is described a method for preparation of polyolefine vinyl polymer composite in which a little amount of water is added during the impregnation. In comparison with 904586 the method in this application has the advantage that it is more simple to carry out in the practice beacuse all the suspension water is added at the same time. The invention is next described in detail. Polyolefine Useful polyolefines include high density polyethylene, low density polyethylene and linear low density polyethylene. The polyethylene can be a homopolymer or a copolymer. The comonomer for ethylene can be e.g. vinyl acetate, vinyl chloride, propene or some other α-olefin, C₁-C₇-alkyl acrylates and -methacrylates, acrylic acid and -methacrylic acid, hydroxy alkyl acrylates and -methacrylates, glycidylacrylate and -methacrylate, dienes such as hexadiene-1,4, hexadiene-1,5, heptadiene-1,6, 2-methyl pentadiene-1,4, octadiene-1,7, 6-methyl heptadiene-1,5 and polyenes such as octatriene and dicyclo pentadiene. Also ethylene-α-olefine-polyene-terpolymers are useful. Useful α-olefines include propylene, butene, pentene, isofrene, hexene or their mixtures, and useful polyenes include hexadiene-1,4, hexadiene-1,5, heptadiene-1,6, 2-methyl pentadiene-1,4, octadiene-1,7, 6-methyl heptadiene-1,5, octatriene, dicyclo pentadiene. In case the ethylene polymer is a copolymer, the share of the ethylene in the copolymer must be at least 50% by weight. The polyolefine can also be comprised of polypropylene and its copolymer. The propene polymers can consist of more than 50% by weight of propylene and can be a random or block copolymer of propylene and ethylene. Also other α-olefines can be conomomers and also dienes as hexadiene-1,4, hexadiene-1,5, heptadiene-1,6, 2-methyl pentadiene-1,4, octadiene-1,7, 6-methyl heptadiene-1,5 and polyenes as octatriene and dicyclo pentadiene or another polar unsaturated monomer. The polyolefine must be in a particle form with a particle size of 0.5-10 mm, most preferably 1-6 mm. When the polyolefine is in a particle form, it is easy to achieve a good agitation during the impregnation phase, which is a precondition for the fact that the concentration of the vinyl monomer becomes the same in all polyolefine particles. If the particles are too large, it may be difficult to keep the suspension stable during the final step of the polymerization. Stability problems can also occur in connection with small particles. Any vinyl monomers which can be polymerized with free radical polymerization technique are suitable to be used as vinyl monomers. Examples of such vinyl monomers are styrene, substituted styrenes such as methyl styrene, isopropyl styrene, chloro styrene, α -methyl styrene and α-ethyl styrene, C₁-C₁₀-alkyl acrylates and methacrylates, hydroxy alkyl acrylates and methacrylates, glycidyl acrylate, glycidyl methacrylate, acrylo nitrile, methacrylonitrile, vinyl halides, maleic anhydrides, acrylic acid, methacrylic acid, acrylic amide, methacrylic amide, vinyl acetate and other alkylates. These vinyl monomers can be used separately or mixed with each other. If it is desired to crosslink the vinyl comonomer a minor amount of another comonomer can be used containing two or more double bonds. The amount of that comonomer with two or more double bonds is 0,01-10 % by weight of the total amount of vinyl monomer. Suitable monomers with two or more double bonds are for example divinyl benzene, di(meth)acrylates such as 1,4-butanediole dimethacrylate and 1,2-butenediol dimethacrylate and di-cyclo pentadiene. The quantity of the vinyl monomer to be polymerized in the polyolefine matrix is 10-200 parts of weight, based on 100 parts of weight of polyolefine. A larger quantity of vinyl monomer than 200 parts of weight causes problems such that it is difficult to keep the polyolefine in a particle form during the impregnation; the particles tend to agglomerate and form a homogenous phase. It is not appropriate to add a smaller quantity of vinyl monomer than 10 parts of weight, since such quantities of vinyl monomer provide only small changes in the properties of the initial polyolefine. Initiators, which are used for polymerizing the vinyl monomer, are initiators, which are conventionally used in the suspension polymerization and include organic peroxides, such as benzoyl peroxide, lauroyl peroxide, t-butyl perbenzoate, t-butyl-peroxy-2-ethyl hexanate, t-butyl peroxide, dikumyl peroxide, di-t-butyl peroxide, bis(t-butyl peroxyisopropyl)benzene, t-butyl peroxy- isopropyl carbonate, as well as azo compounds, such as azobis- isobutyronitrile and azobis-dimethyl valeronitrile. More than one initiator are preferably used simultaneously so that the polymerization starts at a low temperature with a low-temperature initiator and is completed at a high temperature with a high-temperature initiator. The total amounts of the initiator may be 0.01-4 parts of weight, most preferably 0.1-1.2 parts of weight, based on 100 parts hy weight of vinyl monomer. The impregnation is started so that polyolefine particles, vinyl monomer and initiators are added to a reactor in any order. If the initiator or the initiators are in powder form they are suitable dissolved in a part of or the whole amount of the vinyl monomer to be sure of that the amount of initiator is the same in the different polyolefine particles. Of the same reason also the liquid initiators can be mixed with the vinyl monomer before they are mixed with the polyolefine particles. The temperature during the impregnation is 20-130°C depending on the type of polyolefine and vinyl monomer, i.e. depending on how easily the vinyl monomer penetrates into the polyolefine. The impregnation temperature is to be so low that practically no polymerization occurs during the impregnation phase. The impregnation temperature must thus be observed when selecting the initiator. The impregnation generally lasts for 0.2-3.0 hours depending on how easily the vinyl monomer penetrates into the polyolefine particles and depending on whether the impregnation has been performed at an elevated temperature or not. It is not necessary to perform the impregnation in the same reactor as the polymerization. The inventive step in this invention is then that the absorption of the vinyl monomer into the polyolefine particles is carried out in two steps. During the first step the impregnation is carried out totally in the absence of water until 50-99% of the vinyl monomer has been absorbed. To distribute the vinyl monomer it shall be well mixed during the first impregnation step. The agitation rate expressed as the end speed of the agitator is not critical but most preferably it shall be in the range of 0.1-1.0 m/s. If the agitation rate is too low the vinyl monomer can be unequally distributed between the polyolefine particles. On the other hand, if the agitation rate is too high the polyolefin particles may not keep their particle form. Sometime in the end of the impregnation the agitation of the particles gets worse depending on the agitator system, the amount of vinyl monomer and the polyolefine-vinyl monomer couple in question when 50-99% of the vinyl monomer has been absorbed in the polyolefine particles. In this stage of the impregnation the whole amount of the suspension water and stabiliser shall be added to be sure that the vinyl monomer is distributed uniformly between the polyolefin pellets. Thereafter the monomer is absorbed into the polyolefine particles. When 50-99% of the vinyl monomer amount has been absorbed in the polyolefine particles the whole amount of suspension water and suspending agent are added and the agitation rate is increased to values usual in connection with suspension polymerization in other words to such values that it is possible to maintain a good agitation in the reactor and to keep the suspension stable. Such subtances can be used as suspending agents, which are normally used in suspension polymerization of vinyl monomers. These include e.g. water soluble polymers, such as polyvinyl alcohol, polyvinyl pyrrolidone and methyl cellulose or partially water soluble subtances, such as calcium triphosphate and magnesium pyrophosphate. The total amount of suspension water is not critical, but it must be so large that the suspension is maintained during the polymerization, which means 80-1000 parts of weight, more preferably 100-500 parts of weight of water on 100 parts of weight of polyolefine + vinyl monomer. If the first impregnation step has been performed at an elevated temperature, the water is preferably heated to the same temperature, before it is blended with the polyolefine particles swollen by the vinyl monomer. This to prevent the part of the vinyl monomer which has been absorbed into the polyolefine particles from diffusing out of the polyolefine particles due to the sudden decrease in the temperature in case the temperature of the water added is lower than the temperature of the polyolefine impregnated with the vinyl monomer. Time is saved at the same time because no time is wasted to warm up the water in the reactor. After that the suspension water and the stabilisator have been added to the reactor the impregnation continues at the same temperature as before the addition of the water for max 1,5 hours to allow the rest of the amount of the vinyl monomer, 50-1% of the initial amount of vinyl monomer, to be absorbed into the polyolefine pellets. The polymerization of the vinyl monomer which has been absorbed into the polyolefine particles occurs by raising the temperature in the agitated reactor, whereby the initiator decomposes and initiates the polymerization. The polymerization can be performed at one or more temperatures within the temperature range 50-150°C. The polymerization generally lasts for 5-20 hours. After the polymerization has been completed, the reactor is cooled and the product is then finished in a way normal in suspension polymerizations (e.g. washing and drying), and it is then ready for further treatment. The polyolefine particles retain their particle form during the polymerization. In comparison with the original polyolefine particles, the particles are after the polymerization only slightly larger depending on the absorbed and polymerized vinyl monomer. Properties of polymerization product The polymerization product provides a homogenous impression and is esthetically attractive. The vinyl polymer polymerized in the polyolefine particle is distributed as pearls of a size 0.05-2.0 µm, which are homogenously distributed in the polyolefine matrix. The concentration of the vinyl monomer is as high in the middle as in the outer regions of the particle, determined from infrared microscopy. Since the vinyl monomer is polymerized inside the polyolefine particle, part of the polymerized vinyl monomer is in the form of a homopolymer and part in a form grafted on the polyolefine. Even though the share of the grafted vinyl polymer in some cases is smaller than the share of the homopolymer, its existence is important for the morphological stability of the composite during processing. A feature of this invention is that the morphology of the composite remains unchanged after treatment, i.e. that the vinyl polymer remains in the form of a pearl with a size of 0.05-2.0 µm homogenously distributed in the polyolefine matrix. If the polyolefine is modified with vinyl monomers, the polymers of which have high glass transition temperature, as for example styrene and methyl methacrylate, the hardness, rigidity and resistance of the polyolefine can be increased. But if the polyolefine is modified with vinyl monomers, with rubber-like polymers the polyolefine can be made more elastic. Use of the composite Polymer composites prepared according to this invention can be used in many different ways mainly depending on the type of polyolefine and vinyl monomer used as well as their mutual proportions. Accordingly, it is e.g. possible to increase the mechanical strength on many polyolefines by polymerizing in situ a vinyl monomer inside the polyolefine. Also e.g. the hardness and rigidity on the ethylene vinyl acetate copolymer and polypropene can be increased by polymerizing into these in situ styrene. These composites can be used as such and processed into various articles. The composites can also be blended with other thermoplasts whereby the resultant composite has above-mentioned advantages. Ethylene vinyl acetate copolymer - polystyrene composites can be impregnated with some conventional volatile media, such as iso- or n-pentane, and thereafter expanded with water vapour into foamed plastic. Such a foamed plastic has better elastic properties and a better resistance to chemicals than polystyrene foam. Polypropene-polystyrene composite films prepared according to this invention can be stretched in one or two directions and then used as synthetic paper. Ethylene vinyl acetate copolymer - polystyrene composites can be one component in the semiconducting layer of electric cables, which are thereby easy to strip from the cable during coupling work. The adhesion of the polyolefine and also other polymers and materials to itself can be changed by modifying a polyolefine in this way, which can be used in connection with peelable seal applications in for example lids of yoghurt packages and different plastic bag packages. A further application for these modified polyolefines is as compabilisators. If polyolefine A is grafted with vinyl polymer B can this grafted polyolefine A-B work as compabilisator between polyolefine A and vinyl polymer B. EXAMPLES Example 1 50 parts of weight (1000 g) of ethylene vinyl acetate particles with a diameter of 3-4 mm were added into a 10-liter reactor. The ethylene vinyl acetate copolymer was Atochem's product Evatone and contained 28% by weight of vinyl acetate and its melt index was 5 g/10 min, measured with 2.16 kg and at 190°C. 50 parts of weight of 2-ethyl hexyl acrylate and as initiator 0,135 parts of weight of azobisisobutyronitrile (AIBN) and 0,130 parts of weight of benzyl peroxide (BPO) were added thereafter. Before the addition of the monomer and the initiators to the reactor the reactor and the monomer solution were rinsed with nitrogen. The impregnation was carried out at 40°C with an agitation rate of 30 rpm. After 50 minutes ca 90% of the monomer has been absorbed whereafter 290 parts of weight of water and 1 part of weight tricalcium phosphate as stabilisator and 0,03 parts of weight of sodium dodecylbenzene sulphonate were added. The water addition is carried in two steps of approximately equal amounts with the suspension agent in the first one. Before the water was added to the reactor it had been bubbled through with nitrogen. The agitation rate was raised to 200 rpm. The temperature of the reactor was thereafter increased in 20 minutes to 55°C which maintained in 3 hours. Thereafter the temperature was increased to 90°C in 8 hours which was maintained in 7 hours. After cooling, the reactor was emptied and the EVA-poly(2-ethylhexyl acrylate) particles with the size of 4-5 mm was washed and dried. The particles were homogeneous and almost transparent. It could be stated by means of transmission electron microscope (TEM) that the poly(2-ethylhexyl acrylate) was dispersed in form of big pearls of the size of 0,1 µm in the EVA matrix. The product was very elastic and rubberlike. The melt index of the product is ca 1,0 g/10 min. at 230°C and 15 kg. Example 2 This example was carried out in accordance with Example 1 with the difference that the monomer was a mix of 36,5 parts of weight of methyl metacrylate and 13,5 parts of weight of styrene. The initiators used were 0,150 parts of weight of AIBN, 0,10 parts of weight of BPO and 0,075 parts of weight of tert-butyl peroxy perbenzoate (t-BPB). After 65 minutes ca 90% of the monomer has been absorbed in the EVA particles whereafter the suspension water was added. After further 20 minutes the temperature was raised to 55°C and the polymerization was made in the same way as in Example 1 with the difference that the temperature in the end of the polymerization was raised to 260°C in 4 hours. The separate and homogeneous product particles have an opaque appearance and they are much harder than the initial EVA. With TEM it could be stated that poly(methyl metacrylate styrene) is dispersed in form of ca 0,2 µm big pearls in the EVA matrix. The melt index of the product is 0,2 g/ 10 min. at 260°C and 5 kg. Example 3 50 parts of weight (25 kg) of EVA pellets with the diameter 3-4 mm were added to a 200 litre reactor. The EVA was Neste Oy's commercial quality NCPE 5028, containing 28% by weight of vinyl acetate with the melt index of 5 g/10 min. at 190°C and 2,16 kg. 50 parts of weight of styrene and as initiator 0,58 parts of weight of dicetyl peroxy carbonate (d-CPK), 0,13 parts of weight of BPO and 0,050 parts of weight of t-BPB was added to the reactor. The agitation rate was 40 rpm and the temperature 30°C during the impregnation. After 20 minutes ca 60% of the monomer has been absorbed in the EVA pellets. Thereafter 210 parts of weight of water is added and the same stabilisator as in Example 1 and the agitation rate was raised to 105 rpm. After further 40 minutes at this temperature the temperature is increased to 55°C to start the polymerization. Thereafter the temperature is increased in 6 hours to 60°C and is maintained in 2,5 hours whereafter the temperature is raised to 130°C for 3 hours. The product particles with the size of 4-6 mm are free flowing homogeneous and white. With TEM it could be stated that the polystyrene is dispersed in form of ca 0,3 µm pearls in the EVA matrix. With microscope IR it could be stated that the amount of polystyrene is the same in different parts of weight of the EVA pellets (50% ± 2%) and that the polystyrene concentration does not vary between different EVA pellets. The melt index of the product was 1,6 g/10 min. Example 4 This example was carried out as Example 3 with the difference that EVA contained 18% by weight vinyl acetate and the melt index was 2 g/10 min., 190°C and 2,16 kg. 0,040 parts of weight of azo-bisisobutyronitrile (AIBN), 0,31 parts of weight of BPO and 0,050 parts of weight of t-BPB were used as initiators. After that the styrene had been absorbed to ca 60% at the temperature 40-50°C during 30 minutes, water and suspension agent was added and the impregnation thereafter was allowed to continue in 1,5 hours at 50°C. The polymerization was done at 70°C during 1 hour at 70-90°C during 3 hours, at 90°C during 3 hours and finally at 130°C during 3 hours. The product was stated to have the same structure and appearance as in Example 3 and its melt index was 0,3 g/10 min. Example 5 This example was carried out in accordance with Example 4 with the difference that the polyolefine was Neste's commercial product NCPE 0469. This quality is a terpolymer containing 80% of ethylene and butyl acrylate and 2-hydroxy ethyl methacrylate. The polymerization was done in a 22 litre reactor why the amounts of the different materials is 8 times smaller than in Example 4. The product particles are free, homogeneous and white. Example 6 This example was carried out as Example 5 with the difference that the polyolefine was the commercial quality NCPE 5010 of Neste Oy containing 9% by weight vinyl acetate with the melt index of 8 g/ 10 min. The initiator used was 0,25 parts of weight of BPO and 0,04 parts of weight of t-BPB. After 80 minutes impregnation starting at 20°C and ending at 70°C, ca 90% of the monomer had been impregnated whereafter the water and the suspension agent was added. The impregnation was allowed to continue for further 1 hour at 70°C whereafter the temperature was raised to 80°C for 1 hour, 90°C for 4 hours and finally 130°C for 3 hours. The product particles are free flowing, homogeneous and white. Example 7 50 parts of weight, 1000 g of polypropene (PP) in pellet form was added to a 10 litre reactor with a diameter of 3-4 mm. The polypropylene was Neste's commercial quality XB 8050 E which contains 3% of ethylene and has the melt index of 8 g/10 min., 230°C and 216 kg. Thereafter 50 parts of weight of styrene was added, in which styrene 0,2 parts of weight of t-BPB had been dissolved as initiator. After 45 minutes impregnation at 100°C ca 95% of the monomer blend had been absorbed in the PP. After addition of water and suspension agent the same amount as in Example 1, the temperature is raised until 110°C for 4 hours and thereafter to 120°C for 2 hours and finally to 130°C for 2 hours. The 4-6 mm size product pellets are free flowing, homogeneous and white. With TEM it was stated that the polystyrene is dispersed as 0,3 µm big pearls in the PP matrix. The melt index of the product is 2,9 g/10 min. Example 8 50 parts of weight, 750 g of polypropene in pellet form was added to a 10 litre reactor with the diameter of 3-4 mm. PP was neste's commercial quality XB 1851, containing 3% of ethylene and with a melt index 1,8 g/10 min., 230°C and 2,16 kg. Thereafter 50 parts of weight of butyl acrylate was added, in which 0,2 parts of weight of dicumyl peroxide had been dissolved as initiator. After 1 hour impregnation at 105°C, ca 95% of the monomer mixture had been absorbed in the PP pellets. After addition of water and suspension agent, the same amount as in Example 1, the temperature was raised to 120°C during 1 hour to let the last rests of the monomer and the initiator to be absorbed in the pellets. After 4 hours at 120°C the temperature was raised to 130°C for 1 hour and thereafter 140°C for 1 hour. The product pellets are free flowing, homogeneous and white.

Claims: A method for preparing a polyolefine-vinyl polymer composite, in which 10-200 parts by weight of vinyl monomer and 0.01-4.0 parts by weight, based on 100 parts by weight of vinyl monomer, of a free radical polymerization initiator are impregnated into 100 parts by weight of polyolefine particles by blending these at a temperature of 20-130°C in the absence of water whilst maintaining the particle structure of the polyolefine and in which method 80-1000 parts by weight, based on 100 parts by weight of polyolefine and vinyl monomer, of suspension water as well as stabilizing agent, are added to the polyolefine and vinyl monomer before the temperature of the water suspension is increased to polymerize the vinyl monomer, characterized in that the suspension water and stabilizing agent are added when 50-99% of the monomer has been absorbed in the polyolefine particles. A method according to claim 1, characterized in that the polyolefine is a polyethylene or an ethylene copolymer derived from more than 50% by weight of ethylene, together with a comonomer such as vinyl acetate, an α-olefine, acrylic or methacrylic acids or their C₁-C₇ alkyl-esters, a hydroxy alkyl acrylate or methacrylate, a glycidylacrylate, a diene, a polyene or vinyl chloride. A method according to claim 1, characterized in that the polyolefine is a polypropene or a propylene copolymer derived from more than 50% by weight of propene together with a comonomer such as ethylene, an α-olefine or another polar unsaturated monomer. A method according to any one of the preceding claims characterized in that the diameter of the polyolefine particles is from 0.5 to 10 mm. A method as claimed in any one of the preceding claims, characterized in that the vinyl monomer is a monomer polymerizable by free radical polymerization such as styrene, a subtituted styrene (e.g. methyl styrene), isopropyl styrene, chloro styrene, α-methyl styrene and α-ethyl styrene, a C₁-C₁₀ alkyl acrylate or methacrylate, an hydroxyalkyl acrylate or methacrylate, glycidyl acrylate, glycidyl methacrylate, acrylonitrile, methacrylonitrile, a vinyl halide, maleic anhydride, acrylic acid, methacrylic acid, acrylamide, methacrylamide or vinyl acetate. A method as claimed in any one of the preceding claims, characterized in that the vinyl polymer from the vinyl monomer is cross linked by adding 0.01-10% by weight, based on the total amount of the vinyl monomer, of a monomer with two or four double bonds such as divinyl benzene, a diacrylate or dimethacrylate or dicyclopentadiene. A method as claimed in any one of the preceding claims, characterized in that the initiator is an organic free radical polymerization initiator such as a peroxide or an azo compound (e.g. benzoyl peroxide, lauroyl peroxide, t-butyl peroxybenzoate, dicumyl peroxide or azobis-isobutyronitrile). A method as claimed in any one of the preceding claims, characterized in that the polymerization of the vinyl monomer is effected at a temperature of 50-150°C. A method as claimed in any one of the preceding claims, characterized in that the vinyl monomer is polymerized inside the polyolefine particles, so that the vinyl polymer is homogenously dispersed as round pearls with a size of 0.05-2.0 µm in the polyolefine matrix.

Inventors: LEHTINIEMI ISMO, VESTBERG TORVALD, LEHTINIEMI, ISMO, VESTBERG, TORVALD
Applicants: NESTE OY
Application year: 1993
Main classification: C08F255
IPC codes: C08F2, C08F255