Polystyrene modified with a telechelic polyorganosiloxane

Abstract: A crumb-like silicone rubber powder is uniformly dispersed in a polystyrene polymer using conventional equipment, such as a twin screw extruder, to provide a resin having a ten fold improvement in impact strength over the unmodified polymer. The silicone rubber powder is prepared by isolating the particles obtained from a polymerization of an unsaturated monomer in the presence of an aqueous emulsion of a unsaturated telechelic polydiorganosiloxane which has been prepared using an organotin curing catalyst and a dihydrolyzable grafting silane.

Description: The present invention relates to polystyrene polymer compositions having high impact strength. More particularly, the polystyrene polymers are modified with a silicone crumb rubber prepared by polymerizing an unsaturated monomer in the presence of an aqueous emulsion of a non-crosslinked, telechelic polydiorganosiloxane. Polystyrene (PS) is one of the largest volume thermoplastic resins in commercial production today. This ubiquitous material is well suited to many "low performance" applications wherein its brittle nature is of little consequence. Additionally, many other applications requiring greater impact resistance have led to the advent of various modifications of these plastics. Thus, styrene-based copolymers, and particularly PS resins which are modified with organic rubber particles, are a commercially viable alternative to the more exotic and expensive engineering plastics for certain applications. One such system, known in the art as high impact polystyrene (HIPS), can have an impact strength which is an order of magnitude greater than the virgin resin but suffers from poor thermal stability, particularly in the presence of oxygen. These modified PS resins are typically prepared by polymerizing a solution of an unsaturated organic rubber, such as polybutadiene, in styrene monomer. The addition of various rubber compositions to other thermoplastic resin systems has also proved beneficial. For example, JP-A 2-263861 discloses a thermoplastic resin composition having a high impact strength, high heat resistance and good resistance to organic solvents. This composition comprises a blend of polyphenylene ether (PPE) resin, a polyester resin and a rubber-like elastomer and/or modified rubber-like elastomer. A preferred elastomer component of this prior art disclosure is obtained by the graft copolymerization of at least one vinyl monomer with a composite rubber consisting of a silicone rubber and a polyalkyl methacrylate interlocked with each other. In the production of the composite rubber component, a cyclic diorganosiloxane is emulsion polymerized with a crosslinker and, optionally, with a graft crosslinking agent using a sulfonic-acid series emulsifying agent. In a subsequent step, a combination of an alkyl (meth)acrylate, a crosslinker and a graft crosslinking agent is used to swell the silicone particles of the above emulsion and an initiator is then introduced to polymerize this system. In a similar approach, US-A 5,047,472 teaches thermoplastic molding compositions comprising PPE resin or a PPE resin containing a polystyrene resin, which is modified with a multi-stage polyorganosiloxane/vinyl-based graft polymer. These compositions are stated to have improved impact resistance, flame resistance and moldability. In this case, the graft copolymer is prepared by a "co-homopolymerization" technique wherein an emulsion containing a diorganosiloxane, a crosslinker and a graft-linker is polymerized concurrently with the polymerization of a vinyl monomer. The resulting first stage polymeric co-homopolymerized substrate is then grafted with a vinyl polymer in at least one subsequent stage. This multi-stage polydiorganosiloxane polyorganosiloxane/vinyl-based graft polymer formed according to these methods was also employed in US-A 4,939,205 to augment the impact resistance of polycarbonate resin compositions. The graft polymer was further used in US-A 4,939,206 to modify various thermoplastic resins with the object of providing flame retardant compositions having improved impact resistance. Further, US-A 4,690,986 claims a polydiorganosiloxane/polystyrene copolymer. However, our invention is distinguishablee from this latter patent in that crosslinking occurs in our invention between the polydiorganosiloxane molecules during an emulsion polymerization. The latter patent also teaches that the grafting polymer attaches to the polydiorganosiloxane during the emulsion polymerization at the same time as the formation of crosslinks between the polydiorganosiloxane molecules. Further, the crosslinking and attachment of the grafting polymer occurs in a random manner. As a result, neither the molecular weight nor the crosslinking density of the polydiorganosiloxane can be managed or controlled in the art. The resulting polydiorganosiloxane is a crumb rubber which is difficult to process during the copolymerization steps. Crumb rubbers are virtually impossible to characterize, for example, in terms of measuring their molecular weights. In contrast, the present invention teaches that the grafting polymer is attached to an end-capped polydiorganosiloxane during a condensation reaction in the presence of a tin catalyst. The attachment of the grafting group does not occur randomly on the polydiorganosiloxane during our emulsion polymerization, but instead attaches specifically at the two end groups of the polydiorganosiloxane molecules. Because it is not crosslinked, our polydiorganosiloxane is in the form of a gum and not an elastomer upon removal of water from the emulsion. This gum is easy to characterize, i.e., the molecular weight of the gum is readily measured by gel permeation chromatography (GPC). Upon copolymerizing the telechelic polydiorganosiloxane emulsion with styrene monomer and removing the water, the composition of our invention has the consistency of a crumb rubber. The present invention introduces a composition comprising: (A) a polystyrene polymer; and (B) a silicone crumb rubber powder uniformly dispersed in said polystyrene polymer, said silicone crumb rubber prepared by the steps comprising: (I) reacting a preformed aqueous polydiorganosiloxane emulsion comprising water, a surfactant and a plurality of silanol-terminated polydiorganosiloxane molecules, with a grafting silane in the presence of an organotin catalyst to form a telechelic emulsion polymer, wherein said grafting silane has the formula RQSi(X) 2 where X is a hydrolyzable group, Q is an unsaturated organic functional group, R is Q or a saturated monovalent hydrocarbon group of from one to six carbon atoms, and (II) thereafter co-polymerizing an unsaturated monomer with said telechelic emulsion polymer formed in step (I) to form particles therefrom; and (III) recovering the particles resulting from step (II), said composition containing from 5 to 50 parts by weight of said polydiorganosiloxane for each 100 parts by weight of said polystyrene polymer. The polydiorganosiloxane emulsion of step (I) is prepared using conventional methods. A grafting silane is then reacted with the polydiorganosiloxane in emulsion via a condensation reaction which takes place in the presence of a tin catalyst. The grafting silane replaces the silanol groups on the ends of the polydiorganosiloxane molecules to produce an emulsion of a non-crosslinked telechelic polydiorganosiloxane. A telechelic molecule is herein defined as a polydiorganosiloxane molecule with organic functional groups disposed at the polymer chain ends, which can be used to bond chemically to other types of molecules. No crosslinking occurs during formation of the telechelic polydiorganosiloxane emulsion. This is in contrast to the grafting silanes claimed in the prior art (EP 0 550 194), in which the three hydrolyzable groups at the silicon atom of the grafting silanes condense with silanols of other polydiorganosiloxane molecules to produce a crosslinked polyorganosiloxane or an emulsion of silicone rubber. The non-crosslinked telechelic polyorganosiloxanes of this invention therefore have the physical characteristics of a gum upon removal of water from the emulsion. The process of grafting the silane to the preformed aqueous emulsion polymer having a plurality of silanol-terminated polydiorganosiloxane particles is further described in US-A 08/268,349 (DC 4106). In steps (II) and (III), the non-crosslinked telechelic polydiorganosiloxanes are copolymerized with a monomer such as styrene, then recovered to form a crumb rubber powder by separating the water from the polymer particles. The crumb rubber is then added to the polystyrene polymer to improve the physical characteristics of the polystyrene polymer. This invention is an improvement over the prior art, since the starting polydimethylsiloxane emulsion is not pre-cured. The gum nature of our non-crosslinked telechelic polydiorganosiloxanes allow for optimization of the molecular weight, i.e., the characterization of the polydimethylsiloxane prior to addition of the unsaturated monomer. Polystyrene resins modified with the silicone gums of this invention exhibit up to a ten-fold increase in impact resistance over the virgin polystyrene. The crumb rubber powders of the present invention are also readily dispersible in polystyrene resins using conventional process equipment, such as a twin screw extruder. This offers a significant advantage to a plastics manufacturer since both resin and modifying crumb rubber powder are handled as particulate solid feeds and therefore amenable to facile introduction to mixing equipment (e.g., from a hopper). These crumb rubber powders can also be formulated as a "master batch" and used as a concentrate to further modify styrenic plastics. The polystyrene (PS) polymer (A) of this invention is well known in the art and is a homopolymer or copolymer prepared from styrenic monomers. For the present invention, styrenic monomers are substituted or unsubstituted versions of the basic structure Examples of such monomers are styrene, alpha-methylstyrene, chloromethylstyrene and divinyl benzene. These monomers are well known in the art and further description is not considered necessary; however, the interested reader is referred to pages 1-246 of volume 16 of the "Encyclopedia of Polymer Science and Engineering" published by John Wiley & Sons (1989). Atactic polystyrene is the most commercially significant PS and is a preferred component (A). It is, however, also contemplated that the less prevalent syndiotactic and isotactic polystyrene homopolymers, as well as copolymers of styrene with such monomers as acrylates, acrylonitrile and butadiene, also derive significant benefit from modification by our invention. Thus, these copolymers are considered by the inventors herein to fall within our meaning of "a polystyrene polymer". Component (B) is a silicone crumb rubber which is prepared by recovering polydiorganosiloxane emulsion particles from water, such particles having an unsaturated monomer copolymerized therewith. This component is prepared by the following sequence. First, an aqueous silicone emulsion (I) of a silanol-terminated polydiorganosiloxane is prepared by methods well known in the art. In addition to polydiorganosiloxane and water, component (I) also contains at least one surfactant which stabilizes the dispersed polydiorganosiloxane and molecules and/or particles in the emulsion. To achieve the intended impact modification characteristics, the polydiorganosiloxane particles of this emulsion should have an average size of 0.1 to 10 micrometers, preferably from 0.5 to 1 micrometer and should be characterized by a weight average molecular weight (Mw) of greater than 50,000, preferably greater than 100,000. It is preferred that the above emulsion have a solids content ranging from 20 to 70 weight percent, most preferably 65%. These emulsions are well known in the art and may be prepared, for example, by methods wherein cyclic or linear diorganosiloxane species are dispersed in an aqueous continuous phase with the aid of surfactant and are thereafter emulsion polymerized by the introduction of an acid or base catalyst. These methods are illustrated by the disclosures of US-As 3,294,725 and 2,891,920, among others. In preferred embodiments of emulsion (I), the surfactant employed is an anionic type, such as sodium lauryl sulfate or ammonium lauryl sulfate. The catalyst is dodecyl-benenzene sulfonic acid, the latter also acting as a surfactant in the system. Our hydroxyl terminated polydiorganosiloxane emulsion can also be prepared by direct emulsification. In this process, a mixture of water, polydiorganosiloxane and one or more surfactants is processed under high shear conditions using either conventional mixing equipment or high shear devices such as a homogenizer. Methods for preparing these polymer emulsions are described in US-A 4,177,177. For the present invention, the organic groups of the polydiorganosiloxane of emulsion (I) are independently selected from hydrocarbon or halogenated hydrocarbon radicals such as alkyl and substituted alkyl radicals containing from 1 to 20 carbon atoms; cycloalkyl radicals, such as cyclohexyl; and aromatic hydrocarbon radicals, such as phenyl, benzyl and tolyl. Preferred organic groups are lower alkyl radicals containing from 1 to 4 carbon atoms, phenyl and halogen-substituted alkyl such as 3,3,3-trifluoropropyl. Thus, the polydiorganosiloxane can be a homopolymer, a copolymer or a terpolymer containing such organic groups. Examples include systems comprising dimethylsiloxy units and phenylmethylsiloxy units; dimethylsiloxy units and diphenylsiloxy units; and dimethylsiloxy units, diphenylsiloxy units, methyl 3,3,3-trifluoropropyl units and phenylmethylsiloxy units, among others. Most preferably, the polydiorganosiloxane is a polydimethylsiloxane which is terminated with a hydroxyl groups. In step (I), an organotin curing catalyst and a grafting silane are added to the aqueous emulsion. The grafting silane migrates into the particles of the polydiorganosiloxane emulsion and adds to the silanol functional polymer chain ends, via a condensation reaction which takes place in the presence of the tin catalyst. The grafting silane replaces the silanol groups on the ends of the polydiorganosiloxane molecules to produce a non-crosslinked telechelic polydiorganosiloxane. A telechelic molecule is a polydiorganosiloxane molecule with functional organic groups disposed at the chain ends. No crosslinking occurs during formation of the telechelic polydiorganosiloxane emulsion. This is in contrast to the grafting silanes of the prior art, in which the three hydrolyzable groups at the silicon atom of the grafting silanes condense with silanols of other polydiorganosiloxane molecules to produce a crosslinked polydiorganosiloxane or an emulsion of silicone rubber. The non-crosslinked telechelic polydiorganosiloxanes of this invention therefore have the physical characteristics of a gum upon removal of water from the emulsion. The organotin curing catalyst (II) is an organic salt of tin and is illustrated by tin (II) carboxylates, such as stannous oleate and stannous naphthanate; dialkyl tin (IV) carboxylates, such as dibutyltin diacetate and dibutyltin dilaurate; and tin (IV) stannoxanes, as exemplified by the structure (Bu) 2 SnCl-O-(Bu) 2 OH, in which Bu denotes a butyl radical, as taught in US-A 5,034,455. In preferred embodiments, the catalyst is stannous octoate. Preferably, the grafting silane is a silane having the general formula RQSi(X) 2 and partial hydrolysis condensation products thereof, wherein X is a hydrolyzable group selected from the group consisting of alkoxy radicals having 1 to 6 carbon atoms, chloro, hydrido, acetoxy, diorganoamino, oximato and amido groups and in which Q represents a monovalent radical which contains an unsaturated group. R is Q or a saturated monovalent hydrocarbon group of from one to six carbon atoms. In a more preferred embodiment, the grafting silane is R'Q'Si(OR') 2 in which R' is an alkyl radical having 1 to 4 carbon atoms and Q' is selected from the group consisting of an acryloxypropyl, methacryloxypropyl, vinyl, allyl, hexenyl, acrylamidopropyl, a group represented by the formula and a group of the formula HCl·ZN(H)-CH 2 CH 2 -N(H)-CH 2 CH 2 CH 2 -, wherein Z is Specific examples of suitable silanes include gamma-acryloxypropylmethyldimethoxysilane, gamma-methacryloxypropylmethyldiethoxysilane, vinylmethyldimethoxysilane, 5-hexenylmethyldimethoxysilane, allylmethyldimethoxysilane, acrylamidopropylmethyldimethoxysilane and silanes represented by the formulas HCl·ZHN-CH 2 CH 2 -NZ-CH 2 CH 2 CH 2 -SiCH 3 (OCH 3 ) 2 or HCl·ZN(H)-CH 2 CH 2 -N(H)-CH 2 CH 2 CH 2 -SiCH 3 (OCH 3 ) 2 , wherein Me hereinafter denotes a methyl radical and Z is a vinylbenzyl group having the formula Although order of addition in this second step is not considered critical, it is preferred to first add from 0.05 to 2 parts by weight, preferably from 0.3 to 0.6 parts, of the catalyst to 100 parts by weight of the hydroxyl-terminated polydiorganosiloxane in emulsion (I). From 0.1 to 10 parts by weight, preferably 1 part, of the grafting silane is then added to this mixture for each 100 parts by weight of the polydiorganosiloxane and the resultant emulsion is allowed to age to complete the endcapping reaction. When the grafting silane content is less than 0.1 part, incomplete endcapping occurs. If this component exceeds 10 parts, the byproducts formed when the hydrolyzable group X is reacted can destabilize the emulsion. During the aging process, which can take place at room temperature as well as at elevated temperatures, the pH of the emulsion should be maintained between 4 and 10.5. Usually two to four hours at room temperature is sufficient to complete the end-capping process. Further details regarding the above steps used to prepare the silicone gum of this invention may be found in US-As 4,618,642 and 4,954,565, which patents teach systems in combination with fillers for use as elastomeric coatings. The disclosures of these patents also teach suitable emulsions and their preparation for use in this invention. In a third step, at least one unsaturated monomer (II) is polymerized in the presence of the emulsion of non-crosslinked end-capped polydiorganosiloxane particles formed in the second step. The unsaturated groups of this monomer must be capable of reacting with the unsaturated groups of the silane (II). Further, the monomer (II) is selected such that, when it is homopolymerized using a conventional free-radical initiator, it results in a polymer having a glass transition temperature of at least 0°C. Preferably, component (II) is a styrenic monomer of the type described in connection with component (A). Examples of other suitable unsaturated monomers include acrylates, such as methyl acrylate, acrylonitrile and vinyl acetate. In a preferred procedure, a free-radical initiator is added to the emulsion resulting from the above described step and at least one unsaturated monomer, preferably a styrenic monomer, is gradually introduced. The preferred styrenic monomer is of the same type described above for use in the manufacture of component (A) and is compatible therewith. Most preferably, it is chemically identical to the monomer used to produce component (A). It is preferred that from 10 to 80 parts by weight, most preferably from 25 to 55 parts by weight, of the unsaturated monomer is added to the emulsion based on 100 parts by weight of the polydiorganosiloxane content thereof. Suitable initiators to be used in this third step are those which are known to polymerize the unsaturated monomer (II). These include azo compounds, such as azobisisobutyronitrile and 2-2'-azobis(2-methylbutyronitrile), organic peroxides, such as acetyl peroxide, cumene hydroperoxide and benzoyl peroxide and inorganic compounds such as potassium persulfate and ammonium peroxydisulfate, the azo compounds being preferred. The initiator is typically employed at a level of 0.05 to 0.2 parts by weight for each 100 parts by weight of the monomer (II) and is introduced as an organic solvent solution or, preferably, admixed with a portion of the monomer. In this polymerization step, the emulsion containing the initiator is preferably stirred at a temperature of 60 to 70°C. while the monomer is slowly added thereto. A typical addition period occurs in the range of 2 to 3 hours at the above noted temperatures, whereupon the resulting emulsion is heated for an additional 2 to 3 hours. The final step in the preparation of our composition involves the "recovery" of the above prepared particles from the emulsion. This is accomplished by first coagulating the particles by any of the standard methods for breaking emulsions, such as freezing, freeze drying, spray drying or the addition of a salt such as calcium chloride. A favored method is one wherein the emulsion is added, at room temperature, to a stirred excess of a water-soluble organic solvent such as acetone, ethylene glycol, ethanol or isopropyl alcohol, the later being preferred. The precipitated particles are then filtered and dried to form a crumb-like organic modified silicone rubber powder (B). A modified PS composition of the present invention may then be prepared by thoroughly dispersing the organic modified silicone rubber powder (B) in polystyrene polymer (A) at such a level to produce compositions containing an overall polydiorganosiloxane having 5 to 50 parts by weight polystyrene (A). This mixing is accomplished at elevated temperatures by any of the conventional methods used to disperse various components in thermoplastic resins. The temperature and other conditions to be used in such a mixing operation depend on the particular polymer selected and may be determined by routine experimentation by those skilled in the art. For example, the polystyrene polymer may be mixed according to this method at a temperature from 180°C. to 210°C. Alternatively, our organic modified silicone crumb rubber can be premixed with the polystyrene polymer, which is then fed to an extruder. Examples of suitable equipment for this purpose include such machines as twin screw extruders or single screw extruders. To obtain optimum impact resistance in our modified PS polymer, sufficient silicone crumb is used to result in a polydiorganosiloxane content of 10 to 25 parts by weight for each 100 parts by weight of the polystyrene. After components (B) and (A) are thoroughly mixed to provide a uniform blend, this composition can be further processed by conventional techniques, such as extrusion, vacuum forming, injection molding, blow molding or compression molding, to fabricate plastic parts which have significantly improved impact resistance over the unmodified polymer. It is also contemplated herein that the compositions of the invention may further contain fillers and other additives, including those normally employed in conventional styrenic polymers of the art. It is preferred that these systems contain a glass fiber filler which further improves the mechanical properties of fabricated products, particularly when a silane coupling agent is also used, as is well known in the art. Our compositions find utility in various industrial applications where improved toughness is desired in a PS polymer system. Examples include electrical and electronic insulation components, such as motor, coil and transformer insulation; housings for various electrical and electronic equipment, such as machines and hand tools; structural members, such as foam board insulators; furniture; automotive components, such as engine and interior structural components; aircraft interior components; and freezer-to-oven cookware. The following examples are presented to further illustrate the compositions of this invention. All parts and percentages in the examples are on a weight basis and all measurements were obtained at 25°C., unless indicated to the contrary. Example I A 3-methacryloxypropyl functional polydimethylsiloxane emulsion was prepared by adding 1.6 g of stannous octanoate to 500 g of an inionically stabilized aqueous emulsion of polydimethylsiloxane having a solids content of 70 per cent by weight. The emulsion particles were less than 800 nm in average diameter and the polymer had a Mw of greater than 200,000 with silanol functional chain ends. To this polydimethylsiloxane emulsion was mixed 3.3 g of 3-methacryloxypropylethyldimethoxy- silane which was added dropwise to the vortex of the vigorously stirred emulsion. Stirring was continued for 30 minutes after the addition of the silane, after which the reaction was allowed to continue for 24 hours. The emulsion was then adjusted to pH 10 using 14 wt% aqueous ammonium hydroxide. The above latex, 385 g, was then diluted to 30% solids by the addition of 440 ml of dionized H 2 O. The emulsion was stirred and heated to 70°C. in a nitrogen flushed 2 L reactor. A mixture of 50 ml of styrene, purified by passing over activated alumina gel and 0.25 g of VAZO™ 64, available from Dupont, Wilmington, Del. (azobisisobutyronitrile) were added dropwise to the reactor at a rate of 0.6 ml/min. After all the styrene was added to the reaction flask, the temperature was increased to 80°C. for two hours. The reaction was allowed to cool to room temperature overnight while stirring. The emulsion was then coagulated by stirring into 5 liters of isopropyl alcohol. The coagulated solids were separated from the alcohol by filtration and the resulting composition was dried in a vacuum oven at 50°C. for 24 hours. The above silicone rubber powder contained 84% by weight polydimethylsiloxane and was used to modify a general purpose polystyrene polymer (STYRON™ 685D available from Dow Chemical, Midland, Mi.). A Haake™ System 90 TW100 extruder (Haake/Fisons Instruments, Paramus, NJ) was used to form a composite containing various amounts of polydimethylsiloxane as shown in Table 1. The extruder conditions employed were: feed zone 1 temperature = 180°C.; mixing zone 2 temperature = 210°C.; mixing zone 3 and exit temperature = 210°C.; screw speed = 50 revolutions per minute (rpm); die = 3.18 mm (1/8 inch) diameter strand die. The extrudate from the above mixing operation was cooled, chopped into pellets, dried for 2.5 hours at 100°C. and fabricated into impact test bars measuring 12.7 x 12.7 x 3.18 mm (1/2 x 5 x 1/8 inch) using a Boy™ model 15S screw-type injection molding machine (Boy Machine Corp., Exton, PA). The molding parameters used were: mixing zone 1 temperature = 204.4°C. (400°F.); mixing zone 2 temperature = 240.6°C. (465°F.); Nozzle zone 3 dial setting = 52; Mold temperature = 43.3°C. (110°F); Injection pressure = 12.4 MPa (1,800 psi); Screw discharge set point = 3.0; Mold clamp pressure = 25.5 MPa (3,700 psi); Shot size dial = 36; Mold time = 30 seconds. The above described impact test bars were notched and tested for Izod impact strength according to ASTM D 256. The values for the different compositions are given in Table 1. Parts of PDMS in PS Notched Izod Impact (ft-lb/in) Strength (N.m/m) 0 0.23 12.28 12 1.30 69.39 15 2.05 109.43 17.5 2.37 126.51 Example II (comparative) A silicone rubber powder was produced according to Example I, wherein 428 parts of the anionically stabilized polydimethylsiloxane emulsion was crosslinked with 2 parts of stannous octoate and 4.8 parts of methacryloxypropyltrimethoxysilane. The resulting emulsion was aged 15 minutes at room temperature, diluted with 400 parts of water and aged overnight. Five hundred parts of water were then added and 0.1 part of AIBN in 3 cm 3 of styrene were mixed in at a temperature of 50°C. and under a nitrogen purge. Styrene monomer was then introduced over a four hour period as the temperature of the emulsion was maintained between 50 and 65°C. (total styrene added = 100 parts). After standing at room temperature for two days, silicone rubber powder was recovered by pouring the above emulsion into isopropyl alcohol, washing the coagulated solids and followed by drying in ambient air. The silicone rubber powder had a measured polydimethylsiloxane content of 74.3%. Various proportions of the above harvested powder were used to modify general purpose PS, as described in Example 1. Impact resistance of the molded and notched test bars derived therefrom is presented in Table 2, wherein the first column indicates the calculated parts by weight of polydimethylsiloxane present in the modified PS system per 100 parts by weight of polystyrene polymer. Parts Polydimethylsiloxane Per 100 Parts of Polystyrene Polymer Percent Polydimethylsiloxane in Modified Polystyrene Polymer Notched Izod Impact Strength (ft-lb/inch) (N.m/m) 0 (Control) 0 0.23 12.28 11 10 1.21 64.59 15 13 1.35 72.06 18 15 2.25 120.10 21 17 1.96 104.62 25 20 2.14 114.23 33 25 1.68 89.68 Comparison of the impact values in Table 2 to those in Table 1 shows that the compounds prepared in accordance with the present invention achieve comparable, if not superior impact properties over the crosslinked compounds of the prior art seen in Table 2. For example, 17.5 parts of the polydimethylsiloxane prepared in Example 1 showed an impact strength of 126.51 N.m/m (2.37 ft-lb/in), greater than the impact strength of the polydimethylsiloxane prepared in Example 2, where 18 parts of polydimethylsiloxane showed an impact strength of 120.10 N.m/m (2.25 ft-lb/in). The polyorganosiloxanes of the present invention therefore provide equivalent or improved impact properties over the prior art, while also offering the processing benefits of a silicone gum.

Claims: A silicone rubber powder composition prepared by the steps comprising: (I) reacting a preformed aqueous polydiorganosiloxane emulsion comprising water, a surfactant and a plurality of silanol-terminated polydiorganosiloxane molecules, with a grafting silane in the presence of an organotin catalyst to form a telechelic emulsion polymer, wherein said grafting silane has the formula RQSi(X) 2 where X is a hydrolyzable group, Q is an unsaturated organic functional group, R is Q or a saturated monovalent hydrocarbon group of from one to six carbon atoms, and (II) thereafter co-polymerizing an unsaturated monomer with said non-crosslinked telechelic emulsion polymer formed in step (I) to form particles therefrom; and (III) recovering the particles resulting from step (II). The composition according to claim 1 wherein said polydiorganosiloxane is a polydimethylsiloxane which is terminated with a silanol group at each end of its molecule and said unsaturated monomer is a styrenic monomer. The composition according to claim 2 wherein said silane is represented by the formula R'Q'Si(OR') 2 in which R' is an alkyl radical having 1 to 4 carbon atoms and Q' is selected from the group consisting of an acryloxypropyl, methacryloxypropyl, vinyl, allyl, hexenyl, acrylamidopropyl, a group represented by the formula and a group of the formula HCl·ZN(H)-CH 2 CH 2 -N(H)-CH 2 CH 2 CH 2 - wherein Z is The composition according to claim 3 wherein said curing catalyst is selected from the group consisting of a tin (II) carboxylate and a dialkyl tin (IV) carboxylate. The composition according to claim 1 wherein an initiator is added during said co-polymerization of step III. A method of modifying a polystyrene polymer, said method comprising blending 100 parts by weight of said polystyrene polymer with 5 to 50 parts by weight of the silicone rubber powder composition of claim 1. The method according to claim 6 wherein said component (A) is general purpose polystyrene. The method according to claim 7 wherein said component (A) is syndiotactic polystyrene.

Inventors: LEE KENNETH MICHAEL, LILES DONALD TAYLOR, MURRAY DAVID LOGAN, LEE, KENNETH MICHAEL, LILES, DONALD TAYLOR, MURRAY, DAVID LOGAN
Applicants: DOW CORNING, DOW CORNING CORPORATION
Application year: 1995
Main classification: C08G77
IPC codes: C08L25, C08F2, C08L51, C08F290, C08L55, C08G77, C08L83