Polyarylene thioether composition for molding

Abstract: A composition suitable for molding comprises (A) a resin comprising a polyarylene thioether which has a repeating unit as the main constituent and having a melt viscosity (at 310°C under a shear rate of 5/second) of from 1 Pas to 5 × 10³ Pas (10 to 5 × 10⁴ poise); (B) from 0.2 to 90 parts by weight, per 100 parts by weight of component (A), of a cross-linked polyarylene thioether having a melt viscosity (at 310°C under a shear rate of 5/second) of from 5 × 10⁴ to 1 × 10⁸ Pas (5 × 10⁵ to 1 ÿÏ 10⁹ poise) and capable of becoming gel under melting; and (C) from 0 to 400 parts by weight, per 100 parts by weight of components (A) and (B), of a fibrous filler and/or an inorganic filler.

Description: The present invention relates to a polyarylene thioether composition suitable for molding, to a process for the preparation of said composition and to a method of preparing a moulded article from said composition. Polyarylene thioether (hereinafter referred to as PATE) represented by for example, polyphenylene thioether is used in many fields as an engineering plastic having excellent for example, heat-resistance, non-inflammability and chemical resistance. PATE is usually a crystalline polymer and, making the most of this feature, it is used particularly in the field of for example, injection-molding. A conventional PATE as the base resin for a composition for molding is a cross-linked PATE which is prepared by curing a PATE of a relatively low molecular weight, i.e. raising its apparent melt viscosity by forming cross-linked and branch-chained PATE with thermal treatment. PATE prepared in this way has excellent melt molding processability, such as injection molding. A characteristic of such a PATE is that it usually has sufficient anti-flash property (difficulty in occurrence of flash) when it is injection molded. However, on the other hand, conventional PATE has many problems, so far. Namely, it has insufficient mechanical strength, is brittle and is severely colored by thermal treatment. Moreover, because of the severe time-dependent change of its viscosity (namely, the irreversible increase of its viscosity) during melt molding, it is difficult to select suitable molding conditions and to recycle molded scraps. Accordingly, it is not economical to use. On the other hand, the present inventors have developed a process for economically producing a substantially linear PATE of a high molecular weight by carrying out the addition of water and raising the temperature during polymerization (refer to US-A-4,645,826). Since the molecular weight of the substantially linear PATE obtained is sufficiently large, it can be applied to various melt-processings, such as injection molding, without being subjected to any further curing or cross-linking during its polymerization reaction. Such substantially linear and non cross-linked PATE has various characteristics as follows: (1) because of is molecular structure, it has a large mechanical strength; (2) as it is hardly colored in processing, it can easily be colored artificially; (3) as the time-dependent change of its melt viscosity during melt-molding is extremely small, it is easy to process; and (4) because of the ease of recycling of molded scraps, it is quite economical. However, the composition having this substantially linear PATE of high molecular weight as a base resin, does not have sufficient anti-flash properties on injection molding. On the other hand, even in compositions having the conventional cross-linked PATE (aforementioned), which is usually favourable with respect to its anti-flash property, as a base resin, there has been the problem that in injection molding of precision molded products, its anti-flash property is still insufficient. The present inventors have carried out extensive studies to improve the anti-flash property on injection molding the composition of non cross-linked PATE and also the anti-flash property on injection molding to prepare molded products from the conventional cross-linked PATE. At first, the present inventors tried to improve the anti-flash property of the composition for injection molding by increasing the viscosity of its base resin, PATE. However, it was found out that the viscosity of the composition increases in proportion to the viscosity increase of the base resin and its processability (fluidity, for example) for injection molding is damaged. Then, the present inventors studied tracing the method described in JP-A-59-223,753(1984); JP-A-52-149,348(1977); JP-A-55-127,002(1980); JP-A-59-11,357(1984); JP-A-53-66,565(1978) and JP-A-53-22,363(1978). Namely, the method comprises an addition of a PATE of a high viscosity, having a melt-flow value (measured by ASTM-D 1238: at 316°C (600 °F) under a load of 5 kg) of about 5 to 200 g/10 minutes, or a melt viscosity, η*, (at 310°C under a shear rate of 5/second) of around 1 x 10² to 1 x 10⁴ Pas (1 x 10³ to 1 x 10⁵ poise), to the base resin. However, it was realized that the method of adding a PATE of such viscosity could not achieve an effective improvement in the anti-flash property unless a large amount of such PATE of a high viscosity is added. Moreover, it was also found out that when a large amount of such PATE of high viscosity is added, the viscosity of the composition also increased and its processability for injection molding was remarkably damaged. The present inventors have further studied a method for effectively improving the anti-flash property of the composition without any substantial adverse influence on its processability for injection molding and the physical properties of the molded products. As a result, the present inventors have found that by carrying out a method which has never been considered so far, namely, a method of combining a highly cross-linked PATE (which becomes gel when melted) as an anti-flash property improving agent, with a base polymer, the anti-flash property of the composition is remarkably improved without giving any substantial adverse influence on the processability and also on the physical properties of the molded products. Further, side effects of the addition of this highly cross-linked PATE, for example, as a flow-orienting agent, accelerated crystallization of the composition during injection molding and, as a releasing agent, improved releasability of the molded products from molds, have also been found. Furthermore, when said cross-linked PATE is used in a large amount, it has also been found that not only the effects described above, but also an improvement of weld-property in injection molding is obtained. The present invention seeks to provide a composition of PATE suitable for molding, which is excellent with respect to anti-flash property, has high thermal stability and is easily melt-processed and the molded scraps of which can be recycled. Accordingly, the present invention provides a polyarylene thioether composition suitable for molding, which composition comprises: (A) a polyarylene thioether which has a repeating unit as the main constituent and having a melt viscosity (at 310°C under a shear rate of 5/second) of from 1 Pas to 5 x 10³ Pas (10 to 5 x 10⁴ poise); (B) from 0.2 to 90 parts by weight, per 100 parts by weight of component (A), of a cross-linked polyarylene thioether having a melt viscosity (at 310°C under a shear rate of 5/second) of from 5 to 10⁴ to 1 x 10⁸ Pas (5 x 10⁵ to 1 x 10⁹ poise) and being a gel under melting; and (C) from 0 to 400 parts by weight, per 100 parts by weight of components (A) and (B), of a fibrous filler and/or an inorganic filler. By a development of the present invention, a composition suitable for molding having improved anti-flash property compared to a component A only, has been realized while using a substantially linear, for example, non cross-linked PATE as a base polymer. Further, it becomes possible to obtain a composition of PATE for injection molding having an excellent anti-flash property and being sufficiently suitable for use in the field of precision molding even when a conventional cross-linked PATE is used as a base polymer, which is otherwise troublesome. The composition of the PATE for molding according to the present invention comprises the combination of component A as the base polymer and component B as the anti-flash property improving agent and optionally comprises further the combination of fibrous filler and/or inorganic filler. The words "comprises the combination of" means that other reasonable components other than mentioned above can be contained in the composition. The component A as the base polymer, which is the main element of the composition of the present invention, is PATE. PATE herein mentioned generally means a polymer having a repeating unit of -(- Ar - S -)-, as the main constituent (wherein Ar is an arylene group). In the present invention, a polymer having a paraphenylene group as the main constituent among the arylene groups constitutes the component A. For the polymer having paraphenylene group as the main constituent, from the standpoint of physical properties of the composition, such as heat-resistance, moldability and mechanical property, a polymer containing not less than 50 mol% of paraphenylene group, preferably not less than 60 mol%, more preferably not less than 70 mol%, is desirable. As to the arylene group, (-Ar-), other than a paraphenylene group, a metaphenylene group, orthophenylene group, substituted phenylene group, wherein R is an alkyl group (preferably an alkyl group of C₁ to C₆) or a phenyl group and n is an integer of 1 to 4; p,p'-diphenylene sulfon group, p,p'-diphenylene group p,p'-diphenylene ether group, p,p'diphenylene-carbonyl group or a naphthalene group. can be used. From the viewpoint of processability a copolymer containing different kinds of repeating unit is preferable to a homopolymer consisting only of the repeating unit A copolymer of and repeating units is preferred. Particularly, those copolymers containing the respective repeating units in a block form are preferred to those containing them in a random form (for example, as described in EP-A-166451), because the block-copolymer is remarkably excellent in physical properties for example resistance and mechanical property although the block- and random- copolymers are substantially equal in their processabilities. 5 to 50 mol% of repeating unit in the block copolymer is preferable and 10 to 25 mol% is particularly preferable. As for the PATE for component A in the present invention, those having a substantially linear structure are preferred in respect of processability and physical property. A PATE which is non-crosslinked and substantially linear is particularly preferred as component A. The words "PATEs (those) having a substantially linear structure" does not mean the polymers obtained by curing such as oxidation cross-linking or thermal cross-linking but means the polymers obtained by condensation polymerization of a monomer substantially having a bifunctional monomer as the main body. However, within a range of not substantially impairing the physical properties of molded products, for instance, a cross-linked polymer obtained by using an effective amount of a cross-linking agent (for instance, trihalobenzene) during polymerization or a thermally cross-linked polymer obtained by a high temperature curing in the presence of oxygen, may also be used according to the present invention. The component A as a base polymer for the composition of the present invention is desirably a polymer having a melt viscosity, η*, (at 310°C under a shear rate of 5/second) in the range of 1 to 5 x 10³ Pas (10 to 5 x 10⁴ poise), preferably 5 to 5 x 10³ Pas (50 to 5 x 10⁴ poise) and more preferably 10 to 5 x 10³ Pas (100 to 5 x 10⁴ poise). When the melt viscosity, η*, is below 1 Pas (10 poise), it is difficult to melt-process the composition because its fluidity is too high, and even if a molded product can be obtained, its mechanical strength for example, is poor and it is not suitable. On the other hand, when the melt viscosity, η*, is over 5 x 10³ Pas (5 x 10⁴ poise), its fluidity is poor and accordingly the melt-processing of a composition made of the component A is difficult. PATE which meets the above conditions of the resin according to the present invention can be manufactured economically by the method describe in US-A-4,645,826 filed by the present inventors. In addition, a method described in US-A-3,919,177 in which a polymerization aid such as a carboxylic acid salt is added in a large amount to obtain a high molecular weight PATE can also be used. Further, as other materials for compounding, other synthetic resins, various elastomers and various additives for processing, may for example, be combined with component A. The component B as anti-flash property improving agent (which is one of the essential combining elements in the composition according to the present invention) is a PATE having a similar chemical structure to that of component A. Namely, the PATE has the repeating unit -(- Ar - S -)- , (same definition of Ar as described before). However, the repeating unit is not essential as the main constituent although is preferable. The specifically different point of component B from component A is that component B is a cross-linked PATE, which becomes gel under melting, having a melt viscosity, η*, (at 310°C under a shear rate of 5/second) of 5 x 10⁴ to 1 x 10⁸ Pas (5 x 10⁵ to 1 x 10⁹ poise), preferably 1 x 10⁵ to 1 x 10⁸ Pas (1 x 10⁶ to 1 x 10⁹ poise). A melt-flow value (measured by ASTM D-1238, at 316°C (600°F) under a load of 5 kg) of the cross-linked PATE of such high viscosity is less than 1 and is difficult to measure exactly. When η* is below 5 x 10⁴ (5 x 10⁵ poise), because the improvement of anti-flash property is insufficient even when a large amount of such component B is combined with component A, it is not preferable. On the other hand, when η* is over 1 x 10⁸ Pas (1 x 10⁹ poise), component B cannot easily disperse in the molten base polymer as fine particle gels during melt molding and accordingly, the improvement of anti-flash property becomes insufficient and makes the case not preferable. A non cross-linked PATE or lowly cross-linked PATE as an anti-flash improving agent, component B, which does not become a gel under melting, dissolves compatibly into component A even if the PATEs have a high viscosity, and is likely to increase melt viscosity of the composition with less effect on anti-flash property and consequently they are not preferable. As a method for obtaining a cross-linked PATE which becomes a gel under melting, a method for forming a cross-linked structure by using a cross-linking agent during polymerization, for example a method of mixing about 0.05 mol to about 20 mol of a polyhaloarmatic compound substituted with not less than three halogen atoms with 100 mol of a dihaloaramtic compound, further adding appropriate amounts of water and/or an alkali metal carboxylic acid and polymerizing the mixture in the presence of sodium disulfide and a polar organic solvent at 180 to 290°C for an appropriate period of time to obtain a polymer having the necessary properties such as melt viscosity and gel forming; and a method of cross-linking PATE by high temperature curing in the presence of oxygen, for example a method of heating PATE in the presence of oxygen at a temperature of not lower than 200°C but lower than its melting point for an appropriate period of time to obtain the polymer having the necessary properties such as melt viscosity and gel forming, can be used. Particularly, the PATE cross-linked during polymerization obtained by the former method is excellent in color tone and thermal stability as compared with the thermally cross-linked PATE obtained by the latter method, and accordingly, the former method is preferred. The amount of combining component B in the composition suitable for molding of the present invention is in the range of 0.2 to 90 parts by weight, preferably in the range of 0.5 to 80 parts by weight, more preferably in the range of 0.5 to 70 parts by weight, particularly preferable in the range of 0.5 to 60 parts by weight per 100 parts by weight of component A. When the amount of component B is below 0.2 parts by weight, the effect of improving the anti-flash property is likely to be insufficient and on the other hand, when an amount of component B is over 90 parts by weight the fluidity of the composition is greatly lowered and the mechanical property of the molded product is likely to be also lowered. Accordingly, both cases are not preferable. In the composition of the present invention, there is optionally a fibrous filler and/or inorganic filler (component C). Although component C is not essential in view of improving the anti-flash property of the composition, these fillers may combine with component A to improve the physical properties of the molded product, such as the mechanical properties, heat-resistance, electrical properties, chemical-resistance, and sometimes to reduce the cost of the molded product by using the filler as an extending agent. The amount of combination of the filler is 0 to 400 parts by weight per 100 parts by weight of the mixture of components A and B, and to exhibit the effects of the filler, the combination of not less than 0.01 part and not more than 400 parts by weight is preferable, 5 to 300 parts by weight is more preferable and 10 to 250 parts by weight is still more preferable. When the amount of combination of fillers is over 400 parts by weight, the processability of the composition is remarkably damaged and is not preferable. As a fibrous filler, filaments of glass, carbonaceous material, silicon carbide, silica, alumina, zirconia, aramide and whiskers of potassium titanate, wollastonite, calcium sulfate, carbon and boron can for example be mentioned. As an inorganic filler, powders of talc, mica, kaolin, clay, glass, magnesium carbonate, magnesium phosphate, calcium carbonate, calcium silicate, calcium sulfate, calcium phosphate, silicon oxide, aluminum oxide, titanium oxide, iron oxide (including ferrite), copper oxide, zirconia, zinc oxide, silicon carbide, carbon, graphite, boron nitride, molybdenum disulfide and silicon may, for example be mentioned. Other than the above combining elements, other synthetic resins, various elastomers, various additives for processing, etc. can be combined with the composition. As another synthetic resin, polyolefin, polyester (including aromatic polyester), polyamide (including aromatic polyamide), polyamideimide, polyimide, polyether imide, polyether sulfone, polyether ketone, polyether ether ketone, polysulfone, polycarbonate, polyacetal, polyarylene, fluorocarbon resin, epoxy resin, silicone resin, phenol resin, poly(methyl methacrylate), polystyrene and ABS can, for example, be mentioned. As a processing agent, antioxidant, stabilizer, anti-corrosive agent, lubricant, releasing agent, coupling agent, coloring agent, anti-inflammatory agent, bubbling agent and anti-static agent can, for example be mentioned. The composition of PATE suitable for molding of the present invention includes the composition prepared by mixing each of the combining elements and additives as solid powder and also the composition, which is in coherent state, prepared by mixing said elements and additives under molten state. The latter composition is a representative one and is usually manufactured in the form of pellets. The former composition can be manufactured by uniformly mixing each of the combining elements and additives with blenders, mixers or mills. The latter composition is manufactured by molding the former composition into pellets, through melt-kneading with an extruder, etc. The uses of the composition for molding according to the present invention are not necessarily limited to injection-molded products, however, the characteristic points of the composition can be displayed most effectively in injection-molded products. Accordingly, the present invention also provides a method of preparing a molded article, which method comprises injection molding an article using a composition according to the present invention. Of course, it is needless to say that the anti-flash property of the composition is quite excellent in injection molding. Furthermore, there are other features for example, its high crystallisation rate, excellent releasability, excellent heat stability during melt-molding, excellent mechanical properties especially weld-property in injection molding, color and dimensional stability molded products of it and ease of recycling of its molded scraps which makes its molding procedure economical. Taking advantage of these features, the composition can be applied for many fields such as electrics, electronics, precision machineries, cars and aeroplanes. Particularly, it is excellently suitable for precision machineries field. The following Experiments, Examples and Comparative Examples illustrate the present invention. EXPERIMENT 1 FOR PRODUCING POLYMER A-1: Into a titanium-lined autoclave, 1200 kg of N-methylpyrrolidone (NMP) and 420 kg of hydrated sodium sulfide (purity 46.4%) were introduced and by heating the content to about 202°C, 190 kg of water were distilled out. Then, 366 kg of p-dichlorobenzene were introduced and after 5 hours of polymerization at 218°C, 90 kg of water were additionally introduced and the polymerization was performed for 1.5 hours at 260°C and further for 4 hours at 242°C. A slurry containing the formed polymer was obtained. The slurry was sieved through a 0.1 mm mesh screen and only granular polymer was separated, washed with acetone and then with water to obtain a cleaned polymer. The cleaned polymer was immersed into an aqueous 2% solution of NH₄CL at 40°C for 30 minutes and then the treated polymer was washed with water and dried at 80°C for 12 hours under reduced pressure to obtain polymer A-1. The melt viscosity, η*, of the obtained, non cross-linked polymer A-1 was 1 x 10³ Pas (1 x 10⁴ poise) (hereinafter, η* is measured at 310°C under a shearing rate of 5/second). EXPERIMENT 2 FOR PRODUCING POLYMER A-2: Into an autoclave made of SUS 316 stainless steel, 15 kg of NMP and 4.2 kg of hydrated sodium sulfide (purity: 46.4%) were introduced, and by heating the content to about 202°C, 1.6 kg of water were distilled out. Then, 3.65 kg of p-dichlorobenzene were introduced and the polymerization was performed for 2 hours at 240°C. By heating the slurry containing the formed polymer under a reduced pressure, NMP was distilled out. The solid containing the polymer was washed with water to remove salts and washed with acetone and further with water. The washed polymer was dried for 12 hours at 80°C under a reduced pressure. The melt viscosity, η*, of the obtained polymer was 10 Pas (100 poise). The obtained polymer was treated with high temperature curing at 270°C for 6 hours in an oven of air-circulation type to obtain polymer A-2 (powder). The melt viscosity, η*, was 1 x 10³ Pas (1 x 10⁴ poise). EXPERIMENT 3 FOR PRODUCING POLYMER A-3: Into a titanium-lined autoclave, 930 kg of NMP and 423 kg of hydrated sodium sulfide, Na₂S.5H₂O (purity: 46.07%) were introduced and by heating the content gradually to 203°C, 171 kg of water were distilled out. 5kg of water and 44 kg of NMP were additionally introduced and then 365 kg of p-dichlorobenzene were introduced into the autoclave and after 5 hours of polymerization at 220°C, 135 kg of water was charged and the polymerization was performed at 255°C for 4.5 hours. After cooling the polymerization mixture, a slurry obtained was sieved through a 0.1 mm mesh screen and only a granular polymer was separated, washed with acetone and then with water and a cleaned linear polymer was obtained. The cleaned polymer was immersed into an aqueous 2% solution of NH₄Cl at 40°C for 30 minutes under stirring and the treated polymer was washed with water and dried and obtained polymer A-3. The melt viscosity, η*, of polymer A-3, which is linear, was 88 Pas (880 poise). EXPERIMENT 4 FOR PRODUCING POLYMER B-1: Into an autoclave, 2.0 kg of NMP and 420 g of hydrated sodium sulfide (purity: 46.4%) were introduced and the content was heated to about 200°C to distill 90 g of water out. Then, 355 g of p-dichlorobenzene and 11 g of 1,2,4,5-tetrachlorobenzene were introduced into the autoclave and the polymerization was performed for 8 hours at 215°C. Then, 30 g of water were added, the temperature was raised to 250°C in about 30 minutes, and was further polymerized for 0.3 hours at 250°C. The content was once cooled to 210°C in 15 minutes and then heated again to 245°C in 30 minutes. (When the polymerization mixture cooled to 210°C was further cooled to below 60°C and obtained a polymer, the melt viscosity, η*, of the polymer was less than 1 Pas (10 poise) and the polymer was in a state of fine powder). After maintaining the content at 245°C for 12 hours, the content was treated in the same manner as in Example 1 to obtain polymer B-1 which became gel under melting. The melt viscosity, η*, of polymer B-1, cross-linked during polymerization, was 1 x 10⁶ Pas (1 x 10⁷ poise). EXPERIMENT 5 FOR PRODUCING POLYMER B-2: In the same manner as in Experiment 4 for producing the polymer except for using 1,2,4,5-tetrachlorobenzene of 5.5 g, a polymer B-2, being gel under melting was obtained. The melt viscosity, η*, of polymer B-2, cross-linked during polymerization, as 3 x 10⁵ Pas (3 x 10⁶ poise). EXPERIMENT 6 FOR PRODUCING POLYMER B-3: In the same manner as in Experiment 4 for producing the polymer except for using 1,2,4,5-tetrachlorobenzene of 0.55 g, a polymerization was carried out to obtain a polymer B-3. The melt viscosity η*, of polymer B-3, cross-linked during polymerization, was 5 x 10³ Pas (5 x 10⁴ poise). EXPERIMENT 7 FOR PRODUCING POLYMERS B-4 TO B-6: Parts of the polymer A-1 obtained in Experiment 1 was treated for 16 hours at 280°C (for polymer B4), for 6 hours at 280°C (for polymer B5) and for 5 hours at 270°C (for polymer B6) in an oven of air-circurating type to obtain polymers B-4, B-5 and B-6, each being gel under melting except B-6. The melt viscosity, η*, of each of polymers B-4, B-5 and B-6, cross-linked by thermal treatment, was as follows: Polymer B-4; 5 x 10⁵ Pas (5 x 10⁶ poise) Polymer B-5; 1 x 10⁵ Pas (1 x 10⁶ poise) Polymer B-6; 5 x 10³ Pas (5 x 10⁴ poise) EXAMPLES 1 TO 11 AND COMPARATIVE EXAMPLES 1 TO 7 OF PREPARATION OF THE COMPOSITION: Polymers A-1 to A-3 were used as the base polymers which are non cross-linked, linear polymers. Polymer A-2 was used as a model of a thermally cross-linked base polymer of a conventional composition for injection molding. Each of polymers B-1 to B-6 (except B-3 and B-6), which becomes gel under melting, was used as an anti-flash property improving agent for the composition. As a preliminary blending, predetermined parts by weight of each polymer B, which is an anti-flash property improving agent, and glass fibers (13 µm in diameter and 3 mm in length, made by NIHON DENKI GLASS Co.., Ltd.) were blended with 100 parts by weight of the basic polymer (polymer A). The blending was performed, first, by blending polymer A and anti-flash property improving agent (polymer B) with Henchel mixer and then further by blending glass fiber and the mixture (polymer A plus polymer B) with tanbler mixer and a powdery composition was prepared. The powdery composition was melt blended with a twin screw kneading extruder (with a cylinder of 30 mm in diameter, made by PLASTIC KOGAKU KENKYUSHO, MODEL # BT-30) and extruded in a form of strand, rapidly cooled and cut into pellets. PHYSICAL PROPERTIES AND THEIR MEASURING METHODS : (1) Melt Viscosity. Melt viscosity, η*, was measured with KOKA type flow tester, at 310°C under a shear rate of 5/second. (2) Anti-flash Property. A mold for the test of the anti-flash property (provided with a gap of 30 µm for flash forming) was installed to an injection molding machine (made by TOSHIBA KIKAI Co., Ltd., Model: #IS-25EV), and the injection molding was performed on each of the pellet samples under the following conditions: (1) resin temperature of 350 to 360°C; (2) mold temperature of 145°C; and (3) holding pressures of 1,400 kg/cm² for the tests in Table 1 and 1,000 kg/cm² for the tests in Table 2. The length of flash generated through the gaps, was measured and the shorter is the length of the flash, the more excellent is the anti-flash property of the composition. And the sample being extremely poor in anti-flash property was evaluated as 1, the sample being extremely excellent was evaluated as 5 and the sample of conventional composition was evaluated as 3. The results are shown in Tables 1 and 2 collectively. Further, the mold used for the tests has a cavity of a size of 2 mm x 40 mm x 40 mm,and a gate of 2 mm in width was installed at the center of one of the sides of the thus formed square (a size of 40 mm x 40 mm). On the side of the square, opposing the gate, four gaps of 4 mm in width and 6 mm in length (in the direction of injection), with a clearance of 30 µm as mentioned before, have been installed as the two sets with the mutual distance of 2 mm between the two gaps of one set and with the distance of 10 mm between the two sets having the axis of injection as a center of the two sets. (3) Mechanical Properties. An injection molding machine was equipped with the mold for the test and each sample was injection-molded under the following conditions: (1) resin temperature of 350 to 360°C; (2) mold temperature of 145°C; and (3) holding pressure of 1,000 kg/cm². Mechanical properties of the samples were measured in conformity to the ASTM standard and the results are shown in Table 2. A weld tensile strength was measured as follows: The mold for the test has two gates at each edge of the cavity for a sample of tensile strength and test samples for weld properties, which have a welded part at around the center of the dumbbell specimen, were prepared by introducing a resin to be tested from both gates simultaneously. To prepare a dumbbell specimen for measuring conventional tensile properties (without welding part), a resin to be tested was injection molded with one gate closed. Tensile strength and tensile elongation were measured with each dumbbell specimen prepared as above. (4) Crystallinity Index: The index, Ci, was measured, using the same samples prepared by the above test (anti-flash property test), as follows: (I) separate a crystalline scattering strength Ac and an amorphous scattering strength Aa from a wide angle X-ray diffraction pattern of each sample 2ϑ = 17 to 23°; and (2) calculate Ci with the following formula: Ci (%) = [Ac/(Ac + Aa)] x 100 For the detail of the method, refer to "Journal of Applied Polymer Science, Vol. 20 p 2541 (1976). From the Table 2, it can be easily understood that the composition of the present invention has not only the effect of suppressing a forming of flash but also an effect of accelerating crystallization of the composition during melt molding. Furthermore, surprisingly enough, its weld properties are also improved.

Claims: A polyarylene thioether composition suitable for molding, which composition comprises: (A) a polyarylene thioether which has a repeating unit as the main constituent and having a melt viscosity (at 310°C under a shear rate of 5/second) of from 1 Pas to 5 x 10³ Pas (10 to 5 x 10⁴ poise); (B) from 0.2 to 90 parts by weight, per 100 parts by weight of component (A), of a cross-linked polyarylene thioether having a melt viscosity (at 310°C under a shear rate of 5/second) of from 5 to 10⁴ to 1 x 10⁸ Pas (5 x 10⁵ to 1 x 10⁹ poise) and being a gel under melting; and (C) from 0 to 400 parts by weight, per 100 parts by weight of components (A) and (B), of a fibrous filler and/or an inorganic filler. A composition according to claim 1, wherein the said component (A) is a non-cross-linked and substantially linear polyarylene thioether. A composition according to claim 1 or 2, wherein the said component (A) is a copolymer composed of the repeating units and A composition according to any one of the preceding claims, wherein the said component (B) is a cross-linked polyarylene thioether having a melt viscosity of from 1 x 10⁵ to 1 x 10⁸ Pas (1 x 10⁶ to 1 x 10⁹ poise). A composition according to any one of the preceding claims, comprising from 0.5 to 60 parts by weight of component (B) per 100 parts by weight of component (A). A composition according to any one of the preceding claims, which contains not less than 0.01 part by weight of the said component (C) per 100 parts by weight of components (A) and (B). A composition according to any one of the preceding claims, which contains from 10 to 250 parts by weight of the said component (C) per 100 parts by weight of components (A) and (B). A process for the preparation of a composition as defined in any one of claims 1 to 7, which process comprises mixing said components (A), (B) and optionally (C). A method of preparing a molded article, which method comprises injection molding an article using a composition as claimed in any one of claims 1 to 7.

Inventors: FUKUDA MAKOTO, HOSOKAWA TOSHIO, IIZUKA YO, KAWAKAMI YUKICHIKA, SHIIKI ZENYA, SUZUKI SIROU, FUKUDA, MAKOTO, HOSOKAWA, TOSHIO, IIZUKA, YO, KAWAKAMI, YUKICHIKA, SHIIKI, ZENYA, SUZUKI, SIROU
Applicants: KUREHA CHEMICAL IND CO LTD, KUREHA KAGAKU KOGYO KABUSHIKI KAISHA
Application year: 1988
Main classification: C08L81
IPC codes: C08L81