WO2014156946A1 - ポリアリーレンスルフィド樹脂の製造方法およびポリアリーレンスルフィド樹脂組成物 - Google Patents
ポリアリーレンスルフィド樹脂の製造方法およびポリアリーレンスルフィド樹脂組成物 Download PDFInfo
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G75/00—Macromolecular compounds obtained by reactions forming a linkage containing sulfur with or without nitrogen, oxygen, or carbon in the main chain of the macromolecule
- C08G75/14—Polysulfides
- C08G75/16—Polysulfides by polycondensation of organic compounds with inorganic polysulfides
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G75/00—Macromolecular compounds obtained by reactions forming a linkage containing sulfur with or without nitrogen, oxygen, or carbon in the main chain of the macromolecule
- C08G75/02—Polythioethers
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G75/00—Macromolecular compounds obtained by reactions forming a linkage containing sulfur with or without nitrogen, oxygen, or carbon in the main chain of the macromolecule
- C08G75/02—Polythioethers
- C08G75/0204—Polyarylenethioethers
- C08G75/0209—Polyarylenethioethers derived from monomers containing one aromatic ring
- C08G75/0213—Polyarylenethioethers derived from monomers containing one aromatic ring containing elements other than carbon, hydrogen or sulfur
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G75/00—Macromolecular compounds obtained by reactions forming a linkage containing sulfur with or without nitrogen, oxygen, or carbon in the main chain of the macromolecule
- C08G75/02—Polythioethers
- C08G75/0204—Polyarylenethioethers
- C08G75/025—Preparatory processes
- C08G75/0263—Preparatory processes using elemental sulfur
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G75/00—Macromolecular compounds obtained by reactions forming a linkage containing sulfur with or without nitrogen, oxygen, or carbon in the main chain of the macromolecule
- C08G75/14—Polysulfides
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L81/00—Compositions of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing sulfur with or without nitrogen, oxygen or carbon only; Compositions of polysulfones; Compositions of derivatives of such polymers
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L81/00—Compositions of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing sulfur with or without nitrogen, oxygen or carbon only; Compositions of polysulfones; Compositions of derivatives of such polymers
- C08L81/02—Polythioethers; Polythioether-ethers
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L81/00—Compositions of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing sulfur with or without nitrogen, oxygen or carbon only; Compositions of polysulfones; Compositions of derivatives of such polymers
- C08L81/04—Polysulfides
Definitions
- the present invention relates to a method for producing a polyarylene sulfide resin having excellent reactivity and a polyarylene sulfide resin composition produced by the production method.
- Polyarylene sulfide resins represented by polyphenylene sulfide resins (hereinafter sometimes abbreviated as PPS) (hereinafter also abbreviated as PAS) are halogen-free materials because sufficient flame retardancy can be obtained without a halogen-based flame retardant. Has attracted attention as.
- This polyarylene sulfide resin can be generally produced by polymerization reaction in an organic polar solvent using p-dichlorobenzene and sodium sulfide or sodium hydrosulfide and sodium hydroxide as raw materials (Patent Documents 1 and 2). reference).
- Patent Documents 1 and 2 Japanese Patent Documents 1 and 2.
- the purification process for removing by-products such as the organic polar solvent and sodium chloride used in the production process is indispensable, but also the purification process. Even later, chlorine atoms remain in the resin.
- Patent Documents 3 and 4 a method for producing a polyarylene sulfide resin that is melt-polymerized using a diiodo aromatic compound and elemental sulfur without using a chlorine atom and a polar solvent is known (see Patent Documents 3 and 4).
- a polyarylene sulfide resin containing iodine atoms can be obtained, iodine atoms can be sublimated and removed by heating the polymerization reaction product or the reaction soul after the polymerization reaction under reduced pressure. It is possible to keep the iodine concentration in the low.
- the problem to be solved by the present invention is that it does not contain a chlorine atom and is excellent in reactivity with other compounds and resins such as an impact modifier such as an epoxysilane coupling agent and a functional group-containing thermoplastic elastomer.
- An object of the present invention is to provide a polyarylene sulfide resin composition and a method for producing the resin.
- a polymerization inhibitor having a specific functional group is used in a method for producing a polyarylene sulfide resin by melt polymerization of a mixture containing a diiodo compound, solid sulfur, and a sulfur-containing polymerization inhibitor. It has been found that the above-mentioned problems can be solved by using it, and the present invention has been completed.
- the present invention relates to a diiodo aromatic compound, elemental sulfur, the following general formula (1)
- the present invention relates to a method for producing an arylene sulfide resin.
- the present invention has the following general formula (1) at the end.
- the present invention relates to a polyarylene sulfide resin composition.
- a polyarylene sulfide resin composition that does not contain a chlorine atom and has excellent reactivity with other compounds and resins such as an impact modifier such as an epoxy silane coupling agent and a functional group-containing thermoplastic elastomer, and A method for producing the resin can be provided.
- diiodo aromatic compound used in the present invention examples include diiodobenzene, diiodotoluene, diiodoxylene, diiodonaphthalene, diiodobiphenyl, diiodobenzophenone, diiododiphenyl ether, and diiododiphenylsulfone.
- the invention is not limited to these.
- the substitution positions of the two iodine atoms are not particularly limited, but preferably the two substitution positions are as far as possible in the molecule.
- the para position and the 4,4'-position are more preferable.
- a phenyl group, halogen, hydroxy group, nitro group, amino group, C1-6 alkoxy group, carboxy group, carboxylate, arylsulfone and arylketone are substituted on the aromatic ring.
- the elemental sulfur used in the present invention means a substance composed of only sulfur atoms (S 8 , S 6 , S 4 , S 2 etc.), and its form is not limited.
- elemental sulfur is also commercially available as a station method medicament, in the present invention, as long as it can be obtained generically, a mixture of such S 8 and S 6
- the purity is not particularly limited.
- it may be in the form of particles or powder, and the particle diameter is not limited, but the particle diameter is 0.001 to 10 mm, further 0.01 to 5 mm, particularly 0 .01 to 3 mm is preferable.
- X is a hydrogen atom or an alkali metal atom
- a polymerization inhibitor having a group represented by the following formula hereinafter, may be simply abbreviated as a polymerization inhibitor
- Any compound that has a group represented by (1) and inhibits or stops the polymerization reaction in the polymerization reaction of the polyarylene sulfide resin can be used without particular limitation.
- X is a hydrogen atom or an alkali metal atom, and among these, a hydrogen atom is preferable from the viewpoint of good reactivity.
- alkali metal atom include sodium, lithium, potassium, rubidium, cesium and the like, and sodium is preferable.
- R ⁇ 1 >, R ⁇ 2 > may be same or different, respectively, a hydrogen atom, following General formula (a)
- R 1 and R 2 is any one of the monovalent groups represented by the general formulas (a) to (c). Or a compound represented by the following general formula (3)
- Z represents an iodine atom or a mercapto group
- R 3 represents any one of the monovalent groups represented by the general formulas (a) to (c)).
- R 4 represents any one of the monovalent groups represented by the general formulas (a) to (c)).
- the compound represented by the general formula (2) or (3) is preferable from the viewpoint of reactivity, and in the general formula (2) or (3), X is a hydrogen atom. Those are particularly preferred.
- the polyarylene sulfide resin of the present invention is melt polymerized by heating a diiodo aromatic compound as a raw material, elemental sulfur, the polymerization inhibitor, and, if necessary, a catalyst in the presence of a non-oxidizing gas. Can be obtained.
- the blending ratio at that time is in the range of 0.5 to 2 moles, preferably in the range of 0.8 to 1.2 moles of the diiodo aromatic compound per mole of elemental sulfur.
- the polymerization inhibitor is in the range of 0.0001 to 0.1 mol, preferably in the range of 0.0005 to 0.05, with respect to 1 mol of solid sulfur.
- the melt polymerization conditions are not particularly limited, but the temperature ranges from 175 ° C. or higher to the melting point of the PAS resin plus 100 ° C., preferably 180 to 350 ° C., and the absolute pressure is 1 [cPa] to It is desirable to carry out in the range of 100 [kPa], preferably in the range of 13 [cPa] to 60 [kPa].
- the melt polymerization conditions need not be constant.
- the initial conditions are a temperature range of 175 to 270 ° C., preferably a range of 180 to 250 ° C., and an absolute pressure of 6.7 to 100 kPa.
- the final condition is a melting point of the PAS resin obtained from a temperature of 270 ° C.
- fusing point refers to what was measured based on JIS * K-7121 using the differential scanning calorimeter (DSC apparatus by Perkin-Elmer, Pyris * Diamond).
- the melt polymerization reaction is performed by heating a diiodo aromatic compound, elemental sulfur, a polymerization inhibitor and, if necessary, a catalyst in the presence of a non-oxidizing gas.
- the polymerization inhibitor may be added basically at any point, but preferably the diiodo aromatic compound, elemental sulfur, and if necessary, the catalyst is heated in the presence of a non-oxidizing gas.
- the condition of the non-oxidizing gas is that the oxygen concentration in the gas phase is 5% by volume or less, preferably 2% by volume or less, more preferably an atmosphere substantially free of oxygen, that is, inert such as nitrogen, helium, argon, etc. Indicates a gas atmosphere.
- the melt polymerization can be performed using a known resin melt kneader provided with a heating device, a decompression device, and a stirring device, for example, a Banbury mixer, a kneader, a continuous kneader, a single screw extruder, A twin screw extruder etc. are mentioned.
- the melt polymerization is performed in a non-oxidizing atmosphere from the viewpoint of preventing the oxidative crosslinking reaction and obtaining a high degree of polymerization.
- the non-oxidizing atmosphere means an atmosphere having a gas phase oxygen concentration of less than 5% by volume, preferably less than 2% by volume, more preferably substantially free of oxygen, that is, nitrogen, helium, argon, etc. Indicates an inert gas atmosphere.
- the melt polymerization is preferably performed under a condition that substantially does not contain a solvent.
- the condition that substantially does not contain a solvent is that the solvent is 10 parts by mass or less with respect to a total of 100 parts by mass of a diiodo aromatic compound, elemental sulfur, a polymerization inhibitor, and if necessary, a catalyst, Preferably, it means 5 parts by mass or less, more preferably 1 part by mass or less, 0 parts by mass or more, preferably 0.01 parts by mass or more, and more preferably 0.1 parts by mass or more.
- a polymerization rate can be adjusted by adding a nitro compound as a catalyst.
- a nitro compound various nitrobenzene derivatives can be usually used. More specifically, 1,3-diiodo-4-nitrobenzene, 1-iodo-4-nitrobenzene, 2,6-diiodo-4 -Nitrophenol, 2,6-diiodo-4-nitroamine and the like.
- the catalyst is usually added in an amount added as a catalyst, and is, for example, in the range of 0.01 to 20 parts by mass with respect to 100 parts by mass of elemental sulfur.
- the polyarylene sulfide resin having a terminal represented by the general formula (1) is produced by the following reaction.
- reaction formula (1) when diphenyl disulfide having a group represented by the general formula (1) is used, the —SS— bond in the polymerization inhibitor undergoes radical cleavage at the melting temperature (reaction formula (1 )), The generated sulfur radical attacks the adjacent carbon atom of the terminal iodine atom during polymerization, and the iodine atom is eliminated, so that the polyarylene sulfide resin having the group represented by the general formula (1) at the terminal (Wherein reaction formula (2)).
- a polyarylene sulfide resin having a group represented by the general formula (1) at the terminal is generated by recombination with a sulfur radical derived from the —SS— bond in the polymerization inhibitor (wherein the reaction formula (4)).
- the detached iodine atom is in a free state (iodine radical), or iodine radicals are recombined to generate iodine molecules (reaction formula (5)).
- the reaction product obtained by performing the above melt polymerization is once cooled to a solid state, and then heated and polymerized under reduced pressure or in a non-oxidizing atmosphere in the case of atmospheric pressure. Can be reacted.
- the cooling to the solid state is in the range of 100 to 260 ° C, preferably in the range of 130 to 250 ° C, more preferably in the range of 150 to 230 ° C.
- the heating after cooling to the solid state may be performed under the same temperature and pressure conditions as in the melt polymerization.
- the polyarylene sulfide resin having the group represented by the general formula (1) at the terminal of the present invention is derived from the production method, and the polyarylene sulfide having the group represented by the general formula (1) at the terminal
- the reaction product is obtained as a polyarylene sulfide resin composition containing iodine atoms in the range of 0.01 to 10,000 ppm, preferably in the range of 10 to 5,000 ppm with respect to the resin and the polyarylene sulfide resin.
- the polyarylene sulfide resin composition of the present invention contains iodine atoms instead of chlorine atoms as halogen atoms, it is also possible to keep the iodine atom concentration low by utilizing the sublimability of iodine molecules as described above. In that case, it may be 900 ppm or less, preferably 100 ppm or less, and further 10 ppm or less. Although it is possible to remove iodine atoms below the detection limit, it is not practical in view of productivity.
- the polyarylene sulfide resin having a group represented by the general formula (1) at the terminal of the present invention has a resin structure having a structure in which an aromatic ring and a sulfur atom are bonded as a repeating unit, It originates in the manufacturing method, and has the group of the said General formula (1) on the terminal aromatic ring.
- polyarylene sulfide resin having a group represented by the general formula (1) at the terminal of the present invention is represented by the following general formula (5).
- R 5 represents any one of the monovalent groups represented by the general formulas (a) to (c)) or the following general formula (7)
- R 6 represents any one of the monovalent groups represented by the general formulas (a) to (c)).
- a structure that is bonded at the meta position represented by is more preferable.
- the polyarylene sulfide resin of the present invention has the following general formula (10)
- R 7 and R 8 each independently represents a hydrogen atom, an alkyl group having 1 to 4 carbon atoms, a nitro group, an amino group, a phenyl group, a methoxy group, or an ethoxy group).
- Such a structure having a repeating unit having a substituent in the side chain is not preferable because it causes a decrease in crystallinity and heat resistance, and it is preferable that such a repeating unit is not substantially contained.
- “substantially not contained” means a ratio of 2 wt% or less, preferably 0.2 wt%, with respect to the total of the structural portion represented by the formula (5).
- polyarylene sulfide resin includes not only the structural portion represented by the formula (1) but also the following structural formula (11).
- the polyarylene sulfide resin having the group represented by the general formula (1) at the terminal of the present invention has a melting point in the range of 250 to 300 ° C, preferably in the range of 265 to 300 ° C.
- the polyarylene sulfide resin of the present invention has a melt viscosity (V6) measured at 300 ° C. in the range of 1 to 2,000 [Pa ⁇ s], more preferably 5 to 1,700 [Pa ⁇ s]. Range.
- melt viscosity (V6) measured at 300 ° C. is an orifice having a temperature / 300 ° C., a load of 1.96 MPa, an orifice length and an orifice diameter of 10/1 using a flow tester. Represents the melt viscosity after holding for 6 minutes.
- the polyarylene sulfide resin having the group represented by the general formula (1) at the terminal obtained by the production method of the present invention and the resin composition containing the resin may be used alone or in combination with other components.
- melt processing methods such as extrusion molding, compression molding and blow molding, it can be processed into a molded product having excellent heat resistance, molding processability, dimensional stability and the like.
- the polyarylene sulfide resin of the present invention has a group represented by the general formula (1) at the terminal, it is combined with a silane compound or a thermoplastic elastomer having a functional group reactive with the group.
- a resin composition having excellent adhesion and impact resistance can be obtained.
- the blending amount of the silane compound and the thermoplastic elastomer varies depending on the component to be added and the use, and cannot be specified unconditionally. For example, it is in the range of 0.01 to 10 parts by weight, preferably 100 parts by weight of the polyarylene sulfide resin, preferably It is in the range of 0.1 to 5 parts by mass.
- Examples of the silane compound having a functional group reactive with the group represented by the general formula (1) include ⁇ -glycidoxypropyltrimethoxysilane and ⁇ -glycidoxypropyltriethoxysilane.
- silane coupling agents such as ⁇ - (3,4-epoxycyclohexyl) ethyltrimethoxysilane, ⁇ -glycidoxypropylmethyldiethoxysilane, and ⁇ -glycidoxypropylmethyldimethoxysilane.
- thermoplastic elastomer having a functional group reactive with the group represented by the general formula (1) include an epoxy group, an amino group, a hydroxyl group, a carboxy group, a mercapto group, an isocyanate group, and an oxazoline group.
- a plastic elastomer can be mentioned, and particularly preferably, it can be obtained by copolymerization of an ⁇ -olefin and a vinyl polymerizable compound having the functional group.
- Examples of the ⁇ -olefins include ⁇ -olefins having 2 to 8 carbon atoms such as ethylene, propylene, and butene-1.
- Examples of the vinyl polymerizable compounds having the functional group include ⁇ , ⁇ -unsaturated carboxylic acids such as (meth) acrylic acid and (meth) acrylic acid esters and alkyl esters thereof, maleic acid, fumaric acid, and itaconic acid.
- Other unsaturated dicarboxylic acids having 4 to 10 carbon atoms and mono- and diesters thereof, ⁇ , ⁇ -unsaturated dicarboxylic acids such as acid anhydrides and derivatives thereof, glycidyl (meth) acrylate, etc.
- An ethylene-propylene copolymer having at least one functional group selected from the group consisting of the partial structures represented by Copolymer is preferred for improving toughness and impact resistance.
- An inorganic filler can be added to the polyarylene sulfide resin obtained by the production method of the present invention. By blending the inorganic filler, a composition having high rigidity and high heat stability can be obtained.
- inorganic fillers include powdery fillers such as carbon black, calcium carbonate, silica, and titanium oxide, plate-like fillers such as talc and mica, granular fillers such as glass beads, silica beads, and glass balloons, and glass fibers. And fibrous fillers such as carbon fiber and wollastonite fiber, and glass flakes.
- the content of the inorganic filler is in the range of 1 to 300 parts by mass with respect to 100 parts by mass of the polyarylene sulfide resin.
- the polyarylene sulfide resin of the present invention contains, as additives, a release agent, a colorant, a heat stabilizer, an ultraviolet stabilizer, a foaming agent, a rust inhibitor, a flame retardant, and a lubricant with respect to 100 parts by mass of the polyarylene sulfide resin. It can be contained in the range of 1 to 10 parts by mass. Further, similarly, synthetic resins and elastomers as described below can be mixed and used within a range of 1 to 300 parts by mass with respect to 100 parts by mass of the polyarylene sulfide resin.
- These synthetic resins include polyester, polyamide, polyimide, polyetherimide, polycarbonate, polyphenylene ether, polysulfone, polyethersulfone, polyetheretherketone, polyetherketone, polyethylene, polypropylene, polytetrafluoroethylene, polydifluoride. Ethylene fluoride, polystyrene, ABS resin, epoxy resin, silicone resin, phenol resin, urethane resin, liquid crystal polymer, and the like.
- thermoplastic elastomers include polyolefin elastomers, fluorine elastomers, and silicone elastomers.
- the polyarylene sulfide resin of the present invention or the resin composition containing the resin also has various performances such as heat resistance and dimensional stability inherent in the polyarylene sulfide resin.
- Electrical parts such as molded parts, automotive parts such as lamp reflectors and various electrical parts, interior materials such as various buildings, aircraft and automobiles, precision parts such as OA equipment parts, camera parts and watch parts It is widely useful as a material for various molding processes such as injection molding or compression molding, extrusion molding of composites, sheets, pipes, etc., or pultrusion molding, or as a material for fibers or films.
- the PPS resin was pulverized with a small pulverizer and then sieved using a test sieve of Japanese Industrial Standard Z8801 with an aperture of 0.5 mm. 0.5 parts by mass of 3-glycidoxypropyltrimethoxysilane was added to 100 parts by mass of the PPS resin that passed through the sieve, and after mixing uniformly, the melt viscosity V6 was measured. The degree of increase in viscosity was calculated as a magnification from the ratio of melt viscosity V6 after addition / melt viscosity V6 before addition. The higher the degree of increase in viscosity, the higher the reactivity and the better.
- the iodine content in the PPS resin was determined by absorbing the gas and residue generated by burning the PPS resin with a Diane Instruments combustion gas absorption device into pure water, and quantifying the iodine ion in the absorption solution with a Dionex ion chromatograph.
- Example 1 30-0.0 g of p-diiodobenzene (Tokyo Kasei Co., Ltd., p-diiodobenzene purity of 98.0% or more), solid sulfur (sulfur (powder) manufactured by Kanto Chemical Co., Inc.) 27.00 g, 4,4′- Dithiobisbenzoic acid (Wako Pure Chemical Industries, Ltd., 4,4′-dithiobisbenzoic acid, Technical Grade) 0.60 g was heated to 180 ° C. and dissolved and mixed under nitrogen. Next, the temperature was raised to 220 ° C. and the pressure was reduced to an absolute pressure of 26.6 kPa. The obtained molten mixture was melt polymerized for 8 hours by changing the temperature and pressure stepwise so that the absolute pressure was 133 Pa at 320 ° C. By this reaction, 91 g of PPS resin was obtained. The measurement results are shown in Table 1.
- Example 2 89 g of PPS resin was obtained in the same manner as in Example 1, except that “1.0 g of 4,4′-dithiobisbenzoic acid” was used instead of “0.60 g of“ 4,4′-dithiobisbenzoic acid ”. .
- the measurement results are shown in Table 1.
- Example 3 86 g of PPS resin was obtained in the same manner as in Example 1 except that “4,4′-dithiobisbenzoic acid 2.0 g” was used instead of “4,4′-dithiobisbenzoic acid 0.60 g”. .
- the measurement results are shown in Table 1.
- Example 4 93 g of PPS resin was obtained in the same manner as in Example 1 except that “4,4′-dithiobisbenzoic acid 0.15 g” was used instead of “4,4′-dithiobisbenzoic acid 0.60 g”. .
- the measurement results are shown in Table 1.
- Example 5 Heat 300.0 g of p-diiodobenzene, 27.00 g of solid sulfur, 1.0 g of 4,4′-dithiobisbenzoic acid, 0.3 g of 1,3-diiodo-4-nitrobenzene to 180 ° C. Dissolved and mixed. Subsequent operations were performed in the same manner as in Example 1 to obtain 90 g of PPS resin. The measurement results are shown in Table 1.
- Example 6 93 g of PPS resin was obtained in the same manner as in Example 1 except that p-mercaptobenzoic acid (Wako Pure Chemical Industries, Ltd., purity 97%) was used instead of 4,4′-dithiobisbenzoic acid. The measurement results are shown in Table 1.
- Example 7 90 g of PPS resin was obtained in the same manner as in Example 1 except that p-iodobenzoic acid (Wako Pure Chemical Industries, Ltd., purity 98%) was used instead of 4,4′-dithiobisbenzoic acid. The measurement results are shown in Table 1.
- Example 8 To a solid of 248.0 g of p-iodobenzoic acid, 280.0 g of 10% NaOH solution (0.7 mol of NaOH relative to p-iodobenzoic acid) was added and stirred for 1 hour. Only the carboxylic acid type changed to the carboxylic acid Na type was dissolved, and the carboxylic acid type not dissolved was removed by filtration. The filtrate in which the Na carboxylate was dissolved was heated to 80 ° C. under reduced pressure to remove water, and 120 g of sodium p-iodobenzoate was obtained.
- Example 9 90 g of PPS resin was obtained in the same manner as in Example 1 except that p-mercaptophenylacetic acid (Wako Pure Chemical Industries, Ltd., purity 97%) was used instead of 4,4′-dithiobisbenzoic acid. The measurement results are shown in Table 1.
- Example 10 83.4 g of 48% NaOH aqueous solution and 297.4 g of N-methyl-2-pyrrolidone were charged into a pressure vessel and stirred at 230 ° C. for 3 hours. Then, the water was removed by releasing the pressure at 230 ° C., the pressure was reduced to 0.1 MPa, the air was sealed, and the temperature was lowered to 200 ° C. or lower. P-diiodobenzene (329.9 g) was dissolved by heating to 130 ° C. or higher, charged into a reaction vessel, heated to 250 ° C. and stirred for 4 hours.
- the PPS resin of Comparative Example 1 has a low viscosity increase rate in the reactivity evaluation test and is difficult to react with the glycidyl group-containing silane coupling agent.
- the PPS resins of Comparative Examples 2 and 3 were not only able to have a high molecular weight, but also in the reactivity test, the PPS resin gelled and could not be measured.
- Example 11 After obtaining the PPS resin in the same manner as in Example 1, it was further molded into a pellet shape having a diameter of 2 mm ⁇ length of 4 mm, and at atmospheric pressure and under nitrogen gas flow at 150 ° C. for 1 hour, 3 hours, and 20 hours. The amount of iodine after the heat treatment was measured. The results are shown in Table 2.
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Abstract
Description
また、前記の溶融重合は、加熱装置、減圧装置および撹拌装置を備えていれば公知の樹脂の溶融混練機を用いることができ、例えば、バンバリーミキサー、ニーダー、連続混練機、単軸押出機、二軸押出機等が挙げられる。
参考例で製造したPPS樹脂を島津製作所製フローテスター、CFT-500Cを用い、300℃、荷重:1.96×106Pa、L/D=10/1にて、6分間保持した後に測定した。
PPS樹脂を小型粉砕機で粉砕した後、日本工業規格Z8801の目開き0.5mmの試験用篩いを用いて篩った。篩いを通過したPPS樹脂100質量部に対し、3-グリシドキシプロピルトリメトキシシラン0.5質量部を配合し、均一に混合した後に溶融粘度V6を測定した。添加後の溶融粘度V6/添加前の溶融粘度V6の比から粘度上昇度を倍率として算出した。粘度上昇度が大きいほど反応性が高く、優れていることを示す。
PPS樹脂中のヨウ素含有量は、ダイアンインスツルメンツ燃焼ガス吸収装置でPPS樹脂を燃焼させ発生したガスおよび残渣を純水に吸収させ、吸収液中のヨウ素イオンをダイオネクスイオンクロマトグラフで定量した。
理学電気工業株式会社製 蛍光X線分析装置ZSX100eによって、硫黄原子総量を測定し、下記式に基づき、ジスルフィド結合の割合を求めた。
パーキンエルマー製DSCを用いて、50℃から350℃まで20℃/分で昇温し、ポリマーが融解したときの吸熱ピークのピーク温度を測定した。
p-ジヨードベンゼン(東京化成株式会社、p-ジヨードベンゼン純度98.0%以上)300.0g、固体硫黄(関東化学株式会社製、硫黄(粉末))27.00g、4,4’-ジチオビス安息香酸(和光純薬工業株式会社製、4,4’-ジチオビス安息香酸、Technical Grade)0.60gを180℃に加熱してそれらを窒素下で溶解、混合した。次に220℃に昇温し、絶対圧26.6kPaまで減圧した。得られた溶融混合物を、320℃で絶対圧133Paとなるように、段階的に温度と圧力変化させて、8時間溶融重合した。この反応により、PPS樹脂91gを得た。各測定結果を表1に示した。
前記「4,4’-ジチオビス安息香酸0.60g」の替りに、「4,4’-ジチオビス安息香酸1.0g」を用いたこと以外は実施例1と同様にしてPPS樹脂89gを得た。各測定結果を表1に示した。
前記「4,4’-ジチオビス安息香酸0.60g」の替りに、「4,4’-ジチオビス安息香酸2.0g」を用いたこと以外は実施例1と同様にしてPPS樹脂86gを得た。各測定結果を表1に示した。
前記「4,4’-ジチオビス安息香酸0.60g」の替りに、「4,4’-ジチオビス安息香酸0.15g」を用いたこと以外は実施例1と同様にしてPPS樹脂93gを得た。各測定結果を表1に示した。
p-ジヨードベンゼン300.0g、固体硫黄27.00g、4,4’-ジチオビス安息香酸1.0g、1,3-ジヨード-4-ニトロベンゼン0.3gを180℃に加熱してそれらを窒素下で溶解、混合した。以後の操作を実施例1と同様に行い、PPS樹脂90gを得た。各測定結果を表1に示した。
4,4’-ジチオビス安息香酸の替りにp-メルカプト安息香酸(和光純薬株式会社、純度97%)を用いたこと以外は実施例1と同様にしてPPS樹脂93gを得た。各測定結果を表1に示した。
4,4’-ジチオビス安息香酸の替りにp-ヨード安息香酸(和光純薬株式会社、純度98%)を用いたこと以外は実施例1と同様にしてPPS樹脂90gを得た。各測定結果を表1に示した。
p-ヨード安息香酸248.0gの固体に10%NaOH溶液280.0g(p-ヨード安息香酸に対して0.7molのNaOH)を入れて、1時間攪拌した。カルボン酸Na型に変化したものだけが溶解し、溶解しないカルボン酸型のものをろ過によって除去した。カルボン酸Na型が溶解しているろ液を、減圧しながら80度に加温することで水を除去して、p-ヨード安息香酸ナトリウム120gを得た。
4,4’-ジチオビス安息香酸の替りにp-メルカプトフェニル酢酸(和光純薬株式会社、純度97%)を用いたこと以外は実施例1と同様にしてPPS樹脂90gを得た。各測定結果を表1に示した。
48%NaOH水溶液83.4gとN-メチル-2-ピロリドン297.4gを耐圧容器に仕込み、230度で3時間攪拌した。その後、230℃の状態で放圧することで水を除き、0.1MPaまで降圧させ、密閉して200℃以下まで温度を低下させた。p-ジヨードベンゼン329.9gを130℃以上に加熱溶解させて、反応容器に投入し、250℃まで昇温後4時間攪拌した。冷却後、内容物を取り出し、水を加えて攪拌し、ろ過することで未反応のp-ジヨードベンゼンをろ過物として除いた。ろ液の水溶液に塩酸を加えて、水溶液のpHを4に調整し、水溶液中に濃い褐色のオイル状物質が生じ、そこにクロロホルムを加えて、抽出した。水層には、N-メチル-2-ピロリドンやその開環物である4-メチルアミノ酪酸を含むため、水層は破棄した。さらにクロロホルム層の水洗及び分液を2回行った。そしてクロロホルム層に水と希塩酸を加えて、pHを1.0以下に調整し、目的物のN-メチル-(p-ヨードフェニル)-アミノ酪酸は塩酸塩型に変化し、水層側に移動し、水層側には副生成物のp-ヨードフェノールが存在するため、破棄した。残った水溶液に48%NaOH溶液を加えて、pHを4.0に調整することで、塩酸塩が中和され、濃い褐色のN-メチル-(p-ヨードフェニル)-アミノ酪酸が析出し、それをクロロホルムで抽出し、溶媒を減圧除去することで、N-メチル-(p-ヨードフェニル)-アミノ酪酸28.3gを得て、それを核磁気共鳴装置及び質量分析計によって出来ていることを確認した。
前記「4,4’-ジチオビス安息香酸」の替りに「ジフェニルジスルフィド(住友精化株式会社 DPDS)」を用いたこと以外は実施例1と同様にしてPPS樹脂91gを得た。各測定結果を表1に示した。
p-ジヨードベンゼン300.0gの替りに2,5-ジヨード安息香酸(シグマアルドリッチ株式会社 2,5-Diiodobenzoic acid純度97%)340.0gを、かつ4,4’-ジチオビス安息香酸0.60gの替りにジフェニルジスルフィド0.60gを用いたこと以外は実施例1と同様にして、測鎖にカルボキシ基を有するPPS樹脂101gを得た。各測定結果を表1に示した。
p-ジヨードベンゼン300.0g、2,5-ジヨード安息香酸170.0g、固体硫黄27.00g、ジフェニルジスルフィド0.60gを180℃に加熱してそれらを窒素下で溶解、混合した。以後の操作を実施例1と同様に行い、側鎖にカルボキシ基を有するPPS樹脂95gを得た。各測定結果を表1に示した。
実施例1と同様にしてPPS樹脂を得た後、さらに、直径2mm×長さ4mmのペレット状に成形し、大気圧下かつ窒素ガス流通下、150℃で、1時間、3時間、20時間熱処理を施した後のヨウ素量を測定した。その結果を表2に示した。
Claims (7)
- 前記重合禁止剤が下記一般式(2)
または下記一般式(3)
または下記一般式(4)
- 前記混合物中の前記重合禁止剤の含有量が、単体硫黄1モルに対して0.0001~0.1モルの範囲である請求項1または2記載のポリアリーレンスルフィド樹脂の製造方法。
- 前記請求項3~5の何れか一項記載のポリアリーレンスルフィド樹脂組成物と、グリシジル基、カルボキシ基、ヒドロキシ基またはアミノ基と反応性を示す官能基を有する化合物とを含むポリアリーレンスルフィド樹脂組成物。
- 請求項3~6記載のポリアリーレンスルフィド樹脂組成物を成形してなるポリアリーレンスルフィド樹脂成形品。
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Cited By (5)
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WO2016121894A1 (ja) * | 2015-01-26 | 2016-08-04 | 帝人株式会社 | 樹脂組成物 |
JPWO2015033855A1 (ja) * | 2013-09-05 | 2017-03-02 | Dic株式会社 | ポリアリーレンスルフィド繊維及びその製造方法 |
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KR20230022007A (ko) * | 2021-08-06 | 2023-02-14 | 에이치디씨폴리올 주식회사 | 폴리아릴렌 설파이드 스테이플 섬유 및 이의 제조방법 |
Citations (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2513188A (en) | 1948-09-10 | 1950-06-27 | Macallum Alexander Douglas | Mixed phenylene sulfide resins |
US2583941A (en) | 1946-11-13 | 1952-01-29 | Jr Thurlow M Gordon | Device for detecting variations in fluid pressure |
US4605732A (en) | 1984-06-09 | 1986-08-12 | Bayer Aktiengesellschaft | Process for the production of polyarylene sulphides with functional end groups |
US4746758A (en) | 1986-09-29 | 1988-05-24 | Eastman Kodak Company | Processes for preparing iodinated aromatic compounds |
US4786713A (en) | 1987-11-06 | 1988-11-22 | Eastman Kodak Company | Copoly(arylene sulfidex-disulfide) |
JPH04506228A (ja) * | 1989-06-12 | 1992-10-29 | イーストマン コダック カンパニー | 低分子量の反応停止コポリ(アリーレンスルフィド) |
EP0549977A1 (en) | 1991-12-25 | 1993-07-07 | Mitsubishi Petrochemical Co., Ltd. | Carboxyl-containing polyphenylene sulfide, process for producing the same, and resin composition containing the same |
JPH05271530A (ja) | 1992-03-26 | 1993-10-19 | Mitsubishi Petrochem Co Ltd | 熱可塑性樹脂組成物 |
JPH06172489A (ja) | 1992-12-08 | 1994-06-21 | Mitsubishi Petrochem Co Ltd | 熱可塑性樹脂組成物 |
JP2001279097A (ja) | 2000-03-31 | 2001-10-10 | Dainippon Ink & Chem Inc | ポリアリーレンスルフィド組成物 |
JP2008247955A (ja) | 2007-03-29 | 2008-10-16 | Dic Corp | ポリアリーレンスルフィド樹脂組成物 |
JP2010501661A (ja) | 2006-08-24 | 2010-01-21 | エスケー ケミカルズ カンパニー リミテッド | ポリ(アリーレンスルフィド)の製造方法 |
WO2012057319A1 (ja) * | 2010-10-29 | 2012-05-03 | 東レ株式会社 | ポリアリーレンスルフィドの製造方法およびポリアリーレンスルフィド |
EP2980121A1 (en) | 2013-03-25 | 2016-02-03 | DIC Corporation | Method for producing polyarylene sulfide resin, and polyarylene sulfide resin composition |
Family Cites Families (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS578898B2 (ja) | 1973-06-28 | 1982-02-18 | ||
US4952671A (en) * | 1988-07-15 | 1990-08-28 | Eastman Kodak Company | Terminated copoly(arylene sulfide) |
US4945155A (en) * | 1989-05-11 | 1990-07-31 | Eastman Kodak Company | Preparation of low color copoly(arylene sulfide) by heating copoly(arylene sulfide) |
US5175243A (en) * | 1990-11-14 | 1992-12-29 | Phillips Petroleum Company | Process for preparing arylene sulfide polymers with halo benzene containing deactivating group |
JPH05287202A (ja) * | 1992-04-08 | 1993-11-02 | Mitsubishi Petrochem Co Ltd | 熱可塑性樹脂組成物 |
JPH0733974A (ja) * | 1993-07-16 | 1995-02-03 | Mitsubishi Chem Corp | 熱可塑性樹脂組成物 |
US8883960B2 (en) * | 2007-01-04 | 2014-11-11 | Sk Chemicals Co., Ltd. | Polyarylene sulfide resin with excellent luminosity and preparation method thereof |
KR101549205B1 (ko) * | 2008-12-23 | 2015-09-02 | 에스케이케미칼 주식회사 | 폴리아릴렌 설파이드의 제조 방법 |
KR101554010B1 (ko) | 2008-12-31 | 2015-09-18 | 에스케이케미칼 주식회사 | 유리 요오드 저감 폴리아릴렌 설파이드의 제조 방법 |
KR101287729B1 (ko) * | 2009-05-18 | 2013-07-19 | 가부시끼가이샤 구레하 | 폴리아릴렌술피드 및 그의 제조 방법 |
KR101780404B1 (ko) * | 2010-02-01 | 2017-09-21 | 에스케이케미칼 주식회사 | 요오드 저감 폴리아릴렌 설파이드의 제조 방법 |
KR101181571B1 (ko) | 2011-01-26 | 2012-09-13 | 김단 | 이중용기. |
KR102064026B1 (ko) * | 2012-04-13 | 2020-01-08 | 티코나 엘엘씨 | 자동차 적용례를 위한 폴리아릴렌 설파이드 구성요소 |
WO2014025190A1 (ko) | 2012-08-07 | 2014-02-13 | 에스케이케미칼주식회사 | 폴리아릴렌 설파이드 수지 및 그의 제조 방법 |
JP6847572B2 (ja) * | 2014-07-30 | 2021-03-24 | 三菱エンジニアリングプラスチックス株式会社 | ポリアミド樹脂組成物および成形品 |
JP6453147B2 (ja) * | 2015-04-03 | 2019-01-16 | 三菱エンジニアリングプラスチックス株式会社 | ポリアミド樹脂組成物および成形品 |
-
2014
- 2014-03-20 KR KR1020157016795A patent/KR101598792B1/ko active IP Right Review Request
- 2014-03-20 CN CN201911149444.0A patent/CN111073286A/zh not_active Withdrawn
- 2014-03-20 JP JP2014546216A patent/JP5708898B2/ja active Active
- 2014-03-20 US US14/779,346 patent/US9688817B2/en active Active
- 2014-03-20 EP EP22158882.5A patent/EP4029900A1/en not_active Withdrawn
- 2014-03-20 CN CN201480018386.7A patent/CN105051092B/zh active Active
- 2014-03-20 WO PCT/JP2014/057739 patent/WO2014156946A1/ja active Application Filing
- 2014-03-20 EP EP14774358.7A patent/EP2980121B1/en active Active
Patent Citations (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2583941A (en) | 1946-11-13 | 1952-01-29 | Jr Thurlow M Gordon | Device for detecting variations in fluid pressure |
US2513188A (en) | 1948-09-10 | 1950-06-27 | Macallum Alexander Douglas | Mixed phenylene sulfide resins |
US4605732A (en) | 1984-06-09 | 1986-08-12 | Bayer Aktiengesellschaft | Process for the production of polyarylene sulphides with functional end groups |
US4746758A (en) | 1986-09-29 | 1988-05-24 | Eastman Kodak Company | Processes for preparing iodinated aromatic compounds |
US4786713A (en) | 1987-11-06 | 1988-11-22 | Eastman Kodak Company | Copoly(arylene sulfidex-disulfide) |
JPH04506228A (ja) * | 1989-06-12 | 1992-10-29 | イーストマン コダック カンパニー | 低分子量の反応停止コポリ(アリーレンスルフィド) |
EP0549977A1 (en) | 1991-12-25 | 1993-07-07 | Mitsubishi Petrochemical Co., Ltd. | Carboxyl-containing polyphenylene sulfide, process for producing the same, and resin composition containing the same |
JPH05271530A (ja) | 1992-03-26 | 1993-10-19 | Mitsubishi Petrochem Co Ltd | 熱可塑性樹脂組成物 |
JPH06172489A (ja) | 1992-12-08 | 1994-06-21 | Mitsubishi Petrochem Co Ltd | 熱可塑性樹脂組成物 |
JP2001279097A (ja) | 2000-03-31 | 2001-10-10 | Dainippon Ink & Chem Inc | ポリアリーレンスルフィド組成物 |
JP2010501661A (ja) | 2006-08-24 | 2010-01-21 | エスケー ケミカルズ カンパニー リミテッド | ポリ(アリーレンスルフィド)の製造方法 |
JP2008247955A (ja) | 2007-03-29 | 2008-10-16 | Dic Corp | ポリアリーレンスルフィド樹脂組成物 |
WO2012057319A1 (ja) * | 2010-10-29 | 2012-05-03 | 東レ株式会社 | ポリアリーレンスルフィドの製造方法およびポリアリーレンスルフィド |
EP2980121A1 (en) | 2013-03-25 | 2016-02-03 | DIC Corporation | Method for producing polyarylene sulfide resin, and polyarylene sulfide resin composition |
Non-Patent Citations (1)
Title |
---|
See also references of EP2980121A1 |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
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JPWO2015030137A1 (ja) * | 2013-08-30 | 2017-03-02 | Dic株式会社 | ガスケット用樹脂組成物、その製造方法及び二次電池用ガスケット |
JPWO2015030136A1 (ja) * | 2013-08-30 | 2017-03-02 | Dic株式会社 | 水回り部品用樹脂組成物及び流体用配管 |
JPWO2015033855A1 (ja) * | 2013-09-05 | 2017-03-02 | Dic株式会社 | ポリアリーレンスルフィド繊維及びその製造方法 |
WO2016121894A1 (ja) * | 2015-01-26 | 2016-08-04 | 帝人株式会社 | 樹脂組成物 |
CN107001798A (zh) * | 2015-01-26 | 2017-08-01 | 帝人株式会社 | 树脂组合物 |
JPWO2016121894A1 (ja) * | 2015-01-26 | 2017-11-02 | 帝人株式会社 | 樹脂組成物 |
JP2019506517A (ja) * | 2016-03-09 | 2019-03-07 | イニッツ・カンパニー・リミテッドInitz Co.,Ltd. | 優れた表面平滑性及び金属付着性を有するランプリフレクター用の樹脂組成物 |
Also Published As
Publication number | Publication date |
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EP4029900A1 (en) | 2022-07-20 |
EP2980121A1 (en) | 2016-02-03 |
JP5708898B2 (ja) | 2015-04-30 |
KR20150085087A (ko) | 2015-07-22 |
US20160060397A1 (en) | 2016-03-03 |
JPWO2014156946A1 (ja) | 2017-02-16 |
CN105051092A (zh) | 2015-11-11 |
CN111073286A (zh) | 2020-04-28 |
US9688817B2 (en) | 2017-06-27 |
KR101598792B1 (ko) | 2016-03-02 |
EP2980121B1 (en) | 2022-04-13 |
CN105051092B (zh) | 2022-04-26 |
EP2980121A4 (en) | 2016-08-17 |
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