WO2000008079A1 - Copolymere sequence lineaire et composition de resine contenant ledit copolymere - Google Patents
Copolymere sequence lineaire et composition de resine contenant ledit copolymere Download PDFInfo
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- WO2000008079A1 WO2000008079A1 PCT/JP1999/004159 JP9904159W WO0008079A1 WO 2000008079 A1 WO2000008079 A1 WO 2000008079A1 JP 9904159 W JP9904159 W JP 9904159W WO 0008079 A1 WO0008079 A1 WO 0008079A1
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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
- C08L53/00—Compositions of block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers
- C08L53/02—Compositions of block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers of vinyl-aromatic monomers and conjugated dienes
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F297/00—Macromolecular compounds obtained by successively polymerising different monomer systems using a catalyst of the ionic or coordination type without deactivating the intermediate polymer
- C08F297/02—Macromolecular compounds obtained by successively polymerising different monomer systems using a catalyst of the ionic or coordination type without deactivating the intermediate polymer using a catalyst of the anionic type
- C08F297/04—Macromolecular compounds obtained by successively polymerising different monomer systems using a catalyst of the ionic or coordination type without deactivating the intermediate polymer using a catalyst of the anionic type polymerising vinyl aromatic monomers and conjugated dienes
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L25/00—Compositions of, homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an aromatic carbocyclic ring; Compositions of derivatives of such polymers
- C08L25/02—Homopolymers or copolymers of hydrocarbons
- C08L25/04—Homopolymers or copolymers of styrene
- C08L25/08—Copolymers of styrene
- C08L25/14—Copolymers of styrene with unsaturated esters
Definitions
- the present invention relates to a linear block copolymer. More specifically, the present invention relates to a vinyl aromatic hydrocarbon polymer block (S), a synergistic gen polymer block (B), and a vinyl aromatic hydrocarbon / conjugated gen copolymer block.
- the hydrogen polymer block is composed of at least two fractions having different peak molecular weights as a whole, and is provided at each inner end of the vinyl aromatic hydrocarbon polymer block at both ends.
- the present invention also relates to a resin composition containing the linear block copolymer and a styrene-based resin in a specific ratio.
- Block copolymers composed of vinyl aromatic hydrocarbons and conjugated gens and having a relatively high content of vinyl aromatic hydrocarbons are injection-molded by utilizing their properties such as transparency and impact resistance. It is used for applications and extrusion molding of sheets and films.
- a block copolymer comprising a vinyl aromatic hydrocarbon and a conjugated gen and a process for producing the same have been used for the purpose of improving mechanical properties such as impact resistance while maintaining transparency.
- Several methods or compositions have been proposed. For example, Japanese Patent Application Laid-Open No. 52-887888 (corresponding to U.S. Pat. No. 4,167,545) discloses a catalyst for the purpose of improving transparency and impact resistance.
- the branched block copolymer obtained by the method of dividing and adding is disclosed in Japanese Patent Application Laid-Open No. Heisei 4-277509 (US Pat. Nos. 5,227,419 and 1992).
- (Corresponding to U.S. Pat. No. 4,924,490) includes a graded block adopting a method in which a catalyst is dividedly added for the purpose of improving environmental stress cracking resistance.
- a method for producing a polymer is disclosed in Japanese Patent Application Laid-Open No. 63-1455314 (US Patent Nos. 4,939,208 and European Patent No. 2,705,15). the corresponding), in order to obtain transparency and mechanical properties, S E one B E one BZS to -!
- S 2 structure (S and S 2 is the aromatic vinyl homopolymers block, B ⁇ Is a conjugated homogenous polymer block, BZS is Dam
- a method for producing a block copolymer having a W copolymer block (which represents a W copolymer block) is disclosed in Japanese Patent Application Laid-Open No. 7-97418, which discloses transparency and impact resistance.
- Blocks with features such as block ratios, arrangement of polymer blocks, and ratios of the amount of conjugated gen in the portion where the vinyl aromatic hydrocarbon and conjugated gen are random copolymerized for improvement Copolymers are disclosed.
- these block copolymers were subjected to sheet molding as a composition with a styrene-based resin, and then formed into molded articles such as beverage cups and frozen dessert cups.
- the balance of transparency, impact resistance, rigidity, etc. at the time was not sufficient, and further improvement was desired.
- the present inventors have conducted intensive studies in order to solve the above problems associated with the conventional technology. As a result, it includes vinyl aromatic hydrocarbon polymer block (S), conjugated gen polymer block (B), and vinyl aromatic hydrocarbon Z conjugated gen copolymer block (B / S)
- a block copolymer having both ends is a vinyl aromatic hydrocarbon polymer block, and a block having both ends is a vinyl aromatic hydrocarbon polymer.
- At least two fractions having different peak molecular weights are included, and the inner ends of the vinyl aromatic hydrocarbon polymer blocks at both ends are each conjugated with a conjugated polymer block.
- Blocks are directly attached and the inner ends of each of these conjugated diene polymer blocks Have a specific block structure having at least one vinyl aromatic hydrocarbon / conjugated gen copolymer block, and the linear block copolymers have at least different peak molecular weights.
- a linear block copolymer which is also characterized by being composed of two fractions, is surprisingly excellent in rigidity while maintaining high transparency. The present inventors have found that it is possible to obtain a molded article exhibiting impact resistance and having a good balance of transparency, rigidity and impact resistance.
- An object of the invention is to provide a novel linear block copolymer having excellent transparency, impact resistance and rigidity.
- Another object of the present invention is to provide a resin composition comprising the above linear block copolymer and a styrene resin, which is excellent in transparency, impact resistance and rigidity. is there.
- At least two vinyl aromatic hydrocarbon polymer blocks (S)
- a linear block copolymer comprising:
- the total amount of vinyl aromatic hydrocarbon monomer units in the linear block copolymer and the total amount of conjugated diene monomer units in the linear block copolymer are reduced. And 65 to 90% by weight and 35 to 10% by weight, respectively, based on the weight of the linear block copolymer.
- the linear block copolymer is:
- the both terminal polymer blocks of the linear block copolymer are vinyl aromatic hydrocarbon polymer blocks (S),
- Each of the vinyl aromatic hydrocarbon polymer blocks at both ends is directly conjugated to the respective inner end thereof.
- the conjugated diene block (B) has at least one vinyl aromatic hydrocarbon Z-conjugated dienzyme block (BZS) directly bonded to the inner end of each of them. At that time, when two vinyl aromatic hydrocarbon / conjugated gen copolymer blocks (BZS) are directly bonded to their inner ends, respectively, the two copolymer blocks are connected. The blocks during that time are the polymer blocks (S) (B) and (B)
- the linear block copolymer contains at least two different fractions ( ⁇ ) and (3), wherein the fraction () is a gel permeate. Having at least one peak molecular weight in the range of 50,000 to 150,000 in the chromatogram obtained by chromatography (GPC), (3) has at least one peak molecular weight in the range of more than 150,000 and not more than 350,000 in the chromatogram,
- the terminal vinyl aromatic hydrocarbon polymer block has at least one peak in the range of 100,000 to 600,000 in the chromatogram obtained by GPC.
- the linear block copolymer has a weight average molecular weight of 500,000 to 500,000.
- a block copolymer characterized by this is provided.
- a resin comprising 100 parts by weight of the above-mentioned linear block copolymer and 300 to 400 parts by weight of a styrene resin.
- the composition is provided
- a linear block copolymer comprising:
- the total amount of vinyl aromatic hydrocarbon monomer units in the linear block copolymer and the total amount of conjugated diene monomer units in the linear block copolymer are reduced. 65 to 90% by weight and 35 to 10% by weight, respectively, based on the weight of the linear block copolymer,
- the linear block copolymer is:
- the two-terminal polymer block of the linear block copolymer is a vinyl aromatic hydrocarbon polymer block (S),
- Each of the bi-terminal aromatic hydrocarbon polymer blocks has a conjugated gen-polymer block directly bonded to its respective inner end.
- the conjugated diene block (B) has at least one vinyl aromatic hydrocarbon conjugated dienzyme block (BZS) directly bonded to its respective inner end.
- BZS vinyl aromatic hydrocarbon conjugated dienzyme block
- the blocks comprise the polymer blocks (S), (B) and (B / S) having at least one adjacent polymer block selected from the group consisting of:
- the linear block copolymer comprises at least two different fractions ( ⁇ ) and (/ 3), wherein the fraction () is a gel permeation fraction.
- the chromatogram obtained by chromatographic chromatography (GPC) has at least one peak molecular weight in the range of 50,000 to 150,000, Fraction (3) has at least one peak molecular weight in the range above 150,000 and below 350,000 in the chromatogram.
- the end-to-end vinyl aromatic hydrocarbon polymer block has at least one block in the range of 100,000 to 600,000 in the chromatogram obtained by GPC.
- the linear block copolymer has a weight average molecular weight of 500,000 to 500,000.
- B / S represents the vinyl aromatic hydrocarbon / conjugated gen copolymer block
- n is an integer from 1 to 5.
- the block of the vinyl aromatic hydrocarbon polymer at both ends is totally 10 and 0 in the chromatogram obtained by GPC.
- the fraction has at least one peak molecular weight in the range of 50,000 to 120,000 in the chromatogram obtained by GPC. And the fraction (/ 3) has at least one peak molecular weight in the range of 160,000 to 300,000 in the chromatogram.
- the content of the fraction ( ⁇ ;) in the linear block copolymer and the content of the fraction (3) in the linear block copolymer are different.
- a resin composition comprising 100 parts by weight of the linear block copolymer according to any one of the above items 1 to 6, and 30 to 400 parts by weight of a styrene resin.
- the linear block copolymer of the present invention comprises at least two vinyl aromatic hydrocarbon polymer blocks (S) and at least two conjugated gen polymer blocks (B). , And at least one video And a non-aromatic hydrocarbon non-conjugated gen copolymer block (BZS).
- at least two vinyl aromatic hydrocarbon polymer blocks (S) described above each contain a plurality of vinyl aromatic hydrocarbon monomers. Consists of units.
- Two vinyl aromatic hydrocarbon polymer blocks (S) which are both terminal polymer blocks in the linear block copolymer, have different forces. Three or more linear block copolymers If they contain the same polymer block (S), they may be the same.
- the at least two conjugated polymer blocks (B) generally comprise a plurality of conjugated monomer units, which may be the same or different.
- at least one vinyl aromatic hydrocarbon Z conjugated gen copolymer block (B / S) generally comprises a vinyl aromatic hydrocarbon monomer unit and a conjugated gen monomer unit, respectively.
- BZS copolymer blocks
- a vinyl aromatic hydrocarbon monomer unit may be contained in the conjugated diene monomer unit of the polymer block (B) during the polymerization, or the polymer block may be used.
- a conjugated dimer unit may be mixed in an extremely small amount.
- the terminal polymer block is a vinyl aromatic hydrocarbon polymer block (S). And a vinyl aromatic hydrocarbon polymer block at both ends.
- Each block has a conjugated diene polymer block (B) directly attached to its respective inner end.
- their conjugated diene block (B) forces at least one vinyl aromatic hydrocarbon non-conjugated dienzyme block (B / S) directly bonded to their respective inner ends. ).
- linear block copolymer of the present invention has the following formula (1)
- S independently represents the vinyl aromatic hydrocarbon polymer block
- B / S represents the vinyl aromatic hydrocarbon Z conjugated diene copolymer block
- n is an integer from 1 to 5.
- S 1-B ⁇ -BSB 9-S 2 S 1 - B 1 - B / S - B 3 - B / S - B 2 - include those having a block structure S 2 and the like.
- the suffixes of “S” and “B” in the above-described formula representing the block structure are respectively conjugated to the vinyl aromatic hydrocarbon polymer block (S) in the linear block copolymer. Represents the block identification number of the gen-polymer block (B).
- a linear block copolymer having such a block structure is prepared from a vinyl aromatic compound in a hydrocarbon solvent in the presence of an organic lithium compound as an initiator. It can be obtained by polymerizing a hydrocarbon monomer and a conjugated gen monomer.
- the linear block copolymer of the present invention contains at least two different fractions ( ⁇ ) and ( ⁇ ), wherein the fraction (a) is In a chromatogram obtained by one-shot chromatography (GPC), the range is 50,000 to 150,000, preferably 50,000. It has at least one peak molecular weight in the range of 0,000 to 1,200,000 and fraction (3) is 150,000 in the above chromatogram. At least one peak molecular weight in the range of greater than 0 and less than or equal to 350,000, preferably in the range of 160,000 to 300,000. Have.
- GPC one-shot chromatography
- the peak molecular weight of the fraction ( ⁇ ) is less than 50,000 or more than 150,000, or the peak molecular weight of the fraction (/ 3) is 15 If it is less than 0, 000 or more than 350, 000, the impact resistance is reduced, so it is preferable. Not good.
- the content of the fraction () in the linear block copolymer of the present invention is preferably from 30 to 70% by weight, more preferably from 35 to 50% by weight. 65% by weight.
- the content of the fraction (3) in the linear block copolymer of the present invention is preferably from 70 to 30% by weight, more preferably from 65 to 35% by weight. % By weight.
- a linear block copolymer having a so-called no-modal or multi-modal molecular weight distribution containing a plurality of fractions having different peak molecular weights is a copolymer.
- Another new block is formed by adding an initiator and a vinyl aromatic hydrocarbon monomer during the polymerization of the vinyl aromatic hydrocarbon monomer, which constitutes the terminal block on the side where polymerization of the coalesce is initiated.
- a method to generate the polymerization starting point of the linear block copolymer molecular chain to generate fractions with different molecular weights, and vinyl aromatic carbonization that constitutes the terminal block on the polymerization termination side During the polymerization of the hydrogen monomer, a deactivator such as alcohol or water is added to partially inactivate the initiator to partially terminate the polymerization, and then the vinyl aromatic hydrocarbon monomer is again produced. Part of the residue that has not been polymerized after being supplied.
- the method of producing another linear block copolymer molecular chain by continuing the polymerization of styrene and producing fractions having different molecular weights differs depending on whether the method is used alone or in combination.
- a plurality of fractions having a peak molecular weight can be simultaneously produced and obtained. It is also possible to mix separately prepared linear block copolymers with different peak molecular weights. Can also be obtained.
- the fraction ( ⁇ ) thus obtained has a low content of vinyl aromatic hydrocarbon monomer units, and the fraction (3) is a vinyl aromatic hydrocarbon monomer. The content of the unit increases. The reason why the transparency, rigidity and impact resistance of the linear block copolymer of the present invention can be improved by making the molecular weight distribution bimodal or multimodal has not been clarified yet.
- the elastomer (a) which has a low content of vinyl aromatic hydrocarbon monomer units, and a low content of vinyl aromatic hydrocarbon monomer units Due to the coexistence of a high resin-like fraction (3), it is considered that it exhibits good mechanical properties while maintaining the inherently high transparency.
- the peak molecular weight of the linear block copolymer can be determined by GPC. That is, a linear block copolymer is subjected to GPC to obtain a GPC curve, and then monodispersed polystyrene is subjected to GPC, using a calibration curve created from the peak count and molecular weight.
- the peak molecular weight is determined by calculating according to the method [for example, see “Gel Permeation Chromatography”, pp. 81-85 (1976, published by Maruzen Co., Ltd., Japan)]. Can be.
- the content of each fraction of the linear block copolymer can be determined from the area ratio of each peak of the GPC curve.
- the total number of hydrogen polymer blocks is in the range of 100,000 to 60,000, preferably 100,000 in the mouth matogram obtained by GPC.
- a fraction with at least one peak molecular weight in the range of 0 to 50, 000, and 120, 000 to 250, 0 in the above chromatogram. Includes fractions having at least one peak molecular weight in the range of 0, preferably 150,000 to 250,000.
- the peak molecular weight of the vinyl aromatic hydrocarbon polymer block at both ends can be adjusted by changing the amount of the catalyst, the amount of vinyl aromatic hydrocarbon added, and the like when producing the block at both ends. It can be.
- the peak molecular weight of the low molecular weight fraction of the vinyl aromatic hydrocarbon polymer block at both ends is less than 100,000 or more than 60,000, or the high molecular weight fragment If the peak molecular weight of the shot is less than 120,000 or more than 250,000, the impact resistance is lowered, which is not preferable.
- the method for measuring the peak molecular weight of the vinyl aromatic polymer block at both ends will be described later.
- the total amount of the vinyl aromatic hydrocarbon monomer units in the linear block copolymer of the present invention is 65 to 90% by weight based on the weight of the linear block copolymer.
- the total amount of the conjugated monomer units in the linear block copolymer is 35 to 10% by weight based on the weight of the linear block copolymer.
- the rigidity decreases, which is not preferable. Conversely, if the total amount of the vinyl aromatic hydrocarbon monomer units exceeds 90% by weight and the total amount of the conjugated diene monomer units is less than 10% by weight, the impact resistance decreases. I don't like it.
- Examples of the vinyl aromatic hydrocarbon monomer used in the present invention include styrene, o-methylstyrene, p-methylstyrene, p-tert-butylstyrene, 1,3-dimethylstyrene, ⁇ -methylstyrene
- Examples include len, vinyl naphthalene, vinyl anthracene, and 1,1-diphenylethylene, and styrene is particularly preferred. These may be used alone or as a mixture of two or more.
- the conjugated gen according to the present invention is a diolefin having one pair of a double bond, for example, 13-butadiene, 2-methylbutadiene (isoprene).
- Percentage of the vinyl aromatic hydrocarbon polymer block defined by the weight% of the vinyl aromatic hydrocarbon monomer contained in the polymer block (S) with respect to the total weight of the hydrocarbon monomer is preferably from 60 to 95% by weight, more preferably from 65 to 90% by weight.
- block rate refers to the oxidative degradation of a linear block copolymer by using oxamium tetroxide as a catalyst and using butyl octapropoxide. (See the method described in IM Ko 1 thoffet al., J. Polym. ScI. Vol. 1, No. 5, pp.
- the weight of the hydrocarbon polymer block component (however, a vinyl aromatic hydrocarbon polymer block component having an average degree of polymerization of about 30 or less is excluded) is the weight of the linear block copolymer. The value obtained by dividing by the total weight of all the vinyl aromatic hydrocarbon monomers therein is expressed in% by weight.
- the block ratio of the linear block copolymer is determined by the ratio of the vinyl aromatic hydrocarbon monomer of the block copolymer to the vinyl aromatic hydrocarbon monomer in the conjugated gen copolymer block (BZS). It can be adjusted by changing the weight of the ene monomer, the weight ratio thereof, the polymerization reactivity ratio, and the like. Specifically, a method in which a mixture of a vinyl aromatic hydrocarbon monomer and a conjugated gen monomer is continuously supplied to a polymerization system while performing polymerization, or a polar compound acting as a randomizing agent is used. A method for copolymerizing a vinyl aromatic hydrocarbon monomer and a conjugated diene monomer using alone or in combination Block rate can be adjusted by adopting
- Examples of the polar compound as a randomizing agent used in the present invention include ethers such as tetrahydrofuran, diethylene glycol dimethyl ether, and diethylene daricol dibutyl ether; Amines such as mine, tetramethylethylenediamine, thioethers, phosphines, phosphoramides, alkylbenzenesulfonates, and alkoxy of potassium and sodium And the like.
- ethers such as tetrahydrofuran, diethylene glycol dimethyl ether, and diethylene daricol dibutyl ether
- Amines such as mine, tetramethylethylenediamine, thioethers, phosphines, phosphoramides, alkylbenzenesulfonates, and alkoxy of potassium and sodium And the like.
- the peak molecular weight of the vinyl aromatic hydrocarbon polymer block at both ends of the linear block copolymer in the present invention is determined by oxidizing the linear block copolymer when measuring the above-mentioned block rate.
- the peak molecular weight of the linear block copolymer is determined in the same manner as described above. be able to.
- the linear block copolymer of the present invention has a weight average molecular weight of 50,000 to 500,000.
- the weight average molecular weight of the linear block copolymer can be determined by GPC based on the standard polystyrene.
- melt flow rate (MFR) of the linear block copolymer of the present invention [JISK-6870] is used, and the G condition (temperature: 200 ° C.) (Measured at (:, load: 5 Kg)) is preferably 0.1 to 50 g / 10 min, more preferably l ⁇ 20 g Z l 0 min
- the linear block copolymer of the present invention is a vinyl aromatic hydrocarbon monohydrate in a hydrocarbon solvent in the presence of an organic lithium compound as an initiator so as to have the above-described block structure.
- a vinyl aromatic hydrocarbon monomer (2) After polymerization of the S1 block, a conjugated monomer is supplied to the reaction system, and then the S1 (3) B] ⁇ block is polymerized, and then a mixture of vinyl aromatic hydrocarbon monomer and conjugated gen monomer is reacted after polymerization of (3) B] ⁇ block.
- the vinyl aromatic hydrocarbon Z-conjugated gen copolymer block BZS which is continuously supplied to the system and directly bonded to the B block is polymerized. (4) After the B / S block is polymerized, the reaction is carried out.
- the linear block copolymer having a bimodal or multimodal molecular weight distribution of the present invention can be obtained, for example, by further adding an initiator and a vinyl aromatic hydrocarbon unit during step (1) in the above method.
- a new polymerization initiation point by adding a monomer to generate fractions having different molecular weights, or a method such as alcohol or water in the middle of the above step (5).
- the vinyl aromatic hydrocarbon monomer is supplied again to continue the polymerization, and the flux having a different molecular weight is obtained.
- hydrocarbon solvent used for producing the linear block copolymer of the present invention examples include butane, pentane, hexane, isopentane, heptane, octane, and isooctane.
- Fats such as tan Alicyclic hydrocarbons such as aromatic hydrocarbons, cyclopentane, methylcyclopentane, cyclohexane, methylcyclohexane, and ethylcyclohexane; and aromatics such as benzene, toluene, ethylbenzene, and xylene Group hydrocarbons and the like.
- the resin composition of the present invention comprises 30 to 400 parts by weight, preferably 50 to 300 parts by weight of a styrene-based resin with respect to 100 parts by weight of the linear block copolymer. It can be produced by blending in parts by weight. If the styrene-based resin is less than 300 parts by weight, the rigidity is not sufficient, and if it exceeds 400 parts by weight, the impact resistance is lowered, which is not preferable.
- styrene resin used in the present invention a non-rubber-modified styrene polymer or a rubber-modified polystyrene may be used as long as the transparency is not impaired.
- non-rubber-modified styrenic polymers include polystyrene, styrene-high-methylstyrene copolymer, acrylonitrile-styrene copolymer, and styrene (methyl) acrylate.
- the resin composition of the present invention can be produced by any conventionally known compounding method.
- a general kneader such as an open roll, an intensive mixer, an internal mixer, a co-kneader, a continuous kneader with a twin-screw opening and an extruder, and an extruder.
- a melt kneading method, a method of dissolving or dispersing and mixing each component in a solvent, and then removing the solvent by heating are used.
- any additive can be added to the linear block copolymer of the present invention and the resin composition containing the same.
- additives There are no particular restrictions on the type and amount of additives, provided that those commonly used in the formulation of plastics are added in conventional amounts.
- glass fiber Glass beads, silica, calcium carbonate, talc, etc.
- inorganic reinforcing agents organic fibers, organic reinforcing agents such as coumarone-indene resin, organic peroxides, crosslinking agents such as inorganic peroxides, titanium
- examples include pigments, dyes, flame retardants, antioxidants, ultraviolet absorbers, antistatic agents, lubricants, plasticizers, other bulking agents, and mixtures thereof, such as white, black iron, and iron oxide.
- the linear block copolymer and the resin composition of the present invention can be used as they are or colored and molded by the same processing means as ordinary thermoplastic resins, and used for a wide range of applications.
- it can.
- it can be formed by injection molding, blow molding, etc., and can be used for containers of A-components, daily necessities, food, miscellaneous goods, light electric parts and the like.
- extruded products, such as sheets and films are further deep-drawn by methods such as vacuum forming and compressed air forming into food containers, fruits and vegetables and confectionery containers. Therefore, it can be used advantageously for a wide range of applications.
- MFR (gZlOmin) was measured in accordance with JISK-6870.
- the conditions were G conditions (temperature: 200 ° C, load: 5 kg).
- Block rate (% by weight) was calculated by the following equation. Block rate (% by weight)
- the sheet tensile modulus (kgZcm 2 ) in the sheet extrusion direction (machine direction; MD direction) and in the direction perpendicular to the extrusion direction (transverse direction; TD direction). ) was measured and evaluated by the average value (average of the measured values in the MD and TD directions).
- Liquid paraffin was applied to the sheet surface, and the haze value (%) of the sheet was measured according to ASTM D1003. (Incidentally, the smaller the haze value, the higher the transparency.)
- Pneumatic forming pressure forming
- VPF3003 compressed air molding machine
- the cup was obtained from the sheet. Hold the periphery just below the opening of the molding cup (turned-down spout) and instantly squeeze the molding cup in the MD or TD direction.
- Judged. Using six cups, three tests were performed in each of the MD and TD directions.
- a hexane solution containing 8 parts by weight of 1,3-butadiene at a concentration of 25% by weight was added all at once, and the mixture was polymerized at 80 ° C for 15 minutes, and then 1,3-butadiene 9
- Cyclohexane solution containing 25 parts by weight of styrene and 15 parts by weight of styrene at a concentration of 25% by weight was polymerized at 80 ° C while continuously adding over 30 minutes, and then 1,3-butadiene was added.
- a cyclohexane solution containing 8 at a concentration of 25% was added all at once, and polymerization was carried out at 80 ° C for 15 minutes.
- a cyclohexane solution containing 3 parts by weight of styrene at a concentration of 25% by weight was added, and polymerization was performed at 80 ° C. for 5 minutes.
- methanol was added at a 0.4-fold molar amount to n-butyllithium, and the mixture was kept for 5 minutes with stirring.
- 37 parts by weight of styrene was added at a concentration of 25% by weight.
- the resulting cyclohexane solution was added, and polymerized at 80 ° C for 25 minutes.
- methanol was added to the reactor against n-butyllithium in order to completely stop the polymerization.
- the obtained linear block copolymer had a styrene content of 75% by weight and a butadiene content of 25% by weight.
- Table 1 shows that the composition of the linear block copolymer and the styrene-based resin according to the present invention is excellent in rigidity, transparency and impact resistance. Examples 2 to 6, and Comparative Examples 1 to 4
- Example 2 Polymerization was carried out in the same manner as in Example 1 using the amounts of styrene and butadiene shown in Table 1 (weight ratio) to obtain linear block copolymers having the block structures shown in Table 1, respectively.
- the styrene content and the hydrogen content in the linear block copolymer are the weight ratio of butadiene and styrene added, and the peak molecular weight of the linear block copolymer is n —
- the amount of butyllithium (initiator), the timing (timing) and amount of addition of methanol (deactivator), and the block rate are indicated by the BZS block for the linear block copolymer.
- the peak molecular weight of the styrene block is the weight ratio of the S block to the linear block copolymer and the weight ratio of the S block to the metal block.
- the timing was adjusted by changing the position (timing) and amount of addition of the (quenching agent).
- the styrene-n-butyl acrylate copolymer used in Examples 5 and 6 had an n-butyl acrylate content of 14% by weight and an MFR (temperature: 200 °). C, load: 5 kg) was 2.0 g Zl 0 min.
- Block copolymer (a * part) 100 100 100 00 100 100 100 00 100 100 100 100 100 100 100 100 100 100 100 100 100 100 100
- the linear block copolymer of the present invention or a resin composition obtained by blending it with a styrene resin such as polystyrene or styrene-n-butyl acrylate copolymer is molded.
- the resulting molded product has excellent impact resistance and rigidity while maintaining high transparency, so that deep drawn molded products and contents such as frozen dessert cups and beverage cups can be used. It can be used to advantage for vivid food cases, packaging materials, bristles and other applications.
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Description
Claims
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US09/486,989 US6235847B1 (en) | 1998-08-03 | 1999-08-03 | Linear block copolymer and resin composition containing the same |
JP56298899A JP4599495B2 (ja) | 1998-08-03 | 1999-08-03 | 線状ブロック共重合体、及びそれを含む樹脂組成物 |
EP99933229A EP1022296B1 (en) | 1998-08-03 | 1999-08-03 | Linear block copolymer and resin composition containing the same |
DE69941620T DE69941620D1 (de) | 1998-08-03 | 1999-08-03 | Lineares blockcopolymer und harzzusammensetzung die dieses enthält |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
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JP10/218822 | 1998-08-03 | ||
JP21882298 | 1998-08-03 |
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WO2000008079A1 true WO2000008079A1 (fr) | 2000-02-17 |
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PCT/JP1999/004159 WO2000008079A1 (fr) | 1998-08-03 | 1999-08-03 | Copolymere sequence lineaire et composition de resine contenant ledit copolymere |
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US (1) | US6235847B1 (ja) |
EP (1) | EP1022296B1 (ja) |
JP (1) | JP4599495B2 (ja) |
KR (1) | KR100375782B1 (ja) |
CN (1) | CN1177877C (ja) |
DE (1) | DE69941620D1 (ja) |
TW (1) | TW457252B (ja) |
WO (1) | WO2000008079A1 (ja) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
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JPWO2020080202A1 (ja) * | 2018-10-17 | 2021-09-16 | 日本ゼオン株式会社 | 共重合体水素化物およびその製造方法、共重合体水素化物含有組成物、合わせガラス用中間膜、合わせガラス用中間膜積層体、封止材、光学フィルム、医療用成形体およびその製造方法、接着剤、ならびに、接合体およびその製造方法 |
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WO2011040408A1 (ja) * | 2009-09-29 | 2011-04-07 | 電気化学工業株式会社 | 熱収縮性積層フィルム |
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- 1999-08-03 US US09/486,989 patent/US6235847B1/en not_active Expired - Lifetime
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- 1999-08-03 JP JP56298899A patent/JP4599495B2/ja not_active Expired - Fee Related
- 1999-08-03 CN CNB998012416A patent/CN1177877C/zh not_active Expired - Lifetime
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Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7323512B2 (en) * | 2000-06-30 | 2008-01-29 | Asahi Kasei Kabushiki Kaisha | Styrene copolymer composition |
JP2002047387A (ja) * | 2000-08-01 | 2002-02-12 | Asahi Kasei Corp | スチレン系樹脂組成物 |
JP4536226B2 (ja) * | 2000-08-01 | 2010-09-01 | 旭化成ケミカルズ株式会社 | スチレン系樹脂組成物 |
JP2002105154A (ja) * | 2000-10-04 | 2002-04-10 | Asahi Kasei Corp | ブロック共重合体及びその組成物 |
JP2009114308A (ja) * | 2007-11-06 | 2009-05-28 | Asahi Kasei Chemicals Corp | ブロック共重合体組成物又はその水添物の製造方法 |
JP2011041683A (ja) * | 2009-08-21 | 2011-03-03 | Asahi Kasei Chemicals Corp | 人工透析用ダイアライザー本体及びヘッダー用の樹脂組成物、人工透析用ダイアライザー本体及びヘッダー |
JP2011041682A (ja) * | 2009-08-21 | 2011-03-03 | Asahi Kasei Chemicals Corp | 人工透析用ダイアライザー本体及びヘッダー用の樹脂組成物、人工透析用ダイアライザー本体及びヘッダー |
JPWO2020080202A1 (ja) * | 2018-10-17 | 2021-09-16 | 日本ゼオン株式会社 | 共重合体水素化物およびその製造方法、共重合体水素化物含有組成物、合わせガラス用中間膜、合わせガラス用中間膜積層体、封止材、光学フィルム、医療用成形体およびその製造方法、接着剤、ならびに、接合体およびその製造方法 |
US11773193B2 (en) | 2018-10-17 | 2023-10-03 | Zeon Corporation | Hydrogenated copolymer and method of producing the same, hydrogenated copolymer-containing composition, interlayer film for laminated glass, interlayer film laminate for laminated glass, sealing material, optical film, medical shaped article and method of producing the same, adhesive, and assembly and method of producing the same |
JP7388363B2 (ja) | 2018-10-17 | 2023-11-29 | 日本ゼオン株式会社 | 共重合体水素化物およびその製造方法、共重合体水素化物含有組成物、合わせガラス用中間膜、合わせガラス用中間膜積層体、封止材、光学フィルム、医療用成形体およびその製造方法、接着剤、ならびに、接合体およびその製造方法 |
Also Published As
Publication number | Publication date |
---|---|
KR100375782B1 (ko) | 2003-04-03 |
CN1177877C (zh) | 2004-12-01 |
KR20010030777A (ko) | 2001-04-16 |
DE69941620D1 (de) | 2009-12-17 |
TW457252B (en) | 2001-10-01 |
EP1022296A4 (en) | 2001-09-19 |
US6235847B1 (en) | 2001-05-22 |
CN1274374A (zh) | 2000-11-22 |
JP4599495B2 (ja) | 2010-12-15 |
EP1022296A1 (en) | 2000-07-26 |
EP1022296B1 (en) | 2009-11-04 |
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