WO2008020476A1 - Procédé servant à produire un copolymère en blocs et copolymère en blocs ou son produit d'hydrogénation - Google Patents
Procédé servant à produire un copolymère en blocs et copolymère en blocs ou son produit d'hydrogénation Download PDFInfo
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- WO2008020476A1 WO2008020476A1 PCT/JP2006/316109 JP2006316109W WO2008020476A1 WO 2008020476 A1 WO2008020476 A1 WO 2008020476A1 JP 2006316109 W JP2006316109 W JP 2006316109W WO 2008020476 A1 WO2008020476 A1 WO 2008020476A1
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- 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
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- 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
- C08F4/00—Polymerisation catalysts
- C08F4/42—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
- C08F4/44—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides
- C08F4/46—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides selected from alkali metals
- C08F4/48—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides selected from alkali metals selected from lithium, rubidium, caesium or francium
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- 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
- C08F8/00—Chemical modification by after-treatment
- C08F8/04—Reduction, e.g. hydrogenation
Definitions
- Block copolymer production method and block copolymer or hydrogenated product thereof are Block copolymer production method and block copolymer or hydrogenated product thereof
- the present invention relates to a method for producing a block copolymer in which a conjugation monomer and a vinyl aromatic monomer are copolymerized using a lithium initiator, the block copolymer or a hydrogenated product thereof. Concerning additions.
- the production method of the present invention there are a block portion mainly composed of conjugated gen having a high amount of bull bonds, and a block portion composed of a bull aromatic monomer having a narrow molecular weight distribution and a narrow molecular weight distribution.
- a block copolymer can be obtained at a high production rate.
- the amount of bull bonds refers to 1,2-bonds, 3,4-bonds, and 1,2-bonds and conjugated-gen monomers incorporated in 1,4-bonds. 3, 4 — Percentage of what is incorporated in a bond.
- a block copolymer composed of a conjugation monomer and a bull aromatic monomer has elasticity similar to that of vulcanized natural rubber and synthetic rubber at room temperature without vulcanization. In addition, it has the same processability as a thermoplastic resin at high temperatures. For this reason, the block copolymer is widely used in fields such as footwear, plastic modification, asphalt modification, adhesive materials, household products, packaging materials for household appliances, industrial parts, and toys. Further, the hydrogenated product of the block copolymer is excellent in weather resistance and heat resistance. For this reason, the hydrogenated product has been widely put into practical use not only in the above-mentioned fields of application but also in automobile parts and medical devices.
- Patent Document 1 Pamphlet of International Publication No. 00/15681
- Patent Document 2 US Pat. No. 5,654,384
- Patent Document 3 US Pat. No. 5,906,956
- the present invention provides a conjugated gen block portion having a high vinyl bond amount, a narrow molecular weight distribution, a vinyl aromatic block portion, a narrow molecular weight distribution and a high strength.
- An object of the present invention is to provide a production method for obtaining a certain block copolymer at a high production rate, and to provide the block copolymer or a hydrogenated product thereof. Means for solving the problem
- the present invention relates to the following.
- Block copolymerization of conjugation-based monomer and butyl aromatic monomer using lithium initiator and the following substances (1) and (2) must coexist in the polymerization.
- a block copolymer comprising a conjugation monomer and a vinyl aromatic monomer, wherein the vinyl bond content derived from the conjugation monomer is 50% or more, and the block copolymer contains The molecular weight distribution, which is the ratio of the weight average molecular weight and the number average molecular weight of a single peak measured by gel permeation chromatography (GPC), is 30% by weight or more.
- GPC gel permeation chromatography
- the molecular weight distribution which is the ratio of the weight average molecular weight and number average molecular weight of a single peak measured by gel permeation chromatography (GPC), is 1
- a block copolymer or a hydrogenated product thereof characterized in that the molecular weight distribution of a polymer block comprising 2 or less and / or a vinyl aromatic monomer is 1.2 or less
- the production method of the present invention can increase the amount of bull bonds in the conjugated gen block portion in the block copolymer, can narrow the molecular weight distribution of the bull aromatic block portion, and has a narrow and high molecular weight distribution.
- the present invention relates to a production method capable of obtaining a strong block copolymer at a high production rate.
- the production method of the present invention is a method for obtaining a block copolymer comprising a conjugation monomer and a vinyl aromatic monomer at a high production rate.
- the conjugation-based monomer used in the present invention is diolefin having a pair of conjugated double bonds.
- 1,3_butadiene 1,3-butadiene, 2-methyl-1,3-butadiene (isoprene), 2, 3-Dimethyl_1,3-butadiene, 1,3_pentadiene, 2_methyl_1,3_pentadiene, 1,3_hexadiene, etc., particularly preferably 1,3_butadiene.
- examples of the butyl aromatic monomer used in the present invention include, for example, styrene, dimethylolene styrene, p-methylstyrene, dibutylbenzene, 1,1-diphenylethylene, N, N-dimethyl _p —Aminoethylstyrene, N, N-jetyl_p-aminoethylstyrene, and the like. Particularly preferred is styrene, but these may be used alone or in combination of two or more.
- the block copolymer is obtained by anion living polymerization using a lithium initiator in a hydrocarbon solvent.
- the hydrocarbon solvent include aliphatic hydrocarbons such as n-butane, isobutane, n-pentane, n-hexane, n-heptane, and n-octane, cyclohexane, cycloheptane, and methylcycloheptane.
- examples thereof include alicyclic hydrocarbons, and aromatic hydrocarbons such as benzene, toluene, xylene, and ethylbenzene.
- Examples of the lithium initiator include aliphatic and aromatic hydrocarbon lithium compounds having 1 to 20 carbon atoms.
- the lithium compound includes a compound containing one lithium in one molecule, a dilithium compound containing a plurality of lithium in one molecule, a trilithium compound, and a tetralithium compound.
- reaction product of sec_butyllithium, and the reaction product of dibutylbenzene, sec_butyllithium and a small amount of 1,3_butadiene are preferred in terms of polymerization activity.
- the amount of the lithium initiator used depends on the molecular weight of the target block copolymer, but is generally 0.01 to 0.5 phm (parts by weight per 100 parts by weight of the monomer). Preferably, it is from 0.1 to 0.2 phm, and more preferably from 0.02 to 0.15 phm.
- a tertiary amine compound is added when block conjugation of a conjugation monomer and a bull aromatic monomer using a lithium initiator as a polymerization initiator.
- 3rd class Amine compounds include the general formula ⁇ 3 ⁇ 4 3 ⁇ R 2 and R 3 are each a hydrocarbon group having 1 to 20 carbon atoms or a tertiary amino group. ).
- ⁇ , ⁇ , ⁇ ', ⁇ , and -tetramethylethylenediamine are particularly preferred.
- a tertiary amine compound is used to increase the amount of vinyl bonds in the conjugated gen block moiety.
- the amount to be used can be adjusted by the vinyl bond amount of the target conjugation moiety.
- the amount of bull bonds in the conjugated gen block portion targeted in the present application is 50% or more, and the amount of the tertiary amine compound used is preferably 0.1 to 4 (mol / Li) relative to the lithium initiator. It is preferably 0.2 to 3 (mol / Li).
- sodium alkoxide is allowed to coexist during the copolymerization.
- the sodium alkoxide used is a compound represented by the general formula NaOR (wherein R is an alkyl group having 2 to 12 carbon atoms).
- R is an alkyl group having 2 to 12 carbon atoms.
- sodium t-butoxide and sodium t-pentoxide are particularly preferred, with sodium alkoxide having an alkyl group having 3 to 6 carbon atoms being preferred.
- the amount of sodium alkoxide used in the present invention is 0.01 or more and less than 0.1 (molar ratio), preferably 0.01 or more and less than 0.008 (molar ratio) with respect to the tertiary amine compound. ), More preferably 0.03 or more and less than 0.08 (molar ratio), and more preferably 0.04 or more and less than 0.055 (molar ratio).
- a high-strength block copolymer having a conjugated gen block portion having a high amount of bull bonds and a bu aromatic block portion having a narrow molecular weight distribution and a narrow molecular weight distribution can be obtained. It can be obtained at the production rate.
- the block copolymerization method of the conjugation monomer and the vinylol aromatic monomer using the lithium initiator as the polymerization initiator may be batch polymerization, continuous polymerization, or A combination thereof may also be used.
- the batch polymerization method is recommended to obtain a high-strength copolymer with a narrow molecular weight distribution.
- the polymerization temperature is generally 0 ° C ⁇ 15 0 ° C, preferably 30 ° C to 120 ° C, more preferably 50 ° C to 100 ° C.
- the time required for the polymerization varies depending on the conditions, but is usually within 24 hours, particularly preferably from 0.:! To 10 hours.
- the polymerization atmosphere is preferably an inert gas atmosphere such as nitrogen gas.
- the polymerization pressure is not particularly limited as long as it is carried out in a pressure range sufficient to maintain the monomer and solvent in the liquid phase within the above polymerization temperature range.
- care must be taken that impurities that inactivate the initiator and living polymer, such as water, oxygen, carbon dioxide, etc. are not mixed in the polymerization system.
- a coupling reaction can be performed by adding a necessary amount of a bifunctional or higher functional coupling agent at the end of the polymerization.
- Any known bifunctional coupling agent may be used without any particular limitation.
- dihalogen compounds such as dimethyldichlorosilane and dimethyldibutyl silane, dimethyldimethoxysilane, dimethyljetoxysilane, methyl benzoate, ethyl benzoate, phenyl benzoate, phthalate esters, bis And epoxy compounds such as phenol A.
- any known trifunctional or higher polyfunctional coupling agent is not particularly limited.
- trihydric or higher polyalcohols polyepoxy compounds such as epoxidized soybean oil, diglycidyl bisphenol A, etc., general formula R SiX (where R is a hydrocarbon group having 1 to 20 carbon atoms, X is Halogen, n represents an integer of 3 to 4, for example, methylsilyl trichloride, t-butylsilyl trichloride, silicon tetrachloride and bromides thereof, tetramethoxysilane, tetraethoxy An alkoxysilane such as silane, a halogenated tin compound represented by the general formula R_SnX (wherein R is a hydrocarbon group having 1 to 20 carbon atoms, X is a halogen, and n is an integer of 3 to 4),
- polyvalent halogen compounds such as methyltin trichloride, t_butyltin trichloride, tin tetrachlor
- a modifying agent that generates a functional group-containing atomic group can also be subjected to an addition reaction at the living end of the block copolymer obtained by the above-described method.
- the functional group-containing atomic group include a hydroxyl group, a carbonyl group, a thiocarbonyl group, an acid halide group, an acid anhydride group, a carboxynole group, a thiocarboxylate group, an aldehyde group, a thioaldehyde group, and a strong carboxylic acid ester group.
- Examples of the modifying agent having a functional group include tetraglycidylmetaxylenediamine, tetraglycidinole 1,3_bisaminomethylcyclohexane, ⁇ -force prolataton, ⁇ -valerolataton, 4-methoxybenzo Phenone, ⁇ -Glycidchichetiltrimethoxysilane, ⁇ -Grin, Bis ( ⁇ -Glycidoxypropyl) methylpropoxysilane, 1,3-Dimethyl-2-diimidazolidinone, 1,3-Jetyl-2-imidazolid Non, ⁇ , N'-dimethylpropylene urea, ⁇ -methylpyrrolidone and the like.
- the reaction temperature is preferably 0 to 150 ° C, more preferably 20 to 120 ° C.
- the time required for the denaturation reaction varies depending on other conditions, but is preferably within 24 hours, particularly preferably from 0.:! To 10 hours.
- a hydrogenated block copolymer can be obtained by hydrogenating the block copolymer obtained above.
- a hydrogenated block copolymer having a low content of a bull aromatic compound and a high vinyl bond content is effective as an alternative material for a soft chlorinated blu resin as a polypropylene composition.
- hydrogenated block copolymers with a high vinyl aromatic compound content and a high vinyl bond content are, for example, polystyrene, modified poly (phenylene ether) resins, polystyrene, poly (phenylene ether) resins and polypropylene resins. It is extremely effective as a compatibilizing agent.
- Particularly preferred hydrogenation catalysts include titanocene compounds, reducing organometallic compounds, or mixtures of titanocene compounds and reducing organometallic compounds.
- titanocene compound compounds described in JP-A-8-109219 can be used. Specific examples include at least a ligand having a (substituted) cyclopentagenyl skeleton, an indul skeleton, or a fluorenyl skeleton such as biscyclopentaenyl titanium dichloride and monopentamethylcyclopentadienyl titanium trichloride.
- Reducing organometallic compounds include organic alkali metal compounds such as organolithium.
- the hydrogenation reaction is generally carried out in a temperature range of 0 to 200 ° C, more preferably 30 to 150 ° C.
- the hydrogen pressure used in the hydrogenation reaction is recommended to be 0.:! To 15 MPa, preferably 0.2 to: 10 MPa, more preferably 0.3 to 5 MPa.
- the hydrogenation reaction time is usually 3 minutes to 10 hours, preferably 10 minutes to 5 hours.
- the hydrogenation reaction can be carried out as a batch process, a continuous process, or a combination thereof.
- the solution of the block copolymer obtained as described above can remove the catalyst residue, if necessary, and separate the copolymer from the solution.
- Solvent separation methods include, for example, a method in which a polar solvent that is a poor solvent for a copolymer such as acetone or alcohol is added to the reaction solution to precipitate and recover the polymer, and the reaction solution is poured into hot water with stirring.
- a method of removing the solvent by steam stripping and recovering, or a method of directly heating the polymer solution to distill off the solvent can be used.
- the structure of the styrenic block copolymer produced in the present invention can be applied to any structure that is not particularly limited. Examples thereof include those having a structure represented by the following general formula.
- A is a bull aromatic polymer block
- B is a block of a conjugation polymer or a random copolymer of a conjugation monomer and a bull aromatic monomer.
- the boundary of each block does not necessarily need to be clearly distinguished
- n is an integer of 1 or more, preferably an integer of 1 to 5.
- m is an integer of 2 or more, preferably 2 to: 11
- X represents a residue of a coupling agent or a residue of a polyfunctional initiator.
- the weight average molecular weight of the block copolymer obtained in the present invention is recommended to be 50,000 to 500,000, preferably 70,000 to 300,000. Further, the block copolymer has a feature that the molecular weight distribution is narrow.
- the molecular weight distribution of a single peak measured by Gel Permeation Chromatography (GPC) is 1.4 when the bur aromatic content in the block copolymer obtained by batch polymerization is 30% by weight or more. Below, preferably below 1.3 is there.
- the molecular weight distribution of a single peak is 1.2 or less, preferably 1.15 or less, more preferably 1.1 or less. Particularly preferably, it is 1.08 or less.
- the single peak refers to the peak of the remaining polymer that has not undergone the coupling reaction.
- the molecular weight distribution of the polymer comprising the vinyl aromatic compound monomer is 1.2 or less, preferably 1.17 or less.
- the molecular weight of the polymer block consisting of the block copolymer and the bull aromatic compound monomer is the molecular weight of the peak of the chromatogram obtained by measurement by gel permeation chromatography (GPC). It is a weight average molecular weight determined based on a calibration curve (created using the standard molecular weight of standard polystyrene) determined from the measurement of styrene.
- GPC gel permeation chromatography
- the molecular weight distribution of a polymer block composed of a block copolymer and a vinyl aromatic compound monomer can be determined from the measurement by GPC, and is the ratio of the weight average molecular weight to the number average molecular weight.
- the measurement was performed using gas chromatography (manufactured by Shimadzu Corporation, GC-14B).
- the column packing material used was apisong grease, butadiene was 90 ° C.-constant, and styrene was 90 ° to 150 ° C.
- Measurement was performed using an ultraviolet spectrophotometer (manufactured by Shimadzu Corporation, UV-2450).
- the measurement was performed by GPC (the apparatus is manufactured by Waters). Tetrahydrofuran was used as the solvent, and the measurement conditions were a temperature of 40 ° C.
- Commercially known weight average molecular weight and number average molecular weight The weight average molecular weight was calculated
- the molecular weight distribution is the ratio between the weight average molecular weight (Mw) and the number average molecular weight (Mn).
- the block copolymer was decomposed by the tetraacid-aged sumicum acid method described in I. M. Kolthoif, etal., J. Polym. Sci. 1, 429 (1946). Incidentally, osmium acid 0.1 lgZl 25 ml tertiary butanol solution was used for the decomposition. The obtained solution containing a styrene block was measured using GPC in the same manner as in I-4) above.
- the hydrogenated copolymer after hydrogenation was measured with a nuclear magnetic resonance apparatus (device name: DPX-400; manufactured by BRUK ER, Germany).
- the tensile strength was measured according to JIS K6251.
- the tensile speed was 500 mm / min and the measurement temperature was 23 ° C.
- TMEDA n-butyllithium
- NaOAm sodium t-pentoxide
- a cyclohexane solution (concentration 20% by weight) containing 7 parts by weight of styrene was added over 10 minutes, and then polymerized for another 10 minutes (during polymerization, the temperature was controlled at 70 ° C). At this point, the polymer solution was sampled and the polymerization rate of styrene was measured and found to be 100%.
- a cyclohexane solution (concentration 20% by weight) containing 86 parts by weight of butadiene was added over 100 minutes, and then polymerized for another 10 minutes (during polymerization, the temperature was controlled at 70 ° C).
- the polymer solution was sampled and the polymerization rate of butadiene was measured and found to be 100%.
- a cyclohexane solution (concentration 20% by weight) containing 7 parts by weight of styrene was applied for 10 minutes. And then polymerized for another 10 minutes (during polymerization, the temperature was controlled at 70 ° C). At this point, the polymer solution was sampled and the polymerization rate of styrene was measured and found to be 100%.
- the resulting block copolymer had a styrene content of 14.0 wt%, a butadiene bond content of butadiene block of 76.8%, a weight average molecular weight of 188,000 and a molecular weight distribution of 1.06.
- Table 1 shows the analysis results of the obtained copolymer. The molecular weight and molecular weight distribution of the styrene block of the copolymer were measured, and the weight average molecular weight was 1.290,000 and the molecular weight distribution was 1.10.
- the following hydrogenation catalyst was added to the obtained block copolymer as lOOppm as titanium per 100 parts by weight of the block copolymer, and the hydrogenation reaction was carried out at a hydrogen pressure of 0.7 MPa and a temperature of 70 ° C. The Thereafter, methanol was added, and then 0.3 parts by mass of octadecyl-3- (3,5-di-tert-butyl-4-hydroxyphenyl) propionate as a stabilizer was added to 100 parts by mass of the block polymer.
- the hydrogenated copolymer obtained had a hydrogenation rate of 98% and a tensile strength of 124 kgm 2 .
- a reaction vessel purged with nitrogen was charged with 1 liter of dried and purified cyclohexane, and 100 mmol of biscyclopentagenyl titanium dichloride was added. With sufficient stirring, an n-hexane solution containing 200 mmol of trimethylaluminum was added and allowed to react at room temperature for about 3 days.
- a block copolymer was prepared in the same manner as in Example 1. However, the amount of TMEDA added was changed to 2.0 mol, and the amount of NaOAm added was changed to 0.04 mol.
- Table 1 shows the analysis results of the obtained copolymer.
- a block copolymer was prepared in the same manner as in Example 1. However, sodium t-butoxide (hereinafter referred to as NaOBu) was used instead of NaOAm.
- NaOBu sodium t-butoxide
- Table 1 shows the analysis results of the obtained copolymer.
- the resulting hydrogenation ratio of the hydrogenated copolymer is 99% and the tensile strength was m 2 N 122 kg.
- a block copolymer was prepared in the same manner as in Example 1. However, the addition amount of Bu_Li was changed to 0.09 parts by weight, and the addition amount of NaOAm was changed to 0.05 mole.
- Table 1 shows the analysis results of the obtained copolymer.
- a hydrogenated block copolymer was prepared in the same manner as in Example 1 except that a cyclohexane solution containing 5 parts by weight (concentration: 20% by weight) was added and the amount of Bu-Li added was 0.088 parts by weight.
- the resulting hydrogenation ratio of the hydrogenated copolymer is 99% and the tensile strength was m 2 N 378 kg.
- a block copolymer was prepared in the same manner as in Example 1. However, NaOAm was not added.
- Table 1 shows the analysis results of the obtained copolymer.
- the molecular weight and molecular weight distribution of the styrene block of the copolymer were measured and found to be a weight average molecular weight of 0.96 million and a molecular weight distribution of 1.26.
- the obtained copolymer was subjected to a hydrogenation reaction in the same manner as in Example 1 to obtain a hydrogenated copolymer.
- the hydrogenated copolymer obtained had a hydrogenation rate of 98% and a tensile strength of 38 kgm 2 .
- a block copolymer was prepared in the same manner as in Example 1. However, the amount of NaOAm added was changed to 0.12 mol.
- Table 1 shows the analysis results of the obtained copolymer.
- GPC there was a peak in the polymer region, and it was a copolymer with a wide molecular weight distribution.
- a block copolymer was prepared in the same manner as in Example 1. However, the amount of NaOAm added was changed to 0.50 mol.
- Table 1 shows the analysis results of the obtained copolymer. As a result of the GPC measurement, the polymer region had more peaks than in Comparative Example 3, and the copolymer had a wider molecular weight distribution.
- a block having a high bull bond amount, a conjugated gen block portion, and a vinyl aromatic block portion having a narrow molecular weight distribution and a narrow molecular weight distribution and a high strength block It makes it possible to obtain a polymer at a high production rate.
- the block copolymer and its hydrogenated product obtained in the present invention are used in various applications such as packaging materials, automobile parts and medical devices, as well as replacement of soft vinyl chloride resin. Therefore, the present invention that can easily produce the copolymer is extremely useful.
Description
Claims
Priority Applications (10)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP11189378.0A EP2452962B1 (en) | 2006-08-16 | 2006-08-16 | Block copolymer or hydrogenated product thereof |
JP2008529799A JPWO2008020476A1 (ja) | 2006-08-16 | 2006-08-16 | ブロック共重合体の製造方法およびブロック共重合体又はその水素添加物 |
KR1020097002345A KR101050053B1 (ko) | 2006-08-16 | 2006-08-16 | 블록 공중합체의 제조 방법 및 블록 공중합체 또는 그의 수소 첨가물 |
ES11189378.0T ES2623158T3 (es) | 2006-08-16 | 2006-08-16 | Copolímero de bloques o producto hidrogenado del mismo |
ES06796468T ES2401803T3 (es) | 2006-08-16 | 2006-08-16 | Procedimiento para producir copolímero de bloques, y copolímero de bloques o producto hidrogenado del mismo |
CN2006800555422A CN101501090B (zh) | 2006-08-16 | 2006-08-16 | 嵌段共聚物的制造方法及嵌段共聚物或其氢化物 |
EP06796468A EP2058345B1 (en) | 2006-08-16 | 2006-08-16 | Process for producing block copolymer, and block copolymer or hydrogenated product thereof |
US12/310,165 US8138270B2 (en) | 2006-08-16 | 2006-08-16 | Process for producing block copolymer, and block copolymer or hydrogenated product thereof |
PCT/JP2006/316109 WO2008020476A1 (fr) | 2006-08-16 | 2006-08-16 | Procédé servant à produire un copolymère en blocs et copolymère en blocs ou son produit d'hydrogénation |
TW095131593A TW200811207A (en) | 2006-08-16 | 2006-08-28 | Process for producing block copolymer, and block copolymer or hydrogenation product thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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PCT/JP2006/316109 WO2008020476A1 (fr) | 2006-08-16 | 2006-08-16 | Procédé servant à produire un copolymère en blocs et copolymère en blocs ou son produit d'hydrogénation |
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WO2008020476A1 true WO2008020476A1 (fr) | 2008-02-21 |
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PCT/JP2006/316109 WO2008020476A1 (fr) | 2006-08-16 | 2006-08-16 | Procédé servant à produire un copolymère en blocs et copolymère en blocs ou son produit d'hydrogénation |
Country Status (8)
Country | Link |
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US (1) | US8138270B2 (ja) |
EP (2) | EP2452962B1 (ja) |
JP (1) | JPWO2008020476A1 (ja) |
KR (1) | KR101050053B1 (ja) |
CN (1) | CN101501090B (ja) |
ES (2) | ES2623158T3 (ja) |
TW (1) | TW200811207A (ja) |
WO (1) | WO2008020476A1 (ja) |
Cited By (6)
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JP2008045034A (ja) * | 2006-08-16 | 2008-02-28 | Asahi Kasei Chemicals Corp | 新規なブロック共重合体又はその水素添加物 |
CN102317323A (zh) * | 2009-02-18 | 2012-01-11 | 朗盛德国有限责任公司 | 合成高乙烯基二烯橡胶的引发剂体系、用于生产高乙烯基二烯橡胶的方法、及其用于生产高乙烯基二烯橡胶的用途 |
WO2012165120A1 (ja) | 2011-05-27 | 2012-12-06 | 旭化成ケミカルズ株式会社 | 水添共役ジエン系共重合体の製造方法 |
WO2014002984A1 (ja) | 2012-06-26 | 2014-01-03 | 旭化成ケミカルズ株式会社 | 水添ブロック共重合体ペレット、ポリオレフィン系樹脂組成物、及びその成形体 |
JP2016117868A (ja) * | 2014-12-24 | 2016-06-30 | 株式会社クラレ | 重合体の製造方法 |
WO2023249093A1 (ja) * | 2022-06-23 | 2023-12-28 | 株式会社クラレ | 改善された油保持性を有するコポリマーの製造方法 |
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WO2023249093A1 (ja) * | 2022-06-23 | 2023-12-28 | 株式会社クラレ | 改善された油保持性を有するコポリマーの製造方法 |
Also Published As
Publication number | Publication date |
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ES2623158T3 (es) | 2017-07-10 |
US20100016508A1 (en) | 2010-01-21 |
KR101050053B1 (ko) | 2011-07-19 |
TWI343393B (ja) | 2011-06-11 |
TW200811207A (en) | 2008-03-01 |
EP2058345B1 (en) | 2013-02-20 |
EP2452962B1 (en) | 2017-03-22 |
EP2452962A1 (en) | 2012-05-16 |
EP2058345A1 (en) | 2009-05-13 |
ES2401803T3 (es) | 2013-04-24 |
KR20090031933A (ko) | 2009-03-30 |
JPWO2008020476A1 (ja) | 2010-01-07 |
EP2058345A4 (en) | 2009-11-25 |
US8138270B2 (en) | 2012-03-20 |
CN101501090A (zh) | 2009-08-05 |
CN101501090B (zh) | 2011-08-31 |
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