[go: up one dir, main page]

US20040242787A1 - Process for preparing linear block copolymer - Google Patents

Process for preparing linear block copolymer Download PDF

Info

Publication number
US20040242787A1
US20040242787A1 US10/250,851 US25085103A US2004242787A1 US 20040242787 A1 US20040242787 A1 US 20040242787A1 US 25085103 A US25085103 A US 25085103A US 2004242787 A1 US2004242787 A1 US 2004242787A1
Authority
US
United States
Prior art keywords
lithium
block copolymer
aromatic hydrocarbon
vinyl aromatic
conjugated diene
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Abandoned
Application number
US10/250,851
Other languages
English (en)
Inventor
Moon-Seok Chun
Jae-Chol Cho
Kyu-Seok Sim
Choon-Hwa Lee
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
LG Chem Ltd
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Assigned to LG CHEM, LTD. reassignment LG CHEM, LTD. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: CHO, JAE-CHEOL, CHUN, MOON-SEOK, LEE, CHOON-HWA, SIM, KYU-SEOK
Publication of US20040242787A1 publication Critical patent/US20040242787A1/en
Priority to US11/234,521 priority Critical patent/US7160952B2/en
Abandoned legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F297/00Macromolecular compounds obtained by successively polymerising different monomer systems using a catalyst of the ionic or coordination type without deactivating the intermediate polymer
    • C08F297/02Macromolecular 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
    • C08F297/04Macromolecular 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

Definitions

  • the present invention relates to a linear block copolymer and a process for preparing the same, and particularly to a linear block copolymer in which a conjugated diene/vinyl aromatic hydrocarbon copolymer block is located in a block copolymer and a process for preparing the same.
  • Vinyl aromatic hydrocarbon/conjugated diene block copolymers prepared using organolithium and hydrocarbon solvent differ in their microstructures according to a ratio of vinyl aromatic hydrocarbon and conjugated diene, and processing conditions and physical properties of resultant products also differ.
  • a rubber phase block copolymer having vinyl aromatic hydrocarbon contents of 50% or less is prepared by sequentially polymerizing a vinyl aromatic hydrocarbon and a conjugated diene and then introducing a coupling reactant.
  • WO 95/12644 has disclosed using a halogenous silane compound as a coupling reactant, which can shorten polymerization time and obtain a copolymer having vinyl aromatic hydrocarbon polymer blocks of the same molecular weights, but a lithium compound produced in the coupling reaction as a by-product causes discoloration during processing.
  • a vinyl aromatic hydrocarbon block and a conjugated diene block are sequentially prepared and then the vinyl aromatic hydrocarbon is polymerized again, thereby preparing a linear triblock copolymer.
  • a linear or star block copolymer having vinyl aromatic hydrocarbon contents of 60 ⁇ 80% has superior transparency and impact strength and thus is used for packaging containers, etc.
  • the block copolymer is also used for compensating impact strength of general-purpose polystyrene, and it is preferable to use a block copolymer having vinyl aromatic hydrocarbon contents of 70 ⁇ 80% for improving impact strength of polystyrene and for maintaining transparency.
  • a linear or star copolymer having vinyl aromatic hydrocarbon contents of 20 ⁇ 50% has been blended with general-purpose polystyrene.
  • the linear vinyl aromatic hydrocarbon/conjugated diene block copolymer prepared by sequentially introducing monomers does not generate side reactions such as discoloration during the polymerization process, it is suitable for molded products requiring high transparency, and it has superior dispersibility when blended with other resins and thus is suitable for improving impact resistance of polystyrene and for maintaining transparency.
  • U.S. Pat. No. 6,140,433 has disclosed a block copolymer with polydispersity that can improve impact resistance of other resins by sequentially introducing monomers when preparing a vinyl aromatic hydrocarbon/conjugated diene block copolymer, by introducing an initiator twice and introducing a vinyl aromatic hydrocarbon/conjugated diene copolymer block.
  • this method can easily control physical properties and processibility of a product, it is required that an exact amount of initiator is introduced and that polymerization should proceed at a high temperature. Additionally, the copolymer may lower transparency of the product due to side reactions generated by conducting polymerization at a high temperature.
  • a 1 , A 2 , and A 3 are independently vinyl aromatic hydrocarbon blocks having average molecular weights of 100 ⁇ 100,000,
  • B 1 is a conjugated diene block having an average molecular weight of 100 ⁇ 100,000, and
  • (B/A) is a conjugated diene/vinyl aromatic hydrocarbon copolymer block having an average molecular weight of 100 ⁇ 100,000.)
  • the present invention also provides a process for preparing a linear block copolymer comprising the steps of:
  • step b) simultaneously introducing a vinyl aromatic hydrocarbon and a conjugated diene monomer in the reactor of step a) to polymerize until at least 99% of monomers are consumed;
  • step b) introducing a vinyl aromatic hydrocarbon in the reactor of step b) to polymerize until at least 99% of monomers are consumed.
  • the present inventors while studying a process for improving transparency of a block copolymer, sequentially introduced a vinyl aromatic hydrocarbon, a vinyl aromatic hydrocarbon and a conjugated diene monomer, and a vinyl aromatic hydrocarbon, to polymerize them in the presence of a hydrocarbon solvent and an organolithium compound, and they confirmed superior effects for improving transparency and transmissivity of the block copolymer and completed the present invention.
  • the present invention relates to a block copolymer represented by the following Chemical Formula 1 in which a vinyl aromatic hydrocarbon/conjugated diene copolymer block is introduced into a block copolymer by sequentially introducing a vinyl aromatic hydrocarbon, a vinyl aromatic hydrocarbon and a conjugated diene monomer, and a vinyl aromatic hydrocarbon, to polymerize them in the presence of an organolithium compound and a polymerization initiator.
  • a 1 , A 2 , and A 3 are independently vinyl aromatic hydrocarbon blocks having average molecular weights of 100 ⁇ 100,000,
  • B 1 is a conjugated diene block having an average molecular weight of 100 ⁇ 100,000
  • (B/A) is a conjugated diene/vinyl aromatic hydrocarbon copolymer block having an average molecular weight of 100 ⁇ 100,000.)
  • the ratio of the A 1 block and (A 2 +A 3 ) block of the copolymer is preferably 0.1 ⁇ 10, and the ratio of vinyl aromatic hydrocarbon/conjugated diene monomer in the block copolymer is preferably 25:75 ⁇ 50:50.
  • the block copolymer represented by the above Chemical Formula 1 of the present invention preferably has an average molecular weight of 400 ⁇ 400,000, and it may have a monodispersive or polydispersive molecular weight distribution.
  • the vinyl aromatic hydrocarbon used in the present invention includes styrene, ⁇ -methylstyrene, 2-methylstyrene, 4-methylstyrene, 4-propylstyrene, 1-vinyinaphthalene, 4-cyclohexylstyrene, 4-(p-methylphenyl)styrene, or 1-vinyl-5-hexylnaphthalene, etc., and styrene or methylstyrene is preferable.
  • 1,3-butadiene, 2,3-dimethyl-1,3-butadiene, piperylene, 3-butyl-1,3-octadiene, isoprene, or 2-phenyl-1,3-butadiene, etc. can be used alone or in combination, and preferably 1,3-butadiene or isoprene is used.
  • the organolithium compound plays a function as a polymerization initiator.
  • an alkyl lithium compound can be used, and particularly an alkyl lithium compound having a C 3-10 alkyl group is preferable.
  • Other organolithium compounds can be used in addition to the alkyl lithium compound.
  • organolithium compounds methyl lithium, ethyl lithium, isopropyl lithium, n-butyl lithium, sec-butyl lithium, tert-butyl lithium, n-decyl lithium, tert-octyl lithium, phenyl lithium, 1-naphthyl lithium, n-eicosyl lithium, 4-butylphenyl lithium, 4-tollyl lithium, cyclohexyl lithium, 3,5-di-n-heptylcyclohexyl lithium, or 4-cylcopentyl lithium, etc. can be used, and n-butyl lithium or sec-butyl lithium is preferable.
  • n-pentane, n-hexane, n-heptane, isooctane, cyclohexane, toluene, benzene, or xylene, etc. can be used, and other aromatic hydrocarbons or naphthalene hydrocarbons can be used.
  • n-hexane, cyclohexane or a mixed solution thereof is preferable.
  • polar solvent plays a function for controlling vinyl contents and improving polymerization speed when polymerizing a conjugated diene monomer.
  • polar solvent tetrahydrofuran, ethylether, or tetramethylethylenediamine, etc. can be used, and tetrahydrofuran is preferable.
  • the present invention also provides a process for preparing the above-mentioned linear block copolymer.
  • a vinyl aromatic hydrocarbon is introduced and polymerized until at least 99% of monomers are consumed.
  • the structure of the produced active polymer is A 1 .
  • the vinyl aromatic hydrocarbon and conjugated diene monomer are simultaneously introduced and polymerized until at least 99% of monomers are consumed.
  • the conjugated diene is initially consumed to form the conjugated diene block first, and when most of the conjugated diene is consumed, the vinyl aromatic hydrocarbon begins to be consumed to sequentially form a conjugated diene/vinyl aromatic hydrocarbon copolymer block and a vinyl aromatic hydrocarbon block.
  • the structure of the active polymer produced in the second step is A 1 -B 1 -(B/A)-A 2 .
  • a vinyl aromatic hydrocarbon is introduced and polymerized until at least 99% of monomers are consumed.
  • the structure of the produced active polymer is A 1 -B 1 -(B/A)-A 2 -A 3 .
  • water or alcohol is added to the reactor to arrest activity of the active polymer.
  • the polymerization is preferably conducted at a temperature range of ⁇ 50 ⁇ 150° C. and under a pressure range sufficient for maintaining a reactant liquid phase.
  • the block copolymer prepared according to the present invention has superior transparency, and it also has superior transparency when used as an impact reinforcing agent for other resins or molded products.
  • a block copolymer having styrene weight contents of 40% and comprising a butadiene/styrene copolymer block was prepared as follows.
  • styrene as a vinyl aromatic hydrocarbon were introduced and polymerization was conducted until monomers were completely consumed, and 0.5 g of water was added to the reactor to terminate activity of the active copolymer.
  • the molecular weight of the prepared block copolymer was 68,000 g/mol, and the block styrene contents were 36 wt %.
  • a block copolymer having styrene weight contents of 40% was prepared as follows.
  • styrene 300 g were introduced therein as a vinyl aromatic hydrocarbon to polymerize until the styrene was completely consumed, and 0.5 g of water was added to the reactor to terminate activity of the active copolymer.
  • 7.5 g of Irganox1076 and 15.0 g of TNPP were added to the polymerization solution as an antioxidant to prepare a block copolymer.
  • the molecular weight of the prepared block copolymer was 69,000 g/mol, and the block styrene contents were 39 wt %.
  • Example 1 The block copolymers prepared in Example 1 and Comparative Example 1 were made into samples of 2 mm thickness after removing the solvent, and transmissivity and Haze value were measured and are shown in Table 1. TABLE 1 Transparency Example 1 Comparative Example 1 Transmissivity 89.6 89.6 Haze value 5.6 10.3
  • the block copolymer of Example 1 of the present invention in which vinyl aromatic hydrocarbon/conjugated diene copolymer block was introduced into a block copolymer has a low Haze value and thus superior transparency compared to that of Comparative Example 1.
  • the block copolymer of the present invention can remarkably improve transparency by introducing a vinyl aromatic hydrocarbon/conjugated diene copolymer block into a block copolymer, it can be polymerized at a comparatively low temperature by introducing an initiator once, and it has superior transparency when used for an impact reinforcing agent for other resins or molded products.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Graft Or Block Polymers (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
US10/250,851 2001-11-14 2002-11-14 Process for preparing linear block copolymer Abandoned US20040242787A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US11/234,521 US7160952B2 (en) 2001-11-14 2005-09-23 Process for preparing linear block copolymer

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
KR10-2001-0070840A KR100425243B1 (ko) 2001-11-14 2001-11-14 선형의 블록 공중합체의 제조방법
KR2001-70840 2001-11-14
PCT/KR2002/002129 WO2003042266A1 (en) 2001-11-14 2002-11-14 Process for preparing linear block copolymer

Related Child Applications (1)

Application Number Title Priority Date Filing Date
US11/234,521 Continuation-In-Part US7160952B2 (en) 2001-11-14 2005-09-23 Process for preparing linear block copolymer

Publications (1)

Publication Number Publication Date
US20040242787A1 true US20040242787A1 (en) 2004-12-02

Family

ID=19715975

Family Applications (2)

Application Number Title Priority Date Filing Date
US10/250,851 Abandoned US20040242787A1 (en) 2001-11-14 2002-11-14 Process for preparing linear block copolymer
US11/234,521 Expired - Lifetime US7160952B2 (en) 2001-11-14 2005-09-23 Process for preparing linear block copolymer

Family Applications After (1)

Application Number Title Priority Date Filing Date
US11/234,521 Expired - Lifetime US7160952B2 (en) 2001-11-14 2005-09-23 Process for preparing linear block copolymer

Country Status (9)

Country Link
US (2) US20040242787A1 (no)
EP (1) EP1444280B1 (no)
JP (1) JP2005509066A (no)
KR (1) KR100425243B1 (no)
CN (1) CN100344661C (no)
DE (1) DE60230439D1 (no)
NO (1) NO330460B1 (no)
TW (1) TWI304815B (no)
WO (1) WO2003042266A1 (no)

Cited By (24)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20160311958A1 (en) * 2013-12-06 2016-10-27 Lg Chem, Ltd. Block copolymer
US10081698B2 (en) 2013-12-06 2018-09-25 Lg Chem, Ltd. Block copolymer
US10087276B2 (en) 2013-12-06 2018-10-02 Lg Chem, Ltd. Block copolymer
US10150832B2 (en) 2013-12-06 2018-12-11 Lg Chem, Ltd. Block copolymer
US10160822B2 (en) 2013-12-06 2018-12-25 Lg Chem, Ltd. Monomer and block copolymer
US10184021B2 (en) 2013-12-06 2019-01-22 Lg Chem, Ltd. Block copolymer
US10196475B2 (en) 2013-12-06 2019-02-05 Lg Chem, Ltd. Block copolymer
US10196474B2 (en) 2013-12-06 2019-02-05 Lg Chem, Ltd. Block copolymer
US10202480B2 (en) 2013-12-06 2019-02-12 Lg Chem, Ltd. Block copolymer
US10202481B2 (en) 2013-12-06 2019-02-12 Lg Chem, Ltd. Block copolymer
US10227438B2 (en) 2013-12-06 2019-03-12 Lg Chem, Ltd. Block copolymer
US10227436B2 (en) 2013-12-06 2019-03-12 Lg Chem, Ltd. Block copolymer
US10240035B2 (en) 2014-09-30 2019-03-26 Lg Chem, Ltd. Block copolymer
US10239980B2 (en) 2013-12-06 2019-03-26 Lg Chem, Ltd. Block copolymer
US10253130B2 (en) 2013-12-06 2019-04-09 Lg Chem, Ltd. Block copolymer
US10281820B2 (en) 2014-09-30 2019-05-07 Lg Chem, Ltd. Block copolymer
US10287429B2 (en) 2014-09-30 2019-05-14 Lg Chem, Ltd. Block copolymer
US10287430B2 (en) 2014-09-30 2019-05-14 Lg Chem, Ltd. Method of manufacturing patterned substrate
US10295908B2 (en) 2014-09-30 2019-05-21 Lg Chem, Ltd. Block copolymer
US10310378B2 (en) 2014-09-30 2019-06-04 Lg Chem, Ltd. Block copolymer
US10370529B2 (en) 2014-09-30 2019-08-06 Lg Chem, Ltd. Method of manufacturing patterned substrate
US10377894B2 (en) 2014-09-30 2019-08-13 Lg Chem, Ltd. Block copolymer
US10633533B2 (en) 2014-09-30 2020-04-28 Lg Chem, Ltd. Block copolymer
US10703897B2 (en) 2014-09-30 2020-07-07 Lg Chem, Ltd. Block copolymer

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20040032488A (ko) * 2002-10-10 2004-04-17 금호석유화학 주식회사 3원 블록 공중합체 및 제조방법
KR100961383B1 (ko) 2007-05-31 2010-06-07 주식회사 엘지화학 폴리실록산 말단변성 비닐 방향족 탄화수소-공액디엔 블록공중합체 및 이의 제조방법
JP7105240B2 (ja) * 2017-08-29 2022-07-22 Eneosクレイトンエラストマー株式会社 耐摩耗性に優れた感光性印刷版材用ブロック共重合体及びその製造方法

Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4073831A (en) * 1974-02-02 1978-02-14 Sumitomo Chemical Company, Limited Thermoplastic resin composition
US4075285A (en) * 1974-03-09 1978-02-21 Sumitomo Chemical Company, Limited Rubber-modified polystyrene resin composition
US4089913A (en) * 1974-01-10 1978-05-16 Sumitomo Chemical Company, Limited Process for producing transparent block copolymer resin
US4122134A (en) * 1974-02-13 1978-10-24 Sumitomo Chemical Company, Limited Method for producing transparent block copolymer resin
US4704434A (en) * 1986-03-24 1987-11-03 Phillips Petroleum Company Craze-resistant polymodal linear block copolymers with terminal tapered blocks
US4704435A (en) * 1986-03-24 1987-11-03 Phillips Petroleum Company Craze-resistant polymodal linear block copolymers with resinous terminal blocks
US4939208A (en) * 1986-12-04 1990-07-03 Labofina, S.A. Transparent block copolymers having two monovinyl-substituted aromatic blocks of different molecular weight
US5180535A (en) * 1987-08-17 1993-01-19 Nippon Steel Corporation Injection molding of styrene resin
US6031053A (en) * 1994-06-17 2000-02-29 Basf Aktiengesellschaft Thermoplastic elastomer
US6140433A (en) * 1995-08-04 2000-10-31 China Petrochemical Corporation Thermoplastic elastomeric block copolymers and process for the preparation thereof
US6235847B1 (en) * 1998-08-03 2001-05-22 Asahi Kasei Kabushiki Kaisha Linear block copolymer and resin composition containing the same

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0826107B2 (ja) * 1985-10-17 1996-03-13 新日本製鐵株式会社 高耐衝撃性の熱可塑性樹脂成形物
IT1222429B (it) * 1987-07-31 1990-09-05 Enichem Elastromeri S P A Copolimero a blocchi procedimento per la sua preparazione
JP2612588B2 (ja) 1988-04-04 1997-05-21 日本エラストマー株式会社 アスフアルト改質用熱可塑性エラストマー
USH1581H (en) 1993-11-05 1996-08-06 Shell Oil Company Process for the reduction of diene polymer hot melt adhesive color (II)
US5482674A (en) * 1994-07-07 1996-01-09 Crs Holdings, Inc. Free-machining austenitic stainless steel
DE19806785A1 (de) * 1998-02-18 1999-08-19 Basf Ag Verfahren zur Herstellung von Blockcopolymeren durch retardierten anionischen Polymerisation
JP4070865B2 (ja) * 1998-03-09 2008-04-02 旭化成ケミカルズ株式会社 線状ブロック共重合体及び樹脂組成物
CN1376179A (zh) * 2000-06-30 2002-10-23 旭化成株式会社 苯乙烯共聚物组合物

Patent Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4089913A (en) * 1974-01-10 1978-05-16 Sumitomo Chemical Company, Limited Process for producing transparent block copolymer resin
US4073831A (en) * 1974-02-02 1978-02-14 Sumitomo Chemical Company, Limited Thermoplastic resin composition
US4122134A (en) * 1974-02-13 1978-10-24 Sumitomo Chemical Company, Limited Method for producing transparent block copolymer resin
US4075285A (en) * 1974-03-09 1978-02-21 Sumitomo Chemical Company, Limited Rubber-modified polystyrene resin composition
US4704434A (en) * 1986-03-24 1987-11-03 Phillips Petroleum Company Craze-resistant polymodal linear block copolymers with terminal tapered blocks
US4704435A (en) * 1986-03-24 1987-11-03 Phillips Petroleum Company Craze-resistant polymodal linear block copolymers with resinous terminal blocks
US4939208A (en) * 1986-12-04 1990-07-03 Labofina, S.A. Transparent block copolymers having two monovinyl-substituted aromatic blocks of different molecular weight
US5180535A (en) * 1987-08-17 1993-01-19 Nippon Steel Corporation Injection molding of styrene resin
US6031053A (en) * 1994-06-17 2000-02-29 Basf Aktiengesellschaft Thermoplastic elastomer
US6140433A (en) * 1995-08-04 2000-10-31 China Petrochemical Corporation Thermoplastic elastomeric block copolymers and process for the preparation thereof
US6235847B1 (en) * 1998-08-03 2001-05-22 Asahi Kasei Kabushiki Kaisha Linear block copolymer and resin composition containing the same

Cited By (25)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10227436B2 (en) 2013-12-06 2019-03-12 Lg Chem, Ltd. Block copolymer
US10253130B2 (en) 2013-12-06 2019-04-09 Lg Chem, Ltd. Block copolymer
US10087276B2 (en) 2013-12-06 2018-10-02 Lg Chem, Ltd. Block copolymer
US10150832B2 (en) 2013-12-06 2018-12-11 Lg Chem, Ltd. Block copolymer
US10160822B2 (en) 2013-12-06 2018-12-25 Lg Chem, Ltd. Monomer and block copolymer
US10184021B2 (en) 2013-12-06 2019-01-22 Lg Chem, Ltd. Block copolymer
US10196475B2 (en) 2013-12-06 2019-02-05 Lg Chem, Ltd. Block copolymer
US10196474B2 (en) 2013-12-06 2019-02-05 Lg Chem, Ltd. Block copolymer
US10202480B2 (en) 2013-12-06 2019-02-12 Lg Chem, Ltd. Block copolymer
US10202481B2 (en) 2013-12-06 2019-02-12 Lg Chem, Ltd. Block copolymer
US10227437B2 (en) * 2013-12-06 2019-03-12 Lg Chem, Ltd. Block copolymer
US10227438B2 (en) 2013-12-06 2019-03-12 Lg Chem, Ltd. Block copolymer
US10081698B2 (en) 2013-12-06 2018-09-25 Lg Chem, Ltd. Block copolymer
US10239980B2 (en) 2013-12-06 2019-03-26 Lg Chem, Ltd. Block copolymer
US20160311958A1 (en) * 2013-12-06 2016-10-27 Lg Chem, Ltd. Block copolymer
US10370529B2 (en) 2014-09-30 2019-08-06 Lg Chem, Ltd. Method of manufacturing patterned substrate
US10281820B2 (en) 2014-09-30 2019-05-07 Lg Chem, Ltd. Block copolymer
US10287429B2 (en) 2014-09-30 2019-05-14 Lg Chem, Ltd. Block copolymer
US10287430B2 (en) 2014-09-30 2019-05-14 Lg Chem, Ltd. Method of manufacturing patterned substrate
US10295908B2 (en) 2014-09-30 2019-05-21 Lg Chem, Ltd. Block copolymer
US10310378B2 (en) 2014-09-30 2019-06-04 Lg Chem, Ltd. Block copolymer
US10240035B2 (en) 2014-09-30 2019-03-26 Lg Chem, Ltd. Block copolymer
US10377894B2 (en) 2014-09-30 2019-08-13 Lg Chem, Ltd. Block copolymer
US10633533B2 (en) 2014-09-30 2020-04-28 Lg Chem, Ltd. Block copolymer
US10703897B2 (en) 2014-09-30 2020-07-07 Lg Chem, Ltd. Block copolymer

Also Published As

Publication number Publication date
NO20033086L (no) 2003-07-07
CN1479758A (zh) 2004-03-03
WO2003042266A1 (en) 2003-05-22
KR20030039789A (ko) 2003-05-22
NO330460B1 (no) 2011-04-18
NO20033086D0 (no) 2003-07-07
JP2005509066A (ja) 2005-04-07
EP1444280A1 (en) 2004-08-11
KR100425243B1 (ko) 2004-03-30
US20060217509A1 (en) 2006-09-28
TWI304815B (en) 2009-01-01
TW200407340A (en) 2004-05-16
EP1444280B1 (en) 2008-12-17
CN100344661C (zh) 2007-10-24
DE60230439D1 (de) 2009-01-29
US7160952B2 (en) 2007-01-09

Similar Documents

Publication Publication Date Title
US7160952B2 (en) Process for preparing linear block copolymer
JP4989020B2 (ja) スチレンブタジエンブロック共重合体を基礎とした透明耐衝撃性改良ポリスチレン、これを含む重合体混合物、及びこれらの製造方法
US20060229390A1 (en) Asphalt composition comprising linear diblock copolymer
EP0153727A2 (en) Craze-resistant transparent resinous copolymers
US20040024117A1 (en) Process for preparing high impact vinyl aromatic polymer by continuous anion polymerization method
CA1182237A (en) Method for preparing color-free, stabilized polymers of conjugated dienes or vinyl aromatic hydrocarbons or copolymers of conjugated dienes and vinyl aromatic hydrocarbons
KR100622112B1 (ko) 부타디엔/이소프렌/모노비닐 방향족 모노머 헵타블록공중합체 및 그의 제조방법
US20060160971A1 (en) Method for anionic polymerisation of $g(a)-methylstyrene
EP0135962B1 (en) Process for the preparation of branched polymers
US6777499B2 (en) Multiblock interpolymers and processes for the preparation thereof
WO2005030821A1 (en) Conjugated diene polymers and copolymer blocks having high vinyl content prepared using mixed microstructure control agents and process for preparing same
US6992136B2 (en) Transparent block copolymers and production thereof
EP1266916B1 (en) Multiblock copolymer and the preparing method thereof
JP2003532767A (ja) アニオン重合により形成された耐衝撃性改良ポリスチレン
JP2005538239A (ja) 良好な流動能を有する陰イオン重合された耐衝撃性ポリスチレン
KR100425244B1 (ko) 가공성이 우수한 블록 공중합체와 그의 제조방법, 및 이를포함하는 수지 조성물
KR100536184B1 (ko) 투명도가 우수한 고무상 비닐 방향족 탄화수소-공액디엔공중합체 제조방법
KR100536183B1 (ko) 투명도가 우수한 고무상 비닐 방향족 탄화수소-공액디엔공중합체 제조방법
CN113912798A (zh) 一类基于dpe衍生物、丁二烯、异戊二烯、苯乙烯单体的星形嵌段共聚物及制备方法
CN101012298A (zh) 偶联低乙烯基嵌段共聚物组合物的制造方法和所得组合物
KR20040098856A (ko) 단일비닐기를 갖는 방향족 공중합체의 제조방법

Legal Events

Date Code Title Description
AS Assignment

Owner name: LG CHEM, LTD., KOREA, REPUBLIC OF

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:CHUN, MOON-SEOK;CHO, JAE-CHEOL;SIM, KYU-SEOK;AND OTHERS;REEL/FRAME:015566/0913

Effective date: 20030611

STCB Information on status: application discontinuation

Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION