WO2017039189A1 - Copolycarbonate and preparation method therefor - Google Patents

Copolycarbonate and preparation method therefor Download PDF

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Publication number
WO2017039189A1
WO2017039189A1 PCT/KR2016/009043 KR2016009043W WO2017039189A1 WO 2017039189 A1 WO2017039189 A1 WO 2017039189A1 KR 2016009043 W KR2016009043 W KR 2016009043W WO 2017039189 A1 WO2017039189 A1 WO 2017039189A1
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Prior art keywords
copolycarbonate
formula
alkyl
alkylene
substituted
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PCT/KR2016/009043
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French (fr)
Korean (ko)
Inventor
이기재
손영욱
홍무호
반형민
박정준
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주식회사 엘지화학
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Priority claimed from KR1020160019091A external-priority patent/KR101859160B1/en
Application filed by 주식회사 엘지화학 filed Critical 주식회사 엘지화학
Priority to EP16842155.0A priority Critical patent/EP3187523B1/en
Priority to PL16842155T priority patent/PL3187523T3/en
Priority to US15/514,018 priority patent/US10017608B2/en
Priority to CN201680003502.7A priority patent/CN107108877B/en
Priority to JP2017522361A priority patent/JP6464262B2/en
Publication of WO2017039189A1 publication Critical patent/WO2017039189A1/en

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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G64/00Macromolecular compounds obtained by reactions forming a carbonic ester link in the main chain of the macromolecule
    • C08G64/04Aromatic polycarbonates
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G64/00Macromolecular compounds obtained by reactions forming a carbonic ester link in the main chain of the macromolecule
    • C08G64/18Block or graft polymers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G64/00Macromolecular compounds obtained by reactions forming a carbonic ester link in the main chain of the macromolecule
    • C08G64/20General preparatory processes
    • C08G64/30General preparatory processes using carbonates

Definitions

  • the present invention relates to a copolycarbonate having excellent mechanical properties and excellent weather resistance and a method for producing the same.
  • Polycarbonate resin is a polymer material that is used in various fields such as exterior materials, automotive parts, building materials, optical parts, etc. of electrical and electronic products due to its excellent lamella strength, numerical stability, heat resistance and transparency.
  • the present invention is to provide a copolycarbonate having excellent mechanical properties and excellent weather resistance, and a method for producing the same.
  • the present invention provides a copolycarbonate comprising a repeating unit represented by the following formula (1) and a repeating unit represented by the following formula (2) and having a weight average molecular weight of 1,000 to 100, 000 g / mol.
  • the present invention provides a method for producing the copolycarbonate, comprising the step of polymerizing a composition comprising a compound represented by the following formula (3), an aromatic diol compound and a carbonate precursor.
  • the present invention provides a molded article made of the copolycarbonate.
  • a copolycarbonate according to a specific embodiment of the present invention, a manufacturing method thereof, and a molded article will be described in more detail.
  • a copolycarbonate comprising a repeating unit represented by the following Chemical Formula 1 and a repeating unit represented by the following Chemical Formula 2, and having a weight average molecular weight of 1,000 to 10,000 g / mol.
  • Ri to 3 ⁇ 4 are each independently hydrogen or d- 10 alkyl
  • Y is CHO alkylene
  • Z is a bond, -0C0- or -C00-
  • cycloalkylene, 0, S, SO, S0 2, or CO, - Xi to 3 ⁇ 4 are each independently unsubstituted or substituted by a phenyl alkylene, Beach substituted with unsubstituted or alkyl substituted C 3 to
  • R 9 to 2 are each independently hydrogen, d- 10 alkyl, d- ⁇ alkoxy, or halogen,
  • 3 ⁇ 4 is unsubstituted or substituted by phenyl or C- 10 alkylene, unsubstituted or substituted with alkyl or a C 3 -. 15 cycloalkylene, 0, S, SO, S0 2 (or CO in particular, the nose Since polycarbonates contain functional groups linked to Alkyl chains around thio functional groups, polycarbonates can exhibit additional fluidity and weather resistance properties while being excellent in layer resistance, transparency, and heat resistance. have.
  • said Y is d- 5 alkylene.
  • 3 ⁇ 4 to 3 ⁇ 4 are each independently hydrogen or d- 4 alkyl.
  • 3 ⁇ 4 to R 12 are each independently hydrogen, methyl, chloro, or bromo.
  • 3 ⁇ 4 to 3 ⁇ 4 are each independently unsubstituted or substituted with phenyl, straight or branched Cwo alkylene, more preferably methylene, ethane 1,1-diyl, propane-2,2- Diyl, butane-2,2-diyl, 1-phenylethane-1,1-diyl, or diphenylmethylene.
  • 3 ⁇ 4 to 3 ⁇ 4 are cyclonucleic acid -1,1-diyl, 0, S, SO, S0 2 , or CO.
  • the molar ratio of the repeating unit represented by Formula 1 and the repeating unit represented by Formula 2 may be 1: 0.001 to 1: 1, preferably 1: 0.001 to 1: 0.3.
  • the repeating unit represented by the formula (1) is characterized by excellent fluidity and weather resistance
  • the repeating unit represented by the formula (2) is characterized by excellent transparency and impact resistance, which are prepared when including them in the molar ratio Copolycarbonate is preferred because it can exhibit better mechanical properties, fluidity and weather resistance.
  • the copolycarbonate may have a weight average molecular weight of 1,000 to 100,000 g / mol, preferably 10,000 to 100,000 g / mol, more preferably 10,000 to 40,000 g / mol.
  • the copolycarbonate may have a yellowness change amount (dYI) of 20 or less, preferably 1 to 15, and more preferably 3 to 13, based on ASTM G155.
  • dYI yellowness change amount
  • the step of polymerizing a composition comprising a compound represented by the formula (3), an aromatic diol compound and a carbonate precursor; comprising, a method for producing the copolycarbonate may be provided :
  • Ri to 3 ⁇ 4 are each independently hydrogen or Cwo alkyl
  • Y is Cwo alkylene
  • Z is a bond, -0C0- or -coo-
  • Xi to 3 ⁇ 4 is unsubstituted or substituted with d- 10 alkylene, unsubstituted or Cwo alkyl, substituted phenyl C 3 - 15 cycloalkylene, 0, S, SO, S0 2, or CO.
  • aromatic diol compound is a compound represented by the formula (4), and is represented by the formula (2).
  • aromatic diol compound examples include bis (4-hydroxyphenyl) methane, bis (4-hydroxyphenyl) ether, bis (4-hydroxyphenyl) sulfone, bis (4-hydroxyphenyl) sulfoxide, bis (4-hydroxyphenyl) sulfide, bis (4-hydroxyphenyl) ketone, 1, 1-bis (4-hydroxyphenyl) ethane, 2, 2-bis (4-hydroxyphenyl) propane (bisphenol A) , 2,2-bis (4-hydroxyphenyl) butane, 1, 1-bis (4-hydroxyphenyl) cyclonucleic acid (bisphenol Z), 2, 2-bis (4-hydroxy— 3, 5-di Bromophenyl) propane, 2, 2-bis (4-hydroxy-3, 5-dichlorophenyl) propane, 2, 2-bis (4-hydroxy-3-bromophenyl) propane, 2, 2-bis (4-hydroxy-3-chlorophenyl) propane, 2,2-bis ' (4-hydroxy-3-methylphenyl) propane, 2,2-bis (4-hydroxy-3, 5-
  • the .carbonate precursor serves to connect the compound represented by the formula (3) and the compound represented by the formula (4), specific examples thereof phosgene, triphosgene, diphosgene, bromophosgene, dimethyl carbonate, diethyl Carbonate, dibutyl carbonate, dicyclonuclear carbonate diphenyl carbonate, ditoryl carbonate, bis (chlorophenyl) carbonate, m-cresyl carbonate, dinaphthylcarbonate, bis (diphenyl) carbonate or bishaloformate Can be.
  • the compound represented by Formula 3 is 0.1 wt% or more, 1 wt% or more, or 3 wt% or more, 20 wt% or less, 10 wt% or less, based on 100 wt% of the composition, or Up to 7% by weight can be used.
  • the aromatic di compound 40% by weight or more, 50% by weight or more, or 55% by weight or more, or more than 80% by weight, 70% by weight or less, or 65% by weight or less with respect to 100% by weight of the composition. have.
  • the carbonate precursor may be used in an amount of 10 wt% or more, 20 wt% or more, or 30 wt%, 60 wt% or less, 50 wt% or less, or 40 wt% or less, based on 100 wt% of the composition.
  • the polymerization is preferably carried out by interfacial polymerization
  • the polymerization reaction can be carried out at normal pressure and low temperature during the interfacial polymerization and the molecular weight can be easily controlled.
  • the polymerization temperature is 0 ° C to 40 ° C
  • reaction time is preferably 10 minutes to 5 hours.
  • halogenated hydrocarbons such as methylene chloride and chlorobenzene, can be used.
  • the polymerization is preferably carried out in the presence of an acid binder, an alkali metal hydroxide such as sodium hydroxide, potassium hydroxide or an amine compound such as pyridine may be used as the acid binder.
  • an alkali metal hydroxide such as sodium hydroxide, potassium hydroxide or an amine compound such as pyridine may be used as the acid binder.
  • a molecular weight regulator As the molecular weight modifier, d-20 alkylphenol may be used, and specific examples thereof include p-tert-butylphenol, P-cumylphenol, decylphenol, dodecylphenol, tetradecylphenol, nuxadecylphenol, octadecylphenol, and eicosyl. Phenol, docosylphenol, or triacontyl phenol is mentioned.
  • the molecular weight regulator may be added before the start of the polymerization, during the start of the polymerization or after the start of the polymerization.
  • the molecular weight modifier may be used in an amount of 0.01 to 10 parts by weight, preferably 0.1 to 6 parts by weight, based on 100 parts by weight of the aromatic di compound, to obtain a desired molecular weight within this range.
  • tertiary amine compounds such as triethylamine, tetra-n-butylammonium bromide, tetra-n-butylphosphonium bromide, quaternary ammonium compounds, and quaternary phosphonium compounds Accelerators may additionally be used.
  • a molded article made of the copolycarbonate may be provided.
  • the copolycarbonate including the repeating unit represented by Chemical Formula 1 has excellent mechanical properties, and also has improved weather resistance, and thus has a wide field of use as compared to a molded article made of copolycarbonate.
  • the molded article may be one or more selected from the group consisting of antioxidants, plasticizers, antistatic agents, nucleating agents, flame retardants, lubricants, layer enhancers, fluorescent brighteners, ultraviolet absorbers, pigments and dyes, if necessary, in addition to copolycarbonates according to the present invention. It may further include.
  • the copolycarbonate and other additives according to the present invention are well mixed by using a mixer, and then extruded into an extruder to produce pellets, and the pellets are dried and then injected into an injection molding machine. It may include a step.
  • FIG. 1 is a graph of the working curve of the compound prepared in Example 1.
  • Figure 2 is a 1 "NMR graph of the copolycarbonate prepared in Example 1. [Effect of the invention]
  • a copolycarbonate having excellent mechanical properties and excellent weather resistance and a method of manufacturing the same can be provided.
  • 2L main reactor equipped with a nitrogen purge and a condenser and capable of maintaining a room temperature with a circulator, 620g of water, 116.24g of BPA, bis- (4- (2- (4-hy dr) Oxypheny 1) propan-2-yl) phenyl) 3, 0.6 g of 3'-thiodi proionate, 102.5 g of NaOH, and 200 ml of MeCl 2 were added and stirred for several minutes.
  • the produced polycarbonate had a weight average molecular weight of 31,000 g / mol.
  • a polycarbonate was prepared in the same manner as in Example 1 except for changing to 5.8 g.
  • Example 4
  • Example 6 Polycarbonate was prepared in the same manner as in Example 1, except that the amount of PTBP was changed to 3.41 g. Comparative Example 1
  • MI Flowability
  • the copolycarbonate prepared in Example 1 shows not only the level of laminar strength equivalent to that of Comparative Example 1, which is a general polycarbonate, but also very excellent flowability.
  • the copolycarbonate of this embodiment is very excellent in weatherability, which is a property that withstands various climates while maintaining the inherent properties of polycarbonate resin, it is easy to apply to various fields such as exterior materials, automotive parts, building materials of electrical and electronic products.

Abstract

Provided are: a copolycarbonate, which comprises a repeating unit represented by chemical formula 1 and a repeating unit represented by chemical formula 2, and has a weight average molecular weight of 1,000 to 100,000 g/mol; and a preparation method therefor. The copolycarbonate has an excellent mechanical property and weather resistance.

Description

【명세서】  【Specification】
【발명의 명칭】  [Name of invention]
코폴리카보네이트 및 이의 제조방법 【기술분야】  Copolycarbonate and its manufacturing method
관련 출원 (들)과의 상호 인용  Cross Citation with Related Application (s)
본 출원은 2015 년 9 월 1 일자 한국 특허 출원 제 10-2015-0123707 호 및 2016 년 2 월 18 일자 한국 특허 출원 제 10-2016-0019091 호에 기초한 우선권의 이익올 주장하며, 해당 한국 특허 출원들의 문헌에 개시된 모든 내용은 본 명세서의 일부로서 포함된다.  This application claims the benefit of priority based on Korean Patent Application No. 10-2015-0123707 dated September 1, 2015 and Korean Patent Application No. 10-2016-0019091 dated February 18, 2016. All content disclosed in the literature is included as part of this specification.
본 발명은 기계적 물성이 우수하면서도, 내후성 또한 뛰어난 코폴리카보네이트와 이의 제조방법에 관한 것이다.  The present invention relates to a copolycarbonate having excellent mechanical properties and excellent weather resistance and a method for producing the same.
【발명의 배경이 되는 기술】 [Technique to become background of invention]
폴리카보네이트 수지는 우수한 층격강도, 수치안정성, 내열성 및 투명성 등의 물성으로 인하여 전기전자 제품의 외장재, 자동차 부품, 건축 소재, 광학 부품 등의 분야에 다양하게 사용되고 있는 고분자소재이다,  Polycarbonate resin is a polymer material that is used in various fields such as exterior materials, automotive parts, building materials, optical parts, etc. of electrical and electronic products due to its excellent lamella strength, numerical stability, heat resistance and transparency.
이러한 폴리카보네이트 수지는 최근 응용 분야가 확대됨에 따라, 폴리카보네이트 수지 고유의 물성은 유지하면서도 내열성과 내후성 등이 향상된 신규한 구조의 코폴리카보네이트의 개발이 요구되고 있다 .  As the polycarbonate resin is recently expanded in application fields, it is required to develop a novel copolycarbonate having improved heat resistance and weather resistance while maintaining the inherent properties of the polycarbonate resin.
이에 따라, 2 종 이상의 서로 다른 구조의 방향족 디올을 공중합하여 구조가 다른 단위체를 폴리카보네이트의 주쇄에 도입하여 원하는 물성을 얻고자 하는 연구가 시도되고 있다. 그러나, 대부분의 기술들이 생산단가가 높고, 내화학성이나 충격강도 등이 증가하면 반대로 투명성이 저하되고, 투명성이 향상되면 내화학성이나 층격강도 등이 저하되는 등의 한계가 있다. 이에, 경도 등의 기계적 물성이 우수하면서도 내후성 또한 뛰어난 신규한 구조의 코폴리카보네이트에 대한 연구 개발이 여전히 필요하다 .  Accordingly, studies have been attempted to obtain desired physical properties by copolymerizing two or more kinds of aromatic diols having different structures to introduce units having different structures into the main chain of polycarbonate. However, most of the technologies have high production costs, and if the chemical resistance or impact strength is increased, the transparency is lowered. If the transparency is improved, the chemical resistance or the laminar strength is lowered. Therefore, there is still a need for research and development on a novel copolycarbonate having excellent mechanical properties such as hardness and excellent weatherability.
【발명의 내용】 [Content of invention]
【해결하고자 하는 과제】 본 발명은, 기계적 물성이 우수하면서도, 내후성 또한 뛰어난 코폴리카보네이트와, 이의 제조방법을 제공하기 위한 것이다. Problem to be solved The present invention is to provide a copolycarbonate having excellent mechanical properties and excellent weather resistance, and a method for producing the same.
【과제의 해결 수단】 [Measures of problem]
본 발명은, 하기 화학식 1 로 표시되는 반복 단위 및 하기 화학식 2 로 표시되는 반복 단위를 포함하고, 중량 평균 분자량이 1 , 000 내지 100 , 000 g/mol인, 코폴리카보네이트를 제공한다.  The present invention provides a copolycarbonate comprising a repeating unit represented by the following formula (1) and a repeating unit represented by the following formula (2) and having a weight average molecular weight of 1,000 to 100, 000 g / mol.
또한, 본 발명은 하기 화학식 3 으로 표시되는 화합물, 방향족 디올 화합물 및 카보네이트 전구체를 포함하는 조성물을 중합하는 단계;를 포함하는, 상기 코폴리카보네이트의 제조 방법을 제공한다.  In addition, the present invention provides a method for producing the copolycarbonate, comprising the step of polymerizing a composition comprising a compound represented by the following formula (3), an aromatic diol compound and a carbonate precursor.
또, 본 발명은 상기 코폴리카보네이트로 제조되는 성형품을 제공한다. 이하 발명의 구체적인 구현예에 따른 코폴리카보네이트, 이의 제조 방법 및 성형품에 관하여 보다 상세하게 설명하기로 한다. 발명의 일 구현예에 따르면, 하기 화학식 1 로 표시되는 반복 단위 및 하기 화학식 2 로 표시되는 반복 단위를 포함하고, 중량 평균 분자량이 1 , 000 내지 100 , 000 g/mol인, 코폴리카보네이트가 제공될 수 있다:  In addition, the present invention provides a molded article made of the copolycarbonate. Hereinafter, a copolycarbonate according to a specific embodiment of the present invention, a manufacturing method thereof, and a molded article will be described in more detail. According to an embodiment of the present invention, a copolycarbonate is provided, comprising a repeating unit represented by the following Chemical Formula 1 and a repeating unit represented by the following Chemical Formula 2, and having a weight average molecular weight of 1,000 to 10,000 g / mol. Can be:
Figure imgf000003_0001
Figure imgf000003_0001
상기 화학식 1에서,  In Chemical Formula 1,
Ri 내지 ¾는 각각 독립적으로 수소 또는 d-10알킬이고, Ri to ¾ are each independently hydrogen or d- 10 alkyl,
Y는 CHO 알킬렌이고,  Y is CHO alkylene,
Z는 결합, -0C0- 또는 -C00-이고,  Z is a bond, -0C0- or -C00-,
Xi 내지 ¾는 각각 독립적으로 비치환되거나 또는 페닐로 치환된 알킬렌, 비치환되거나 또는 알킬로 치환된 C3-15 사이클로알킬렌, 0, S , SO , S02 , 또는 CO이고, And 15 cycloalkylene, 0, S, SO, S0 2, or CO, - Xi to ¾ are each independently unsubstituted or substituted by a phenyl alkylene, Beach substituted with unsubstituted or alkyl substituted C 3 to
[화학식 2] [Formula 2]
Figure imgf000004_0001
Figure imgf000004_0001
상기 화학식 2에서,  In Chemical Formula 2,
R9 내지 2 는 각각 독립적으로 수소, d-10 알킬, d-ω 알콕시, 또는 할로겐이고, R 9 to 2 are each independently hydrogen, d- 10 alkyl, d-ω alkoxy, or halogen,
¾ 는 비치환되거나 또는 페닐로 치환된 C-10 알킬렌, 비치환되거나 또는에 알킬로 치환된 C3-15사이클로알킬렌, 0, S, SO, S02( 또는 CO이다. 특히, 상기 코폴리카보네이트는 Thio 작용기를 중심으로 Alkyl chain 이 연결된 작용기를 포함하기 때문에, 기존의 폴리카보네이트가 갖는 고유한 특성인 내층격성, 투명성, 내열성 등이 우수하면서도, 우수한 유동성 및 내후성 특성 등을 추가로 나타낼 수 있다. ¾ is unsubstituted or substituted by phenyl or C- 10 alkylene, unsubstituted or substituted with alkyl or a C 3 -. 15 cycloalkylene, 0, S, SO, S0 2 (or CO in particular, the nose Since polycarbonates contain functional groups linked to Alkyl chains around thio functional groups, polycarbonates can exhibit additional fluidity and weather resistance properties while being excellent in layer resistance, transparency, and heat resistance. have.
이 때, 상기 Y는 d-5 알킬렌인 것이 바람직하다. At this time, it is preferable that said Y is d- 5 alkylene.
또한 상기 ¾ 내지 ¾ 는 각각 독립적으로, 수소, 또는 d-4 알킬인 것이 바람직하다. In addition, it is preferable that ¾ to ¾ are each independently hydrogen or d- 4 alkyl.
그리고, 상기 ¾ 내지 R12는 각각 독립적으로 수소, 메틸, 클로로, 또는 브로모이다. 또한 바람직하게는, ¾ 내지 ¾는 각각 독립적으로 비치환되거나 또는 페닐로 치환된 직쇄 또는 분지쇄의 Cwo 알킬렌이며, 보다 바람직하게는 메틸렌, 에탄ᅳ1,1-디일, 프로판 -2 ,2-디일, 부탄 -2 ,2-디일, 1-페닐에탄 -1,1- 디일, 또는 디페닐메틸렌이다. 또한 바람직하게는, ¾ 내지 ¾ 는 사이클로핵산 -1,1-디일, 0, S, SO, S02, 또는 CO이다. And ¾ to R 12 are each independently hydrogen, methyl, chloro, or bromo. Also preferably, ¾ to ¾ are each independently unsubstituted or substituted with phenyl, straight or branched Cwo alkylene, more preferably methylene, ethane 1,1-diyl, propane-2,2- Diyl, butane-2,2-diyl, 1-phenylethane-1,1-diyl, or diphenylmethylene. Also preferably, ¾ to ¾ are cyclonucleic acid -1,1-diyl, 0, S, SO, S0 2 , or CO.
또, 상기 화학식 1 로 표시되는 반복 단위와, 화학식 2 로 표시되는 반복 단위의 몰 비는 1:0.001 내지 1:1, 바람직하게는 1:0.001 내지 1:0.3 일 수 있다.  In addition, the molar ratio of the repeating unit represented by Formula 1 and the repeating unit represented by Formula 2 may be 1: 0.001 to 1: 1, preferably 1: 0.001 to 1: 0.3.
상기 화학식 1 로 표시되는 반복 단위는 유동성, 및 내후성이 우수한 특징이 있고, 화학식 2 로 표시되는 반복 단위는 투명성과 내충격성이 우수한 특징이 있는데, 이들을 상기 몰 비율로 포함하였을 때, 제조되는 코폴리카보네이트가 보다 우수한 기계적 물성, 유동성 및 내후성을 나타낼 수 있어 바람직하다 . The repeating unit represented by the formula (1) is characterized by excellent fluidity and weather resistance, the repeating unit represented by the formula (2) is characterized by excellent transparency and impact resistance, which are prepared when including them in the molar ratio Copolycarbonate is preferred because it can exhibit better mechanical properties, fluidity and weather resistance.
또, 상기 코폴리카보네이트는 중량평균 분자량이 1,000 내지 100,000 g/mol, 바람직하게는 10,000 내지 100,000 g/mol, 보다 바람직하게는 10,000 내지 40,000 g/mol일 수 있다.  In addition, the copolycarbonate may have a weight average molecular weight of 1,000 to 100,000 g / mol, preferably 10,000 to 100,000 g / mol, more preferably 10,000 to 40,000 g / mol.
또한, 상기 코폴리카보네이트는 ASTM G155 에 의거하여 측정한 황색도 변화량 (dYI)이 20 이하, 바람직하게는 1 내지 15, 더욱 바람직하게는 3 내지 13일 수 있다. 한편, 발명의 또 다른 구현예에 따르면, 하기 화학식 3 으로 표시되는 화합물, 방향족 디올 화합물 및 카보네이트 전구체를 포함하는 조성물을 중합하는 단계 ;를 포함하는, 상기 코폴리카보네이트의 제조 방법이 제공될 수 있다:  In addition, the copolycarbonate may have a yellowness change amount (dYI) of 20 or less, preferably 1 to 15, and more preferably 3 to 13, based on ASTM G155. On the other hand, according to another embodiment of the invention, comprising the step of polymerizing a composition comprising a compound represented by the formula (3), an aromatic diol compound and a carbonate precursor; comprising, a method for producing the copolycarbonate may be provided :
[화학식 3]  [Formula 3]
Figure imgf000005_0001
Figure imgf000005_0001
상기 화학식 3에서,  In Chemical Formula 3,
Ri 내지 ¾는 각각 독립적으로 수소 또는 Cwo알킬이고,  Ri to ¾ are each independently hydrogen or Cwo alkyl,
Y는 Cwo 알킬렌이고,  Y is Cwo alkylene,
Z는 결합, -0C0- 또는 -coo-이고,  Z is a bond, -0C0- or -coo-,
Xi 내지 ¾ 는 비치환되거나 또는 페닐로 치환된 d-10 알킬렌, 비치환되거나 또는 Cwo 알킬로 치환된 C3-15 사이클로알킬렌, 0, S, SO, S02, 또는 CO이다. Xi to ¾ is unsubstituted or substituted with d- 10 alkylene, unsubstituted or Cwo alkyl, substituted phenyl C 3 - 15 cycloalkylene, 0, S, SO, S0 2, or CO.
그리고, 상기 방향족 디올 화합물은 화학식 4 로 표시되는 화합물로서, 상기 화학식 2에 대웅된다.  In addition, the aromatic diol compound is a compound represented by the formula (4), and is represented by the formula (2).
[화학식 4]
Figure imgf000006_0001
[Formula 4]
Figure imgf000006_0001
상기 화학식 4 에서, X3 및 R9 내지 R12는 상기 화학식 2 에서 정의한 바와 같다. In Chemical Formula 4, X 3 and R 9 to R 12 are as defined in Chemical Formula 2.
상기 방향족 디올 화합물의 구체적인 예로, 비스 (4-히드록시페닐)메탄, 비스 (4-히드록시페닐)에테르, 비스 (4-히드록시페닐)설폰, 비스 (4- 히드록시페닐)설폭사이드, 비스 (4-히드록시페닐)설파이드, 비스 (4- 히드록시페닐)케톤, 1 , 1-비스 (4-히드록시페닐)에탄, 2, 2-비스 (4- 히드록시페닐)프로판 (비스페놀 A) , 2,2-비스 (4-히드록시페닐)부탄, 1 , 1- 비스 (4-히드록시페닐)시클로핵산 (비스페놀 Z) , 2 , 2-비스 (4-히드록시— 3 , 5- 디브로모페닐)프로판, 2 , 2-비스 (4-히드록시 -3 , 5-디클로로페닐)프로판, 2 , 2- 비스 (4-히드록시 -3-브로모페닐)프로판, 2, 2-비스 (4-히드록시 -3- 클로로페닐)프로판, 2 , 2-비스' (4-히드록시 -3-메틸페닐)프로판, 2,2-비스 (4- 히드록시 -3 , 5-디메틸페닐)프로판 및 1,1-비스 (4-히드록시페닐 )-1-페닐에탄으로 이루어진 군으로부터 선택된 1종 이상의 화합물을 포함할 수 있다. Specific examples of the aromatic diol compound include bis (4-hydroxyphenyl) methane, bis (4-hydroxyphenyl) ether, bis (4-hydroxyphenyl) sulfone, bis (4-hydroxyphenyl) sulfoxide, bis (4-hydroxyphenyl) sulfide, bis (4-hydroxyphenyl) ketone, 1, 1-bis (4-hydroxyphenyl) ethane, 2, 2-bis (4-hydroxyphenyl) propane (bisphenol A) , 2,2-bis (4-hydroxyphenyl) butane, 1, 1-bis (4-hydroxyphenyl) cyclonucleic acid (bisphenol Z), 2, 2-bis (4-hydroxy— 3, 5-di Bromophenyl) propane, 2, 2-bis (4-hydroxy-3, 5-dichlorophenyl) propane, 2, 2-bis (4-hydroxy-3-bromophenyl) propane, 2, 2-bis (4-hydroxy-3-chlorophenyl) propane, 2,2-bis ' (4-hydroxy-3-methylphenyl) propane, 2,2-bis (4-hydroxy-3, 5-dimethylphenyl) propane And 1,1-bis (4-hydroxyphenyl) -1-phenylethane From may comprise at least one compound selected.
또한, 상기 .카보네이트 전구체는 상기 화학식 3 으로 표시되는 화합물 및 상기 화학식 4 로 표시되는 화합물을 연결하는 역할을 하는 것으로, 이의 구체적인 예로 포스겐, 트리포스겐, 디포스겐, 브로모포스겐, 디메틸 카보네이트, 디에틸 카보네이트, 디부틸 카보네이트, 디시클로핵실 카보네이트 디페닐 카보네이트, 디토릴 카보네이트, 비스 (클로로페닐) 카보네이트, m- 크레실 카보네이트, 디나프틸카보네이트, 비스 (디페닐) 카보네이트 또는 비스할로포르메이트를 들 수 있다.  In addition, the .carbonate precursor serves to connect the compound represented by the formula (3) and the compound represented by the formula (4), specific examples thereof phosgene, triphosgene, diphosgene, bromophosgene, dimethyl carbonate, diethyl Carbonate, dibutyl carbonate, dicyclonuclear carbonate diphenyl carbonate, ditoryl carbonate, bis (chlorophenyl) carbonate, m-cresyl carbonate, dinaphthylcarbonate, bis (diphenyl) carbonate or bishaloformate Can be.
상기 중합시, 상기 화학식 3 으로 표시되는 화합물은, 상기 조성물 100 중량 %에 대해 0. 1 중량 % 이상, 1 중량 % 이상, 또는 3 중량 % 이상이고, 20 중량 % 이하, 10 중량 % 이하, 또는 7 중량 % 이하를 사용할 수 있다. 또한, 상기 방향족 디을 화합물은, 상기 조성물 100 중량 %에 대해 40 중량 % 이상, 50 중량 % 이상, 또는 55 중량 ¾> 이상이고, 80 중량 이하, 70 중량 ¾ 이하, 또는 65 중량 % 이하로 사용할 수 있다. In the polymerization, the compound represented by Formula 3 is 0.1 wt% or more, 1 wt% or more, or 3 wt% or more, 20 wt% or less, 10 wt% or less, based on 100 wt% of the composition, or Up to 7% by weight can be used. In addition, the aromatic di compound, 40% by weight or more, 50% by weight or more, or 55% by weight or more, or more than 80% by weight, 70% by weight or less, or 65% by weight or less with respect to 100% by weight of the composition. have.
또한, 상기 카보네이트 전구체는, 상기 조성물 100 중량 %에 대해 10 중량 % 이상, 20 중량 % 이상, 또는 30 중량 %이고, 60 증량 % 이하 50 중량 % 이하, 또는 40 중량 % 이하로 사용할 수 있다.  The carbonate precursor may be used in an amount of 10 wt% or more, 20 wt% or more, or 30 wt%, 60 wt% or less, 50 wt% or less, or 40 wt% or less, based on 100 wt% of the composition.
이 때 , 상기 중합은 계면 중합으로 수행하는 것이 바람직하며, 계면 중합시 상압과 낮은 온도에서 중합 반웅이 가능하며 분자량 조절이 용이하다. 상기 중합 온도는 0°C 내지 40°C , 반웅 시간은 10 분 내지 5 시간이 바람직하다. 또한, 반웅 중 pH 는 9 이상 또는 11 이상으로 유지하는 것이 바람직하다. At this time, the polymerization is preferably carried out by interfacial polymerization, the polymerization reaction can be carried out at normal pressure and low temperature during the interfacial polymerization and the molecular weight can be easily controlled. The polymerization temperature is 0 ° C to 40 ° C, reaction time is preferably 10 minutes to 5 hours. In addition, it is preferable to keep pH in reaction of 9 or more or 11 or more.
상기 중합에 사용할 수 있는 용매로는, 당업계에서 코폴리카보네이트의 중합에 사용되는 용매이면 특별히 제한되지 않으며 , 일례로 메틸렌클로라이드, 클로로벤젠 등의 할로겐화 탄화수소를 사용할 수 있다.  As a solvent which can be used for the said superposition | polymerization, if it is a solvent used for superposition | polymerization of copolycarbonate in the art, it will not specifically limit, For example, halogenated hydrocarbons, such as methylene chloride and chlorobenzene, can be used.
또한, 상기 중합은 산결합제의 존재 하에 수행하는 것이 바람직하며, 상기 산결합제로 수산화나트륨, 수산화칼륨 등의 알칼리금속 수산화물 또는 피리딘 등의 아민 화합물을 사용할 수 있다.  In addition, the polymerization is preferably carried out in the presence of an acid binder, an alkali metal hydroxide such as sodium hydroxide, potassium hydroxide or an amine compound such as pyridine may be used as the acid binder.
또한, 상기 중합시 코폴리카보네이트의 분자량 조절을 위하여, 분자량 조절제의 존재 하에 중합하는 것이 바람직하다. 상기 분자량 조절제로 d-20 알킬페놀을 사용할 수 있으며, 이의 구체적인 예로 p-tert-부틸페놀, P- 쿠밀페놀, 데실페놀, 도데실페놀, 테트라데실페놀, 핵사데실페놀, 옥타데실페놀, 에이코실페놀, 도코실페놀 또는 트리아콘틸페놀을 들 수 있다. 상기 분자량 조절제는, 중합 개시 전, 중합 개시 중 또는 중합 개시 후에 투입될 수 있다. 상기 분자량 조절제는 상기 방향족 디을 화합물 100 중량부 대비 0.01 내지 10 중량부, 바람직하게는 0.1 내지 6 중량부를 사용할 수 있으며, 이 범위 내에서 원하는 분자량올 얻을 수 있다.  In addition, to control the molecular weight of the copolycarbonate during the polymerization, it is preferable to polymerize in the presence of a molecular weight regulator. As the molecular weight modifier, d-20 alkylphenol may be used, and specific examples thereof include p-tert-butylphenol, P-cumylphenol, decylphenol, dodecylphenol, tetradecylphenol, nuxadecylphenol, octadecylphenol, and eicosyl. Phenol, docosylphenol, or triacontyl phenol is mentioned. The molecular weight regulator may be added before the start of the polymerization, during the start of the polymerization or after the start of the polymerization. The molecular weight modifier may be used in an amount of 0.01 to 10 parts by weight, preferably 0.1 to 6 parts by weight, based on 100 parts by weight of the aromatic di compound, to obtain a desired molecular weight within this range.
또한, 상기 중합 반웅의 촉진을 위하여, 트리에틸아민, 테트라 -n- 부틸암모늄브로마이드, 테트라 -n-부틸포스포늄브로마이드 등의 3 차 아민 화합물, 4 차 암모늄 화합물, 4 차 포스포늄 화합물 등과 같은 반웅 촉진제를 추가로 사용할 수 있다. 발명의 또 다른 구현예에 따르면, 상기 코폴리카보네이트로 제조되는 성형품이 제공될 수 있다. 앞서 설명한 바와 같이, 상기 화학식 1로 표시되는 반복 단위를 포함하는 코폴리카보네이트는 기계적 물성이 우수하면서도, 내후성 또한 향상되어 기존에 사용되던 코폴리카보네이트로 제조되는 성형품에 비하여 웅용 분야가 넓다. Also, in order to promote the polymerization reaction, reactions such as tertiary amine compounds such as triethylamine, tetra-n-butylammonium bromide, tetra-n-butylphosphonium bromide, quaternary ammonium compounds, and quaternary phosphonium compounds Accelerators may additionally be used. According to another embodiment of the invention, a molded article made of the copolycarbonate may be provided. As described above, the copolycarbonate including the repeating unit represented by Chemical Formula 1 has excellent mechanical properties, and also has improved weather resistance, and thus has a wide field of use as compared to a molded article made of copolycarbonate.
상기 성형품은 본 발명에 따른 코폴리카보네이트 외에, 필요에 따라 산화방지제, 가소제, 대전방지제, 핵제, 난연제, 활제, 층격보강제, 형광증백제, 자외선흡수제, 안료 및 염료로 이루어진 군으로부터 선택된 1종 이상을 추가로 포함할 수 있다.  The molded article may be one or more selected from the group consisting of antioxidants, plasticizers, antistatic agents, nucleating agents, flame retardants, lubricants, layer enhancers, fluorescent brighteners, ultraviolet absorbers, pigments and dyes, if necessary, in addition to copolycarbonates according to the present invention. It may further include.
상기 성형품의 제조 방법의 일례로, 본 발명에 따른 코폴리카보네이트와 기타 첨가제를 믹서를 이용하여 잘 흔합한 후에, 압출기로 압출 성형하여 펠릿으로 제조하고, 상기 펠릿을 건조시킨 다음 사출 성형기로 사출하는 단계를 포함할 수 있다.  As an example of the method for producing the molded article, the copolycarbonate and other additives according to the present invention are well mixed by using a mixer, and then extruded into an extruder to produce pellets, and the pellets are dried and then injected into an injection molding machine. It may include a step.
【도면의 간단한 설명】 [Brief Description of Drawings]
도 1은 실시예 1에서 제조한 화합물의 工^ 그래프이다.  1 is a graph of the working curve of the compound prepared in Example 1. FIG.
도 2는 실시예 1에서 제조한 코폴리카보네이트의 1 "NMR 그래프이다. 【발명의 효과】 Figure 2 is a 1 "NMR graph of the copolycarbonate prepared in Example 1. [Effect of the invention]
본 발명에 따르면, 기계적 물성이 우수하면서도, 내후성 또한 뛰어난 코폴리카보네이트와 이를 제조할 수 있는 방법이 제공될 수 있다.  According to the present invention, a copolycarbonate having excellent mechanical properties and excellent weather resistance and a method of manufacturing the same can be provided.
【발명을 실시하기 위한 구체적인 내용】 [Specific contents to carry out invention]
발명을 하기의 실시예에서 보다 상세하게 설명한다. 단, 하기의 실시예는 본 발명을 예시하는 것일 뿐, 본 발명의 내용이 하기의 실시예에 의하여 한정되는 것은 아니다. 실시예: 코폴리카보네이트의 제조  The invention is explained in more detail in the following examples. However, the following examples are only for exemplifying the present invention, and the contents of the present invention are not limited to the following examples. Example: Preparation of Copolycarbonate
실시예 1 (1) bi s-(4-(2-(4-hydroxyphenyl )propan-2-yl )pheny 1 )3 , 3'- thiodip
Figure imgf000009_0001
Example 1 (1) bi s- (4- (2- (4-hydroxyphenyl) propan-2-yl) pheny 1) 3, 3'- thiodip
Figure imgf000009_0001
3,3'-Thiodipropionic acid 5g 을 등근 플라스크에 메틸렌클로라이드 용매 50ml 에 용해한 후, 상온에서 옥살릴클로라이드 7.47g 및 DMF O.OOlg 을 적가하여 4 시간 가량 상온에서 교반하고, 감압회전 증발기를 통하여 용매를 제거하여 3,3-Thiodipropionic chloride 를 얻었다. 그리고, 수득한 3,3'- Thiodipropionic chloride 를 다른 정제 과정 없이 Dichloromethane 50ml 에 녹인 후 Bisphenol A 13.12g 과 NaOH 2.3g 및 물 50ml 에 천천히 첨가하여 24 시간 동안 상온에서 교반하였다. HC1 50ml 을 첨가하여 반웅을 종결한 후 물과 Dichloromethane 을 통해 씻어주었다. 최종 화합물인 bis-(4-(2-(4— hydroxyphenyl )propan-2-yl )phenyl )3,3'-thiodipropionate 를 최종 수율 85%로 수득하였다. After dissolving 5 g of 3,3'-Thiodipropionic acid in 50 ml of methylene chloride solvent in a back flask, 7.47 g of oxalyl chloride and DMF O.OOlg were added dropwise at room temperature and stirred at room temperature for about 4 hours. 3,3-Thiodipropionic chloride was obtained by removal. Then, the obtained 3,3'- Thiodipropionic chloride was dissolved in 50 ml of dichloromethane without any other purification process, and then slowly added to 13.12 g of Bisphenol A, 2.3 g of NaOH, and 50 ml of water, followed by stirring at room temperature for 24 hours. 50 ml of HC1 was added to terminate the reaction, followed by washing with water and dichloromethane. A final compound, bis- (4- (2- (4—hydroxyphenyl) propan-2-yl) phenyl) 3,3'-thiodipropionate, was obtained with a final yield of 85%.
상기 화합물의 1 NMR은 도 1에 나타내었다. 1 NMR of the compound is shown in FIG. 1.
(2) 코폴리카보네이트 수지의 제조 (2) Preparation of Copolycarbonate Resin
질소 퍼지와 콘덴서가 구비되고, 서클레이터 (circulator)로 상온 유지가 가능한 2L 메인 반웅기에 물 620g, BPA 116.24g, 상기 (1)에서 제조한 bis-(4-(2-( 4-hy dr oxypheny 1 )propan-2-yl ) phenyl )3, 3'-thiodi pro ionate 0.6g, NaOH 102.5g, MeCl2 200ml를 투입하고, 수분간 교반시켰다. 2L main reactor equipped with a nitrogen purge and a condenser and capable of maintaining a room temperature with a circulator, 620g of water, 116.24g of BPA, bis- (4- (2- (4-hy dr) Oxypheny 1) propan-2-yl) phenyl) 3, 0.6 g of 3'-thiodi proionate, 102.5 g of NaOH, and 200 ml of MeCl 2 were added and stirred for several minutes.
질소 퍼징을 멈추고 1L 등근 바닥 플라스크에 트리포스겐 62g 과 MeCl2 120g 을 넣고 트리포스겐을 용해시킨 다음 용해된 트리포스겐 용액을 천천히 BPA 용액이 녹아 있는 메인 반응기에 투입하고, 투입이 완료되면 PTBP(p— tert- 부틸페놀) 2.28g 을 넣고 10 여분간 교반시켰다. 교반이 완료된 후 40 중량 %의 NaOH 수용액 97g 을 넣은 후 커플링 제로서 TEA 1.16g 을 투입하였다. 이 때, 반웅 pH 는 11~13 을 유지하였다. 층분히 반웅이 이루어지도록 시간을 두고 반웅을 종결하기 위해 HC1 을 투입하여 pH 를 3~4 로 떨어뜨렸다. 그리고, 교반올 중지하여 폴리머층과 물층을 분리한 다음 물층은 제거하고 순수한Stop nitrogen purging, add 62 g of Triphosgene and 120 g of MeCl 2 in a 1 L isometric bottom flask, dissolve the Triphosgen, and slowly add the dissolved Triphosgen solution to the main reactor in which the BPA solution is dissolved. 2.28 g of tert-butylphenol) were added and stirred for about 10 minutes. After stirring was completed, 97 g of 40 wt% NaOH aqueous solution was added thereto, and then 1.16 g of TEA was added as a coupling agent. At this time, the reaction pH maintained 11-13. In order to complete the reaction, the pH was dropped to 3-4 by adding HC1 to terminate the reaction. And, Stop the stirring and separate the polymer and water layers, then remove the water layer and
¾0를 다시 투입하여 수세하는 과정을 3~5회 반복 수행하였다. ¾0 was added again and washed three to five times.
수세가 완전히 이루어지면 폴리머층만 추출하고 메탄올, ¾0 등을 이용한 비용매를 사용하여 재침법으로 폴리머 결정체를 수득하였다. 이 때, 제조된 폴리카보네이트는 중량평균분자량이 31,000 g/mol이었다.  After complete washing with water, only the polymer layer was extracted and polymer crystals were obtained by reprecipitation using a nonsolvent using methanol, ¾0, and the like. At this time, the produced polycarbonate had a weight average molecular weight of 31,000 g / mol.
이와 같이 제조한 코폴리카보네이트의 i NMR은 도 2에 나타내었다. 실시예 2 I NMR of the copolycarbonate thus prepared is shown in FIG. 2. Example 2
BPA 의 사용량을 115.5g 으로 변경하고 bi s-(4-(2-(4- hydroxyphenyl )propan-2-yl ) phenyl )3 , 3'-thiodi propionate 의 사용량을 2.4g 으로 변경한 것을 제외하고는 상기 실시예 1 과 동일한 방법으로 폴리카보네이트를 제조하였다. 실시예 3  Except for changing the amount of BPA to 115.5g and the amount of bis- (4- (2- (4-hydroxyphenyl) propan-2-yl) phenyl) 3 and 3'-thiodi propionate to 2.4g Polycarbonate was prepared in the same manner as in Example 1. Example 3
BPA 의 사용량을 114.2g 으로 변경하고, bi s_(4-(2-(4- hydroxyphenyl )propan-2-yl )phenyl )3 , 3'-thiodipropionate 의 사용량을 Change the amount of BPA to 114.2 g, and change the amount of bi s_ (4- (2- (4-hydroxyphenyl) propan-2-yl) phenyl) 3,3'-thiodipropionate
5.8g 으로 변경한 것을 제외하고는 상기 실시예 1 과 동일한 방법으로 폴리카보네이트를 제조하였다. 실시예 4 A polycarbonate was prepared in the same manner as in Example 1 except for changing to 5.8 g. Example 4
BPA 의 사용량을 111.6g 으로 변경하고, bi s-(4-(2-(4- hydr oxypheny 1 )prop an-2-y 1 )phenyl )3 , 3'-thiodipropionate 의 사용량을 12.6g 으로 변경한 것을 제외하고는 상기 실시예 1 과 동일한 방법으로 폴리카보네이트를 제조하였다. 실시예 5  Change the amount of BPA used to 111.6g and the amount of bi s- (4- (2- (4-hydroxyoxyy 1) prop an-2-y 1) phenyl) 3 and 3'-thiodipropionate to 12.6g Except that polycarbonate was prepared in the same manner as in Example 1. Example 5
PTBP의 사용량을 1.97g으로 변경한컷을 제외하고는 상기 실시예 1과 동일한 방법으로 폴리카보네이트를 제조하였다. 실시예 6 PTBP의 사용량을 3.41g으로 변경한 것을 제외하고는 상기 실시예 1과 동일한 방법으로 폴리카보네이트를 제조하였다. 비교예 1 Polycarbonate was prepared in the same manner as in Example 1, except that the PTBP was changed to 1.97 g. Example 6 Polycarbonate was prepared in the same manner as in Example 1, except that the amount of PTBP was changed to 3.41 g. Comparative Example 1
bis-(4-(2-( 4-hydr oxypheny 1 )propan-2-yl ) phenyl )3,3'- thiodipropionate 를 사용하지 않고, BPA 를 116.47g 사용한 것을 제외하고는 실시예 1과 동일한 방법으로 폴리카보네이트를 제조하였다. 비교예 2  Except for using bis- (4- (2- (4-hydr oxypheny 1) propan-2-yl) phenyl) 3,3'-thiodipropionate and 116.47 g of BPA, the same procedure as in Example 1 Polycarbonate was prepared. Comparative Example 2
bi s-( 4- (2- (4-hydr oxypheny 1 )propan-2-yl ) henyl )3,3'- thiodipropionate 를 사용하지 않고, BPA 를 116.47g사용하고, PTBP 를 1.97g 사용한 것을 제외하고는 실시예 1 과 동일한 방법으로 폴리카보네이트를 제조하였다. 비교예 3  Except not using bi s- (4- (2- (4-hydr oxypheny 1) propan-2-yl) henyl) 3,3'- thiodipropionate, 116.47 g of BPA, and 1.97 g of PTBP Was prepared in the same manner as in Example 1. Comparative Example 3
b i s- ( 4- ( 2- ( 4-hydr oxypheny 1 )propan-2-yl ) henyl )3,3'- thiodipropionate 를 사용하지 않고, BPA 를 116.47g 사용하고, PTBP 를 3.41g 사용한 것을 제외하고는 실시예 1 과 동일한 방법으로 폴리카보네이트를 제조하였다. 실험예: 코폴리카보네이트의 물성 평가  Except for using bis- (4- (2- (4-hydroxyoxyy 1) propan-2-yl) henyl) 3,3'-thiodipropionate, 116.47g of BPA, and 3.41g of PTBP Was prepared in the same manner as in Example 1. Experimental Example: Evaluation of Physical Properties of Copolycarbonate
상기 실시예 1 및 비교예 1 에서 제조한 폴리카보네이트의 사출시편의 특성을 하기의 방법으로 측정하였고, 그 결과를 표 1에 나타내었다.  The characteristics of the injection specimens of the polycarbonate prepared in Example 1 and Comparative Example 1 were measured by the following method, the results are shown in Table 1.
* 중량평균분자량 (g/mol): Agilent 1200 series 를 이용하여, PC standard로 검량하여 측정하였다.  * Weight average molecular weight (g / mol): Agilent 1200 series was measured by calibration with PC standard.
* 흐름성 (MI): ASTM D1238(300°C, 1.2kg조건)에 의거하여 측정하였다.* Flowability (MI): measured according to ASTM D1238 (300 ° C., 1.2 kg conditions).
* 유리전이 온도 ( , °C): 시차주사열량분석기 (Differential Scanning Calor imetry, DSC) * Glass transition temperature (, ° C): Differential Scanning Calorimetry (DSC)
* 층격강도 (IMP, J/m): ASTM D256(l/8 inch, Notched Izod)에 의거하여 23°C에서 측정하였다. * 내후성 (dYI , 500t ime) : 제논 내후성 시험기 (Zenon Whether 0 meter )를 이용하여 ASTM G155 에 의거하여 시편의 황색도 (Yel low Index)의 변화량 (dYI )를 측정하였다. 【표 1】 * Lamellar strength (IMP, J / m): measured at 23 ° C according to ASTM D256 (l / 8 inch, Notched Izod). * Weather resistance (dYI, 500t ime): The change amount (dYI) of the yellow low index (dYI) of the specimen was measured according to ASTM G155 using a Zenon Whether or Zero meter. Table 1
Figure imgf000012_0001
상기 표 1 을 참고하면, 실시예 1 에서 제조한 코폴리카보네이트는 일반적인 폴리카보네이트인 비교예 1 과 비교하여 동등 수준의 층격강도를 나타낼 뿐만 아니라, 매우 우수한 흐름성을 나타내는 것을 확인할 수 있다. 또한, 이러한 실시예의 코폴리카보네이트는 폴리카보네이트 수지 고유의 물성은 유지하면서도 각종 기후에 견디는 성질인 내후성이 매우 우수하므로 전기전자 제품의 외장재, 자동차 부품, 건축 소재와 같은 다양한 분야에 적용이 용이하다.
Figure imgf000012_0001
Referring to Table 1, it can be seen that the copolycarbonate prepared in Example 1 shows not only the level of laminar strength equivalent to that of Comparative Example 1, which is a general polycarbonate, but also very excellent flowability. In addition, the copolycarbonate of this embodiment is very excellent in weatherability, which is a property that withstands various climates while maintaining the inherent properties of polycarbonate resin, it is easy to apply to various fields such as exterior materials, automotive parts, building materials of electrical and electronic products.

Claims

【특허청구범위】 [Patent Claims]
【청구항 1】  [Claim 1]
하기 화학식 1 로 표시되는 반복 단위 및 하기 화학식 2 로 표시되는 반복 단위를 포함하고,  It includes a repeating unit represented by the formula (1) and a repeating unit represented by the formula (2),
중량 평균 분자량이 1 , 000 내지 100 , 000 g/mol인, 코폴리카보네이트: [화학식 1]  Copolycarbonates having a weight average molecular weight of from 1,000 to 100, 000 g / mol:
Figure imgf000013_0001
Figure imgf000013_0001
상기 화학식 1에서,  In Chemical Formula 1,
Ri 내지 ¾는 각각 독립적으로 수소 또는 Cwo알킬이고,  Ri to ¾ are each independently hydrogen or Cwo alkyl,
Y는 Cwo 알킬렌이고,  Y is Cwo alkylene,
Z는 결합, -0C0- 또는 -C00-이고,  Z is a bond, -0C0- or -C00-,
Xi 내지 ¾는 각각 독립적으로 비치환되거나 또는 페닐로 치환된 d-lc 알킬렌, 비치환되거나 또는 에 알킬로 치환된 C3-15 사이클로알킬렌, 0, S , SO , S02 , 또는 CO이고, Xi to ¾ are each independently unsubstituted phenyl, or a d- lc alkylene, unsubstituted or substituted with a C 3 alkyl substituted with - and 15 cycloalkylene, 0, S, SO, S0 2, or CO ,
[화학식 2]  [Formula 2]
Figure imgf000013_0002
Figure imgf000013_0002
상기 화학식 2에서,  In Chemical Formula 2,
¾ 내지 R12 는 각각 독립적으로 수소, d-ω 알킬, d-10 알콕시 또는 할로겐이고, ¾ to R 12 are each independently hydrogen, d-ω alkyl, d- 10 alkoxy or halogen,
¾ 는 비치환되거나 또는 페'닐로 치환된 Cwo 알킬렌, 비치환되거나 또는 c— 10 알킬로 치환된 C3-15 사이클로알킬렌, 0, ^ SO, S02 , 또는 C0이다. 15 cycloalkylene, 0, ^ SO, S0 2, or C0 - ¾ is unsubstituted or Fe "Nilo Cwo substituted alkylene, unsubstituted or substituted with c- 10 alkyl C 3.
【청구항 2】 제 1항에 있어서, [Claim 2] The method of claim 1,
Y는 d-5 알킬렌인 것을 특징으로 하는, 코폴리카보네이트. Y is d- 5 alkylene, copolycarbonate.
【청구항 3] [Claim 3]
제 1항에 있어서,  The method of claim 1,
상기 ¾ 내지 ¾ 는 각각 독립적으로, 수소, 또는 d-4 알킬인 것을 특징으로 하는, 코폴리카보네이트. Wherein ¾ to ¾ are each independently hydrogen or d- 4 alkyl, copolycarbonate.
【청구항 4】 [Claim 4]
제 1항에 있어서,  The method of claim 1,
상기 화학식 1 로 표시되는 반복 단위와, 화학식 2 로 표시되는 반복 단위의 몰 비는 1 :0.001 내지 1 : 1인, 코폴리카보네이트.  The molar ratio of the repeating unit represented by the formula (1) and the repeating unit represented by the formula (2) is 1: 0.001 to 1: 1, copolycarbonate.
【청구항 5】 [Claim 5]
제 1항에 있어서,  The method of claim 1,
ASTM G155 에 의거하여 측정한 황색도 변화량 (dYI )이 20 이하인, 코폴리카보네이트.  The copolycarbonate whose yellowness change (dYI) measured according to ASTM G155 is 20 or less.
【청구항 6] [Claim 6]
하기 화학식 3 으로 표시되는 화합물, 방향족 디을 화합물 및 카보네이트 전구체를 포함하는 조성물을 중합하는 단계 ;를 포함하는, 제 1항의 코폴리카보네이트의 제조 방법:  A method for producing a copolycarbonate according to claim 1 comprising the step of polymerizing a composition comprising a compound represented by the following formula (3), an aromatic di compound and a carbonate precursor:
[화학식 3]  [Formula 3]
Figure imgf000014_0001
Figure imgf000014_0001
상기 화학식 3에서,  In Chemical Formula 3,
Ri 내지 ¾는 각각 독립적으로 수소 또는 d-10알킬이고, Ri to ¾ are each independently hydrogen or d- 10 alkyl,
Y는 d-u) 알킬렌이고, z는 결합, -oco—또는—coo-이고, Y is du) alkylene, z is a combination, -oco—or—coo-
Xi 내지 X2 는 비치환되거나 또는 페닐로 치환된 d-u) 알킬렌, 비치환되거나 또는 Cwo 알킬로 치환된 C3-15 사이클로알킬렌, 0, S , SO, S02 , 또는 CO어다. Let 15 cycloalkylene, 0, S, SO, S0 2, CO or - Xi to X 2 is a du) alkylene, substituted or unsubstituted Cwo alkyl, or C 3 substituted with unsubstituted or phenyl beach.
【청구항 7】 [Claim 7]
제 6항에 있어서,  The method of claim 6,
상기 화학식 3 으로 표시되는 화합물은 상기 조성물 100 중량 %에 대해 0. 1 중량 % 이상 및 20 중량 % 이하를 사용하는 것을 특징으로 하는, 코폴리카보네이트의 제조 방법 .  Compound represented by the formula (3) is characterized in that the use of 0.01% by weight or more and 20% by weight or less with respect to 100% by weight of the composition, a method for producing a copolycarbonate.
【청구항 8】 [Claim 8]
제 1 항 내지 제 5 항 중 어느 한 항의 코폴리카보네이트로 제조되는, 성형품.  A molded article made of the copolycarbonate of any one of claims 1 to 5.
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3773812A (en) * 1963-01-02 1973-11-20 Exxon Alkylene-bridged esters
JP2002249472A (en) * 2000-12-04 2002-09-06 Ricoh Co Ltd Aromatic polycarbonate resin and photosensitive material for electrophotography
JP2008274239A (en) * 2007-03-30 2008-11-13 Univ Kanagawa Hyper branched polycarbonate and its manufacturing method
JP2010001432A (en) * 2008-06-23 2010-01-07 Idemitsu Kosan Co Ltd Comonomer for production of polycarbonate resin and method for producing same
KR20150032174A (en) * 2013-09-17 2015-03-25 주식회사 엘지화학 Adamantane derivatives capping monomer, and method for preparing polycarbonate copolymer with improved flow using thereof

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3773812A (en) * 1963-01-02 1973-11-20 Exxon Alkylene-bridged esters
JP2002249472A (en) * 2000-12-04 2002-09-06 Ricoh Co Ltd Aromatic polycarbonate resin and photosensitive material for electrophotography
JP2008274239A (en) * 2007-03-30 2008-11-13 Univ Kanagawa Hyper branched polycarbonate and its manufacturing method
JP2010001432A (en) * 2008-06-23 2010-01-07 Idemitsu Kosan Co Ltd Comonomer for production of polycarbonate resin and method for producing same
KR20150032174A (en) * 2013-09-17 2015-03-25 주식회사 엘지화학 Adamantane derivatives capping monomer, and method for preparing polycarbonate copolymer with improved flow using thereof

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112739744A (en) * 2018-08-10 2021-04-30 株式会社Lg化学 Polycarbonate and method for producing same
CN112739744B (en) * 2018-08-10 2023-01-20 株式会社Lg化学 Polycarbonate and method for producing same

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