KR930003712B1 - Aromatic polyester polymer and produce for preparation of the aromatic polyester polymer - Google Patents

Aromatic polyester polymer and produce for preparation of the aromatic polyester polymer Download PDF

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KR930003712B1
KR930003712B1 KR1019900001418A KR900001418A KR930003712B1 KR 930003712 B1 KR930003712 B1 KR 930003712B1 KR 1019900001418 A KR1019900001418 A KR 1019900001418A KR 900001418 A KR900001418 A KR 900001418A KR 930003712 B1 KR930003712 B1 KR 930003712B1
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repeating unit
component
aromatic polyester
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KR910015618A (en
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이도묵
이규완
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주식회사 삼양사
김상응
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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
    • C08G63/00Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/68Polyesters containing atoms other than carbon, hydrogen and oxygen
    • C08G63/688Polyesters containing atoms other than carbon, hydrogen and oxygen containing sulfur
    • C08G63/6884Polyesters containing atoms other than carbon, hydrogen and oxygen containing sulfur derived from polycarboxylic acids and polyhydroxy compounds
    • C08G63/6886Dicarboxylic acids and dihydroxy compounds
    • 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
    • C08G63/00Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/02Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds
    • C08G63/60Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds derived from the reaction of a mixture of hydroxy carboxylic acids, polycarboxylic acids and polyhydroxy compounds
    • C08G63/605Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds derived from the reaction of a mixture of hydroxy carboxylic acids, polycarboxylic acids and polyhydroxy compounds the hydroxy and carboxylic groups being bound to aromatic rings
    • 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
    • C08G63/00Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/78Preparation processes
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    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K19/00Liquid crystal materials
    • C09K19/04Liquid crystal materials characterised by the chemical structure of the liquid crystal components, e.g. by a specific unit
    • C09K19/38Polymers
    • C09K19/3804Polymers with mesogenic groups in the main chain
    • C09K19/3809Polyesters; Polyester derivatives, e.g. polyamides

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Abstract

The wholly aromatic polyester crystal polymer comprises: (A) the units of the oxybenzoil component of formulas (I) and (II); (B) the units of the dioxy component of formulas (III) and (IV); and (C) the units of the dicarboxy component of formulas (V) and (VI). The said polymer contains 10-70 No % of the unit of (A) component; 15-45 No % of the unit of (B) component; and the same No of the unit of (C) with (A) w.r.t. total number of all units in the polymer. Pref. the polymer is prepd. by polymerization of hydroxy benzoic acid, metahydroxy benzoic acid, bi-phenol, bis-(4-hydroxy phenyl) sulfon, terephthalic acid, isophthalic acid or derivs, thereof.

Description

전방향족 폴리에스테르 액정중합체와 그의 제조방법Wholly aromatic polyester liquid crystal polymer and preparation method thereof

본발명은 전방향족(Wholly aromatic)폴리에스테르 액정중합체에 관한 것으로서, 더욱 상세하게는 파라히드록시벤조산, 메타히드록시벤조산, 비페놀, 비스-(4-히드록시페닐)설폰, 테레프탈산, 이소프탈산 또는 이들의 화합물의 유도체를 출발물질로 하여 공중합시키므로써 제조되는 열안정성을 포함한 제반 물리기계적 특성이 우수하면서도 성형가공이 용이한 전방향족 폴리에스테르액정중합체와 그를 제조하는 방법에 관한 것이다.FIELD OF THE INVENTION The present invention relates to Wholly aromatic polyester liquid crystal polymers, more particularly parahydroxybenzoic acid, metahydroxybenzoic acid, biphenol, bis- (4-hydroxyphenyl) sulfone, terephthalic acid, isophthalic acid or The present invention relates to a wholly aromatic polyester liquid crystal polymer having excellent physico-mechanical properties including heat stability prepared by copolymerizing derivatives of these compounds as starting materials and being easy to be molded and processed.

일반적으로 전방향족 폴리에스테르는 방향족환(aromatic ring)의 열역학적 안정성과 분자사슬의 강직한 구조특성 때문에 열안정성 및 내열성, 물리기계적 특성, 내화학적 특성, 내오일성, 방사능에 대한 저항성, 형태 안정성 등이 매우 좋다. 이 때문에 전방향족 액정중합체는 기계, 전기, 전자부품, 자동차부품 등 여러 분야에서 널리 사용되고 있으며, 그 잠재적인 활용가능성에도 많은 관심과 기대가 모아지고 있다.Generally, the aromatic aromatic polyester has a high thermal stability, heat resistance, physical and mechanical properties, chemical resistance, oil resistance, radiation resistance, and morphological stability due to the thermodynamic stability of the aromatic ring and the rigid structural properties of the molecular chain. very good. For this reason, the wholly aromatic liquid-crystalline polymer is widely used in various fields such as mechanical, electrical, electronic parts, automobile parts, etc., and much attention and expectation are attracted to its potential applicability.

그러나, 이러한 전방향족 폴리에스테르는 융점이 너무 높아서 성형 가공하는데 상당한 어려움이 있고, 가공 과정중 분해에 의한 특성손실이 심각하기 때문에, 전방향족 폴리에스테르 개발이후 이에 대해 끊임없이 연구가 진행되고 있다.However, such an wholly aromatic polyester has a very high melting point, which is a significant difficulty in forming, and since the loss of properties due to decomposition during processing is severe, studies have been continuously conducted since the development of the wholly aromatic polyester.

따라서, 본발명은 상기와 같이 종래에 문제되었던 전방향족 폴리에스테르중합체의 성형가공성 및 특성손실의 문제를 해결하기 위해서, 새로운 성분과 조성으로 이루어진 신규한 구조의 전방향족 폴리에스테르액정중합체와 그 제조방법을 제공하는데 그 목적이 있다.Therefore, the present invention is to solve the problem of moldability and loss of properties of the wholly aromatic polyester polymer, which has been conventionally problem as described above, a wholly aromatic polyester liquid crystal polymer of a novel structure composed of a new component and composition and a manufacturing method thereof The purpose is to provide.

이하, 본발명을 상세히 설명하면 다음과 같다.Hereinafter, the present invention will be described in detail.

본발명은 전방향족 폴리에스테르중합체에 있어서, 다음 구조식(Ⅰ)로 표시되는 반복단위와 다음 구조식(Ⅱ)로 표시되는 반복단위인 옥시벤조일성분의 반복단위와, 다음 구조식(Ⅲ)으로 표시되는 반복단위와 다음 구조식(Ⅳ)로 표시되는 반복단위인 디옥시성분의 반복단위, 그리고 다음 구조식(Ⅴ)로 표시되는 반복단위와 구조식(Ⅵ)으로 표시되는 반복단위인 디카르복시 성분의 반복단위로 구성되어 있는 전방향족 폴리에스테르액정중합체를 그 특징으로 한다.The present invention, in the wholly aromatic polyester polymer, the repeating unit represented by the following structural formula (I), the repeating unit of the oxybenzoyl component which is a repeating unit represented by the following structural formula (II), and the repeating represented by the following structural formula (III) Unit and a repeating unit of the dioxy component which is a repeating unit represented by the following structural formula (IV), and a repeating unit represented by the following structural formula (V) and a repeating unit of the dicarboxy component which is a repeating unit represented by the structural formula (VI). It is characterized by the wholly aromatic polyester liquid crystal polymer.

Figure kpo00001
Figure kpo00001

이하, 본발명을 더욱 상세히 설명하면 다음과 같다.Hereinafter, the present invention will be described in more detail.

본발명은 기본적으로 옥시벤조일성분과 디옥시성분 및 디카르복시성분의 반복단위들로 구성되어 있는 바, 상기 옥시벤조일성분의 반복단위로는 상기 구조식(Ⅰ)과 (Ⅱ)의 반복단위가 구성되어 있으며, 그들의 총 구성비율은 전체 구성성분의 반복단위 갯수에 대해 10∼70%, 바람직하게는 20∼50%로 구성되어 있는 것이좋다.The present invention basically consists of the repeating units of the oxybenzoyl component, the dioxy component and the dicarboxy component, and the repeating units of the structural formulas (I) and (II) are composed of the repeating units of the oxybenzoyl component. It is preferable that their total composition ratio is 10 to 70%, preferably 20 to 50% with respect to the number of repeating units of the whole component.

또한, 상기 디옥시성분의 반복단위들로는 상기 구조식(Ⅲ)과 (Ⅳ)의 반복단위가 구성되어 있으며, 그들의 총 구성비율은 45∼15%, 바람직하게는 40∼25%로 구성된 것이 좋다.In addition, the repeating units of the deoxy component are composed of the repeating units of the structural formulas (III) and (IV), and their total composition ratio is preferably 45 to 15%, preferably 40 to 25%.

그리고, 상기 디카르복시성분의 반복단위들로서는 상기 구조식(Ⅴ)의 반복단위와 상기 구조식(Ⅵ)의 반복단위가 혼합구성되어 있으며, 그들의 총구성 비율은 상기 디옥시성분 반복단위의 총 구성비율과 동일하게 구성되어 있는 것이다.The repeating units of the dicarboxy component include a repeating unit of the structural formula (V) and a repeating unit of the structural formula (VI), and their total composition ratio is determined by the total constituent ratio of the repeating unit of the deoxy component. It is configured in the same way.

이때, 본발명에 따르면 상기 구조식(Ⅱ)의 반복단위는 전체 옥시벤조일성분의 반복단위 갯수에 대해 10∼70%, 바람직하게는 20∼50%로 구성되어 있으며, 상기 구조식(Ⅲ)의 반복단위는 전체 디옥시성분의 반복단위 갯수에 대해 30∼80%, 바람직하게는 40∼70%로 구성되어 있고, 상기 구조식(Ⅵ)의 반복단위는 전체 디카르복시성분의 반복단위중 5∼70%, 바람직하게는 20∼50%로 구성되어 있다.At this time, according to the present invention, the repeating unit of the structural formula (II) is composed of 10 to 70%, preferably 20 to 50% of the total number of repeating units of the oxybenzoyl component, and the repeating unit of the structural formula (III) Is composed of 30 to 80%, preferably 40 to 70% of the total number of repeating units of the deoxy component, and the repeating unit of the formula (VI) is 5 to 70% of the repeating units of the total dicarboxy component, Preferably it consists of 20-50%.

한편, 본발명에 따른 상기와 같은 전방향족 폴리에스테르액정중합체를 제조하는 공정을 살펴보면, 용융중합에 의해 제조되는데, 교반자, 질소유입구, 콘덴서 및 온도지시계가 장치된 3구 유리플라스크에다 상기 구조식(Ⅰ)∼(Ⅵ)의 반복단위들을 유도할 수 있는 화합물 즉, 구조식(Ⅰ)의 반복단위를 유도하는 파라히드록시벤조산, 구조식(Ⅱ)의 반복단위를 유도하는 메타히드록시벤조산, 구조식[Ⅲ]의 반복단위를 유도하는 4,4'-비페놀, 구조식(Ⅳ)의 반복단위를 유도하는 비스-(4-히드록시페닐)설폰, 구조식(Ⅴ)의 반복단위를 유도하는 테레프탈산, 그리고 구조식(Ⅵ)의 반복단위를 유도하는 이소프탈산을 출발물질로 하여 각기 상기의 반복단위 갯수에 상응하는 동일한 수의 몰% 비율로 투입한다.On the other hand, looking at the process for producing a wholly aromatic polyester liquid crystal polymer as described above according to the present invention, it is prepared by melt polymerization, the structural formula (3) in the three-necked glass flask equipped with agitator, nitrogen inlet, condenser and temperature indicator ( A compound capable of inducing repeating units of I) to (VI), namely parahydroxybenzoic acid inducing repeating unit of formula (I), metahydroxybenzoic acid inducing repeating unit of formula (II), structural formula [III ] 4,4'-biphenol which induces repeating units of bis, bis- (4-hydroxyphenyl) sulfone inducing repeating units of formula (IV), terephthalic acid inducing repeating units of formula (V), and structural formula Using isophthalic acid, which derives the repeating units of (VI), as a starting material, each is added in the same number of mole% ratios corresponding to the number of repeating units described above.

더 상세하게는 파라히드록시벤조산과 메타히드록시벤조산의 옥시벤조일성분 총 함량 10∼70몰%와, 4,4'-비페놀과 비스-(4-히드록시페닐)설폰의 디옥시성분 총 함량 45∼15몰%, 그리고 테레프탈산과 이소프탈산의 디카르복시성분 총 함량 45∼15몰%를 첨가하되, 이때 디옥시성분과 디카르복시성분은 등몰량으로 첨가한다.More specifically, 10 to 70 mol% of the total content of oxybenzoyl component of parahydroxybenzoic acid and metahydroxybenzoic acid, and the total content of dioxy component of 4,4'-biphenol and bis- (4-hydroxyphenyl) sulfone 45-15 mol% and 45-15 mol% of terephthalic acid and the total content of the dicarboxy components of isophthalic acid are added, At this time, the dioxy component and the dicarboxy component are added in equimolar amount.

이렇게 반응물을 투입하고나서 공중합시키기 전에 초산무수물(acetic anhydride)을 투입한 후, 전기히터로 가열되는 스테인레스염욕(salt bath)에 반응플라스크를 적당히 잠기게 하고, 140℃∼180℃에서, 바람직하기로는 145℃∼160℃에서 2∼10시간 동안 초산무수물을 환류(reflux)시키면서 공중합반응을 실시한다.After adding the reactant and copolymerizing acetic anhydride before copolymerization, the reaction flask is appropriately immersed in a stainless salt bath heated by an electric heater, and preferably at 140 ° C to 180 ° C, preferably The copolymerization reaction is carried out at reflux of acetic anhydride for 2 to 10 hours at 145 ° C to 160 ° C.

본발명에서는 반응시키기 직전에 플라스크내부의 공기는 수분을 함유하지 않은 고순도질소로 완전히 치환되며 감압을 걸기 시작할 때까지 질소분위기를 계속 유지할 수 있도록 질소유입구를 통해서 질소를 공급해준다. 상기 온도에서의 환류과정이 충분히 이루어진 다음에는 1∼3시간에 걸쳐 약 320℃까지 승온시키는데, 이 과정에는 과잉의 초산무수물이 모두 유출되어 나온다. 그후 온도가 240℃∼270℃에 이르면 반응기내의 반응물이 비등방성 액상(anisotropic melt phase)을 형성하게 되며, 320℃ 부근에서 약 1시간 정도 중합시킨 후 어느정도 점성을 가지게 되면 서서히 감압을 걸어 20∼90분 더 중합시키고 생성된 중합체를 얻는다.In the present invention, just before the reaction, the air in the flask is completely replaced with high-purity nitrogen containing no moisture, and nitrogen is supplied through the nitrogen inlet to keep the nitrogen atmosphere until the pressure is reduced. After sufficient reflux at this temperature, the temperature is raised to about 320 ° C. over 1 to 3 hours, in which excess excess acetic anhydride flows out. After that, when the temperature reaches 240 ℃ ~ 270 ℃, the reactants in the reactor form an anisotropic melt phase, and after polymerization for about 1 hour in the vicinity of 320 ℃, if it has some viscosity, it is gradually reduced to 20 ~ 90 More minutes are polymerized and the resulting polymer is obtained.

본발명에 따르면 중합체의 합성의 효율을 높이기 위해서 촉매를 사용할 수도 있는데, 바람직한 촉매로는 알카리금속 또는 알칼리토금속의 염, 메틸스테노인산, 메톡시 또는 부톡시 등의 유기바나듐화합물, 게르마늄산화물 및 이들의 혼합물 등을 사용할 수 있다.According to the present invention, a catalyst may be used to increase the efficiency of the synthesis of the polymer. Preferred catalysts include salts of alkali metals or alkaline earth metals, organic vanadium compounds such as methyl stenophosphoric acid, methoxy or butoxy, germanium oxides, and the like. Mixtures thereof and the like can be used.

이상과 같은 반응조성과 반응과정을 통해 제조된 전방향족 액정 폴리에스테르는 피브릴화 현상이 현저히 감소하게 되며, 점도가 높은 중합체로서 성형성이 좋으면서도 전방향족 액정 폴리에스테르의 일반적특성인 고강력, 고모듈러스, 열안정성 및 내열성을 보유하게 된다.The wholly aromatic liquid crystal polyester prepared through the reaction composition and the reaction process as described above significantly reduces the fibrillation phenomenon, and is a high viscosity polymer having good moldability and high strength, which is a general characteristic of the wholly aromatic liquid crystal polyester. It has high modulus, thermal stability and heat resistance.

또한, 합성된 중합체의 고유점도는 측정온도 45℃ 용질농도 0.5g/dl의 파라클로로페놀용액중에서 1.0∼1.4g/dl이었으며, 이들 중합체를 300℃∼350℃ 온도 범위에서 방사하여 강도 3.8∼5.4g/d, 신도 1.7∼2.5%, 탄성모듈러스 460∼510g/d인 섬유를 얻을 수 있다. 그리고 방사된 섬유를 질소기류 또는 감압(≤2mmHg)하의 조건으로 180℃∼250℃에서 10시간에 걸쳐 단계적으로 열처리하게 되면 강도 및 신도가 각각 12∼16.5g/d, 1.9∼2.8%, 그리고 탄성모듈러스는 892∼1004g/d로 증가하였다.In addition, the intrinsic viscosity of the synthesized polymer was 1.0 to 1.4 g / dl in a parachlorophenol solution having a measurement temperature of 45 ° C. solute concentration of 0.5 g / dl, and the polymer was spun at a temperature range of 300 ° C. to 350 ° C. to give a strength of 3.8 to 5.4. g / d, elongation 1.7-2.5%, elastic modulus 460-510g / d can be obtained. When the spun fiber is heat-treated stepwise at 180 ° C. to 250 ° C. over 10 hours under nitrogen gas flow or reduced pressure (≦ 2 mmHg), strength and elongation are 12 to 16.5 g / d, 1.9 to 2.8%, and elasticity, respectively. Modulus increased from 892 to 1004 g / d.

이하, 본발명을 실시예에 의거 보다 구체적으로 설명한다.Hereinafter, the present invention will be described in more detail with reference to Examples.

본실시에에서 방향족 폴리에스테르의 고유점도 ηinh는 다음의 식으로부터 계산하였다.In this embodiment, the intrinsic viscosity ηinh of the aromatic polyester was calculated from the following equation.

Figure kpo00002
Figure kpo00002

여기서, ηrel은 상대점도, ln은 상용로그, C는 용액의 농도(0.5g/dl)이다.Where rel is the relative viscosity, ln is the commercial log and C is the concentration of the solution (0.5 g / dl).

[실시예 1]Example 1

교반자, 질소유입관 및 콘덴서를 장치한 1ℓ의 3구 반응플라스크에 파라히드록시벤조산 165.7g(12몰), 메타히드록시벤조산 41.4g(0.3몰), 4,4'-비페놀 167.59g(0.9몰), 비스-(4-히드록시페닐)설폰 150.17g(0.5몰), 테레프탈산 166.13g(1.0몰), 이소프탈산 83.07(0.5몰), 초산무수물 551.29g(5.4몰)을 투입하고 반응관내부를 질소로 치환한다. 계속적인 질소유입을 통해 질소분위기를 유지시키면서 온도를 150℃로 올린다. 온도가 150℃에 도달하면 3시간 30분동안 환류반응시킨 다음, 10분당 15℃의 승온속도로 320℃까지 온도를 올린다.165.7 g (12 mol) of parahydroxybenzoic acid, 41.4 g (0.3 mol) of metahydroxybenzoic acid, and 167.59 g of 4,4'-biphenol in a 1 L three-necked reaction flask equipped with a stirrer, a nitrogen inlet tube and a condenser 0.9 mole), bis- (4-hydroxyphenyl) sulfone 150.17 g (0.5 mole), terephthalic acid 166.13 g (1.0 mole), isophthalic acid 83.07 (0.5 mole), acetic anhydride 551.29 g (5.4 mole) Replace the part with nitrogen. The temperature is raised to 150 ° C while maintaining the nitrogen atmosphere through continuous nitrogen inflow. When the temperature reaches 150 ° C., the reaction is refluxed for 3 hours 30 minutes, and the temperature is raised to 320 ° C. at a temperature rising rate of 15 ° C. per 10 minutes.

이때의 승온과정 초기에는 과잉의 초산무수물과 아세틸화반응의 생성유출물인 초산이 왕성하게 빠져나오게 되며, 250℃∼260℃에 이르게 되면 뿌옇고 불투명한 비등방성액상을 형성하게 된다. 또한, 온도가 320℃에 도달하게 되면 이 온도에서 1시간 더 반응시켜 분자량을 어느정도 올린 다음, 감압을 100mmHg까지 서서히 걸어주고 1시간후 생성물중합체를 채취한다.At the beginning of the temperature increase process, excess acetic anhydride and acetic acid, which is a effluent of the acetylation reaction, come out vigorously, and when it reaches 250 ° C. to 260 ° C., a cloudy and opaque anisotropic liquid phase is formed. When the temperature reaches 320 ° C., the reaction is further carried out at this temperature for 1 hour to raise the molecular weight to some extent, and then the pressure is gradually reduced to 100 mmHg and the product polymer is collected after 1 hour.

이때 얻어지는 생성물중합체는 점성이 크며 예사성(filament forming property)이 있는 용융물로서 붉은색이 약간 감도는 짙은 갈색을 띤다. 이 중합체의 고유점도는 1.4dl/g, 연화점은 198℃, 흐름온도는 310℃였으며, 320℃에서 방사시킨 후 물성측정결과 강도 4.5g/d, 신도 1.8%, 탄성모듈러스 490g/d인 섬유를 얻었다.The resulting product polymer is viscous and melts with a filament forming property, which has a dark brown color with slightly red color. The polymer had an intrinsic viscosity of 1.4 dl / g, a softening point of 198 ° C, and a flow temperature of 310 ° C. After spinning at 320 ° C, the physical properties of the polymer were 4.5g / d, 1.8% elongation and 490g / d elastic modulus. Got it.

이때, 이 섬유를 180℃에서 250℃까지 단계적으로 온도를 올리면서 감압(≤2mmHg)열처리하여 강도 15.8g/d, 신도 2.7%, 그리고 탄성모듈러스는 920g/d로 증가된 섬유를 얻었다. 얻어진 섬유는 320℃에서 사출 성형하여 인장강도 997kg/cm2인 성형물을 얻었다.At this time, the fiber was heat-treated under reduced pressure (≤2mmHg) while gradually increasing the temperature from 180 ° C to 250 ° C to obtain a fiber having an intensity of 15.8g / d, an elongation of 2.7%, and an elastic modulus of 920g / d. The obtained fiber was injection molded at 320 ° C. to obtain a molded product having a tensile strength of 997 kg / cm 2 .

[실시예 2]Example 2

실시예 1과 동일한 반응장치에 파라히드록시벤조산 138.12g(1.0몰), 메타히드록시벤조산 69.06g(0.5몰), 4,4'-비페놀 167.59g(0.9몰), 비스-(4-히드록시페닐)설폰 150.17g(0.6몰), 테레프탈산 166.13g(1.0몰), 이소프탈산 83.07g(0.5몰), 초산무수물 551.29g(5.4몰)을 투입하고 실시예 1과 동일한 제조과정에 의해 중합체를 합성한다.138.12 g (1.0 mol) of parahydroxybenzoic acid, 69.06 g (0.5 mol) of metahydroxybenzoic acid, 167.59 g (0.9 mol) of 4,4'-biphenol, and bis- (4-hydride) in the same reactor as in Example 1 Roxyphenyl) sulfone 150.17 g (0.6 mole), terephthalic acid 166.13 g (1.0 mole), isophthalic acid 83.07 g (0.5 mole), acetic anhydride 551.29 g (5.4 mole) was added and the polymer was prepared in the same manner as in Example 1. Synthesize

얻어진 중합체의 고유점도는 1.25dl/g, 연화점은 189℃, 흐름온도는 298℃였으며, 310℃에서 방사하여 강도 4.2g/d, 신호 2.1%, 탄성모듈러스 473g/d인 섬유를 얻을 수 있었다. 이 섬유를 실시예 1과 동일한 조건으로 감압 열처리하면 강도가 14.7g/d, 신도는 2.1%로 증가하고 탄성모듈러스는 892g/d인 섬유를 얻게 되었다.The obtained polymer had an inherent viscosity of 1.25 dl / g, a softening point of 189 ° C, and a flow temperature of 298 ° C. The fiber was spun at 310 ° C to obtain a fiber having a strength of 4.2 g / d, a signal of 2.1%, and an elastic modulus of 473 g / d. When the fiber was heat-treated under the same conditions as in Example 1, the strength was increased to 14.7 g / d, the elongation was increased to 2.1%, and the elastic modulus was 892 g / d.

얻어진 섬유는 310℃에서 성형하여 인장강도 945kg/cm2인 성형물을 얻었다.The obtained fiber was molded at 310 ° C. to obtain a molded product having a tensile strength of 945 kg / cm 2 .

[실시예 3]Example 3

파라히드록시벤조산 165.7g(1.2몰), 메타히드록시벤조산 41.4g(0.3몰), 4,4'-비페놀 167.59g(0.9몰), 비스-(4-히드록시페닐)설폰 150.17g(0.6몰), 테레프탈산 124.6g(0.75몰), 이소프탈산 124.6g(0.75몰), 초산무수물 551.29g(5.4몰)을 실시예 1과 동일한 반응장치에 넣고 동일한 방법으로 제조하였다. 얻어진 중합체의 고유점도는 1.32dl/g, 연화점은 191℃, 흐름온도는 295℃였으며, 310℃에서 방사하여 강도 4.0g/d, 신도 2.0%, 탄성모듈러스 465g/d인 섬유를 얻었다.165.7 g (1.2 mole) parahydroxybenzoic acid, 41.4 g (0.3 mole) metahydroxybenzoic acid, 167.59 g (0.9 mole) 4,4'-biphenol, 150.17 g bis- (4-hydroxyphenyl) sulfone Mole), 124.6 g (0.75 mole) of terephthalic acid, 124.6 g (0.75 mole) of isophthalic acid, and 551.29 g (5.4 mole) of acetic anhydride were added to the same reactor as in Example 1, and prepared in the same manner. The obtained polymer had an inherent viscosity of 1.32 dl / g, a softening point of 191 ° C., and a flow temperature of 295 ° C., and was spun at 310 ° C. to obtain fibers having a strength of 4.0 g / d, elongation of 2.0% and elastic modulus of 465 g / d.

실시예 1과 동일한 방법으로 열처리하여 강도 13.2g/d, 신도 2.5%, 탄성모듈러스 902g/d인 섬유를 얻었으며, 330℃에서 성형하여 인장강도 932kg/cm2인 성형물을 얻었다.Heat treatment was performed in the same manner as in Example 1 to obtain a fiber having a strength of 13.2 g / d, elongation of 2.5% and an elastic modulus of 902 g / d, and a molded product having a tensile strength of 932 kg / cm 2 was formed at 330 ° C.

Claims (5)

전방향족 폴리에스테르중합체에 있어서, 다음 구조식(Ⅰ)로 표시되는 반복단위와 다음 구조식(Ⅱ)로 표시되는 반복단위인 옥시벤조일성분의 반복단위와, 다음 구조식(Ⅲ)으로 표시되는 반복단위와 다음 구조식(Ⅳ)로 표시되는 반복단위인 디옥시성분의 반복단위, 그리고 다음 구조식(Ⅴ)로 표시되는 반복단위와 다음 구조식(Ⅵ)으로 표시되는 반복단위인 디카르복시 성분의 반복단위로 구성되어 있는 것을 특징으로 하는 전방향족 폴리에스테르액정중합체.In the wholly aromatic polyester polymer, the repeating unit represented by the following structural formula (I), the repeating unit represented by the oxybenzoyl component which is the repeating unit represented by the following structural formula (II), the repeating unit represented by the following structural formula (III), and the following Consisting of a repeating unit of the dioxy component, the repeating unit represented by the structural formula (IV), and a repeating unit of the dicarboxy component, the repeating unit represented by the following structural formula (VI) A wholly aromatic polyester liquid crystal polymer, characterized in that.
Figure kpo00003
Figure kpo00003
제1항에 있어서, 상기 옥시벤조일성분의 반복단위는 전체 중합체에 함유되어 있는 반복단위들의 갯수를 기준으로 할때 10∼70%의 구성비율로 이루어져 있고, 상기 디옥시성분의 반복단위는 전체 중합체에 함유되어 있는 반복단위들의 갯수를 기준으로 할때 15∼45%의 구성비율로 이루어져 있으며, 상기 디카르복시 성분의 반복단위는 상기 디옥시성분의 반복단위와 동일한 수로 구성되어 있는 것을 특징으로 하는 전방향족 폴리에스테르액정중합체.According to claim 1, wherein the repeating unit of the oxybenzoyl component consists of 10 to 70% of the constituent ratio based on the number of repeating units contained in the entire polymer, the repeating unit of the deoxy component is the whole polymer Based on the number of repeating units contained in the composition ratio of 15 to 45%, the repeating unit of the dicarboxy component is characterized in that the same number as the repeating unit of the deoxy component Aromatic Polyester Liquid Crystal Polymer. 제1항에 있어서, 상기 구조식(Ⅱ)의 반복단위는 전체 옥시벤조일성분의 반복단위에 대해 10∼70%로 함유되어 있고, 상기 구조식(Ⅲ)의 반복단위는 전체 디옥시성분의 반복단위에 대해 30∼80%로 함유되어 있으며, 상기 구조식(Ⅵ)의 반복단위는 전체 디카르복시 성분의 반복단위에 대해 5∼70%로 함유되어 있는 것을 특징으로 하는 전방향족 폴리에스테르액정중합체.The repeating unit of the structural formula (II) is contained in 10 to 70% of the repeating unit of the total oxybenzoyl component, and the repeating unit of the structural formula (III) It is contained in 30 to 80%, the repeating unit of the formula (VI) is a wholly aromatic polyester liquid crystal polymer, characterized in that contained in 5 to 70% relative to the repeating unit of the total dicarboxy component. 전방향족 폴리에스테르중합체를 제조함에 있어서, 출발물질로 파라히드록시벤조산과 메타히드록시벤조산의 옥시벤조일성분 총 합량 10∼70몰%와, 4,4'-비페놀과 비스-(4-히드록시페닐)설폰의 디옥시성분 총합량 45∼15몰%, 그리고 테레프탈산과 이소프탈산의 디카르복시 성분 총 합량 45∼15몰%를 사용하고, 여기에 초산무수물을 혼합 반응시켜서 제조함을 특징으로 하는 전방향족 폴리에스테르액정중합체의 제조방법.In preparing the wholly aromatic polyester polymer, a total amount of 10 to 70 mol% of the total oxybenzoyl component of parahydroxybenzoic acid and metahydroxybenzoic acid as a starting material, 4,4'-biphenol and bis- (4-hydroxy 45-15 mol% of total dioxy components of phenyl) sulfone and 45-15 mol% of total dicarboxy components of terephthalic acid and isophthalic acid are used, and it is made by mixing and reacting acetic anhydride here. Method for producing aromatic polyester liquid crystal polymer. 제4항에 있어서, 상기 디카르복시 성분은 상기 디옥시성분과 등몰량으로 첨가 사용하는 것을 특징으로 하는 전방향족 폴리에스테르액정중합체의 제조방법.The method for producing an wholly aromatic polyester liquid crystal polymer according to claim 4, wherein the dicarboxy component is added and used in an equimolar amount with the dioxy component.
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