KR20120067523A - Furan type polyester and method for preparing the same - Google Patents

Furan type polyester and method for preparing the same Download PDF

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KR20120067523A
KR20120067523A KR1020100128961A KR20100128961A KR20120067523A KR 20120067523 A KR20120067523 A KR 20120067523A KR 1020100128961 A KR1020100128961 A KR 1020100128961A KR 20100128961 A KR20100128961 A KR 20100128961A KR 20120067523 A KR20120067523 A KR 20120067523A
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furan
based polyester
alkylene group
formula
independently
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KR101715220B1 (en
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이영철
김상용
김백진
김명준
서강진
정지혜
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한국생산기술연구원
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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
    • C08G63/02Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds
    • C08G63/06Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds derived from hydroxycarboxylic acids
    • 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
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J5/00Manufacture of articles or shaped materials containing macromolecular substances
    • C08J5/18Manufacture of films or sheets
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F6/00Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
    • D01F6/58Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products
    • D01F6/62Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products from polyesters

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Abstract

PURPOSE: A furan-based polyester is provided to be manufactured from carboxylic acid and/or alcohol capable of obtaining from biomass, and to provide a container, a film, and fiber. CONSTITUTION: A furan-based polyester is in chemical formula 1 or 2. In chemical formula 1, R^1 and R^2 is respectively C1-9 alkylene group, i and j is respectively 0 or 1, p is an integer from 0-3, R^3 is C2-9 alkylene group, and n is as an integer, a repeat number of a repeating unit. The weight average molecular weight of the furan-based polyester is 5,000-1,000,000. In chemical formula, R^4 is respectively C1-9 alkylene group, w, x, y, and z is respectively as an integer, a repeat number of a repeating unit. The weight average molecular weight of the furan-based polyester is 5,000-1,000,000.

Description

퓨란계 폴리에스터 및 이의 제조방법 {FURAN TYPE POLYESTER AND METHOD FOR PREPARING THE SAME}Furan polyester and manufacturing method thereof {FURAN TYPE POLYESTER AND METHOD FOR PREPARING THE SAME}

본 발명은 폴리에스터에 관한 것으로서, 보다 상세하게는 퓨란계 폴리에스터 및 이의 제조방법에 관한 발명이다.The present invention relates to a polyester, and more particularly, to an furan polyester and a method for producing the same.

지구상의 화석연료를 채취하여 생산과 소비활동에 이용한 후에 최종적으로 이산화탄소(CO2)와 물로 분해되는 것은 현 인류의 생산, 소비패턴이다. 고형물 또한 폐기물로써 방치, 소각 및 분해되어 CO2와 물로 분해된다. 이 결과, 우리를 둘러싸고 있는 지구환경에 CO2와 폐기물을 방출, 축적을 반복하는 '일방통행'으로 지구환경을 악화시켜오고 있다. 한편 바이오매스(biomass)의 이용은 화석연료를 대신하여 지구상의 생물의 생성물을 연료와 원료로서 이용한다. 이용 후 분해 및 소각된 결과 배출되는 CO2는 재차 식물에 흡수되며 또한 폐기물의 형태로 배출된 바이오매스는 에너지 등으로 재이용 된다. 즉, 물질이 순환이 되면서 '탄소순환' 또는 '물질순환'에 의해 CO2나 폐기물이 지구환경에 축적되지 않는다. 바이오매스의 이용은 산업혁명 이래 계속 되어온 화석연료 소비와 CO2, 폐기물 방출 및 축적이라고 하는 '일방통행'을 자연의 메커니즘인 '순환형'으로 되돌린다고 하는 개념이다. It is the current human production and consumption pattern that fossil fuels are collected and used in production and consumption activities and finally decomposed into carbon dioxide (CO 2 ) and water. Solids are also left as waste, incinerated and broken down into CO 2 and water. As a result, the global environment has been deteriorated by a one-way street that emits and accumulates CO 2 and waste in the surrounding environment. On the other hand, the use of biomass uses the products of life on earth as fuel and raw material instead of fossil fuel. The CO 2 emitted as a result of decomposition and incineration after use is absorbed by the plant again, and the biomass discharged in the form of waste is reused as energy. In other words, as the material is circulated, CO 2 or waste is not accumulated in the global environment by 'carbon cycle' or 'material cycle'. The use of biomass is the concept of returning the 'one-way' of fossil fuel consumption, CO 2 and waste emission and accumulation since the Industrial Revolution back to the natural mechanism of circulation.

현재 바이오플라스틱은 대부분 생분해성 포장재로 쓰이고 있다. 바이오플라스틱의 물성(강도, 내구성 등)이 기존의 플라스틱보다 현저히 떨어지기 때문에 다른 소재로는 사용되기 어렵다. 또한 까다로운 공정과 가격면에서 화석원료로부터 얻어진 플라스틱에 비해 경제성이 떨어지기 때문이다. 따라서 새로운 특성을 지닌 바이오 플라스틱 소재개발 및 바이오 플라스틱의 고기능화 기술개발과 가격 경쟁력을 갖는 새로운 바이오 플라스틱 연구 및 개발이 필요한 상황이다.Currently, bioplastics are mostly used as biodegradable packaging. The properties of bioplastics (strength, durability, etc.) are significantly lower than those of conventional plastics, making them difficult to use with other materials. It is also economically inferior to plastics obtained from fossil raw materials in demanding processes and prices. Therefore, it is necessary to develop bioplastic materials with new characteristics, high functionalization technology of bioplastics, and research and development of new bioplastics with price competitiveness.

따라서 본 발명이 이루고자 하는 첫 번째 기술적 과제는 상기 종래기술의 문제점을 해결하기 위하여, 카르복실산 및/또는 알코올로부터 제조될 수 있는 우수한 물성을 갖는 퓨란계 폴리에스터를 제공하는 것이다.Accordingly, the first technical problem to be achieved by the present invention is to provide a furan-based polyester having excellent physical properties that can be prepared from carboxylic acids and / or alcohols in order to solve the problems of the prior art.

본 발명이 이루고자 하는 두 번째 기술적 과제는 카르복실산 및/또는 알코올로부터 상기 퓨란계 폴리에스터를 제조하는 방법을 제공하는 것이다.The second technical problem to be achieved by the present invention is to provide a method for producing the furan-based polyester from carboxylic acid and / or alcohol.

본 발명이 이루고자 하는 세번째 기술적 과제는 상기 퓨란계 폴리에스터로부터 얻을 수 있는 필름, 섬유 및 용기를 제공하는 것이다.The third technical problem to be achieved by the present invention is to provide a film, fiber and a container obtained from the furan-based polyester.

본 발명의 일 측면에 따르면, 본 발명은 하기 화학식 1로 표시되는 퓨란계 폴리에스터를 제공한다.According to one aspect of the present invention, the present invention provides a furan-based polyester represented by the following formula (1).

[화학식 1][Formula 1]

Figure pat00001
Figure pat00001

화학식 1에서,In Formula 1,

R1 및 R2는 각각 독립적으로 C1 -9 알킬렌기, 보다 바람직하게는 C1 -6 알킬렌기, 보다 더욱 바람직하게는 C1 -3 알킬렌기이고,R 1 and R 2 are each independently a C 1 -9 alkylene group, more preferably C 1 -6 alkylene group, still more preferably a C 1 -3 alkylene group,

i 및 j는 각각 독립적으로 0 또는 1이고,i and j are each independently 0 or 1,

p는 0 내지 3의 정수이고,p is an integer from 0 to 3,

R3는 C2 -9 알킬렌기, 보다 바람직하게는 C2 -6 알킬렌기, 보다 더욱 바람직하게는 C3 -5 알킬렌기이고,And R 3 is C 2 -9 alkylene group, more preferably C 2 -6 alkylene group, still more preferably C 3 -5 alkylene group,

n은 정수로서 반복단위의 반복수이고, n is an integer that is the number of repetitions of the repeating unit,

상기 퓨란계 폴리에스터의 중량평균분자량은 5,000 내지 1,000,000이다. The weight average molecular weight of the furan-based polyester is 5,000 to 1,000,000.

본 발명의 다른 일 측면에 따르면, 본 발명은 하기 화학식 2로 표시되는 퓨란계 폴리에스터를 제공한다.According to another aspect of the present invention, the present invention provides a furan-based polyester represented by the following formula (2).

[화학식 2][Formula 2]

Figure pat00002
Figure pat00002

화학식 2에서,In Formula 2,

R4은 각각 독립적으로 C1 -9 알킬렌기, 보다 바람직하게는 C1 -6 알킬렌기, 보다 더욱 바람직하게는 C3 -5 알킬렌기이고, R 4 are each independently C 1 -9 alkylene group, more preferably C 1 -6 alkylene group, still more preferably C 3 -5 alkylene group,

w, x, y 및 z는 각각 독립적으로 정수로서 반복단위의 반복수이고,w, x, y and z are each independently an integer number of repetitions of the repeating unit,

R5는 각각 독립적으로 C1 -9 알킬기, 보다 바람직하게는 C1 -6 알킬기, 보다 더욱 바람직하게는 C1 -3 알킬기이고, R 5 are each independently a C 1 -9 alkyl, more preferably C 1 -6 alkyl group, still more preferably C 1 -3 alkyl,

상기 퓨란계 폴리에스터의 중량평균분자량은 5,000 내지 1,000,000이다. The weight average molecular weight of the furan-based polyester is 5,000 to 1,000,000.

본 발명의 또 다른 일측면에 따르면, 본 발명의 퓨란계 폴리에스터의 제조방법은According to another aspect of the present invention, the method for producing a furan-based polyester of the present invention

2,5-디히드록시메틸퓨란을 준비하는 단계(a);(A) preparing 2,5-dihydroxymethylfuran;

상기 2,5-디히드록시메틸퓨란을 산화반응을 이용하여 퓨란-2,5-디카르복실산으로 제조하는 단계(b); 및(B) preparing the 2,5-dihydroxymethylfuran into furan-2,5-dicarboxylic acid using an oxidation reaction; And

상기 퓨란-2,5-디카르복실산을 하기 화학식 3으로 표시되는 화합물과 하기 화학식 4 및 5로 표시되는 화합물 중에서 선택된 하나 이상으로 반응시켜 퓨란계 폴리에스터를 제조하는 단계(c)를(C) preparing a furan-based polyester by reacting the furan-2,5-dicarboxylic acid with at least one selected from a compound represented by the following Formula 3 and a compound represented by the following Formulas 4 and 5

포함한다..

[화학식 3](3)

Figure pat00003
Figure pat00003

화학식 3에서 R6은 C1 -9 알킬렌기, 보다 바람직하게는 C1 -6 알킬렌기, 보다 더욱 바람직하게는 C3 -5 알킬렌기이고,And R 6 is C 1 -9 alkylene group, more preferably C 1 -6 alkylene group, still more preferably C 3 -5 alkylene group in the formula (3),

[화학식 4][Formula 4]

Figure pat00004
Figure pat00004

화학식 4에서 R7은 각각 독립적으로 C1 -9 알킬렌기, 보다 바람직하게는 C1 -6 알킬렌기, 보다 더욱 바람직하게는 C1 -3 알킬렌기이고, q는 각각 독립적으로 0 또는 1이고,In formula 4 R 7 are each independently C 1 -9 alkylene group, more preferably C 1 -6 alkylene group, still more preferably a C 1 -3 alkylene group, q is each independently 0 or 1,

[화학식 5][Chemical Formula 5]

Figure pat00005
Figure pat00005

화학식 5에서 R8은 각각 독립적으로 C1 -9 알킬기, 보다 바람직하게는 C1 -6 알킬기, 보다 더욱 바람직하게는 C1 -3 알킬기이고, r 및 s는 각각 독립적으로 정수로서 반복단위의 반복수이고, 화학식 5로 표시되는 화합물의 중량평균분자량은 1,000 내지 200,000이다. In formula 5 R 8 are each independently C 1 -9 alkyl, more preferably C 1 -6 alkyl group, and still more preferably a C 1 -3 alkyl group, r and s are repeated in the repeating unit as a constant, each independently The weight average molecular weight of the compound represented by the formula (5) is 1,000 to 200,000.

본 발명의 또 다른 일 측면은 상기 퓨란계 폴리에스터로 제조한 섬유(fiber)를 제공할 수 있다. Another aspect of the present invention can provide a fiber (fiber) made of the furan-based polyester.

본 발명의 또 다른 일 측면은 상기 퓨란계 폴리에스터로 제조한 필름(film) 또는 용기(bottle)를 제공할 수 있다.Another aspect of the present invention may provide a film or a bottle made of the furan-based polyester.

상술한 바와 같이 본 발명은 바이오매스로부터 얻어질 수 있는 카르복실산 및/또는 알코올로부터 제조될 수 있는 우수한 물성을 갖는 퓨란계 폴리에스터를 제공할 수 있고, 바이오매스로부터 얻을 수 있는 카르복실산 및/또는 알코올로부터 상기 퓨란계 폴리에스터를 제조하는 방법을 제공할 수 있으며, 또한 상기 퓨란계 폴리에스터로부터 얻을 수 있는 용기, 필름 및 섬유를 제공할 수 있다.As described above, the present invention can provide a furan-based polyester having excellent physical properties that can be prepared from carboxylic acids and / or alcohols obtainable from biomass, and carboxylic acids obtainable from biomass and It is possible to provide a method for producing the furan-based polyester from the alcohol, and also to provide a container, a film and a fiber which can be obtained from the furan-based polyester.

도 1은 본 발명의 일 실시예에 따른 퓨란계 폴리에스터의 제조방법의 공정을 개략적으로 나타낸 공정도이다.
도 2는 본 발명의 비교예와 실시예에 따라 제조된 퓨란계 폴리에스터의 적외선 스펙트럼을 나타낸 도면이다.
도 3은 본 발명의 비교예와 실시예에 따라 제조된 퓨란계 폴리에스터의 4000~2600 cm-1 적외선 스펙트럼을 나타낸 도면이다.
도 4는 본 발명의 비교예와 실시예에 따라 제조된 퓨란계 폴리에스터의 2000~400 cm-1 적외선 스펙트럼을 나타낸 도면이다.
도 5는 본 발명의 비교예와 실시예에 따라 제조된 퓨란계 폴리에스터의 시차 열분석기(DSC)의 열분석 스펙트럼을 나타낸 도면이다.
1 is a process diagram schematically showing a process of a furan-based polyester manufacturing method according to an embodiment of the present invention.
Figure 2 is a view showing the infrared spectrum of the furan-based polyester prepared according to the comparative example and the embodiment of the present invention.
3 is a view showing a 4000 ~ 2600 cm -1 infrared spectrum of the furan-based polyester prepared according to the comparative example and the embodiment of the present invention.
4 is a view showing a 2000 ~ 400 cm -1 infrared spectrum of the furan-based polyester prepared according to the comparative example and the embodiment of the present invention.
5 is a diagram illustrating a thermal analysis spectrum of a differential thermal analyzer (DSC) of a furan-based polyester prepared according to a comparative example and an embodiment of the present invention.

이하, 본 발명에 따른 퓨란계 폴리에스터, 이의 제조방법 및 이로부터 제조되는 필름 및 섬유 제품의 바람직한 실시예를 첨부도면을 참조하여 상세히 설명하기로 하되, 첨부도면을 참조함에 있어서 동일하거나 대응하는 구성요소는 동일한 도면번호를 부여하고 이에 대한 중복되는 설명은 생략하기로 한다. Hereinafter, with reference to the accompanying drawings, preferred embodiments of the furan-based polyester, a method for producing the same and a film and a fiber product produced therefrom will be described in detail with reference to the accompanying drawings, the same or corresponding configuration Elements are given the same reference numerals and redundant description thereof will be omitted.

또한, 이하에서 사용될 및/또는 이라는 용어는 복수의 관련된 기재된 항목들의 조합 또는 복수의 관련된 기재된 항목들 중의 어느 항목을 포함한다. Also, the term and / or as used below includes any combination of a plurality of related items or any of a plurality of related items.

본 발명의 일 측면에 따르면, 본 발명은 하기 화학식 1로 표시되는 퓨란계 폴리에스터를 제공한다.According to one aspect of the present invention, the present invention provides a furan-based polyester represented by the following formula (1).

[화학식 1][Formula 1]

Figure pat00006
Figure pat00006

화학식 1에서,In Formula 1,

R1 및 R2는 각각 독립적으로 C1 -9 알킬렌기, 보다 바람직하게는 C1 -6 알킬렌기, 보다 더욱 바람직하게는 C1 -3 알킬렌기이고,R 1 and R 2 are each independently a C 1 -9 alkylene group, more preferably C 1 -6 alkylene group, still more preferably a C 1 -3 alkylene group,

i 및 j는 각각 독립적으로 0 또는 1이고,i and j are each independently 0 or 1,

p는 0 내지 3의 정수이고,p is an integer from 0 to 3,

R3는 C2 -9 알킬렌기, 보다 바람직하게는 C2 -6 알킬렌기, 보다 더욱 바람직하게는 C3 -5 알킬렌기이고,And R 3 is C 2 -9 alkylene group, more preferably C 2 -6 alkylene group, still more preferably C 3 -5 alkylene group,

n은 정수로서 반복단위의 반복수이고, n is an integer that is the number of repetitions of the repeating unit,

상기 퓨란계 폴리에스터의 중량평균분자량은 5,000 내지 1,000,000이다. The weight average molecular weight of the furan-based polyester is 5,000 to 1,000,000.

본 발명의 다른 일 측면에 따르면, 본 발명은 하기 화학식 2로 표시되는 퓨란계 폴리에스터를 제공한다.According to another aspect of the present invention, the present invention provides a furan-based polyester represented by the following formula (2).

[화학식 2][Formula 2]

Figure pat00007
Figure pat00007

화학식 2에서,In Formula 2,

R4은 각각 독립적으로 C1 -9 알킬렌기, 보다 바람직하게는 C1 -6 알킬렌기, 보다 더욱 바람직하게는 C3 -5 알킬렌기이고, R 4 are each independently C 1 -9 alkylene group, more preferably C 1 -6 alkylene group, still more preferably C 3 -5 alkylene group,

w, x, y 및 z는 각각 독립적으로 정수로서 반복단위의 반복수이고,w, x, y and z are each independently an integer number of repetitions of the repeating unit,

R5는 각각 독립적으로 C1 -9 알킬기, 보다 바람직하게는 C1 -6 알킬기, 보다 더욱 바람직하게는 C1 -3 알킬기이고, R 5 are each independently a C 1 -9 alkyl, more preferably C 1 -6 alkyl group, still more preferably C 1 -3 alkyl,

상기 화학식 2의 퓨란계 폴리에스터의 중량평균분자량은 5,000 내지 1,000,000이다.The weight average molecular weight of the furan polyester of the formula (2) is 5,000 to 1,000,000.

도 1은 본 발명의 일 실시예에 따른 퓨란계 폴리에스터의 제조방법의 공정을 개략적으로 나타낸 도면이다.1 is a view schematically showing a process of a furan-based polyester manufacturing method according to an embodiment of the present invention.

도 1을 참조하여 설명하면, 본 발명의 또 다른 일 측면에 따른 퓨란계 폴리에스터의 제조방법(S100)은Referring to Figure 1, according to another aspect of the present invention manufacturing method of furan polyester (S100) is

2,5-디히드록시메틸퓨란을 준비하는 단계(S101);Preparing a 2,5-dihydroxymethylfuran (S101);

상기 2,5-디히드록시메틸퓨란을 산화반응을 이용하여 퓨란-2,5-디카르복실산으로 제조하는 단계(S103); 및Preparing 2,5-dihydroxymethylfuran to furan-2,5-dicarboxylic acid using an oxidation reaction (S103); And

상기 퓨란-2,5-디카르복실산을 하기 화학식 3으로 표시되는 화합물과 하기 화학식 4 및 5로 표시되는 화합물 중에서 선택된 하나 이상으로 반응시켜 퓨란계 폴리에스터를 제조하는 단계(S105)를 포함한다.And reacting the furan-2,5-dicarboxylic acid with at least one selected from a compound represented by the following Chemical Formula 3 and a compound represented by the following Chemical Formulas 4 and 5 to prepare a furan-based polyester (S105). .

[화학식 3](3)

Figure pat00008
Figure pat00008

화학식 3에서 R6은 C1 -9 알킬렌기, 보다 바람직하게는 C1 -6 알킬렌기, 보다 더욱 바람직하게는 C3 -5 알킬렌기이고,And R 6 is C 1 -9 alkylene group, more preferably C 1 -6 alkylene group, still more preferably C 3 -5 alkylene group in the formula (3),

[화학식 4][Formula 4]

Figure pat00009
Figure pat00009

화학식 4에서 R7은 각각 독립적으로 C1 -9 알킬렌기, 보다 바람직하게는 C1 -6 알킬렌기, 보다 더욱 바람직하게는 C1 -3 알킬렌기이고, q는 각각 독립적으로 0 또는 1이고,In formula 4 R 7 are each independently C 1 -9 alkylene group, more preferably C 1 -6 alkylene group, still more preferably a C 1 -3 alkylene group, q is each independently 0 or 1,

[화학식 5][Chemical Formula 5]

Figure pat00010
Figure pat00010

화학식 5에서 R8은 각각 독립적으로 C1 -9 알킬기, 보다 바람직하게는 C1 -6 알킬기, 보다 더욱 바람직하게는 C1 -3 알킬기이고, r 및 s는 각각 독립적으로 정수로서 반복단위의 반복수이고, 화학식 5로 표시되는 화합물의 중량평균분자량은 1,000 내지 200,000이다.In formula 5 R 8 are each independently C 1 -9 alkyl, more preferably C 1 -6 alkyl group, and still more preferably a C 1 -3 alkyl group, r and s are repeated in the repeating unit as a constant, each independently The weight average molecular weight of the compound represented by the formula (5) is 1,000 to 200,000.

여기서 단계(S105)는 Where step S105 is

상기 퓨란-2,5-디카르복실산을 화학식 3으로 표시되는 화합물과 반응시키는 단계(S107); 및Reacting the furan-2,5-dicarboxylic acid with a compound represented by Formula 3 (S107); And

상기 단계(S107)의 반응 생성물과 화학식 4 및 5로 표시되는 화합물 중에서 선택된 하나 이상을 반응시켜 퓨란계 폴리에스터를 제조하는 단계(S109)를 포함할 수 있다.It may include a step (S109) of producing a furan-based polyester by reacting the reaction product of the step (S107) with one or more selected from the compounds represented by Formulas 4 and 5.

여기서 단계(S107)는 160 내지 200℃에서 1 내지 10시간 반응시키고, 단계(S109)는 160 내지 200℃에서 1 내지 20시간 반응시키고, 감압하면서 160 내지 200℃에서 0.1 내지 5시간 반응시키고 200 내지 230℃에서 0.1 내지 5시간 반응시키는 것이 바람직하다.Here step (S107) is reacted for 1 to 10 hours at 160 to 200 ℃, step (S109) is reacted for 1 to 20 hours at 160 to 200 ℃, 0.1 to 5 hours at 160 to 200 ℃ reaction under reduced pressure and 200 to It is preferable to make it react at 230 degreeC for 0.1 to 5 hours.

본 발명의 또 다른 일 실시예에 따르면 상기 2,5-디히드록시메틸퓨란은 단당류 또는 다당류 탄수화물로부터 제조된 것임을 특징으로 한다. 바이오매스의 일종인 단당류 또는 다당류 탄수화물로부터 2,5-디히드록시메틸퓨란을 얻을 수 있으며 이러한 바이오매스를 이용하는 방법은 친환경적이다.According to another embodiment of the present invention, the 2,5-dihydroxymethylfuran is characterized in that it is prepared from monosaccharides or polysaccharide carbohydrates. 2,5-dihydroxymethylfuran can be obtained from monosaccharide or polysaccharide carbohydrate, which is a kind of biomass, and the method of using such biomass is environmentally friendly.

본 발명의 또 다른 일 실시예에 따르면 화학식 4 및 5로 표시되는 화합물 중에서 선택된 하나 이상의 화합물은 상기 퓨란-2,5-디카르복실산 100몰부에 대하여 0.001 내지 0.5몰부, 보다 바람직하게는 0.003 내지 0.2몰부이다.According to another embodiment of the present invention at least one compound selected from compounds represented by Formulas 4 and 5 is 0.001 to 0.5 mole parts, more preferably 0.003 to about 100 mole parts of the furan-2,5-dicarboxylic acid 0.2 mole parts.

본 발명의 또 다른 일 실시예에 따르면, 단계(S105)는 용융 축합 반응(melting condensation reaction)시켜 퓨란계 폴리에스터를 제조하는 단계인 것을 특징으로 한다.According to another embodiment of the present invention, step (S105) is characterized in that the step of producing a furan-based polyester by melting condensation reaction (melting condensation reaction).

본 발명의 또 다른 일 실시예에 따르면, 단계(S107) 및 (S109)는 용융 축합 반응(melting condensation reaction)으로 수행되는 단계인 것을 특징으로 한다.According to another embodiment of the present invention, the step (S107) and (S109) is characterized in that the step performed by the melting condensation reaction (melting condensation reaction).

본 발명의 또 다른 일 측면은 상기 퓨란계 폴리에스터로 제조한 섬유(fiber)를 제공할 수 있다. Another aspect of the present invention can provide a fiber (fiber) made of the furan-based polyester.

본 발명의 또 다른 일 측면은 상기 퓨란계 폴리에스터로 제조한 필름(film)을 제공할 수 있다.Another aspect of the present invention may provide a film made of the furan-based polyester.

본 발명의 또 다른 일 측면은 상기 퓨란계 폴리에스터로 제조한 용기를 제공할 수 있다.Another aspect of the present invention can provide a container made of the furan-based polyester.

[실시예][Example]

본 발명에서 구현하고자 하는 퓨란계 폴리에스터, 이의 제조방법 및 이로부터 제조된 필름 및 섬유제품의 바람직한 실시예를 아래에 기재하였으며, 이에 의하여 본 발명이 제한되지는 않는다. Furan-based polyester to be implemented in the present invention, a method for producing the same and a preferred embodiment of the film and fiber products produced therefrom are described below, but the present invention is not limited thereto.

<시약 및 재료><Reagents and Materials>

2,5-Dihydroxymethylfuran (DHMF, 97%)는 바이오매스에서 제조된 것을 PennAKem사에서 구입하여 사용하였고 KMnO4 (99%), NaOH (98%), HCl (35-36%), celite, butane-1,4-diol (BDO, 99%)는 삼전화학에서 구입하였으며 pentaerythritol (99%), pentaerythritol ethoxylate (3/4 EO/OH), PVA (hydrolyzed 80%;Mw 9,500, 87-89%;Mw 18,000)는 Aldrich사에서 구입하여 사용하였다. 촉매로 사용된 Tyzor촉매는 Aldrich사의 titanium(Ⅳ)(triethanolaminato)-isopropoxide를 사용하였다. 이 실험에서 사용한 모든 시료는 별도의 정제 없이 사용하였다.2,5-Dihydroxymethylfuran (DHMF, 97%) was purchased from PennAKem, manufactured by Biomass, and used KMnO 4 (99%), NaOH (98%), HCl (35-36%), celite, butane- 1,4-diol (BDO, 99%) was purchased from Samjeon Chem. Pentaerythritol (99%), pentaerythritol ethoxylate (3/4 EO / OH), PVA (hydrolyzed 80%; M w 9,500, 87-89%; M w 18,000) was purchased from Aldrich. Tyzor catalyst used as a catalyst was titanium (IV) (triethanolaminato) -isopropoxide from Aldrich. All samples used in this experiment were used without further purification.

<합성><Synthesis>

제조예Manufacturing example 1.  One. FuranFuran -2,5--2,5- dicarboxlicdicarboxlic acidacid 의 합성 Synthesis of

1L 비이커에 10%-NaOH (24eq) 수용액 750ml와 DHMF 10g (0.078 mol)을 넣고 상온에서 충분히 교반시킨 후 KMnO4 60g (4.8eq)을 넣고 15분 동안 교반시켰다. 준비된 celite 감압여과를 이용하여 밝은 황색의 투명한 용액을 얻었다. 여과액을 비이커로 옮겨 상온에서 pH 1 이하가 될 때까지 HCl을 적하시켰다. 다시 용액을 감압 여과 하여 침전물과 분리하고 침전물을 증류수로 세척하여 진공오븐에서 건조시켰다. 이 실험에서 밝은 황색의 고체를 얻었으며 수율은 52% 였다 (반응식 1). 합성된 furan-2,5-dicarboxylic acid(FDCA)는 별도의 정제과정 없이 다음 중합반응에 사용하였다.750 ml of 10% -NaOH (24eq) aqueous solution and 10 g (0.078 mol) of DHMF were added to a 1L beaker, and the mixture was sufficiently stirred at room temperature. Then, 60 g (4.8eq) of KMnO4 was added thereto and stirred for 15 minutes. A bright yellow transparent solution was obtained by using the prepared celite vacuum filtration. The filtrate was transferred to a beaker and HCl was added dropwise until the pH was 1 or less at room temperature. The solution was filtered under reduced pressure to separate the precipitate, and the precipitate was washed with distilled water and dried in a vacuum oven. In this experiment a light yellow solid was obtained with a yield of 52% (Scheme 1). The synthesized furan-2,5-dicarboxylic acid (FDCA) was used in the next polymerization without any purification.

[반응식 1][Reaction Scheme 1]

Figure pat00011
Figure pat00011

비교예 1. Poly ( butylene furandicarboxylate ) ( PBF )의 중합 Comparative Example 1. Poly (butylene polymerization of furandicarboxylate ) ( PBF )

모노머 FDCA 5g (0.032mol)에 대하여 BDO 5.7ml (2eq)를 함께 플라스크에 넣고, 180℃, 질소분위기 하에서 4시간 동안 교반하였으며 이 때의 교반속도는 50rpm이였다. Catalyst를 주입하고 9시간 동안 교반하였다. 온도 180℃를 유지하고 질소주입을 중단한 후 감압을 하며 1시간 동안 교반을 하였다. 온도를 210℃까지 올린 후 1시간 동안 교반하였다. 상온, 상압으로 천천히 전환시킨 후 phenol과 TCE를 6:4로 섞은 용매에 녹여 과량의 메탄올에 침전시켜 잔존하는 FDCA를 제거 후 여과시켜 고분자를 회수하였다. 이것을 진공오븐에 건조시켜 연갈색의 고분자 fiber를 얻었다(반응식 2).5.7 ml (2 eq) of BDO was added together to 5 g (0.032 mol) of monomer FDCA, and the mixture was stirred for 4 hours at 180 ° C. under a nitrogen atmosphere. The stirring speed was 50 rpm. Catalyst was injected and stirred for 9 hours. The temperature was maintained at 180 ° C. and the nitrogen injection was stopped, followed by stirring for 1 hour under reduced pressure. The temperature was raised to 210 ° C. and stirred for 1 hour. After slowly converting to room temperature and atmospheric pressure, phenol and TCE were dissolved in a solvent mixed with 6: 4 and precipitated in excess methanol to remove the remaining FDCA and filtered to recover the polymer. This was dried in a vacuum oven to obtain a light brown polymer fiber (Scheme 2).

[반응식 2] Scheme 2

Figure pat00012
Figure pat00012

실시예Example 1.  One. PolyPoly (( butylenebutylene furandicarboxylatefurandicarboxylate -- coco -- pentaerythritolpentaerythritol ) () ( PBFPPBFP )의 중합Polymerization of

모노머 FDCA 5g에 대하여 BDO 5.7ml를 함께 플라스크에 넣고, 180℃, 질소분위기 하에서 4시간 동안 50 rpm으로 교반하였다. Catalyst와 pentaerythritol을 주입하고 9시간 동안 교반하였다. 온도 180℃를 유지하고 질소주입을 중단한 후 감압하면서 1시간, 온도를 210℃까지 올린 후 1시간 동안 교반하였으며 상온, 상압으로 천천히 전환시켰다. Phenol과 TCE를 6:4로 섞은 용매에 녹여 과량의 메탄올에 침전시켜 잔존하는 FDCA를 제거 후 여과시켜 고분자를 회수하였다. 이것을 진공 오븐에 건조시켜 연갈색의 고분자 fiber를 얻었다(반응식 3).5.7 ml of BDO was added together to 5 g of monomer FDCA and stirred at 50 rpm for 4 hours under a nitrogen atmosphere at 180 ° C. Catalyst and pentaerythritol were injected and stirred for 9 hours. The temperature was maintained at 180 ° C., and the nitrogen injection was stopped. Then, the pressure was raised to 210 ° C. for 1 hour, the mixture was stirred for 1 hour, and slowly converted to room temperature and atmospheric pressure. Phenol and TCE were dissolved in a solvent of 6: 4, precipitated in excess methanol to remove residual FDCA, and then filtered to recover the polymer. This was dried in a vacuum oven to obtain a light brown polymer fiber (Scheme 3).

[반응식 3]Scheme 3

Figure pat00013
Figure pat00013

실시예Example 2.  2. PolyPoly (( butylenebutylene furandicarboxylatefurandicarboxylate -- coco -- pentaerythritolpentaerythritol ethoxylateethoxylate ) () ( PBFPEPBFPE )의 중합Polymerization of

단량체 FDCA 5g에 대하여 BDO 5.7ml를 함께 플라스크에 넣고, 180℃, 질소분위기 하에서 4시간 동안 50rpm으로 교반하였다. Catalyst와 pentaerythritol ethoxylate를 주입하고 9시간 동안 교반하였다. 온도 180℃를 유지하며 질소주입을 중단한 후 감압을 하며 1시간 동안 교반을 하였고 온도 210℃에서 1시간 동안 교반하였다. 상온, 상압으로 천천히 전환한 다음 phenol과 TCE를 6:4로 섞은 용매에 녹여 과량의 메탄올에 침전시켜 잔존하는 FDCA를 제거 후 여과시켜 고분자를 회수하였다. 이것을 진공오븐에 건조시켜 연갈색의 고분자 fiber를 얻었다(반응식 4).5.7 ml of BDO was added to the flask with respect to 5 g of monomer FDCA, and stirred at 50 rpm for 4 hours under a nitrogen atmosphere at 180 ° C. Catalyst and pentaerythritol ethoxylate were injected and stirred for 9 hours. After the nitrogen injection was stopped while maintaining the temperature at 180 ° C, the mixture was stirred under reduced pressure and stirred for 1 hour at 210 ° C. After slowly switching to normal temperature and pressure, the mixture was dissolved in a solvent mixed with phenol and TCE 6: 4 and precipitated in excess methanol to remove residual FDCA, and then filtered to recover the polymer. This was dried in a vacuum oven to obtain a light brown polymer fiber (Scheme 4).

[반응식 4]Scheme 4

Figure pat00014
Figure pat00014

실시예Example 3. Poly[ 3. Poly [ butylenebutylene furandicarboxylatefurandicarboxylate -- coco -poly(-poly ( vinylvinyl alcoholalcohol )] ()] ( PBFPVAPBFPVA 80, PBFPVA 88)의 중합 80, polymerization of PBFPVA 88)

단량체 FDCA 5g에 대하여 BDO 5.7ml를 함께 플라스크에 넣고, 180℃, 질소분위기 하에서 4시간 동안 50rpm으로 교반하였다. Catalyst와 PVA 80%를 주입하고 9시간 동안 교반하였다. 온도 180℃를 유지하며 질소주입을 중단한 후 감압을 하며 1시간 동안 교반을 하였고 온도 210℃에서 1시간 동안 교반 하였다. 상온, 상압으로 천천히 전환한 다음 phenol과 TCE 를 6:4로 섞은 용매에 녹여 과량의 메탄올에 침전시켜 잔존하는 FDCA를 제거 후 여과시켜 고분자를 회수하였다. 이것을 진공 오븐에 건조시켜 연갈색의 고분자fiber를 얻었다(반응식 5). 이와 같은 방법으로 PVA 87-89%에 대한 실험도 진행하였다.5.7 ml of BDO was added to the flask with respect to 5 g of monomer FDCA, and stirred at 50 rpm for 4 hours under a nitrogen atmosphere at 180 ° C. 80% of the catalyst and PVA were injected and stirred for 9 hours. After the nitrogen injection was stopped while maintaining the temperature at 180 ° C, the mixture was stirred under reduced pressure for 1 hour and stirred at 210 ° C for 1 hour. After slowly switching to normal temperature and normal pressure, phenol and TCE were dissolved in a solvent mixed with 6: 4 and precipitated in excess methanol to remove residual FDCA and filtered to recover the polymer. This was dried in a vacuum oven to obtain a light brown polymer fiber (Scheme 5). In this way, the experiments were also performed on PVA 87-89%.

[반응식 5]Scheme 5

Figure pat00015
Figure pat00015

<분석><Analysis>

구조확인Check structure

합성된 모노머의 구조를 분석하기 위하여 적외선분광기와 1H-NMR (Bruker, 600MHz)을 사용하였으며 용매는 TMS가 포함된 dimethylsulfoxide-d (99.9 atom% D)를 사용하였다. 또한 중합체를 확인하기 위하여 적외선 분광기와 1H-NMR과 13C-NMR (Bruker, 600MHz)을 사용하였으며 용매는 TMS를 포함한 trifluoroacetic acid-d (99.5 atom% D)를 사용하였다.In order to analyze the structure of the synthesized monomer, an infrared spectrometer and 1 H-NMR (Bruker, 600MHz) were used, and dimethylsulfoxide-d (99.9 atom% D) containing TMS was used. In addition, an infrared spectrometer, 1 H-NMR and 13 C-NMR (Bruker, 600MHz) were used to identify the polymer, and trifluoroacetic acid-d (99.5 atom% D) containing TMS was used as a solvent.

고유점도Intrinsic viscosity

고유점도는 phenol과 1,1,2,2-tetrachloroethane의 부피비를 6:4로 제조한 혼합용매인 PTCE에 측정할 시료를 용해시켜서 0.1~0.5 d/dl의 농도로 5개 시료를 만든 후 Brookfield viscometer로 절대 점도를 측정하여 계산식을 통해 구하였다.Intrinsic viscosity is Brookfield after dissolving the sample to be measured in PTCE, a mixed solvent prepared in 6: 4 by volume ratio of phenol and 1,1,2,2-tetrachloroethane, and making five samples at the concentration of 0.1-0.5 d / dl. Absolute viscosity was measured with a viscometer and calculated through a formula.

열적 특성 조사Thermal Characteristic Investigation

합성한 고분자중합체의 융점(Tm)과 유리전이온도(Tg)를 조사하기 위하여 Differential Scanning Calorimeter(DSC, PerkinElmer)를 사용하였다. DSC를 이용하여 질소분위기 하에 0℃에서 250℃까지 승온속도 10℃/min으로 하여 융점을 측정하였다. 열적안정성을 측정하기 위하여 Thermogravimetric analyzer(TGA, PerkinElmer)를 사용하였으며 TGA를 이용하여 질소분위기 하에 상온에서 800℃까지 시료에 따라 승온속도 10℃/min으로 측정하였다.Differential Scanning Calorimeter (DSC, PerkinElmer) was used to investigate the melting point (T m ) and glass transition temperature (T g ) of the synthesized polymer. The melting point was measured using DSC using a heating rate of 10 ° C./min from 0 ° C. to 250 ° C. under a nitrogen atmosphere. Thermogravimetric analyzer (TGA, PerkinElmer) was used to measure the thermal stability, and the temperature was raised at 10 ℃ / min according to the sample from room temperature to 800 ℃ under nitrogen atmosphere using TGA.

인장강도The tensile strength 측정 Measure

중합된 polyester의 인장강도와 파단신율은 Zwick/Roell사의 Z005를 사용하여 측정하였다. 각 시료의 고분자중합체를 가열유압프레스기를 사용하여 시료의 융점보다 20℃ 높은 온도에서 가열하여 2000 psi로 1분 동안 압착하여 두께가 0.16-0.18 mm의 균일한 필름을 제조하고 dog-bone 형태로 시편을 만들어 측정하였다.Tensile strength and elongation at break of the polymerized polyester were measured using Z005 of Zwick / Roell. The polymer of each sample was heated at a temperature higher than the melting point of the sample by using a heating hydraulic press, and pressed at 2000 psi for 1 minute to prepare a uniform film having a thickness of 0.16-0.18 mm, and in the form of a dog-bone specimen. Was made and measured.

<결과 및 고찰>Results and Discussion

1. One. FuranFuran -2,5--2,5- dicarboxlicdicarboxlic acidacid (( FDCAFDCA )의 합성 ) Synthesis

본 연구에서는 퓨란계 polyester를 중합하기 위하여 모노머를 합성하였다. 2,5-furandimethnaol을 KMnO4로 산화시켜 dicarboxylic acid로서 FDCA를 합성하였다 (반응식 1 참조). In this study, monomers were synthesized to polymerize furan polyester. 2,5-furandimethnaol was oxidized with KMnO 4 to synthesize FDCA as dicarboxylic acid (see Scheme 1).

합성한 FDCA의 1H-NMR 스펙트럼에서 용매는 DMSO를 사용하였으며 13.58(s, Hb, 2H), 7.25(s, Ha, 2H) ppm에서 나타나는 FDCA의 특성 피크를 확인하였고 또한 초기물질에서 확인되었던 CH2의 피크가 사라짐으로써 원하는 모노머가 합성되었음을 알 수 있었다. FDCA 모노머의 FT-IR 스펙트럼에서 초기 물질에서 없었던 1710-1725cm-1의 (-COO-) 피크를 확인하여 합성이 되었음을 알 수 있었다. DSC Thermogram으로서 합성된 모노머의 DSC에 의한 열적 성질 분석을 통하여, FDCA의 융점이 350.2℃임을 알 수 있다.In the 1 H-NMR spectrum of the synthesized FDCA, solvent was used as DMSO, and the characteristic peaks of FDCA which were found at 13.58 (s, Hb, 2H) and 7.25 (s, Ha, 2H) ppm were also identified. By disappearing the peak of 2 , it turned out that the desired monomer was synthesize | combined. From the FT-IR spectrum of the FDCA monomer, the (-COO-) peak of 1710-1725cm -1 , which was not present in the initial material, was confirmed, indicating that the synthesis was performed. Thermal characterization by DSC of the monomer synthesized as DSC Thermogram shows that the melting point of FDCA is 350.2 ° C.

2. 2. 퓨란계Furan 폴리에스터(Furan type Polyester)의Of polyester type (Furan type Polyester) 중합 polymerization

NMRNMR 분석 analysis

본 연구에서는 furan계 모노머인 FDCA와 BDO를 소량의 linker 존재하에 melting condensation시켜 branched polymer를 제조하였고 조성을 분석하기 위해 1H-NMR과 13C-NMR을 이용하여 실험하였다. 용매는 trifluoroacetic acid-d를 사용하였다. 용매의 피크는 11.50(s, OH, 1H)ppm에서 나타난다.In this study, to the furan-based monomer of FDCA and BDO under a small amount of the linker present melting condensation was tested using a 1 H-NMR and 13 C-NMR to analyze the branched polymer composition was prepared. Trifluoroacetic acid-d was used as a solvent. The peak of the solvent is found at 11.50 (s, OH, 1H) ppm.

Polyesters의 중합체는 furan ring의 수소를 기준으로 그 피크에 있는 면적을 적분한 값을 이용하여 각 구조의 수소 조성비를 구하여 1H-NMR을 분석하였다.The polymer of polyesters was analyzed by 1H-NMR by calculating the hydrogen composition ratio of each structure by integrating the area at the peak based on the hydrogen of the furan ring.

PBF는 1H-NMR에서 furan ring에서 기인한 피크가 7.33(m, furan, 2H) ppm, 1,4-butandiol에서 기인한 피크가4.51(m, OCH2, 4H), 1.99(m, CH2, 4H) ppm에서 나타났다.PBF had 7.33 (m, furan, 2H) ppm peaks at 1 H-NMR, 1.1 (m, OCH 2 , 4H) and 1.99 (m, CH 2 ) peaks at 1,4-butandiol. , 4H) ppm.

13C-NMR에서 용매 피크는 122.03, 163.30ppm에서 나타났으며 furan ring에서 기인한 피크는 113.83~119.46(m, furan, 2C), 163.77~164.64(m, furan, 2C), 148.09(s, furan, 2C) ppm에서, 1,4-butandiol에서 기인한 피크는 26.71(s, CH2, 2C), 69.00(s, OCH2, 2C) ppm에서 나타났다.In 13C-NMR, solvent peaks were found at 122.03 and 163.30 ppm, and peaks attributable to furan ring were 113.83 to 119.46 (m, furan, 2C), 163.77 to 164.64 (m, furan, 2C), and 148.09 (s, furan, At 2C) ppm, peaks attributable to 1,4-butandiol were found at 26.71 (s, CH 2 , 2C), 69.00 (s, OCH 2 , 2C) ppm.

PBF외 PBFP, PBFPE, PBFPVA80, PBFPVA88의 구조를 NMR 시험방법으로 확인하였다.The structures of PBFP, PBFPE, PBFPVA80, and PBFPVA88 in addition to PBF were confirmed by NMR test methods.

IRIR 분석 analysis

IR을 통해 중합된 polyesters의 구조를 분석하였다. IR 스펙트럼에서 에스터 결합의 생성결과로 1738 cm-1에서 C=O stretching과 1270 cm-1에서 C-O stretching이 나타났다. 3110 cm-1과1580 cm-1을 통해 furan ring의 C=C 결합을 확인하였다(도 2 내지 4).The structure of the polymerized polyesters was analyzed by IR. As a result of the ester coupling in the IR spectrum, C = O stretching at 1738 cm -1 and CO stretching at 1270 cm -1 . C = C binding of the furan ring was confirmed through 3110 cm −1 and 1580 cm −1 (FIGS. 2 to 4).

고유점도Intrinsic viscosity

합성한 폴리에스터의 고유점도를 측정하기 위해 Brookfield viscometer를 이용하여 절대 점도를 구하였고 변환공식인 식 1에 따라 계산하여 고유점도(intrinsic viscosity, I.V.) 값을 구하여 표 1에 나타내었다. PBF는 0.54의 값을 가지며 PBFP는 0.48, PBFPE는 0.69, PBFPVA80은 0.82, PBFPVA88은 0.64값을 가졌다. PBFP를 제외한 대부분의 linker가 포함된 중합체의 I.V.값이 PBF보다 높은 값을 가지는 것을 알 수 있었다.In order to measure the intrinsic viscosity of the synthesized polyester, absolute viscosity was obtained using a Brookfield viscometer, and the intrinsic viscosity (I.V.) was calculated according to Equation 1, which is shown in Table 1 below. PBF had a value of 0.54, PBFP had 0.48, PBFPE had 0.69, PBFPVA80 had 0.82, and PBFPVA88 had 0.64. It was found that the I.V. value of the polymer containing most linkers except PBFP had a higher value than PBF.

[식 1][Formula 1]

Figure pat00016
Figure pat00016

식 1에서 [η]는 고유점도(intrinsic viscosity, I.V.), ηsp는 비점도(specific viscosity)이고, c는 측정하려는 고분자의 농도이다.In Equation 1, [η] is the intrinsic viscosity (IV), η sp is the specific viscosity, and c is the concentration of the polymer to be measured.

시료sample 고유점도(I.V.)Intrinsic Viscosity (I.V.) 비교예 1(PBF)Comparative Example 1 (PBF) 0.540.54 실시예 1(PBFP)Example 1 (PBFP) 0.480.48 실시예 2(PBFPE)Example 2 (PBFPE) 0.690.69 실시예 3(PBFPVA 80)Example 3 (PBFPVA 80) 0.820.82 실시예 3(PBFPVA 88)Example 3 (PBFPVA 88) 0.640.64

열적 특성Thermal properties

도 5에 폴리에스터 중합체의 DSC thermogram을 나타내었다. PBF의 Tg는 38.5℃였으며 PBFP는 38.0℃, PBFPE는 36.5℃, PBFPVA80은 37.5℃, PBFPVA88은 38.0℃를 확인하였으며 전체적으로 봤을 때 linker가 첨가된 중합체의 경우 PBF의 Tg 보다 밑도는 수치를 나타내었다. PBF의 Tc는 109.8℃였으며 PBFP는 110.5℃, PBFPE는 107.5℃, PBFPVA80은 104.6℃, PBFPVA88은 104.9℃로 나타났으며 linker가 들어간 중합체 대부분이 PBF보다 낮은 Tg를 보였다. PBF의 Tm은 161.5℃이며 PBFP는 160.5℃, PBFPE는 161.5℃, PVAPBF80은 164.1℃, PBFPVA88은 166.8℃로 linker가 PVA로 사용된 중합체가 좀 더 높은 Tm을 나타내었다.5 shows the DSC thermogram of the polyester polymer. The Tg of PBF was 38.5 ° C, PBFP was 38.0 ° C, PBFPE was 36.5 ° C, PBFPVA80 was 37.5 ° C, and PBFPVA88 was 38.0 ° C. The Tc of PBF was 109.8 ° C, PBFP was 110.5 ° C, PBFPE was 107.5 ° C, PBFPVA80 was 104.6 ° C and PBFPVA88 was 104.9 ° C. Most of the polymers containing linker showed lower Tg than PBF. The Tm of PBF was 161.5 ° C, PBFP was 160.5 ° C, PBFPE was 161.5 ° C, PVAPBF80 was 164.1 ° C, and PBFPVA88 was 166.8 ° C.

인장특성 측정Tensile Properties Measurement

FDCA와 BDO및 여러 linker와 중합된 고분자들의 기계적 물성을 측정하였다. 필름 성형 후 dog-bone 형태로 시편을 만들어 인장특성을 측정하였다.The mechanical properties of polymers polymerized with FDCA, BDO and various linkers were measured. Tensile properties were measured after the film was molded in dog-bone form.

Claims (13)

하기 화학식 1로 표시되는 퓨란계 폴리에스터.
[화학식 1]
Figure pat00017

화학식 1에서,
R1 및 R2는 각각 독립적으로 C1 -9 알킬렌기이고,
i 및 j는 각각 독립적으로 0 또는 1이고,
p는 0 내지 3의 정수이고,
R3는 C2 -9 알킬렌기이고,
n은 정수로서 반복단위의 반복수이고,
상기 퓨란계 폴리에스터의 중량평균분자량은 5,000 내지 1,000,000이다.
Furan-based polyester represented by the following formula (1).
[Formula 1]
Figure pat00017

In Formula 1,
R 1 and R 2 are each independently a C 1 -9 alkylene group,
i and j are each independently 0 or 1,
p is an integer from 0 to 3,
And R 3 is C 2 -9 alkylene group,
n is an integer that is the number of repetitions of the repeating unit,
The weight average molecular weight of the furan-based polyester is 5,000 to 1,000,000.
제1항에 있어서,
R1 및 R2는 각각 독립적으로 C1 -6 알킬렌기이고,
R3는 C2 -6 알킬렌기인 것을 특징으로 하는 퓨란계 폴리에스터.
The method of claim 1,
R 1 and R 2 are each independently a C 1 -6 alkyl group,
R 3 is a furan-based polyester, characterized in that C 2 -6 alkylene group.
제2항에 있어서,
R1 및 R2는 각각 독립적으로 C1 -3 알킬렌기이고,
R3는 C3 -5 알킬렌기인 것을 특징으로 하는 퓨란계 폴리에스터.
The method of claim 2,
R 1 and R 2 are each independently a C 1 -3 alkylene group,
R 3 is a furan-based polyester, characterized in that C 3 -5 alkylene group.
하기 화학식 2로 표시되는 퓨란계 폴리에스터.
[화학식 2]
Figure pat00018

화학식 2에서,
R4은 각각 독립적으로 C1 -9 알킬렌기이고,
w, x, y 및 z는 각각 독립적으로 정수로서 반복단위의 반복수이고,
R5는 각각 독립적으로 C1 -9 알킬기이고,
상기 퓨란계 폴리에스터의 중량평균분자량은 5,000 내지 1,000,000이다.
Furan-based polyester represented by the following formula (2).
(2)
Figure pat00018

In Formula 2,
R 4 are each independently C 1 -9 alkylene group,
w, x, y and z are each independently an integer number of repetitions of the repeating unit,
R 5 are each independently a C 1 -9 alkyl,
The weight average molecular weight of the furan-based polyester is 5,000 to 1,000,000.
제4항에 있어서,
R4 는 C1 -6 알킬렌기이고,
R5는 C1 -6 알킬기인 것을 특징으로 하는 퓨란계 폴리에스터.
The method of claim 4, wherein
And R 4 is C 1 -6 alkyl group,
R 5 is a furan-based polyester, characterized in that C 1 -6 alkyl group;
제5항에 있어서,
R4 는 C3 -5 알킬렌기이고,
R5는 C1 -3 알킬기인 것을 특징으로 하는 퓨란계 폴리에스터.
The method of claim 5,
And R 4 is C 3 -5 alkylene group,
R 5 is a furan-based polyester, characterized in that C 1 -3 alkyl.
2,5-디히드록시메틸퓨란을 준비하는 단계(a);
상기 2,5-디히드록시메틸퓨란을 산화반응을 이용하여 퓨란-2,5-디카르복실산으로 제조하는 단계(b); 및
상기 퓨란-2,5-디카르복실산을 하기 화학식 3으로 표시되는 화합물과 하기 화학식 4 및 5로 표시되는 화합물 중에서 선택된 하나 이상으로 반응시켜 퓨란계 폴리에스터를 제조하는 단계(c)를
포함하는 퓨란계 폴리에스터의 제조방법.
[화학식 3]
Figure pat00019

화학식 3에서 R6은 C1 -9 알킬렌기이고,
[화학식 4]

화학식 4에서 R7은 각각 독립적으로 C1 -9 알킬렌기이고, q는 각각 독립적으로 0 또는 1이고,
[화학식 5]
Figure pat00021

화학식 5에서 R8은 각각 독립적으로 C1 -9 알킬기이고, r 및 s는 각각 독립적으로 정수로서 반복단위의 반복수이고, 화학식 5로 표시되는 화합물의 중량평균분자량은 1,000 내지 200,000이다.
(A) preparing 2,5-dihydroxymethylfuran;
(B) preparing the 2,5-dihydroxymethylfuran into furan-2,5-dicarboxylic acid using an oxidation reaction; And
(C) preparing a furan-based polyester by reacting the furan-2,5-dicarboxylic acid with at least one selected from a compound represented by the following Formula 3 and a compound represented by the following Formulas 4 and 5
Method for producing a furan-based polyester comprising.
(3)
Figure pat00019

And R 6 is C 1 -9 alkylene group in the formula (3),
[Chemical Formula 4]

In formula 4 R 7 are each independently C 1 -9 alkylene group, q is each independently 0 or 1,
[Chemical Formula 5]
Figure pat00021

In formula 5 R 8 are each independently C 1 -9 alkyl group, r and s are each independently an integer number of repetitions of the repeating unit, the weight average molecular weight of the compound represented by the formula (5) is 1,000 to 200,000.
제7항에 있어서, 단계(c)는
상기 퓨란-2,5-디카르복실산을 화학식 3으로 표시되는 화합물과 반응시키는 단계(d); 및
상기 단계(d)의 반응 생성물과 화학식 4 및 5로 표시되는 화합물 중에서 선택된 하나 이상을 반응시켜 퓨란계 폴리에스터를 제조하는 단계(e)를
포함하는 것을 특징으로 하는 퓨란계 폴리에스터의 제조방법.
8. The method of claim 7, wherein step (c)
(D) reacting the furan-2,5-dicarboxylic acid with a compound represented by Formula 3; And
(E) preparing a furan polyester by reacting the reaction product of step (d) with at least one selected from compounds represented by Formulas 4 and 5
Method for producing a furan-based polyester comprising a.
제8항에 있어서,
단계(d)는 160 내지 200℃에서 1 내지 10시간 반응시키고,
단계(e)는 160 내지 200℃에서 1 내지 20시간 반응시키고, 감압하면서 160 내지 200℃에서 0.1 내지 5시간 반응시키고 200 내지 230℃에서 0.1 내지 5시간 반응시키는 것을 특징으로 하는 퓨란계 폴리에스터의 제조방법.
The method of claim 8,
Step (d) is reacted for 1 to 10 hours at 160 to 200 ℃,
Step (e) of the furan-based polyester, characterized in that the reaction for 1 to 20 hours at 160 to 200 ℃, 0.1 to 5 hours at 160 to 200 ℃ and 0.1 to 5 hours at 200 to 230 ℃ while reducing the pressure Manufacturing method.
제7항에 있어서,
화학식 4 및 5로 표시되는 화합물 중에서 선택된 하나 이상의 화합물은 상기 퓨란-2,5-디카르복실산 100몰부에 대하여 0.001 내지 0.5몰부인 것을 특징으로 하는 퓨란계 폴리에스터의 제조방법.
The method of claim 7, wherein
At least one compound selected from the compounds represented by Formulas 4 and 5 is a method for producing a furan-based polyester, characterized in that 0.001 to 0.5 mole parts relative to 100 mole parts of the furan-2,5-dicarboxylic acid.
제1항 내지 제6항의 퓨란계 폴리에스터로 제조한 섬유.A fiber made of the furan polyester of claim 1. 제1항 내지 제6항에 따른 퓨란계 폴리에스터로 제조한 필름.A film made of the furan polyester according to claim 1. 제1항 내지 제6항에 따른 퓨란계 폴리에스터로 제조한 용기.
A container made of furan polyester according to claim 1.
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Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR880014004A (en) * 1987-05-13 1988-12-22 스태미카본 베.뷔. Aromatic polyesters and articles made therefrom
WO2010077133A1 (en) * 2008-12-30 2010-07-08 Furanix Technologies B.V. A process for preparing a polymer having a 2,5-furandicarboxylate moiety within the polymer backbone and such (co)polymers
KR20100106505A (en) * 2008-01-31 2010-10-01 사이텍 설패이스 스페셜티즈, 에스.에이. Powder compositon

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR880014004A (en) * 1987-05-13 1988-12-22 스태미카본 베.뷔. Aromatic polyesters and articles made therefrom
KR20100106505A (en) * 2008-01-31 2010-10-01 사이텍 설패이스 스페셜티즈, 에스.에이. Powder compositon
WO2010077133A1 (en) * 2008-12-30 2010-07-08 Furanix Technologies B.V. A process for preparing a polymer having a 2,5-furandicarboxylate moiety within the polymer backbone and such (co)polymers

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