KR101947491B1 - Method of manufacturing polyethyleneterephthalate copolymer - Google Patents
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Abstract
본 발명은 공중합 폴리에스테르의 제조방법에 관한 것으로, 더욱 상세하게는 기존 폴리에틸렌테레프탈레이트 결합을 이루는 에틸렌글라이콜(EG, Ethyleneglycol)과 테레프탈산(TPA, Terephthalic acid) 외에 추가로 폴리에틸렌글라이콜(PEG)의 체인수가 1 내지 50개인 한 방향 말단기로 분자량이 800 내지 50,000인 변성 PDMS(Polydimethylsiloxane)를 도입하여 내마모성이 개선된 공중합 폴리에틸렌테레프탈레이트의 제조방법에 관한 것이다.
이에, 본 발명은 공중합 폴리에틸렌테레프탈레이트 제조 시 폴리에틸렌글라이콜(PEG)의 체인수가 1 내지 50개인 한 방향 말단기로 분자량이 800 내지 50,000인 변성 PDMS를 추가하여 내마모성이 개선된 공중합 폴리에틸렌테레프탈레이트를 제조할 수 있다.More particularly, the present invention relates to a method for producing a copolymerized polyester, and more particularly, to a method for producing a copolymerized polyester by adding polyethylene glycol (PEG (polyethyleneglycol)) to ethylene glycol (EG, Ethyleneglycol) and terephthalic acid ) Having a chain number of 1 to 50 with one terminal block having a molecular weight of 800 to 50,000 is introduced to improve the abrasion resistance of the copolymerized polyethylene terephthalate.
Accordingly, the present invention relates to a process for preparing a copolymerized polyethylene terephthalate having improved wear resistance by adding modified PDMS having a molecular weight of 800 to 50,000 with one end terminal having a number of chains of polyethylene glycol (PEG) of 1 to 50 in the production of the copolymerized polyethylene terephthalate Can be manufactured.
Description
본 발명은 공중합 폴리에스테르의 제조방법에 관한 것으로, 더욱 상세하게는 기존 폴리에틸렌테레프탈레이트 결합을 이루는 에틸렌글라이콜(EG, Ethyleneglycol)과 테레프탈산(TPA, Terephthalic acid) 외에 추가로 폴리에틸렌글라이콜(PEG)의 체인수가 1 내지 50개이며 분자량이 800 내지 50,000인 한 방향 말단기 변성 PDMS(Polydimethylsiloxane)를 도입하여 내마모성이 개선된 공중합 폴리에틸렌테레프탈레이트의 제조방법에 관한 것이다.More particularly, the present invention relates to a method for producing a copolymerized polyester, and more particularly, to a method for producing a copolymerized polyester by adding polyethylene glycol (PEG (polyethyleneglycol)) to ethylene glycol (EG, Ethyleneglycol) and terephthalic acid ) Having a chain number of 1 to 50 and a molecular weight of 800 to 50,000 by introducing PDMS (Polydimethylsiloxane) in one-directional end. The present invention relates to a method for producing a copolymerized polyethylene terephthalate having improved abrasion resistance.
일반적으로, 폴리에스테르 수지, 특히 폴리에틸렌테레프탈레이트 수지는 디카르복실산 또는 이의 에스테르 형성성 유도체 및 디올 또는 이의 에스테르 형성성 유도체로부터 합성되는 선상 고분자로, 가격이 저렴하면서도, 기계적 특성과 화학적 물성이 우수할 뿐만 아니라 가스 차단성 또한 우수하여 각종 용기, 필름, 섬유 등의 제조에 폭 넓게 사용되고 있다. 한편, 폴리에스테르는 축합 중합법으로 제조되는데, 외부 조건에 따른 평형반응으로 고온, 고진공의 조건을 통해 상업적으로 사용 가능한 점도를 얻게 되며, 이때 최종 중합물 내에 일정량의 올리고머가 잔류하게 된다.Generally, polyester resins, especially polyethylene terephthalate resins, are linear polymers synthesized from dicarboxylic acids or ester-forming derivatives thereof and diols or ester-forming derivatives thereof, which are low in cost and excellent in mechanical properties and chemical properties But also has excellent gas barrier properties and is widely used for the production of various containers, films and fibers. On the other hand, the polyester is produced by condensation polymerization method. In the equilibrium reaction according to external conditions, a commercially available viscosity is obtained through high temperature and high vacuum conditions, and a certain amount of oligomer remains in the final polymer.
종래의 폴리에틸렌테레프탈레이트는 타 수지에 비해 내마모성이 약하여 내마모성이 요구되는 분야(수지 사출물, 원사, 필름 등)에 적용하기 어려운 문제점이 있었다.Conventional polyethylene terephthalate has a problem that it is difficult to apply it to a field (resin injection molding, yarn, film, etc.) which requires less abrasion resistance than other resins.
본 발명의 목적은 공중합 폴리에틸렌테레프탈레이트의 제조 시 폴리에틸렌글라이콜(PEG)의 체인수가 1 내지 50개이며 분자량이 800 내지 50,000인 한 방향 말단기 변성 폴리디메틸실록산(PDMS)을 추가로 도입하여 내마모성이 개선된 공중합 폴리에틸렌테레프탈레이트의 제조방법을 제공하는 것이다.It is an object of the present invention to provide a method for producing a copolymerized polyethylene terephthalate by further introducing one-end modified polydimethylsiloxane (PDMS) having a number of chains of polyethylene glycol (PEG) of 1 to 50 and a molecular weight of 800 to 50,000, And a method for producing the improved copolymerized polyethylene terephthalate.
상술한 목적을 달성하기 위한 본 발명의 하나의 양상은, 에틸렌글라이콜(EG, Ethyleneglycol)과 테레프탈산(TPA, Terephthalic acid)의 슬러리(Slurry)화 단계;상기 슬러리의 에스테르화 반응 단계; 및 중축합 반응 단계;를 포함하고, 상기 중축합 반응 후단에 하기 일반식(I)의 폴리에틸렌글라이콜(PEG)의 체인수가 1 내지 50개이며 분자량이 800 내지 50,000인 바람직하게는 분자량이 1,000내지 15,000인 한 방향 말단기 변성 폴리디메틸실록산(PDMS)을 폴리에틸렌테레프탈레이트 반응에 투입하는 것을 특징으로 하는 공중합 폴리에틸렌테레프탈레이트의 제조방법을 제공한다.According to an aspect of the present invention, there is provided a method for producing a slurry of ethylene glycol (EG) and terephthalic acid (TPA), the step of esterifying the slurry, Wherein the number of chains of polyethylene glycol (PEG) represented by the following general formula (I) is 1 to 50, the molecular weight is 800 to 50,000, and the molecular weight is preferably 1,000 (PDMS) in an amount of from 1 to 15,000 is introduced into a polyethylene terephthalate reaction. The present invention also provides a method for producing a copolymerized polyethylene terephthalate.
(I)
(식 중, R= -(CH2-CH2-O)m-, m=1 내지 50(Wherein R = - (CH 2 -CH 2 -O) m-, m = 1 to 50
T= 수산기 또는 카르복실기 또는 아민기)T = a hydroxyl group or a carboxyl group or an amine group)
이때, 변성 폴리디메틸실록산(PDMS)이 공중합 폴리에틸렌테레프탈레이트 총중량에 대하여 0.1 내지 20 중량%, 더욱 바람직하게는 0.5 내지 5 중량%일 수 있다. 이때, 변성 폴리디메틸실록산(PDMS)이 공중합 폴리에틸렌테레프탈레이트 총중량에 대하여 0.1 중량% 미만이면 내마모성이 떨어지고, 20 중량%를 초과하면 기계적 물성이 떨어진다. In this case, the modified polydimethylsiloxane (PDMS) may be 0.1 to 20 wt%, more preferably 0.5 to 5 wt%, based on the total weight of the copolymerized polyethylene terephthalate. At this time, when the modified polydimethylsiloxane (PDMS) is less than 0.1% by weight based on the total weight of the copolymerized polyethylene terephthalate, the abrasion resistance is poor, and when it exceeds 20% by weight, the mechanical properties are poor.
또한, 상기 폴리디메틸실록산(PDMS)의 말단기가 수산기 또는 카르복실기인 것을 특징으로 하는 공중합 폴리에틸렌테레프탈레이트의 제조방법을 제공한다. The present invention also provides a method for producing a copolymerized polyethylene terephthalate, wherein the terminal group of the polydimethylsiloxane (PDMS) is a hydroxyl group or a carboxyl group.
본 발명은 공중합 폴리에틸렌테레프탈레이트 제조 시 한 방향 말단기 변성 PDMS를 추가하여 내마모성이 개선된 공중합 폴리에틸렌테레프탈레이트를 제조할 수 있다.The present invention can produce copolymerized polyethylene terephthalate having improved abrasion resistance by adding unidirectionally short-term modified PDMS when preparing the copolymerized polyethylene terephthalate.
도 1은 마찰마모특성 분석을 위한 마모시험 시편을 나타낸 것이다.
도 2는 마찰마모특성 분석을 위한 마모시험 장치구조를 나타낸 것이다.Fig. 1 shows a wear test specimen for analysis of friction wear characteristics.
2 shows a structure of a wear test apparatus for analyzing friction wear characteristics.
본 발명에 따른 공중합 폴리에틸렌테레프탈레이트의 제조방법은 에틸렌글라이콜(EG, Ethyleneglycol)과 테레프탈산(TPA, Terephthalic acid)의 슬러리(Slurry)화 단계; 에스테르화 반응 단계; 및 중축합 반응 단계;를 포함하고, 상기 중축합 반응 후단에 폴리에틸렌글라이콜의 폴리에틸렌글라이콜(PEG)의 체인수가 1 내지 50개이며 분자량이 800 내지 50,000인 한 방향 말단기 변성 PDMS를 투입하는 것을 특징으로 한다.The method for producing a copolymerized polyethylene terephthalate according to the present invention comprises the steps of slurrying ethylene glycol (EG) and terephthalic acid (TPA); An esterification reaction step; End-modified PDMS having a number of chains of polyethylene glycol (PEG) of polyethylene glycol of 1 to 50 and a molecular weight of 800 to 50,000 at the end of the polycondensation reaction, .
본 발명에서는 상기 변성 PDMS를 폴리에틸렌테레프탈레이트의 내마모 개선 효과를 발현시키기 위하여 중축합 반응 후단에 투입함을 바람직하다. 상기 변성 PDMS를 중축합 반응 후단에 투입할 경우, 결합도 99% 이상을 얻게된다.In the present invention, it is preferable that the modified PDMS is added to the post-polycondensation reaction stage in order to exhibit the anti-abrasion effect of polyethylene terephthalate. When the modified PDMS is introduced into the subsequent stage of the polycondensation reaction, the degree of bonding is 99% or more.
본 발명에서 추가로 투입되는 폴리디메틸실록산은 하기 일반식(I)의 구조를 갖는 것으로 n값은 1 내지 50인 화합물이다.The polydimethylsiloxane further added in the present invention is a compound having the structure of the following general formula (I) and having an n value of 1 to 50.
(I)
(식 중, R= -(CH2-CH2-O)m-, m=1 내지 50(Wherein R = - (CH2-CH2-O) m-, m = 1 to 50
T= 수산기 또는 카르복실기 또는 아민기)T = a hydroxyl group or a carboxyl group or an amine group)
변성 PDMS는 한 방향 말단기가 OH, -COOH 또는 NH2로 구성되어 있으며, 본 발명에서는 OH 또는 -COOH를 사용하여 폴리에틸렌테레프탈레이트에 중합시키는 것을 주 대상으로 하며, 가장 바람직하게는 기존 Diol류 (-OH)기의 중합 결합을 활용하여 OH를 가지는 변성 PDMS를 주 대상으로 하며, 그 예는 하기 화학식과 같다.
[화학식]
[Chemical Formula]
본 발명의 상기 변성 PDMS의 분자량은 800 내지 50,000의 범위인 것이 바람직하고, 더욱 바람직하게는 1,000 내지 15,000일 수 있다. 이 때, 변성 PDMS의 분자량이 800 미만이면 내마모성이 떨어지고, 50,000을 초과하면 중축합 반응성이 떨어지게 된다. 또한 상기 변성 PDMS의 폴리에틸렌글라이콜(PEG)의 체인수가 1 내지 50개를 범위로 하는것이 바람직하며, 더욱 바람직하게는 1 내지 20개일 수 있다. 이 때, 변성 PDMS의 폴리에틸렌글라이콜(PEG)의 체인수가 1개 미만이면 중축합 반응성이 떨어지고 되고, 50개를 초과하면 내마모성이 떨어지게 된다.The molecular weight of the modified PDMS of the present invention is preferably in the range of 800 to 50,000, more preferably 1,000 to 15,000. If the molecular weight of the modified PDMS is less than 800, the abrasion resistance is deteriorated. If the molecular weight exceeds 50,000, the polycondensation reactivity is deteriorated. The number of chains of polyethylene glycol (PEG) in the modified PDMS is preferably in the range of 1 to 50, more preferably 1 to 20. At this time, when the number of chains of polyethylene glycol (PEG) in the modified PDMS is less than 1, the polycondensation reactivity is lowered, and when it exceeds 50, the abrasion resistance is lowered.
본 발명은 중축합 반응 후단에 변성 PDMS를 투입하는 것을 특징으로 한다. The present invention is characterized in that denatured PDMS is introduced into the latter stage of the polycondensation reaction.
상기 변성 PDMS는 폴리에틸렌테레프탈레이트의 내마모 개선 효과를 발현시키기 위하여 중축합 반응 후단에 투입하는 것이 바람직하다. 상기 변성 PDMS를 중축합 반응 후단에 투입할 경우, 결합도 99% 이상을 얻게 된다. 중합물에 도입시 슬러리화 단계 및 에스테르화 반응 단계 또는 중축합 초기 단계에서 투입할 경우, 중합물의 점도 상승이 어렵고 변성 PDMS의 반응율이 낮아 기대효과를 확보하기 어려운 문제가 있다. 또한 중축합 반응 후단 투입 시에도 변성 PDMS에 따른 용융점도가 상승하는 문제가 발생되어 기존 폴리에스터 중합 조건과 달리 중축합 반응 조건을 설정하여야 한다. It is preferable that the modified PDMS is introduced into the latter stage of the polycondensation reaction in order to exhibit the anti-wear effect of the polyethylene terephthalate. When the modified PDMS is introduced into the subsequent stage of the polycondensation reaction, the degree of bonding is 99% or more. It is difficult to increase the viscosity of the polymer and the reaction rate of the modified PDMS is low when it is added in the slurrying step and the esterification reaction step or the initial stage of the polycondensation. Also, when the post-polycondensation reaction is carried out, there is a problem that the melt viscosity of the modified PDMS is increased. Therefore, polycondensation reaction conditions should be set differently from the conventional polyester polymerization conditions.
이때 폴리디메틸실록산의 첨가되는 양은, 공중합 폴리에틸렌테레프탈레이트 총중량에 대하여 0.1 내지 20중량%가 바람직하며, 0.5 내지 5중량%가 보다 바람직하다. 폴리디메틸실록산의 함유량이 0.1 중량% 미만이면 표면으로 마이그레이션되는 양이 적어 내마모성의 개선효과가 미미하며, 함유량이 20 중량%를 초과하면 생산성이 떨어지게 된다.The amount of the polydimethylsiloxane to be added is preferably 0.1 to 20% by weight, more preferably 0.5 to 5% by weight, based on the total weight of the copolymerized polyethylene terephthalate. When the content of the polydimethylsiloxane is less than 0.1% by weight, the amount migrated to the surface is small and the effect of improving the abrasion resistance is insignificant. When the content exceeds 20% by weight, the productivity is decreased.
이하, 본 발명을 하기 실시예에 의거하여 좀더 상세하게 설명한다. 단, 하기 실시예는 본 발명을 예시하기 위한 것일 뿐 한정하지는 않으며, 본 발명의 실시예 및 비교예에서 제조된 사의 물성 평가는 다음과 같은 방법으로 실시하였다.Hereinafter, the present invention will be described in more detail with reference to the following examples. However, the following examples are intended to illustrate the present invention and are not to be construed as limiting the scope of the present invention. The properties of the yarns prepared in Examples and Comparative Examples of the present invention were evaluated in the following manner.
- 트라이볼러지(tribology)특성- tribology characteristic
도 1은 마모시험 시편을, 도 2는 마모 시험 장치 구조를 나타낸 것이다. Fig. 1 shows a wear test specimen, and Fig. 2 shows a wear test apparatus structure.
JIS K7218 방법에 따라 물성을 측정하였다.The physical properties were measured according to JIS K7218 method.
즉, 링 모양의 시편을 시험기에 장착하고 일정한 하중 및 속도를 선정하여 회전시키면 얼마의 힘이 걸리는지와 마모량을 평가하여 마찰마모특성을 분석하였다. 링 모양의 시편은 플라스틱 소재 및 금속(S45C, 구리, SUS 등)이 있고 필요에 따라 다른 소재도 제작이 가능하다. 하중은 0.1 kgf ~ 500 kgf, 속도 1mm/sec ~ 1000 mm/sec 및 마모거리는 1~10km 범위에서 측정하였다.That is, when the ring type specimen was mounted on the tester, and a certain load and speed were selected and rotated, the friction wear characteristics were analyzed by evaluating how much force was applied and the amount of wear. Ring-shaped specimens are made of plastic material and metal (S45C, copper, SUS, etc.) and other materials can be manufactured as required. The load was measured in the range of 0.1 kgf to 500 kgf, the speed of 1 mm / sec to 1000 mm / sec, and the wear distance of 1 to 10 km.
1. Ring-on-ring 평가조건 : 상대제=금속(S45C), 하중=11.8 kgf, 속도=300mm/s, 시간=120min1. Ring-on-ring evaluation condition: Relative agent = metal (S45C), load = 11.8 kgf, speed = 300 mm / s, time = 120 min
2. Pin-on-disk 평가조건 : 상대제=동일수지, 하중=2kgf, 속도=2Hz, 시간=30min2. Pin-on-disk evaluation condition: Relative agent = same resin, load = 2 kgf, speed = 2 Hz, time = 30 min
실시예Example 1 One
테레프탈산 100 중량부에 대하여 에틸렌 글리콜 50 중량부 슬러리를 에스테르화 반응기에 투입하고, 250℃에서 4시간동안 물을 반응기 밖으로 유출시키면서 에스테르화 반응을 진행시켜 비스(2-하이드록시에틸) 테레프탈레이트[bis(2-hydroxyethyl) terephthalate]를 제조하였다. 이때, 인계 내열안정제를 에스테르화 반응 말기에 300ppm 투입하였다. 이후, 중합 촉매로서 안티몬 촉매를 중축합반응 초기에 300ppm을 투입하고, 250℃에서 285℃까지 60℃/hr로 승온함과 동시에, 압력을 0.1torr까지 감압하여 중축합 반응을 진행하였으며, 중축합 반응 후단에 말단기가 수산기이고 폴리에틸렌글라이콜(PEG)의 체인수가 1개이며 분자량이 5,000인 한 방향 말단기 변성 PDMS를 0.5중량% 투입하여 중축합 반응을 진행하여 중합물을 제조하였다. 상기 실시예에서는 JNC사의 FMDA-21 제품을 적용하였다.50 parts by weight of ethylene glycol was added to the esterification reactor to 100 parts by weight of terephthalic acid and the esterification reaction was carried out while allowing water to flow out of the reactor at 250 DEG C for 4 hours to obtain bis (2-hydroxyethyl) terephthalate [bis (2-hydroxyethyl) terephthalate]. At this time, 300 ppm of a phosphorus-based heat stabilizer was added at the end of the esterification reaction. Thereafter, 300 ppm of an antimony catalyst as a polymerization catalyst was added at the initial stage of the polycondensation reaction, the temperature was raised from 250 ° C. to 285 ° C. at 60 ° C./hr, the pressure was reduced to 0.1 torr to conduct a polycondensation reaction, After the end of the reaction, 0.5 wt% of one end of a short-term modified PDMS having a terminal hydroxyl group, a number of chains of polyethylene glycol (PEG) and a molecular weight of 5,000 was added, and a polycondensation reaction was carried out to prepare a polymer. In the above embodiment, the FMDA-21 product of JNC was applied.
상기 제조된 중합물을 260℃에서 압출기를 이용하여 혼런 펠레타이즈를 얻고, 이 펠레타이즈를 105℃에서 4시간 이상 충분히 건조한 후, 250℃에서 사출기를 이용하여 시험편을 제작하였다.The obtained polymer was kneaded at 260 캜 by using an extruder to obtain Horon pelletize, and the pelletized was sufficiently dried at 105 캜 for 4 hours or more, and then a test piece was produced at 250 캜 using an injection machine.
실시예Example 2 2
말단기가 수산기이고 분자량이 5,000인 한 방향 말단기 변성 PDMS를 중축합 반응 후단에 5중량% 투입한 것을 제외하고는 실시예 1과 동일한 방법으로 중합물을 제조하였다.A polymer was prepared in the same manner as in Example 1, except that 5% by weight of the end-group short-term modified PDMS having a hydroxyl group and a molecular weight of 5,000 was added to the end of the polycondensation reaction.
실시예Example 3 3
말단기가 수산기이고 분자량이 15,000인 한 방향 말단기 변성 PDMS를 중축합 반응 후단에 5중량% 투입하여 중축합 반응을 진행하여 실시예 1과 동일한 방법으로 중합물을 제조하였다. 상기 실시예에서는 JNC사의 FMDA-26 제품을 적용하였다.The polymer was prepared in the same manner as in Example 1, except that 5% by weight of short-term modified PDMS having a terminal hydroxyl group and a molecular weight of 15,000 was added to the end of the polycondensation reaction. In the above embodiment, the FMDA-26 product of JNC was applied.
비교예Comparative Example 1 One
변성 PDMS를 투입하지 않은 것을 제외하고는 실시예 1과 같은 방법으로 중합물을 제조하였다.Polymerization was carried out in the same manner as in Example 1 except that denatured PDMS was not added.
표 1에서 나타난 바와 같이 상기 일반식(I)의 폴리에틸렌글라이콜(PEG)의 체인수가 1 내지 20개이며 분자량이 5,000 내지 15,000인 한 방향 말단기 변성 PDMS를 중축합 후단에 투입한 경우, 변성 PDMS를 투입하지 않은 비교예 대비 내마모성이 매우 향상되는 것을 확인 할 수 있었다.As shown in Table 1, when one-directionally short-term modified PDMS having 1 to 20 chains of polyethylene glycol (PEG) represented by the general formula (I) and having a molecular weight of 5,000 to 15,000 was added to the post-polycondensation stage, It was confirmed that the abrasion resistance was significantly improved as compared with the comparative example in which PDMS was not applied.
이상에서 본 발명의 바람직한 실시예에 대하여 상세하게 설명하였으나, 본 발명은 상술한 실시예에 국한되는 것은 아니고, 본 발명의 취지 또는 범위를 벗어나지 않고 본 발명을 다양하게 변경하고 변형할 수 있다는 사실은 당업자에게 자명할 것이다. 따라서, 본 발명의 보호범위는 첨부한 특허청구범위 및 그와 균등한 범위로 정해져야 할 것이다.While the present invention has been particularly shown and described with reference to exemplary embodiments thereof, it is to be understood that the invention is not limited to the disclosed embodiments, but, on the contrary, Will be apparent to those skilled in the art. Therefore, the scope of protection of the present invention should be defined in the appended claims and their equivalents.
Claims (4)
상기 슬러리의 에스테르화 반응 단계; 및
중축합 반응 단계;를 포함하고,
상기 중축합 반응 후단에 하기 화학식으로 표시되고 분자량이 5,000 내지 15,000인 한 방향 말단기 변성 폴리디메틸실록산(PDMS)을 공중합 폴리에틸렌테레프탈레이트 총중량에 대하여 0.5 내지 5중량% 투입하여 공중합 폴리에틸렌테레프탈레이트를 제조하는 단계를 포함하며,
상기 공중합 폴리에틸렌테레프탈레이트는 링-온-링(ring-on-ring) 조건의 동마찰계수가 0.04~0.15이고, 핀-온-디스크(pin-on-disk) 조건의 동마찰계수가 0.03~0.13인 것을 특징으로 하는 공중합 폴리에틸렌테레프탈레이트의 제조방법.
[화학식]
Slurrying of ethylene glycol (EG, Ethyleneglycol) and terephthalic acid (TPA, terephthalic acid);
An esterification reaction step of the slurry; And
A polycondensation reaction step,
(PDMS) represented by the following chemical formula and having a molecular weight of 5,000 to 15,000 at 0.5 to 5% by weight based on the total weight of the copolymerized polyethylene terephthalate, ≪ / RTI >
The copolymer polyethylene terephthalate has a kinetic friction coefficient in a ring-on-ring condition of 0.04 to 0.15 and a dynamic friction coefficient in a pin-on-disk condition of 0.03 to 0.13 Wherein the copolymer is polyethylene terephthalate.
[Chemical Formula]
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| JP2624060B2 (en) | 1991-10-09 | 1997-06-25 | 信越化学工業株式会社 | One-end diol siloxane compound and method for producing the same |
| JP3583557B2 (en) | 1996-08-12 | 2004-11-04 | タキロン株式会社 | Method for producing additive-containing thermoplastic resin molded article |
| JP2008274182A (en) * | 2007-05-07 | 2008-11-13 | Teijin Fibers Ltd | Method for producing polyethylene naphthalate resin |
| KR101473085B1 (en) | 2013-02-07 | 2014-12-15 | 주식회사 효성 | Preparation Method of Polyethylene Polyester based Polymer |
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Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2624060B2 (en) | 1991-10-09 | 1997-06-25 | 信越化学工業株式会社 | One-end diol siloxane compound and method for producing the same |
| JP3583557B2 (en) | 1996-08-12 | 2004-11-04 | タキロン株式会社 | Method for producing additive-containing thermoplastic resin molded article |
| JP2008274182A (en) * | 2007-05-07 | 2008-11-13 | Teijin Fibers Ltd | Method for producing polyethylene naphthalate resin |
| KR101473085B1 (en) | 2013-02-07 | 2014-12-15 | 주식회사 효성 | Preparation Method of Polyethylene Polyester based Polymer |
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| Title |
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