KR930004621B1 - Process for preparation of polyarylene sulfide polymer - Google Patents

Process for preparation of polyarylene sulfide polymer Download PDF

Info

Publication number
KR930004621B1
KR930004621B1 KR1019890017796A KR890017796A KR930004621B1 KR 930004621 B1 KR930004621 B1 KR 930004621B1 KR 1019890017796 A KR1019890017796 A KR 1019890017796A KR 890017796 A KR890017796 A KR 890017796A KR 930004621 B1 KR930004621 B1 KR 930004621B1
Authority
KR
South Korea
Prior art keywords
water
polymer
polymerization
arylene sulfide
sulfide polymer
Prior art date
Application number
KR1019890017796A
Other languages
Korean (ko)
Other versions
KR910011948A (en
Inventor
김낙중
정문조
박건유
성 박
이범용
Original Assignee
한국과학기술연구원
박원희
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 한국과학기술연구원, 박원희 filed Critical 한국과학기술연구원
Priority to KR1019890017796A priority Critical patent/KR930004621B1/en
Publication of KR910011948A publication Critical patent/KR910011948A/en
Application granted granted Critical
Publication of KR930004621B1 publication Critical patent/KR930004621B1/en

Links

Classifications

    • 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
    • C08G61/00Macromolecular compounds obtained by reactions forming a carbon-to-carbon link in the main chain of the macromolecule
    • C08G61/02Macromolecular compounds containing only carbon atoms in the main chain of the macromolecule, e.g. polyxylylenes
    • C08G61/10Macromolecular compounds containing only carbon atoms in the main chain of the macromolecule, e.g. polyxylylenes only aromatic carbon atoms, e.g. polyphenylenes
    • 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
    • C08G75/00Macromolecular compounds obtained by reactions forming a linkage containing sulfur with or without nitrogen, oxygen, or carbon in the main chain of the macromolecule
    • C08G75/02Polythioethers

Landscapes

  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Polymers With Sulfur, Phosphorus Or Metals In The Main Chain (AREA)

Abstract

The arylene sulfide polymer is prepared by (1) reacting an alkali metal sulfide and polyhalogenated aromatic compound in an organic amide solvent, (2) dehydrating the reactant by distillation, (3) filtering the dehydrated and washing with methanol and hot water, and (4) drying. The absorbent packed into the aborbing tower is phosphorus pentoxide, zeolite, magnesium perchlorate, gamma-alumina, manganese dioxide, silica gel, sulfuric acid or their mixture. The polymer is useful for electronic and electric components and molded articles such as films, sheets and fibers.

Description

아릴렌설파이드 중합체의 제조방법Process for preparing arylene sulfide polymer

본 발명은 아릴렌설파이드 중합체의 제조방법에 관한 것으로서, 아릴렌설파이드의 제조과정에서 중합반응이 진행됨에 따라 알칼리금속황화물로부터 유리되는 결정수를 제거함으로써, 중합속도를 증진시킬 뿐만 아니라 생성되는 중합체의 분자량을 증가시킬 수 있는 아릴렌설파이드 중합체의 제조방법에 관한 것이다.The present invention relates to a method for preparing an arylene sulfide polymer, wherein by removing the crystal water liberated from alkali metal sulfides as the polymerization reaction proceeds in the preparation of the arylene sulfide, the polymerization rate of the resulting polymer The present invention relates to a method for preparing an arylene sulfide polymer capable of increasing molecular weight.

아릴렌설파이드 중합체는 1967년 미국 필립스 석유회사에서 상업적 생산공정을 발명(USP3354129)한 이래 중합체의 우수한 내열성으로 인하여 전기, 전자, 자동차 등의 분야에서 사용되어 왔으며, 1975년 고분자량의 중합체 합성법이 발명(USP3919177)된 후 내열성 필름이나 섬유등의 용도로도 사용이 되고 있는 고분자 물질이다. 현재 널리 사용되고 있는 중합방법은 파라디클로로벤젠과 알칼리금속황화물을 유기아미드 용매중에서 축중합 반응시켜 아릴렌설파이드 중합체를 제조하는 방법이다.Arylene sulfide polymers have been used in the fields of electricity, electronics, automobiles, etc. due to the excellent heat resistance of the polymers since the invention of the USP3354129 by Philips Petroleum Company in 1967, and in 1975, high molecular weight polymer synthesis was invented. (USP3919177) After being used, it is a polymer material that is also used for heat-resistant films and fibers. The polymerization method currently widely used is a method for preparing arylene sulfide polymers by condensation polymerization of paradichlorobenzene and alkali metal sulfides in an organic amide solvent.

Figure kpo00001
Figure kpo00001

이러한 방법 이외에도 알칼리금속황화물을 대신 알칼리금속의 이황화물등 기타 황화합물 사용하는 방법(USP3869433)도 발표되어 있으며, 파라디클로로벤젠 대신 디클로로나프탈렌등 다른 방향족 염화물을 사용하는 방법도 발표되어 있다.In addition to these methods, the use of other sulfur compounds such as alkali metal disulfides (USP3869433) instead of alkali metal sulfides has also been published, and the use of other aromatic chlorides such as dichloronaphthalene in place of paradichlorobenzene has also been disclosed.

최근에는 원료물질의 변화보다는 중합체의 분자량을 증가시키는 합성법을 개발하는 방향으로 연구가 수행되고 있으며, 분자량을 높이는 방법으로는 중합기능기가 3개인 삼염화방향족 화합물을 소량 첨가하여 가교 결합을 도입하는 방법(USP3354129)과 알칼리금속 카르복시산, 알칼리금속 수산화물, 탄산리튬 등의 촉매물질을 사용하는 방법(USP3919177)이 발표되어 있다.Recently, research has been conducted to develop a synthetic method of increasing the molecular weight of a polymer rather than a change of raw materials.A method of increasing the molecular weight is a method of introducing a crosslinking bond by adding a small amount of trichloroaromatic compound having three polymerization functional groups ( USP3354129) and a method of using a catalytic material such as alkali metal carboxylic acid, alkali metal hydroxide, lithium carbonate (USP3919177) are disclosed.

본 발명은 아릴렌설파이드 중합체의 분자량을 증가시키는 방법에 관한 것으로서, 종래의 방법은 반응혼합물 중에 촉매나 반응물질을 첨가함으로써 중합체의 분자량을 증가시킨 반면, 본 발명은 반응원료 물질은 동일하게 사용하면서 단지 중합반응중에 탈수과정을 도입함으로써 중합체의 분자량을 증가시키는 것을 특징으로 한다.The present invention relates to a method for increasing the molecular weight of an arylene sulfide polymer, while the conventional method increases the molecular weight of a polymer by adding a catalyst or a reactant in a reaction mixture, while the present invention uses the same reaction raw material. It is characterized by increasing the molecular weight of the polymer by only introducing a dehydration process during the polymerization reaction.

본 발명을 보다 상세히 설명하면 다음과 같다. 현재 널리 사용되고 있는 중합방법은 디할로 치환 방향족 화합물로서 파라디클로로벤젠을 사용하고 알칼리금속화합물로서 황화나트륨을 사용하고 용매로서 N-메틸-2-피를리돈을 사용하고 있다. 황산나트륨은 통상 분자당 6-9분자의 결정수를 포함하고 있으며, 이 결정수를 제거한 후 중합반응을 시작하게 된다. 결정수를 제거하는 방법으로는 황화나트륨을 유기아미드 용매에 용해시킨후 증류하는 방법(USP3354129)이 사용되고 있다.Hereinafter, the present invention will be described in detail. Currently widely used polymerization methods use paradichlorobenzene as a dihalo substituted aromatic compound, sodium sulfide as an alkali metal compound, and N-methyl-2-pyridone as a solvent. Sodium sulfate usually contains 6-9 molecules of crystallized water per molecule. After removing the crystallized water, the polymerization reaction starts. As a method of removing crystalline water, a method of dissolving sodium sulfide in an organic amide solvent and then distilling (USP3354129) is used.

그러나 황화나트륨의 결정수는 증류후에도 완전히 제거되지 않으며, 증류조건에 따라 황화나트륨 1분자당 0.5-2.5분자의 결정수가 황화나트륨과 유기아미드 용매와 착화합물을 이루어 잔류하게 된다.However, the crystallized water of sodium sulfide is not completely removed even after distillation, and depending on the distillation conditions, 0.5-2.5 molecules of crystallized water remain as a complex compound with sodium sulfide and an organic amide solvent.

이 착화합물과 파라디클로로벤젠을 반응기에 넣고 중합하면, 중합이 진행됨에 따라 착화합물이 가지고 있는 물이 유리되어 반응물 내에 존재하게 된다. 이 유리된 물은 중합체의 분자량이 증가하는 것을 억제한다. 따라서 본 발명은 이 유리된 물을 중합반응계로부터 효과적으로 제거함으로써 반응속도를 증진시킬뿐 아니라 중합체의 유기용매에 대한 용해도를 증진시켜 중합체의 분자량을 증가시키는 중합방법에 관한 것이다.When the complex compound and paradichlorobenzene are put into a reactor and polymerized, as the polymerization proceeds, the water of the complex compound is released and is present in the reactant. This liberated water inhibits the increase in molecular weight of the polymer. Accordingly, the present invention relates to a polymerization method for increasing the molecular weight of a polymer by enhancing the reaction rate as well as enhancing the solubility of the polymer in an organic solvent by effectively removing the liberated water from the polymerization reaction system.

본 발명에서 물을 제거하는 방법으로는 반응기에 증류탑을 설치하여 반응이 진행되는 동안 계속하여 반응물을 증류하여 물을 분리하는 방법이다. 제올라이트 등의 흡습제를 충전한 흡수탑을 반응기에 설치하여 반응용매를 기체상태 혹 액체상태로 흡수제와 접촉시켜 반응용매중에서 유리된 물을 제거하는 방법, 또는 반응혼합물을 직접 흡습제와 접촉시켜 물을 제거하는 방법이 사용된다.In the present invention, a method of removing water is to install a distillation column in a reactor to continuously distill the reactant to separate water while the reaction is in progress. Absorption column filled with an absorbent such as zeolite is installed in the reactor and the reaction solvent is contacted with the absorbent in gas or liquid state to remove free water from the reaction solvent, or the reaction mixture is directly contacted with the absorbent to remove water. Method is used.

본 발명을 실시예를 들어 설명하면 다음과 같다.An embodiment of the present invention will be described as follows.

[실시예 1]Example 1

1ι의 사구 플라스크에 증류탑을 설치하고, 황화나트륨(46.5%) 126g과 수산화나트륨 0.5g, N-메틸-2-피롤리돈 250g을 넣고 질소기류하에서 가열하여 혼합물의 온도가 206℃가 될때까지 증류하여 물을 제거하였다.A distillation column was installed in a 1ι four-necked flask, and 126 g of sodium sulfide (46.5%), 0.5 g of sodium hydroxide, and 250 g of N-methyl-2-pyrrolidone were heated under nitrogen stream, and distilled until the temperature of the mixture reached 206 ° C. Water was removed.

이때 제거된 물의 양은 50g이다. 이상과 같은 방법으로 제조한 탈수된 혼합물을 150℃까지 냉각한 후 여기에 p-디클로로벤젠 112.5g과 N-메틸-2-피롤리돈 50g을 넣고, 비등점에서 환류시키며 중합과정에서 유리되는 물을 증류제거하면서 5시간 동안 중합하였다.The amount of water removed is 50 g. The dehydrated mixture prepared by the above method was cooled to 150 ° C, and then 112.5 g of p-dichlorobenzene and 50 g of N-methyl-2-pyrrolidone were added thereto, refluxed at a boiling point, and water liberated during the polymerization process. The polymerization was carried out for 5 hours while distilling off.

생성된 중합체 혼합물을 여과하여 메탄올과 뜨거운 물로 세척한 후 80℃ 진공 건조기에서 밤새 건조하여 고유점도가 0.24dl/g인 백색의 아릴렌설파이드 중합체 45g을 얻었다.The resulting polymer mixture was filtered, washed with methanol and hot water, and dried overnight in a vacuum dryer at 80 ° C. to obtain 45 g of a white arylene sulfide polymer having an intrinsic viscosity of 0.24 dl / g.

[비교예 1]Comparative Example 1

한편 실시예 1과 동일한 조성의 혼합물을 넣고, 중합반응 과정에서 유리된 물을 증류조작으로 제거하지 않는 외는 실시예 1과 동일하게 6시간 중합하여, 고유점도가 0.10dl/g인 백색의 아릴렌설파이드 중합체를 얻었다.On the other hand, a mixture of the same composition as in Example 1 was added, and polymerization was performed for 6 hours in the same manner as in Example 1 except that the water liberated in the polymerization process was not removed by distillation, and thus white arylene having an intrinsic viscosity of 0.10 dl / g was used. A sulfide polymer was obtained.

[실시예 2]Example 2

실시예 1에서와 같은 방법으로 제조한 탈수된 혼합물과 p-디클로로벤젠 112.5g과 N-메틸-2-피롤리돈 50g을 증류탑이 설치된 고압반응기에 넣고 중합과정에서 유리되는 물을 제거하면서(증류에 의하여 제거된 물의 양은 15.5g이었음) 700kpa 260℃에서 3시간 30분동안 중합하였다. 이후 실시예 1에서와 동일한 방법으로 세척 건조하여 고유점도가 0.25dl/g인 백색의 아릴렌설파이드 중합체 74g을 얻었다.A dehydrated mixture prepared in the same manner as in Example 1, 112.5 g of p-dichlorobenzene and 50 g of N-methyl-2-pyrrolidone were placed in a high pressure reactor equipped with a distillation column while removing water liberated during polymerization (distillation). The amount of water removed by 15.5 g) was polymerized at 700 kpa 260 ° C. for 3 hours 30 minutes. Thereafter, washing and drying were performed in the same manner as in Example 1 to obtain 74 g of a white arylene sulfide polymer having an intrinsic viscosity of 0.25 dl / g.

[비교예 2]Comparative Example 2

한편 실시예 2와 동일한 조성의 혼합물을 넣고, 중합과정 중에 유리되는 물을 증류조작으로 제거하지 않는 외는 실시예 2와 동일하게 4시간 동안 중합하여, 고유점도가 0.18dl/g인 백색의 아릴렌설파이드 중합체를 얻었다.Meanwhile, a mixture of the same composition as in Example 2 was added, except that water freed during the polymerization process was not removed by distillation, and then polymerized for 4 hours in the same manner as in Example 2, with a white arylene having an intrinsic viscosity of 0.18 dl / g A sulfide polymer was obtained.

[실시예 3]Example 3

증류탑이 설치된 1ι의 고압반응기에 황화나트륨(46.5%) 126g과 수산화나트륨 0.5g, 리튬아세테이트 76.5g N-메틸-2-피롤리돈 250g을 넣고 질소기류하에서 가열하여 혼합물의 온도가 200℃가 될때까지 증류하여 78g의 물을 제거하였다. 이러한 방법으로 제조한 탈수된 혼합물에 p-디클로로벤젠 112.5g과, N-메틸-2-피롤리돈 50g을 넣고 중합과정에서 유리되는 물을 제거하면서(증류에 의하여 제거된 물의 양은 15.5g이었음) 260℃에서 3시간 30분 동안 중합한 후 실시예 1에서와 같은 방법으로 세척, 건조하여 고유점도가 0.49dl/g인 백색의 아릴렌설파이드 중합체 77g을 얻었다.In a high pressure reactor equipped with a distillation column, 126 g of sodium sulfide (46.5%), 0.5 g of sodium hydroxide, and 76.5 g of lithium acetate, 250 g of N-methyl-2-pyrrolidone were heated under nitrogen stream, and the mixture became 200 ° C. Distilled to remove 78 g of water. 112.5 g of p-dichlorobenzene and 50 g of N-methyl-2-pyrrolidone were added to the dehydrated mixture prepared in this manner, and the water liberated during the polymerization was removed (the amount of water removed by distillation was 15.5 g). After polymerization at 260 ° C. for 3 hours 30 minutes, washing and drying were carried out in the same manner as in Example 1 to obtain 77 g of a white arylene sulfide polymer having an intrinsic viscosity of 0.49 dl / g.

[비교예 3]Comparative Example 3

한편 실시예 3과 동일한 조성의 혼합물을 넣고, 중합반응 과정에서 유리되는 물을 증류조작으로 제거하지 않는 외는 실시예 3과 동일하게 4시간 중합하여 고유점도가 0.34dl/g인 백색의 아릴렌설파이드 중합체를 얻었다.Meanwhile, a mixture of the same composition as in Example 3 was added, except that the water liberated in the polymerization process was not removed by distillation. The polymerization was carried out for 4 hours in the same manner as in Example 3 to give a white arylene sulfide having an intrinsic viscosity of 0.34 dl / g. A polymer was obtained.

[실시예 4]Example 4

증류탑이 설치된 1ι의 고압반응기에 황화나트륨(46.5%) 126g과 수산화나트륨 0.5g, 리튬아세테이트 76.5g, N-메틸-2-피롤리돈 250g을 넣고 질소기류하에서 가열하여 혼합물의 온도가 206℃가 될때까지 증류하여 71g의 물을 제거하였다. 여기에 100g의 p-디클로로벤젠과 m-디클로로벤젠 11g, 트리클로로벤젠 1.0g, N-메틸-2-피롤리돈 50g을 넣고 고압반응기에 설치된 증류탑 내에 제올라이트(몰레큘라시브 4A)를 충전하여 중합과정에서 유리되는 물을 제올라이트에 흡수제거하면서 260℃에서 3시간 30분 동안 중합한 후 실시예 1에서와 같은 방법으로 세척, 건조하여 고유점도가 0.4dl/g인 백색의 아릴렌설파이드 중합체 76g을 얻었다.In a high pressure reactor equipped with a distillation column, 126 g of sodium sulfide (46.5%), 0.5 g of sodium hydroxide, 76.5 g of lithium acetate, and 250 g of N-methyl-2-pyrrolidone were heated under a nitrogen stream, and the mixture was heated at 206 ° C. Distilled to remove 71 g of water. 100 g of p-dichlorobenzene, 11 g of m-dichlorobenzene, 1.0 g of trichlorobenzene, and 50 g of N-methyl-2-pyrrolidone were charged, and the zeolite (molecular 4A) was charged into a distillation column installed in a high pressure reactor to polymerize. 76 g of a white arylene sulfide polymer having an intrinsic viscosity of 0.4 dl / g was polymerized by polymerization in 260 ° C. for 3 hours and 30 minutes while absorbing and removing water liberated in the process. Got it.

[비교예 4][Comparative Example 4]

한편, 실시예 4와 동일한 조성의 혼합물을 넣고, 중합반응 과정에서 유리되는 물을 제올라이트에 흡수 제거하지 않는 외는 실시예 4와 동일하게 4시간 중합하여 고유점도가 0.3dl/g인 백색의 아릴렌설파이드 중합체를 얻었다.On the other hand, a mixture of the same composition as in Example 4 was added, except that the water liberated in the polymerization process was not absorbed and removed from the zeolite for 4 hours in the same manner as in Example 4 to give a white arylene having an intrinsic viscosity of 0.3 dl / g. A sulfide polymer was obtained.

[실시예 5]Example 5

증류탑이 설치된 1ι의 고압반응기에 황화나트륨(46.5%) 126g과 수산화나트륨 0.5g, 리튬아세테이트 76.5g, N-메틸-2-피롤리돈 250g을 넣고 질소기류하에서 가열하여 혼합물의 온도가 210℃가 될때까지 증류하여 71g의 물을 제거하였다. 여기에 224g의 비스 p-클로로페닐술폰과, N-메틸-2-피롤리돈 50g을 넣고 실시예 4에서와 동일한 방법으로 중합과정에서 유리되는 물을 제거하면서 200℃에서 3시간 30분 동안 중합한 후, 실시예 1에서와 같은 방법으로 세척, 건조하여 고유점도가 0.45dl/g인 백색의 아릴렌설파이드 중합체 167g을 얻었다.In a high pressure reactor equipped with a distillation column, 126 g of sodium sulfide (46.5%), 0.5 g of sodium hydroxide, 76.5 g of lithium acetate, and 250 g of N-methyl-2-pyrrolidone were heated under a nitrogen stream. Distilled to remove 71 g of water. 224 g of bis p-chlorophenylsulfone and 50 g of N-methyl-2-pyrrolidone were added thereto, and polymerization was performed at 200 ° C. for 3 hours and 30 minutes while removing water liberated in the polymerization process in the same manner as in Example 4. Thereafter, the resultant was washed and dried in the same manner as in Example 1 to obtain 167 g of a white arylene sulfide polymer having an intrinsic viscosity of 0.45 dl / g.

[비교예 5][Comparative Example 5]

한편 실시예 5와 동일한 조성의 혼합물을 사용하고 중합과정에서 유리되는 물을 제거하지 않는 외는 실시예 4에서와 동일한 방법으로 4시간 중합하여 고유점도 0.37dl/g인 백색의 아릴렌설파이드 중합체를 얻었다.Meanwhile, except that the mixture having the same composition as in Example 5 and not removing water liberated in the polymerization process was polymerized for 4 hours in the same manner as in Example 4 to obtain a white arylene sulfide polymer having an intrinsic viscosity of 0.37 dl / g. .

상기 실시예 및 비교예로부터 본 발명에서와 같이 반응계로부터 중합과정에서 유리되는 물을 제거하면서 중합시키면, 모든 반응 조건이 동일하고 단지 중합반응에서 유리되는 물을 제거치 않는 비교예보다 생성물의 고유점도가 30% 정도 상승됨으로서 미루어 보아 그만큼 중합도가 증가하게 되며, 중합시간도 10% 정도 단축되는 효과 있음을 알 수 있다.When the polymerization is carried out by removing the water liberated in the polymerization process from the reaction system as in the present invention from the above examples and comparative examples, the intrinsic viscosity of the product than the comparative example that all the reaction conditions are the same and does not remove the free water in the polymerization reaction Since the increase of about 30%, the degree of polymerization increases accordingly, and it can be seen that the polymerization time is also reduced by about 10%.

Claims (3)

유기아미드 용매중에서 알칼리금속황화물과 다할로 치환 방향족 화합물을 반응시켜 아릴렌설파이드 중합체를 얻는 방법에 있어서, 중합반응이 진행됨에 따라 알칼리금속황화물로부터 유리되는 물을 반응계로부터 제거함을 특징으로 하는 아릴렌설파이드 중합체의 제조방법.A method of obtaining an arylene sulfide polymer by reacting an alkali metal sulfide with a polyhalo substituted aromatic compound in an organic amide solvent, wherein the water liberated from the alkali metal sulfide is removed from the reaction system as the polymerization reaction proceeds. Method of Making Polymers. 제1항에 있어서, 물을 제거하는 방법이 증류조작인 아릴렌설파이드 중합체의 제조방법.The method for producing an arylene sulfide polymer according to claim 1, wherein the method of removing water is distillation. 제1항에 있어서, 물을 제거하는 방법이 오산화인, 제올라이트, 과염소산마그시움, 감마알루미나, 산화망간, 실리카겔, 염화칼슘 또는 황산을 단독 혹은 복합적으로 사용하는 것인 아릴렌설파이드 중합체의 제조방법.The method for producing arylene sulfide polymer according to claim 1, wherein the method for removing water is using pentoxide, zeolite, magnesium perchlorate, gamma alumina, manganese oxide, silica gel, calcium chloride or sulfuric acid alone or in combination.
KR1019890017796A 1989-12-02 1989-12-02 Process for preparation of polyarylene sulfide polymer KR930004621B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR1019890017796A KR930004621B1 (en) 1989-12-02 1989-12-02 Process for preparation of polyarylene sulfide polymer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
KR1019890017796A KR930004621B1 (en) 1989-12-02 1989-12-02 Process for preparation of polyarylene sulfide polymer

Publications (2)

Publication Number Publication Date
KR910011948A KR910011948A (en) 1991-08-07
KR930004621B1 true KR930004621B1 (en) 1993-06-02

Family

ID=19292476

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1019890017796A KR930004621B1 (en) 1989-12-02 1989-12-02 Process for preparation of polyarylene sulfide polymer

Country Status (1)

Country Link
KR (1) KR930004621B1 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115197732B (en) * 2022-06-07 2023-12-22 中国矿业大学(北京) Preparation method of high-quality synthetic spinnable asphalt and carbon fiber

Also Published As

Publication number Publication date
KR910011948A (en) 1991-08-07

Similar Documents

Publication Publication Date Title
US5840830A (en) Process for producing poly(arylene sulfide)
CA1086895A (en) Production of arylene sulfide polymer
CA2165594C (en) Process for producing poly (phenylene sulfide)
US5342920A (en) Process for the preparation of polyarylene sulfide and an apparatus for the preparation thereof
EP1440996B1 (en) Process for production of polyarylene sulfide
EP0240016B1 (en) Process for preparation of polyphenylene-sulfide resins
CA1086896A (en) Production of p-phenylene sulfide polymers
CA1113645A (en) Aromatic sulfide/sulfone polymer production
JP3603359B2 (en) Method for producing polyarylene sulfide
CA1317407C (en) Aromatic sulfideamide polymer and method for producing the same
JPH09286861A (en) Production of polyarylene sulfide
KR930004621B1 (en) Process for preparation of polyarylene sulfide polymer
JPH05222196A (en) Production of polyarylene sulfide
US5328980A (en) Method of preparing poly(arylene sulfide) polymers, polymers and polymer blends
JP5888556B2 (en) Cross-linked polyarylene sulfide resin and method for producing the same
CN112011052B (en) Functional boron-containing polyarylene sulfide copolymer and preparation method thereof
JP2707118B2 (en) Method for producing high molecular weight polyphenylene sulfide resin
EP0261988B1 (en) Aromatic sulphide amide polymers and a process for the production thereof
JP2024132932A (en) Method for producing polyarylene sulfide resin
EP0325060B1 (en) Aromatic sulfideamide polymer and method for producing the same
JPS62252430A (en) Production of polyphenylene sulfide
JP2024132933A (en) Method for producing polyarylene sulfide resin
JPH04503967A (en) Method for producing copoly(arylene sulfide)
JPH0574611B2 (en)
US3880815A (en) Arylene sulfide polymers

Legal Events

Date Code Title Description
A201 Request for examination
E902 Notification of reason for refusal
G160 Decision to publish patent application
E701 Decision to grant or registration of patent right
GRNT Written decision to grant
FPAY Annual fee payment

Payment date: 19990106

Year of fee payment: 7

LAPS Lapse due to unpaid annual fee