KR20190101285A - Crosslinker masterbatch for hydrogenated nitrile rubber, hydrogenated nitrile rubber composition and cross-linked hydrogenated nitrile rubber molded article - Google Patents
Crosslinker masterbatch for hydrogenated nitrile rubber, hydrogenated nitrile rubber composition and cross-linked hydrogenated nitrile rubber molded article Download PDFInfo
- Publication number
- KR20190101285A KR20190101285A KR1020190016750A KR20190016750A KR20190101285A KR 20190101285 A KR20190101285 A KR 20190101285A KR 1020190016750 A KR1020190016750 A KR 1020190016750A KR 20190016750 A KR20190016750 A KR 20190016750A KR 20190101285 A KR20190101285 A KR 20190101285A
- Authority
- KR
- South Korea
- Prior art keywords
- nitrile rubber
- hydrogenated nitrile
- hnbr
- carbon black
- masterbatch
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J3/00—Processes of treating or compounding macromolecular substances
- C08J3/20—Compounding polymers with additives, e.g. colouring
- C08J3/22—Compounding polymers with additives, e.g. colouring using masterbatch techniques
- C08J3/226—Compounding polymers with additives, e.g. colouring using masterbatch techniques using a polymer as a carrier
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J3/00—Processes of treating or compounding macromolecular substances
- C08J3/24—Crosslinking, e.g. vulcanising, of macromolecules
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/10—Metal compounds
- C08K3/14—Carbides
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L15/00—Compositions of rubber derivatives
- C08L15/005—Hydrogenated nitrile rubber
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2315/00—Characterised by the use of rubber derivatives
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2415/00—Characterised by the use of rubber derivatives
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K2201/00—Specific properties of additives
- C08K2201/002—Physical properties
- C08K2201/006—Additives being defined by their surface area
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/02—Elements
- C08K3/04—Carbon
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/04—Oxygen-containing compounds
- C08K5/14—Peroxides
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Processes Of Treating Macromolecular Substances (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
Description
본 발명은 수소화 니트릴 고무용 가교제 마스터배치(Masterbatch)와 해당 마스터배치를 이용하여 이루어지는 수소화 니트릴 고무 조성물 및 수소화 니트릴 고무 가교 성형품에 관한 것이다.The present invention relates to a crosslinking agent masterbatch for hydrogenated nitrile rubber, a hydrogenated nitrile rubber composition and a hydrogenated nitrile rubber crosslinked molded article formed by using the masterbatch.
수소화 니트릴 고무(이하 'HNBR'이라고 기재하는 경우가 있음)는 니트릴 고무(NBR)에 수소를 첨가하여 내열성이나 내후성을 개량한 고무로서, 자동차용 벨트재료나 각종 오일실(oil seal), 패킹 등으로서 사용되고 있다.Hydrogenated nitrile rubber (hereinafter sometimes referred to as 'HNBR') is a rubber that improves heat resistance and weather resistance by adding hydrogen to nitrile rubber (NBR), and is used for automobile belt materials, various oil seals, packings, etc. It is used as.
1,3-비스(제3부틸 퍼옥시 이소프로필)벤젠은 주로 합성고무나 합성수지의 가교제나 경화제로서 사용되는 유기 과산화물이다. 이 유기 과산화물은 분자중에 -O-O- 결합을 갖고 있기 때문에, 비교적 낮은 온도에서 열적으로 분해되거나 혹은 환원성 물질과 반응하여 용이하게 유리 라디칼을 생성한다. 생성된 유리 라디칼은 불포화 이중결합에 부가반응이나 수소 등의 분리반응을 일으켜서 합성고무 등을 가교시키거나 경화시킨다. 1,3-비스(제3부틸 퍼옥시 이소프로필)벤젠은 HNBR의 가교제로서도 사용된다.1,3-bis (tert-butyl peroxy isopropyl) benzene is an organic peroxide mainly used as a crosslinking agent or curing agent for synthetic rubber or synthetic resin. Since these organic peroxides have -O-O- bonds in their molecules, they thermally decompose or react with reducing substances at relatively low temperatures to easily generate free radicals. The generated free radicals cause addition reactions or separation reactions such as hydrogen to unsaturated double bonds to crosslink or cure synthetic rubbers. 1,3-bis (tert-butyl peroxy isopropyl) benzene is also used as a crosslinking agent of HNBR.
종래, HNBR의 가교제인 유기 과산화물의 촉입(첨가혼련) 공정에서는, 단품의 유기 과산화물을 롤이나 밀폐식 혼련기 등을 이용하여 촉입한다. 그러나 이 혼련작업은 작업자의 숙련을 요하며, 유기 과산화물을 균일하게 분산시키기 위하여 매우 긴 시간이 걸리고, 또한 혼련작업 중에 HNBR이 롤에서 탈락하는(감기지 않게 됨) 등 롤 작업에 따른 제조상의 문제가 있었다.Conventionally, in the step (adding and kneading) process of the organic peroxide which is a crosslinking agent of HNBR, the organic peroxide of a single product is entered using a roll, a sealed kneader, etc. However, the kneading operation requires the skill of the operator, takes a very long time to uniformly disperse the organic peroxide, and also the manufacturing problems due to the roll operation, such as the HNBR drop off (not wound) during the kneading operation There was.
그래서 유기 과산화물의 분산성에 관한 문제를 해소하기 위하여, 유기 과산화물을 함유한 마스터배치가 사용되고 있다. 1,3-비스(제3부틸 퍼옥시 이소프로필)벤젠을 주성분으로 하는 마스터배치도 시장에는 이미 몇 가지 존재하며, 니치유(주)사 제조 퍼부틸 P-40, 페록시몬 F40 등이 알려져 있다. 이들 마스터배치는 희석제로서 탄산칼슘이나 실리카라는 불활성 무기 충전제를 이용하는 것이 일반적이다.Thus, in order to solve the problem of dispersibility of organic peroxides, a masterbatch containing organic peroxides is used. There are already several masterbatches based on 1,3-bis (tert-butyl peroxy isopropyl) benzene on the market, and Nichiyu Co., Ltd. perbutyl P-40 and peroxymon F40 are known. These masterbatches generally use an inert inorganic filler such as calcium carbonate or silica as the diluent.
이들 마스터배치를 이용함으로써, HNBR에 촉입하는 경우의 촉입 시간을 종래의 15분 정도에서 10분 정도로 단축시키는 것이 가능해졌다. 그러나 혼련작업 중에 HNBR이 롤에서 탈락한다는 제조상의 문제는 개선되지 않았다.By using these masterbatches, it is possible to shorten the tapping time in the case of tapping into HNBR by about 15 minutes to about 10 minutes. However, the manufacturing problem of HNBR dropping off the roll during kneading was not improved.
또한, 마스터배치의 희석제로서 탄산칼슘 등의 무기 충전제를 배합시키고 싶지 않다는 요망이 존재한다. 그래서 마스터배치의 희석제를 무기 충전제 대신에 HNBR로 한 결과, 마스터배치 중의 1,3-비스(제3부틸 퍼옥시 이소프로필)벤젠의 함유량을 높이기 어렵다는 점이 판명되었다. 즉, 1,3-비스(제3부틸 퍼옥시 이소프로필)벤젠을 HNBR에 대하여 10 내지 50 질량%의 비율로 혼합분산시키는 것을 시도하였다. 그러나 HNBR과의 상용성이 반드시 높은 것은 아니기 때문에, 1,3-비스(제3부틸 퍼옥시 이소프로필)벤젠이 HNBR로부터 쉽게 분리(블룸)되어 시트 생지 모양의 마스터배치를 작성하기가 어려웠다.In addition, there is a desire not to blend an inorganic filler such as calcium carbonate as the diluent of the masterbatch. Therefore, when the diluent of the masterbatch was HNBR instead of the inorganic filler, it was found that it was difficult to increase the content of 1,3-bis (tertbutylperoxy isopropyl) benzene in the masterbatch. That is, an attempt was made to mix and disperse 1,3-bis (tert-butyl peroxy isopropyl) benzene in a ratio of 10 to 50% by mass relative to HNBR. However, since compatibility with HNBR is not necessarily high, 1,3-bis (tert-butyl peroxy isopropyl) benzene was easily separated (bloomed) from HNBR, making it difficult to produce sheet dough-like masterbatches.
희석제로서 HNBR과 저분자량의 폴리부타디엔 올리고머를 병용한 1,3-비스(제3부틸 퍼옥시 이소프로필)벤젠을 주성분으로 하는 마스터배치가 특허문헌 1에 개시되어 있다.Patent Literature 1 discloses a masterbatch mainly composed of 1,3-bis (tert-butyl peroxy isopropyl) benzene in which HNBR and a low molecular weight polybutadiene oligomer are used in combination.
그러나 특허문헌 1의 마스터배치는 폴리부타디엔 올리고머를 성분으로서 함유하는 것이며, 해당 올리고머를 함유하지 않는 HNBR 조성물로 할 수는 없다.However, the masterbatch of patent document 1 contains a polybutadiene oligomer as a component, and cannot be made into the HNBR composition which does not contain this oligomer.
본 발명은 이와 같은 상황을 감안하여 이루어진 것이다. 즉, 본 발명의 과제는 1,3-비스(제3부틸 퍼옥시 이소프로필)벤젠의 함유량이 높아 혼련작업 중에 HNBR이 롤에서 탈락한다는 가공작업에 있어서의 문제점을 해소할 수 있는 HNBR용 유기 과산화물 마스터배치를 제공하는 것이다. 또한, 해당 마스터배치를 이용하여 이루어지는 HNBR 조성물 및 HNBR 가교 성형품을 제공하는 것이다.This invention is made | formed in view of such a situation. That is, the problem of the present invention is that the organic peroxide for HNBR which can solve the problem in the processing work that the content of 1,3-bis (tert-butyl peroxy isopropyl) benzene is high and HNBR falls off from the roll during kneading operation is solved. To provide a masterbatch. Moreover, it is providing the HNBR composition and HNBR crosslinked molded article which use this masterbatch.
본 발명자는 상기 과제를 해결하기 위해서 HNBR의 조성에 대하여 검토를 진행하였다. 그 결과, HNBR의 결합 아크릴로니트릴량(이하, 「결합 AN량」이라고 기재하는 경우가 있음)을 적정한 범위로 함으로써 1,3-비스(제3부틸 퍼옥시 이소프로필)벤젠과의 상용성을 높이는 것이 가능해짐을 알아내었다. 또한, 보강제로서 첨가하는 카본블랙에 대해서도 적정한 조성을 알아내었다. 본 발명은 이와 같은 지견을 기초로 하여 완성하기에 이른 것이다.MEANS TO SOLVE THE PROBLEM This inventor examined the composition of HNBR in order to solve the said subject. As a result, compatibility with 1,3-bis (tert-butyl peroxy isopropyl) benzene is achieved by setting the amount of bound acrylonitrile of HNBR (hereinafter sometimes referred to as "bound AN amount") to an appropriate range. Found out it was possible to raise. Moreover, the appropriate composition was also found about the carbon black added as a reinforcing agent. The present invention has been completed based on such knowledge.
즉, 본 발명의 HNBR용 유기 과산화물 마스터배치는 HNBR, 1,3-비스(제3부틸 퍼옥시 이소프로필)벤젠 및 카본블랙을 함유하며, 상기 HNBR의 결합 AN량은 25 질량% 미만이고, 상기 1,3-비스(제3부틸 퍼옥시 이소프로필)벤젠의 함유량은 10 내지 30 질량%이고, 상기 카본블랙의 함유량은 10 내지 30 질량%이다.That is, the organic peroxide masterbatch for HNBR of the present invention contains HNBR, 1,3-bis (tert-butyl peroxy isopropyl) benzene, and carbon black, and the amount of binding AN of HNBR is less than 25% by mass. Content of 1, 3-bis (tertiary butyl peroxy isopropyl) benzene is 10-30 mass%, and content of the said carbon black is 10-30 mass%.
또한, 본 발명의 HNBR용 유기 과산화물 마스터배치는 HNBR의 무니점도(mooney viscosity) ML1+4(100℃)가 30 내지 100인 것이 바람직하다.In addition, the organic peroxide masterbatch for HNBR of the present invention preferably has Mooney viscosity ML 1 + 4 (100 ° C) of HNBR of 30 to 100.
또한, 본 발명의 HNBR용 유기 과산화물 마스터배치는 상기 카본블랙의 질소흡착비표면적이 20 내지 80 m2/g이고, DBP 흡수량이 50 내지 160 cm3/100g인 것이 바람직하다.The organic peroxide masterbatches for the HNBR of the invention is a nitrogen adsorption specific surface area of the carbon black from 20 to 80 m 2 / g, preferably in the DBP absorption is 50 to 160 cm 3 / 100g.
또한, 본 발명의 HNBR 조성물은 상기 HNBR용 유기 과산화물 마스터배치를 이용하여 이루어지는 것이다.In addition, the HNBR composition of the present invention is made by using the organic peroxide masterbatch for HNBR.
또한, 본 발명의 HNBR 가교 성형품은 상기 HNBR 조성물을 가교성형하여 이루어지는 것이다.The HNBR crosslinked article of the present invention is obtained by crosslinking the HNBR composition.
본 발명의 HNBR용 유기 과산화물 마스터배치는 1,3-비스(제3부틸 퍼옥시 이소프로필)벤젠의 함유량이 높아 혼련작업 중에 HNBR이 롤에서 탈락한다는 가공작업에 있어서의 문제점을 해소할 수 있다.The organic peroxide masterbatch for HNBR of the present invention has a high content of 1,3-bis (tertiary butyl peroxy isopropyl) benzene, which can solve the problem in the processing work in which HNBR falls off from the roll during kneading.
이하, 본 발명의 실시형태를 상세하게 설명한다. 단, 본 발명의 범위는 이하에 설명하는 구체예로서의 실시형태에 한정되는 것은 아니다.EMBODIMENT OF THE INVENTION Hereinafter, embodiment of this invention is described in detail. However, the scope of the present invention is not limited to embodiment as a specific example demonstrated below.
본 실시형태의 HNBR용 유기 과산화물 마스터배치(이하, '마스터배치'라고 기재하는 경우가 있음)는 HNBR, 1,3-비스(제3부틸 퍼옥시 이소프로필)벤젠 및 카본블랙을 함유한다. 이하, 각 성분에 대하여 설명한다.The organic peroxide masterbatch for HNBR of this embodiment (Hereinafter, it may be described as "masterbatch") contains HNBR, 1, 3-bis (tertiary butyl peroxy isopropyl) benzene, and carbon black. Hereinafter, each component is demonstrated.
(( HNBRHNBR ))
HNBR은 아크릴로니트릴-부타디엔 공중합 폴리머인 니트릴 고무가 갖는 폴리머 주쇄 중의 불포화결합을 수소화시킴으로써 내열성, 내약품성, 내후성 등을 개량한 고무이다.HNBR is a rubber which improves heat resistance, chemical resistance, weather resistance and the like by hydrogenating unsaturated bonds in the polymer main chain of the nitrile rubber which is an acrylonitrile-butadiene copolymer polymer.
HNBR의 폴리머 주쇄 중에 잔류하고 있는 불포화결합량의 기준으로서 요오드값(g/100g)이 이용된다. 내열성을 고려하면, 요오드값(g/100g)이 20 이하인 것이 바람직하고, 15 이하인 것이 더욱 바람직하다. 한편, HNBR에 적당히 불포화결합을 잔존시킴으로써 과산화물 가교나 특수 가교(아민 가교 등)를 수행할 수 있어, 내열성, 기계적 강도, 내유성 등의 향상의 관점으로부터 바람직하다.An iodine value (g / 100g) is used as a reference for the amount of unsaturated bonds remaining in the polymer backbone of HNBR. In consideration of heat resistance, the iodine value (g / 100g) is preferably 20 or less, more preferably 15 or less. On the other hand, peroxide crosslinking and special crosslinking (such as amine crosslinking) can be carried out by appropriately remaining unsaturated bonds in HNBR, which is preferable from the viewpoint of improvement of heat resistance, mechanical strength, oil resistance and the like.
HNBR은 아크릴 고무에 가까운 내열성을 갖고, 우수한 화학적 안정성을 구비하고 있다. 또한, 기계적 강도, 내마모성 등도 우수하다. 그 때문에 오일 실이나 패킹 등의 용도에 대하여 알맞은 성질을 갖고 있다.HNBR has heat resistance close to acrylic rubber and has excellent chemical stability. Moreover, mechanical strength, abrasion resistance, etc. are also excellent. Therefore, it has suitable properties for applications such as oil seals and packings.
본 발명자는 HNBR과 1,3-비스(제3부틸 퍼옥시 이소프로필)벤젠의 상용성을 높이기 위해서, HNBR의 결합 AN량에 주목하였다. HNBR의 결합 AN량이 많아지면 일반적으로 HNBR의 극성은 높아지고, HNBR의 내유성, 내마모성 등이 향상된다. 그러나 1,3-비스(제3부틸 퍼옥시 이소프로필)벤젠과의 관계에서 적정한 결합 AN량은 불분명하였다. 그래서 검토를 진행한 결과, HNBR의 결합 AN량이 25 질량% 미만이면 1,3-비스(제3부틸 퍼옥시 이소프로필)벤젠을 고농도로 함유시켜도 분리(블룸)가 잘 일어나지 않음을 알아내었다.The present inventors paid attention to the amount of binding AN of HNBR in order to increase the compatibility between HNBR and 1,3-bis (tert-butyl peroxy isopropyl) benzene. In general, when the amount of bound AN in HNBR increases, the polarity of HNBR increases and oil resistance, abrasion resistance, and the like of HNBR improve. However, the appropriate amount of binding AN was unclear in relation to 1,3-bis (tert-butyl peroxy isopropyl) benzene. Therefore, as a result of examination, it was found that separation (bloom) does not occur well even when the amount of binding AN of HNBR is less than 25% by mass, even if it contains a high concentration of 1,3-bis (tert-butyl peroxy isopropyl) benzene.
이 결과는 1,3-비스(제3부틸 퍼옥시 이소프로필)벤젠의 용해도 파라미터 Sp값이 저결합 AN량의 HNBR과 가까운 범위에 있기 때문이라고 추측되었다. 또한, HNBR의 결합 AN량이 25 질량% 미만이면 HNBR과의 혼련 설비의 혼합조 내의 오염도 경감되었다.This result was presumed to be because the solubility parameter Sp value of 1, 3-bis (tert-butyl peroxy isopropyl) benzene was in the range close to HNBR of low binding AN amount. Moreover, when the amount of binding AN of HNBR was less than 25 mass%, the contamination in the mixing tank of the kneading apparatus with HNBR was also reduced.
HNBR의 무니점도 ML1+4(100℃)는 기계적 강도나 가공성의 관점으로부터 30 내지 100인 것이 바람직하고, 30 내지 80인 것이 더욱 바람직하다. 여기서 무니점도 ML1+4(100℃)는 JIS K 6300-1:2013에 준거하여 측정된다.It is preferable that it is 30-100, and, as for the Mooney viscosity ML1 + 4 (100 degreeC) of HNBR, it is more preferable that it is 30-80 from a viewpoint of mechanical strength or workability. A Mooney viscosity ML 1 + 4 (100 degreeC) is measured based on JISK6300-1: 2013 here.
HNBR로서는 예를 들어, 닛폰제온사 제조의 제트폴(Zetpol, 등록상표), 랑세스사 제조의 터반(Therban, 등록상표) 등을 이용할 수 있다.As the HNBR, for example, a Nippon Xeon company Jetpol (registered trademark), LANXESS manufactured Terban (Therban, registered trademark) and the like can be used.
(1,3-(1,3- 비스(제3부틸 퍼옥시 이소프로필)벤젠Bis (tertbutyl peroxy isopropyl) benzene ))
1,3-비스(제3부틸 퍼옥시 이소프로필)벤젠은 1,3-비스[1-(tert-부틸퍼옥시)-1-메틸에틸]벤젠이라고도 칭해지는 유기 과산화물이다. 백색의 분체이고, CAS번호 25155-25-3의 화합물이다.1,3-bis (tert-butyl peroxy isopropyl) benzene is an organic peroxide also called 1,3-bis [1- (tert-butylperoxy) -1-methylethyl] benzene. It is a white powder, and is a compound of CAS number 25155-25-3.
(카본블랙)(Carbon black)
마스터배치에는 보강제로서 카본블랙이 첨가된다. 보강제로서는 카본블랙 이외에도 실리카(화이트카본), 탄산마그네슘, 클레이 등이 있지만, 카본블랙이 바람직하다. 적절한 카본블랙을 선정함으로써 가공 작업성을 더 개선할 수 있다.The masterbatch contains carbon black as a reinforcing agent. Examples of the reinforcing agent include silica (white carbon), magnesium carbonate and clay in addition to carbon black, but carbon black is preferable. By selecting the appropriate carbon black, the workability can be further improved.
카본블랙으로서는 질소흡착비표면적이 20 내지 80 m2/g인 카본블랙이 바람직하고, 30 내지 50 m2/g인 카본블랙이 더욱 바람직하다. 카본블랙의 질소흡착비표면적이 상기 수치 범위보다 작으면, 카본블랙의 분산이 불충분해져서 생지가 경화되어 롤 가공성이 저하된다. 한편, 카본블랙의 질소흡착비표면적이 상기 수치 범위보다 크면, 생지의 습태 강도(green strength)가 저하되어 롤 가공성이 저하된다. 카본블랙의 질소흡착비표면적은 JIS K 6217:1997에 준거하여 측정할 수 있다.As carbon black, carbon black whose nitrogen adsorption specific surface area is 20-80 m <2> / g is preferable, and carbon black whose 30-50 m <2> / g is more preferable. If the nitrogen adsorption specific surface area of the carbon black is smaller than the above numerical range, the dispersion of the carbon black becomes insufficient, the dough is cured, and roll workability is lowered. On the other hand, when the nitrogen adsorption specific surface area of carbon black is larger than the said numerical range, the green strength of a dough will fall and roll workability will fall. The nitrogen adsorption specific surface area of carbon black can be measured based on JISK6217: 1997.
또한, 카본블랙으로서는 DBP(디부틸프탈레이트) 흡수량이 50 내지 160 cm3/100g인 카본블랙이 바람직하고, 100 내지 150 cm3/100g인 카본블랙이 더욱 바람직하다. DBP 흡수량은 카본블랙의 응집체(aggregate)간의 공극율의 지표가 된다. 카본블랙의 DBP 흡수량이 상기 수치 범위 내에 있으면 롤 가공성이 양호해진다. 카본블랙의 DBP 흡수량은 JIS K 6217:1997에 준거하여 측정할 수 있다.Moreover, as carbon black, carbon black whose DBP (dibutyl phthalate) absorption amount is 50-160 cm <3> / 100g is preferable, and carbon black whose 100-150 cm <3> / 100g is more preferable. The amount of DBP absorption is indicative of the porosity between the aggregates of carbon black. Roll workability becomes it favorable that the DBP absorption amount of carbon black exists in the said numerical range. The DBP absorption amount of carbon black can be measured based on JISK6217: 1997.
(마스터배치)(Master batch)
마스터배치에 있어서의 1,3-비스(제3부틸 퍼옥시 이소프로필)벤젠의 함유량은 10 내지 30 질량%이고, 20 내지 30 질량%가 바람직하다. 또한, 마스터배치에 있어서의 카본블랙의 함유량은 10 내지 30 질량%이고, 20 내지 30 질량%가 바람직하다. 마스터배치에 있어서 1,3-비스(제3부틸 퍼옥시 이소프로필)벤젠 및 카본블랙 이외의 성분이 기본적으로 HNBR이 된다. 마스터배치는 이와 같이 1,3-비스(제3부틸 퍼옥시 이소프로필)벤젠을 고농도로 함유하는 것이다. 1,3-비스(제3부틸 퍼옥시 이소프로필)벤젠 및 카본블랙의 함유량이 상기 수치 범위 내에 있으면, 혼련성이나 롤 가공성이 우수하여 혼련작업 중에 HNBR이 롤에서 탈락한다는 가공작업에 있어서의 문제점을 해소할 수 있다.The content of 1,3-bis (tert-butyl peroxy isopropyl) benzene in the masterbatch is 10 to 30 mass%, preferably 20 to 30 mass%. Moreover, content of the carbon black in masterbatch is 10-30 mass%, and 20-30 mass% is preferable. In the masterbatch, components other than 1,3-bis (tert-butyl peroxy isopropyl) benzene and carbon black are basically HNBR. The masterbatch thus contains a high concentration of 1,3-bis (tert-butyl peroxy isopropyl) benzene. If the content of 1,3-bis (tert-butyl peroxy isopropyl) benzene and carbon black is within the above numerical range, there is a problem in processing that HNBR falls off from the roll during the kneading operation due to excellent kneading property and roll workability. Can be solved.
마스터배치에는 범용성이 요구되기 때문에, HNBR, 1,3-비스(제3부틸 퍼옥시 이소프로필)벤젠 및 카본블랙 이외의 성분으로서 가공조제 등의 첨가제를 배합할 수 있다. 이들 첨가제는 필요에 따라 적당히 첨가된다.Since versatility is required for masterbatch, additives, such as a processing aid, can be mix | blended as components other than HNBR, 1, 3-bis (tertiary butyl peroxy isopropyl) benzene, and carbon black. These additives are suitably added as needed.
(마스터배치의 제조방법)(Manufacturing method of master batch)
마스터배치의 제조에 이용하는 혼련장치로서는 대기의 영향을 극력 차단하기 위해서 밀폐식 혼련장치를 이용하는 것이 바람직하다. 혼련장치는 배치식이어도 되고, 연속식이어도 된다. 배치식 혼련장치로서는 가압니더, 밴버리믹서, 오픈롤 등이 있다. 연속식 혼련장치로서는 1축 압출기, 2축 압출기, 피더루더 등이 있다.As a kneading apparatus used for manufacturing a masterbatch, it is preferable to use a sealed kneading apparatus in order to cut off the influence of air as much as possible. The kneading apparatus may be a batch type or a continuous type. Batch kneading apparatuses include pressurized kneaders, Banbury mixers, open rolls, and the like. Examples of the continuous kneading apparatus include a single screw extruder, a twin screw extruder, a feeder loader and the like.
마스터배치는 상기 혼련장치를 이용하여 각 성분을 10분 정도 혼련함으로써 조제할 수 있다. 구체적으로는, HNBR 폴리머를 소련(素練)한 후에, 1,3-비스(제3부틸 퍼옥시 이소프로필)벤젠과 카본블랙 등을 사전에 프리믹스한 혼합물을 2 내지 3회로 나누어 투입하고, 10분 정도 혼련시킴으로써 수행된다.The masterbatch can be prepared by kneading each component for about 10 minutes using the kneading apparatus. Specifically, after the HNBR polymer was sovietized, a mixture of 1,3-bis (tert-butyl peroxy isopropyl) benzene, carbon black and the like premixed in advance was added in two to three portions, and 10 was added. By kneading for about a minute.
얻어진 마스터배치는 가교에 필요한 유기 과산화물량에 상당하는 비율로 계량되고, HNBR 및 다른 성분과 혼합되어 용융 혼련 등을 수행함으로써 HNBR 조성물로서 얻을 수 있다. 또한, 얻어진 HNBR 조성물을 통상적으로 수행되는 HNBR의 가교 성형조건에 의해 가교성형함으로써 가교 성형품으로 할 수 있다.The obtained masterbatch is weighed at a ratio corresponding to the amount of organic peroxide required for crosslinking, and can be obtained as an HNBR composition by mixing with HNBR and other components to perform melt kneading or the like. In addition, the obtained HNBR composition can be formed into a crosslinked molded article by crosslinking molding under the crosslinking conditions of HNBR which are usually performed.
종래, 저융점이며 분체인 1,3-비스(제3부틸 퍼옥시 이소프로필)벤젠을 HNBR에 촉입할 때에는 롤 작업이 매우 길어 약품 비산에 의한 작업환경의 악화, 또한 HNBR이 롤에서 탈락한다는 문제를 갖는 것이었다. 본 실시형태의 마스터배치를 채택함으로써 작업자의 숙련을 필요로 하지 않고, 작업시간의 대폭적인 단축이 가능해졌다. 또한, 혼련작업 중에 HNBR이 롤에서 탈락한다는 문제가 해소되어 작업환경이 개선되고, 안전작업의 확보가 가능해졌다.Conventionally, when the low melting point and powder 1,3-bis (tert-butyl peroxy isopropyl) benzene is contacted with HNBR, the roll operation is very long, which causes deterioration of the working environment due to chemical scattering and the problem of HNBR falling off the roll. It was to have. By adopting the masterbatch of the present embodiment, it is possible to drastically shorten the working time without requiring the operator's skill. In addition, the problem of HNBR falling off the roll during kneading was eliminated, and the working environment was improved, and safety work was secured.
실시예Example
이하, 실시예와 비교예에 의해 본 발명을 설명하는데, 이들 실시예는 본 발명을 한정하는 것은 아니다.Hereinafter, although an Example and a comparative example demonstrate this invention, these Examples do not limit this invention.
(마스터배치 원료)Masterbatch Raw Material
HNBR: 닛폰제온사 제조 제트폴 2000L, 3110, 4310Hnbr: jet pole 2000l, 3110, 4310 by Nippon Zeon
HNBR: 랑세스사 제조 터반 AT LT2004VPHNBR: LANXESS manufactured turban AT LT2004VP
각 HNBR의 결합 AN량 및 무니점도는 표 1에 나타내었다.Binding AN amount and Mooney viscosity of each HNBR are shown in Table 1.
1,3-비스(제3부틸 퍼옥시 이소프로필)벤젠: 가야쿠아쿠조사 제조 퍼카독스141,3-bis (tert-butyl peroxy isopropyl) benzene: percadox 14 manufactured by Kayaku Acquizo
카본블랙: 도카이카본사 제조 카본블랙, SRF-HS(시스트SVH), SRF(시스트S), FEF(시스트SO), MAF(시스트116)Carbon black: carbon black manufactured by Tokai Carbon Co., Ltd., SRF-HS (Sist SVH), SRF (Sist S), FEF (Sist SO), MAF (Sist 116)
각 카본블랙의 질소흡착비표면적 및 DBP 흡수량은 표 2에 나타내었다.The nitrogen adsorption specific surface area and DBP absorption amount of each carbon black are shown in Table 2.
실리카: 도소·실리카사 제조 침전법 실리카, Nipsil ERSilica: Precipitation silica made by Tosoh Silica, Nipsil ER
(마스터배치 조성물의 제조)(Preparation of Masterbatch Composition)
마스터배치 제조용 혼련기로서 니더(니혼스핀들세이조사 제조 가압식 3l니더)를 이용하였다.A kneader (a pressurized 3 l kneader manufactured by Nippon Spindle Co., Ltd.) was used as a kneader for producing a master batch.
표 3에 기재된 조성으로 HNBR 폴리머를 소련한 후에, 1,3-비스(제3부틸 퍼옥시 이소프로필)벤젠과 보강제를 사전에 프리믹스한 혼합물을 3회로 나누어 투입하고, 회전수 30 rpm으로 10분간 혼련하였다.After sieving the HNBR polymer with the composition shown in Table 3, a mixture of 1,3-bis (tert-butyl peroxy isopropyl) benzene and a premix premixed was added three times, and the mixture was rotated at 30 rpm for 10 minutes. Kneaded.
얻어진 각 마스터배치 조성물을 이용하여 다음의 각 항목의 평가를 수행하고, 그 결과를 표 3에 나타내었다.Each masterbatch composition thus obtained was used to evaluate each of the following items, and the results are shown in Table 3.
(( 니더Kneader 혼련성Kneading ))
니더에 의한 혼련 시 및 혼련 후의 상황에 대하여 하기 관점으로부터 평가를 수행하였다.The evaluation was performed from the following viewpoints about the kneading by kneader and the situation after kneading.
○: 특별히 문제 없고, 혼련성 양호(Circle): There is no problem in particular, and kneading property is favorable
△: 전력토크가 낮고, 반죽이 불충분함△: low power torque, insufficient dough
×: 반죽이 잘 안 되거나 또는 반죽할 수 없는, 특히 니더 배출시에 모래 모양으로 되어 생지로서 뭉치지 않을 때에는 × 중에서도 가장 나쁜 상태임X: It is the worst state among x when kneading | mixing is difficult or it cannot be kneaded, especially when it becomes sand-like at the time of kneading discharge and does not stick together as a dough.
(롤 가공성)(Roll workability)
12인치 오픈롤을 이용하여 각 마스터배치 조성물을 혼련하여 롤 가공성을 이하의 기준으로 평가하였다. 여기서 배깅(bagging)이란 롤에 감은 생지가 롤 표면으로부터 떠올라 나이프가 들어가지 않아 시트 피딩작업을 할 수 없게 되는 현상을 말한다.Each masterbatch composition was kneaded using a 12 inch open roll to evaluate roll workability based on the following criteria. Here, bagging refers to a phenomenon in which dough rolled up on a roll rises from the surface of the roll so that the knife does not enter and sheet feeding cannot be performed.
○: 가공성 양호○: good workability
△: 약간 배깅됨(감기 어려움)△: slightly bagged (difficult to wind)
×: 배깅이 심함(감을 수 없음)×: bagging is severe (can't be wound)
(( 생지Dough 재단의 용이성) Ease of foundation)
각 마스터배치 조성물을 이용하여 5 mm 두께의 시트 생지를 조제하였다. 조제한 시트 생지를 실온하에서 24시간 방랭한 후, 가위로 재단하였다.Each masterbatch composition was used to prepare sheet dough 5 mm thick. The prepared sheet dough was left to cool at room temperature for 24 hours, and then cut with scissors.
○: 쉽게 재단이 가능○: easy cutting
△: 약간 딱딱하지만 재단 가능△: slightly hard but can be cut
×: 딱딱해서 재단이 어려움×: hard to cut
표 3의 평가 결과로부터 알 수 있는 바와 같이, 실시예 1 내지 2의 마스터배치 조성물은 니더 혼련성, 롤 가공성 및 생지 재단의 용이성에 있어서 양호한 성능을 갖고 있었다. 비교예 1의 마스터배치 조성물은 HNBR의 결합 AN량이 25 질량%이기 때문에, 니더 혼련시의 반죽이 불충분해져서 롤 혼련시에 약간의 배깅이 발생하고, 니더 혼련성, 롤 가공성 및 생지 재단의 용이성에 있어서 약간 뒤떨어져 있었다. 비교예 2의 마스터배치 조성물은 HNBR의 결합 AN량이 36 질량%이기 때문에, 니더 배출시에 스펀지 모양이 되어 롤에 감기지 않고, 그 이후의 성능 평가를 수행할 수 없었다. 비교예 3의 마스터배치 조성물은 카본블랙의 함유량이 많고, HNBR의 결합 AN량이 크기 때문에 니더 배출시에 스펀지 모양이 되어 모든 성능이 뒤떨어져 있었다.As can be seen from the evaluation results in Table 3, the masterbatch compositions of Examples 1 to 2 had good performances in kneader kneading, roll workability, and ease of dough cutting. In the masterbatch composition of Comparative Example 1, the amount of HNBR bound AN is 25% by mass, so that the dough during kneading becomes insufficient and some bagging occurs during kneading of the kneader. I was a bit behind. In the masterbatch composition of Comparative Example 2, since the amount of binding AN of HNBR was 36% by mass, it did not form a sponge in the kneader discharge and was not wound on a roll, and performance evaluation thereafter could not be performed. The masterbatch composition of Comparative Example 3 had a high carbon black content and a large amount of H in the amount of bound AN of HNBR, resulting in a sponge-like shape at the time of kneader discharge, resulting in inferior performance.
비교예 4 내지 6의 마스터배치 조성물은 카본블랙의 종류가 다른 것이지만, 카본블랙의 함유량이 많아 니더 혼련성, 롤 가공성 및 생지 재단의 용이성의 모든 성능에 있어서 뒤떨어져 있었다. 비교예 7의 마스터배치 조성물은 보강제로서 실리카를 이용한 것이지만, 생지 점도가 매우 높아져서 롤 혼련시에 배깅이 발생하고, 생지 재단의 용이성도 뒤떨어져 있었다.Although the masterbatch composition of Comparative Examples 4-6 differs in the kind of carbon black, since the content of carbon black is large, it was inferior in all the performances of kneader kneading | mixing property, roll workability, and the ease of dough cutting. Although the masterbatch composition of the comparative example 7 used silica as a reinforcing agent, the dough viscosity became very high, the bagging generate | occur | produced at the time of roll kneading | mixing, and the ease of dough cutting was inferior.
비교예 8의 마스터배치 조성물은 카본블랙의 함유량이 많기 때문에 롤 가공성에서 뒤떨어져 있었다. 비교예 9의 마스터배치 조성물은 가교제의 함유량이 많기 때문에, 니더 배출시에 모래 모양으로 되어 생지로서 뭉치지 않아 그 이후의 성능평가를 수행할 수 없었다.The masterbatch composition of the comparative example 8 was inferior in roll workability because there was much content of carbon black. Since the masterbatch composition of the comparative example 9 had a large content of a crosslinking agent, it turned into sand at the time of kneading | discharging a kneader, and it did not aggregate as a dough, and performance evaluation after that could not be performed.
Claims (5)
상기 수소화 니트릴 고무의 결합 아크릴로니트릴량이 25 질량% 미만이고,
상기 1,3-비스(제3부틸 퍼옥시 이소프로필)벤젠의 함유량이 10 내지 30 질량%이고,
상기 카본블랙의 함유량이 10 내지 30 질량%인 것을 특징으로 하는 수소화 니트릴 고무용 유기 과산화물 마스터배치.Hydrogenated nitrile rubber, 1,3-bis (tertbutyl peroxy isopropyl) benzene and carbon black,
The amount of bonded acrylonitrile of the hydrogenated nitrile rubber is less than 25% by mass,
The content of the 1,3-bis (tert-butyl peroxy isopropyl) benzene is 10 to 30% by mass,
An organic peroxide masterbatch for hydrogenated nitrile rubber, wherein the carbon black content is 10 to 30% by mass.
상기 수소화 니트릴 고무의 무니점도 ML1+4(100℃)가 30 내지 100인 것인 수소화 니트릴 고무용 유기 과산화물 마스터배치.The method of claim 1,
An organic peroxide masterbatch for hydrogenated nitrile rubber in which the Mooney viscosity ML 1 + 4 (100 ° C.) of the hydrogenated nitrile rubber is 30 to 100.
상기 카본블랙은 질소흡착비표면적이 20 내지 80 m2/g이고, DBP 흡수량이 50 내지 160 cm3/100g인 것을 특징으로 하는 수소화 니트릴 고무용 유기 과산화물 마스터배치.The method according to claim 1 or 2,
The carbon black had a specific surface area of nitrogen adsorption of 20 to 80 m 2 / g, DBP absorption of hydrogenated nitrile rubbers organic peroxide masterbatches, characterized in that 50 to 160 cm 3 / 100g.
The hydrogenated nitrile rubber crosslinked molded article formed by crosslinking the hydrogenated nitrile rubber composition of Claim 4.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2018029421A JP7064901B2 (en) | 2018-02-22 | 2018-02-22 | Crosslinking agent for hydrided nitrile rubber Master batch, hydrided nitrile rubber composition and hydrided nitrile rubber crosslinked molded product |
JPJP-P-2018-029421 | 2018-02-22 |
Publications (2)
Publication Number | Publication Date |
---|---|
KR20190101285A true KR20190101285A (en) | 2019-08-30 |
KR102194087B1 KR102194087B1 (en) | 2020-12-22 |
Family
ID=67713613
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
KR1020190016750A KR102194087B1 (en) | 2018-02-22 | 2019-02-13 | Crosslinker masterbatch for hydrogenated nitrile rubber, hydrogenated nitrile rubber composition and cross-linked hydrogenated nitrile rubber molded article |
Country Status (3)
Country | Link |
---|---|
JP (1) | JP7064901B2 (en) |
KR (1) | KR102194087B1 (en) |
CN (1) | CN110183691A (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112500588B (en) * | 2020-12-08 | 2021-07-27 | 南京工业大学 | Method for preparing high-fluidity carbon black master batch by peroxide in-situ degradation of polypropylene |
CN116761853A (en) * | 2021-01-25 | 2023-09-15 | 积水技术成型株式会社 | Resin composition, resin molded body, and method for producing same |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH1087889A (en) * | 1996-09-09 | 1998-04-07 | Zeon Kasei Co Ltd | Organic peroxide-containing masterbatch and rubber composition |
JP2000212333A (en) * | 1999-01-20 | 2000-08-02 | Nok Corp | Hydrogenated nbr composition |
KR20080031334A (en) | 2005-06-28 | 2008-04-08 | 빅-비올렉스 에스아 | Ergonomic razor handle provided with an improved grip |
KR101760874B1 (en) * | 2016-03-18 | 2017-07-24 | 한국타이어 주식회사 | Tire carcass and tire comprising the same |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP3543388B2 (en) * | 1994-09-30 | 2004-07-14 | 日本ゼオン株式会社 | Vulcanizable acrylic rubber composition |
WO1996017015A1 (en) * | 1994-11-30 | 1996-06-06 | Nippon Zeon Co., Ltd. | Vulcanizable rubber composition, seal to be used in dynamic state, and material therefor |
JP3597955B2 (en) * | 1996-09-24 | 2004-12-08 | ゼオン化成株式会社 | Manufacturing method of organic peroxide masterbatch |
CA2436742A1 (en) * | 2003-06-26 | 2004-12-26 | Bayer Inc. | Polymer blends comprising nitrile rubber |
JP2008031334A (en) * | 2006-07-31 | 2008-02-14 | Nok Elastomers Processing Co Ltd | Organic peroxide masterbatch for hydrogenated nitrile butadiene rubber (nbr) |
JP2011038056A (en) * | 2009-08-18 | 2011-02-24 | Sumitomo Rubber Ind Ltd | Rubber composition for bladder and bladder |
JP6494082B2 (en) * | 2014-11-26 | 2019-04-03 | 住友ゴム工業株式会社 | Rubber composition for fenders and fenders |
JP6677967B2 (en) * | 2014-12-18 | 2020-04-08 | Nok株式会社 | Hydrogenated nitrile rubber composition and oil seal for drive train |
-
2018
- 2018-02-22 JP JP2018029421A patent/JP7064901B2/en active Active
-
2019
- 2019-02-13 KR KR1020190016750A patent/KR102194087B1/en active IP Right Grant
- 2019-02-21 CN CN201910128280.7A patent/CN110183691A/en active Pending
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH1087889A (en) * | 1996-09-09 | 1998-04-07 | Zeon Kasei Co Ltd | Organic peroxide-containing masterbatch and rubber composition |
JP2000212333A (en) * | 1999-01-20 | 2000-08-02 | Nok Corp | Hydrogenated nbr composition |
KR20080031334A (en) | 2005-06-28 | 2008-04-08 | 빅-비올렉스 에스아 | Ergonomic razor handle provided with an improved grip |
KR101760874B1 (en) * | 2016-03-18 | 2017-07-24 | 한국타이어 주식회사 | Tire carcass and tire comprising the same |
Also Published As
Publication number | Publication date |
---|---|
KR102194087B1 (en) | 2020-12-22 |
JP7064901B2 (en) | 2022-05-11 |
JP2019143059A (en) | 2019-08-29 |
CN110183691A (en) | 2019-08-30 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP1985657B1 (en) | Hydrogenated nbr composition | |
CN105646959B (en) | A kind of rubber composition, preparation method and its application in 3D printing air core tyre | |
KR20190101285A (en) | Crosslinker masterbatch for hydrogenated nitrile rubber, hydrogenated nitrile rubber composition and cross-linked hydrogenated nitrile rubber molded article | |
JP2010013494A (en) | Rubber composition for under tread | |
US6743860B2 (en) | Thermoplastic resin composition and production processes thereof | |
EP1427774B1 (en) | Masterbatch comprising rubber compounds, fillers, plasticizers and curatives | |
EP1473322B1 (en) | Cement for modification of rubber articles and process for production thereof | |
JP4615989B2 (en) | Rubber composition and pneumatic tire | |
RU2458943C1 (en) | Method of producing thermoplastic elastomeric composition | |
JP2009167294A (en) | Method for manufacturing rubber composition for use in tire | |
JP2007161822A (en) | Rubber composition for tire | |
JP3344187B2 (en) | Hydrogenated NBR composition for CFC-resistant refrigerant | |
JPWO2019188339A1 (en) | Rubber composition and method for reducing adhesion to the surface of the kneader using the rubber composition | |
KR101653758B1 (en) | Composite of rubber for o-ring and manufacturing method of the same | |
CN109280278A (en) | A kind of automobile gears dust cover rubber-plastics material and preparation method thereof | |
JP2006117744A (en) | Vibration-damping material | |
JP2008031334A (en) | Organic peroxide masterbatch for hydrogenated nitrile butadiene rubber (nbr) | |
KR20010011008A (en) | Composition for the preparation of thermoplastic elastomer and process method thereof | |
KR100823499B1 (en) | A crosslink agent for crosslinking of thermoplastic elastomer | |
RU2218366C2 (en) | Rubber mixture for carcass-cushion rubbers | |
JP4606760B2 (en) | Method for producing butyl rubber composition | |
JP3301127B2 (en) | Rubber parts with excellent Freon refrigerant resistance | |
JP2022100542A (en) | Desulfurized rubber, rubber composition containing desulfurized rubber, and pneumatic tire including rubber portion composed of vulcanized and molded rubber composition | |
JPH0299533A (en) | Rubber composition | |
JPH06128419A (en) | Production of rubber composition |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A201 | Request for examination | ||
E902 | Notification of reason for refusal | ||
E701 | Decision to grant or registration of patent right | ||
GRNT | Written decision to grant |