JPH0481610B2 - - Google Patents
Info
- Publication number
- JPH0481610B2 JPH0481610B2 JP59196286A JP19628684A JPH0481610B2 JP H0481610 B2 JPH0481610 B2 JP H0481610B2 JP 59196286 A JP59196286 A JP 59196286A JP 19628684 A JP19628684 A JP 19628684A JP H0481610 B2 JPH0481610 B2 JP H0481610B2
- Authority
- JP
- Japan
- Prior art keywords
- weight
- acrylate
- monomers
- acrylic copolymer
- copolymer rubber
- Prior art date
- Legal status (The legal status 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 status listed.)
- Expired - Lifetime
Links
- 239000000178 monomer Substances 0.000 claims description 36
- 229920001971 elastomer Polymers 0.000 claims description 26
- 239000005060 rubber Substances 0.000 claims description 26
- 229920006243 acrylic copolymer Polymers 0.000 claims description 19
- -1 acrylic ester Chemical class 0.000 claims description 12
- 229910052799 carbon Inorganic materials 0.000 claims description 7
- 125000005250 alkyl acrylate group Chemical group 0.000 claims description 6
- 150000001993 dienes Chemical class 0.000 claims description 6
- 125000003700 epoxy group Chemical group 0.000 claims description 6
- 229910052717 sulfur Inorganic materials 0.000 claims description 5
- 239000011593 sulfur Substances 0.000 claims description 5
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims description 4
- 238000004519 manufacturing process Methods 0.000 claims description 4
- 239000003795 chemical substances by application Substances 0.000 claims description 3
- 238000007334 copolymerization reaction Methods 0.000 claims description 3
- 150000001451 organic peroxides Chemical class 0.000 claims 1
- 238000004073 vulcanization Methods 0.000 description 11
- 229920000058 polyacrylate Polymers 0.000 description 9
- 238000006116 polymerization reaction Methods 0.000 description 9
- 229920000800 acrylic rubber Polymers 0.000 description 8
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 description 6
- 238000004132 cross linking Methods 0.000 description 5
- RRHGJUQNOFWUDK-UHFFFAOYSA-N Isoprene Chemical compound CC(=C)C=C RRHGJUQNOFWUDK-UHFFFAOYSA-N 0.000 description 4
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 4
- 125000004432 carbon atom Chemical group C* 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 230000000704 physical effect Effects 0.000 description 4
- PMJHHCWVYXUKFD-UHFFFAOYSA-N piperylene Natural products CC=CC=C PMJHHCWVYXUKFD-UHFFFAOYSA-N 0.000 description 4
- PMJHHCWVYXUKFD-SNAWJCMRSA-N (E)-1,3-pentadiene Chemical group C\C=C\C=C PMJHHCWVYXUKFD-SNAWJCMRSA-N 0.000 description 3
- STMDPCBYJCIZOD-UHFFFAOYSA-N 2-(2,4-dinitroanilino)-4-methylpentanoic acid Chemical compound CC(C)CC(C(O)=O)NC1=CC=C([N+]([O-])=O)C=C1[N+]([O-])=O STMDPCBYJCIZOD-UHFFFAOYSA-N 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000007906 compression Methods 0.000 description 3
- 230000006835 compression Effects 0.000 description 3
- VOZRXNHHFUQHIL-UHFFFAOYSA-N glycidyl methacrylate Chemical compound CC(=C)C(=O)OCC1CO1 VOZRXNHHFUQHIL-UHFFFAOYSA-N 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- OJOWICOBYCXEKR-KRXBUXKQSA-N (5e)-5-ethylidenebicyclo[2.2.1]hept-2-ene Chemical compound C1C2C(=C/C)/CC1C=C2 OJOWICOBYCXEKR-KRXBUXKQSA-N 0.000 description 2
- BAPJBEWLBFYGME-UHFFFAOYSA-N Methyl acrylate Chemical compound COC(=O)C=C BAPJBEWLBFYGME-UHFFFAOYSA-N 0.000 description 2
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 2
- 150000001412 amines Chemical class 0.000 description 2
- 150000003863 ammonium salts Chemical class 0.000 description 2
- 238000013329 compounding Methods 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 229920001577 copolymer Polymers 0.000 description 2
- 229920003244 diene elastomer Polymers 0.000 description 2
- 229910052736 halogen Inorganic materials 0.000 description 2
- 150000002367 halogens Chemical class 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- RPQRDASANLAFCM-UHFFFAOYSA-N oxiran-2-ylmethyl prop-2-enoate Chemical compound C=CC(=O)OCC1CO1 RPQRDASANLAFCM-UHFFFAOYSA-N 0.000 description 2
- 238000010059 sulfur vulcanization Methods 0.000 description 2
- KOMNUTZXSVSERR-UHFFFAOYSA-N 1,3,5-tris(prop-2-enyl)-1,3,5-triazinane-2,4,6-trione Chemical compound C=CCN1C(=O)N(CC=C)C(=O)N(CC=C)C1=O KOMNUTZXSVSERR-UHFFFAOYSA-N 0.000 description 1
- SLBOQBILGNEPEB-UHFFFAOYSA-N 1-chloroprop-2-enylbenzene Chemical compound C=CC(Cl)C1=CC=CC=C1 SLBOQBILGNEPEB-UHFFFAOYSA-N 0.000 description 1
- HECLRDQVFMWTQS-RGOKHQFPSA-N 1755-01-7 Chemical compound C1[C@H]2[C@@H]3CC=C[C@@H]3[C@@H]1C=C2 HECLRDQVFMWTQS-RGOKHQFPSA-N 0.000 description 1
- OEPOKWHJYJXUGD-UHFFFAOYSA-N 2-(3-phenylmethoxyphenyl)-1,3-thiazole-4-carbaldehyde Chemical compound O=CC1=CSC(C=2C=C(OCC=3C=CC=CC=3)C=CC=2)=N1 OEPOKWHJYJXUGD-UHFFFAOYSA-N 0.000 description 1
- JJRUAPNVLBABCN-UHFFFAOYSA-N 2-(ethenoxymethyl)oxirane Chemical compound C=COCC1CO1 JJRUAPNVLBABCN-UHFFFAOYSA-N 0.000 description 1
- PTJDGKYFJYEAOK-UHFFFAOYSA-N 2-butoxyethyl prop-2-enoate Chemical compound CCCCOCCOC(=O)C=C PTJDGKYFJYEAOK-UHFFFAOYSA-N 0.000 description 1
- FWWXYLGCHHIKNY-UHFFFAOYSA-N 2-ethoxyethyl prop-2-enoate Chemical compound CCOCCOC(=O)C=C FWWXYLGCHHIKNY-UHFFFAOYSA-N 0.000 description 1
- HFCUBKYHMMPGBY-UHFFFAOYSA-N 2-methoxyethyl prop-2-enoate Chemical compound COCCOC(=O)C=C HFCUBKYHMMPGBY-UHFFFAOYSA-N 0.000 description 1
- REEBWSYYNPPSKV-UHFFFAOYSA-N 3-[(4-formylphenoxy)methyl]thiophene-2-carbonitrile Chemical compound C1=CC(C=O)=CC=C1OCC1=C(C#N)SC=C1 REEBWSYYNPPSKV-UHFFFAOYSA-N 0.000 description 1
- ZNBNBTIDJSKEAM-UHFFFAOYSA-N 4-[7-hydroxy-2-[5-[5-[6-hydroxy-6-(hydroxymethyl)-3,5-dimethyloxan-2-yl]-3-methyloxolan-2-yl]-5-methyloxolan-2-yl]-2,8-dimethyl-1,10-dioxaspiro[4.5]decan-9-yl]-2-methyl-3-propanoyloxypentanoic acid Chemical compound C1C(O)C(C)C(C(C)C(OC(=O)CC)C(C)C(O)=O)OC11OC(C)(C2OC(C)(CC2)C2C(CC(O2)C2C(CC(C)C(O)(CO)O2)C)C)CC1 ZNBNBTIDJSKEAM-UHFFFAOYSA-N 0.000 description 1
- YEQPPBCBKNMCKW-UHFFFAOYSA-N 5-bicyclo[2.2.1]hept-2-enylmethyl 2-chloroacetate Chemical compound C1C2C(COC(=O)CCl)CC1C=C2 YEQPPBCBKNMCKW-UHFFFAOYSA-N 0.000 description 1
- INYHZQLKOKTDAI-UHFFFAOYSA-N 5-ethenylbicyclo[2.2.1]hept-2-ene Chemical compound C1C2C(C=C)CC1C=C2 INYHZQLKOKTDAI-UHFFFAOYSA-N 0.000 description 1
- HRPVXLWXLXDGHG-UHFFFAOYSA-N Acrylamide Chemical compound NC(=O)C=C HRPVXLWXLXDGHG-UHFFFAOYSA-N 0.000 description 1
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 239000004593 Epoxy Substances 0.000 description 1
- JIGUQPWFLRLWPJ-UHFFFAOYSA-N Ethyl acrylate Chemical compound CCOC(=O)C=C JIGUQPWFLRLWPJ-UHFFFAOYSA-N 0.000 description 1
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical compound COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 description 1
- GYCMBHHDWRMZGG-UHFFFAOYSA-N Methylacrylonitrile Chemical compound CC(=C)C#N GYCMBHHDWRMZGG-UHFFFAOYSA-N 0.000 description 1
- 235000021355 Stearic acid Nutrition 0.000 description 1
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 description 1
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 description 1
- 125000003545 alkoxy group Chemical group 0.000 description 1
- 125000000217 alkyl group Chemical group 0.000 description 1
- XYLMUPLGERFSHI-UHFFFAOYSA-N alpha-Methylstyrene Chemical compound CC(=C)C1=CC=CC=C1 XYLMUPLGERFSHI-UHFFFAOYSA-N 0.000 description 1
- 230000003712 anti-aging effect Effects 0.000 description 1
- 238000012662 bulk polymerization Methods 0.000 description 1
- COXYCFKHVQFUPA-UHFFFAOYSA-N but-2-enyl prop-2-enoate Chemical compound CC=CCOC(=O)C=C COXYCFKHVQFUPA-UHFFFAOYSA-N 0.000 description 1
- CQEYYJKEWSMYFG-UHFFFAOYSA-N butyl acrylate Chemical compound CCCCOC(=O)C=C CQEYYJKEWSMYFG-UHFFFAOYSA-N 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000003431 cross linking reagent Substances 0.000 description 1
- KBLWLMPSVYBVDK-UHFFFAOYSA-N cyclohexyl prop-2-enoate Chemical compound C=CC(=O)OC1CCCCC1 KBLWLMPSVYBVDK-UHFFFAOYSA-N 0.000 description 1
- 239000013013 elastic material Substances 0.000 description 1
- 238000007720 emulsion polymerization reaction Methods 0.000 description 1
- XJELOQYISYPGDX-UHFFFAOYSA-N ethenyl 2-chloroacetate Chemical compound ClCC(=O)OC=C XJELOQYISYPGDX-UHFFFAOYSA-N 0.000 description 1
- SUPCQIBBMFXVTL-UHFFFAOYSA-N ethyl 2-methylprop-2-enoate Chemical compound CCOC(=O)C(C)=C SUPCQIBBMFXVTL-UHFFFAOYSA-N 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 238000010528 free radical solution polymerization reaction Methods 0.000 description 1
- LNMQRPPRQDGUDR-UHFFFAOYSA-N hexyl prop-2-enoate Chemical compound CCCCCCOC(=O)C=C LNMQRPPRQDGUDR-UHFFFAOYSA-N 0.000 description 1
- 229910000378 hydroxylammonium sulfate Inorganic materials 0.000 description 1
- 239000003999 initiator Substances 0.000 description 1
- SINFYWWJOCXYFD-UHFFFAOYSA-N methoxymethyl prop-2-enoate Chemical compound COCOC(=O)C=C SINFYWWJOCXYFD-UHFFFAOYSA-N 0.000 description 1
- NFWSQSCIDYBUOU-UHFFFAOYSA-N methylcyclopentadiene Chemical compound CC1=CC=CC1 NFWSQSCIDYBUOU-UHFFFAOYSA-N 0.000 description 1
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 description 1
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 description 1
- 229940065472 octyl acrylate Drugs 0.000 description 1
- ANISOHQJBAQUQP-UHFFFAOYSA-N octyl prop-2-enoate Chemical compound CCCCCCCCOC(=O)C=C ANISOHQJBAQUQP-UHFFFAOYSA-N 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- PNJWIWWMYCMZRO-UHFFFAOYSA-N pent‐4‐en‐2‐one Natural products CC(=O)CC=C PNJWIWWMYCMZRO-UHFFFAOYSA-N 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 230000000379 polymerizing effect Effects 0.000 description 1
- ARJOQCYCJMAIFR-UHFFFAOYSA-N prop-2-enoyl prop-2-enoate Chemical compound C=CC(=O)OC(=O)C=C ARJOQCYCJMAIFR-UHFFFAOYSA-N 0.000 description 1
- VMBJJCDVORDOCF-UHFFFAOYSA-N prop-2-enyl 2-chloroacetate Chemical compound ClCC(=O)OCC=C VMBJJCDVORDOCF-UHFFFAOYSA-N 0.000 description 1
- PNXMTCDJUBJHQJ-UHFFFAOYSA-N propyl prop-2-enoate Chemical compound CCCOC(=O)C=C PNXMTCDJUBJHQJ-UHFFFAOYSA-N 0.000 description 1
- 239000012744 reinforcing agent Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000008117 stearic acid Substances 0.000 description 1
- 238000010557 suspension polymerization reaction Methods 0.000 description 1
- KUAZQDVKQLNFPE-UHFFFAOYSA-N thiram Chemical compound CN(C)C(=S)SSC(=S)N(C)C KUAZQDVKQLNFPE-UHFFFAOYSA-N 0.000 description 1
- 229960002447 thiram Drugs 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 235000014692 zinc oxide Nutrition 0.000 description 1
- 239000011787 zinc oxide Substances 0.000 description 1
Landscapes
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Description
(産業上の利用分野)
本発明は共役ジエン系単量体及びエポキシ基含
有不飽和単量体を使用する硫黄加硫可能なアクリ
ル共重合ゴムの製造方法に関するものである。
(従来の技術及び解決すべき問題点)
アクリルゴムはアクリル酸エステルを主成分と
する弾性体であり、一般に耐熱性、耐油性、耐オ
ゾン性などに優れたゴムとして知られているが、
ゴム分子主鎖に二重結合を有していないため、一
般には架橋点となる活性基を有する単量体を共重
合させたもが良く知られている。
架橋点となる単良体成分としては2−クロロエ
チルビニルエーテル、ビニルクロロアテート、ア
リルクロロアセテート、ビニルベンジルクロライ
ド、5−クロロアセトキシメチル−2−ノルボル
ネンなどの如きハロゲン系単量体あるいはアリル
グリシジルエーテル、グリシジルアクリレート、
グリシジルメタクリレートなどのエポキシ系単量
体が従来から良く使用されている。この様な単量
体成分を含むアクリルゴムは通常の硫黄あるいは
含硫黄有機化合物−加硫促進剤系では加硫するこ
とができず、アミン類、アンモニウム塩、金属石
鹸−硫黄などが架橋剤として一般に使用されてい
るが、加硫速度が遅く、最適な加硫物性を得るた
めには、長時間の熱処理を必要としなければなら
ないという欠点がある。又、アミン類、アンモニ
ウム塩の使用は、加硫中に臭気を発生したり、最
終製品が衛生の点から医薬用、食品用などの用途
に使用できないという欠点もある。さらに架橋用
単量体としてハロゲン系単量体を使用したアクリ
ルゴムでは、加硫時に金型を腐食させたり、製品
と接する金属を腐食させ問題となつている。この
様な欠点を改良するために、ジシクロペンタジエ
ン、メチルシクロペンタジエン、エチリデンノル
ボルネン、ビニリデンノルボルネン、ブタジエ
ン、イソプレン、ピペリレン、アクリルアクレー
ト、2−ブテニルアクリレート、トリアリルイソ
シアヌレートなどを架橋用単量体成分とする硫黄
加硫可能なアクリルゴムも既に知られているが、
加硫速度が十分でなく加硫物性、耐熱性、耐圧縮
永久ひずみ性など、実用上充分満足できるもので
はない。
(問題点を解決するための手段)
本発明者らは前記欠点を改善すべく種々検討し
た結果、架橋用単量体としてジエン系単量体とエ
ポキシ基含有不飽和単量体とを共重合させること
により、硫黄加硫可能で、実用特性の釣り合いの
とれたアクリル共重合ゴムが得られることを見い
だし、この知見に基づいて本発明を完成するに至
つた。
従つて、本発明の目的は従来のアクリルゴムの
特徴である耐熱性、耐油性、耐オゾン性を損うこ
となく、従来のアクリルゴムの欠点である加硫速
度がジエン系ゴムと同程度まで改良されたアクリ
ル共重合ゴムの製造方法を提供することにある。
本発明の目的は、(1)アルキルアクリレートおよ
びアルコキシアルキルアクリレートより選ばれる
少なくとも1種のアクリル酸エステル40〜99.4重
量%、(2)ジエン系単量体(1分子中に共重合可能
な共役炭素2重結合と非共役炭素2重結合を各々
1個以上含有する単量体を除く)0.5〜20重量%、
(3)エポキシ基含有不飽和単量体0.1〜10重量%、
(4)上記以外のモノビニル系およびモノビニリデン
系不飽和単量体より選ばれる少なくとも1種の単
量体0〜30重量%とをラジカル共重合させること
を特徴とするアクリル共重合ゴムの製造方法を用
いることにより達せられる。
本発明に使用される成分(1)のアルキルアクリレ
ートとしてはメチルアクリレート、エチルアクリ
レート、プロピルアクリレート、ブチルアクリレ
ート、ヘキシルアクリレート、シクロヘキシルア
クリレート、オクチルアクリレートなどが挙げら
れる。好ましくは炭素数1〜8、更に好ましくは
炭素数2〜4のアルキル基を有するアルキルアク
リレートである。また、アルコキシアルキルアク
リレートとしてはメトキシメチルアクリレート、
メトキシエチルアクリレート、エトキシエチルア
クリレート、ブトキシエチルアクリレートなどの
炭素数1〜4のアルコキシ基を有するものが好ま
しい例として挙げられる。
これらのアクリル酸エステルと使用量は使用全
単量体中(以下も同様)40〜99.4重量%、好まし
くは60〜98重量%である。また、アルキルアクリ
レートとアルコキシアルキルアクリレートを使用
して耐油性、耐寒性のバランスを満足させる場合
には、アルコキシアルキルアクリレートが20〜50
重量%の割合でアルキルアクリレートと併用され
ることが好ましい。
本発明に使用される成分(2)ジエン系単量体とし
てはブタジエン、メチルブタジエン、イソブレ
ン、ピペリレン、ベンタジエン、エチリデンノル
ボルネン、ビニルノルボルネンなどが挙げられ
る。本発明では、1分子中に共重合可能な共役炭
素2重結合と非共役炭素2重結合を各々1個以上
含有する単量体は使用されない。好ましくはブタ
ジエン、イソプレン、ピペリレンなどである。こ
れらジエン系単量体の使用量は0.5〜20重量%、
好ましくは1〜15重量%、より好ましくは1〜10
重量%である。0.5重量%以下では得られるアク
リル共重合ゴムの加硫速度が極めて遅くなる。ま
た20重量%以上になると得られるアクリル共重合
ゴムの加硫物は硬さが著しく高くなり、強度、伸
びの低下が著しい。
本発明に使用される成分(3)エポキシ基含有不飽
和単量体としてはビニルグリシジルエーテル、ア
リルグリシジルエーテル、グリシジルアクリレー
ト、グリシジルメタクリレートなどが挙げられ
る。好ましくはアリルグリシジルエーテル、グリ
シジルメタクリレートである。これらエポキシ基
含有不飽和単量体の使用量は0.1〜10重量%、好
ましくは0.5〜5重量%である。0.1重量%以下で
は得られるアクリル共重合ゴムの加硫物性は改善
されない。また10重量%以上になると得られるア
クリル共重合ゴムの加硫物の硬さが著しく高くな
り、強度、伸びその低下が著しい。
本発明に使用される成分(4)上記以外のモノビニ
ル系およびモノビニリデン系不飽和単量体は、得
られるアクリル共重合ゴムの機械的特性および耐
油性を改良するために必要に応じて用いるもので
あり、例えばモノビニル系化合物としては、アク
リロニトリル、酢酸ビニル、スチレン、α−メチ
ルスチレン、アクリルアミドのような単量体が挙
げられ、モノビニリデン系単量体としてはメチル
メタクリレート、エチルメタクリレート、メタク
リロニトリル、塩化ビニリデンのような単量体が
挙げられる。使用量は30重量%以下である。
本発明においては、前記単量体嵌合物を通常使
用されるラジカル開始剤を用いて乳化重合、懸濁
重合、溶液重合あるいは塊状重合など公知の重合
様式で重合することにより本発明のアクリル共重
合ゴムを容易に製造することができる。重合は回
分重合で行うか、または1種以上の成分単量体を
重合中に連続あるいは継続的に加えて行うことが
できる。重合温度は−10℃〜100℃の範囲である
が、好ましくは2〜80℃である。
かくして得られるアクリル共重合ゴムはジエン
系ゴムで通常使用される硫黄加硫系、補強剤、充
てん剤、可塑剤、老化防止剤などの配合剤を必要
に応じ添加し、混練、加硫することにより、従来
のアクリルゴムの利点である耐熱性、耐油性、耐
オゾン性などを損うことなく、従来のアクリルゴ
ムの欠点である加硫物性、耐圧縮永久ひずみ性を
改善し、実用特性の釣り合いのとれたアクリル共
重合ゴム加硫物を得ることができる。また、該共
重合ゴムは硫黄加硫系だけでなくパーオキサイド
加硫系も同様に使用できる。
本発明で得られるアクリル共重合ゴムの加硫物
は、耐熱性、耐オゾン性などを必要とする多くの
分野での用途に有用である。かかる用途として
は、ガスケツト、ホース、コンベアベルト、パツ
キン、オイルシールなど種々のゴム製品が挙げら
れる。
次に実施例により本発明を具体的に説明する
が、実施例により本発明が制限されるものではな
い。
実施例 1
第1表に示す重合処方に従つて、内容積10の
オートクレーブを使用し、30℃で重合反応を行つ
た。
転化率90%に達したのち、単量体100重量部当
り0.2重量部のヒドロキシルアミン硫酸塩を添加
し、反応を停止させた。反応終了跡、重合生成物
を塩析し、充分水洗した後減圧乾燥器にて乾燥さ
せて目的のアクリル共重合ゴムを得た。
(Industrial Application Field) The present invention relates to a method for producing a sulfur-vulcanizable acrylic copolymer rubber using a conjugated diene monomer and an epoxy group-containing unsaturated monomer. (Prior art and problems to be solved) Acrylic rubber is an elastic material whose main component is acrylic ester, and is generally known as a rubber with excellent heat resistance, oil resistance, ozone resistance, etc.
Since the main chain of the rubber molecule does not have a double bond, it is generally well known to copolymerize monomers with active groups that serve as crosslinking points. Examples of simple components that serve as crosslinking points include halogen monomers such as 2-chloroethyl vinyl ether, vinyl chloroacetate, allyl chloroacetate, vinylbenzyl chloride, 5-chloroacetoxymethyl-2-norbornene, and allyl glycidyl ether. , glycidyl acrylate,
Epoxy monomers such as glycidyl methacrylate have been commonly used. Acrylic rubber containing such monomer components cannot be vulcanized with ordinary sulfur or sulfur-containing organic compound-vulcanization accelerator systems, and amines, ammonium salts, metal soaps-sulfur, etc. are used as crosslinking agents. Although commonly used, they have the disadvantage of slow vulcanization rates and the need for long heat treatments to obtain optimal vulcanization properties. Furthermore, the use of amines and ammonium salts has the disadvantage that they generate odor during vulcanization and that the final product cannot be used for medical, food, or other purposes due to hygiene reasons. Furthermore, acrylic rubber that uses a halogen monomer as a crosslinking monomer has problems in that it corrodes the mold during vulcanization and corrodes the metal that comes into contact with the product. In order to improve these drawbacks, crosslinking monomers such as dicyclopentadiene, methylcyclopentadiene, ethylidene norbornene, vinylidene norbornene, butadiene, isoprene, piperylene, acryl acrylate, 2-butenyl acrylate, triallylisocyanurate, etc. Sulfur-curable acrylic rubber as a body component is already known, but
The vulcanization rate is not sufficient, and the vulcanization properties, heat resistance, compression set resistance, etc. are not fully satisfactory for practical purposes. (Means for Solving the Problems) As a result of various studies to improve the above drawbacks, the present inventors copolymerized a diene monomer and an epoxy group-containing unsaturated monomer as a crosslinking monomer. It was discovered that by doing so, an acrylic copolymer rubber that is sulfur-curable and has well-balanced practical properties can be obtained, and based on this knowledge, the present invention was completed. Therefore, the purpose of the present invention is to reduce the vulcanization rate, which is a disadvantage of conventional acrylic rubber, to the same level as diene rubber, without impairing the heat resistance, oil resistance, and ozone resistance, which are the characteristics of conventional acrylic rubber. An object of the present invention is to provide an improved method for producing acrylic copolymer rubber. The object of the present invention is to (1) 40 to 99.4% by weight of at least one acrylic ester selected from alkyl acrylates and alkoxyalkyl acrylates, (2) diene monomers (conjugated carbon atoms that can be copolymerized in one molecule). (excluding monomers containing one or more double bonds and one or more non-conjugated carbon double bonds) 0.5 to 20% by weight,
(3) 0.1 to 10% by weight of epoxy group-containing unsaturated monomer,
(4) A method for producing an acrylic copolymer rubber, comprising radical copolymerization with 0 to 30% by weight of at least one monomer selected from monovinyl and monovinylidene unsaturated monomers other than those mentioned above. This can be achieved by using Examples of the alkyl acrylate as component (1) used in the present invention include methyl acrylate, ethyl acrylate, propyl acrylate, butyl acrylate, hexyl acrylate, cyclohexyl acrylate, and octyl acrylate. Preferably it is an alkyl acrylate having an alkyl group having 1 to 8 carbon atoms, more preferably 2 to 4 carbon atoms. In addition, as alkoxyalkyl acrylate, methoxymethyl acrylate,
Preferred examples include those having an alkoxy group having 1 to 4 carbon atoms, such as methoxyethyl acrylate, ethoxyethyl acrylate, and butoxyethyl acrylate. The amount of these acrylic esters used is 40 to 99.4% by weight, preferably 60 to 98% by weight, based on the total monomers used (the same applies hereinafter). In addition, when using alkyl acrylate and alkoxyalkyl acrylate to satisfy the balance of oil resistance and cold resistance, alkoxyalkyl acrylate is
Preferably, it is used in combination with alkyl acrylate in a proportion by weight. The component (2) diene monomer used in the present invention includes butadiene, methylbutadiene, isobrene, piperylene, bentadiene, ethylidenenorbornene, vinylnorbornene, and the like. In the present invention, a monomer containing one or more each of one or more copolymerizable conjugated carbon double bonds and one or more nonconjugated carbon double bonds in one molecule is not used. Preferred are butadiene, isoprene, piperylene and the like. The amount of these diene monomers used is 0.5 to 20% by weight.
Preferably 1 to 15% by weight, more preferably 1 to 10% by weight
Weight%. If the amount is less than 0.5% by weight, the vulcanization rate of the resulting acrylic copolymer rubber becomes extremely slow. Furthermore, when the amount exceeds 20% by weight, the resulting acrylic copolymer rubber vulcanizate has a significantly increased hardness and a significant decrease in strength and elongation. Examples of component (3) epoxy group-containing unsaturated monomer used in the present invention include vinyl glycidyl ether, allyl glycidyl ether, glycidyl acrylate, and glycidyl methacrylate. Preferred are allyl glycidyl ether and glycidyl methacrylate. The amount of these epoxy group-containing unsaturated monomers used is 0.1 to 10% by weight, preferably 0.5 to 5% by weight. If the amount is less than 0.1% by weight, the vulcanized physical properties of the resulting acrylic copolymer rubber will not be improved. Moreover, when the amount exceeds 10% by weight, the hardness of the vulcanizate of the acrylic copolymer rubber obtained becomes extremely high, and the strength and elongation are significantly reduced. Component (4) used in the present invention: Monovinyl and monovinylidene unsaturated monomers other than those listed above are used as necessary to improve the mechanical properties and oil resistance of the resulting acrylic copolymer rubber. For example, monovinyl compounds include monomers such as acrylonitrile, vinyl acetate, styrene, α-methylstyrene, and acrylamide, and monovinylidene monomers include methyl methacrylate, ethyl methacrylate, and methacrylonitrile. , and monomers such as vinylidene chloride. The amount used is 30% by weight or less. In the present invention, the acrylic polymer of the present invention is produced by polymerizing the monomer composite using a commonly used radical initiator in a known polymerization mode such as emulsion polymerization, suspension polymerization, solution polymerization, or bulk polymerization. Polymerized rubber can be easily produced. The polymerization can be carried out batchwise or by adding one or more component monomers continuously or continuously during the polymerization. The polymerization temperature is in the range of -10°C to 100°C, preferably 2 to 80°C. The thus obtained acrylic copolymer rubber is kneaded and vulcanized with the addition of compounding agents such as sulfur vulcanization, reinforcing agents, fillers, plasticizers, and anti-aging agents, which are commonly used in diene rubbers, as necessary. This improves the vulcanizable properties and compression set resistance, which are the disadvantages of conventional acrylic rubber, without sacrificing the advantages of conventional acrylic rubber, such as heat resistance, oil resistance, and ozone resistance. A balanced acrylic copolymer rubber vulcanizate can be obtained. In addition, not only sulfur-cured copolymer rubber but also peroxide-vulcanized copolymer rubber can be used. The acrylic copolymer rubber vulcanizate obtained in the present invention is useful in many fields requiring heat resistance, ozone resistance, etc. Such uses include various rubber products such as gaskets, hoses, conveyor belts, packings, and oil seals. Next, the present invention will be specifically explained with reference to Examples, but the present invention is not limited to the Examples. Example 1 According to the polymerization recipe shown in Table 1, a polymerization reaction was carried out at 30°C using an autoclave with an internal volume of 10. After reaching 90% conversion, 0.2 parts by weight of hydroxylamine sulfate per 100 parts by weight of monomer was added to stop the reaction. After the completion of the reaction, the polymerization product was salted out, thoroughly washed with water, and then dried in a vacuum dryer to obtain the desired acrylic copolymer rubber.
【表】
タン
[Front] Tan
【表】
かくして得られた6種類のアクリル共重合ゴム
を下記の配合処方に従つて冷却下のオープンロー
ルにて配合物を調製し、次いで170℃で20分間プ
レス加硫を行い、その後、更にギヤーオーブン中
で150℃で16時間の熱処理を行つた。
これらの加硫物についてJISK−6301に準じて
加硫物の性質を測定した。得られた物性を第3表
に示した。
アクリル共重合ゴム(第2表参照) 100(重量部)
ステアリン酸 1
HAFカーボン 50
亜鉛華1号 3
硫黄 0.3
テトラメチルチウラムジサルフアイド
2 [Table] The six types of acrylic copolymer rubbers obtained in this way were prepared according to the formulation below using an open roll under cooling, and then press vulcanized at 170°C for 20 minutes. Heat treatment was carried out at 150° C. for 16 hours in a gear oven. The properties of these vulcanizates were measured according to JISK-6301. The obtained physical properties are shown in Table 3. Acrylic copolymer rubber (see Table 2) 100 (parts by weight) Stearic acid 1 HAF carbon 50 Zinc white No. 1 3 Sulfur 0.3 Tetramethylthiuram disulfide
2
【表】
実施例 2
実施例1の第1表重合処方に準じ、第4表で示
される単量体仕込み組成に従い、実施例1と同様
の重合反応および分離操作を行い、目的のアクリ
ル共重合ゴムを得た。[Table] Example 2 According to the polymerization recipe in Table 1 of Example 1, and according to the monomer charging composition shown in Table 4, the same polymerization reaction and separation operation as in Example 1 were carried out to obtain the desired acrylic copolymerization. Got the rubber.
【表】
かくして得られた11種類のアクリル共重合ゴム
を第5表の配合処方に従い冷却下のオープンロー
ルにて配合物を調製し、次いで170℃で20分間プ
レス加硫を行い、その後、更にギヤーオーブン中
で150℃で16時間の熱処理を行つた。
これらの加硫物についてJISK−6301に準じて
加硫物の性質を測定した。得られた物性を第6表
に示した。[Table] The 11 types of acrylic copolymer rubbers obtained in this way were prepared in an open roll under cooling according to the compounding recipe in Table 5, and then press vulcanized at 170°C for 20 minutes. Heat treatment was carried out at 150° C. for 16 hours in a gear oven. The properties of these vulcanizates were measured according to JISK-6301. The obtained physical properties are shown in Table 6.
【表】【table】
【表】
本発明で得られるアクリル共重合ゴムは第3表
および第6表に示したように、公知技術によるア
クリル共重合体では、プレス加硫、熱処理後の加
硫物性は実用上充分満足できるものではないのに
対し、本発明のアクリル共重合ゴムは、硫黄加硫
系を用いると、加硫物性、耐圧縮永久ひずみ性が
改善される。[Table] As shown in Tables 3 and 6, the acrylic copolymer rubber obtained by the present invention has vulcanized physical properties that are sufficiently satisfactory for practical use after press vulcanization and heat treatment. On the other hand, the acrylic copolymer rubber of the present invention has improved vulcanization properties and compression set resistance when a sulfur vulcanization system is used.
Claims (1)
ルキルアクリレートより選ばれる少なくとも1種
のアクリル酸エステル40〜99.4重量%、(2)ジエン
系単量体(1分子中に共重合可能な共役炭素2重
結合と非共役炭素2重結合を各々1個以上含有す
る単量体を除く)0.5〜20重量%、(3)エポキシ基
含有不飽和単量体0.1〜10重量%、(4)上記以外の
モノビニル系およびモノビニリデン系不飽和単量
体より選ばれる少なくとも1種の単量体0〜30重
量%とをラジカル共重合させることを特徴とす
る、硫黄系加硫剤および有機過酸化物により加硫
可能なアクリル共重合ゴムの製造方法。1 (1) 40 to 99.4% by weight of at least one acrylic ester selected from alkyl acrylates and alkoxyalkyl acrylates, (2) diene monomer (contains copolymerizable conjugated carbon double bonds and non-copolymerizable carbon double bonds in one molecule). (excluding monomers each containing one or more conjugated carbon double bonds) 0.5 to 20% by weight, (3) epoxy group-containing unsaturated monomers 0.1 to 10% by weight, (4) monovinyl series other than the above and Vulcanizable with a sulfur-based vulcanizing agent and an organic peroxide, characterized by radical copolymerization with 0 to 30% by weight of at least one monomer selected from monovinylidene unsaturated monomers. Method for producing acrylic copolymer rubber.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP19628684A JPS6173708A (en) | 1984-09-19 | 1984-09-19 | Production of acrylic copolymer rubber |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP19628684A JPS6173708A (en) | 1984-09-19 | 1984-09-19 | Production of acrylic copolymer rubber |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6173708A JPS6173708A (en) | 1986-04-15 |
JPH0481610B2 true JPH0481610B2 (en) | 1992-12-24 |
Family
ID=16355272
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP19628684A Granted JPS6173708A (en) | 1984-09-19 | 1984-09-19 | Production of acrylic copolymer rubber |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6173708A (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2005120143A (en) * | 2003-10-14 | 2005-05-12 | Jsr Corp | Epoxy-group-containing rubber, its production method, its composition, and laminate |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS53125493A (en) * | 1977-04-08 | 1978-11-01 | Kureha Chem Ind Co Ltd | Copolymer containing alkyl acrylates |
JPS5757707A (en) * | 1980-09-26 | 1982-04-07 | Asahi Chem Ind Co Ltd | Copolymer latex for self-adhesive and self-adhesive composition |
CA1188442A (en) * | 1981-12-21 | 1985-06-04 | Theodore D. Goldman | Diene/acrylate base impact modifier for pvc |
JPS59179511A (en) * | 1983-03-30 | 1984-10-12 | Japan Synthetic Rubber Co Ltd | Copolymer emulsion |
JPS60203615A (en) * | 1984-03-28 | 1985-10-15 | Japan Synthetic Rubber Co Ltd | Multicomponent copolymer rubber and production thereof |
-
1984
- 1984-09-19 JP JP19628684A patent/JPS6173708A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS6173708A (en) | 1986-04-15 |
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