JPH0768448B2 - Microwave Vulcanization Method for Epichlorohydrin Rubber - Google Patents
Microwave Vulcanization Method for Epichlorohydrin RubberInfo
- Publication number
- JPH0768448B2 JPH0768448B2 JP62120384A JP12038487A JPH0768448B2 JP H0768448 B2 JPH0768448 B2 JP H0768448B2 JP 62120384 A JP62120384 A JP 62120384A JP 12038487 A JP12038487 A JP 12038487A JP H0768448 B2 JPH0768448 B2 JP H0768448B2
- Authority
- JP
- Japan
- Prior art keywords
- rubber
- weight
- epichlorohydrin
- parts
- mol
- 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
- 238000004073 vulcanization Methods 0.000 title claims description 27
- 238000000034 method Methods 0.000 title claims description 16
- 229920005558 epichlorohydrin rubber Polymers 0.000 title description 12
- 229920001971 elastomer Polymers 0.000 claims description 54
- 239000005060 rubber Substances 0.000 claims description 54
- 239000000203 mixture Substances 0.000 claims description 51
- BRLQWZUYTZBJKN-UHFFFAOYSA-N Epichlorohydrin Chemical group ClCC1CO1 BRLQWZUYTZBJKN-UHFFFAOYSA-N 0.000 claims description 29
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 24
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 18
- 238000010438 heat treatment Methods 0.000 claims description 15
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 claims description 14
- 239000000292 calcium oxide Substances 0.000 claims description 14
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 claims description 14
- 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 claims description 13
- IAYPIBMASNFSPL-UHFFFAOYSA-N Ethylene oxide Chemical compound C1CO1 IAYPIBMASNFSPL-UHFFFAOYSA-N 0.000 claims description 12
- 239000003795 chemical substances by application Substances 0.000 claims description 11
- 229920001577 copolymer Polymers 0.000 claims description 10
- 238000001035 drying Methods 0.000 claims description 7
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 claims description 5
- 239000000920 calcium hydroxide Substances 0.000 claims description 5
- 229910001861 calcium hydroxide Inorganic materials 0.000 claims description 5
- VTHJTEIRLNZDEV-UHFFFAOYSA-L magnesium dihydroxide Chemical compound [OH-].[OH-].[Mg+2] VTHJTEIRLNZDEV-UHFFFAOYSA-L 0.000 claims description 5
- 239000000347 magnesium hydroxide Substances 0.000 claims description 5
- 229910001862 magnesium hydroxide Inorganic materials 0.000 claims description 5
- 239000000395 magnesium oxide Substances 0.000 claims description 5
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 claims description 5
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 claims description 5
- 150000002736 metal compounds Chemical class 0.000 claims description 3
- 230000004580 weight loss Effects 0.000 claims description 3
- 238000005187 foaming Methods 0.000 description 21
- 230000000052 comparative effect Effects 0.000 description 14
- 230000006835 compression Effects 0.000 description 11
- 238000007906 compression Methods 0.000 description 11
- 230000000704 physical effect Effects 0.000 description 11
- 230000000694 effects Effects 0.000 description 10
- 238000013329 compounding Methods 0.000 description 7
- 238000002156 mixing Methods 0.000 description 6
- -1 trithiol- s-triazine compound Chemical class 0.000 description 6
- 239000004709 Chlorinated polyethylene Substances 0.000 description 4
- 229910002012 Aerosil® Inorganic materials 0.000 description 3
- 239000002253 acid Substances 0.000 description 3
- 230000002411 adverse Effects 0.000 description 3
- 230000032683 aging Effects 0.000 description 3
- 229910052801 chlorine Inorganic materials 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 229920000642 polymer Polymers 0.000 description 3
- 238000010057 rubber processing Methods 0.000 description 3
- 229920001897 terpolymer Polymers 0.000 description 3
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 2
- PDQAZBWRQCGBEV-UHFFFAOYSA-N Ethylenethiourea Chemical compound S=C1NCCN1 PDQAZBWRQCGBEV-UHFFFAOYSA-N 0.000 description 2
- 239000000460 chlorine Substances 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 239000000470 constituent Substances 0.000 description 2
- 239000000178 monomer Substances 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- 229920006295 polythiol Polymers 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- UMGDCJDMYOKAJW-UHFFFAOYSA-N thiourea Chemical compound NC(N)=S UMGDCJDMYOKAJW-UHFFFAOYSA-N 0.000 description 2
- VXEGSRKPIUDPQT-UHFFFAOYSA-N 4-[4-(4-methoxyphenyl)piperazin-1-yl]aniline Chemical group C1=CC(OC)=CC=C1N1CCN(C=2C=CC(N)=CC=2)CC1 VXEGSRKPIUDPQT-UHFFFAOYSA-N 0.000 description 1
- 229910002016 Aerosil® 200 Inorganic materials 0.000 description 1
- 241000156978 Erebia Species 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 239000006087 Silane Coupling Agent Substances 0.000 description 1
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Natural products NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 1
- 238000005299 abrasion Methods 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 229910052910 alkali metal silicate Inorganic materials 0.000 description 1
- 125000005907 alkyl ester group Chemical group 0.000 description 1
- 230000003712 anti-aging effect Effects 0.000 description 1
- 238000001354 calcination Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000006229 carbon black Substances 0.000 description 1
- 125000001309 chloro group Chemical group Cl* 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 229920005561 epichlorohydrin homopolymer Polymers 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 238000010574 gas phase reaction Methods 0.000 description 1
- 229920001519 homopolymer Polymers 0.000 description 1
- 229920002681 hypalon Polymers 0.000 description 1
- OHOJRYNNXNLLOK-UHFFFAOYSA-N imidazolidine-2,4-dithione Chemical class S=C1CNC(=S)N1 OHOJRYNNXNLLOK-UHFFFAOYSA-N 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 238000010348 incorporation Methods 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 229920001084 poly(chloroprene) Polymers 0.000 description 1
- 239000012744 reinforcing agent Substances 0.000 description 1
- 239000005049 silicon tetrachloride Substances 0.000 description 1
- 229920006027 ternary co-polymer Polymers 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- 150000003585 thioureas Chemical class 0.000 description 1
- 239000004636 vulcanized rubber Substances 0.000 description 1
Landscapes
- Compositions Of Macromolecular Compounds (AREA)
Description
【発明の詳細な説明】 (産業上の利用分野) 本発明は、エピクロルヒドリン系ゴムをマイクロ波照射
によって加硫する方法に関する。TECHNICAL FIELD The present invention relates to a method for vulcanizing epichlorohydrin rubber by microwave irradiation.
(従来技術) 近年ゴム加工業界においては、チューブあるいはホース
等の連続加硫成形が可能なゴム材料について加硫工程に
おける省エネルギー化あるいは省力化のためにマイクロ
波加硫を行う動きが盛んになりつつある。しかし、耐油
性ゴム材料としてチューブやホースあるいはダイヤフラ
ム等の主に自動車関係部品に使用されるエピクロルヒド
リンゴムについては、上記マイクロ波加熱を利用した加
硫技術は加熱時の発泡の問題や加硫物の物性バランスの
問題があって未だ十分に検討されたとは言い難い。(Prior Art) In recent years, in the rubber processing industry, microwave vulcanization of rubber materials capable of continuous vulcanization molding such as tubes and hoses has become popular in order to save energy or labor in the vulcanization process. is there. However, as for the epichlorohydrin rubber mainly used for automobile-related parts such as tubes, hoses or diaphragms as the oil resistant rubber material, the vulcanization technology using the microwave heating described above is a problem of foaming at the time of heating and vulcanization products. It is hard to say that it has not been fully examined due to the problem of physical property balance.
(発明が解決しようとする問題点) 一般にゴムをマイクロ波によって加硫するに際して加熱
に伴う発泡を抑制するためには酸化カルシウムの添加が
有効であることが知られている。エピクロルヒドリンゴ
ムの場合酸化カルシウムによって発泡を抑制するために
は多量の添加が必要である。しかし、多量の配合はエピ
クロルヒドリンゴムにおいては、マイクロ波によって通
常行われる如き発熱作用とは逆に発熱温度が低下し、加
硫が十分に行われないという問題が起きた。また得られ
た加硫ゴムもその物性、特に引張強さ、耐圧縮永久歪性
及び耐水性が著しく低下して製品の品質を損う弊害も生
じた。(Problems to be Solved by the Invention) It is generally known that the addition of calcium oxide is effective for suppressing foaming due to heating when vulcanizing rubber by microwaves. In the case of epichlorohydrin rubber, it is necessary to add a large amount of calcium oxide in order to suppress foaming. However, in the case of blending a large amount of the compound, in the case of epichlorohydrin rubber, the exothermic temperature is lowered contrary to the exothermic action usually performed by microwaves, and there is a problem that the vulcanization is not performed sufficiently. In addition, the obtained vulcanized rubber also had the adverse effect of impairing the quality of the product because its physical properties, particularly tensile strength, compression set resistance and water resistance, were significantly reduced.
(問題を解決するための手段) 本発明者らは、上記の如き発泡や加硫物々性の低下のな
い、マイクロ波加硫可能なエピクロルヒドリン系ゴム加
硫用組成物を得る目的で鋭意検討を行った。その結果、
特定モノマー成分より構成されるエピクロルヒドリン共
重合体ゴム又はゴム混合物に特定量の酸化カルシウムと
酸化マグネシウム,水酸化マグネシウム又は水酸化カル
シウムとの併用及び特定含水量の乾式法もしくは焼成湿
式法によって得られたホワイトカーボンを配合したゴム
組成物が上記目的を達成するものであることを見出した
ものである。(Means for Solving the Problem) The inventors of the present invention have earnestly studied for the purpose of obtaining a microwave vulcanizable epichlorohydrin-based rubber vulcanizing composition that does not cause foaming and deterioration of vulcanizate properties as described above. I went. as a result,
Obtained by dry or calcination wet method with specific amount of calcium oxide and magnesium oxide, magnesium hydroxide or calcium hydroxide in combination with epichlorohydrin copolymer rubber or rubber mixture composed of specific monomer components It has been found that a rubber composition containing white carbon achieves the above object.
すなわち、本発明は、共重合体ゴム又はゴム混合物の構
成単位がエピクロルヒドリン50〜70モル%、エチレンオ
キサイド30〜50モル%、アリルグリシジルエーテル0〜
10モル%であるエピクロルヒドリン系ゴム100重量部に
対して、(イ)酸化カルシウム1〜6重量部、(ロ)酸
化マグネシウム,水酸化マグネシウム及び水酸化カルシ
ウムから選ばれる金属化合物1〜4重量部であり、且つ
上記(イ)成分及び(ロ)成分の合計量が2〜8重量
部、(ハ)30℃、50%RHにおける平衡吸着水分量であっ
て、105℃、4時間後の乾燥減量がそれぞれ2重量%以
下の乾式法ホワイトカーボン又は焼成湿式法ホワイトカ
ーボン5〜25重量部及び(ニ)上記ゴムの加硫剤を配合
した組成物をマイクロ波照射により加熱加硫することを
特徴とするエピクロルヒドリン系ゴムのマイクロ波加硫
方法である。That is, in the present invention, the constitutional unit of the copolymer rubber or the rubber mixture is epichlorohydrin 50 to 70 mol%, ethylene oxide 30 to 50 mol%, allyl glycidyl ether 0 to
1 to 4 parts by weight of (a) calcium oxide, 1 to 4 parts by weight of a metal compound selected from (b) magnesium oxide, magnesium hydroxide and calcium hydroxide, based on 100 parts by weight of epichlorohydrin rubber of 10 mol%. Yes, and the total amount of the above (a) component and (b) component is 2 to 8 parts by weight, (c) the equilibrium adsorbed water content at 30 ° C, 50% RH, and the loss on drying after 105 ° C for 4 hours Is 2% by weight or less of dry method white carbon or calcined wet method white carbon 5 to 25 parts by weight, and (d) a composition containing the rubber vulcanizing agent is heated and vulcanized by microwave irradiation. A method for microwave vulcanizing epichlorohydrin rubber.
本発明に用いられるエピクロルヒドリン系ゴムは、エピ
クロルヒドリン50〜70%モル、エチレンオキサイド30〜
50モル%、アリルグリシジルエーテル0〜10モル%より
構成される二元重合体ゴム、三共重合体ゴム又は上記構
成成分よりなるゴム混合物から選ばれる。The epichlorohydrin-based rubber used in the present invention comprises epichlorohydrin 50-70% mol, ethylene oxide 30-
It is selected from a binary polymer rubber, a terpolymer rubber or a rubber mixture composed of the above-mentioned constituents, which is composed of 50 mol% and 0 to 10 mol% of allyl glycidyl ether.
エピクロルヒドリン系ゴムがゴム混合物の場合は、エピ
クロルヒドリン単独重合体の他、上記モノマー成分から
構成される任意の組成の二元もしくは三元共重合体を適
宜ブレンドして上記モル組成範囲のゴム混合物にして用
いられる。When the epichlorohydrin-based rubber is a rubber mixture, in addition to the epichlorohydrin homopolymer, a binary or ternary copolymer of any composition composed of the above monomer components is appropriately blended to obtain a rubber mixture having the above molar composition range. Used.
ブレンド用ゴムの二元もしくは三元共重合体ゴムとして
は、エピクロルヒドリン10〜90モル%とエチレンオキサ
イド90〜10モル%との二元共重合体ゴム、エピクロルヒ
ドリン80〜99モル%とアリルグリシジルエーテル20〜1
モル%との二元共重合体ゴム、エピクロルヒドリン10〜
89モル%、エチレンオキサイド89〜10モル%及びアリル
グリシジルエーテル1〜20モル%との三元共重合体ゴム
などが好ましく用いられる。As the binary or terpolymer rubber of the blending rubber, a binary copolymer rubber of epichlorohydrin 10 to 90 mol% and ethylene oxide 90 to 10 mol%, epichlorohydrin 80 to 99 mol% and allyl glycidyl ether 20 ~ 1
Binary copolymer rubber with mol%, epichlorohydrin 10 ~
A terpolymer rubber of 89 mol%, 89 to 10 mol% of ethylene oxide and 1 to 20 mol% of allyl glycidyl ether is preferably used.
本発明のエピクロルヒドリン系ゴムにおいて、その構成
成分であるエピクロルヒドリンの上記組成割合が70モル
%を超えるか、あるいは50モル%より少ないとマイクロ
波による加熱の際に発泡を生じるようになるので好まし
くない。この発泡の原因としては上記範囲を超える場合
は、加熱により発生したガスが組成物を通過し難くなる
ことに主として起因し、上記範囲より少ない場合は、加
硫速度が発泡速度より遅くなることに主として起因する
ものと考えられる。In the epichlorohydrin-based rubber of the present invention, it is not preferable that the composition ratio of epichlorohydrin as a constituent component thereof exceeds 70 mol% or is less than 50 mol% because foaming will occur during heating by microwaves. As the cause of this foaming, if it exceeds the above range, it is mainly due to the fact that the gas generated by heating becomes difficult to pass through the composition, and if it is less than the above range, the vulcanization rate becomes slower than the foaming rate. It is thought to be mainly due to this.
本発明のエピクロルヒドリン系ゴムにアリルグリシジル
エーテルが導入されると耐熱老化性が特に優れた加硫物
となるので該成分の導入は好ましいものである。しか
し、アリルグリシジルエーテルの導入量が10モル%を超
えるとマイクロ波加熱の際発泡しやすくなることが分っ
た。これは加硫速度の低下によるものと考えられる。When allyl glycidyl ether is introduced into the epichlorohydrin-based rubber of the present invention, a vulcanized product having particularly excellent heat aging resistance is obtained, and therefore introduction of the component is preferable. However, it has been found that when the amount of allyl glycidyl ether introduced exceeds 10 mol%, foaming tends to occur during microwave heating. This is considered to be due to the decrease in vulcanization rate.
本発明に用いられるエピクロルヒドリン系ゴムは、共重
合体ゴム及びゴム混合物共に100℃におけるムニー粘度
が一般に使用されている40〜150程度のものでよいが、
良好な押し出し性、加硫物々性を得るためには50〜100
程度のものがより好ましい。The epichlorohydrin-based rubber used in the present invention may have a Munney viscosity at 100 ° C. of about 40 to 150, which is generally used for both the copolymer rubber and the rubber mixture,
50 to 100 for good extrusion and vulcanizability
The thing of a grade is more preferable.
本発明組成物に配合される(イ)成分の酸化カルシウム
は、エピクロルヒドリン100重量部に対して1〜6重量
部、好ましくは1〜4重量部の量が選ばれる。配合量が
1重量部未満では発泡抑制効果が小さく、また6重量部
を超えると後記するようにマイクロ波エネルギー効率が
低下すると共に加硫物性に悪影響を与える。The amount of calcium oxide of the component (a) to be blended in the composition of the present invention is 1 to 6 parts by weight, preferably 1 to 4 parts by weight, based on 100 parts by weight of epichlorohydrin. If the blending amount is less than 1 part by weight, the effect of suppressing foaming is small, and if it exceeds 6 parts by weight, the microwave energy efficiency is lowered and the vulcanized physical properties are adversely affected as described later.
本発明における酸化カルシウムの配合は組成物中の水分
を吸収し、マイクロ波加硫時の発泡を防ぐ目的で添加さ
れるものであり、マイクロ波加硫の添加剤として知られ
ているものである。しかしながら、本発明の如きエピク
ロルヒドリン系ゴムへの適用においては酸化カルシウム
の大量の配合はマイナス効果を生み、マイクロ波による
昇温効果が低下し、エネルギー効率を悪化させることが
判明した。また、得られた加硫物も物性中、引張強さ,
耐圧縮永久歪性,耐水性が損われるという弊害も現われ
た。本発明においては、上記の如く比較的少量の酸化カ
ルシウムと後記する(ロ)成分である酸化マグネシウ
ム,水酸化マグネシウム又は水酸化カルシウムとの併用
及び(ハ)成分の特定ホワイトカーボンとの組合せにお
いて、加硫時の発泡がなく、マイクロ波エネルギー効率
が良好で、かつ上記の如き物性に問題がなく、特に耐圧
縮永久歪性のよい加硫物が得られるものである。The compounding of calcium oxide in the present invention is added for the purpose of absorbing water in the composition and preventing foaming during microwave vulcanization, and is known as an additive for microwave vulcanization. . However, in the application to the epichlorohydrin-based rubber as in the present invention, it has been found that the incorporation of a large amount of calcium oxide has a negative effect, the heating effect by the microwave is lowered, and the energy efficiency is deteriorated. In addition, the vulcanizate thus obtained has the following physical properties: tensile strength,
It also had the adverse effect of impairing compression set resistance and water resistance. In the present invention, in combination with a relatively small amount of calcium oxide as described above and magnesium oxide, magnesium hydroxide or calcium hydroxide which is the component (b) described later, and in combination with the specific white carbon of the component (c), It is possible to obtain a vulcanized product which has no foaming during vulcanization, has good microwave energy efficiency, has no problems with the above-mentioned physical properties, and has particularly good compression set resistance.
本発明組成物において、上記酸化カルシウムと併用され
る(ロ)成分の酸化マグネシウム,水酸化マグネシウム
又は水酸化カルシウムの添加は、マイクロ波加硫時にお
ける発泡の抑制と共に、特に優れた耐圧縮永久歪性を得
ることにある。(ロ)成分の配合量はエピクロルヒドリ
ン系ゴム100重量部に対して1〜4重量部であり、1重
量部未満では上記耐圧縮永久歪性の向上効果が小さく、
また4重量部を超えると加硫物の耐水性が悪化するよう
になる。In the composition of the present invention, addition of magnesium oxide, magnesium hydroxide, or calcium hydroxide as the component (b) used in combination with the above-mentioned calcium oxide suppresses foaming during microwave vulcanization, and exhibits particularly excellent compression set resistance. To get sex. The compounding amount of the component (b) is 1 to 4 parts by weight with respect to 100 parts by weight of the epichlorohydrin rubber, and if it is less than 1 part by weight, the effect of improving the compression set resistance is small.
If it exceeds 4 parts by weight, the water resistance of the vulcanizate will deteriorate.
本発明組成物においては、加硫時の発泡抑制効果と良好
な耐圧縮永久歪性を得るためには、(ロ)成分と前記
(イ)成分の酸化カルシウムとの合計量がエピクロルヒ
ドリン系ゴム100重量部に対して少なくとも2重量部必
要であり、また得られた加硫物の良好な耐水性を保持す
るためには(イ)成分及び(ロ)成分の合計量で多くと
も8重量部、好ましくは6重量部に留めるべきである。In the composition of the present invention, in order to obtain the effect of suppressing foaming during vulcanization and good compression set resistance, the total amount of the component (b) and the calcium oxide of the component (a) is epichlorohydrin rubber 100. It is necessary to have at least 2 parts by weight with respect to parts by weight, and in order to maintain good water resistance of the obtained vulcanizate, the total amount of components (a) and (b) is at most 8 parts by weight, It should preferably remain at 6 parts by weight.
本発明において(イ)成分及び(ロ)成分と共に用いら
れる(ハ)成分の乾式法ホワイトカーボン又は焼成湿式
法ホワイトカーボンは、マイクロ波加硫の際発泡を生ず
ることなしに加硫物々性、特に耐水性を向上させる効果
がある。その配合量はエピクロルヒドリン100重量部に
対して5〜25重量部の範囲である。5重量部未満では上
記耐水性向上効果が小さく、また25重量部を超えると発
泡しやすくなると共に加硫物の耐圧縮永久歪性が損われ
る。The dry-process white carbon or the calcined wet-process white carbon of the component (c) used together with the component (a) and the component (b) in the present invention has vulcanized physical properties without causing foaming during microwave vulcanization, Especially, it has an effect of improving water resistance. The compounding amount is in the range of 5 to 25 parts by weight with respect to 100 parts by weight of epichlorohydrin. If it is less than 5 parts by weight, the above-mentioned water resistance improving effect is small, and if it exceeds 25 parts by weight, foaming tends to occur and the compression set resistance of the vulcanized product is impaired.
本発明に用いられる乾式法ホワイトカーボンとは、通常
四塩化珪素の熱分解等の気相反応によって製造されたも
のをいう。また焼成湿式法ホワイトカーボンとは、珪酸
アルカリの酸分解など湿式法によって製造されたホワイ
トカーボンを400〜900℃に焼成処理したものをいう。こ
れら乾式法もしくは焼成湿式法ホワイトカーボンは、30
℃、50%RHにおける平衡吸着水分量が2重量%以下のも
のが本発明の目的のためには好ましく、またその粒径は
1mμ〜50μのものが使用に適する。ゴム用ホワイトカー
ボンとして最も一般的に使用されている湿式法ホワイト
カーボンは、30℃、50%RHでの平衡吸着水分量が5重量
%を超えており、これを本発明に適用すると加熱時に発
泡するので不適当である。上記平衡吸着水分量の測定
は、105℃で4時間乾燥後の減量分を計量することによ
って行われる。本発明に用いられる乾式法ホワイトカー
ボンの市販品としてはアエロジル(日本アエロジル社)
があり、焼成湿式法ホワイトカーボンの市販品としては
カープレックスCS−5,CS−7(塩野義製薬社)がある。The dry-process white carbon used in the present invention refers to one produced by a gas phase reaction such as thermal decomposition of silicon tetrachloride. Further, the calcined wet method white carbon refers to white carbon produced by a wet method such as acid decomposition of alkali silicate and calcined at 400 to 900 ° C. These dry or calcined wet white carbons have 30
For the purpose of the present invention, it is preferable that the equilibrium adsorbed water content at ℃ and 50% RH is 2% by weight or less.
The one of 1 mμ to 50 μ is suitable for use. Wet method white carbon most commonly used as white carbon for rubber has an equilibrium adsorbed water content of more than 5% by weight at 30 ° C. and 50% RH. It is inappropriate because it does. The equilibrium adsorbed water content is measured by measuring the weight loss after drying for 4 hours at 105 ° C. Aerosil (Nippon Aerosil Co., Ltd.) is a commercially available product of the dry process white carbon used in the present invention.
There are Carplex CS-5 and CS-7 (Shionogi Pharmaceutical Co., Ltd.) as commercially available products of calcined wet method white carbon.
本発明に用いられる加硫剤は、エピクロルヒドリン系ゴ
ム中の塩素原子を介して加硫するタイプのものから単独
又は併用して用いられる。加硫物の物性、特に良好な耐
熱老化性を得る目的からはポリチオール類又はその誘導
体あるいはチオウレア類の加硫剤が好ましい。The vulcanizing agent used in the present invention is of a type in which epichlorohydrin-based rubber is vulcanized via a chlorine atom, and is used alone or in combination. Vulcanizing agents of polythiols or their derivatives or thioureas are preferable for the purpose of obtaining physical properties of the vulcanized product, particularly good heat aging resistance.
ポリチオール系加硫剤としては、ジ又はトリチオール−
s−トリアジン化合物(特公昭48−36926号公報)、2,5
−ジメルカプト−1,3,4−チアジアゾール化合物(米国
特許第4288576号明細書)、2,3−ジメルカプトピラジン
化合物(特公昭58−14468号公報)、2,3−ジメルカプト
キノキサリン化合物(特公昭58−14469号公報)、3,5−
ジメルカプト−1,2,4−トリアゾール化合物(特公昭57
−46463号公報)、2,4−ジチオヒダントイン化合物(特
公昭58−14467号公報、特公昭61−50505号公報、特開昭
57−34160号公報)などが挙げられる。As the polythiol vulcanizing agent, di- or trithiol-
s-triazine compound (Japanese Patent Publication No. 48-36926), 2,5
-Dimercapto-1,3,4-thiadiazole compound (U.S. Pat. No. 4,288,576), 2,3-dimercaptopyrazine compound (Japanese Patent Publication No. 58-14468), 2,3-dimercaptoquinoxaline compound (Japanese Patent Publication No. 58-14469), 3,5-
Dimercapto-1,2,4-triazole compound (JP-B-57
-46463), 2,4-dithiohydantoin compounds (Japanese Patent Publication No. 58-14467, Japanese Patent Publication No. 61-50505, Japanese Patent Laid-Open No.
57-34160).
チオウレア系加硫剤としては、2−メルカプトイミダゾ
リン(エチレンチオウレア)化合物、2−メルカプトピ
リミジン化合物(何れも特公昭43−5758号公報)などが
挙げられる。Examples of the thiourea-based vulcanizing agent include a 2-mercaptoimidazoline (ethylenethiourea) compound and a 2-mercaptopyrimidine compound (both JP-B-43-5758).
加硫剤の配合量はエピクロルヒドリン系ゴム100重量部
に対して0.1〜10重量部の範囲が適当である。The compounding amount of the vulcanizing agent is appropriately in the range of 0.1 to 10 parts by weight with respect to 100 parts by weight of epichlorohydrin rubber.
本発明組成物には、当該技術分野において通常行われる
ような各種の配合剤、例えば受酸剤、補強剤、充填剤、
シランカップリング剤、可塑剤、老化防止剤等の添加は
自由である。特に、マイクロ波による安定した高発熱性
を得るためにはカーボンブラックの配合は好ましく、通
常エピクロルヒドリン系ゴム100重量部に対して30〜100
重量部の範囲で添加することができる。The composition of the present invention contains various compounding agents such as those commonly used in the art, such as an acid acceptor, a reinforcing agent, a filler,
Addition of silane coupling agent, plasticizer, antiaging agent, etc. is free. In particular, in order to obtain stable high heat build-up by microwaves, it is preferable to add carbon black, and usually 30 to 100 parts by weight based on 100 parts by weight of epichlorohydrin rubber.
It can be added in the range of parts by weight.
本発明組成物の混合は、その混合順序には特に制約はな
く、混合機としては従来のゴム加工分野において利用さ
れているミキシングロール、バンバリーミキサーや各種
ニーダ類を利用することができる。The mixing order of the composition of the present invention is not particularly limited, and a mixing roll, a Banbury mixer or various kneaders used in the conventional rubber processing field can be used as a mixer.
本発明組成物を加硫させるマイクロ波は300〜3,000MHz
の電磁波であり、通常は2,450MHzと915MHzのいずれかが
利用される。マイクロ波連続加硫ラインでは、ゴム用押
出機又はベント式押出機から2〜50m/分程度で吐出され
たゴム組成物を、ベルトコンベアー等の搬送機を有し、
温度100〜250℃に保持された長さ0.5〜20m程度のマイク
ロ波加熱部に連続的に搬入して0.5〜50Kw程度の出力で1
50〜300℃程度まで加熱することによって加硫が行われ
るが、通常は更にこれを150〜300℃程度に加温された熱
風炉を通過させて加硫を完結せしめている。The microwave for vulcanizing the composition of the present invention is 300 to 3,000 MHz.
Electromagnetic waves, and either 2,450 MHz or 915 MHz is normally used. In the microwave continuous vulcanization line, the rubber composition discharged from the rubber extruder or the vent type extruder at about 2 to 50 m / min, has a conveyor such as a belt conveyor,
It is continuously loaded into a microwave heating unit with a length of about 0.5 to 20 m and maintained at a temperature of 100 to 250 ° C, and an output of about 0.5 to 50 Kw
Vulcanization is performed by heating to about 50 to 300 ° C, but normally, this is passed through a hot air oven heated to about 150 to 300 ° C to complete vulcanization.
本発明組成物から得られる連続加硫成形物は本組成物の
みからなる単一品の他、他のゴム組成物との積層体を押
出機から吐出させて積層体のまま加熱加硫することも可
能である。このような積層体の例としては、外層とし
て、クロロプレンゴム,クロルスルホン化ポリエチレ
ン,塩素化ポリエチレンなどの耐候性,耐オゾン性,耐
摩耗性等に特に優れたゴム組成物を用い、内層に本発明
組成物を用いた二層ゴム管を挙げることができる。特
に、塩素化ポリエチレンと塩素化エチレン−(メタ)ア
クリル酸の低級アルキルエステル共重合体との二元混合
物、あるいは該二元混合物に更にエピクロルヒドリン系
重合体を混合した三元混合物をゴム成分とした加硫用ゴ
ム組成物を本発明組成物との二層ゴム管の外層ゴムに用
いると非常に優れた接着性をもつ積層ゴム材料となるの
で大変好ましい。上記ゴムの二元もしくは三元混合物と
しては、通常知られている塩素含量20〜50重量%の塩素
化ポリエチレン5〜95重量%に塩素含量2〜45重量%の
塩素化エチレン−(メタ)アクリル酸の低級アルキルエ
ステル共重合体((メタ)アクリル酸の低級アルキルエ
ステル含量2〜20重量%)95〜5重量%を混合した二元
混合物、あるいは該二元混合物100重量部に対して、エ
ピクロルヒドリン単独重合体、エピクロルヒドリン−エ
チレンオキシド共重合体、エピクロルヒドリン−エチレ
ンオキシド−アリルグリシジルエーテル共重合体等のエ
ピクロルヒドリン系重合体3〜30重量部を混合した三元
混合物がゴム成分として好ましい。また本発明組成物を
二層ゴム管の外層として、また三層ゴム管の内層,外
層,中間層として用いることもできる。The continuous vulcanization molded product obtained from the composition of the present invention may be a single product consisting of the present composition alone, or a laminate with another rubber composition may be discharged from an extruder and heated and vulcanized as it is. It is possible. As an example of such a laminate, a rubber composition such as chloroprene rubber, chlorosulfonated polyethylene, or chlorinated polyethylene having excellent weather resistance, ozone resistance, and abrasion resistance is used as the outer layer, and A two-layer rubber tube using the inventive composition can be mentioned. In particular, the rubber component was a binary mixture of chlorinated polyethylene and a lower alkyl ester copolymer of chlorinated ethylene- (meth) acrylic acid, or a ternary mixture of the binary mixture further mixed with an epichlorohydrin-based polymer. It is very preferable to use the rubber composition for vulcanization for the outer rubber layer of the two-layer rubber tube with the composition of the present invention, since a laminated rubber material having very excellent adhesiveness is obtained. As a binary or ternary mixture of the above rubbers, there are commonly known chlorinated polyethylene having a chlorine content of 20 to 50% by weight and chlorinated polyethylene of 5 to 95% by weight and chlorinated ethylene- (meth) acrylic having a chlorine content of 2 to 45% by weight. Acid lower alkyl ester copolymer ((meth) acrylic acid lower alkyl ester content 2 to 20% by weight) Binary mixture of 95 to 5% by weight, or epichlorohydrin based on 100 parts by weight of the binary mixture. A ternary mixture obtained by mixing 3 to 30 parts by weight of an epichlorohydrin-based polymer such as a homopolymer, an epichlorohydrin-ethylene oxide copolymer and an epichlorohydrin-ethylene oxide-allyl glycidyl ether copolymer is preferable as the rubber component. Further, the composition of the present invention can be used as an outer layer of a two-layer rubber tube and as an inner layer, an outer layer or an intermediate layer of a three-layer rubber tube.
(実施例) 実施例1〜6 比較例1〜13 第1表A欄に示されるゴム組成物を内容量1.7のイン
ターナルミキサーで5分間混練し、これにB欄の配合剤
を加えて60〜70℃に加温した7インチロールで混練した
後リボン状に取出し、これを45mmφ、L/D16、圧縮比1.4
のスクリューと外径10mm、内径7mmの口金を有する押出
機に供給して5m/分の速度でチューブを連続成形した。
次いで上記速度で出力2Kw、2,450MHz、長さ2mのマイク
ロ波加熱部を通過させ、続いて有効長25m、250℃に加温
した熱風炉を通過させてチューブを加硫せしめた。得ら
れた加硫物について第2表に示されるような物性試験を
行った。(Examples) Examples 1 to 6 Comparative Examples 1 to 13 The rubber compositions shown in column A of Table 1 were kneaded with an internal mixer having an internal capacity of 1.7 for 5 minutes, and the compounding agent of column B was added to this to 60 After kneading with a 7-inch roll heated to ~ 70 ℃, take it out in a ribbon shape, 45mmφ, L / D16, compression ratio 1.4
The tube was continuously molded at a speed of 5 m / min by feeding it to an extruder having a screw and a die having an outer diameter of 10 mm and an inner diameter of 7 mm.
Next, the tube was vulcanized by passing it through a microwave heating unit having an output of 2 Kw, 2,450 MHz and a length of 2 m at the above speed, and then passing it through a hot air oven heated to 250 ° C. with an effective length of 25 m. The physical properties of the obtained vulcanized products were tested as shown in Table 2.
一方、上記方法において押出機の口金として直径25mmの
金型を用いて丸棒として押出した以外は同様にして加硫
物を得た。この加硫物を長さ12.7mmに切断して第2表に
示す圧縮永久歪試験に用いた。On the other hand, a vulcanized product was obtained in the same manner as in the above method, except that a die having a diameter of 25 mm was used as the die of the extruder and extruded as a round bar. This vulcanized product was cut to a length of 12.7 mm and used for the compression set test shown in Table 2.
なお、第2表におけるチューブの発泡状態は、マイクロ
波加熱部を出た直後のチューブを切断して16倍の顕微鏡
で断面を観察したものの結果であり、その評価は下記の
とおりである。In addition, the foaming state of the tube in Table 2 is the result of observing the cross section with a microscope of 16 times after cutting the tube immediately after leaving the microwave heating part, and the evaluation is as follows.
優:気泡が全く認められない。Excellent: No bubbles are recognized.
良:気泡が僅か認められる。Good: A few bubbles are recognized.
可:気泡が多数認められる。Acceptable: Many bubbles are recognized.
不可:スポンジ状 また、最終加硫物の発泡状態は、上記マイクロ波加熱後
の発泡状態の判定に沿った結果となることが実験によっ
て確められている。Impossible: Sponge-like shape It has been confirmed by experiments that the foamed state of the final vulcanized product has a result in accordance with the judgment of the foamed state after microwave heating.
第2表における物性試験は、チューブの発泡状態が可以
下のものについては行わなかった。The physical property test shown in Table 2 was not conducted for tubes whose foaming state was acceptable or less.
第1表において註(1)〜(7)のゴムと(8)〜(1
4)の配合剤は以下のものを用いた。In Table 1, notes (1) to (7) rubber and (8) to (1
The following were used as the compounding agents in 4).
(1)ムーニー粘度 55 (ML1+4(100℃)以下同
じ) (2)ムーニー粘度 65 構成比(モル) エピクロルヒドリン(EP)/エチレン
オキサイド(EO)=60/40 (3)ムーニー粘度 80 構成比(モル) EP/EO=40/60 (4)ムーニー粘度 50 構成比(モル) EP/EO=80/20 (5)ムーニー粘度 50 構成比(モル) EP/アリルグリシジルエーテル(AGE)
=95/5 (6)ムーニー粘度 60 構成比(モル) EP/EO/AGE=55/40/5 (7)ムーニー粘度 50 構成比(モル) EP/EO/AGE=60/25/15 (8)「アエロジル200」日本アエロジル社製 平衡吸着水分量(30℃、50%RH、以下同じ) 1.8重量% (但し、105℃、4時間後の減量値、以下同じ) (9)「カープレックスCS−5」塩野義製薬社製 平衡吸着水分量 2.0重量% (10)「ニップシルVN−3」日本シリカ社製 平衡吸着水分量 7.5重量% (11)「カープレックス#1120」塩野義製薬社製 平衡吸着水分量 6.6重量% (12)「シーストS」東海カーボン社製 (13)「アデカサイザーRS−700」アデカ アーガス化
学社製 (14)「C.M.L.#21」近江化学社製 第2表の結果から明らかなように、本発明組成物より得
られた加硫物は全く発泡が生じていない。しかも加硫物
の各物性においてもそれぞれ優れた結果が得られてい
る。特にゴム成分中にアリルグリシジルエーテルを含む
実施例5,6は耐熱老化性に優れ軟化し難いため、硬度及
び引張強さに優れた値を示している。また比較例6との
対比より明らかなように本発明組成物は(ロ)成分を含
むため加硫物の耐圧縮永久歪性が特に優れている。(1) Mooney viscosity 55 (ML1 + 4 (100 ° C) and below) (2) Mooney viscosity 65 Composition ratio (mol) Epichlorohydrin (EP) / Ethylene oxide (EO) = 60/40 (3) Mooney viscosity 80 Composition ratio (mol) ) EP / EO = 40/60 (4) Mooney viscosity 50 composition ratio (mol) EP / EO = 80/20 (5) Mooney viscosity 50 composition ratio (mol) EP / allyl glycidyl ether (AGE)
= 95/5 (6) Mooney viscosity 60 composition ratio (mol) EP / EO / AGE = 55/40/5 (7) Mooney viscosity 50 composition ratio (mol) EP / EO / AGE = 60/25/15 (8) ) "Aerosil 200" manufactured by Nippon Aerosil Co., Ltd. Equilibrium adsorbed water content (30 ° C, 50% RH, same below) 1.8% by weight (however, 105 ° C, weight loss after 4 hours, same below) (9) "Carplex CS -5 "Shionogi Pharmaceutical Co., Ltd. equilibrium adsorption water content 2.0% by weight (10)" NIPSIL VN-3 "Nihon Silica Co., Ltd. equilibrium adsorption water content 7.5% by weight (11)" Carplex # 1120 "Shionogi Pharmaceutical Co., Ltd. equilibrium Adsorbed water content 6.6% by weight (12) "Cast S" manufactured by Tokai Carbon Co., Ltd. (13) "ADEKA Sizer RS-700" manufactured by Adeka Argus Chemical Co., Ltd. (14) "CML # 21" manufactured by Omi Chemical Co., Ltd. As is clear from the results shown in Table 2, the vulcanized product obtained from the composition of the present invention did not cause foaming at all. In addition, excellent results have been obtained for each physical property of the vulcanized product. In particular, Examples 5 and 6 in which allyl glycidyl ether is contained in the rubber component are excellent in heat aging resistance and hard to be softened, and therefore show excellent values in hardness and tensile strength. Further, as is clear from comparison with Comparative Example 6, the composition of the present invention contains the component (b), and therefore the vulcanized product has particularly excellent compression set resistance.
これに対して、ホワイトカーボンとして湿式法のものを
用いた比較例1、比較例2及び比較例3、ホワイトカー
ボン量が過量の比較例5、酸化カルシウムを含まない比
較例7、ゴム組成比が本発明範囲外の比較例11,12、ゴ
ム組成比中エチレンオキサイド量及びアリルグリシジル
エーテル量が本発明範囲外の比較例13は、いずれもマイ
クロ波加硫時の発泡が著しいため発泡なしで加硫物を得
ることができず、特に比較例5,7は加硫物がスポンジ状
になっている。On the other hand, Comparative Example 1, Comparative Example 2 and Comparative Example 3 using the wet method as the white carbon, Comparative Example 5 with an excessive amount of white carbon, Comparative Example 7 containing no calcium oxide, the rubber composition ratio is Comparative Examples 11 and 12 outside the scope of the present invention, Comparative Example 13 in which the amount of ethylene oxide and the amount of allyl glycidyl ether in the rubber composition ratio are outside the scope of the present invention are all foamed at the time of microwave vulcanization, so that addition without foaming was performed. A vulcanizate could not be obtained, and particularly in Comparative Examples 5 and 7, the vulcanizate was sponge-like.
また、ホワイトカーボン量が零の比較例4は発泡なしで
加硫しているが加硫物の耐水性が著しく悪い。(イ)成
分の酸化カルシウム量が過量の比較例8,10と(ロ)成分
の金属化合物量が過量の比較例9は、(イ)成分と
(ロ)成分の合計量が本発明の範囲をも超えており、い
ずれも加硫物の耐水性が悪化している。また酸化カルシ
ウム量の多い比較例8,10はマイクロ波エネルギー効率が
やや悪化しており、耐圧縮永久性も悪い。Further, Comparative Example 4 in which the amount of white carbon is zero is vulcanized without foaming, but the water resistance of the vulcanized product is extremely poor. In Comparative Examples 8 and 10 in which the amount of calcium oxide of the component (a) is excessive and in Comparative Example 9 in which the amount of the metal compound of the component (b) is excessive, the total amount of the component (b) and the component (b) is within the range of the present invention. The water resistance of the vulcanizate is poor. Further, in Comparative Examples 8 and 10 having a large amount of calcium oxide, the microwave energy efficiency was slightly deteriorated and the compression resistance was also poor.
(発明の効果) エピクロルヒドリンゴムの従来の加硫方式である加熱炉
あるいは水蒸気加熱においては、加硫に数十分単位の時
間を必要とするため連続加硫が殆んど不可能であった
が、本発明に用いられる組成物では、マイクロ波エネル
ギー効率がよく、しかも発泡なしに分単位で加硫が十分
に行われ、加硫物性も優れているので連続加硫を必要と
するチューブ,ホース等の長尺物の成形用組成物として
非常に優れており、ゴム加工業界の省エネルギー化、省
力化の要請に十分応えることができるものである。(Effect of the Invention) In a heating furnace or steam heating which is a conventional vulcanization method of epichlorohydrin rubber, continuous vulcanization was almost impossible because vulcanization requires several tens of minutes. The composition used in the present invention has good microwave energy efficiency, is sufficiently vulcanized in minutes without foaming, and has excellent vulcanization physical properties. Therefore, a tube or a hose requiring continuous vulcanization. It is extremely excellent as a molding composition for long products such as the above, and can sufficiently meet the demand for energy saving and labor saving in the rubber processing industry.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 大浦 慶子 大阪府東大阪市鴻池町1−6−11 (72)発明者 的場 康夫 大阪府豊中市少路2−1−1−208 (56)参考文献 特開 昭56−109246(JP,A) 特開 昭54−135843(JP,A) 特開 昭58−32653(JP,A) ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Keiko Oura 1-6-11 Konoike-cho, Higashiosaka-shi, Osaka (72) Inventor Yasuo Matoba 2-1-1-208 Shoji, Toyonaka-shi, Osaka (56) References JP-A-56-109246 (JP, A) JP-A-54-135843 (JP, A) JP-A-58-32653 (JP, A)
Claims (1)
エピクロルヒドリン50〜70モル%、エチレンオキサイド
30〜50モル%、アリルグリシジルエーテル0〜10モル%
であるエピクロルヒドリン系ゴム100重量部に対して、
(イ)酸化カルシウム1〜6重量部、(ロ)酸化マグネ
シウム,水酸化マグネシウム及び水酸化カルシウムから
選ばれる金属化合物1〜4重量部であり、且つ上記
(イ)成分及び(ロ)成分の合計量が2〜8重量部、
(ハ)30℃、50%RHにおける平衡吸着水分量であって、
105℃、4時間後の乾燥減量がそれぞれ2重量%以下の
乾式法ホワイトカーボン又は焼成湿式法ホワイトカーボ
ン5〜25重量部及び(ニ)上記ゴムの加硫剤を配合した
組成物をマイクロ波照射により加熱加硫することを特徴
とするエピクロルヒドリン系ゴムのマイクロ波加硫方
法。1. A constitutional unit of a copolymer rubber or a rubber mixture is epichlorohydrin 50 to 70 mol%, ethylene oxide.
30-50 mol%, allyl glycidyl ether 0-10 mol%
With respect to 100 parts by weight of epichlorohydrin-based rubber,
(A) 1 to 6 parts by weight of calcium oxide, (b) 1 to 4 parts by weight of a metal compound selected from magnesium oxide, magnesium hydroxide and calcium hydroxide, and the total of the above (a) component and (b) component 2 to 8 parts by weight,
(C) Equilibrium adsorbed water content at 30 ° C and 50% RH,
Microwave irradiation of a composition containing 5 to 25 parts by weight of dry-process white carbon or calcined wet-process white carbon whose weight loss after drying at 105 ° C for 4 hours is 2% by weight or less and (d) a vulcanizing agent for the above rubber A method for microwave vulcanization of epichlorohydrin-based rubber, which comprises vulcanizing by heating with.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62120384A JPH0768448B2 (en) | 1987-05-18 | 1987-05-18 | Microwave Vulcanization Method for Epichlorohydrin Rubber |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62120384A JPH0768448B2 (en) | 1987-05-18 | 1987-05-18 | Microwave Vulcanization Method for Epichlorohydrin Rubber |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63284259A JPS63284259A (en) | 1988-11-21 |
| JPH0768448B2 true JPH0768448B2 (en) | 1995-07-26 |
Family
ID=14784876
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62120384A Expired - Lifetime JPH0768448B2 (en) | 1987-05-18 | 1987-05-18 | Microwave Vulcanization Method for Epichlorohydrin Rubber |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0768448B2 (en) |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS54135246A (en) * | 1978-04-11 | 1979-10-20 | Ito Sunao | Production of 100 percent buckwheat flour |
| JPS56109246A (en) * | 1980-02-04 | 1981-08-29 | Osaka Soda Co Ltd | Elastomer composition having excellent permanent compression set resistance |
| JPS5832653A (en) * | 1981-08-20 | 1983-02-25 | Osaka Soda Co Ltd | Vulcanizable rubber composition having improved rancidity and gasoline resistance |
-
1987
- 1987-05-18 JP JP62120384A patent/JPH0768448B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63284259A (en) | 1988-11-21 |
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