JPS6225175B2 - - Google Patents
Info
- Publication number
- JPS6225175B2 JPS6225175B2 JP4120882A JP4120882A JPS6225175B2 JP S6225175 B2 JPS6225175 B2 JP S6225175B2 JP 4120882 A JP4120882 A JP 4120882A JP 4120882 A JP4120882 A JP 4120882A JP S6225175 B2 JPS6225175 B2 JP S6225175B2
- Authority
- JP
- Japan
- Prior art keywords
- vulcanization
- zno
- amount
- cao
- 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
Links
Landscapes
- Compositions Of Macromolecular Compounds (AREA)
Description
本発明はエチレン・プロピレン・ジエン三元共
重合ゴム(以下EPDMという)を基材に用いて、
厚生省434号に合格する食品用途各種ゴム製品を
常圧連続押出加硫方法で製造することが可能なゴ
ム組成物(以下コンパウンドという)を得ること
に関する。EPDMは優れた耐候性、耐熱性、耐水
性、耐薬品性を備えていることにより、これらの
特性を要求される食品用途ゴム製品、すなわち、
コーヒーサイホン用ゴム、圧力なベパツキン、も
ちつき器パツキン、ソーラー温水器用ホース類等
に適用されている。
この様な製品を生産する方法としては、プレス
加硫、インジエクシヨン加硫、押出缶加硫が用い
られているのが一般的である。ところが、ソーラ
ー温水器用ホースの様に押出し成型が必要でかつ
長尺の製品が要求される場合、従来の缶加硫方式
では対応することが困難であるばかりでなく、生
産性の点で常圧連続加硫、すなわち塩浴加硫
(LCM)、熱空気加硫(HAV)、高周波加硫
(UHF)、流動床加硫(PCM)に比べて著しく劣
つている問題をかかえている。
本発明者は鋭意研究の結果、この様な欠点を補
う為、常圧連続加硫方式(以下CV方式)によつ
て厚生省告示434号を合格するゴム製品を得るコ
ンパウンドを見出した。
CV方式と缶加硫方式に用いるコンパウンドの
主な違いは、CV方式には消泡剤として生石灰
(以下CaO)が必要不可欠であるが、缶加硫方式
には不要であるという点である。缶加硫方式では
加硫工程でコンパウンド中の水分が蒸発するのを
外圧により押え込んで、ゴム製品の発泡を防止し
ているのを特徴とするのに対して、CV方式の場
合CaOを配合することにより、コンパウンド中の
水分を安定なCa(OH)2に変換させ発泡を防止し
ているのが一般的な方法である。
厚生省告示434号に合格する製品を得る場合の
ゴム用配合剤を選択するにあたり考慮すべき点
は、配合剤もしくは加硫による反応生成物が、厚
生省告示434号の蒸発残留物の項で規定する抽出
液すなわち4%の酢酸水溶液に対し可溶性である
か否かということである。すなわち当然のことな
がら可溶性であれば、蒸発残留物を著しく多くす
る要因となる。CaOを配合することにより生成す
るCa(OH)2は4%酢酸水溶液に可溶性であるこ
とからCaOを配合したコンパウンドから得た、ゴ
ム製品は厚生省告示434号の蒸発残留物(以下蒸
発残)の規制値を相当上まわることが予測出来
る。
また亜鉛華(ZnO)はゴムの加硫反応に不可欠
な加硫活性剤であるがこれも4%酢酸水溶液に可
溶性であることから同様な欠点を備えている。
缶加硫方式に用いられるコンパウンドは前述し
た様にCaOを配合する必要がなく、蒸発残を多く
する配合剤としては、亜鉛華、カーボンブラツ
ク、タルク、クレー等であるが、特に著しく影響
を及ぼすのはZnOである。通常のゴム製品に用い
られているZnOの配合量は3〜6重量部(以下
PHR)程度であるが、過去の研究でこの配合量
では蒸発残を合格することが可能であることが実
証されている。本発明者ら出願特開昭54−78745
号を参照。
しかし、CV方式の様に蒸発残を特に多くする
様な配合剤を複数種類(ZnOとCaO)配合するこ
とが必要なコンパウンドを用いた場合、蒸発残を
合格することが難しくなることは云うまでもな
い。
本発明者は、前述した様なCV方式に用いるコ
ンパウンドの欠点を解消する方法を種々検討した
結果、ZnOと炭素数が比較的少い脂肪酸亜鉛塩と
を併用することにより、ZnOの配合量を通常の配
合量に比べ著しく少くすることが可能になつた結
果、CaOを配合しても厚生省告示434号の蒸発残
を規制値以下に保ち、かつ、CV方式において製
品の発泡が防止出来るコンパウンドを発見した。
一般に厚生省告示434号を合格するCV方式用コ
ンパウンドを得るにはEPDMに限られた補強剤、
充てん剤及び限られた加硫促進剤、更にZnO、
CaO等の適量配合することが最低限必要である。
ここで限られた補強剤、充てん剤及び加硫系と
は、本発明者が先に特許出願した特開昭54−
78745に準拠するものである。
すなわち、補強剤とはカーボンブラツク(フア
ーネスブラツク)、充てん剤とはクレー、タルク
類であるが、カーボンブラツク単独の配合系が最
も好ましい。
本発明はCV方式によりゴム製品を得るのに必
要なZnO、CaOの配合量を可能な限り少くなくす
るという発想に基づくものであるが、鋭意検討し
た結果、不都合な点が生ずることが分つた。
すなわち、ZnOの配合量を減少するに従い蒸発
残は減少し好結果につながるが、著しく加硫度が
低下する傾向が現われ、圧縮永久歪、引張強度、
永久伸び等のゴム物性が悪化する。
また加硫速度が遅くなる程、CV方式により得
られるゴム製品中の発泡現象がより著しくなる
為、発泡防止の為にCaOの配合量を増加せねばな
らない結果となり、蒸発残を減少するという目的
を満たすことが出来ない。第1図および第2図に
これらの関係を示した。第1図は、第1表に示し
た基本配合による加硫ゴム組成物において、亜鉛
華1号の配合量と、加硫物の圧縮永久歪および蒸
発残留物量の関係を示したものである。
第2図は、第1表に示した基本配合による加硫
ゴム組成物において、亜鉛華1号およびCaOの配
合量と、加硫物の蒸発残留物量の関係を示したも
のである。
なお、加硫条件は、いずれも160℃×30分、プ
レス加硫で行なつた。
The present invention uses ethylene-propylene-diene ternary copolymer rubber (hereinafter referred to as EPDM) as a base material,
This invention relates to obtaining a rubber composition (hereinafter referred to as a compound) that can be used to produce various rubber products for food use that pass the Ministry of Health and Welfare No. 434 by an ordinary pressure continuous extrusion vulcanization method. EPDM has excellent weather resistance, heat resistance, water resistance, and chemical resistance, so it is suitable for food-use rubber products that require these properties.
It is applied to rubber for coffee siphons, pressure pads, mochi maker pads, hoses for solar water heaters, etc. Press vulcanization, in-die extension vulcanization, and extrusion can vulcanization are generally used to produce such products. However, when long products that require extrusion molding, such as hoses for solar water heaters, are not only difficult to handle using the conventional can vulcanization method, but also normal pressure is not suitable for productivity. It has the problem of being significantly inferior to continuous vulcanization, that is, salt bath vulcanization (LCM), hot air vulcanization (HAV), high frequency vulcanization (UHF), and fluid bed vulcanization (PCM). As a result of intensive research, the present inventors have discovered a compound that can be used to make rubber products that pass the Ministry of Health and Welfare Notification No. 434 using a normal pressure continuous vulcanization method (hereinafter referred to as the "CV method") in order to compensate for these drawbacks. The main difference between the compounds used in the CV method and the can vulcanization method is that the CV method requires quicklime (CaO) as an antifoaming agent, but the can vulcanization method does not require it. The can vulcanization method uses external pressure to suppress the evaporation of water in the compound during the vulcanization process, preventing foaming of the rubber product, whereas the CV method contains CaO. A common method is to convert the water in the compound into stable Ca(OH) 2 and prevent foaming. Points to consider when selecting a compounding agent for rubber in order to obtain a product that passes the Ministry of Health and Welfare Notification No. 434 are that compounding agents or reaction products from vulcanization are specified in the evaporation residue section of the Ministry of Health and Welfare Notification No. 434. The question is whether or not it is soluble in the extract, that is, a 4% acetic acid aqueous solution. That is, as a matter of course, if it is soluble, it becomes a factor that significantly increases the amount of evaporation residue. Since Ca(OH) 2 produced by blending CaO is soluble in a 4% acetic acid aqueous solution, rubber products obtained from compounds containing CaO are subject to evaporation residue (hereinafter referred to as evaporation residue) according to Ministry of Health and Welfare Notification No. 434. It can be predicted that the amount will exceed the regulation value considerably. Zinc white (ZnO) is a vulcanization activator essential for the vulcanization reaction of rubber, but it also has the same drawback because it is soluble in a 4% acetic acid aqueous solution. As mentioned above, the compound used in the can vulcanization method does not need to contain CaO, and the additives that increase the amount of evaporation residue include zinc white, carbon black, talc, clay, etc., but they have a particularly significant effect. is ZnO. The amount of ZnO used in ordinary rubber products is 3 to 6 parts by weight (hereinafter referred to as
PHR), but past research has demonstrated that it is possible to pass the evaporation residue level with this blending amount. The present inventors applied for Japanese Patent Application Publication No. 54-78745.
See issue. However, it goes without saying that when using a compound that requires the combination of multiple types of compounding agents (ZnO and CaO) that produce a particularly large amount of evaporation residue, such as the CV method, it becomes difficult to pass the evaporation residue test. Nor. As a result of various studies on ways to overcome the drawbacks of the compound used in the CV method as described above, the inventor of the present invention found that the amount of ZnO can be reduced by using ZnO together with a fatty acid zinc salt having a relatively small number of carbon atoms. As a result, we have developed a compound that can keep the evaporation residue below the regulated value in Ministry of Health and Welfare Notification No. 434 even if CaO is added, and prevent foaming of products in the CV method. discovered. In general, to obtain a compound for CV method that passes Ministry of Health and Welfare Notification No. 434, reinforcing agent limited to EPDM,
Fillers and limited vulcanization accelerators, plus ZnO,
The minimum requirement is to incorporate an appropriate amount of CaO, etc. The limited reinforcing agents, fillers, and vulcanization systems here refer to JP-A No. 54-117, for which the present inventor previously applied for a patent.
78745. That is, although the reinforcing agent is carbon black (furnace black) and the filler is clay or talc, a blending system containing carbon black alone is most preferable. The present invention is based on the idea of minimizing the amount of ZnO and CaO necessary to obtain rubber products using the CV method, but as a result of intensive study, it was found that there were some disadvantages. . In other words, as the blending amount of ZnO decreases, the evaporation residue decreases, leading to good results, but there is a tendency for the degree of vulcanization to decrease significantly, and compression set, tensile strength,
Rubber physical properties such as permanent elongation deteriorate. In addition, as the vulcanization rate becomes slower, the foaming phenomenon in the rubber products obtained by the CV method becomes more pronounced, which results in the need to increase the amount of CaO blended to prevent foaming, and the purpose is to reduce evaporation residue. cannot be fulfilled. These relationships are shown in FIGS. 1 and 2. FIG. 1 shows the relationship between the blending amount of Zinc White No. 1 and the compression set and evaporation residue amount of the vulcanizate in a vulcanized rubber composition having the basic formulation shown in Table 1. FIG. 2 shows the relationship between the blending amounts of Zinc White No. 1 and CaO and the amount of evaporation residue of the vulcanizate in a vulcanized rubber composition having the basic formulation shown in Table 1. The vulcanization conditions were press vulcanization at 160° C. for 30 minutes.
【表】
ここで本発明者はZnOに代わる加硫活性剤とし
て、各種脂肪酸亜鉛、及び有機亜鉛化合物等の適
用を試みた結果、オクチル酸亜鉛等の炭素数7以
上13以下の脂肪酸亜鉛塩は著しい加硫活性効果が
有ることを発見した。
これ以外の有機酸亜鉛塩も蒸発残の減少には効
果を有するがステアリン酸亜鉛で代表される炭素
数14以上の脂肪酸亜鉛は加硫活性効果が小さい、
すなわち加硫速度が遅く圧縮永久歪が大きい、更
にゴム製品の表面に脂肪酸及びその他の配合剤が
析出する現象すねわちブリードが生じ好ましい製
品が得られない欠点がある。
さらに炭素数6以下の脂肪酸亜鉛塩及び脂肪酸
以外の有機酸亜鉛塩として酢酸亜鉛、アセチルア
セトン亜鉛、ナフテン酸亜鉛等はそれぞれコンパ
ウンドに不溶性であり、著しい悪臭が有る、加硫
活性効果が少い等、いずれも問題点を備えており
実用性の点で適用することが不可能である。
一方、ZnOの代りに炭素数7以上13以下の脂肪
酸亜鉛塩を配合したコンパウンドは他の類似化合
物を配合したコンパウンドが備えている欠点を補
うのみならず、ZnOを単独で配合したコンパウン
ドに比べ初期の加硫活性効果がより顕著であるこ
とから、CV方式により生産する場合には製品の
形状保持性、ラインの高速化等の面で好ましい要
因となるが、その反面、ZnOに比べ加硫活性の持
続性に欠けるという欠点を備えている。
しかし、本発明者は炭素数7以上13以下の脂肪
酸亜鉛塩とZnOを併用することにより、この欠点
を改めることに成功した。
すなわち、炭素数7以上13以下の脂肪酸亜鉛塩
で加硫反応の初期活性を持たせ、ZnOで持続性を
持たせるという発想に基づくものである。
特に炭素数7以上13以下の脂肪酸亜鉛塩を配合
した効果はきわだつており、ZnOの配合量を減少
させる効果があるばかりか、加硫速度を著しく促
進する為CaOの配合量を少量にしえる。
この結果厚生省告示434号の蒸発残を規格値以
下に保つことが非常に有利になつたばかりか、
CaOを配合することにより著しく悪化する圧縮永
久歪を向上させる効果もあることを見付けだし
た。
本発明者は更にこの点を追求した結果、食品用
途に適用されるゴム製品の外観、物性、及び厚生
省434号等をバランスさせるには、炭素数7以上
13以下の脂肪酸亜鉛塩ZnO、CaOをそれぞれ適量
配合する必要が有ることを見い出した。
すなわち、炭素数7以上13以下の脂肪酸亜鉛塩
は0.1〜6PHR、ZnOは0.1〜3PHR、CaOは0.5〜
3PHRの範囲内で併用することが望ましいが、さ
らにCV方式において、特に生産性を重視するの
であればオクチル酸亜鉛は1〜3PHR、ZnOは1
〜2PHR、CaOは1〜2.5PHRを配合することが
好ましい。ZnOを配合せず、炭素数7以上13以下
の脂肪酸亜鉛塩を単純に増量した配合例では、加
硫活性の持続性は若干改良されるものの、ZnO、
炭素数7以上13以下の脂肪酸亜鉛塩を併用したケ
ース程改良効果は無かつた。
本発明のEPDMとはエチレン・プロピレン・ジ
シクロペンタジエン三元共重合ゴム、エチレン・
プロピレン・2―エチリデンノルボーネン三元共
重合ゴム、エチレン・プロピレン・1,4―ヘキ
サジエン三元共重合ゴム等である。以下実施例を
示す。しかし本発明は実施例に限定されるもので
はない。
実施例
第2表に、配合処方、加硫条件および得られた
加硫ゴムの諸物性を示した。[Table] As a result of trying to apply various zinc fatty acids and organic zinc compounds as vulcanization activators in place of ZnO, the inventor found that zinc salts of fatty acids with carbon atoms of 7 to 13, such as zinc octylate, It was discovered that it has a significant vulcanization activity effect. Other organic acid zinc salts are also effective in reducing evaporation residue, but fatty acid zinc with 14 or more carbon atoms, represented by zinc stearate, has a small vulcanization activity effect.
That is, the vulcanization rate is slow, the compression set is large, and fatty acids and other compounding agents precipitate on the surface of the rubber product, which causes bleeding, making it difficult to obtain a desirable product. Furthermore, zinc acetate, zinc acetylacetone, zinc naphthenate, etc. as zinc salts of fatty acids with carbon atoms of 6 or less and zinc salts of organic acids other than fatty acids are insoluble in compounds, have a significant odor, have little vulcanization activation effect, etc. All of them have problems and cannot be applied in terms of practicality. On the other hand, a compound containing zinc salt of a fatty acid having 7 to 13 carbon atoms instead of ZnO not only compensates for the drawbacks of compounds containing other similar compounds, but also improves initial performance compared to compounds containing ZnO alone. Since the vulcanization activity effect of ZnO is more pronounced, it is a favorable factor in terms of product shape retention and line speedup when produced by the CV method. The disadvantage is that it lacks sustainability. However, the present inventor succeeded in correcting this drawback by using ZnO in combination with a fatty acid zinc salt having 7 to 13 carbon atoms. That is, it is based on the idea that initial activity of the vulcanization reaction is provided by a fatty acid zinc salt having 7 or more and 13 or less carbon atoms, and sustainability is provided by ZnO. In particular, the effect of blending a fatty acid zinc salt with a carbon number of 7 or more and 13 or less is remarkable, and it not only has the effect of reducing the blended amount of ZnO, but also significantly accelerates the vulcanization rate, making it possible to reduce the blended amount of CaO. As a result, it has not only become very advantageous to keep the evaporation residue below the standard value according to Ministry of Health and Welfare Notification No. 434, but also
It has been found that the addition of CaO has the effect of improving compression set, which is significantly worse. As a result of further pursuing this point, the present inventor found that in order to balance the appearance, physical properties, and Ministry of Health and Welfare No. 434 of rubber products applied to food applications, the number of carbon atoms must be 7 or more.
It has been found that it is necessary to mix appropriate amounts of fatty acid zinc salts ZnO and CaO with a weight of 13 or less. In other words, fatty acid zinc salt with carbon number of 7 to 13 is 0.1 to 6 PHR, ZnO is 0.1 to 3 PHR, and CaO is 0.5 to 6 PHR.
It is desirable to use them together within the range of 3PHR, but in the CV method, if productivity is particularly important, zinc octylate should be used in the range of 1 to 3PHR, and ZnO should be used in the range of 1 to 3PHR.
~2PHR, and CaO is preferably blended in an amount of 1 to 2.5PHR. In a formulation example in which ZnO is not blended and the amount of fatty acid zinc salt having 7 or more and 13 or less carbon atoms is simply increased, the sustainability of vulcanization activity is slightly improved, but ZnO,
The improvement effect was not as great as in the case where a fatty acid zinc salt having 7 to 13 carbon atoms was used in combination. EPDM of the present invention is ethylene/propylene/dicyclopentadiene terpolymer rubber, ethylene/propylene/dicyclopentadiene ternary copolymer rubber,
These include propylene/2-ethylidenenorbornene ternary copolymer rubber, ethylene/propylene/1,4-hexadiene ternary copolymer rubber, and the like. Examples are shown below. However, the present invention is not limited to the examples. Examples Table 2 shows the formulation, vulcanization conditions, and physical properties of the obtained vulcanized rubber.
【表】【table】
第1図は、EPDM加硫ゴム組成物における亜鉛
華1号の配合量と、加硫物の圧縮永久歪および蒸
発残留物量の関係図であり、第2図は、同じく亜
鉛華1号およびCaOの配合量と、加硫物の蒸発残
留物の量の関係図である。
Figure 1 is a diagram showing the relationship between the blending amount of zinc white No. 1 in an EPDM vulcanized rubber composition and the compression set and evaporation residue amount of the vulcanizate. FIG. 2 is a diagram showing the relationship between the amount of vulcanizate and the amount of evaporation residue of the vulcanizate.
Claims (1)
ム100重量部に対して、亜鉛華1号0.1〜5重量
部、炭素数7以上13以下の脂肪酸亜鉛塩を0.1〜
6重量部、酸化カルシウムを0.1〜5重量部を配
合することを特徴とする厚生省告示434号の蒸発
残留物の基準に合格するゴム組成物。1. For 100 parts by weight of ethylene-propylene-diene ternary copolymer rubber, add 0.1 to 5 parts by weight of Zinc White No. 1 and 0.1 to 5 parts by weight of fatty acid zinc salt having 7 to 13 carbon atoms.
6 parts by weight of calcium oxide, and 0.1 to 5 parts by weight of calcium oxide.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4120882A JPS58157842A (en) | 1982-03-15 | 1982-03-15 | Rubber composition for use of food and hygiene |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4120882A JPS58157842A (en) | 1982-03-15 | 1982-03-15 | Rubber composition for use of food and hygiene |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58157842A JPS58157842A (en) | 1983-09-20 |
| JPS6225175B2 true JPS6225175B2 (en) | 1987-06-02 |
Family
ID=12601985
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4120882A Granted JPS58157842A (en) | 1982-03-15 | 1982-03-15 | Rubber composition for use of food and hygiene |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS58157842A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2528033B2 (en) * | 1990-10-31 | 1996-08-28 | 豊田合成株式会社 | Ethylene propylene rubber compound |
| CN110054836A (en) * | 2019-04-18 | 2019-07-26 | 武汉金发科技有限公司 | A kind of PP composite material and preparation method thereof and fatty acid zinc are in the application for reducing PP composite material VOC |
-
1982
- 1982-03-15 JP JP4120882A patent/JPS58157842A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS58157842A (en) | 1983-09-20 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4480054A (en) | Foamable polymer blend compositions | |
| EP0024550B1 (en) | Expandable composition based on epdm rubber or polychloroprene and closed cell sponge rubber made therefrom | |
| US4983685A (en) | Methods for production of crosslinked rubber products | |
| MXPA02009075A (en) | Rubber vulcanizates having improved ageing properties. | |
| US4172939A (en) | Vulcanizable ethylene/vinyl acetate/carbon monoxide terpolymers | |
| JP2001226489A (en) | Method for crosslinking isoprene/isobutylene rubber or ethylene/propylene/diene rubber containing ethylidenenorbornene as unsaturated component or blend thereof and crosslinked rubber product made by the method | |
| JPS6225175B2 (en) | ||
| US4275181A (en) | Curable blends of chloroprene polymer and ethylene copolymer | |
| JP3501504B2 (en) | Halogenated butyl rubber composition | |
| JPS6038443A (en) | Foamable polymer blend | |
| JP3604498B2 (en) | Heat resistant rubber composition with excellent fluidity | |
| JPH08225691A (en) | Ethylene-α-olefin-non-conjugated diene copolymer rubber composition | |
| JPS59213743A (en) | Vulcanizable rubber composition | |
| JPH06313047A (en) | Improved vulcanized eva rubber | |
| EP0595551B1 (en) | Radiator hose | |
| JP3563156B2 (en) | Synthetic rubber composition | |
| JP2774615B2 (en) | EPDM rubber composition | |
| JPH0827333A (en) | Rubber composition | |
| JPS58101126A (en) | Expandable vinyl chloride resin composition for gasket of refrigerator | |
| JPH066640B2 (en) | Chloroprene rubber composition | |
| JP2583381B2 (en) | Rubber composition | |
| WO1997016484A1 (en) | RUBBER COMPOSITION COMPRISING HIGHLY SATURATED NITRILE COPOLYMER RUBBER AND ETHYLENE-α-OLEFIN COPOLYMER RUBBER | |
| JP3086892B2 (en) | Chlorinated polyethylene composition | |
| JPS6295337A (en) | Vulcanized rubber composition | |
| JP2000006146A (en) | Method for treating powder vulcanized rubber and its rubber composition |