JPS58157842A - Rubber composition for use of food and hygiene - Google Patents

Rubber composition for use of food and hygiene

Info

Publication number
JPS58157842A
JPS58157842A JP4120882A JP4120882A JPS58157842A JP S58157842 A JPS58157842 A JP S58157842A JP 4120882 A JP4120882 A JP 4120882A JP 4120882 A JP4120882 A JP 4120882A JP S58157842 A JPS58157842 A JP S58157842A
Authority
JP
Japan
Prior art keywords
zinc
vulcanization
rubber
fatty acid
ministry
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.)
Granted
Application number
JP4120882A
Other languages
Japanese (ja)
Other versions
JPS6225175B2 (en
Inventor
Yoshio Tanimoto
谷本 嘉雄
Koichi Iketani
池谷 孝一
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sumitomo Chemical Co Ltd
Original Assignee
Sumitomo Chemical Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Sumitomo Chemical Co Ltd filed Critical Sumitomo Chemical Co Ltd
Priority to JP4120882A priority Critical patent/JPS58157842A/en
Publication of JPS58157842A publication Critical patent/JPS58157842A/en
Publication of JPS6225175B2 publication Critical patent/JPS6225175B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Compositions Of Macromolecular Compounds (AREA)

Abstract

PURPOSE:The titled composition capable of producing rubber products coming up to Notification No.434 of the Ministry of Public Welfare by normal continuous extrusion vulcanization process at normal pressure, obtained by blending ethylene.propylene.diene terpolymer rubber with zinc white, a zinc salt of a fatty acid and calcium oxide. CONSTITUTION:100pts.wt. ethylene.propylene.diene terpolymer rubber in blended with 0.1-5pts.wt. zinc white No.1, 0.1-6pts.wt. zinc salt of 7-13C fatty acid and 0.1-5pts.wt. calcium oxide. The composition comes up to the standard of evaporation residue, regulated by Notification No.434 of the Ministry of Public Welfare. The initial activity of valcanization reaction is maintained by the zinc salt of the fatty acid, and durability is kept by zinc white. In continuous extrusion vulcanization process at normal pressure, especially in case that productivity is a matter of great account, 1-3pts.wt. zinc octylate, 1-2pts.wt. zinc white and 1-2.5pts.wt. calcium oxide are preferably added to the rubber.

Description

【発明の詳細な説明】 本発明はエチレン・プロピレン・ジエン三光共重合ゴム
(以下EPQMという)を基材に用いて、厚生省484
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(以下コンパラ
・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、圧力な器パツキン、
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。
Detailed Description of the Invention The present invention uses ethylene-propylene-diene three-light copolymer rubber (hereinafter referred to as EPQM) as a base material,
This invention relates to obtaining a rubber composition (hereinafter referred to as "comparado") that can be used to produce various rubber products for food use that meet the requirements of the No. EPDM has excellent weather resistance, heat resistance, water resistance, and chemical resistance, so it can be used in food-use rubber products that require these properties, such as rubber for coffee siphons, pressure vessel packing,
It is applied to mochi pounders, hoses for solar water heaters, etc.

この様な゛製品を生産する方法としては、プレス加硫、
インジェクシ1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(HAY )、高周波加硫
(UHF)、流動床加硫(PCM)に比べて著しく劣っ
ている問題をかかえている。
Methods for producing such products include press vulcanization,
Generally, injector vulcanization and extrusion can vulcanization are used. 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. Continuous vulcanization, ie, salt bath vulcanization (LCM), hot air vulcanization (HAY), high frequency vulcanization (UHF), and fluidized bed vulcanization (PCM), suffer from the problem of being significantly inferior.

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)によって厚生省告示4
84号を合格するゴム製品を得るコンパウンドを見出し
た。
As a result of intensive research, the present inventor has developed a continuous vulcanization method (hereinafter referred to as the "CV method") in order to compensate for these shortcomings and comply with Ministry of Health, Labor and Welfare Notification 4.
We have discovered a compound that produces rubber products that pass No. 84.

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C1O)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Cλ(oi−t)、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。
The main difference between the compounds used in the CV method and the can vulcanization method is that quicklime (hereinafter referred to as C1O) is essential as an antifoaming agent in the CV method, but it is not necessary in the can vulcanization method. The can vulcanization method is characterized by using external pressure to suppress the evaporation of moisture in the compound during the vulcanization process, thereby preventing foaming of the rubber product, whereas the CV method uses CaO. A common method is to convert moisture in the compound into stable Cλ(oi-t) and prevent foaming.

厚生省告示484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484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Ch(0f()*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484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。
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. 484 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. 484. 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. It can be predicted that rubber products obtained from compounds containing Ch(0f()*CaO produced by blending CaO) will considerably exceed the regulatory value of evaporation residue (hereinafter referred to as evaporation residue) of the Ministry of Health and Welfare Notification No. 484. .

また亜鉛華(ZnU)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。
Furthermore, zinc white (ZnU) 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% aqueous acetic acid solution.

缶加硫方式に用いられるコンパラン・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、カー示ンブラック、タルク、クレー
等であるが、特番ζ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
8〜6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。
Comparand used in the can vulcanization method does not require the addition of CaO as mentioned above, and additives that increase the amount of evaporation residue include zinc white, carbon black, talc, clay, etc. ZnO has a significant influence on ζ. The amount of ZnO used in ordinary rubber products is about 8 to 6 parts by weight (hereinafter referred to as PHR), but past research has demonstrated that it is possible to pass the evaporation residue test with this amount. ing.

本発明者ら出願特開昭54−78745号を参照。See Japanese Patent Application No. 54-78745.

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C20)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。
However, it goes without saying that when using a compound that requires the combination of multiple types of compounding agents (ZnO and C20) that produce a particularly large amount of evaporation residue, such as the CV method, it becomes difficult to pass the evaporation residue test. Nor.

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船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
ることが可能になった結果、CaOを配合しても厚生省
告示484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。
As a result of various studies on ways to eliminate the drawbacks of the compound used in the CV method as described above, the inventor of the present invention found that by using ZnO and a fatty acid salt having a relatively small number of carbon atoms together, the blending amount of ZnO can be reduced. As a result, even if CaO is added, the evaporation residue can be kept below the regulation value of Ministry of Health and Welfare Notification No. 484, and CV
We have discovered a compound that can prevent foaming of products using this method.

一般に厚生省告示484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。
In general, in order to obtain a compound for the CV method that passes the Ministry of Health and Welfare Notification No. 484, it is necessary at least to mix limited reinforcing agents, fillers, and limited vulcanization accelerators with EPDM, as well as appropriate amounts of ZnO, CaO, etc. be.

ここで眼られた補強剤、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54−78746に準拠
するものである。
The reinforcing agent, filler, and vulcanization system mentioned here are based on Japanese Patent Application Laid-Open No. 54-78746, for which the present inventor previously applied for a patent.

すなわち、補強剤とはカーボンブラック()1−ネスブ
ラック)、充てん剤とはクレー、タルク類であるか、カ
ーボンブラック単独の配合系が最も好ましい。
That is, it is most preferable that the reinforcing agent is carbon black (1-nes black) and the filler is clay or talc, or that the filler is a blend of carbon black alone.

本発明はCV方式によりゴム製品を得るのに必要なZn
O1CaOの配合量を可渉な限り少くなくするという発
想に基づくものであるカイ、鋭意検討した結果、不都合
な点が生ずることが分った。
The present invention uses Zn necessary to obtain rubber products by the CV method.
Although this method is based on the idea of reducing the amount of O1CaO mixed as much as possible, as a result of intensive study, it was found that there are some disadvantages.

すなわち、ZnOの配合量を減少するに従(1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。
In other words, as the amount of ZnO is reduced (1), the evaporation residue decreases, leading to good results, but there is a tendency for the degree of vulcanization to decrease significantly, and rubber physical properties such as compression set, tensile strength, and permanent elongation deteriorate. do.

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−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l、N
In addition, as the vulcanization rate becomes slower, the foaming phenomenon in rubber products obtained by the CV method becomes more pronounced, so in order to prevent foaming, it is necessary to increase the amount of CaO blended, thereby reducing the amount of evaporation residue. L, N who cannot fulfill the purpose
.

第1図および第2図にこれらの関係を示した。These relationships are shown in FIGS. 1 and 2.

I41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。
Diagram I41 shows the relationship between the amount of Zinc White No. 1 blended and the compression set and evaporation residue amount of the vulcanizate in the vulcanized rubber composition having the basic formulation shown in Table 1.

第2図は、m1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。
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 m1.

なお、加硫条件は、いずれも160℃X80分、プレス
加硫で行なった。
The vulcanization conditions were press vulcanization at 160° C. for 80 minutes.

第  1  表 基  本  配  合 ※1 共同薬品製R−800 4!2  ジンク−ジメチル−ジチオカーバメート※8
 ジンク−ジエチル−ジチオカーバメート※4 ジンク
−ジ−n−ブチル−ジチオカーバメート※6 ジペンタ
メチレンチウラムへキササルファイド壷6 弁上石灰製
 ペスターPP ※7 堺化学製兼鉛華特1号 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。
Table 1 Basic formulation *1 Kyodo Yakuhin R-800 4!2 Zinc-dimethyl-dithiocarbamate *8
Zinc-diethyl-dithiocarbamate *4 Zinc-di-n-butyl-dithiocarbamate *6 Dipentamethylene lentithurum hexasulfide pot 6 Pester PP made by Bengami Lime *7 Kanamekatoku No. 1 manufactured by Sakai Chemicals Here, the present invention As a result of trying to apply various zinc fatty acids and organic zinc compounds as vulcanization activators to replace ZnO, they found that zinc salts of fatty acids with 7 to 13 carbon atoms, such as zinc octylate, have a remarkable vulcanization activating effect. I discovered that.

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
遅く圧縮永久侑が大きい、史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。
Other organic acid zinc salts are also effective in reducing evaporation residue, but fatty acid zinc with 14 or more carbon atoms, such as zinc stearate, has a small vulcanization activation effect, that is, the vulcanization rate is slow and the compression resistance is low. Historically, fatty acids and other compounding agents precipitate on the surface of rubber products, which causes bleed, making it difficult to obtain desirable products.

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、アー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、著しい感興が有へυ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。
Furthermore, zinc acetate, zinc acetylacetone,
Zinc naphthenate and the like are each insoluble in the compound, and they all have problems such as being extremely irritating and having little υ sulfuric acid activation effect, making them impossible to apply from a practical point of view.

一方、ZnOの代りに炭素数7以上18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、Z
nO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、Zn01ζ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。
On the other hand, a compound containing a fatty acid zinc salt having 7 to 18 carbon atoms instead of ZnO not only compensates for the drawbacks of compounds containing other similar compounds, but also improves ZnO.
Since the initial vulcanization activation effect is more pronounced than in compounds containing nO alone, it is a favorable factor in terms of product shape retention, line speedup, etc. when produced by the Cv method. However, on the other hand, it has the disadvantage of lacking in sustainability of vulcanization activity compared to Zn01ζ.

しかし、本発明者は炭素数7以上18以下の脂肪酸亜鉛
塩とZnOを併用することにより、どの欠点を改めるこ
とに成功した。
However, the present inventors succeeded in correcting these drawbacks by using ZnO in combination with a fatty acid zinc salt having 7 to 18 carbon atoms.

すなわち、炭素数7以上18以下の1旨肪酸亜鉛塩で加
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。
That is, it is based on the idea that the initial activity of the vulcanization reaction is provided by a monofatty acid zinc salt having 7 or more and 18 or less carbon atoms, and the durability is provided by ZnO.

特に炭素数7以上18以下の脂肪酸亜鉛塩を配合した効
果はきわたっており、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Cooの
配合着を少量゛にしえる。
In particular, the effect of blending a fatty acid zinc salt with a carbon number of 7 or more and 18 or less is significant, 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 amount of Coo blended. .

この結果厚生省告示484号の蒸発残を規格値以下に保
つことが非常に有利になったばかりか、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。
As a result, it has been found that not only is it extremely advantageous to maintain the evaporation residue below the standard value according to Ministry of Health and Welfare Notification No. 484, but it is also effective in improving compression set, which is significantly worsened by adding CaO.

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484号等を
バランスさせるには、炭素数7以上18以下の脂肪酸亜
鉛塩ZnO。
As a result of further pursuing this point, the present inventor found that in order to balance the appearance, physical properties, Ministry of Health and Welfare No. 484, etc. of rubber products applied to food applications, fatty acid zinc salt ZnO having 7 or more and 18 or less carbon atoms.

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。
It has been found that it is necessary to mix appropriate amounts of CaO.

すなわち、炭素数7以上18以下の脂肪酸亜鉛塩は0.
1〜(5PHR%ZnOは0.1〜8PHR。
That is, the fatty acid zinc salt having 7 or more and 18 or less carbon atoms has 0.
1~(5PHR%ZnO is 0.1~8PHR.

CaOは0,6〜3PHR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l 〜9PHR,Zn
Oは1〜2PHR。
It is desirable to use CaO in combination within the range of 0.6 to 3 PHR, but in the Cv method, if productivity is particularly important, zinc octylate should be used in the range of 1 to 9 PHR, Zn.
O is 1-2 PHR.

C@0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18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、Z n O,炭素数7以上1
8以下の脂肪酸亜鉛塩を併用したケース程改良効果は無
かった。
It is preferable to blend 1 to 2.5 PHR of C@0. In a formulation example in which ZnO is not blended and the amount of fatty acid zinc salt having 7 to 18 carbon atoms is simply increased, the sustainability of vulcanization activity is slightly improved;
The improvement effect was not as great as in the case where a fatty acid zinc salt of 8 or less was used in combination.

本発明のEPDMとはエチレン・プロピレン・ジシクロ
ペンタジェン三元共重合ゴム、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
番プロピレン・1.4−へ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。
The EPDM of the present invention is ethylene/propylene/dicyclopentadiene terpolymer rubber, ethylene/propylene/
These include 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.

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 2 of Examples shows the formulation, vulcanization conditions, and physical properties of the obtained vulcanized rubber.

s2表の脚注 [1g1)住友化学工業■製F、PDM(*2)東海カ
ーボン製FEFタイプカーボンブラックC*8)出光興
産製パラフィン系プロセスオイル(本4)共同薬品製加
工助剤 (本5)ジンク−ジメチル−ジチオカルバメート(に6
)ジンク−ジエチル−ジチオカルバメート(*7)ジン
ク−n−ブチル−ジチオカルバメート(*8)ジペンタ
メチレンチオウレアへキササルファイド(*9)厚生省
告示484号の蒸発残留物の基準は80ppm以下であ
る。加硫条件160℃×16分加硫である。
Footnotes to s2 table [1g1] F, PDM manufactured by Sumitomo Chemical Co., Ltd. (*2) FEF type carbon black C manufactured by Tokai Carbon *8) Paraffin-based process oil manufactured by Idemitsu Kosan (Book 4) Processing aid manufactured by Kyodo Yakuhin (Book 5) ) zinc-dimethyl-dithiocarbamate (ni6
) Zinc-diethyl-dithiocarbamate (*7) Zinc-n-butyl-dithiocarbamate (*8) Dipentamethylenethiourea hexasulfide (*9) The standard for evaporation residue according to Ministry of Health and Welfare Notification No. 484 is 80 ppm or less. The vulcanization conditions were 160°C x 16 minutes.

(4clO)加硫条件は200℃×6分の熱空気連続加
硫である。
(4clO) The vulcanization conditions were continuous hot air vulcanization at 200°C for 6 minutes.

【図面の簡単な説明】[Brief explanation of the drawing]

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$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Ca
Oの配合量と、加硫物の蒸発残留物の量の関係図である
。 第1図 2845 亜鉛華1号配合量(PHR) 第2図 12845 亜鉛華1号配合量(PHR)
Figure 1 is a diagram showing the relationship between the amount of zinc white No. 1 blended in an EPDM vulcanized rubber composition and the compression set $ and amount of evaporation residue of the vulcanizate. Ca
FIG. 3 is a diagram showing the relationship between the amount of O added and the amount of evaporation residue of the vulcanizate. Fig. 1 2845 Zinc white No. 1 blending amount (PHR) Fig. 2 12845 Zinc white No. 1 blending amount (PHR)

Claims (1)

【特許請求の範囲】[Claims] エチレン・プロピレン−ジエン三元共重合ゴム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18以下の脂肪酸亜船塩を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484号の蒸発残留物の基準に合格する
ゴム組成物。
Zinc white No. 1 0.1 to 5 parts by weight, carbon number 7 per 100 parts by weight of ethylene-propylene-diene ternary copolymer rubber
A rubber composition that passes the evaporation residue standards of the Ministry of Health and Welfare Notification No. 484, which is characterized by blending 0.1 to 6 parts by weight of fatty acid submersal salts of 18 or less and 0.1 to 5 parts by weight of calcium oxide. thing.
JP4120882A 1982-03-15 1982-03-15 Rubber composition for use of food and hygiene Granted JPS58157842A (en)

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 true JPS58157842A (en) 1983-09-20
JPS6225175B2 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)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04168135A (en) * 1990-10-31 1992-06-16 Toyoda Gosei Co Ltd Ethylene-propylene rubber composition
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

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04168135A (en) * 1990-10-31 1992-06-16 Toyoda Gosei Co Ltd Ethylene-propylene rubber composition
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

Also Published As

Publication number Publication date
JPS6225175B2 (en) 1987-06-02

Similar Documents

Publication Publication Date Title
US3882197A (en) Alpha-olefin copolymer blends
US4983685A (en) Methods for production of crosslinked rubber products
DE60111147T2 (en) High and low molecular weight EPDM rubber
JP5346285B2 (en) Polyolefin thermoplastic vulcanized elastomer
CA2372540A1 (en) Process for improving flowability of olefins during gas-phase (co-)polymerisation in a fluidised bed reactor incorporating process aid additives
CN102822262A (en) Nbr composition and rubber material for sealing
CN110423408A (en) Short vulcanization ethylene propylene diene rubber and preparation method thereof
US4268637A (en) Elimination of bloom in [vul-cup] peroxide crosslinked elastomer compounds
JPH068367B2 (en) Elastomer composition
DE2310018C3 (en) Process for the production of quadripolymers and their use for the production of vulcanizates
MXPA02009075A (en) Rubber vulcanizates having improved ageing properties.
JPS58157842A (en) Rubber composition for use of food and hygiene
US3554960A (en) Clay-loaded elastomers
US4010129A (en) Novel processing aids for natural and synthetic rubber compounds
JP3191592B2 (en) Ethylene-α-olefin-non-conjugated diene copolymer rubber composition
JPH1121395A (en) Rubber composition, vulcanized rubber composition, radiator hose, heater hose or radiator packing
JP3604498B2 (en) Heat resistant rubber composition with excellent fluidity
JPS6038443A (en) Foamable polymer blend
EP1683835B1 (en) Epdm composition
CA1257436A (en) Cured rubber blend and process for the production thereof
JPS59213743A (en) Vulcanizable rubber composition
JPS5933140B2 (en) Elastomer composition
EP0595551B1 (en) Radiator hose
JP3563156B2 (en) Synthetic rubber composition
JPS5915345B2 (en) High hardness rubber composition