JP2753676B2 - Conductive rubber foam and method for producing the same - Google Patents

Conductive rubber foam and method for producing the same

Info

Publication number
JP2753676B2
JP2753676B2 JP22518493A JP22518493A JP2753676B2 JP 2753676 B2 JP2753676 B2 JP 2753676B2 JP 22518493 A JP22518493 A JP 22518493A JP 22518493 A JP22518493 A JP 22518493A JP 2753676 B2 JP2753676 B2 JP 2753676B2
Authority
JP
Japan
Prior art keywords
weight
parts
vulcanization
foaming
hardness
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
Application number
JP22518493A
Other languages
Japanese (ja)
Other versions
JPH0753758A (en
Inventor
利和 松岡
保 長谷川
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.)
KUREHA ERASUTOMAA KK
Original Assignee
KUREHA ERASUTOMAA KK
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 KUREHA ERASUTOMAA KK filed Critical KUREHA ERASUTOMAA KK
Priority to JP22518493A priority Critical patent/JP2753676B2/en
Publication of JPH0753758A publication Critical patent/JPH0753758A/en
Application granted granted Critical
Publication of JP2753676B2 publication Critical patent/JP2753676B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
  • Conductive Materials (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】この発明は、EPDMを主成分と
し、連続気泡を有し、低硬度で、かつ導電性に優れた導
電性ゴム発泡体およびその製造法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a conductive rubber foam having EPDM as a main component, having open cells, low hardness, and excellent conductivity, and a method for producing the same.

【0002】[0002]

【従来の技術】EPDMは、耐熱性、耐薬品性、耐候性
および電気的性質に優れているため、各種の分野で広く
利用されているが、近年、低硬度のゴム組成物に対する
要望が高まり、各種の方法で低硬度のゴム組成物が製造
されている。そして、硬度を低くするに当り、可塑剤の
使用量を節約するため、従来は、分解性発泡剤を含むコ
ンパウンドを金型の凹部一杯に充填し、これを上記分解
性発泡剤の分解温度以上の温度の加圧下で加熱して発泡
反応および加硫反応を終了させ、しかるのち圧力を解放
して発泡させる、いわゆる加圧発泡を行うのが一般的で
あった。そして、導電性を与える場合は、上記のコンパ
ウンドに導電剤を添加していた。
2. Description of the Related Art EPDM is widely used in various fields because of its excellent heat resistance, chemical resistance, weather resistance and electrical properties. In recent years, however, there has been an increasing demand for rubber compositions having low hardness. Low hardness rubber compositions have been produced by various methods. In order to reduce the amount of the plasticizer used in reducing the hardness, conventionally, a compound containing a decomposable foaming agent is filled in the mold to fill the entire concave portion, and this is filled at a temperature higher than the decomposition temperature of the decomposable foaming agent. In general, the foaming reaction and the vulcanization reaction are completed by heating under pressure at the temperature described above, and then the pressure is released to cause foaming, that is, so-called pressure foaming. And when giving conductivity, the conductive agent was added to the said compound.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、上記の
加圧発泡法で製造されたEPDM発泡体は、その気泡形
態が独立気泡であるため、硬度が高くなり、かつ圧縮後
の形状回復性が悪いという問題があった。そして、導電
性を付与するためにカーボンブラックの添加量を増大す
ると、コンパウンドの粘度が高くなって発泡が抑制さ
れ、この発泡を容易にするために可塑剤を増量すると、
得られた発泡体が粘着性をおび、さらにブリードアウト
が発生するという問題があった。
However, the EPDM foam produced by the above-mentioned pressure foaming method has a high hardness and a poor shape recovery after compression since the foam is a closed cell. There was a problem. And when increasing the addition amount of carbon black to impart conductivity, the viscosity of the compound increases, foaming is suppressed, and when the plasticizer is increased to facilitate this foaming,
There is a problem that the obtained foam has tackiness and bleed out occurs.

【0004】この発明は、EPDM発泡体の気泡を連続
気泡にすると、硬度が低下し、形状回復性が向上し、ま
たカーボンブラックに炭酸カルシウムを併用すると、カ
ーボンブラックを増量しなくても導電性が向上するとい
う知見に基づいてなされたものであり、気泡が連続気泡
であり、硬度が低く、導電性が高く、かつ形状回復性に
優れ、ブリードアウトの生じない導電性ゴム発泡体およ
びその製造法を提供するものである。
According to the present invention, when the cells of the EPDM foam are made into open cells, the hardness is reduced and the shape recoverability is improved, and when calcium carbonate is used in combination with carbon black, the conductivity is improved without increasing the amount of carbon black. The conductive rubber foam, which is an open cell, has low hardness, high conductivity, and is excellent in shape recovery, does not cause bleed-out, and its production. It provides the law.

【0005】[0005]

【課題を解決するための手段】すなわち、第1発明に係
る導電性ゴム発泡体は、EPDM100重量部に対しカ
ーボンブラックが10〜40重量部、並びに炭酸カルシ
ウム、シリカおよびシリケートのいずれか1種もしくは
2種以上が合計20〜80重量部配合されており、かつ
気泡形態が連続気泡であり、硬度(アスカーF硬度)が
80度以下、抵抗率が1×106 Ωcm以下であることを
特徴とする。
That is, the conductive rubber foam according to the first invention comprises 10 to 40 parts by weight of carbon black per 100 parts by weight of EPDM, and one or more of calcium carbonate, silica and silicate. A total of 20 to 80 parts by weight of two or more types are blended, and the cell form is open cells, the hardness (Asker F hardness) is 80 degrees or less, and the resistivity is 1 × 10 6 Ωcm or less. I do.

【0006】また、第2発明に係る導電性ゴム発泡体の
製造法は、EPDM100重量部に対しカーボンブラッ
クを10〜40重量部、炭酸カルシウム、シリカおよび
シリケートのいずれか1種もしくは2種以上を合計20
〜80重量部、分解性発泡剤、加硫剤、加硫促進剤、可
塑剤およびその他必要な配合剤をそれぞれ適量配合して
混練りし、得られたコンパウンドを金型に充填し、上記
分解性発泡剤の分解温度よりも低い温度の加圧下で一次
加硫を行い、次いで上記分解性発泡剤の分解温度よりも
高い温度の常圧下で二次加硫を行うと同時に発泡させて
連続気泡と独立気泡が混在する発泡ゴムとし、次いでこ
の発泡ゴムを圧縮して上記の独立気泡を破壊することを
特徴とする。
The method for producing a conductive rubber foam according to the second invention is characterized in that 10 to 40 parts by weight of carbon black and at least one of calcium carbonate, silica and silicate are added to 100 parts by weight of EPDM. Total 20
~ 80 parts by weight, decomposable foaming agent, vulcanizing agent, vulcanization accelerator, plasticizer and other necessary compounding agents are mixed in appropriate amounts and kneaded, and the obtained compound is filled in a mold, and Primary vulcanization is performed under pressure at a temperature lower than the decomposition temperature of the decomposable foaming agent, and then secondary vulcanization is performed at normal pressure at a temperature higher than the decomposition temperature of the decomposable foaming agent, and simultaneously foamed to open cells. And closed cells are mixed, and then the foamed rubber is compressed to destroy the closed cells.

【0007】この発明で使用するEPDMは、制限がな
く、一般的に使用されているものであれば全て使用可能
である。また、カーボンブラックは、導電効果を有する
ものであれば、いずれも使用可能であるが、吸油量の余
り多くないものが好ましい。この発明では、上記のカー
ボンブラックに炭酸カルシウム、シリカ、シリケートの
いずれか1種または2種以上が併用されるが、この炭酸
カルシウムとしては重質および軽質の炭酸カルシウム
が、シリカとしては湿式シリカおよび乾式シリカが、ま
たシリケートとしてはアルミニウムシリケートおよびカ
ルシウムシリケート等が使用可能である。
The EPDM used in the present invention is not limited, and any commonly used EPDM can be used. Any carbon black can be used as long as it has a conductive effect, but it is preferable that the carbon black does not have too much oil absorption. In the present invention, any one or more of calcium carbonate, silica and silicate are used in combination with the above carbon black. Heavy and light calcium carbonate is used as the calcium carbonate, and wet silica and silica are used as the silica. Dry silica can be used, and silicates such as aluminum silicate and calcium silicate can be used.

【0008】また、分解性発泡剤は、従来から使用され
ているものであり、アゾジカルボンアミド、ジニトロソ
ペンタメチレンテトラアミン、オキシビスベンゾチアゾ
ール等が例示される。また、加硫剤、加硫促進剤および
可塑剤は、従来使用しているものをそのまま使用するこ
とができる。
[0008] The decomposable blowing agent has been conventionally used, and examples thereof include azodicarbonamide, dinitrosopentamethylenetetraamine, and oxybisbenzothiazole. As the vulcanizing agent, vulcanization accelerator and plasticizer, those conventionally used can be used as they are.

【0009】第2発明では、一次加硫の際、コンパウン
ドを金型の凹部一杯に充填し、温度を上記分解性発泡剤
の分解温度よりも低く設定することにより、加硫速度を
調節し、加圧下で急激な発泡を抑制して加硫速度と発泡
剤の分解速度をバランスさせるものであり、その温度は
上記発泡剤の分解温度よりも低い温度であり、特に90
〜150℃が好ましい。また、その際の加硫時間は5〜
30分が好ましい。一方、二次加硫は、加硫および発泡
を完結させるためのものであり、上記の一次加硫で得ら
れた半加硫品を常圧下に置き、上記分解性発泡剤の分解
温度よりも高い温度で加熱し、常圧下で発泡させる。こ
の二次加硫温度は、上記分解温度よりも高い温度であ
り、特に130〜180℃が好ましい。また、その反応
時間は5〜60分が好ましい。なお、上記の分解温度
は、EPDMに他の配合剤と共に配合した状態での実際
の分解温度であり、発泡助剤の添加により分解温度が低
下しているときは、この低下した分解温度をいう。
In the second invention, at the time of the primary vulcanization, the compound is filled into the entire concave portion of the mold, and the temperature is set lower than the decomposition temperature of the decomposable foaming agent, thereby controlling the vulcanization rate, It suppresses rapid foaming under pressure and balances the vulcanization rate and the decomposition rate of the foaming agent. The temperature is lower than the decomposition temperature of the foaming agent, particularly 90
~ 150 ° C is preferred. The vulcanization time at that time is 5
30 minutes is preferred. On the other hand, the secondary vulcanization is for completing vulcanization and foaming, and the semi-vulcanized product obtained by the above primary vulcanization is placed under normal pressure, and the temperature is lower than the decomposition temperature of the decomposable foaming agent. Heat at high temperature and foam under normal pressure. This secondary vulcanization temperature is higher than the above decomposition temperature, and particularly preferably 130 to 180 ° C. The reaction time is preferably 5 to 60 minutes. The above-mentioned decomposition temperature is an actual decomposition temperature in a state where EPDM is blended with other compounding agents. When the decomposition temperature is lowered by adding a foaming aid, the decomposition temperature refers to the lowered decomposition temperature. .

【0010】この発明では、上記の二次加硫によって得
られた独立気泡および連続気泡の混在する半連泡の発泡
ゴムを圧縮し、これによって上記の独立気泡を破壊して
連続気泡に変形するが、上記の圧縮手段としては、一定
の間隙で対向して回転する一対のローラ間に上記の発泡
ゴムを通す方法が好ましい。
[0010] In the present invention, the semi-open-cell foamed rubber in which closed cells and open cells obtained by the secondary vulcanization are mixed is compressed, whereby the closed cells are broken and deformed into open cells. However, as the above-mentioned compression means, a method of passing the above-mentioned foamed rubber between a pair of rollers rotating opposite to each other with a certain gap is preferable.

【0011】[0011]

【作用】第1発明の導電性ゴム発泡体は、EPDMの発
泡体であるため、従来と同様に耐熱性、耐薬品性および
耐候性等に優れている。そして、カーボンブラックに炭
酸カルシウム、シリカおよびシリケートのいずれか1種
もしくは2種以上が併用されているため、カーボンブラ
ックの配合量が比較的少ないにもかかわらず、抵抗率が
1×106 Ωcm以下であって導電性に優れている。ま
た、カーボンブラックの配合量が比較的少ないため、加
硫前の粘度が低くなって発泡が容易になり、気泡が均一
に形成される。しかも、気泡形態が連続気泡であるた
め、可塑剤の配合量を少なくしても、硬度(アスカーF
硬度)が80度以下に低下すると共に、形状回復性が良
好になる。
Since the conductive rubber foam of the first invention is an EPDM foam, it has excellent heat resistance, chemical resistance, weather resistance, etc. as in the prior art. Further, since one or more of calcium carbonate, silica and silicate are used in combination with carbon black, the resistivity is 1 × 10 6 Ωcm or less despite the relatively small amount of carbon black. And has excellent conductivity. Further, since the compounding amount of carbon black is relatively small, the viscosity before vulcanization becomes low, foaming becomes easy, and bubbles are formed uniformly. In addition, since the cell form is open cells, even if the amount of the plasticizer is reduced, the hardness (ASKER F
Hardness) is reduced to 80 degrees or less, and the shape recoverability is improved.

【0012】ただし、上記カーボンブラックの配合量が
EPDM100重量部に対し10重量部未満の場合は、
抵抗率が過大になり、反対に40重量部を超えると、硬
度が過大になる。また、炭酸カルシウム、シリカおよび
シリケートの配合量が20重量部未満の場合は、電気抵
抗の低下が不十分になり、本発明の目的である導電効果
が得られず、反対に80重量部を超えた場合は、硬度が
増大し、発泡度が低下する。
However, when the compounding amount of the carbon black is less than 10 parts by weight based on 100 parts by weight of EPDM,
If the resistivity is too high, and if it exceeds 40 parts by weight, the hardness will be too high. On the other hand, when the amount of calcium carbonate, silica and silicate is less than 20 parts by weight, the electric resistance is insufficiently reduced, and the conductive effect, which is the object of the present invention, cannot be obtained. If so, the hardness increases and the degree of foaming decreases.

【0013】第2発明によれば、EPDMを主体とし分
解性発泡剤を含むコンパウンドを金型に充填し、分解性
発泡剤の分解温度よりも低い温度で一次加硫を行うの
で、この一次加硫では、発泡が抑制されて加硫のみが進
行し、この加硫が半ば進行した状態で上記の分解温度よ
りも高い温度で二次加硫を行うので、連続気泡と独立気
泡が混在する発泡ゴムが得られ、この発泡ゴムを圧縮し
て上記の独立気泡を破壊することにより、連続気泡から
なるEPDM発泡体が得られる。そして、上記のコンパ
ウンドには、カーボンブラックに炭酸カルシウム、シリ
カおよびシリケート等が併用されるため、第1発明の導
電性ゴム発泡体が得られる。
According to the second invention, the mold is filled with a compound mainly composed of EPDM and containing a decomposable foaming agent, and the primary vulcanization is performed at a temperature lower than the decomposition temperature of the decomposable foaming agent. In the vulcanization, foaming is suppressed and only vulcanization proceeds, and secondary vulcanization is performed at a temperature higher than the decomposition temperature in the state where this vulcanization has progressed halfway, so foaming in which open cells and closed cells are mixed A rubber is obtained, and the foamed rubber is compressed to break the closed cells, thereby obtaining an EPDM foam composed of open cells. In the above compound, calcium carbonate, silica, silicate and the like are used in combination with carbon black, so that the conductive rubber foam of the first invention is obtained.

【0014】ただし、一次加硫の際の温度が低過ぎた
り、時間が短か過ぎたりした場合は、加硫が不足して一
次加硫の目的が達成されず、反対に上記一次加硫の温度
が高過ぎたり、時間が長過ぎたりした場合は、加硫が進
み過ぎて二次加硫の際の発泡が困難になる。また、二次
加硫の際の温度が低過ぎたり、時間が短か過ぎたりした
場合は、発泡および加硫の反応が終了していないため、
発泡が起きず、反対に上記二次加硫の温度が高過ぎた場
合は、加硫および発泡の反応が急激に起き、発泡のバラ
ンスと加硫のバランスが崩れて発泡異常が生じる。
However, if the temperature at the time of the primary vulcanization is too low or the time is too short, the purpose of the primary vulcanization cannot be achieved due to insufficient vulcanization. If the temperature is too high or the time is too long, vulcanization proceeds too much and foaming during secondary vulcanization becomes difficult. Also, if the temperature during the secondary vulcanization is too low or the time is too short, the reaction of foaming and vulcanization is not completed,
If foaming does not occur and the temperature of the secondary vulcanization is too high, the reaction of vulcanization and foaming occurs rapidly, and the balance between foaming and vulcanization is lost, resulting in abnormal foaming.

【0015】[0015]

【実施例】EPDM100重量部に対してカーボンブラ
ックその他種々の添加剤を下記の表1に示す配合比(重
量部)で配合し、バンバリーミキサー、ニーダー、ロー
ル等で混練りし、実施例1および比較例1〜4のコンパ
ウンドを得た。ただし、カーボンブラックには導電性カ
ーボンブラックを使用した。また、発泡剤には分解温度
220℃のADCA(アゾジカルボンアミド)系発泡剤
を尿素系発泡助剤と共に使用し、分解温度を約155℃
に低下させた。
EXAMPLE 100 parts by weight of EPDM were mixed with carbon black and other various additives in the mixing ratio (parts by weight) shown in Table 1 below, and kneaded with a Banbury mixer, a kneader, a roll, and the like. Compounds of Comparative Examples 1 to 4 were obtained. However, conductive carbon black was used as carbon black. An ADCA (azodicarbonamide) foaming agent having a decomposition temperature of 220 ° C. is used together with a urea foaming auxiliary as a foaming agent.
Lowered.

【0016】 表 1 実施例1 比較例1 比較例2 比較例3 比較例4 EPDM 100 100 100 100 100 カーボンブラック 20 20 20 50 50 炭酸カルシウム 40 100 5 − − ステアリン酸 3 3 3 3 3 亜鉛華 5 5 5 5 5 可塑剤 50 50 50 50 100 分解性発泡剤 15 15 15 15 15 発泡助剤 2 2 2 2 2 加硫促進剤 3 3 3 3 3 硫黄 2 2 2 2 2Table 1 Example 1 Comparative Example 1 Comparative Example 2 Comparative Example 3 Comparative Example 4 EPDM 100 100 100 100 100 Carbon black 20 20 20 50 50 Calcium carbonate 40 100 5 − − Stearic acid 3 3 3 3 3 Zinc white 5 5 5 5 5 Plasticizer 50 50 50 50 100 Degradable foaming agent 15 15 15 15 15 Foaming aid 2 2 2 2 2 Vulcanization accelerator 3 3 3 3 3 Sulfur 2 2 2 2 2

【0017】得られたコンパウンドを一次加硫用金型の
凹部(幅250mm、長さ250mm、深さ5mm)にその容
積の105%充填し、110℃で15分間の一次加硫を
行い、得られた半加硫品を二次加硫用金型の凹部(幅5
00mm、長さ500mm、深さ14mm)に入れ、常圧下、
160℃で15分間の二次加硫を行い、加硫および発泡
を完結させた。得られたゴム発泡体を2本の平行なロー
ラ間(間隙1mm)に通して独立気泡を破壊し、ほぼ全部
の気泡を連続気泡に形成した。こうして得られた導電性
ゴム発泡体の性能を下記の表2に示す。
The obtained compound is filled in a concave portion (width 250 mm, length 250 mm, depth 5 mm) of a primary vulcanization mold at 105% of its volume and subjected to primary vulcanization at 110 ° C. for 15 minutes. The semi-vulcanized product is placed in the concave portion (width 5
00mm, length 500mm, depth 14mm) under normal pressure,
Secondary vulcanization was performed at 160 ° C. for 15 minutes to complete vulcanization and foaming. The obtained rubber foam was passed between two parallel rollers (gap of 1 mm) to break closed cells, and almost all the cells were formed into open cells. The performance of the conductive rubber foam thus obtained is shown in Table 2 below.

【0018】 表 2 実施例1 比較例1 比較例2 比較例3 比較例4 電気抵抗率(Ωcm) 5×103 6×103 5×106 1×103 1×104 硬度(度) 50 85 52 90 80 ブリード 無 無 無 無 有 発泡度 優 可 良 不可 可 気泡形態 連続 連続 連続 独立 独立 形状回復性 ○ ○ △ × ×Table 2 Example 1 Comparative Example 1 Comparative Example 2 Comparative Example 3 Comparative Example 4 Electric resistivity (Ωcm) 5 × 10 3 6 × 10 3 5 × 10 6 1 × 10 3 1 × 10 4 Hardness (degree) 50 85 52 90 80 Bleed No No No No Yes Bubble degree Excellent Good Good Not good Possible Bubble form Continuous Continuous Continuous Independent Independent Shape recovery ○ ○ △ × ×

【0019】上記の表2において、硬度はアスカーF硬
度計による測定値である。ブリードの有無は、70℃の
ギアーオーブンに入れて360時間放置した後、肉眼で
確認した。また、発泡度は、体積比で8倍以上を優、6
倍以上を良、3倍以上を可とし、ほとんど発泡していな
いものを不可とした。また、気泡形態は、吸水率がほぼ
100%のものを連続気泡、20%以下を独立気泡と判
定した。また、形状回復性は、50%圧縮にて70℃の
ギアーオーブンに入れ、22時間放置した後、開放して
30分後の回復性により判定し、回復率80%以上を
〇、50%以上を△、50%未満を×とした。
In Table 2 above, the hardness is a value measured by an Asker F hardness meter. The presence or absence of bleed was visually confirmed after being left in a gear oven at 70 ° C. for 360 hours. Also, the foaming degree is more than 8 times by volume ratio,
A value of at least 2 times was acceptable, and a value of at least 3 times was acceptable. Regarding the bubble form, those having a water absorption of almost 100% were determined to be open cells, and those having a water absorption of 20% or less were determined to be closed cells. The shape recoverability was determined by the recoverability after 30 minutes after being placed in a gear oven at 70 ° C. under 50% compression, left for 22 hours, and then opened. The recovery rate was 80% or more, Δ, 50% or more. Is rated as Δ, and less than 50% is rated as x.

【0020】上記の表1および表2から明らかなよう
に、カーボンブラックおよび炭酸カルシウムをそれぞれ
適量配合した実施例1は、気泡が連続気泡であり、電気
抵抗および硬度が低く、ブリードアウトがなく、発泡度
および形状回復性に優れている。これに対し、炭酸カル
シウムが過剰な比較例1は硬度が過大で、発泡度が悪
く、また炭酸カルシウムが少ない比較例2は電気抵抗が
高い。また、カーボンブラックを多くし、炭酸カルシウ
ムを省略した比較例3は硬度が過大で、気泡が独立気泡
であり、発泡度および形状回復性が劣っており、また上
記比較例3の可塑剤を多くして発泡度および硬度を改善
しようとした比較例4は、硬度と発泡度に若干の改善が
認められるものの、ブリードアウトが発生した。なお、
上記実施例1および比較例1、2の配合のコンパウンド
をそれぞれ一次加硫用の金型に充填し、従来と同様に分
解性発泡剤の分解温度よりも高い温度(170℃)で加
圧発泡を行って加硫反応および発泡反応を完結させ、し
かるのち常圧下で発泡させた場合は、いずれも気泡が独
立気泡となり、形状回復性が悪かった。
As is clear from Tables 1 and 2 above, in Example 1 in which carbon black and calcium carbonate were blended in appropriate amounts, the cells were open cells, had low electric resistance and hardness, had no bleed-out, Excellent foaming degree and shape recovery. On the other hand, Comparative Example 1 with excessive calcium carbonate has excessive hardness and poor foaming degree, and Comparative Example 2 with small calcium carbonate has high electric resistance. Comparative Example 3, in which carbon black was increased and calcium carbonate was omitted, had excessive hardness, closed cells, poor foaming degree and poor shape recovery, and increased the amount of plasticizer in Comparative Example 3 above. In Comparative Example 4 in which the degree of foaming and the hardness were to be improved, although the hardness and the degree of foaming were slightly improved, bleed-out occurred. In addition,
Each of the compounds of Examples 1 and Comparative Examples 1 and 2 was filled in a mold for primary vulcanization, and foamed under pressure at a temperature (170 ° C.) higher than the decomposition temperature of the decomposable foaming agent in the same manner as before. Was carried out to complete the vulcanization reaction and the foaming reaction. Thereafter, when the foaming was carried out under normal pressure, the bubbles became closed cells and the shape recovery was poor.

【0021】上記実施例1における炭酸カルシウムに代
えて湿式シリカ(徳山曹達社製、商品名「トクシールG
U」)を40重量部加え、その他は実施例1と同様にし
て実施例2の導電性ゴム発泡体を製造した。また、上記
の炭酸カルシウムに代えてアルミニウムシリケートを4
0重量部加え、その他は実施例1と同様にして実施例3
の導電性ゴム発泡体を製造した。この実施例2および実
施例3の導電性ゴム発泡体の性能は、下記の表3に示す
とおり、実施例1と同様に優れていた。
In place of calcium carbonate in Example 1 above, wet silica (trade name “TOKUSEAL G” manufactured by Tokuyama Soda Co., Ltd.)
U ") was added, and the other procedure was the same as that of Example 1 to produce a conductive rubber foam of Example 2. In addition, aluminum silicate is used instead of the above calcium carbonate.
Example 3 was added in the same manner as in Example 1 except for adding 0 parts by weight.
Was produced. As shown in Table 3 below, the performance of the conductive rubber foams of Examples 2 and 3 was excellent as in Example 1.

【0022】 表 3 実施例2 実施例3 電気抵抗率(Ωcm) 3×103 2×103 硬度(度) 55 50 ブリード 無 無 発泡度 優 優 気泡形態 連続 連続 形状回復性 ○ ○ Table 3 Example 2 Example 3 Electric resistivity (Ωcm) 3 × 10 3 2 × 10 3 Hardness (degree) 55 50 Bleed No No Foaming degree Excellent Excellent Bubble morphology Continuous Continuous Shape recovery ○ ○

【0023】[0023]

【発明の効果】以上に説明したように、請求項1記載の
発明は、EPDMからなる導電性ゴム発泡体であるた
め、耐熱性、耐薬品性および耐候性等に優れると共に、
カーボンブラックに炭酸カルシウム、シリカおよびシリ
ケートのいずれか1種もしくは2種以上が併用されてい
るため、カーボンブラックの配合量が比較的少ないにも
かかわらず、高い導電性を有し、かつ加硫前の粘度が低
くなって発泡が容易になり、気泡が均一に形成され、し
かも気泡が連続気泡であるため、硬度が低く、形状回復
性が良好であり、可塑剤を大量に使用する必要がない。
As described above, the first aspect of the present invention is a conductive rubber foam made of EPDM, which is excellent in heat resistance, chemical resistance, weather resistance, and the like.
Since one or more of calcium carbonate, silica, and silicate are used in combination with carbon black, it has high conductivity despite the relatively small amount of carbon black, and before vulcanization. Has low viscosity, foaming is easy, bubbles are formed uniformly, and since the cells are open cells, the hardness is low, the shape recovery is good, and it is not necessary to use a large amount of plasticizer. .

【0024】そして、請求項2に記載の発明は、EPD
M100重量部に対しカーボンブラックを10〜40重
量部、炭酸カルシウム、シリカおよびシリケートのいず
れか1種もしくは2種以上を合計20〜80重量部およ
び分解性発泡剤その他の添加剤を必要量配合して混練り
し、得られたコンパウンドを金型内に充填し、上記分解
性発泡剤の分解温度よりも低い温度の加圧下で一次加硫
を行い、次いで上記分解性発泡剤の分解温度よりも高い
温度の常圧下で二次加硫を行うと同時に発泡させて連続
気泡と独立気泡が混在する発泡ゴムとし、次いでこの発
泡ゴムを圧縮して上記の独立気泡を破壊する方法である
から、上記請求項1に記載された導電性ゴム発泡体を容
易に製造することができる。
The invention according to claim 2 is an EPD.
A required amount of 10 to 40 parts by weight of carbon black, 20 to 80 parts by weight in total of one or more of calcium carbonate, silica and silicate and a decomposable foaming agent and other additives is added to 100 parts by weight of M. And kneading, filling the obtained compound into a mold, performing primary vulcanization under pressure at a temperature lower than the decomposition temperature of the decomposable foaming agent, and then performing the primary vulcanization at a temperature lower than the decomposition temperature of the decomposable foaming agent. Performing secondary vulcanization under normal pressure at a high temperature and foaming at the same time to form a foamed rubber in which open cells and closed cells are mixed, and then compressing the foamed rubber to destroy the closed cells, The conductive rubber foam according to claim 1 can be easily manufactured.

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 EPDM100重量部に対しカーボンブ
ラックが10〜40重量部、並びに炭酸カルシウム、シ
リカおよびシリケートのいずれか1種もしくは2種以上
が合計20〜80重量部配合されており、気泡形態が連
続気泡であり、硬度(アスカーF硬度)が80度以下、
抵抗率が1×106 Ωcm以下であることを特徴とする導
電性ゴム発泡体。
1. A carbon foam is mixed with 10 to 40 parts by weight and a total of 20 to 80 parts by weight of one or more of calcium carbonate, silica and silicate based on 100 parts by weight of EPDM. It is an open cell with a hardness (Asker F hardness) of 80 degrees or less,
A conductive rubber foam having a resistivity of 1 × 10 6 Ωcm or less.
【請求項2】 EPDM100重量部に対しカーボンブ
ラックを10〜40重量部、炭酸カルシウム、シリカお
よびシリケートのいずれか1種もしくは2種以上を合計
20〜80重量部、分解性発泡剤、加硫剤、加硫促進
剤、可塑剤およびその他必要な配合剤をそれぞれ適量配
合して混練りし、得られたコンパウンドを金型に充填
し、上記分解性発泡剤の分解温度よりも低い温度の加圧
下で一次加硫を行い、次いで上記分解性発泡剤の分解温
度よりも高い温度の常圧下で二次加硫を行うと同時に発
泡させ連続気泡と独立気泡が混在する発泡ゴムとし、次
いでこの発泡ゴムを圧縮して上記の独立気泡を破壊する
ことを特徴とする導電性ゴム発泡体の製造法。
2. 10 to 40 parts by weight of carbon black, 20 to 80 parts by weight of one or more of calcium carbonate, silica and silicate based on 100 parts by weight of EPDM, decomposable foaming agent, vulcanizing agent , A vulcanization accelerator, a plasticizer and other necessary compounding agents are each compounded in an appropriate amount and kneaded, and the obtained compound is filled in a mold and subjected to pressure under a temperature lower than the decomposition temperature of the decomposable foaming agent. Primary vulcanization, then secondary vulcanization under normal pressure at a temperature higher than the decomposition temperature of the decomposable foaming agent, and simultaneously foaming to form a foamed rubber in which open cells and closed cells are mixed, and then this foamed rubber A method for producing a conductive rubber foam, characterized in that the foam is compressed to break the closed cells.
JP22518493A 1993-08-17 1993-08-17 Conductive rubber foam and method for producing the same Expired - Lifetime JP2753676B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22518493A JP2753676B2 (en) 1993-08-17 1993-08-17 Conductive rubber foam and method for producing the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22518493A JP2753676B2 (en) 1993-08-17 1993-08-17 Conductive rubber foam and method for producing the same

Publications (2)

Publication Number Publication Date
JPH0753758A JPH0753758A (en) 1995-02-28
JP2753676B2 true JP2753676B2 (en) 1998-05-20

Family

ID=16825285

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22518493A Expired - Lifetime JP2753676B2 (en) 1993-08-17 1993-08-17 Conductive rubber foam and method for producing the same

Country Status (1)

Country Link
JP (1) JP2753676B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH11125956A (en) * 1997-10-22 1999-05-11 Casio Electron Mfg Co Ltd Electrifying member and electronic image forming device using that
JP6599118B2 (en) * 2015-03-31 2019-10-30 三和化工株式会社 EPDM open cell body and method for producing the same

Also Published As

Publication number Publication date
JPH0753758A (en) 1995-02-28

Similar Documents

Publication Publication Date Title
EP1512713B1 (en) Composition for polyolefin resin foam, foam of the same, and process for producing foam
EP0016348B1 (en) Method of making polyethylene blend foams having improved compressive strength and foams prepared by said method
JP3547758B2 (en) EPDM composition and method for producing the same
CA1136393A (en) Handling additive for silicone elastomers comprising boric acid and ethylene glycol or glycerol
EP1954750B1 (en) Foamable composition for production of foamed plastics
JP2753676B2 (en) Conductive rubber foam and method for producing the same
JP2866308B2 (en) Conductive foam rubber and method for producing the same
JPH0742361B2 (en) Method of manufacturing sponge rubber products
JPH0216338B2 (en)
CA1206700A (en) Low density cellular polyvinyl chloride
CN103642080B (en) Natural rubber sponge with high compressive load retention rate and preparation method thereof
KR20140083360A (en) Flame-retarded thermal insulating foam of chemical cross-linked polyvinyl chloride based and manufacturing method of the same
JP2007211119A (en) Flame-retardant epdm foamed body and method for producing the same
JP4974538B2 (en) EPDM foam and method for producing the same
JP3423365B2 (en) Composition for producing open-cell resin foam
JP3565815B2 (en) Conductive cross-linked polyethylene foam and method for producing the same
CN104893061A (en) Peculiar smell-adsorbing environmentally-friendly flame-retardant foamed plastic and preparation method thereof
JP4782306B2 (en) Open-cell cross-linked polyolefin foam and method for producing the same
KR102111505B1 (en) Manufacturing method for low hardness, high elasticity, and wear-resistant wheelchair wheel foam embedded materials and their internal materials
CN110845781B (en) PE foam material yoga mat and preparation method thereof
JPS58101126A (en) Expandable vinyl chloride resin composition for gasket of refrigerator
JP2003096224A (en) Production method of oscillation-restrictive bridging resin foam
CN112226085A (en) Flame-retardant organic silicon foam catalyst and preparation method thereof
JPS62112636A (en) Electrically conductive crosslinked polyethylene foam
JP2003171489A (en) Rubber foamed material for sealing