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JP3642890B2 - Method for producing silicone rubber foam - Google Patents
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JP3642890B2 - Method for producing silicone rubber foam - Google Patents

Method for producing silicone rubber foam Download PDF

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Publication number
JP3642890B2
JP3642890B2 JP22834496A JP22834496A JP3642890B2 JP 3642890 B2 JP3642890 B2 JP 3642890B2 JP 22834496 A JP22834496 A JP 22834496A JP 22834496 A JP22834496 A JP 22834496A JP 3642890 B2 JP3642890 B2 JP 3642890B2
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Japan
Prior art keywords
silicone rubber
pressure
rubber composition
foam
curing
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Expired - Fee Related
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JP22834496A
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Japanese (ja)
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JPH1067039A (en
Inventor
智 小田嶋
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Shin Etsu Polymer Co Ltd
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Shin Etsu Polymer Co Ltd
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Priority to JP22834496A priority Critical patent/JP3642890B2/en
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  • Extrusion Moulding Of Plastics Or The Like (AREA)
  • Molding Of Porous Articles (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は、断熱材、OA機器用ロール、緩衝材、化粧用パフ、各種成形体の軽量化等に用いられるシリコーン系ゴム発泡体の製造方法に関するものである。
【0002】
【従来の技術】
熱可塑性樹脂発泡体を製造する方法としては、発泡剤を用いて化学反応によって気泡を発生させる化学発泡と、気体を直接樹脂に混合する物理発泡とが一般的に知られており、シリコーン系ゴム分野では、専ら硬化反応と同時に化学発泡を行う方法が採られてきた。そしてこの方法によって得られる気泡径は、例えば特開平7-241934号公報に示されるように、シリコーンゴムパウダーを混入することにより気泡径とその分散性が均一で微細な気泡を有する発泡体を得る工夫がなされているが、この方法によっても気泡径は 300〜 700μm程度であり、また本発明者の研究によれば、シリコーン系ゴム組成物の硬化方法を種々の方法で制御することにより、 100超〜 300μm程度の気泡径が得られるが、これ以下にはならなかった。
【0003】
【発明が解決しようとする課題】
しかし、上記従来のゴム 泡体の製造方法、特にシリコーン系ゴム発泡体の製造方法では、発泡と硬化が加熱という1つの制御条件で同時に進行し且つ発泡温度と硬化温度が接近しているため、微細で均一な気泡径と気泡の均一な分散性を有する[以下単に(均一な)と略す]発泡体を安定して得ることが困難であり、また均一な発泡体を安定して得る為には、硬化速度と発泡速度を高度に制御する必要があった。それによっても気泡径は前記の範囲が限度であり、より微細な気泡径を有する発泡体を得ることは不可能であった。
すなわち本発明は、硬化速度と発泡速度を高度に制御することなく気泡径が 100μm以下の均一な発泡体を安定して生産性良く得ることができる、シリコーン系ゴム発泡体の製造方法を提供するものである。
【0004】
【課題を解決するための手段】
本発明は前記従来の問題点を解決したシリコーン系ゴム発泡体の製造方法に関するものであり、押出機を使用し、未硬化または半硬化状態のシリコーン系ゴム組成物に、常温常圧で気体の物質(以下単に気体物質という)を、その臨界圧力以上、臨界温度以上で浸透、拡散させた後、圧力を低下させて未硬化あるいは半硬化状態で発泡させ、成形硬化を行うシリコーン系ゴム発泡体の製造方法において、気体物質の注入部における、気体物質とシリコーン系ゴム組成物との接触面積S(cm2の絶対値Sと、シリコーン系ゴム組成物の押出速度V(cm3/min.)の絶対値Vとの関係が、S≧2Vであり、圧力を低下させる速度が10kgf/cm2/sec.以上であることを特徴とするものである。
【0005】
【発明の実施の形態】
即ち、本発明者は、均一なシリコーン系ゴム発泡体を安定して生産性良く得るためには、物理発泡により、微細な気泡を連続的に発生させればよいことに着眼し、その方法、条件、原料について種々検討を重ねた結果本発明に到達した。以下に本発明について詳しく述べる。
【0006】
本発明において気体物質を臨界温度以上、臨界圧力以上としてシリコーン系ゴム組成物へ浸透、拡散させるのは、気体物質を高密度かつ速やかにシリコーン系ゴム組成物中へ浸透、拡散させるためである。
また、気体物質の注入部における気体物質とシリコーン系ゴム組成物との接触面積S(cm2の絶対値Sと、シリコーン系ゴム組成物の押出速度V(cm3/min.)の絶対値Vとの関係を、S≧2Vとするのは、臨海温度以上、臨界圧力以上にある気体物質を、シリコーン系ゴム組成物中へ均一且つ十分に浸透、拡散させるためで、Sの値が2V未満では圧力を低下させたとき発泡する気泡数が少なくなり、発泡体としての十分な性能のものを得ることができない。つまりシリコーン系ゴムを発泡させる目的は低硬度の成形体を得ることにあり、具体的には発泡前に硬度50のものを発泡体とした時に20〜40 とするためには、発泡倍率1.5 以上とする必要があるが、S<2Vではこのような発泡体を得ることができない。
【0007】
さらに本発明において圧力を10kgf/cm2/sec.以上の速度で低下させるのは、 100μm以下、具体的には100 μmの微細な気泡を形成させるためであり、10kgf/cm2/sec.未満の速度で低下させると気泡径は 100μm超、著しくは 500μm以上となり、目的の発泡体を得ることができない。また、圧力を低下させる速度の上限は特に限定されないが、工業的には 500kgf/cm2/sec.以下で設計するのが実用的である。
【0008】
本発明に用いられるシリコーン系ゴム組成物としては、従来公知の物を用いれば良く、シロキサン結合を有する高分子化合物とパーオキサイドとからなるもの、シロキサン結合を有する高分子化合物及び珪素原子に直結した水素原子を1分子中に少なくとも2個以上有するオルガノハイドロジェンポリシロキサンと白金系触媒とからなるものなどが挙げられる。
また、上記シロキサン結合を有する高分子化合物及びオルガノハイドロジェンポリシロキサンは、エポキシ基、アクリル基、ハロゲン原子等を含むものであっても良い。
【0009】
さらに本発明においては、シリコーン系ゴム組成物の硬化剤として、硬化温度の異なる2種以上のものを併用し、まず前記硬化剤として少なくとも1種を残して、その他の硬化剤によりシリコーン系ゴム組成物の半硬化を行い、気体物質を注入浸透、拡散させた後、圧力を低下させて半硬化状態で発泡させ、残った硬化剤を使用して加熱硬化を行えば、発泡時の組成物の粘度調整が任意にでき、発泡状態の制御及び成形が容易にできる。なおシリコーン系ゴム組成物には、必要に応じて、難燃剤、老化防止剤、耐候性向上剤、耐衝撃性向上剤、補強剤、着色剤、導電性付与剤等の各種添加剤を添加することは差し支えない。なお、本発明における未硬化あるいは半硬化状態とは、押出機、ダイス内において塑性流動し、所望の形に成形、硬化させることが可能な状態を示す。
【0010】
本発明に使用される気体物質としては、特に制限はないが、水素、ヘリウム、窒素、酸素、ネオン、アルゴン、二酸化炭素、メタン、エタン、プロパン、ブタン、エチレン、プロピレン等及びこれらの混合物から選ばれた少なくとも1種のものが例示され、化学的に安定であり、臨界温度が常温に近いことから特に二酸化炭素が好ましい。
【0011】
本発明に用いられる装置としては、図1のような公知の押出機が使用可能である。この際前述のように気体物質5(図1ではCO2 5) の注入部における、気体物質5とシリコーン系ゴム組成物1との接触面積S(cm2の絶対値Sとシリコーン系ゴム組成物1の押出速度V(cm3/min.)の絶対値Vとの関係を、S≧2Vとすることが均一なシリコーン系ゴム発泡体6を得るのに必要であり、この気体物質注入部は、押出機中の、少なくとも1カ所以上に設けられている圧縮部以後に設けるか、図1のようにギアポンプ3によりシリコーン系ゴム組成物1の圧を一定値以上に上昇させる部分の後に設けることが良く、このようにすれば、気体物質5の押出機内での逆流を防ぐことができる。
また、本発明におけるSと2Vの関係を満たす手段としては、この気体物質5の注入部に空間を設けてそこに多孔質物体4を充填し、この多孔質物体4を介して気体物質5を注入すれば、所望の接触面積を容易に得ることができるとともにシリコーン系ゴム組成物1が気体物質注入部に逆流するのを防ぐことができる。
【0012】
シリコーン系ゴム組成物を硬化させる方法としては、加熱、電子線照射、UV照射、放射線照射等が例示され、シリコーン系ゴム組成物の種類により適宜選択することが可能であるが、安全性、汎用性を考慮すると加熱、または電子線照射による方法が好ましく、更には、本発明においてはシリコーン系ゴム組成物を発泡させた後に硬化させるため、発泡した未硬化または半硬化状態のシリコーン系ゴム組成物が断熱性を有するようになるので、高周波加熱による方法か、電子線照射による方法などの、熱伝導性に影響を与えず、内部まで均一に硬化させる方法を用いることが最も好ましい。
【0013】
【実施例】
次に実施例を挙げて本発明を説明する。
(実施例1)
気体物質と組成物との接触面積Sを250cm2となるような多孔質セラミックスを充填した気体物質注入部をギアポンプの後に設けた50mm単軸ゴム用押出機に、シリコーン系ゴムコンパウンド「KE151−U」(信越化学製、商品名) 100重量部と加硫剤・ビス−2,4 - ジクロロベンゾイルパーオキサイド・「C−2」(信越化学製、商品名)3重量部とからなる混練物(比重1.15)を供給した。
ギアポンプにより上記混練物圧を150kgf/cm2まで上昇させるとともに温度を50℃まで上昇させ、二酸化炭素を上記多孔質セラミックスを介して50℃、152kgf/cm2で供給し、φ2mmの丸ダイスから押し出すと同時に圧力を2秒間で開放しシリコーンゴム組成物の発泡体を得た。このときの組成物の押出速度Vは43.5cm3/min とした。これを高周波加熱により、 180℃で2分間処理した後、 200℃のオーブンで4時間アフターキュアしてシリコーンゴム発泡体を得た。
この時の発泡倍率は 2.6倍、気泡の平均サイズは42μm、気泡サイズの標準偏差は 3.1μmであった。
【0014】
(比較例1)
実施例1で使用した押出機中の同じ位置の気体物質注入部に、気体物質と混練物との接触面積Sが 50cm2となるような多孔質セラミックスを充填し、シリコーンゴムコンパウンド「KE151−U」(前出) 100重量部と加硫剤・ビス−2,4 - ジクロロベンゾイルパーオキサイド・「C−2」(前出)3重量部とからなる混練物を供給した。
ギアポンプにより混練物圧を150kgf/cm2まで上昇させるとともに、温度を50℃まで上昇させ、二酸化炭素を上記多孔質セラミックスを介して50℃、152kgf/cm2で供給し、φ2mmの丸ダイスから押し出すと同時に圧力を2秒間で解放した。このときの混練物押出速度Vを43.5cm3/min とした。
これを高周波加熱により、 180℃で2分間処理した後、 200℃のオーブンで4時間アフターキュアしてシリコーンゴム組成物発泡体を得た。この時の発泡倍率は 1.2倍で、気泡数が少なく発泡体と呼べるものではなかった。
【0015】
【発明の効果】
本発明によれば、硬化速度と発泡速度を高度に制御することなしに、気泡のサイズが 100μm未満の、均一で微細な気泡径と均一な気泡分散性を有するシリコーン系ゴム発泡体を安定して得ることができるので、製造コストダウンができ、様々な用途への応用が可能となる。
【図面の簡単な説明】
【図1】本発明において用いられる押出機の一例の縦断面図である。
【符号の説明】
1 シリコーン系ゴム組成物、 6 シリコーン系ゴム発泡体。
2 スクリュー、
3 ギアポンプ、
4 多孔質物体、
5 CO2 (気体物質)、
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a method for producing a silicone rubber foam used for heat insulation, rolls for OA equipment, cushioning materials, cosmetic puffs, weight reduction of various molded articles, and the like.
[0002]
[Prior art]
As a method for producing a thermoplastic resin foam, chemical foaming in which bubbles are generated by a chemical reaction using a foaming agent and physical foaming in which a gas is directly mixed with a resin are generally known. Silicone rubber In the field, a method of performing chemical foaming simultaneously with the curing reaction has been employed. The bubble diameter obtained by this method is, for example, as shown in JP-A-7-241934, by mixing silicone rubber powder, a foam having uniform and fine dispersibility is obtained. Although the device has been devised, the bubble diameter is about 300 to 700 μm even by this method, and according to the study of the present inventor, by controlling the curing method of the silicone rubber composition by various methods, 100 A bubble diameter of ultra-300 μm was obtained, but it was not less than this.
[0003]
[Problems to be solved by the invention]
However, in the above conventional rubber foam production method, particularly the silicone rubber foam production method, foaming and curing proceed simultaneously under one control condition of heating, and the foaming temperature and the curing temperature are close to each other. It is difficult to stably obtain a foam having a fine and uniform bubble diameter and a uniform dispersibility of bubbles [hereinafter simply referred to as (uniform)], and to obtain a uniform foam stably. However, it was necessary to control the curing rate and the foaming rate to a high degree. Even in this case, the bubble diameter is limited to the above range, and it was impossible to obtain a foam having a finer bubble diameter.
That is, the present invention provides a method for producing a silicone rubber foam, which can stably obtain a uniform foam having a cell diameter of 100 μm or less and high productivity without highly controlling the curing rate and the foaming rate. Is.
[0004]
[Means for Solving the Problems]
The present invention relates to a method for producing a silicone rubber foam that solves the above-mentioned conventional problems, and an extruder is used to apply a gas at normal temperature and pressure to an uncured or semi-cured silicone rubber composition. A silicone rubber foam that is molded and cured by infiltrating and diffusing a substance (hereinafter simply referred to as a gaseous substance) above its critical pressure and above its critical temperature, and then reducing the pressure to foam it in an uncured or semi-cured state. In the manufacturing method, the absolute value S of the contact area S (cm 2 ) between the gas substance and the silicone rubber composition in the injection part of the gas substance and the extrusion rate V (cm 3 / min. Of the silicone rubber composition). ) In relation to the absolute value V is S ≧ 2 V, and the pressure reducing speed is 10 kgf / cm 2 / sec. Or more.
[0005]
DETAILED DESCRIPTION OF THE INVENTION
That is, the present inventor noticed that fine bubbles need only be continuously generated by physical foaming in order to stably obtain a uniform silicone rubber foam with good productivity. As a result of various studies on conditions and raw materials, the present invention has been achieved. The present invention is described in detail below.
[0006]
In the present invention, the gaseous substance is permeated and diffused into the silicone rubber composition at a critical temperature or higher and a critical pressure or higher in order to permeate and diffuse the gaseous substance into the silicone rubber composition quickly and with high density.
In addition, the absolute value S of the contact area S (cm 2 ) between the gaseous substance and the silicone rubber composition in the injection part of the gaseous substance and the absolute value of the extrusion rate V (cm 3 / min.) Of the silicone rubber composition The relationship with V is set to S ≧ 2V in order to uniformly and sufficiently permeate and diffuse a gas substance having a temperature above the critical temperature and above the critical pressure into the silicone rubber composition. If the pressure is lower, the number of foamed bubbles decreases when the pressure is lowered, and a foam having sufficient performance cannot be obtained. In other words, the purpose of foaming the silicone rubber is to obtain a molded product having a low hardness, specifically 20 to 40 when a foam having a hardness of 50 before foaming . In order to achieve this, it is necessary to set the expansion ratio to 1.5 or more, but such foam cannot be obtained with S <2V.
[0007]
Further, in the present invention, the pressure is decreased at a rate of 10 kgf / cm 2 / sec. Or more in order to form fine bubbles of 100 μm or less, specifically 100 μm, and less than 10 kgf / cm 2 / sec. The bubble diameter becomes over 100 μm, remarkably over 500 μm, and the desired foam cannot be obtained. In addition, the upper limit of the speed at which the pressure is reduced is not particularly limited, but industrially it is practical to design at 500 kgf / cm 2 / sec.
[0008]
As the silicone rubber composition used in the present invention, a conventionally known material may be used, which is composed of a polymer compound having a siloxane bond and a peroxide, a polymer compound having a siloxane bond, and a silicon atom. Examples thereof include those comprising an organohydrogenpolysiloxane having at least two hydrogen atoms in one molecule and a platinum catalyst.
The polymer compound having a siloxane bond and the organohydrogenpolysiloxane may contain an epoxy group, an acrylic group, a halogen atom, or the like.
[0009]
Furthermore, in the present invention, two or more types of curing agents having different curing temperatures are used in combination as the curing agent for the silicone rubber composition, and at least one of the curing agents is left as the curing agent. After semi-curing the material, injecting and diffusing the gaseous substance, reducing the pressure, foaming in the semi-cured state, and performing heat curing using the remaining curing agent, the composition of the foamed composition The viscosity can be adjusted arbitrarily, and the foaming state can be easily controlled and molded. In addition, various additives such as flame retardants, anti-aging agents, weather resistance improvers, impact resistance improvers, reinforcing agents, colorants, and conductivity imparting agents are added to the silicone rubber composition as necessary. There is no problem. In addition, the uncured or semi-cured state in the present invention indicates a state in which it can be plastically flowed in an extruder and a die, and molded and cured into a desired shape.
[0010]
The gaseous substance used in the present invention is not particularly limited, but is selected from hydrogen, helium, nitrogen, oxygen, neon, argon, carbon dioxide, methane, ethane, propane, butane, ethylene, propylene, and the like and mixtures thereof. In particular, carbon dioxide is preferable because it is chemically stable and has a critical temperature close to room temperature.
[0011]
As an apparatus used in the present invention, a known extruder as shown in FIG. 1 can be used. At this time, as described above, the absolute value S of the contact area S (cm 2 ) between the gaseous substance 5 and the silicone rubber composition 1 and the silicone rubber composition in the injection portion of the gaseous substance 5 (CO 2 5 in FIG. 1). In order to obtain a uniform silicone rubber foam 6, it is necessary that the relationship between the extrusion rate V (cm 3 / min.) Of the product 1 and the absolute value V is S ≧ 2 V, and this gas substance injection portion Is provided after the compression part provided in at least one place in the extruder, or after the part where the pressure of the silicone rubber composition 1 is raised to a certain value or more by the gear pump 3 as shown in FIG. If it does in this way, the backflow in the extruder of the gaseous substance 5 can be prevented.
Further, as means for satisfying the relationship between S and 2V in the present invention, a space is provided in the injection part of the gaseous substance 5 and the porous object 4 is filled therewith, and the gaseous substance 5 is filled through the porous object 4. By injecting, the desired contact area can be easily obtained and the silicone rubber composition 1 can be prevented from flowing back to the gas substance injection portion.
[0012]
Examples of the method for curing the silicone rubber composition include heating, electron beam irradiation, UV irradiation, radiation irradiation and the like, and can be appropriately selected depending on the type of the silicone rubber composition. In view of the properties, a method by heating or electron beam irradiation is preferable. Further, in the present invention, since the silicone rubber composition is foamed and then cured, the foamed uncured or semi-cured silicone rubber composition is used. Therefore, it is most preferable to use a method of uniformly curing to the inside without affecting the thermal conductivity, such as a method using high-frequency heating or a method using electron beam irradiation.
[0013]
【Example】
Next, an Example is given and this invention is demonstrated.
(Example 1)
A silicone rubber compound “KE151-U” was placed in a 50 mm single-screw rubber extruder provided with a gas material injection part after a gear pump filled with porous ceramics having a contact area S of 250 cm 2 between the gas material and the composition. "(Shin-Etsu Chemical, trade name) 100 parts by weight and vulcanizing agent, bis-2,4-dichlorobenzoyl peroxide," C-2 "(Shin-Etsu Chemical, trade name) 3 parts by weight A specific gravity of 1.15) was supplied.
The kneaded product pressure is increased to 150 kgf / cm 2 by a gear pump, the temperature is increased to 50 ° C., carbon dioxide is supplied at 50 ° C. and 152 kgf / cm 2 through the porous ceramic, and extruded from a φ2 mm round die. At the same time, the pressure was released in 2 seconds to obtain a foamed silicone rubber composition. The extrusion rate V of the composition at this time was 43.5 cm 3 / min. This was treated by high frequency heating at 180 ° C. for 2 minutes, and then after-cured in an oven at 200 ° C. for 4 hours to obtain a silicone rubber foam.
At this time, the expansion ratio was 2.6 times, the average bubble size was 42 μm, and the standard deviation of the bubble size was 3.1 μm.
[0014]
(Comparative Example 1)
In the gas substance injection portion at the same position in the extruder used in Example 1, porous ceramics having a contact area S between the gas substance and the kneaded material of 50 cm 2 is filled, and the silicone rubber compound “KE151-U” is filled. (Supra) 100 parts by weight and a vulcanizing agent, bis-2,4-dichlorobenzoyl peroxide and "C-2" (supra) 3 parts by weight were fed.
The kneaded material pressure is increased to 150 kgf / cm 2 by a gear pump, the temperature is increased to 50 ° C., carbon dioxide is supplied at 50 ° C. and 152 kgf / cm 2 through the porous ceramic, and extruded from a φ2 mm round die. At the same time, the pressure was released in 2 seconds. The kneaded product extrusion speed V at this time was 43.5 cm 3 / min.
This was treated by high frequency heating at 180 ° C. for 2 minutes and then aftercured in an oven at 200 ° C. for 4 hours to obtain a silicone rubber composition foam. The foaming ratio at this time was 1.2 times, and the number of bubbles was small, so it was not a foam.
[0015]
【The invention's effect】
According to the present invention, a silicone rubber foam having a uniform and fine cell diameter and uniform cell dispersibility with a cell size of less than 100 μm can be stabilized without highly controlling the curing rate and the foaming rate. Therefore, the manufacturing cost can be reduced and application to various uses becomes possible.
[Brief description of the drawings]
FIG. 1 is a longitudinal sectional view of an example of an extruder used in the present invention.
[Explanation of symbols]
1 silicone rubber composition, 6 silicone rubber foam.
2 screws,
3 Gear pump,
4 porous objects,
5 CO 2 (gas substance),

Claims (1)

押出機を使用し、未硬化または半硬化状態のシリコーン系ゴム組成物に、常温常圧で気体の物質を、その臨界圧力以上、臨界温度以上で浸透、拡散させた後、圧力を低下させて未硬化あるいは半硬化状態で発泡させ、成形硬化を行うシリコーン系ゴム発泡体の製造方法において、常温常圧で気体の物質の注入部における、常温常圧で気体の物質とシリコーン系ゴム組成物との接触面積S(cm2の絶対値Sと、シリコーン系ゴム組成物の押出速度V(cm3/min.)の絶対値Vとの関係が、S≧2Vであり、圧力を低下させる速度が10kgf/cm2/sec.以上であることを特徴とするシリコーン系ゴム発泡体の製造方法。Using an extruder, in a silicone rubber composition in an uncured or semi-cured state, infiltrate and diffuse a gaseous substance at room temperature and normal pressure above its critical pressure and above its critical temperature, and then reduce the pressure. In a method for producing a silicone rubber foam, which is foamed in an uncured or semi-cured state and cured by molding, a gas substance at normal temperature and pressure and a silicone rubber composition in an injection part of the gas substance at normal temperature and pressure The relationship between the absolute value S of the contact area S (cm 2 ) and the absolute value V of the extrusion rate V (cm 3 / min.) Of the silicone rubber composition is S ≧ 2V, and the pressure is reduced. Of 10 kgf / cm 2 / sec. Or more, a method for producing a silicone rubber foam, wherein
JP22834496A 1996-08-29 1996-08-29 Method for producing silicone rubber foam Expired - Fee Related JP3642890B2 (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9395668B2 (en) 2014-10-09 2016-07-19 Synztec Co., Ltd. Pressure-applying fixing roller and fixing device

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB0500986D0 (en) 2005-01-18 2005-02-23 Zotefoams Plc Silicone foams, process to make them and applications thereof
JP5003905B2 (en) * 2008-04-16 2012-08-22 信越化学工業株式会社 Method for producing silicone rubber foam
TWI456810B (en) 2009-09-15 2014-10-11 名碩電腦(蘇州)有限公司 Light-emitting diode

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9395668B2 (en) 2014-10-09 2016-07-19 Synztec Co., Ltd. Pressure-applying fixing roller and fixing device

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