JPH04240295A - Production of expanded graphite sheet - Google Patents
Production of expanded graphite sheetInfo
- Publication number
- JPH04240295A JPH04240295A JP3085713A JP8571391A JPH04240295A JP H04240295 A JPH04240295 A JP H04240295A JP 3085713 A JP3085713 A JP 3085713A JP 8571391 A JP8571391 A JP 8571391A JP H04240295 A JPH04240295 A JP H04240295A
- Authority
- JP
- Japan
- Prior art keywords
- expanded graphite
- sheet
- expanded
- parts
- water
- 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
Links
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 51
- 239000010439 graphite Substances 0.000 title claims abstract description 51
- 229910002804 graphite Inorganic materials 0.000 title claims abstract description 51
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 6
- 239000002002 slurry Substances 0.000 claims abstract description 13
- 229920003235 aromatic polyamide Polymers 0.000 claims abstract description 12
- 239000000835 fiber Substances 0.000 claims abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 25
- 239000002245 particle Substances 0.000 claims description 18
- 239000011230 binding agent Substances 0.000 claims description 15
- 238000000034 method Methods 0.000 claims description 15
- 239000004760 aramid Substances 0.000 claims description 13
- 239000012783 reinforcing fiber Substances 0.000 claims description 7
- 238000002156 mixing Methods 0.000 claims description 6
- 238000010298 pulverizing process Methods 0.000 claims description 3
- 241000531908 Aramides Species 0.000 abstract 1
- 239000002994 raw material Substances 0.000 description 9
- 229920006231 aramid fiber Polymers 0.000 description 6
- 239000010425 asbestos Substances 0.000 description 6
- 239000004816 latex Substances 0.000 description 6
- 229920000126 latex Polymers 0.000 description 6
- 229910052895 riebeckite Inorganic materials 0.000 description 6
- 238000007789 sealing Methods 0.000 description 6
- 239000000463 material Substances 0.000 description 5
- 238000002485 combustion reaction Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000000839 emulsion Substances 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- 238000010009 beating Methods 0.000 description 2
- 206010061592 cardiac fibrillation Diseases 0.000 description 2
- 235000013351 cheese Nutrition 0.000 description 2
- 230000002600 fibrillogenic effect Effects 0.000 description 2
- 239000012784 inorganic fiber Substances 0.000 description 2
- 239000012744 reinforcing agent Substances 0.000 description 2
- 239000012779 reinforcing material Substances 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 238000004438 BET method Methods 0.000 description 1
- 229920003043 Cellulose fiber Polymers 0.000 description 1
- 229920000561 Twaron Polymers 0.000 description 1
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 description 1
- 229920000800 acrylic rubber Polymers 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 125000000129 anionic group Chemical group 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 125000002091 cationic group Chemical group 0.000 description 1
- -1 cellulose fibers Chemical class 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 239000003431 cross linking reagent Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 239000013013 elastic material Substances 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000008394 flocculating agent Substances 0.000 description 1
- 229920001973 fluoroelastomer Polymers 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 239000005011 phenolic resin Substances 0.000 description 1
- 229920000058 polyacrylate Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000004537 pulping Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 229920002379 silicone rubber Polymers 0.000 description 1
- 239000004945 silicone rubber Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 229920001187 thermosetting polymer Polymers 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- 239000004762 twaron Substances 0.000 description 1
- 235000014692 zinc oxide Nutrition 0.000 description 1
- 239000011787 zinc oxide Substances 0.000 description 1
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H13/00—Pulp or paper, comprising synthetic cellulose or non-cellulose fibres or web-forming material
- D21H13/36—Inorganic fibres or flakes
- D21H13/46—Non-siliceous fibres, e.g. from metal oxides
- D21H13/50—Carbon fibres
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H13/00—Pulp or paper, comprising synthetic cellulose or non-cellulose fibres or web-forming material
- D21H13/10—Organic non-cellulose fibres
- D21H13/20—Organic non-cellulose fibres from macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
- D21H13/26—Polyamides; Polyimides
Abstract
Description
【0001】0001
【産業上の利用分野】本発明は膨張黒鉛シートに関し、
更に詳しくは一般産業用や内燃機関の各種接合面をシー
ルするためのガスケット類などに用いられる耐熱性アス
ベストフリーの黒鉛シートの製造方法に関する。[Industrial Application Field] The present invention relates to an expanded graphite sheet.
More specifically, the present invention relates to a method for manufacturing a heat-resistant asbestos-free graphite sheet for use in general industry and gaskets for sealing various joint surfaces of internal combustion engines.
【0002】0002
【従来の技術】従来のガスケット類としてはアスベスト
を基材としたジョイントシートやビーターシートが使用
されてきた。しかしアスベストの人体への有害性からそ
の使用が規制される方向に進んでいる。ー方可撓性膨張
黒鉛シートも知られており、これはシール性、耐熱性に
は優れているものの、シートの機械的強度が低く、実際
の使用場面に於ける取り扱いに問題がある上に、耐水性
、耐油性に劣るという欠点を有する。[Prior Art] Joint sheets and beater sheets made of asbestos have been used as conventional gaskets. However, due to the toxicity of asbestos to the human body, the use of asbestos is being regulated. -Flexible expanded graphite sheets are also known, and although they have excellent sealing properties and heat resistance, they have low mechanical strength and are difficult to handle in actual use. However, it has the disadvantage of poor water resistance and oil resistance.
【0003】これらの代替としてアラミドパルプや無機
繊維に充填材を加え、ゴム状弾性体を結合剤にしたシー
トが開発されている。これらのシートは乾式法または湿
式法により製造されるが、機械強度を始め、耐熱性やシ
ール性がアスベストシートに劣るという欠点を有する。As an alternative to these, sheets have been developed in which fillers are added to aramid pulp or inorganic fibers, and a rubber-like elastic material is used as a binder. These sheets are manufactured by a dry method or a wet method, but they have the disadvantage that they are inferior to asbestos sheets in mechanical strength, heat resistance, and sealing properties.
【0004】このためこれら可撓性膨張黒鉛シートの改
良が試みられている。たとえば特開平2−124767
号公報のようにゴム状バインダーを膨張黒鉛粒子に塗布
し、シートの耐折性や耐油性の改良を計っているが、単
独成形体の用途にまで至っていない。また特開昭62−
288180号公報のように膨張黒鉛成形体に水溶性の
熱硬化性樹脂を含浸し、樹詣を加熱硬化させて、機械強
度や液体の不浸透性を改善しているが、最も重要な特性
である可撓性を失い、取り扱い上の問題も解決するに至
っていない。更に特開昭60−71578号公報や、特
開昭63−72780号公報のように膨張黒鉛粒子に補
強用の繊維や結合剤を配合する方法が示されているが、
効果が充分でなく、脆さや機械強度を充分カバーするこ
とはできていない。[0004] For this reason, attempts have been made to improve these flexible expanded graphite sheets. For example, JP-A-2-124767
As in the publication, a rubber-like binder is applied to expanded graphite particles in an attempt to improve the folding durability and oil resistance of the sheet, but this method has not reached the point where it can be used as a single molded product. Also, JP-A-62-
As in Japanese Patent No. 288180, an expanded graphite molded body is impregnated with a water-soluble thermosetting resin and the resin is heated and hardened to improve mechanical strength and liquid impermeability, but the most important properties are It has lost some flexibility and handling problems have not yet been solved. Furthermore, as in JP-A-60-71578 and JP-A-63-72780, a method of blending reinforcing fibers and a binder with expanded graphite particles is disclosed.
The effect is not sufficient, and it is not possible to fully compensate for brittleness and mechanical strength.
【0005】[0005]
【発明が解決しようとする課題】本発明が解決しようと
する課題は従来のこの種黒鉛シート就中膨張黒鉛シート
の欠点を解消し、優れた機械的強度を有するアスベスト
フリーの膨張黒鉛シートを新たに開発することである。[Problems to be Solved by the Invention] The problems to be solved by the present invention are to eliminate the drawbacks of conventional graphite sheets of this type, especially expanded graphite sheets, and to create a new asbestos-free expanded graphite sheet with excellent mechanical strength. The goal is to develop
【0006】[0006]
【課題を解決するための手段】この課題は50倍以上に
膨張した膨張黒鉛を0.02〜0.3g/cm3の嵩密
度となるように圧縮し、これを粉砕後、アラミドパルプ
繊維をフィブリル化して比表面積を3.0m2/g以上
とした補強用繊維と共に結合剤の存在下に水に懸濁させ
て抄紙用スラリーを製造し、このスラリーを湿式抄紙し
てシート化することによって解決される。[Means for solving the problem] This problem involves compressing expanded graphite that has expanded more than 50 times to a bulk density of 0.02 to 0.3 g/cm3, crushing it, and then fibrillating it with aramid pulp fibers. This problem was solved by producing a slurry for papermaking by suspending it in water in the presence of a binder together with reinforcing fibers that have a specific surface area of 3.0 m2/g or more, and wet-processing this slurry to form a sheet. Ru.
【0007】[0007]
【発明の作用並びに構成】本発明に於いては膨張黒鉛を
先ず所定の嵩密度に圧縮する。従来の50倍以上に膨張
した膨張黒鉛はこれを粉砕してもそのままでは水に均一
に懸濁してスラリー化できず、水の表面に浮くため抄紙
できない。またアセトンの如き親水性溶媒を少量用いる
方法も知られているが、この方法でも黒鉛粒子が水に浮
く傾向があり、決して望ましい方法ではない。従ってこ
のままでは抄紙しても均一なシートを得ることができず
、またたとえできたとしても機械的強度は極めて小さく
到底実用に供し得ない。このため本発明に於いては先ず
この膨張黒鉛粒子を0.02〜0.3g/cm3、好ま
しくは0.05〜0.15g/cm3の嵩密度となるよ
うに圧縮する。嵩密度が0.02g/cm3より低いと
膨張黒鉛粒子の空洞中の膨張ガスが抜け難く、水中で撹
拌を行い粉砕しても原料が浮いた状態のままである。
また嵩密度が0.3g/cm3より大きいと水中での粉
砕が難しくなると共に粉砕された原料が粒状となり膨張
黒鉛の特性が失われる。上記の嵩密度の原料を粉砕する
と膨張黒鉛の特性を失うことなく、水に懸濁され、アラ
ミドパルプ繊維に定着されて理想的な抄紙原料となる。In the present invention, expanded graphite is first compressed to a predetermined bulk density. Expanded graphite, which has expanded more than 50 times as much as conventional graphite, cannot be homogeneously suspended in water and made into a slurry even if it is pulverized, and it floats on the surface of the water, making it impossible to make paper. A method using a small amount of a hydrophilic solvent such as acetone is also known, but even with this method, the graphite particles tend to float on water, so it is by no means a desirable method. Therefore, even if paper is made in this state, it is not possible to obtain a uniform sheet, and even if it were possible, the mechanical strength is extremely low and it cannot be put to practical use at all. Therefore, in the present invention, the expanded graphite particles are first compressed to a bulk density of 0.02 to 0.3 g/cm3, preferably 0.05 to 0.15 g/cm3. When the bulk density is lower than 0.02 g/cm3, it is difficult for the expanded gas in the cavities of the expanded graphite particles to escape, and the raw material remains in a floating state even if it is stirred and pulverized in water. Furthermore, if the bulk density is greater than 0.3 g/cm3, it becomes difficult to crush in water, and the crushed raw material becomes granular and loses the properties of expanded graphite. When a raw material with the above-mentioned bulk density is pulverized, it is suspended in water and fixed to aramid pulp fibers without losing the properties of expanded graphite, making it an ideal raw material for papermaking.
【0008】本発明に於いて50倍以上に膨張した膨張
黒鉛を圧縮する手段は所定の嵩密度とできる手段であれ
ば原則的にはどのような手段でも良いが、特に水平コン
ベヤーと傾斜コンベヤーの組み合わせにより連続的に締
めつける圧縮手段が好ましい。この際たとえば従来から
知られている特願昭53−71694号に示される金網
ケースを使用する方法では嵩密度を0.05〜0.1g
/cm3のように圧縮することはできるが量産化が難し
い。尚膨張黒鉛としては平均として50倍以上に膨張し
たものを使用する。従って50倍以上に膨張した黒鉛粒
子だけを使用してもよいし、50倍以下の膨張黒鉛と5
0倍以上の膨張黒鉛とを混合して全体として50倍以上
となるようにして使用してもよい。しかし乍ら平均して
50倍未満では目的物シートの可撓性やシール性が低下
する。[0008] In the present invention, the means for compressing the expanded graphite that has expanded more than 50 times may be any means in principle as long as it can achieve a predetermined bulk density, but in particular horizontal conveyors and inclined conveyors are suitable. Compression means that are continuously tightened by a combination are preferred. In this case, for example, in the conventionally known method of using a wire mesh case shown in Japanese Patent Application No. 53-71694, the bulk density is 0.05 to 0.1 g.
/cm3, but mass production is difficult. As the expanded graphite, one used is one that has expanded 50 times or more on average. Therefore, only graphite particles expanded 50 times or more may be used, or expanded graphite particles 50 times or less and 50 times expanded graphite particles may be used.
It may be used by mixing it with 0 times or more expanded graphite so that the total amount becomes 50 times or more. However, if it is less than 50 times on average, the flexibility and sealing properties of the target sheet will deteriorate.
【0009】本発明に於いては圧縮した黒鉛は次いで粉
砕される。粉砕は湿式及び乾式いずれも採用することが
できる。湿式法の場合は圧縮黒鉛を予め水と混合した状
態で粉砕し、得られた粉砕物は水と分離することなく、
そのまま次のスラリー調製に使用する。粉砕手段は通常
ミキサータイプの粉砕機が好ましく使用されるが、抄紙
分野で使用される叩解機を使用しても良い。粉砕物の大
きさは通常50メッシュ以下、好ましくは60〜100
メッシュ程度である。乾式粉砕の場合は水の非存在下に
圧縮黒鉛を上記湿式粉砕の場合と同様の大きさとなるよ
うに粉砕する。粉砕機としては剪断力による粉砕機が望
ましく、たとえば高速ミキサーが例示できる。乾式粉砕
された粉砕物はこれを予め水と混合してからスラリー調
製に使用しても良く、また粉砕物を直接スラリー調製に
使用しても良い。In the present invention, the compressed graphite is then crushed. Both wet and dry crushing methods can be used. In the case of the wet method, compressed graphite is mixed with water beforehand and ground, and the resulting ground material does not separate from the water.
Use it as is for the next slurry preparation. As the crushing means, a mixer type crusher is usually preferably used, but a beating machine used in the paper making field may also be used. The size of the crushed material is usually 50 mesh or less, preferably 60 to 100 mesh.
It is about the size of a mesh. In the case of dry pulverization, compressed graphite is pulverized in the absence of water to the same size as in the case of wet pulverization. As the pulverizer, a pulverizer using shear force is preferable, such as a high-speed mixer. The dry pulverized product may be mixed with water in advance and then used for slurry preparation, or the pulverized product may be used directly for slurry preparation.
【0010】本発明に於いて使用される補強用繊維は水
中で膨張黒鉛粒子を定着させ、抄紙に必要な濃度に希釈
しても分離せずに均一に分散せしめる作用を有する。こ
れが高強度膨張黒鉛シートを得る重要なポイントになる
。この条件を満たすために補強用繊維は次の特性を備え
ている必要がある。
(1)補強用繊維は水中でイオン的に中性又は陽性であ
ること。膨張黒鉛粒子は水中でアニオン性を示すので、
セルロース繊維のように同じイオンを持った繊維を叩解
してフィブリル化を進めても完全に定着させることはで
きない。
(2)繊維を叩解してフィブリル化を進めて、繊維の比
表面積を3.0m2/g以上にすること。膨張黒鉛粒子
の比表面積が大きいのでこれを定着させる繊維もまたフ
ィブリル化を行い、比表面積を3.0m2/g以上にし
て、物理的にも吸着し易くする必要がある。このためモ
ノフィラメントに近い無機繊維や金属繊維では補強剤の
効果を示すことはできない。以上の条件に該当する補強
用繊維は耐熱性優れた、パラ系、メタ系のアラミド繊維
をパルプ化したものが最も有効である。The reinforcing fiber used in the present invention has the function of fixing expanded graphite particles in water and uniformly dispersing them without separating even when diluted to a concentration required for paper making. This is an important point in obtaining a high-strength expanded graphite sheet. In order to meet this condition, reinforcing fibers must have the following properties. (1) The reinforcing fibers must be ionically neutral or positive in water. Expanded graphite particles exhibit anionic properties in water, so
Even if fibers with the same ions, such as cellulose fibers, are beaten and fibrillated, they cannot be completely fixed. (2) Beating the fibers to promote fibrillation so that the specific surface area of the fibers is 3.0 m2/g or more. Since the expanded graphite particles have a large specific surface area, the fibers to which they are fixed must also be fibrillated to have a specific surface area of 3.0 m2/g or more to facilitate physical adsorption. For this reason, inorganic fibers and metal fibers similar to monofilaments cannot exhibit the effect of reinforcing agents. The most effective reinforcing fibers that meet the above conditions are those made by pulping para- and meta-aramid fibers that have excellent heat resistance.
【0011】アラミド繊維自体は知られたものであり、
本発明に於いても従来から知られた各種のアラミド繊維
が使用できる。この従来のアラミド繊維を所定の比表面
積となるようにフィブリル化して使用する。この際のフ
ィブリル化手段は特に限定されず、通常の手段が採用さ
れる。比表面積が3.0m2/g以上、好ましくは5.
0〜8.0m2/gである必要があり、3.0m2/g
未満では充分に黒鉛粒子を定着できず、望ましくない。
このアラミド繊維のスラリー中での使用量は3〜25重
量部、好ましくは5〜15重量部程度である。[0011] Aramid fiber itself is known;
In the present invention, various conventionally known aramid fibers can be used. This conventional aramid fiber is used after being fibrillated to have a predetermined specific surface area. The fibrillation means at this time is not particularly limited, and ordinary means may be employed. The specific surface area is 3.0 m2/g or more, preferably 5.
Must be 0-8.0m2/g, 3.0m2/g
If it is less than that, graphite particles cannot be sufficiently fixed, which is not desirable. The amount of aramid fiber used in the slurry is about 3 to 25 parts by weight, preferably about 5 to 15 parts by weight.
【0012】本発明に於いては目的物シートの機械的強
度を向上せしめるために結合剤を使用する。結合剤は水
溶性、エマルジョン型或いは粉末の形でも使用できるが
、特にエマルジョン型は微粒子でしかも水中で分散され
易く、徐々に定着されるので特に好ましい。これらの結
合剤としてNR、NBR、SBR、CRおよびアクリル
ゴムのラテックスを強度や耐熱性、耐油性等の特性に合
った用途に使用できる。更に耐熱性を必要とする場合は
フェノール樹脂とNBRラテックスの併用を始め、シリ
コーンゴムおよびフッ素ゴムのエマルジョン等を使用す
ることもできる。In the present invention, a binder is used to improve the mechanical strength of the object sheet. The binder can be used in a water-soluble, emulsion or powder form, but an emulsion type is particularly preferred since it is fine particles and easily dispersed in water, and is gradually fixed. As these binders, latexes of NR, NBR, SBR, CR, and acrylic rubber can be used depending on the properties such as strength, heat resistance, and oil resistance. If further heat resistance is required, phenol resin and NBR latex may be used in combination, and emulsions of silicone rubber and fluororubber may also be used.
【0013】本発明に於いては上記各材料を水に懸濁せ
しめて抄紙用スラリーとするが、この際の各材料の配合
割合は、
膨張黒鉛粒子:60〜95重量部
アラミドパルプ:3〜25重量部
結合剤:1〜20重量部
の組成で構成され、引張り強度が1.0kg/mm2以
上の高強度のシートで耐熱性を充分具備するためには、
膨張黒鉛粒子:70〜85重量部
アラミドパルプ:10〜20重量部
結合剤:5〜10重量部
の配合が良い。尚これらの原料液はパルプを核に膨張黒
鉛粒子が定着されているので原料液を1〜2%の濃度に
希釈しても分離することなく均一に分散されていて、水
に浮くことがないので抄紙装置を用いて高強度のシート
を得ることができる。[0013] In the present invention, each of the above-mentioned materials is suspended in water to form a slurry for paper making, and the mixing ratio of each material at this time is as follows: Expanded graphite particles: 60-95 parts by weight Aramid pulp: 3-95 parts by weight 25 parts by weight Binder: In order to have a high strength sheet with a tensile strength of 1.0 kg/mm2 or more and sufficient heat resistance, it is composed of 1 to 20 parts by weight.
Expanded graphite particles: 70 to 85 parts by weight Aramid pulp: 10 to 20 parts by weight Binder: 5 to 10 parts by weight. In addition, these raw material liquids have expanded graphite particles fixed to the pulp core, so even if the raw material liquid is diluted to a concentration of 1 to 2%, it will not separate and be uniformly dispersed, and will not float on water. Therefore, high-strength sheets can be obtained using papermaking equipment.
【0014】抄紙用スラリーを抄紙するに際しては通常
湿式抄紙法が採用され、湿式抄紙法自体の条件や装置は
従来のものが夫々そのまま適宜に採用される。かくして
得られる本発明の目的とするシートは膨張黒鉛よりなる
にもかかわらず、極めて機械的強度が大きく、また耐熱
性も優れ、その他可撓性を具備し、極めて優れたシール
性を有するため、一般産業用や内燃機関の各種接合面を
シールするためのガスケットとして極めて好適である。
尚本発明に於いて比表面積は次の方法で測定したもので
ある。本発明に於いて比表面積はベット(BET)法に
てN2(30%)とHe(70%)との混合ガスを用い
て測定したものである。[0014] When making paper from a papermaking slurry, a wet papermaking method is usually adopted, and the conventional conditions and equipment for the wet papermaking method itself can be used as appropriate. Although the sheet thus obtained is made of expanded graphite, it has extremely high mechanical strength, excellent heat resistance, flexibility, and extremely excellent sealing properties. It is extremely suitable as a gasket for general industrial use and for sealing various joint surfaces of internal combustion engines. In the present invention, the specific surface area is measured by the following method. In the present invention, the specific surface area is measured by the BET method using a mixed gas of N2 (30%) and He (70%).
【0015】[0015]
【実施例】以下実施例に基づいて本発明を更に具体的に
説明するが、本発明はこれに限定されるものではない。
尚特に明示しない限り単位は全て重量部である。EXAMPLES The present invention will be explained in more detail below based on Examples, but the present invention is not limited thereto. All units are parts by weight unless otherwise specified.
【実施例1】ミキサーに水200部とアラミド繊維パル
プ(アクゾ社製トワロンパルプ1096)を10部投入
し、約5分間撹拌してパルプを叩解し、配合チエストへ
水3000部を一緒に落とす(この時のパルプの比表面
積は7.5m2/gである)。一方150倍に膨張した
黒鉛粒子85部を嵩密度が0.08g/cm3になるよ
うに圧縮してスポンジ状とした。この原料をミキサーに
水2000部と共に約10分間撹拌し粉砕して配合チエ
ストへ落とし、アラミドパルプと混合した。1〜2分撹
拌するだけでアラミドパルプを核に膨張黒鉛の粒子が凝
集し、均一な分散液が得られた。更に結合剤としてNB
Rラテックス(日本ゼオン(株)製ニッポール1571
▲C▼)を固形分換等で5部を加え3〜4分間撹拌して
定着した。この場合アラミドパルプの配合量が少ないの
で、NBRラテックスは撹拌のみで定着することができ
た。またNBRの架橋助剤の亜鉛華を少量加えた。この
原料を抄き網を設けたタンクに入れ均一に分散させた後
に水切りを行いシート化した。更にサクションポンプで
搾水し、フェルトに挟みプレスで圧縮して脱水を行った
。このシートを120℃のオーブンに入れ乾燥を行い、
カレンダーロールを通してシートの密度を1.3g/c
m3に調整した。最後に150℃で20分間架橋を行っ
た。[Example 1] Add 200 parts of water and 10 parts of aramid fiber pulp (Twaron Pulp 1096 manufactured by Akzo) to a mixer, stir for about 5 minutes to beat the pulp, and drop 3000 parts of water together into the blended cheese ( The specific surface area of the pulp at this time is 7.5 m2/g). On the other hand, 85 parts of graphite particles expanded 150 times were compressed into a sponge shape to have a bulk density of 0.08 g/cm3. This raw material was mixed with 2000 parts of water in a mixer for about 10 minutes, pulverized, and dropped into a blended cheese, where it was mixed with aramid pulp. After stirring for just 1 to 2 minutes, the expanded graphite particles agglomerated around the aramid pulp, and a uniform dispersion was obtained. Furthermore, NB as a binder
R latex (Nippol 1571 manufactured by Nippon Zeon Co., Ltd.)
5 parts of ▲C▼) were added by changing the solid content, and the mixture was stirred for 3 to 4 minutes to be fixed. In this case, since the amount of aramid pulp blended was small, the NBR latex could be fixed only by stirring. Also, a small amount of zinc white, which is a crosslinking agent for NBR, was added. This raw material was placed in a tank equipped with a paper mesh, uniformly dispersed, and then drained to form a sheet. Furthermore, water was squeezed out using a suction pump, and the material was sandwiched between felts and compressed using a press to remove water. Place this sheet in an oven at 120°C to dry it.
The density of the sheet is 1.3g/c through a calender roll.
Adjusted to m3. Finally, crosslinking was performed at 150°C for 20 minutes.
【0016】[0016]
【実施例2】アラミドパルプ15部、膨張黒鉛75部、
NBRラテックス固形換算10部を用いた以外は実施例
1と同じ方法でシート化した。但しパルプと結合剤の使
用量が増えているので、ラテックスの定着が良くない。
カチオン性の凝集剤、たとえばサンフロックCH799
P(三洋化成(株)製)0.1部を溶かした水溶液を添
加して定着した。[Example 2] 15 parts of aramid pulp, 75 parts of expanded graphite,
A sheet was formed in the same manner as in Example 1 except that 10 parts of NBR latex solid was used. However, since the amount of pulp and binder used has increased, the fixation of latex is not good. Cationic flocculants such as Sunfloc CH799
An aqueous solution containing 0.1 part of P (manufactured by Sanyo Chemical Co., Ltd.) was added for fixation.
【0017】[0017]
【実施例3〜8】実施例1及び2に於いて膨張黒鉛、ア
ラミドパルプ及びNBRラテックスの配合割合を表1の
ように変化させ、その他は同様に処理してシートを製造
した。Examples 3 to 8 Sheets were produced in the same manner as in Examples 1 and 2, except that the blending ratios of expanded graphite, aramid pulp, and NBR latex were changed as shown in Table 1.
【表1】
実施例1と実施例2で得たシートの可撓性膨張黒鉛シー
トの特性をJISR3453に従い測定した。測定結果
を表2にJISR3453の1種、2種及び3種の規格
値と対比した。[Table 1] The properties of the flexible expanded graphite sheets obtained in Example 1 and Example 2 were measured according to JISR3453. The measurement results are shown in Table 2 and compared with the standard values of JISR3453 Type 1, Type 2, and Type 3.
【表2】
表2から明らかなように実施例1〜2の各シートの特性
はJISR3453の規格値をほぼ満足している。[Table 2] As is clear from Table 2, the characteristics of each sheet of Examples 1 and 2 substantially satisfy the standard values of JISR3453.
【0018】上記実施例1〜8で得た各シートについて
(即ち補強剤及び結合剤の添加量を変化させた時の各シ
ートについて)その変化量とシートの引っ張り強度との
関係及び同じくその変化量と応力緩和率との関係を調査
した。この結果を第1図(引っ張り強度)及び第2図(
応力の緩和率)に示す。但し第1及び2図に於いて、点
線はNBR配合10%の場合を、実線は5%の場合を示
す。第1〜2図から明らかな通り補強材及び結合剤の添
加量が変わると目的物シートの引っ張り強度や応力緩和
率が変化する。即ちこれら添加剤の配合割合が多くなる
と引っ張り強度は大きくなるが、耐熱性の目安の一つで
ある応力緩和率は逆に低下する。従って補強材や結合剤
の添加量を目的物シートの用途に合わせて適宜に選択す
ることにより所望のシートとすることができる。For each sheet obtained in Examples 1 to 8 above (that is, for each sheet when the amount of reinforcing agent and binder added was changed), the relationship between the amount of change and the tensile strength of the sheet, and the same change. The relationship between the amount and stress relaxation rate was investigated. The results are shown in Figure 1 (tensile strength) and Figure 2 (
(stress relaxation rate). However, in FIGS. 1 and 2, the dotted line indicates the case where the NBR content is 10%, and the solid line indicates the case where the NBR content is 5%. As is clear from FIGS. 1 and 2, when the amounts of reinforcing material and binder added change, the tensile strength and stress relaxation rate of the target sheet change. That is, as the proportion of these additives increases, the tensile strength increases, but the stress relaxation rate, which is one of the indicators of heat resistance, decreases. Therefore, a desired sheet can be obtained by appropriately selecting the amount of reinforcing material and binder added depending on the intended use of the sheet.
【0019】[0019]
【発明の効果】本発明のシートは可撓性膨張黒鉛シート
に比較すると機械強度や柔軟性が大巾に向上し、実際の
使用場面に於ける取扱が容易となる。また耐水、耐油性
の特性も改善され、アスベストジョイントシートのJI
S規格もほぼ満足している。以上のような特徴をもった
本発明のシートは一般産業用のガスケットを始め、内燃
機関の周辺のガスケット類にアスベストジョイントシー
トと同様に使用できる。[Effects of the Invention] Compared to flexible expanded graphite sheets, the sheet of the present invention has greatly improved mechanical strength and flexibility, and is easier to handle in actual use. The water and oil resistance properties have also been improved, and asbestos joint sheet JI
The S standard is also almost satisfied. The sheet of the present invention having the above characteristics can be used in general industrial gaskets and gaskets around internal combustion engines in the same way as asbestos joint sheets.
【0020】[0020]
図1〜2はいずれも黒鉛シートの原料配合比と引張り強
度又は応力緩和率との関係を示すグラフである。1 and 2 are graphs showing the relationship between the raw material blending ratio of graphite sheets and the tensile strength or stress relaxation rate.
Claims (3)
張黒鉛を0.02〜0.3g/cm3の嵩密度になるよ
うに圧縮し、これを粉砕した黒鉛粒子、(B)アラミド
パルプ繊維をフィブリル化してその比表面積を3.0m
2/g以上となした補強用繊維、(C)結合剤、及び (D)水とを懸濁せしめて抄紙用スラリーとなし、この
スラリーを湿式抄紙してシート化することを特徴とする
膨張黒鉛シートの製造法。Claim 1: (A) graphite particles obtained by compressing expanded graphite that has expanded more than 50 times on average to a bulk density of 0.02 to 0.3 g/cm3 and pulverizing it; (B) aramid pulp; Fibrillate the fibers and increase the specific surface area to 3.0m
2/g or more reinforcing fibers, (C) a binder, and (D) water are suspended to form a papermaking slurry, and this slurry is wet-processed to form a sheet. Method for manufacturing graphite sheets.
が、(A)60〜95重量部、(B)5〜25重量部、
及び(C)1〜15重量部である請求項1に記載の製造
法。2. The blending ratio of (A), (B) and (C) is (A) 60 to 95 parts by weight, (B) 5 to 25 parts by weight,
and (C) 1 to 15 parts by weight.
に記載の製造法。Claim 3: Claim 1 in which the compressed product of expanded graphite is wet-pulverized.
The manufacturing method described in.
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3085713A JP2931882B2 (en) | 1991-01-23 | 1991-01-23 | Manufacturing method of expanded graphite sheet |
EP92306679A EP0579879B1 (en) | 1991-01-23 | 1992-07-21 | Production method of expanded graphite sheet and expanded graphite sheet obtained thereby |
DE69205421T DE69205421T2 (en) | 1991-01-23 | 1992-07-21 | A process for producing an expanded graphite sheet and an expanded graphite sheet obtained by this process. |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3085713A JP2931882B2 (en) | 1991-01-23 | 1991-01-23 | Manufacturing method of expanded graphite sheet |
EP92306679A EP0579879B1 (en) | 1991-01-23 | 1992-07-21 | Production method of expanded graphite sheet and expanded graphite sheet obtained thereby |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH04240295A true JPH04240295A (en) | 1992-08-27 |
JP2931882B2 JP2931882B2 (en) | 1999-08-09 |
Family
ID=26132113
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3085713A Expired - Lifetime JP2931882B2 (en) | 1991-01-23 | 1991-01-23 | Manufacturing method of expanded graphite sheet |
Country Status (3)
Country | Link |
---|---|
EP (1) | EP0579879B1 (en) |
JP (1) | JP2931882B2 (en) |
DE (1) | DE69205421T2 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1999010598A1 (en) * | 1997-08-26 | 1999-03-04 | Toyo Tanso Kabushiki Kaisya | Expanded graphite sheet for electromagnetic wave shielding and process for producing the same |
JP2008274053A (en) * | 2007-04-26 | 2008-11-13 | Nippon Pillar Packing Co Ltd | Sheet gasket |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100731967B1 (en) * | 1999-07-22 | 2007-06-25 | 토요 탄소 가부시키가이샤 | Heating element |
US6451486B1 (en) | 2000-05-01 | 2002-09-17 | The Gillette Company | Battery cathode including a mixture of manganese dioxide with carbon particles of expanded and non-expanded graphite |
US6921610B2 (en) | 2001-07-11 | 2005-07-26 | The Gillette Company | Battery |
JP2006521999A (en) * | 2003-03-31 | 2006-09-28 | ウー シン,ヤン | Method for producing expanded graphite product |
EP1518842A1 (en) * | 2003-09-23 | 2005-03-30 | Advanced Energy Technology Inc. | Reactive additive that promotes material flow for moulding compounds |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1992002354A1 (en) * | 1990-08-01 | 1992-02-20 | Mcallister Richard G | High modulus media of reinforcing materials and thermoplastic fibrets |
-
1991
- 1991-01-23 JP JP3085713A patent/JP2931882B2/en not_active Expired - Lifetime
-
1992
- 1992-07-21 DE DE69205421T patent/DE69205421T2/en not_active Expired - Fee Related
- 1992-07-21 EP EP92306679A patent/EP0579879B1/en not_active Expired - Lifetime
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1999010598A1 (en) * | 1997-08-26 | 1999-03-04 | Toyo Tanso Kabushiki Kaisya | Expanded graphite sheet for electromagnetic wave shielding and process for producing the same |
JP2008274053A (en) * | 2007-04-26 | 2008-11-13 | Nippon Pillar Packing Co Ltd | Sheet gasket |
Also Published As
Publication number | Publication date |
---|---|
JP2931882B2 (en) | 1999-08-09 |
DE69205421D1 (en) | 1995-11-16 |
EP0579879B1 (en) | 1995-10-11 |
EP0579879A1 (en) | 1994-01-26 |
DE69205421T2 (en) | 1996-06-05 |
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