Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPH0316436B2 - - Google Patents
[go: Go Back, main page]

JPH0316436B2 - - Google Patents

Info

Publication number
JPH0316436B2
JPH0316436B2 JP60176998A JP17699885A JPH0316436B2 JP H0316436 B2 JPH0316436 B2 JP H0316436B2 JP 60176998 A JP60176998 A JP 60176998A JP 17699885 A JP17699885 A JP 17699885A JP H0316436 B2 JPH0316436 B2 JP H0316436B2
Authority
JP
Japan
Prior art keywords
weight
parts
inorganic
filler
added
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
JP60176998A
Other languages
Japanese (ja)
Other versions
JPS6241399A (en
Inventor
Setsuo Toyoshima
Shinichiro Takaguchi
Shigeru Arai
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.)
Honshu Paper Co Ltd
Original Assignee
Honshu Paper 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 Honshu Paper Co Ltd filed Critical Honshu Paper Co Ltd
Priority to JP17699885A priority Critical patent/JPS6241399A/en
Publication of JPS6241399A publication Critical patent/JPS6241399A/en
Publication of JPH0316436B2 publication Critical patent/JPH0316436B2/ja
Granted legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H05ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
    • H05KPRINTED CIRCUITS; CASINGS OR CONSTRUCTIONAL DETAILS OF ELECTRIC APPARATUS; MANUFACTURE OF ASSEMBLAGES OF ELECTRICAL COMPONENTS
    • H05K1/00Printed circuits
    • H05K1/02Details
    • H05K1/03Use of materials for the substrate
    • H05K1/0313Organic insulating material
    • H05K1/0353Organic insulating material consisting of two or more materials, e.g. two or more polymers, polymer + filler, + reinforcement
    • H05K1/0366Organic insulating material consisting of two or more materials, e.g. two or more polymers, polymer + filler, + reinforcement reinforced, e.g. by fibres, fabrics
    • HELECTRICITY
    • H05ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
    • H05KPRINTED CIRCUITS; CASINGS OR CONSTRUCTIONAL DETAILS OF ELECTRIC APPARATUS; MANUFACTURE OF ASSEMBLAGES OF ELECTRICAL COMPONENTS
    • H05K1/00Printed circuits
    • H05K1/02Details
    • H05K1/03Use of materials for the substrate
    • H05K1/0313Organic insulating material
    • H05K1/0353Organic insulating material consisting of two or more materials, e.g. two or more polymers, polymer + filler, + reinforcement
    • H05K1/0373Organic insulating material consisting of two or more materials, e.g. two or more polymers, polymer + filler, + reinforcement containing additives, e.g. fillers

Landscapes

  • Paper (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

〔産業上の利用分野〕 本発明は、抄造法を利用して密度の高い無機質
繊維シートを製造する方法に関する。 〔従来の技術〕 抄造法を利用して得られる例えばガラス繊維等
による無機質繊維シートは、一般的なバインダー
の添加量、すなわち、20%以下のバインダーの添
加量の場合には、通常0.22g/cm3以下の空〓に満
ちた低密度シートとして製造されているのが普通
であり、該シートにおける高気孔性を利用するよ
うな用途には適するものの、高密度が要求される
分野での用途、例えば、コンポジツトタイプのプ
リント回路基板、断熱用発泡樹脂ボードに対する
面材等の用途に供せられる無機質繊維シートとし
ては、十分に満足され得ないのが実情である。 例えば、コンポジツトタイプのプリント回路基
板に対して、従来の抄造法による無機質繊維シー
トを利用する場合には、該シートが嵩高・低密度
であるため、樹脂含浸後のプリプレグ積層プレス
工程でのプレス機への仕込み枚数を少なくしなけ
ればならなく、しかも、成形によつて得られた積
層板は、必然的に樹脂含浸比率の高いものになつ
ているため、反りやねじれが発生し易く、加熱下
での寸法安定性が不十分である等の欠点を有す
る。 このため、ガラス繊維シート等における無機質
繊維同士の空〓を無機質充填剤等で充填し、樹脂
含浸率の低い高密度シートを得る方法として、例
えば特開昭54−50583号公報には、既成のガラス
繊維製不織布に対して無機質充填剤を含浸させる
方法が提案されている。 〔発明が解決しようとする課題〕 しかるに、前段工程で得られた既成の無機質繊
維シートに対して、無機質充填剤によるスラリー
を含浸あるいは塗工することからなる後段工程を
付す方法は、その製造工程が2工程になるため、
設備の点およびエネルギーの消費の点等において
不経済になるだけでなく、無機質充填剤によるス
ラリーの含浸あるいは塗工工程でのスラリー中の
無機質充填剤の沈降を防止させるために、スラリ
ー中に増粘剤を添加しなければならなく、得られ
る無機質繊維シートの用途によつては、忌み嫌わ
れる添加剤の使用が己むを得なくなる等の欠点を
有する。 また、抄造法によつて無機質繊維シート中に填
料が内填されているシートを得る方法、すなわ
ち、粉末状の填料を含む無機質繊維スラリーを抄
造することによつて、シート中に填料が内填され
ている無機質繊維シートを得る方法においては、
填料を歩留まり良く保持させることが難しく、高
密度の無機質繊維シートが得られない。 すなわち、パルプ原料から填料含有紙を得る際
に通常利用されているところの硫酸アルミニウム
等の無機質凝集剤やポリアクリルアミド等のイオ
ン性高分子凝集剤を、無機質繊維によるスラリー
中に添加し、これを抄造しても、抄造工程中に填
料がワイヤーから抜け落ちてしまうために、歩留
まり良く填料を無機質繊維に定着させることが難
しく、またさらに、無機質繊維スラリー中で填料
の定着が悪く、填料が沈降してしまい、これが、
得られる無機質繊維シート中での填料の分布を不
均一にさせ、シートの品質を悪化させる等の弊害
が避けられない。 これに対して本発明は、繊維成分として、細径
無機質繊維が配合されているものを利用し、ま
た、填料の定着剤として、カチオン系高分子物質
とアニオン系高分子物質、あるいはカチオン系高
分子物質とノニオン系高分子物質との組み合わせ
からなる高分子物質を併用することにより、スラ
リー中の填料を細径無機質繊維に効率良く定着さ
せ、高密度の無機質繊維シートを抄造法によつて
得る方法を提供する。 〔課題を解決するための手段〕 本発明の無機質繊維シートの製造方法は、平均
繊維径が3μ以下の細径無機質繊維が5重量%以
上の割合で配合されている無機質繊維100重量部
に対して、填料50〜300重量部と、カチオン系高
分子物質とアニオン系高分子物質、あるいは、カ
チオン系高分子物質とノニオン系高分子物質との
組み合わせによる定着剤とが添加されている抄造
用の水性スラリーを調製する工程と、得られた抄
造用の水性スラリーを、脱水、抄造する工程とか
らなるものである。 前記構成からなる本発明の無機質繊維シートの
製造方法において、水性スラリーに利用される無
機質繊維成分には、通常の無機質繊維シートを得
る際に利用されている各種の無機質繊維と同一の
繊維、例えば、ガラス繊維、セラミツク繊維、ロ
ツクウール、アルミナ繊維、炭素繊維等が利用さ
れる。 無機質繊維中の5重量%以上の割合で配合され
る細径無機質繊維は、該繊維による十分な表面積
によつて填料の定着歩留まりを高める作用を果た
させるものであつて、細径無機質繊維の平均繊維
径が3μを超えるようになると、該細径無機質繊
維による十分な表面積が得られなくなるため、填
料の定着歩留まりが低下する。 このため、無機質繊維中の5重量%以上を占め
る細径無機質繊維は、平均繊維径が3μ以下、好
ましくは、1μ以下のものが利用される。 また、無機質繊維の全体に対して前述の細径無
機質繊維が5重量%未満になると、細径無機質繊
維による填料の定着歩留まりの向上作用が十分で
なくなり、高密度の無機質繊維シートが得られな
くなる。 水性スラリー中に添加される填料には、紙やプ
ラスチツク成形品等の填料として利用されている
通常の填料、例えば、酸化アルミニウム、水酸化
アルミニウム、酸化マグネシウム、水酸化マグネ
シウム、カオリン、クレー、タルク、酸化チタ
ン、けい石、ワラストナイト、チタン酸カリウ
ム、ガラス粉末等の無機質粉末や、尿素・ホルマ
リン樹脂粉末、エポキシ樹脂粉末、フエノール樹
脂粉末等の有機質粉末、さらには、アルミニウム
粉等の金属粉末等が使用される。 水性スラリー中の填料が無機質繊維100重量部
に対して50重量部未満になると、密度の十分に高
い無機質繊維シートが得られ難くなり、また、
300重量部を超えると、得られる無機質繊維シー
トにおける繊維成分が減少することのために、強
度の十分な無機質繊維シートが得られなくなる。 本発明の無機質繊維シートの製造方法において
は、水性スラリー中の填料を細径無機質繊維に効
果的に定着させる定着剤として、カチオン系高分
子物質とアニオン系高分子物質、あるいは、カチ
オン系高分子物質とノニオン系高分子物質との組
み合わせによる複数の高分子物質が併用される。 なお、定着剤として利用される高分子物質の代
表的なものは、以下の通りである。 カチオン系高分子物質 カチオン変性ポリアクリルアミド、カチオン変
性澱粉、ポリアミド・ポリアミン・エピクロルヒ
ドリン樹脂、ポリエチレンイミン等、 アニオン系高分子物質 アニオン変性ポリアクリルアミド、澱粉および
その誘導体、ポリビニルアルコール、さらには、
例えば、アクリル酸、メタクリル酸、マレイン酸
またはその無水物、フマル酸、イタコン酸、ビニ
ルスルホン酸またはそれらの塩等からなるカルボ
キシル基やスルホン基等を有する各種のモノマー
によるホモポリマー、または、これらのモノマー
と他の共重合可能なモノマー、例えば、エチレ
ン、ブチレン、ジイソブチレン、デセン、ドデセ
ン、アクリロニトリル、アクリル酸メチル、アク
リル酸エチル、メタクリル酸メチル、メタクリル
酸エチル、スチレン、酢酸ビニル等とのコポリマ
ー等、 ノニオン系高分子物質 ノニオン変性ポリアクリルアミド、ヒドロキシ
エチルセルロース、グアーガム等、 無機質繊維による水性スラリー中への定着剤の
添加は、例えば、カチオン系高分子物質とアニオ
ン系高分子物質との組み合わせからなる定着剤の
場合には、カチオン系高分子物質を添加した後に
アニオン系高分子物質を添加することが、また、
カチオン系高分子物質とノニオン系高分子物質と
の組み合わせからなる定着剤の場合には、ノニオ
ン系高分子物質を添加した後にカチオン系高分子
物質を添加するのが、定着剤による定着作用の点
から好ましい結果が得られることが確認されてい
る。 カチオン系高分子物質とアニオン系高分子物質
との組み合わせからなる定着剤、あるいは、カチ
オン系高分子物質とノニオン系高分子物質との組
み合わせからなる定着剤は、水性スラリー中の無
機質繊維に対する0.1〜1重量%程度の添加量で、
十分な定着作用が発揮される。 本発明の無機質繊維シートの製造方法において
は、前述の通り、カチオン系高分子物質とアニオ
ン系高分子物質との組み合わせからなる定着剤、
あるいは、カチオン系高分子物質とノニオン系高
分子物質との組み合わせからなる定着剤が利用さ
れるが、特に、後者のカチオン系高分子物質とノ
ニオン系高分子物質との組み合わせによる定着剤
を利用する場合には、水力学的剪断力下において
も高い定着作用が奏されることが、動的濾水度試
験器(Dynamic Dranage Jar)を利用した填料
の定着率の測定試験、すなわち、無機質繊維と填
料と定着剤とを配合した水性スラリーを、動的濾
水度試験器の濾水ジヤー内に投入し、高速回転す
る攪拌羽根によつて幅広い水力学的剪断力を与え
た後、底部のワイヤーから抜け落ちた填料を濾紙
で受け、これを定量することからなる填料の定着
率の測定試験によつて、明らかになつている。 前述の填料の定着率の測定試験に利用した水性
スラリーの種類と、得られた填料の定着率とにつ
いて説明する。 水性スラリーの調製 平均繊維径が9μのガラス繊維50重量部と、平
均繊維径が0.7μの細径ガラス繊維50重量部とを利
用し、ガラス繊維濃度0.05重量%の分散液を得た
後、さらに、クレー粉末120重量部を添加し、続
いて、バインダー成分たる繊維状ポリビニルアル
コール10重量部と、第1表の所定欄に記載されて
いる定着剤とを順次添加し、高速回転する攪拌羽
根による攪拌処理を1分間行なうことによつて水
性スラリーを調製した。
[Industrial Application Field] The present invention relates to a method for producing a high-density inorganic fiber sheet using a papermaking method. [Prior Art] Inorganic fiber sheets made of, for example, glass fibers obtained using a paper-making method usually have a binder content of 0.22 g/min when the amount of binder added is 20% or less. It is usually manufactured as a low-density sheet filled with voids of cm 3 or less, and although it is suitable for applications that take advantage of the high porosity of the sheet, it is not suitable for applications in fields where high density is required. The reality is that, for example, inorganic fiber sheets that can be used as face materials for composite-type printed circuit boards and heat-insulating foam resin boards are not fully satisfactory. For example, when using an inorganic fiber sheet made by the conventional papermaking method for a composite type printed circuit board, the sheet is bulky and low density, so it is difficult to press in the prepreg lamination press process after resin impregnation. The number of sheets loaded into the machine must be reduced, and since the laminates obtained by molding inevitably have a high resin impregnation ratio, they are prone to warping and twisting, and are prone to warping and twisting when heated. It has disadvantages such as insufficient dimensional stability at the bottom. For this reason, as a method of filling the voids between inorganic fibers in a glass fiber sheet etc. with an inorganic filler etc. to obtain a high density sheet with a low resin impregnation rate, for example, Japanese Patent Application Laid-open No. 54-50583 describes a ready-made method. A method has been proposed in which glass fiber nonwoven fabric is impregnated with an inorganic filler. [Problems to be Solved by the Invention] However, a method in which a subsequent step of impregnating or coating a ready-made inorganic fiber sheet obtained in the first step with a slurry containing an inorganic filler is difficult to achieve in the manufacturing process. Since it is a two-step process,
Not only is it uneconomical in terms of equipment and energy consumption, but it is also necessary to add additives to the slurry in order to prevent the inorganic filler from impregnating the slurry or from settling in the slurry during the coating process. A sticky agent must be added, and depending on the use of the obtained inorganic fiber sheet, the use of a disliked additive may become unavoidable. In addition, there is a method for obtaining a sheet in which a filler is embedded in an inorganic fiber sheet by a paper-making method, that is, by forming an inorganic fiber slurry containing a powdered filler, the filler is embedded in the sheet. In the method of obtaining an inorganic fiber sheet,
It is difficult to retain the filler at a good yield, and a high-density inorganic fiber sheet cannot be obtained. That is, inorganic flocculants such as aluminum sulfate and ionic polymer flocculants such as polyacrylamide, which are commonly used when obtaining filler-containing paper from pulp raw materials, are added to a slurry of inorganic fibers. Even if the paper is made, it is difficult to fix the filler to the inorganic fibers with a good yield because the filler falls off the wire during the papermaking process.Furthermore, the fixation of the filler in the inorganic fiber slurry is poor and the filler settles. So this is
Unavoidable disadvantages include uneven distribution of the filler in the obtained inorganic fiber sheet and deterioration of the quality of the sheet. In contrast, the present invention utilizes a mixture of small-diameter inorganic fibers as a fiber component, and uses a cationic polymer substance, an anionic polymer substance, or a cationic polymer substance as a filler fixing agent. By using a polymer material consisting of a combination of a molecular material and a nonionic polymer material, the filler in the slurry is efficiently fixed on the small-diameter inorganic fibers, and a high-density inorganic fiber sheet can be obtained by the papermaking method. provide a method. [Means for Solving the Problems] The method for producing an inorganic fiber sheet of the present invention is based on 100 parts by weight of inorganic fibers containing 5% by weight or more of small-diameter inorganic fibers with an average fiber diameter of 3 μ or less. For papermaking, 50 to 300 parts by weight of filler and a fixing agent made of a combination of a cationic polymeric substance and an anionic polymeric substance, or a combination of a cationic polymeric substance and a nonionic polymeric substance are added. This process consists of a step of preparing an aqueous slurry, and a step of dewatering and papermaking the obtained aqueous slurry for papermaking. In the method for producing an inorganic fiber sheet of the present invention having the above-mentioned structure, the inorganic fiber component used in the aqueous slurry includes the same fibers as the various inorganic fibers used to obtain a normal inorganic fiber sheet, for example. , glass fiber, ceramic fiber, rock wool, alumina fiber, carbon fiber, etc. are used. The fine inorganic fibers blended in an amount of 5% by weight or more in the inorganic fibers have a sufficient surface area to increase the fixation yield of the filler. When the average fiber diameter exceeds 3 μ, a sufficient surface area cannot be obtained by the small-diameter inorganic fibers, and the fixing yield of the filler decreases. For this reason, the small-diameter inorganic fibers that account for 5% by weight or more of the inorganic fibers have an average fiber diameter of 3 μ or less, preferably 1 μ or less. Furthermore, if the above-mentioned small-diameter inorganic fibers are less than 5% by weight based on the total inorganic fibers, the effect of improving the fixation yield of filler by the small-diameter inorganic fibers will not be sufficient, and a high-density inorganic fiber sheet will not be obtained. . The fillers added to the aqueous slurry include common fillers used as fillers for paper and plastic molded products, such as aluminum oxide, aluminum hydroxide, magnesium oxide, magnesium hydroxide, kaolin, clay, talc, Inorganic powders such as titanium oxide, silica, wollastonite, potassium titanate, glass powder, organic powders such as urea/formalin resin powder, epoxy resin powder, phenol resin powder, and metal powders such as aluminum powder, etc. is used. If the amount of filler in the aqueous slurry is less than 50 parts by weight per 100 parts by weight of inorganic fibers, it will be difficult to obtain an inorganic fiber sheet with a sufficiently high density;
If it exceeds 300 parts by weight, the fiber component in the resulting inorganic fiber sheet will decrease, making it impossible to obtain an inorganic fiber sheet with sufficient strength. In the method for producing an inorganic fiber sheet of the present invention, a cationic polymer substance and an anionic polymer substance or a cationic polymer substance are used as fixing agents to effectively fix the filler in the aqueous slurry to the small diameter inorganic fibers. A plurality of polymeric substances are used in combination with a substance and a nonionic polymeric substance. Note that typical polymeric substances used as fixing agents are as follows. Cationic polymer substances such as cation-modified polyacrylamide, cation-modified starch, polyamide/polyamine/epichlorohydrin resin, polyethyleneimine, etc., anionic polymer substances such as anion-modified polyacrylamide, starch and its derivatives, polyvinyl alcohol, and even
For example, homopolymers made of various monomers having carboxyl or sulfonic groups such as acrylic acid, methacrylic acid, maleic acid or its anhydride, fumaric acid, itaconic acid, vinyl sulfonic acid or their salts, or Copolymers of monomers with other copolymerizable monomers, such as ethylene, butylene, diisobutylene, decene, dodecene, acrylonitrile, methyl acrylate, ethyl acrylate, methyl methacrylate, ethyl methacrylate, styrene, vinyl acetate, etc. , nonionic polymeric substances Nonionic modified polyacrylamide, hydroxyethyl cellulose, guar gum, etc. Addition of a fixing agent to an aqueous slurry made of inorganic fibers is, for example, a fixing agent consisting of a combination of a cationic polymeric substance and an anionic polymeric substance. In the case of an agent, the anionic polymeric substance may be added after the cationic polymeric substance is added;
In the case of a fixing agent consisting of a combination of a cationic polymeric substance and a nonionic polymeric substance, the point of the fixing effect of the fixing agent is to add the cationic polymeric substance after adding the nonionic polymeric substance. It has been confirmed that favorable results can be obtained. A fixing agent consisting of a combination of a cationic polymeric substance and an anionic polymeric substance, or a fixing agent consisting of a combination of a cationic polymeric substance and a nonionic polymeric substance, has a ratio of 0.1 to With an addition amount of about 1% by weight,
Sufficient fixing effect is exhibited. As mentioned above, in the method for producing an inorganic fiber sheet of the present invention, a fixing agent consisting of a combination of a cationic polymeric substance and an anionic polymeric substance,
Alternatively, a fixing agent made of a combination of a cationic polymeric substance and a nonionic polymeric substance is used, and in particular, a fixing agent made of a combination of a cationic polymeric substance and a nonionic polymeric substance is used. In some cases, a test to measure the fixation rate of fillers using a Dynamic Drainage Jar shows that a high fixation effect is exhibited even under hydraulic shear force. An aqueous slurry containing a filler and a fixing agent is introduced into the drainage jar of a dynamic freeness tester, and after applying a wide range of hydraulic shear force using a stirring blade that rotates at high speed, This has been clarified by a test to measure the fixation rate of the filler, which consists of collecting the filler that has fallen out with a filter paper and quantifying it. The type of aqueous slurry used in the above-mentioned filler fixation rate measurement test and the obtained filler fixation rate will be explained. Preparation of aqueous slurry After obtaining a dispersion with a glass fiber concentration of 0.05% by weight using 50 parts by weight of glass fibers with an average fiber diameter of 9μ and 50 parts by weight of small diameter glass fibers with an average fiber diameter of 0.7μ, Furthermore, 120 parts by weight of clay powder was added, and then 10 parts by weight of fibrous polyvinyl alcohol as a binder component and the fixing agent listed in the specified column of Table 1 were sequentially added. An aqueous slurry was prepared by stirring for 1 minute.

【表】【table】

【表】 また、各水性スラリーの填料の定着率〔歩留ま
り(%)〕を、水性スラリーを得る際の攪拌速度
と共に第2表に示す。
Table 2 Table 2 also shows the filler fixation rate (yield (%)) of each aqueous slurry, along with the stirring speed at which the aqueous slurry was obtained.

【表】 さらに、前述の攪拌速度500rpmで攪拌して得
られた水性スラリーを常法に基づく手抄きに付
し、無機質繊維シートを得た。 得られた各無機質繊維シートの坪量と密度とを
第3表(その1)に示す。
[Table] Further, the aqueous slurry obtained by stirring at the above-mentioned stirring speed of 500 rpm was subjected to manual papermaking in a conventional manner to obtain an inorganic fiber sheet. The basis weight and density of each obtained inorganic fiber sheet are shown in Table 3 (Part 1).

【表】【table】

【表】 また、前述の攪拌速度1500rpmで攪拌(高剪断
力下)して得られた水性スラリーを常法に基づく
手抄きに付し、無機質繊維シートを得た。 得られた各無機質繊維シートの坪量と密度とを
第3表(その2)に示す。
[Table] In addition, the aqueous slurry obtained by stirring at the above-mentioned stirring speed of 1500 rpm (under high shear force) was subjected to manual papermaking in a conventional manner to obtain an inorganic fiber sheet. The basis weight and density of each obtained inorganic fiber sheet are shown in Table 3 (Part 2).

〔作用〕[Effect]

本発明の無機質繊維の製造方法においては、無
機質繊維成分として、平均繊維径が3μ以下の細
径無機質繊維が5重量%以上の割合で配合されて
いる無機質繊維を利用し、この無機質繊維100重
量部に対して、50〜300重量部の填料と、カチオ
ン系高分子物質とアニオン系高分子物質とによる
定着剤、あるいは、カチオン系高分子物質とノニ
オン系高分子物質とによる定着剤とが添加されて
いる抄造用の水性スラリーを、脱水、抄造するこ
とからなるもので、カチオン系高分子物質とアニ
オン系高分子物質との併用による定着剤の作用、
あるいは、カチオン系高分子物質とノニオン系高
分子物質との併用による定着剤の作用により、水
性スラリー中の細径無機質繊維に対して、填料を
効率良く定着させ得る。 したがつて、本発明方法においては、脱水、抄
造に付される水性スラリーにおける前述の作用に
よつて、従来の脱水、抄造法によつては得ること
のできなかつた高密度の無機質繊維シートが得ら
れる。 〔実施例〕 以下、本発明の無機質繊維シートの製造方法の
具体的な構成を実施例をもつて説明し、得られた
無機質繊維シートの物性等について、比較のため
に製造した無機質繊維シートの物性等と併せて説
明する。 実施例 1 平均繊維径0.7μ、繊維長10mm以下の細径ガラス
繊維10重量部を水中に分散させ、ガラス繊維濃度
0.05重量%の分散液を得た後、填料としての平均
粒径2μのクリー粉末64重量部を添加し、粗大粒
子塊がなくなるまで十分に攪拌した。 次いで、平均繊維径9μ、繊維長6mmのEガラ
ス繊維90重量部を添加し、さらに、バインダー成
分としての繊維状ポリビニルアルコール18重量部
を添加して攪拌した。 しかる後に、定着剤として、固形成分換算で
0.5重量部のノニオン系ポリアクリルアミドを添
加後、さらに、同じく、固形成分換算で0.5重量
部のカチオン系ポリアクリルアミドを添加し、填
料を十分に定着させ、得られた水性スラリーを常
法による手抄きに付し、本発明の目的製品である
無機質繊維シートを得た。 実施例 2 平均繊維径0.7μ、繊維長10mm以下の細径ガラス
繊維33重量部を水中に分散させ、ガラス繊維濃度
0.05重量%の分散液を得た後、填料としての水酸
化マグネシウム200重量部を添加し、粗大粒子塊
がなくなるまで十分に攪拌した。 次いで、平均繊維径9μ、繊維長6mmのEガラ
ス繊維67重量部を添加し、さらに、バインダー成
分としての繊維状ポリビニルアルコール18重量部
を添加して攪拌した。 しかる後に、定着剤として、固形成分換算で
0.5重量部のノニオン系ポリアクリルアミドを添
加後、さらに、同じく、固形成分換算で0.5重量
部のカチオン系ポリアクリルアミドを添加し、填
料を十分に定着させ、得られた水性スラリーを実
施例1と同一方法からなる手抄きに付し、本発明
の目的製品である無機質繊維シートを得た。 実施例 3 平均繊維径0.7μ、繊維長10mm以下の細径ガラス
繊維50重量部を水中に分散させ、ガラス繊維濃度
0.05重量%の分散液を得た後、填料としての酸化
アルミニウム80重量部を添加し、粗大粒子塊がな
くなるまで十分に攪拌した。 次いで、平均繊維径9μ、繊維長6mmのEガラ
ス繊維50重量部を添加し、さらに、バインダー成
分としての繊維状ポリビニルアルコール18重量部
を添加して攪拌した。 しかる後に、定着剤として、固形成分換算で
0.5重量部のノニオン系ポリアクリルアミドを添
加後、さらに、同じく、固形成分換算で0.5重量
部のカチオン系ポリアクリルアミドを添加し、填
料を十分に定着させ、得られた水性スラリーを実
施例1と同一の方法による手抄きに付し、本発明
の目的製品である無機質繊維シートを得た。 実施例 4 実施例1の手順において、填料として300重量
部のクレー粉末を利用し、また、定着剤として、
固形成分換算で0.5重量部のカチオン系ポリアク
リルアミドを添加後、さらに、同じく、固形成分
換算で0.5重量部のノニオン系ポリアクリルアミ
ドを添加する以外は、全て、実施例1と同一の手
順に付し、本発明の目的製品である無機質繊維シ
ートを得た。 実施例 5 細径ガラス繊維として、平均繊維径3μ、繊維
長15mm以下の細径ガラス繊維10重量部を利用する
以外は、全て実施例1と同一の手順に付し、本発
明の目的製品である無機質繊維シートを得た。 実施例 6 平均繊維径3μ、繊維長10mm以下のアルミナシ
リカ系細径セラミツク繊維10重量部を水中に分散
させ、セラミツク繊維の濃度0.05重量%の分散液
を得た後、平均粒径2μのクレー粉末64重量部を
添加し、粗大粒子塊がなくなるまで十分に攪拌し
た。 次いで、平均繊維径10μ、繊維長30mm以下のセ
ラミツク繊維90重量部を添加し、以後の手順は、
実施例1の対応する手順と同一に処方することに
より、本発明の目的製品である無機質繊維シート
を得た。 実施例 7 平均繊維径0.7μ、繊維長10mm以下の細径ガラス
繊維10重量部を水中に分散させ、ガラス繊維濃度
0.05重量%の分散液を得た後、填料として平均粒
径2μのクレー粉末64重量部を添加し、粗大粒子
塊がなくなるまで十分に攪拌し、次いで、平均繊
維径9μ、繊維長6mmのEガラス繊維90重量部を
添加した後、さらに、定着剤として、固形成分換
算で0.5重量部のノニオン系ポリアクリルアミド
と、同じく、固形成分換算で0.5重量部のカチオ
ン系ポリアクリルアミドとを添加し、填料を十分
に定着させることによつて水性スラリーを調整し
た。 得られた無機質繊維の水性スラリーを、円網抄
紙機を利用して抄造した。 なお、抄紙機中で、濃度15重量%のアクリル系
エマルジヨン(ダウ・ケミカル社、DOW2647)
を、ガラス繊維シートのガラス繊維成分に対して
固形分成分換算で11重量%の割合で、スプレー法
で塗布し、ヤンキードライヤーで乾燥することに
よつて、連続巻き取り形態の本発明の目的製品で
ある無機質繊維シートを得た。 実施例 8 実施例1の手順において、平均粒径2μのクレ
ー粉末64重量部の代わりに、平均粒径2μのクレ
ー粉末50重量部を利用し、それ以外の手順は、全
て、実施例1の対応する手順と同一に処方するこ
とにより、本発明の目的製品である無機質繊維シ
ートを得た。 実施例 9 平均繊維径3μ、繊維長10mm以下のアルミナシ
リカ系細径セラミツク繊維10重量部を水中に分散
させ、セラミツク繊維の濃度0.05重量%の分散液
を得た後、水酸化マグネシウム300重量部を添加
し、粗大粒子塊がなくなるまで十分に攪拌した。 次いで、平均繊維径10μ、繊維長30mm以下のセ
ラミツク繊維90重量部を添加し、さらに、バイン
ダー成分としての繊維状ポリビニルアルコール18
重量部を添加して攪拌した。 しかる後に、定着剤として、固形成分換算で
0.5重量部のカチオン系ポリアクリルアミドを添
加後、さらに、同じく、固形成分換算で0.5重量
部のアニオン系ポリアクリルアミドを添加して十
分に定着させ、得られた水性スラリーを常法によ
る手抄きに付し、本発明の目的製品である無機質
繊維シートを得た。 実施例 10 平均繊維径1μ、繊維長10mm以下の細径アルミ
ナ繊維10重量部を水中に分散させ、アルミナ繊維
の濃度0.05重量%の分散液を得た後、填料として
の酸化アルミニウム50重量部を添加し、粗大粒子
塊がなくなるまで十分に攪拌し、次いで、平均繊
維径10μ、繊維長6mmのアルミナ繊維90重量部を
添加して攪拌した。 しかる後に、定着剤として、固形成分換算で
0.5重量部のカチオン系ポリアクリルアミドを添
加し、さらに、同じく、固形成分換算で0.5重量
部のアニオン系ポリアクリルアミドを添加し、填
料を十分に定着させ、得られた水性スラリーを常
法による手抄き付し、本発明の目的製品である無
機質繊維シートを得た。 実施例 11 平均繊維径0.7μ、繊維長10mm以下の細径ガラス
繊維10重量部を水中に分散させ、ガラス繊維の濃
度0.05重量%の分散液を得た後、平均粒径2μのク
レー粉末300重量部を添加し、粗大粒子塊がなく
なるまで十分に攪拌した。 次いで、平均繊維径10μのロツクウール90重量
部を添加し、さらに、バインダー成分としての繊
維状ポリビニルアルコール18重量部を添加して攪
拌した。 しかる後に、定着剤として、固形成分換算で
0.5重量部のノニオン系ポリアクリルアミドを添
加後、さらに、同じく、固形成分換算で0.5重量
部のカチオン系ポリアクリルアミドを添加し、得
られた水性スラリーを常法による手抄きに付し、
本発明の目的製品である無機質繊維シートを得
た。 以上各実施例における抄造成分組成を第4表に
示す。 また、得られた無機質繊維シートの物性を、填
料の歩留まりと併せて第5表に示す。 なお、無機質繊維シートの坪量は、VIS P
8124により、また、密度は、JIS P 8118によつ
て測定した数値である。 さらに、填料歩留まりは、JIS P 8209に規定
されるパルプ試験用手すきシートマシンによる抄
紙時のワイヤー濾液を採取し、濾過、乾燥した後
に重量を測定し、水性スラリーに投入した填料の
配合量に対する濾液中の填料の含有量を、灰分に
よつて算出し、両者の比率で表示した。
In the method for producing inorganic fibers of the present invention, inorganic fibers containing 5% by weight or more of small-diameter inorganic fibers with an average fiber diameter of 3 μ or less are used as the inorganic fiber component, and 100% by weight of this inorganic fiber is used. 50 to 300 parts by weight of filler and a fixing agent made of a cationic polymeric substance and an anionic polymeric substance, or a fixing agent made of a cationic polymeric substance and a nonionic polymeric substance are added. This process consists of dehydrating and paper-making an aqueous slurry for paper-making, which is made by using a cationic polymeric substance and an anionic polymeric substance in combination.
Alternatively, the filler can be efficiently fixed to the small-diameter inorganic fibers in the aqueous slurry by the action of a fixing agent using a combination of a cationic polymeric substance and a nonionic polymeric substance. Therefore, in the method of the present invention, a high-density inorganic fiber sheet that could not be obtained by conventional dehydration and papermaking methods is produced by the above-mentioned action in the aqueous slurry subjected to dewatering and papermaking. can get. [Example] Hereinafter, the specific structure of the method for producing an inorganic fiber sheet of the present invention will be explained using examples, and the physical properties of the obtained inorganic fiber sheet will be explained using the following example. This will be explained along with the physical properties. Example 1 10 parts by weight of small diameter glass fibers with an average fiber diameter of 0.7μ and a fiber length of 10 mm or less were dispersed in water, and the glass fiber concentration was
After obtaining a 0.05% by weight dispersion, 64 parts by weight of Cree powder having an average particle size of 2 μm as a filler was added, and the mixture was sufficiently stirred until there were no coarse particle agglomerates. Next, 90 parts by weight of E glass fibers having an average fiber diameter of 9 μm and a fiber length of 6 mm were added, and further, 18 parts by weight of fibrous polyvinyl alcohol as a binder component was added and stirred. After that, as a fixing agent, it is added as a solid component.
After adding 0.5 parts by weight of nonionic polyacrylamide, 0.5 parts by weight of cationic polyacrylamide (calculated as a solid component) was added to fully fix the filler, and the resulting aqueous slurry was hand-sheeted by a conventional method. An inorganic fiber sheet, which is the object product of the present invention, was obtained. Example 2 33 parts by weight of small glass fibers with an average fiber diameter of 0.7 μm and a fiber length of 10 mm or less were dispersed in water to reduce the glass fiber concentration.
After obtaining a 0.05% by weight dispersion, 200 parts by weight of magnesium hydroxide as a filler was added, and the mixture was sufficiently stirred until there were no coarse particle agglomerates. Next, 67 parts by weight of E glass fibers having an average fiber diameter of 9 μm and a fiber length of 6 mm were added, and further, 18 parts by weight of fibrous polyvinyl alcohol as a binder component was added and stirred. After that, as a fixing agent, it is added as a solid component.
After adding 0.5 parts by weight of nonionic polyacrylamide, 0.5 parts by weight of cationic polyacrylamide (calculated as solid components) was added to sufficiently fix the filler, and the resulting aqueous slurry was prepared in the same manner as in Example 1. The inorganic fiber sheet, which is the object product of the present invention, was obtained by hand-sheeting. Example 3 50 parts by weight of small diameter glass fibers with an average fiber diameter of 0.7μ and a fiber length of 10 mm or less were dispersed in water to reduce the glass fiber concentration.
After obtaining a 0.05% by weight dispersion, 80 parts by weight of aluminum oxide as a filler was added, and the mixture was sufficiently stirred until there were no coarse particle agglomerates. Next, 50 parts by weight of E glass fibers having an average fiber diameter of 9 μm and a fiber length of 6 mm were added, and further, 18 parts by weight of fibrous polyvinyl alcohol as a binder component was added and stirred. After that, as a fixing agent, it is added as a solid component.
After adding 0.5 parts by weight of nonionic polyacrylamide, 0.5 parts by weight of cationic polyacrylamide (calculated as solid components) was added to sufficiently fix the filler, and the resulting aqueous slurry was prepared in the same manner as in Example 1. The inorganic fiber sheet, which is the object product of the present invention, was obtained by hand-sheeting by the method described above. Example 4 In the procedure of Example 1, 300 parts by weight of clay powder was utilized as a filler, and as a fixing agent,
The same procedure as in Example 1 was followed except that after adding 0.5 parts by weight of cationic polyacrylamide in terms of solid components, 0.5 parts by weight of nonionic polyacrylamide in terms of solid components was added. An inorganic fiber sheet, which is the object product of the present invention, was obtained. Example 5 The same procedure as in Example 1 was followed except that 10 parts by weight of fine glass fibers with an average fiber diameter of 3 μm and a fiber length of 15 mm or less were used as the fine glass fibers, and the objective product of the present invention was obtained. An inorganic fiber sheet was obtained. Example 6 10 parts by weight of alumina-silica-based small-diameter ceramic fibers with an average fiber diameter of 3μ and a fiber length of 10mm or less were dispersed in water to obtain a dispersion with a ceramic fiber concentration of 0.05% by weight, and then clay with an average particle diameter of 2μ was dispersed in water. 64 parts by weight of powder was added and thoroughly stirred until there were no coarse particle agglomerates. Next, 90 parts by weight of ceramic fibers with an average fiber diameter of 10μ and a fiber length of 30mm or less were added, and the subsequent steps were as follows.
By carrying out the same formulation as the corresponding procedure of Example 1, an inorganic fiber sheet, which is the target product of the present invention, was obtained. Example 7 10 parts by weight of small diameter glass fibers with an average fiber diameter of 0.7μ and a fiber length of 10 mm or less were dispersed in water, and the glass fiber concentration was
After obtaining a 0.05% by weight dispersion, 64 parts by weight of clay powder with an average particle diameter of 2 μm was added as a filler, stirred thoroughly until there were no coarse particle agglomerates, and then E with an average fiber diameter of 9 μm and a fiber length of 6 mm was added. After adding 90 parts by weight of glass fiber, 0.5 parts by weight of nonionic polyacrylamide in terms of solid components and 0.5 parts by weight of cationic polyacrylamide in terms of solid components were further added as a fixing agent to form a filler. An aqueous slurry was prepared by thoroughly fixing. The obtained aqueous slurry of inorganic fibers was made into paper using a cylinder paper machine. In addition, an acrylic emulsion (Dow Chemical Company, DOW2647) with a concentration of 15% by weight was used in the paper machine.
is applied by a spray method at a ratio of 11% by weight calculated as a solid component based on the glass fiber component of a glass fiber sheet, and dried with a Yankee dryer to produce a continuously wound product of the present invention. An inorganic fiber sheet was obtained. Example 8 In the procedure of Example 1, 50 parts by weight of clay powder with an average particle size of 2μ was used instead of 64 parts by weight of clay powder with an average particle size of 2μ, and all other procedures were the same as in Example 1. An inorganic fiber sheet, which is the object product of the present invention, was obtained by formulating in the same manner as the corresponding procedure. Example 9 10 parts by weight of alumina-silica-based small-diameter ceramic fibers with an average fiber diameter of 3 μm and a fiber length of 10 mm or less were dispersed in water to obtain a dispersion with a ceramic fiber concentration of 0.05% by weight, followed by 300 parts by weight of magnesium hydroxide. was added and thoroughly stirred until there were no coarse particle lumps. Next, 90 parts by weight of ceramic fibers with an average fiber diameter of 10 μm and a fiber length of 30 mm or less were added, and 18 parts by weight of fibrous polyvinyl alcohol as a binder component was added.
parts by weight were added and stirred. After that, as a fixing agent, it is added as a solid component.
After adding 0.5 parts by weight of cationic polyacrylamide, 0.5 parts by weight of anionic polyacrylamide (calculated as a solid component) was added and sufficiently fixed, and the resulting aqueous slurry was subjected to manual papermaking by a conventional method. An inorganic fiber sheet, which is the object product of the present invention, was obtained. Example 10 10 parts by weight of small alumina fibers with an average fiber diameter of 1 μm and a fiber length of 10 mm or less were dispersed in water to obtain a dispersion liquid with an alumina fiber concentration of 0.05% by weight, and then 50 parts by weight of aluminum oxide as a filler was added. Then, 90 parts by weight of alumina fibers having an average fiber diameter of 10 μm and a fiber length of 6 mm were added and stirred. After that, as a fixing agent, it is added as a solid component.
0.5 parts by weight of cationic polyacrylamide was added, and 0.5 parts by weight of anionic polyacrylamide (calculated as a solid component) was added to fully fix the filler, and the resulting aqueous slurry was hand-sheeted by a conventional method. Then, an inorganic fiber sheet, which is the object product of the present invention, was obtained. Example 11 10 parts by weight of small glass fibers with an average fiber diameter of 0.7μ and a fiber length of 10mm or less were dispersed in water to obtain a dispersion with a glass fiber concentration of 0.05% by weight, followed by 300 parts of clay powder with an average particle diameter of 2μ. Parts by weight were added and stirred thoroughly until there were no coarse particle lumps. Next, 90 parts by weight of rock wool having an average fiber diameter of 10 μm was added, and further, 18 parts by weight of fibrous polyvinyl alcohol as a binder component was added and stirred. After that, as a fixing agent, it is added as a solid component.
After adding 0.5 parts by weight of nonionic polyacrylamide, 0.5 parts by weight of cationic polyacrylamide (calculated as a solid component) was added, and the resulting aqueous slurry was subjected to manual papermaking in a conventional manner.
An inorganic fiber sheet, which is the object product of the present invention, was obtained. Table 4 shows the composition of the papermaking components in each of the Examples above. Further, the physical properties of the obtained inorganic fiber sheet are shown in Table 5 together with the yield of filler. The basis weight of the inorganic fiber sheet is VIS P
8124, and the density is a value measured according to JIS P 8118. Furthermore, the filler yield is calculated by collecting the wire filtrate during paper making using a manual sheet machine for pulp testing as specified in JIS P 8209, filtering and drying, and then measuring the weight. The filler content was calculated based on the ash content and expressed as a ratio of the two.

【表】【table】

【表】【table】

【表】【table】

【表】 比較例 1 水性スラリー中の無機質繊維として、平均繊維
径9μ、繊維長6mmのEガラス繊維のみを利用し、
また、定着剤として、ガラス繊維に対する1重量
%のカチオン系ポリアクリルアミドを利用する以
外は、全て、実施例1と同一の手順によつて、比
較のための無機質繊維シートを得た。 比較例 2 定着剤として、ガラス繊維に対する1重量%の
カチオン系ポリアクリルアミドを利用する以外
は、全て、実施例2の手順と同一の手順により、
比較のための無機質繊維シートを得た。 比較例 3 水性スラリー中の無機質繊維として、平均繊維
径9μ、繊維長6mmのEガラス繊維のみを利用し、
また、填料および定着剤の添加を省略し、それ以
外は、全て、実施例1と同一の手順によつて、比
較のための無機質繊維シートを得た。 比較例 4 水性スラリー中の無機質繊維として、平均繊維
径9μ、繊維長6mmのEガラス繊維のみを利用し、
填料および定着剤の添加を省略し、それ以外は、
全て、実施例7の手順と同一の手順によつて、比
較のための無機質繊維シートを得た。 比較例 5 実施例1の手順において、細径ガラス繊維3重
量部とEガラス繊維97重量部を利用する以外は、
全て、実施例1と同一の手順により、比較のため
の無機質繊維シートを得た。 比較例 6 実施例1の手順において、填料として、クレー
粉末350重量部を利用する以外は、全て、実施例
1と同一の手順により、比較のための無機質繊維
シートを得た。 比較例 7 実施例1の手順において、填料として、クレー
粉末40重量部を利用する以外は、全て、実施例1
と同一の手順により、比較のための無機質繊維シ
ートを得た。 比較例 8 実施例1の手順において、細径ガラス繊維とし
て、平均繊維径5μ、繊維長10mmのガラス繊維を
利用する以外は、全て、実施例1と同一の手順に
より、比較のための無機質繊維シートを得た。 以上各実施例における抄造成分組成を第6表に
示す。 また、得られた無機質繊維シートの物性を、填
料の歩留まりと併せて第7表に示す。
[Table] Comparative Example 1 Using only E glass fibers with an average fiber diameter of 9μ and a fiber length of 6mm as the inorganic fibers in the aqueous slurry,
In addition, an inorganic fiber sheet for comparison was obtained in the same manner as in Example 1 except that 1% by weight of cationic polyacrylamide based on the glass fibers was used as a fixing agent. Comparative Example 2 All procedures were the same as those of Example 2, except that 1% by weight of cationic polyacrylamide based on glass fibers was utilized as the adhesion promoter.
An inorganic fiber sheet was obtained for comparison. Comparative Example 3 Using only E glass fibers with an average fiber diameter of 9μ and a fiber length of 6mm as the inorganic fibers in the aqueous slurry,
Further, an inorganic fiber sheet for comparison was obtained by omitting the addition of filler and fixing agent, and otherwise following the same procedure as in Example 1. Comparative Example 4 Using only E glass fibers with an average fiber diameter of 9μ and a fiber length of 6mm as the inorganic fibers in the aqueous slurry,
Omit the addition of fillers and fixatives; otherwise,
An inorganic fiber sheet for comparison was obtained by the same procedure as in Example 7. Comparative Example 5 The procedure of Example 1 was repeated except that 3 parts by weight of small diameter glass fibers and 97 parts by weight of E glass fibers were used.
An inorganic fiber sheet for comparison was obtained by the same procedure as in Example 1. Comparative Example 6 An inorganic fiber sheet for comparison was obtained in the same manner as in Example 1 except that 350 parts by weight of clay powder was used as a filler. Comparative Example 7 The procedure of Example 1 was repeated except that 40 parts by weight of clay powder was used as the filler.
An inorganic fiber sheet for comparison was obtained using the same procedure as described above. Comparative Example 8 Inorganic fibers for comparison were prepared in the same manner as in Example 1, except that glass fibers with an average fiber diameter of 5 μm and a fiber length of 10 mm were used as the small diameter glass fibers. Got a sheet. Table 6 shows the composition of the papermaking components in each of the examples above. Further, the physical properties of the obtained inorganic fiber sheet are shown in Table 7 together with the yield of filler.

【表】【table】

【表】【table】

〔発明の効果〕〔Effect of the invention〕

本発明方法は、抄造法によつて無機質繊維シー
トを得るものであり、従来の抄造法によつては得
ることのできなかつた高密度の無機質繊維シート
が得られるので、前段工程で得られた既成の無機
質繊維シートに対して填料を含浸させる無機質繊
維シートの製造方法と比較して、製造設備上、お
よび、エネルギーの消費の点等において、遥かに
優れた方法により、高密度が要求される分野での
無機質繊維シート、例えば、コンポジツトタイプ
のプリント回路基板や、断熱用の発泡樹脂ボード
に対する面材等の用途に供し得る無機質繊維シー
トが、効率良く得られる。 また、本発明方法によつて得られる無機質繊維
シートは、前段工程で得られた既成の無機質繊維
シートに対して填料を含浸させたものや、あるい
は、大量の填料を含有するスラリーによつて得ら
れる抄造シートからなる無機質繊維シートと比較
して、シートの内部に填料が均一に分布したもの
が得られるため、無機質繊維シートの物性が均質
で、品質の良好なものが得られる。
The method of the present invention obtains an inorganic fiber sheet by a paper-making method, and it can obtain a high-density inorganic fiber sheet that could not be obtained by conventional paper-making methods. Compared to the manufacturing method of inorganic fiber sheets in which fillers are impregnated into existing inorganic fiber sheets, this method is far superior in terms of manufacturing equipment and energy consumption, and requires high density. An inorganic fiber sheet that can be used in the field, for example, as a face material for a composite type printed circuit board or a foamed resin board for heat insulation, can be efficiently obtained. In addition, the inorganic fiber sheet obtained by the method of the present invention can be obtained by impregnating the existing inorganic fiber sheet obtained in the previous step with a filler, or by using a slurry containing a large amount of filler. Compared to an inorganic fiber sheet made from a paper-made sheet, the filler is evenly distributed inside the sheet, so the physical properties of the inorganic fiber sheet are uniform and the quality is good.

Claims (1)

【特許請求の範囲】[Claims] 1 平均繊維径が3μ以下の細径無機質繊維が5
重量%以上の割合で配合されている無機質繊維
100重量部に対して、50〜300重量部の填料、及
び、カチオン系高分子物質とアニオン系高分子物
質とによる定着剤、あるいは、カチオン系高分子
物質とノニオン系高分子物質とによる定着剤が添
加されている水性スラリーを、脱水、抄造するこ
とを特徴とする無機質繊維シートの製造方法。
1 Small diameter inorganic fibers with an average fiber diameter of 3 μ or less 5
Inorganic fibers blended in a proportion of % by weight or more
50 to 300 parts by weight of filler per 100 parts by weight, and a fixing agent made of a cationic polymeric substance and an anionic polymeric substance, or a fixing agent made of a cationic polymeric substance and a nonionic polymeric substance. 1. A method for producing an inorganic fiber sheet, which comprises dewatering and paper-making an aqueous slurry to which is added.
JP17699885A 1985-08-13 1985-08-13 Inorganic sheet Granted JPS6241399A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17699885A JPS6241399A (en) 1985-08-13 1985-08-13 Inorganic sheet

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17699885A JPS6241399A (en) 1985-08-13 1985-08-13 Inorganic sheet

Publications (2)

Publication Number Publication Date
JPS6241399A JPS6241399A (en) 1987-02-23
JPH0316436B2 true JPH0316436B2 (en) 1991-03-05

Family

ID=16023387

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17699885A Granted JPS6241399A (en) 1985-08-13 1985-08-13 Inorganic sheet

Country Status (1)

Country Link
JP (1) JPS6241399A (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03897A (en) * 1989-05-29 1991-01-07 Hokuetsu Paper Mills Ltd Production of flame-retardant paper or flame-retardant board
JPH04239533A (en) * 1991-01-22 1992-08-27 Honshu Paper Co Ltd Production of inorganic fiber substrate prepreg sheet and insulating laminate
US5736209A (en) * 1993-11-19 1998-04-07 E. Kashoggi, Industries, Llc Compositions having a high ungelatinized starch content and sheets molded therefrom
IT1312070B1 (en) 1999-04-14 2002-04-04 Revetex S R L REINFORCEMENT FIBER FOR BITUMINOUS CONGLOMERATES USED IN ROAD FLOORS AND PROCEDURE TO CREATE THE FIBER.
KR102408138B1 (en) * 2021-09-14 2022-06-15 주식회사 엔바이오니아 Ceramic Paper and Manufacturing Method Thereof

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5771466A (en) * 1980-10-20 1982-05-04 Kuraray Co Sheet like article and method
FR2553121B1 (en) * 1983-10-06 1986-02-21 Arjomari Prioux PAPER SHEET, ITS PREPARATION METHOD AND ITS APPLICATIONS, IN PARTICULAR AS A SUBSTITUTION PRODUCT FOR IMPREGNATED GLASS VEILS

Also Published As

Publication number Publication date
JPS6241399A (en) 1987-02-23

Similar Documents

Publication Publication Date Title
US5134179A (en) Composite fiberboard and process of manufacture
US6042936A (en) Microsphere containing circuit board paper
US4963603A (en) Composite fiberboard and process of manufacture
KR101329927B1 (en) Compositions containing expandable microspheres and an ionic compound, as well as methods of making and using the same
CN101528847B (en) Improved urea-formaldehyde resin composition and process for making fiber mats
JPH0127198B2 (en)
US4405744A (en) Filler for paper, card or board, a process for its manufacture, and paper, card or board containing the filler
CN108026697A (en) The top sizing of fine and close film
BRPI0509409B1 (en) aramid paper and aramid paper production process
JPH01224250A (en) Paper, paper products, films, composites and other silicate-polymer construction materials
IE52660B1 (en) Gypsum wallboard paper
KR20140143292A (en) Water-dispersed composition of hydrophobic powder and method for preparing pulp paper and glass fiber using the same
US3949014A (en) Binder
FI63081B (en) PAPPERSPRODUKT MED STOR FYLLAEMNESHALT
US3036950A (en) Process for incorporating resins into paper
KR100903932B1 (en) Chemical composition and process
JPH0316436B2 (en)
US4395306A (en) Method for preparing fibrous mats from a fibrous suspension
US3035965A (en) Paper composed of synthetic fibers, and fibrous binder for use in the manufacture thereof
CN109577102A (en) A kind of electrolytic capacitor paper and preparation method thereof
EP0406354A1 (en) COMPOSITE FIBER PANEL AND METHOD FOR THE PRODUCTION THEREOF.
EP1963567B1 (en) Pipd paper and components made therefrom
JPS62101B2 (en)
JP7729093B2 (en) Manufacturing method of molded body
CN114635309B (en) Papermaking method of high-conductivity water environment