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JPH0450432B2 - - Google Patents
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JPH0450432B2 - - Google Patents

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Publication number
JPH0450432B2
JPH0450432B2 JP61307836A JP30783686A JPH0450432B2 JP H0450432 B2 JPH0450432 B2 JP H0450432B2 JP 61307836 A JP61307836 A JP 61307836A JP 30783686 A JP30783686 A JP 30783686A JP H0450432 B2 JPH0450432 B2 JP H0450432B2
Authority
JP
Japan
Prior art keywords
fibers
fluorine
paper
fiber
fluorocarbon
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
JP61307836A
Other languages
Japanese (ja)
Other versions
JPS63165598A (en
Inventor
Toshiaki Suzuki
Kyoshi Isobe
Hideo Shimizu
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.)
Tomoegawa Co Ltd
Original Assignee
Tomoegawa 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 Tomoegawa Paper Co Ltd filed Critical Tomoegawa Paper Co Ltd
Priority to JP30783686A priority Critical patent/JPS63165598A/en
Publication of JPS63165598A publication Critical patent/JPS63165598A/en
Publication of JPH0450432B2 publication Critical patent/JPH0450432B2/ja
Granted legal-status Critical Current

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  • 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、フツ素樹脂自体の有する耐熱性、耐
薬品性、耐侯性、不燃性、電気絶縁性、非粘着性
等の優れた特性をそのまま紙状物として発揮でき
るフツ素繊維紙とその製造方法に関するものであ
る。 〈従来の技術〉 近年、合成樹脂のめざましい発達とともに、こ
れら合成樹脂を主成分とした種々の合成繊維紙が
開発され、広く産業分野に利用されている。中で
もフツ素樹脂は優れた耐熱性と耐薬品性とを有す
るためそのシート化が検討されてきており、フイ
ルム、フエルト、クロス等のシート状加工物が提
案されている。しかしながら、これらシート状加
工物においては、フイルムは透気性、透液性に欠
け、フエルトは薄葉物となりにくく、クロスは孔
径が大きすぎる等の欠点を有しているため、用途
面で大きな制約があつた。このような問題を解決
するためにフツ素繊維の紙状物が望まれている
が、フツ素繊維の紙状物は、フツ素樹脂固有の特
性、即ち、表面エネルギーが小さく非粘着性であ
るため繊維間結合力が不足し、未だ得られていな
のが実状である。 〈発明が解決しようとする問題点〉 本発明は、上記の様な事情に鑑みなされたもの
で、フツ素樹脂からなるシートを湿式抄造法によ
り紙状物として提供するものである。 〔問題点を解決するための手段〕 本発明者らはフツ素繊維からなる紙状物を得る
べく鋭意検討を進めた結果、フツ素繊維と天然パ
ルプ又はPVA繊維とを混合してフツ素繊維混抄
紙を作製し、フツ素繊維の繊維間を熱融着せしめ
た後、天然パルプ又はPVA繊維を除去すること
によつてフツ素繊維紙が得られることを見出し
た。即ち、本発明はフツ素繊維と天然パルプ又は
PVA繊維とを湿式抄造法により混抄し乾燥して
ハンドリング可能なフツ素繊維混抄紙を作製し、
次に該紙をフツ素繊維の軟化点以上の温度で熱圧
着してフツ素繊維の繊維間を熱融着して耐湿潤強
力紙とした後、湿式抄造する際に用いた天然パル
プ又はPVA繊維を溶解する溶媒に浸漬して天然
パルプ又はPVA繊維を溶解し、さらに必要によ
り溶媒で洗浄することによつて天然パルプ又は
PVA繊維を除去し、然るのち、再乾燥すること
によつて得られるフツ素繊維紙及びその製造方法
を提供するものである。 本願発明のフツ素繊維は、テトラフルオルエチ
レン〜エチレン共重合体が使用される。 該テトラフルオルエチレン〜エチレン共重合体
は軟化温度が低く、加工性に優れ、水分散性の向
上したフツ素繊維を提供する。本発明におけるフ
ツ素繊維は、湿式抄紙法により紙状物とするため
に、繊維長が1〜20mmの短繊維であることが必要
で、かつその繊維径は2〜30μmφであることが
好ましい。ここで、例えば、繊維長が短いと強度
が弱くなつてしまい、逆に長いと地合が悪くな
り、また、繊維径が細いと繊維がヨレ易くなつて
しまい、逆に太いとシートが粗いものとなつてし
まう、等の欠点を生じてしまう。 湿式抄造する際に用いられる天然パルプとして
は、通常製紙用として用いられる木材、綿、麻、
わら等の植物繊維があげられる。また、天然高分
子や合成高分子からなる製紙用紙力増強剤などを
用いることができる。 本発明のフツ素繊維紙の製造方法においては、
まず湿式抄造方法によつてフツ素繊維混抄紙を作
製する。この場合、まずフツ素繊維と天然パルプ
又はPVA繊維とを所定の配合比にて水に離解分
散する。次に該分散液をそのまま湿式抄紙機に適
用する。通常のセルロース繊維紙のごとき抄造直
前での叩解工程は敢て要しない。この際、湿式抄
造法であれば抄紙機の種類等に限定されることな
く公知の湿式抄造法が使用できる。湿式抄造法は
水を媒体としてフツ素繊維と天然パルプ又は
PVA繊維の分散や混合が最も容易であるうえ、
界面活性剤や粘剤等の添加剤によるコントロール
が可能であり、均一な地合の紙状物を得るのに最
も有効である。 次に、得られたフツ素繊維混抄紙中のフツ素繊
維同志を固着し繊維間結合を得るために熱圧着が
施されるが、この手段としては、ホツトプレスや
ヒートロール等の公知の方法が適用できる。この
場合、処理温度は、フツ素繊維の軟化点以上に設
定することが必要で通常180〜300℃程度である。
その際のニツプ圧力、加圧時間等の条件は、フツ
素繊維の種類すなわち軟化点、繊維の硬さ、繊維
径等により、適宜設定すればよい。このような温
度設定による熱圧着処理によりフツ素繊維間にお
いて熱融着による結合が生ずる。 次に熱圧着されたフツ素繊維混抄紙から天然パ
ルプ又はPVA繊維を除去するために溶媒による
溶解除去する方法が用いられるが、この場合、フ
ツ素繊維は広範囲な薬品に対して耐薬品性がある
ことから、用いられる溶媒は天然パルプ又は
PVA繊維の種類を考慮して適宜選択すればよい。
例えば天然パルプの場合は無機酸が、又、PVA
繊維の場合は温水が溶媒として使用される。ま
た、溶媒の攪拌、加熱や回流等の溶解除去条件
は、生産性等を考慮して適宜設定される。この様
にして天然パルプ又はPVA繊維を除去した後、
必要に応じて水等で洗浄し任意の方法で再乾燥す
ることによつてフツ素繊維紙が得られる。 更に、所望の物理的特性を持つたフツ素繊維紙
を得るためにはフツ素繊維の種類、繊維径、繊維
長や配合率、抄造条件、熱圧着条件等を適宜コン
トロールすることによつて達成することができ
る。 〈実施例〉 本発明を実施例により更に説明する。なお、配
合比率はすべて重量基準で表わす。 実施例 1 テトラフルオルエチレンとエチレンの共重合体
からなる熱可塑性フツ素繊維(旭硝子社製アフロ
ンCOP、10μmφ×11mm品使用)80部と叩解度
40°SRに叩解されたNBKP20部とを水に分散混合
し、ベタイン型両性界面活性剤(大和化学工業社
製、デスグランB使用)を対原料(フツ素繊維と
パルプに対して。以下も同様)0.5%加え、原料
濃度0.5%で攪拌器により融解した。その後アク
リルアミド系分散剤(ダイヤフロツク社製アクリ
パーズPMP使用)を対原料1%加えて、TAPPI
スタンダードシートマシンでシート化し、乾燥し
て坪量115g/m2のフツ素繊維混抄紙を得た。そ
の後このフツ素繊維混抄紙を220℃10Kg/cm220分
間加熱加圧処理し、更に常温で98%H2SO4液に
浸してフツ素繊維混抄紙中のパルプ分を溶解し、
これを水洗して再び乾燥して本発明のフツ素繊維
紙を得た。 実施例 2 テトラフルオルエチレンとエチレンの共重合体
からなる熱可塑性フツ素繊維(旭硝子社製アフロ
ンCOP、10μm×6mm品使用)90部とPVA繊維
(クラレ社製VPB105−1使用)10部とを水に分
散混合し、ベタイン型両性界面活性剤(大和化学
工業社製デスブランB使用)を対原料0.5%加え、
原料濃度0.5%で攪拌器により離解した。その後
アクリルアミド系分散剤を対原料2%加えて
TAPPIスタンダードシートマシンでシート化し
ヤンキードライヤーで乾燥して坪量111g/m2
フツ素繊維混抄紙を得た。ついで該紙を222℃10
Kg/cm220分間加熱加圧処理し更に90℃以上の熱水
に浸してPVA繊維を溶解し、水洗した後乾燥し
て本発明のフツ素繊維紙を得た。 実施例 3 テトラフルオルエチレンとエチレンの共重合体
からなる熱可塑性フツ素繊維(旭硝子社製アフロ
ンCOP、10μmφ×5mm品使用)95部と微小繊維
状セルローズ(ダイセル化学工業社製MFC)5
部とを水に分散混合し、ベタイン型両性界面活性
剤(大和化学工業社製デスグランB使用)を対原
料0.5%加え、原料濃度0.5%で攪拌器により理解
し、アクリルアミド系分散剤を対原料2%加え
て、TAPPIスタンダードシートマシンでシート
化し、乾燥して坪量140g/m2のフツ素繊維混抄
紙を得た。ついで該紙を220℃10Kg/cm220分間加
熱加圧処理し更に常温で98%H2SO4液に浸して
フツ素繊維混抄紙中の微小繊維セルローズ分を溶
解し、これを水洗して再び乾燥して本発明のフツ
素繊維紙を得た。 実施例 4 実施例1と同様にしてフツ素繊維混抄紙を得た
後、該紙で220℃、200Kg/cm、3m/minの条件
でハードロールにより加熱加圧処理し、更に常温
で98%H2SO4液に浸してフツ素繊維混抄紙中の
バルブ分を溶解し、これを水洗して再び乾燥して
本発明のフツ素繊維紙を得た。 以上のごとく、実施例1〜4で得られたフツ素
繊維紙は、第1表に示す様に、通常の紙状物とし
て取り扱う上で何ら支障ない程度に十分な物理特
性を持つハンドリング可能なシートであり、その
構造は第1図に示す拡大図のとおりフツ素繊維1
が不規則方向に配向し、かつ該繊維の交点2で熱
融着した多孔質の紙層構造を持つたシートである
ことが確認された。また、湿式抄造する際に用い
られたパルプ又はPVA繊維は、完全に除去され
ているのが顕微鏡並びに呈色反応テストにより確
認された。
<Industrial Field of Application> The present invention allows the excellent properties of the fluororesin itself, such as heat resistance, chemical resistance, weather resistance, nonflammability, electrical insulation, and non-adhesiveness, to be exhibited as they are in the form of a paper-like product. This paper relates to fluorine fiber paper and its manufacturing method. <Prior Art> In recent years, with the remarkable development of synthetic resins, various synthetic fiber papers containing these synthetic resins as main ingredients have been developed and are widely used in industrial fields. Among them, fluorocarbon resins have excellent heat resistance and chemical resistance, so their production into sheets has been studied, and sheet-like processed products such as films, felts, and cloths have been proposed. However, these sheet-like processed products have drawbacks such as film lacking in air permeability and liquid permeability, felt not being easily made into thin sheets, and cloth having too large pore diameter, so there are major limitations in terms of use. It was hot. In order to solve these problems, paper-like materials made of fluorocarbon fibers are desired, but paper-like materials made from fluorocarbon fibers have the unique characteristics of fluorocarbon resins, namely, low surface energy and non-adhesion. Therefore, the bonding strength between fibers is insufficient, and the actual situation is that it has not yet been achieved. <Problems to be Solved by the Invention> The present invention has been made in view of the above-mentioned circumstances, and provides a sheet made of fluororesin as a paper-like product by a wet papermaking method. [Means for Solving the Problems] The present inventors have carried out extensive studies in order to obtain a paper-like material made of fluorocarbon fibers, and as a result, they have found that fluorocarbon fibers are produced by mixing fluorocarbon fibers with natural pulp or PVA fibers. We have discovered that fluorocarbon paper can be obtained by producing a mixed paper, heat-sealing the fluorocarbon fibers, and then removing the natural pulp or PVA fibers. That is, the present invention uses fluorine fiber and natural pulp or
By mixing PVA fiber with wet papermaking method and drying it, we create a fluorine fiber mixed paper that can be handled.
Next, the paper is thermocompressed at a temperature higher than the softening point of the fluorine fibers to heat-fuse the fibers of the fluorine fibers to make moisture-resistant strong paper, and then the natural pulp or PVA used for wet papermaking is Natural pulp or PVA fibers are dissolved by immersing them in a solvent that dissolves fibers, and further washed with a solvent if necessary to produce natural pulp or PVA fibers.
The present invention provides a fluorine fiber paper obtained by removing PVA fibers and then re-drying the paper, and a method for producing the same. For the fluorine fiber of the present invention, a tetrafluoroethylene-ethylene copolymer is used. The tetrafluoroethylene-ethylene copolymer has a low softening temperature, excellent processability, and provides fluorine fibers with improved water dispersibility. The fluorine fibers used in the present invention need to be short fibers with a fiber length of 1 to 20 mm, and preferably have a fiber diameter of 2 to 30 μmφ in order to be made into a paper-like product by a wet papermaking method. Here, for example, if the fiber length is short, the strength will be weak; conversely, if the fiber length is long, the formation will be poor; if the fiber diameter is thin, the fibers will easily twist; and if the fiber diameter is thick, the sheet will be rough. This results in disadvantages such as: The natural pulps used in wet papermaking include wood, cotton, hemp, and
Examples include plant fibers such as straw. Further, a paper strength enhancer made of a natural polymer or a synthetic polymer can be used. In the method for producing fluorine fiber paper of the present invention,
First, fluorine fiber mixed paper is produced by a wet papermaking method. In this case, first, fluorine fibers and natural pulp or PVA fibers are disintegrated and dispersed in water at a predetermined blending ratio. The dispersion is then directly applied to a wet paper machine. Unlike ordinary cellulose fiber paper, the beating process immediately before papermaking is not necessary. At this time, any known wet papermaking method can be used without being limited to the type of paper machine. The wet papermaking method uses water as a medium to process fluorine fibers and natural pulp or
PVA fibers are the easiest to disperse and mix;
It can be controlled by additives such as surfactants and adhesives, and is most effective in obtaining paper-like materials with uniform texture. Next, thermocompression bonding is performed in order to fix the fluorine fibers in the obtained fluorine fiber mixed paper together and obtain fiber-to-fiber bonding, and known methods such as hot press and heat roll can be used for this purpose. Applicable. In this case, the treatment temperature needs to be set above the softening point of the fluorine fiber, and is usually about 180 to 300°C.
Conditions such as nip pressure and pressurizing time may be appropriately set depending on the type of fluorine fiber, that is, softening point, fiber hardness, fiber diameter, etc. By thermocompression bonding treatment using such temperature settings, bonding occurs between the fluorocarbon fibers by heat fusion. Next, a method of dissolving and removing natural pulp or PVA fibers using a solvent is used to remove the natural pulp or PVA fibers from the thermocompressed fluorine fiber mixed paper, but in this case, fluorine fibers are resistant to a wide range of chemicals. Therefore, the solvent used is natural pulp or
It may be selected appropriately considering the type of PVA fiber.
For example, in the case of natural pulp, inorganic acids and PVA
In the case of fibers, warm water is used as a solvent. Further, conditions for dissolving and removing the solvent, such as stirring, heating, and circulation, are appropriately set in consideration of productivity and the like. After removing the natural pulp or PVA fibers in this way,
Fluorine fiber paper can be obtained by washing with water or the like if necessary and re-drying by any method. Furthermore, in order to obtain fluorocarbon fiber paper with desired physical properties, this can be achieved by appropriately controlling the type of fluorocarbon fiber, fiber diameter, fiber length, blending ratio, papermaking conditions, thermocompression bonding conditions, etc. can do. <Examples> The present invention will be further explained by examples. All compounding ratios are expressed on a weight basis. Example 1 80 parts of thermoplastic fluorocarbon fiber made of a copolymer of tetrafluoroethylene and ethylene (Afron COP manufactured by Asahi Glass Co., Ltd., 10 μmφ x 11 mm product) and beating degree
Disperse and mix 20 parts of NBKP beaten to 40°SR in water, and add a betaine type amphoteric surfactant (manufactured by Daiwa Chemical Co., Ltd., using Desgrand B) to the raw materials (for fluorocarbon fibers and pulp. The same applies below) ) 0.5% and melted with a stirrer at a raw material concentration of 0.5%. After that, 1% of the raw material was added with an acrylamide-based dispersant (using Acrypas PMP manufactured by Diafloc Co., Ltd.), and TAPPI
It was formed into a sheet using a standard sheet machine and dried to obtain a fluorine fiber mixed paper having a basis weight of 115 g/m 2 . After that, this fluorine fiber mixed paper was heated and pressurized at 220°C at 10 kg/cm 2 for 20 minutes, and then immersed in 98% H 2 SO 4 solution at room temperature to dissolve the pulp in the fluorine fiber mixed paper.
This was washed with water and dried again to obtain the fluorine fiber paper of the present invention. Example 2 90 parts of thermoplastic fluorocarbon fiber made of a copolymer of tetrafluoroethylene and ethylene (Aflon COP, 10 μm x 6 mm manufactured by Asahi Glass Co., Ltd.) and 10 parts of PVA fiber (VPB105-1 manufactured by Kuraray Co., Ltd.) were used. Disperse and mix in water, add 0.5% of betaine type amphoteric surfactant (using Desblan B manufactured by Daiwa Chemical Industry Co., Ltd.) based on the raw material,
Disintegration was performed using a stirrer at a raw material concentration of 0.5%. Then add 2% acrylamide dispersant to the raw material.
It was formed into a sheet using a TAPPI standard sheet machine and dried using a Yankee dryer to obtain a fluorine fiber mixed paper with a basis weight of 111 g/m 2 . Then the paper was heated to 222℃10
Kg/cm 2 The paper was heated and pressurized for 20 minutes, then immersed in hot water of 90° C. or higher to dissolve the PVA fibers, washed with water, and then dried to obtain the fluorine fiber paper of the present invention. Example 3 95 parts of thermoplastic fluorocarbon fiber made of a copolymer of tetrafluoroethylene and ethylene (Aflon COP manufactured by Asahi Glass Co., Ltd., 10 μmφ x 5 mm) and 5 parts of microfibrous cellulose (MFC manufactured by Daicel Chemical Industries, Ltd.)
Disperse and mix in water, add 0.5% betaine-type amphoteric surfactant (using Desglan B manufactured by Daiwa Chemical Industry Co., Ltd.) to the raw material, mix with a stirrer at a raw material concentration of 0.5%, and add the acrylamide-based dispersant to the raw material. 2% was added, formed into a sheet using a TAPPI standard sheet machine, and dried to obtain fluorine fiber mixed paper with a basis weight of 140 g/m 2 . Next, the paper was heated and pressurized at 220°C for 20 minutes at 10 kg/cm 2 and then immersed in 98% H 2 SO 4 solution at room temperature to dissolve the fine cellulose fibers in the fluorine fiber-mixed paper, which was then washed with water. It was dried again to obtain the fluorine fiber paper of the present invention. Example 4 After obtaining fluorine fiber mixed paper in the same manner as in Example 1, the paper was heated and pressurized using a hard roll at 220°C, 200 kg/cm, and 3 m/min, and further heated to 98% at room temperature. The bulb portion in the fluorine fiber mixed paper was dissolved by dipping it in H 2 SO 4 liquid, and this was washed with water and dried again to obtain the fluorine fiber paper of the present invention. As shown in Table 1, the fluorine fiber papers obtained in Examples 1 to 4 have sufficient physical properties and are easy to handle without causing any problems when handled as ordinary paper-like materials. It is a sheet, and its structure is as shown in the enlarged view in Figure 1.
It was confirmed that the sheet had a porous paper layer structure in which the fibers were oriented in irregular directions and were thermally fused at the intersection points 2 of the fibers. Furthermore, it was confirmed through a microscope and a color reaction test that the pulp or PVA fibers used during wet papermaking were completely removed.

【表】【table】

【表】 〈発明の効果〉 従来、フツ素繊維はその本質的な特性から多孔
質の薄葉状シートを得ることはできなかつたが、
本発明によりフツ素繊維の紙状物の製造が可能と
なつた。従つて本発明で得られたフツ素繊維紙
は、フツ素樹脂自体が有する耐熱性、耐薬品性、
不燃性、電気絶縁性、非粘着性等の優れた機能を
そのまま紙状物として多くの用途に発揮すること
ができ、例えば断熱材料、濾過材料、スペーサ
ー、絶縁材料、非粘着材料等として広く産業分野
に用いることができる。
[Table] <Effects of the invention> Conventionally, it was not possible to obtain porous thin sheets from fluorine fibers due to their essential characteristics.
The present invention has made it possible to produce paper-like products made of fluorine fibers. Therefore, the fluorocarbon fiber paper obtained in the present invention has the heat resistance, chemical resistance, and
Excellent functions such as nonflammability, electrical insulation, and non-adhesive properties can be used in many applications as a paper-like material, such as insulating materials, filtration materials, spacers, insulating materials, non-adhesive materials, etc. Can be used in the field.

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

第1図は本発明のフツ素繊維紙の表面拡大図で
ある。 1…フツ素繊維、2…固着部。
FIG. 1 is an enlarged view of the surface of the fluorine fiber paper of the present invention. 1...Fluorine fiber, 2...Adhesion part.

Claims (1)

【特許請求の範囲】 1 不規則方向に配向した短繊維状のテトラフル
オルエチレン−エチレン共重合体よりなるフツ素
繊維により構成され、該繊維の繊維間が熱融着に
より結合されていることを特徴とするフツ素繊維
紙。 2 テトラフルオルエチレン−エチレン共重合体
よりなるフツ素繊維と天然パルプとを湿式抄造法
により混抄し乾燥して得たフツ素繊維混抄紙を、
フツ素繊維の軟化点以上で熱圧着してフツ素繊維
の繊維間を熱融着させた後、天然パルプを無機酸
により溶解除去し、再乾燥することを特徴とする
フツ素繊維紙の製造方法。 3 テトラフルオルエチレン−エチレン共重合体
よりなるフツ素繊維とPVA繊維とを湿式抄造法
により混抄し乾燥して得たフツ素繊維混抄紙を、
フツ素繊維の軟化点以上で熱圧着してフツ素繊維
の繊維間を熱融着させた後、PVA繊維を温水に
より溶解除去し、再乾燥することを特徴とするフ
ツ素繊維の製造方法。
[Scope of Claims] 1. Consisting of fluorine fibers made of short fibers of tetrafluoroethylene-ethylene copolymer oriented in irregular directions, and the fibers of the fibers are bonded by heat fusion. Fluorine fiber paper featuring 2 Fluorine fiber mixed paper obtained by mixing fluorine fibers made of tetrafluoroethylene-ethylene copolymer and natural pulp using a wet papermaking method and drying the paper.
Production of fluorocarbon fiber paper, which is characterized in that the fibers of the fluorocarbon fibers are thermally bonded at a temperature higher than the softening point of the fluorocarbon fibers, and then the natural pulp is dissolved and removed using an inorganic acid, and then re-dried. Method. 3 Fluorine fiber mixed paper obtained by mixing fluorine fibers made of tetrafluoroethylene-ethylene copolymer and PVA fibers using a wet papermaking method and drying the paper.
A method for producing fluorine fibers, which comprises heat-sealing the fibers of the fluorine fibers by thermocompression bonding at a temperature equal to or higher than the softening point of the fluorine fibers, then dissolving and removing the PVA fibers with hot water, and drying again.
JP30783686A 1986-12-25 1986-12-25 Fluorocarbon fiber paper and its production Granted JPS63165598A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP30783686A JPS63165598A (en) 1986-12-25 1986-12-25 Fluorocarbon fiber paper and its production

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP30783686A JPS63165598A (en) 1986-12-25 1986-12-25 Fluorocarbon fiber paper and its production

Publications (2)

Publication Number Publication Date
JPS63165598A JPS63165598A (en) 1988-07-08
JPH0450432B2 true JPH0450432B2 (en) 1992-08-14

Family

ID=17973784

Family Applications (1)

Application Number Title Priority Date Filing Date
JP30783686A Granted JPS63165598A (en) 1986-12-25 1986-12-25 Fluorocarbon fiber paper and its production

Country Status (1)

Country Link
JP (1) JPS63165598A (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0397993A (en) * 1989-07-06 1991-04-23 Tomoegawa Paper Co Ltd Production of fluorinated fiber paper
JP5599140B2 (en) * 2008-09-02 2014-10-01 株式会社巴川製紙所 Sound absorbing structure member and sound absorbing structure
CN104205869B (en) 2012-03-21 2017-11-21 株式会社巴川制纸所 Microphone apparatus, microphone unit, microphone structure and electronic equipment
JP5606580B2 (en) * 2013-04-17 2014-10-15 株式会社巴川製紙所 Sound transmission material

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5953960B2 (en) * 1981-03-16 1984-12-27 日本紙業株式会社 Acid- and alkali-resistant paper with breathability and liquid permeability

Also Published As

Publication number Publication date
JPS63165598A (en) 1988-07-08

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