JPS6357733A - Method and apparatus for producing fiber integrated body - Google Patents

Method and apparatus for producing fiber integrated body

Info

Publication number
JPS6357733A
JPS6357733A JP61202191A JP20219186A JPS6357733A JP S6357733 A JPS6357733 A JP S6357733A JP 61202191 A JP61202191 A JP 61202191A JP 20219186 A JP20219186 A JP 20219186A JP S6357733 A JPS6357733 A JP S6357733A
Authority
JP
Japan
Prior art keywords
fibers
electric field
positive
fiber
negative electrodes
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
Application number
JP61202191A
Other languages
Japanese (ja)
Other versions
JPH0751729B2 (en
Inventor
Tomohito Itou
伊藤 友仁
Hidetoshi Hirai
秀敏 平井
Renichi Isomura
磯村 廉一
Fukuo Gomi
五味 福夫
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.)
Toyota Industries Corp
Original Assignee
Toyoda Automatic Loom Works 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 Toyoda Automatic Loom Works Ltd filed Critical Toyoda Automatic Loom Works Ltd
Priority to JP61202191A priority Critical patent/JPH0751729B2/en
Publication of JPS6357733A publication Critical patent/JPS6357733A/en
Publication of JPH0751729B2 publication Critical patent/JPH0751729B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Abstract

PURPOSE:To accelerate settling of oriented and bridged fibers without disturbing a liquid fiber suspension by the effect of gradient force and to improve the productivity of a fiber integrated body by imparting an intensity gradient in a vertical direction to the electric field between positive and negative electrodes. CONSTITUTION:The opposed spacing of the positive and negative electrodes 2a, 2b is gradually narrowed from the upper part thereof toward the lower part to form the electric field of the intensity gradient increasing from the upper part toward the lower part to the electric field. Anion and cation exchange membranes 3a, 3b are respectively perpendicularly provided to the inside of the electrodes 2a, 2b. The liquid fiber suspension prepd. by dispersing fibers such as whiskers into a dielectric liquid 9 such as CCl4 is injected into the above-mentioned electric field to orient the individual fibers in the liquid 9 in such a state in which the fibers are pointed at one end to the electrode 2a and at the other end to 2b. The fibers are simultaneously bridged and settled. The settling speed is additionally increased by the gradient force based on the intensity gradient of the above-mentioned electric field as compared to the settling speed by the gravity alone.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は繊維集積体の製造方法並びに¥i置、更に詳し
くいえばwLNの多くが一次元配向したとくに繊維強化
金属の製造に用いて好適な繊維集積体の製造方法並びに
装置に関する。
[Detailed Description of the Invention] [Industrial Application Field] The present invention is suitable for use in the production of fiber aggregates and in the production of fiber-reinforced metals in which most of the wLN is one-dimensionally oriented. The present invention relates to a method and apparatus for producing a fiber aggregate.

[従来の技術] 従来、繊維強化金属の製造に使用される短t11維又は
ウィスカ等の比較的短い繊維の繊維集積体を1qるため
に、以下のような方法が試みられている。
[Prior Art] Conventionally, the following methods have been attempted in order to reduce the size of a fiber aggregate of relatively short fibers such as short T11 fibers or whiskers used in the production of fiber-reinforced metals.

その一つには第2図に示すように遠心成形装置を用いる
方法がある(特開昭60−65200号公報)。この遠
心成形装置においては、外筒21内に配置された多孔円
筒容器23内の濾過膜25内に炭化I↑索ウィスカ等の
繊維が供給管24から供給されて遠心作用により該V&
維の中空集積体26を成形する方法である。なお、該図
中22は排水口を示す。
One of them is a method using a centrifugal molding apparatus as shown in FIG. 2 (Japanese Patent Laid-Open No. 60-65200). In this centrifugal forming apparatus, fibers such as carbonized I↑ wire whiskers are supplied from a supply pipe 24 into a filtration membrane 25 in a porous cylindrical container 23 disposed in an outer cylinder 21, and the V&
This is a method of forming a hollow aggregate 26 of fibers. Note that 22 in the figure indicates a drain port.

また、他の従来の方法として、第3図に示すように吸引
成形装置を用いて配向させる方法がある。
Further, as another conventional method, as shown in FIG. 3, there is a method of orienting using a suction molding device.

この方法では、シリンダ31内に所定の繊維混合液34
を入れ、該混合液34を該シリンダ31の上部に配置さ
れた加圧プランジャー32を用いて加圧するとともに、
該シリンダ31の底部に配置された濾過材33から濾液
を真空吸引させて除去することにより該繊維を配向させ
て集積する方法である。これらの他に抄紙法、又はスプ
レー法等の方法がある。
In this method, a predetermined fiber mixture 34 is placed in the cylinder 31.
and pressurize the mixed liquid 34 using the pressurizing plunger 32 disposed at the top of the cylinder 31,
In this method, the filtrate is removed by vacuum suction from the filter medium 33 disposed at the bottom of the cylinder 31, thereby orienting and accumulating the fibers. In addition to these methods, there are methods such as paper making method and spray method.

しかし上記の方法、とくに上記の遠心成形装置又は吸引
成形装置を用いる方法によって成形される繊維集積体で
は、繊維の多くが一次元配向されるものではなく二次元
配向又は三次元配向されるものである。従ってこれらの
方法では、該繊維集積体をIN強化金属にしたときの強
度が所定の一次元方向に十分に強化されないこと、繊維
容積率が低いこと及び圧縮成形時のスプリングバッグが
大きいこと等の欠点がある。
However, in the fiber aggregate formed by the above method, especially the method using the above centrifugal molding device or suction molding device, many of the fibers are not one-dimensionally oriented but two-dimensionally or three-dimensionally oriented. be. Therefore, these methods have problems such as the fact that when the fiber aggregate is made into an IN-reinforced metal, the strength is not sufficiently strengthened in a predetermined one-dimensional direction, the fiber volume ratio is low, and the spring bag is large during compression molding. There are drawbacks.

即も従来の繊維を所定の一次元方向に配向させて繊維集
積体を得たいという願望があるにもかかわらず、該繊維
の多くが一次元配向された繊維集積体は得られず、二次
元配向または三次元配向された繊維集積体が得られるに
過ぎなかった。
Although there is a desire to obtain a fiber aggregate by orienting conventional fibers in a predetermined one-dimensional direction, most of the fibers cannot be obtained in one-dimensional orientation, and two-dimensional fiber aggregates cannot be obtained. Only oriented or three-dimensionally oriented fiber aggregates were obtained.

[発明が解決しようとする問題点] 本発明は、繊維の多くが一次元配向した上記集積体を得
るために、短繊維、ウィスカ等の繊維を誘電液体中に分
散させた繊維懸濁液を、正負電極間に醸成された電界内
に注入して該繊維を静電配向させると同時に橋絡させ、
同配向m維を順次重力沈降させて集積するという技術思
想を基礎としている。
[Problems to be Solved by the Invention] In order to obtain the above-mentioned aggregate in which most of the fibers are one-dimensionally oriented, the present invention uses a fiber suspension in which short fibers, whiskers, and other fibers are dispersed in a dielectric liquid. , injected into an electric field created between positive and negative electrodes to electrostatically orient the fibers and simultaneously bridge them;
It is based on the technical idea that m-fibers with the same orientation are sequentially sedimented by gravity and accumulated.

しかしながら、かかる基礎技術を工業的に実施するため
に生ずる問題も少なくな(、その一つに上記配向11維
沈降時聞の短縮という問題がある。
However, there are a number of problems that arise when implementing this basic technology industrially (one of them is the problem of shortening the sedimentation time of the oriented 11 fibers).

勿論同問題の一般的な解決手段として、第1に配向繊維
を単に重力沈降させるのではなく、繊維懸濁液をより積
極的に吸引排出すること、第2に電界の伜さを増して繊
維の橋絡を密にすることなどが考えられる。ところが前
者のような繊維懸濁液の積極吸引も、これが過ぎると力
学的な液の乱れが生じ易く、後者のような電界強度を増
すこともこれに比例して電気力学的な液の乱れを誘起す
ることとなり、いずれの手段によっても繊維の配向精度
を劣化させる結果、−次元配向繊維の集積という基礎技
術本来の使命達成が損われる。
Of course, as a general solution to the same problem, firstly, the fiber suspension is not simply allowed to settle by gravity, but the fiber suspension is more actively suctioned and discharged, and secondly, the electric field is increased to increase the strength of the fibers. Possible solutions include creating closer bridges between the two parties. However, active suction of the fiber suspension in the former case tends to cause mechanical disturbance of the liquid, and increasing the electric field strength in the latter case also causes proportional electrodynamic disturbance in the liquid. As a result, the orientation accuracy of the fibers is degraded by any means, thereby impairing the achievement of the original mission of the basic technology, which is the accumulation of -dimensionally oriented fibers.

本発明は、繊維懸濁液に乱れを生じさせることなく、配
向橋絡Ia維の沈降を速めることを解決すべき技術課題
とするものである。
The technical problem to be solved by the present invention is to accelerate the settling of oriented and bridged Ia fibers without causing disturbance in the fiber suspension.

[問題点を解決するための手段] 本発明は上記課題解決のため、上記基礎技術に加えて正
負電極間に醸成される電界に強度勾配を付与するもので
あり、具体的には該電界をその上方部から下方部に向か
うにつれて順次強大とする新規な構成を採用している。
[Means for Solving the Problems] In order to solve the above problems, the present invention provides, in addition to the above basic technology, an intensity gradient to the electric field created between the positive and negative electrodes. A new structure is adopted in which the strength increases gradually from the upper part to the lower part.

このように上下方向に強度勾配の付与された電界が醸成
されると、グラジェント力の作用により繊維懸濁液を乱
すことなく配向橋絡繊維の沈降が加速される。
When an electric field with an intensity gradient in the vertical direction is created in this way, the gradient force accelerates the sedimentation of the oriented bridging fibers without disturbing the fiber suspension.

上記電界に強度勾配を付与するには、正負電極を上下方
向複数組に分断し、その各々に異なった電圧を印加して
電界の強さを段階的に変化させることもできるが、正負
電極の対向間隔をその上方部から下方部に向かうにつれ
て順次狭小となし、醸成される電界の強さを連続して変
化させることが望ましい。
In order to impart an intensity gradient to the above electric field, it is possible to divide the positive and negative electrodes into multiple sets in the vertical direction and apply different voltages to each set to change the strength of the electric field in stages. It is desirable that the facing distance be made narrower from the upper part toward the lower part, and the strength of the electric field created can be continuously changed.

正負電極の各内側には導電性amの短絡を防ぎ、かつ繊
維懸濁液の乱流を抑制する隔膜が設けられるが、該隔膜
は傾設された電極とはかかわりなくともに鉛直状に配設
される。何故ならばもしも該隔膜が傾設された電極と平
行の状態で配置されると、隔膜間隔の広大な上方部で橋
絡した繊維群が、沈降につれて順次狭小となる該隔膜と
干渉してその端末部分に曲折を生じるからである。
A diaphragm is provided inside each of the positive and negative electrodes to prevent short-circuiting of the conductive am and to suppress turbulence of the fiber suspension, but the diaphragm is arranged vertically regardless of the inclined electrodes. be done. This is because if the diaphragm is placed parallel to the tilted electrode, the group of fibers bridged in the upper part of the diaphragm gap will interfere with the diaphragm, which becomes narrower as it sinks, causing the diaphragm to become narrower. This is because the terminal portion is bent.

該隔膜としては繊維懸濁液の乱流防止作用を有するイオ
ン交換膜とするのが好ましく、その場合、正電極の内側
には陰イオン交換膜が、負電極の内側には陽イオン交換
膜が配置される。これによって該陰イオン交換膜が正電
極側に発生する陽イオンの繊維配向域への透過侵入を阻
止し、同様に該陽イオン交換膜が負電極側に発生する陰
イオンの繊維配向域への透過侵入を阻止するため、イオ
ンに起因する繊維懸濁液の乱れは巧みに防止される。
The diaphragm is preferably an ion exchange membrane that prevents turbulence of the fiber suspension; in that case, an anion exchange membrane is placed inside the positive electrode, and a cation exchange membrane is placed inside the negative electrode. Placed. As a result, the anion exchange membrane prevents cations generated on the positive electrode side from permeating into the fiber orientation region, and similarly, the cation exchange membrane prevents anions generated on the negative electrode side from entering the fiber orientation region. In order to prevent permeation, ion-induced disturbances of the fiber suspension are effectively prevented.

繊維集積体の製造は、短繊維、ウィスカ等の繊維を誘電
液体中に分散させて繊維懸濁液とすることから始まる。
The production of fiber aggregates begins with dispersing fibers such as staple fibers and whiskers in a dielectric liquid to form a fiber suspension.

上記繊維としては、短繊維及びウィスカの範躊に入るも
ののすべてを用いることができ、その径及び長さはとく
に限定されない。該繊維の材質としては、繊維懸濁液と
して所定の電界内に注入された際、誘電液体中で静電配
向するものであればよく、例えば、アルミナ、シリカ、
アルミナ−シリカ、ベリリヤ、炭素、炭化珪素、窒化珪
素、ガラスのほか各種金属等を使用することができる。
As the above-mentioned fibers, all fibers that fall within the category of short fibers and whiskers can be used, and the diameter and length thereof are not particularly limited. The fibers may be made of any material that electrostatically aligns in the dielectric liquid when injected into a predetermined electric field as a fiber suspension, such as alumina, silica,
Alumina-silica, beryllia, carbon, silicon carbide, silicon nitride, glass, and various metals can be used.

また、該!l維のうちの2種以上を混合して使用するこ
ともできる。
Also applicable! It is also possible to use a mixture of two or more types of fibers.

上記誘電液体とは、電圧の印加により誘電性を示す液体
をいい、これには四塩化炭素、フッ素塩素置換炭化水素
、n−ヘキサン又はシクロヘキサン等が挙げられる。こ
れらの誘電液体のうち四塩化炭素がとくに好ましく、ま
た、フッ素塩素置換炭化水素は取扱い上、安全性の面で
優れている。
The above-mentioned dielectric liquid refers to a liquid that exhibits dielectric properties upon application of voltage, and examples thereof include carbon tetrachloride, fluorochlorine-substituted hydrocarbons, n-hexane, and cyclohexane. Among these dielectric liquids, carbon tetrachloride is particularly preferred, and fluorochlorine-substituted hydrocarbons are superior in handling safety.

なお、該誘電液体中に繊維をなるべく均一に分散させる
には、通常界面活性剤特にノニオン系界面活性剤を適当
量添加することが望ましい。
In order to disperse the fibers as uniformly as possible in the dielectric liquid, it is usually desirable to add a suitable amount of a surfactant, particularly a nonionic surfactant.

続いては上記繊維懸濁液を正負電極間に醸成される電界
内に注入して、v4’m液体中で個々のmMをその一端
が正電極に他端が負電極に指向した(−次元配向)状態
に配向させ、同時に橋絡をともなってこれを沈降させる
ことである。
The fiber suspension was then injected into the electric field created between the positive and negative electrodes, directing the individual mM in the v4'm liquid with one end toward the positive electrode and the other end toward the negative electrode (-dimension). (orientation) state, and at the same time, precipitate it with bridging.

正負電極間に電圧を印加して醸成される上記電界の強さ
は、通常的0.5〜5kv/cmで、これが0.2kv
/C11程度以下では繊維の静電配向が十分でなく、ま
た1Qkv/cll程度以上においては繊維懸濁液に撹
乱が生じて繊維の配向精度が劣化する。もつとも好まし
い電界の強さは約1〜2kv/cIIlである。なお、
該電界の強さは、使用繊維の種類、誘電液体の誘電特性
及び製造される繊維集積体の厚さなどにより、もつとも
好ましい値が設定される。なお、本発明においては、正
負電極間における電界の強さが上下方向に異なるもので
あるけれども、いずれも上記強さの範囲内で選択される
。静電配向された個々の繊維の多くはその配向方向に橋
絡して質量を増し、浮遊繊維よりもその沈降が促進され
るが、上記電界の強度勾配に基づくグラジェント力によ
り該沈降速度は一層増幅される。
The strength of the electric field created by applying a voltage between the positive and negative electrodes is usually 0.5 to 5kv/cm, which is 0.2kv/cm.
If it is less than about /C11, the electrostatic orientation of the fibers will not be sufficient, and if it is more than about 1Qkv/cll, the fiber suspension will be disturbed and the precision of fiber orientation will deteriorate. The most preferred electric field strength is about 1-2 kv/cII. In addition,
The strength of the electric field is set to a preferable value depending on the type of fiber used, the dielectric properties of the dielectric liquid, the thickness of the fiber assembly to be produced, and the like. In the present invention, although the strength of the electric field between the positive and negative electrodes is different in the vertical direction, both are selected within the above range of strength. Many of the electrostatically oriented individual fibers are bridged in the direction of their orientation, increasing their mass, and their sedimentation is promoted more than floating fibers, but the gradient force based on the intensity gradient of the electric field reduces the sedimentation rate. further amplified.

沈降した配向繊維は順次容器の内底壁上に集積されるが
、これが所望厚さに達するまでの間上記繊維懸濁液の注
入は続けられ、容器の底壁からはほぼ等量の液の排出が
行われる。冒頭述べたようにこの液の排出には注意が肝
要で、液に力学的な乱れの生じない程度に流量を調節し
たうえで、自然流出若しくは吸引排出させることが望ま
しい。
The sedimented oriented fibers are accumulated on the inner bottom wall of the container, but the injection of the fiber suspension continues until the desired thickness is reached, and approximately the same amount of liquid is poured from the bottom wall of the container. Evacuation takes place. As mentioned at the beginning, it is important to be careful when discharging this liquid, and it is desirable to adjust the flow rate to such an extent that no mechanical turbulence occurs in the liquid, and then allow it to flow out naturally or by suction.

上記流排出は容器の内底面上に配設された濾過体を介し
て行うことが、流量の調節ばかりでなく繊維の漏出や液
の乱れを防止するうえで効果的であり、該濾過体として
はたとえば多孔質セラミックなどを使用することができ
る。
It is effective not only to adjust the flow rate but also to prevent leakage of fibers and turbulence of the liquid by discharging the flow through a filter arranged on the inner bottom surface of the container. For example, porous ceramic can be used.

かくて集積を終え、残留誘電液体の排出除去をまって取
出された繊維集積体は、所望の寸法形状に裁断するなど
して繊維強化金属用の繊維成形体となされるものである
After the accumulation is completed and the residual dielectric liquid is discharged and removed, the fiber aggregate is taken out and cut into a desired size and shape to form a fiber molded body for fiber-reinforced metal.

本発明方法の実施には、例えば第1図に模式的に示すよ
うな装置が用いられる。図中1は、繊維懸濁液を注入し
うるよう上方の開放された有底箱形状の容器で、その内
側壁には互いに対向し、かつその対向間隔が上方部から
下方部に向かうにつれて狭小となされた正及び負の電極
2a12bが取付けられ、該正及び負の電極2a、2b
の各内側には、陰及び陽のイオン交換膜3a、3bが鉛
直状に配設されて繊維配向域4が画定されている。
For carrying out the method of the present invention, for example, an apparatus as schematically shown in FIG. 1 is used. In the figure, 1 is a box-shaped container with an open top and a bottom so that the fiber suspension can be injected. Positive and negative electrodes 2a12b are attached, and the positive and negative electrodes 2a, 2b
On each inner side, negative and positive ion exchange membranes 3a and 3b are arranged vertically to define a fiber orientation region 4.

上記容器1の底壁には例えば図示しない吸引装置とも接
続可能な導管5及びコツクロからなる排液手段が設けら
れ、これに連通する同容器1の内底壁上には上記繊維配
向域4の全域にわたって濾過体7が装設されている。な
お、8は正負電極2a、2b間に所定の電界を醸成する
ため、該正負電極2a12bと接続された電圧印加装置
である。また、図は繊維懸濁液が注入されたのち、その
誘電液体9中で静電配向され、かつ橋絡した繊紺群1○
が沈Q1ノで、濾過体7上に順次集積される状態を示し
たものである。
The bottom wall of the container 1 is provided with a drainage means consisting of a conduit 5 and a draining means that can be connected to a suction device (not shown), and on the inner bottom wall of the container 1 communicating with this, the fiber orientation area 4 is connected. A filter body 7 is installed over the entire area. Note that 8 is a voltage application device connected to the positive and negative electrodes 2a12b in order to create a predetermined electric field between the positive and negative electrodes 2a and 2b. The figure also shows a group of dark blue fibers 1○ which are electrostatically oriented and bridged in the dielectric liquid 9 after the fiber suspension is injected.
is the precipitate Q1, which shows the state in which it is sequentially accumulated on the filter body 7.

[発明の効果] 本発明の繊維集積体の製造方法は、繊維を誘電液体中に
分散させた繊維懸濁液を正負電極間に醸成された電界内
に注入し、該繊維を静電的に配向橋絡させて沈降せしめ
る際、上記電界にその上方部から下方部に向かうにつれ
て強大となるような強度勾配を付与したものであるから
、グラジェント力の作用により液に乱れを生じさせるこ
となく上記配向橋絡1a雑の沈降を速めて、IN集積体
の生産性を格段と向上させることができる。
[Effects of the Invention] The method for producing a fiber aggregate of the present invention involves injecting a fiber suspension in which fibers are dispersed in a dielectric liquid into an electric field created between positive and negative electrodes, and electrostatically dissipating the fibers. When the liquid is caused to settle by bridging the orientation, the electric field is given an intensity gradient that becomes stronger as it goes from the upper part to the lower part, so the liquid is not disturbed by the action of the gradient force. By accelerating the sedimentation of the miscellaneous oriented bridges 1a, the productivity of the IN aggregate can be significantly improved.

さらに本発明の繊維集積体の製造装置は、対向する正負
電極間隔をその上方部から下方部に向かうにつれて狭小
とするようにしたものであるから、該正負型山間には一
定の電圧を印加するのみで、上記電界に連続した強度勾
配を付与することができる。しかも正負電極の傾設とい
う簡単な手段であるため、その傾度調節によってグラジ
エン1−力の効果を最大限に発揮させることができる。
Furthermore, in the fiber assembly manufacturing apparatus of the present invention, the interval between the opposing positive and negative electrodes is made narrower from the upper part toward the lower part, so that a constant voltage is applied between the positive and negative type peaks. A continuous intensity gradient can be imparted to the electric field by simply applying the electric field. Moreover, since it is a simple method of tilting the positive and negative electrodes, the effect of the gradient force can be maximized by adjusting the tilt.

[実施例] 以下、本発明の実施例について説明する。[Example] Examples of the present invention will be described below.

実施例1 第1図に示す装置における正負電極2a、2bの下端部
対向間隔りを10CII11同電極2a、2bの傾度α
をそれぞれ56に設定し、フッ素塩素置換疾化水素より
なる訓電液体9中にアルミナ短繊維を懸濁させ7: I
維懸濁液を、上記正負電極2a、2b間に醸成される電
解内に注入して液面高さをト」を15c+aとし、液の
流出を止めた状態で配向橋絡繊維にグラジェント力を作
用させて沈降を促進させ、繊維集積高さhがiQmmに
なるまでの沈降時間を測定した。なお、上記電解の強さ
は1kV/Cm及び1.5kv/cm1懸濁液のl!推
溌度は59/又及び2.5(1/又の各条件で試駆した
Example 1 In the device shown in FIG.
were set to 56, respectively, and the alumina short fibers were suspended in a training liquid 9 made of fluorine-chlorine substituted hydrogen chloride 7: I
The fiber suspension is injected into the electrolyte created between the positive and negative electrodes 2a and 2b, the liquid level is set to 15c+a, and a gradient force is applied to the oriented bridging fibers while stopping the outflow of the liquid. was applied to promote sedimentation, and the sedimentation time until the fiber accumulation height h reached iQmm was measured. The strength of the above electrolysis is 1kV/Cm and 1.5kV/cm1 of the suspension. The thrust was tested under conditions of 59/m and 2.5 (1/m).

実施例2 上記正負電極2a、2bのll!i度αをそれぞれ10
0に設定したこと以外は実施例1と同様の条件で試験し
た。
Example 2 ll! of the positive and negative electrodes 2a and 2b! i degree α is 10 each
The test was conducted under the same conditions as in Example 1 except that the value was set to 0.

比較例 上記正負電極2a12bの対向間隔を1Qciとして鉛
直状に配設し、配向橋絡繊維を専ら重力沈降させること
以外は実施例1と同様の条件で試験した。
Comparative Example A test was conducted under the same conditions as in Example 1, except that the positive and negative electrodes 2a12b were arranged vertically with an opposing interval of 1Qci, and the oriented bridging fibers were exclusively allowed to settle by gravity.

実施例1.2及び比較例における」―記沈降時間の測定
結果を表1に示す。
Table 1 shows the measurement results of the sedimentation times in Example 1.2 and Comparative Example.

表  1Table 1

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

第1図は本発明装置の一実施例を示す説明断面図、第2
図は従来の遠心成形装置を示す一部破断説明図、第3図
は同じ〈従来の吸引成形装置の説明図である。 1・・・容器   2a・・・正電極  2b・・・負
電極3a・・・陰イオン交換膜 3b・・・陽イオン交
換膜4・・・繊維配向域   7・・・濾過体8・・・
電圧印加装置   9・・・誘電液体10・・・繊維群 特許出願人  株式会社豊田自助織磯製作所代理人  
 弁理士  大川 宏 同    弁理士  丸山明夫 第1図 第2図 第3図 真空C81
FIG. 1 is an explanatory sectional view showing one embodiment of the device of the present invention, and FIG.
The figure is a partially cutaway explanatory view showing a conventional centrifugal molding apparatus, and FIG. 3 is an explanatory view of the same conventional suction molding apparatus. 1... Container 2a... Positive electrode 2b... Negative electrode 3a... Anion exchange membrane 3b... Cation exchange membrane 4... Fiber orientation region 7... Filter body 8...
Voltage application device 9...Dielectric liquid 10...Fiber group patent applicant Toyoda Jisuke Oriiso Seisakusho Co., Ltd. agent
Patent attorney Hirodo Okawa Patent attorney Akio Maruyama Figure 1 Figure 2 Figure 3 Vacuum C81

Claims (3)

【特許請求の範囲】[Claims] (1)短繊維、ウイスカ等の繊維を誘電液体中に分散さ
せた繊維懸濁液を、正負電極間に醸成された電界内に注
入して該繊維を静電配向させると同時に橋絡させ、同配
向繊維を順次重力沈降させて集積するようにした繊維集
積体の製造方法において、上記電界は正負電極間の上方
部から下方部に向かうにつれて強大となされていること
を特徴とする繊維集積体の製造方法。
(1) A fiber suspension in which short fibers, whiskers, and other fibers are dispersed in a dielectric liquid is injected into an electric field created between positive and negative electrodes to electrostatically orient the fibers and simultaneously bridge them; A method for producing a fiber assembly in which the same oriented fibers are accumulated by gravity sedimentation, wherein the electric field becomes stronger from the upper part to the lower part between the positive and negative electrodes. manufacturing method.
(2)上方の開放された容器と、該容器の内側壁に支持
されて対向し、かつその対向間隔が上方部から下方部に
向かうにつれて、狭小となされた正及び負の電極と、該
正及び負の電極の各内側でほぼ鉛直状に配設された陰及
び陽のイオン交換膜と、上記容器の底壁に設けられた排
液手段と、上記両電極に接続された電圧印加装置とから
なる繊維集積体の製造装置。
(2) An upper open container, positive and negative electrodes supported by the inner wall of the container and facing each other, and whose opposing distance becomes narrower from the upper part to the lower part; and negative and positive ion exchange membranes arranged substantially vertically inside each of the negative electrodes, a drainage means provided on the bottom wall of the container, and a voltage application device connected to both the electrodes. A manufacturing device for a fiber aggregate consisting of.
(3)上記容器の内底面上にろ過体を装設してなる特許
請求の範囲第2項記載の装置。
(3) The device according to claim 2, wherein a filter is installed on the inner bottom surface of the container.
JP61202191A 1986-08-28 1986-08-28 Method and apparatus for manufacturing fiber assembly Expired - Lifetime JPH0751729B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61202191A JPH0751729B2 (en) 1986-08-28 1986-08-28 Method and apparatus for manufacturing fiber assembly

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61202191A JPH0751729B2 (en) 1986-08-28 1986-08-28 Method and apparatus for manufacturing fiber assembly

Publications (2)

Publication Number Publication Date
JPS6357733A true JPS6357733A (en) 1988-03-12
JPH0751729B2 JPH0751729B2 (en) 1995-06-05

Family

ID=16453470

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61202191A Expired - Lifetime JPH0751729B2 (en) 1986-08-28 1986-08-28 Method and apparatus for manufacturing fiber assembly

Country Status (1)

Country Link
JP (1) JPH0751729B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005244154A (en) * 2003-07-10 2005-09-08 Showa Denko Kk Fixture for use in capacitor manufacture, method for manufacturing capacitor, and capacitor
JP2011080188A (en) * 2009-10-02 2011-04-21 Robert Buerkle Gmbh Apparatus and method for producing molding comprising fibrous material

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005244154A (en) * 2003-07-10 2005-09-08 Showa Denko Kk Fixture for use in capacitor manufacture, method for manufacturing capacitor, and capacitor
JP2011080188A (en) * 2009-10-02 2011-04-21 Robert Buerkle Gmbh Apparatus and method for producing molding comprising fibrous material

Also Published As

Publication number Publication date
JPH0751729B2 (en) 1995-06-05

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