JPH0680240B2 - Equipment for manufacturing oriented fiber aggregates - Google Patents
Equipment for manufacturing oriented fiber aggregatesInfo
- Publication number
- JPH0680240B2 JPH0680240B2 JP282986A JP282986A JPH0680240B2 JP H0680240 B2 JPH0680240 B2 JP H0680240B2 JP 282986 A JP282986 A JP 282986A JP 282986 A JP282986 A JP 282986A JP H0680240 B2 JPH0680240 B2 JP H0680240B2
- Authority
- JP
- Japan
- Prior art keywords
- fibers
- dielectric liquid
- rectifying body
- orientation
- fiber
- 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 - Fee Related
Links
- 239000000835 fiber Substances 0.000 title claims description 143
- 238000004519 manufacturing process Methods 0.000 title claims description 27
- 239000007788 liquid Substances 0.000 claims description 66
- 238000007599 discharging Methods 0.000 claims description 4
- 230000003247 decreasing effect Effects 0.000 claims description 2
- 238000001914 filtration Methods 0.000 description 12
- 238000000465 moulding Methods 0.000 description 8
- VZGDMQKNWNREIO-UHFFFAOYSA-N tetrachloromethane Chemical compound ClC(Cl)(Cl)Cl VZGDMQKNWNREIO-UHFFFAOYSA-N 0.000 description 8
- 239000006185 dispersion Substances 0.000 description 7
- 239000000463 material Substances 0.000 description 7
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 4
- 239000000919 ceramic Substances 0.000 description 3
- 230000010354 integration Effects 0.000 description 3
- 238000004062 sedimentation Methods 0.000 description 3
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical class [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 description 3
- LTPBRCUWZOMYOC-UHFFFAOYSA-N Beryllium oxide Chemical compound O=[Be] LTPBRCUWZOMYOC-UHFFFAOYSA-N 0.000 description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- 239000000706 filtrate Substances 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical class CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 2
- 239000002736 nonionic surfactant Substances 0.000 description 2
- 229910010271 silicon carbide Inorganic materials 0.000 description 2
- 239000000377 silicon dioxide Substances 0.000 description 2
- 238000004381 surface treatment Methods 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical class C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000000748 compression moulding Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000002269 spontaneous effect Effects 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
Landscapes
- Manufacture Of Alloys Or Alloy Compounds (AREA)
- Nonwoven Fabrics (AREA)
- Paper (AREA)
Description
【発明の詳細な説明】 [産業上の利用分野] 本発明は配向繊維集積体の製造装置、更に詳しくいえば
繊維の多くが一次元配向した繊維集積体の製造装置に関
する。この「一次元配向」とは、例えば繊維の多くが、
すべてほぼ同一の方向に向いていることを意味する。な
お、これは、該繊維集積体における場合のみならず以下
に述べる配向工程等においても同様に用いられる。TECHNICAL FIELD The present invention relates to an apparatus for producing an oriented fiber assembly, and more specifically to an apparatus for producing a fiber assembly in which many fibers are one-dimensionally oriented. This "one-dimensional orientation" means that, for example, most of the fibers
It means that they all face in almost the same direction. Note that this is used not only in the case of the fiber assembly but also in the orientation step and the like described below.
[従来の技術] 従来、短繊維又はウイスカ等の比較的短い繊維から成る
繊維集積体を得るために以下のような装置を用いること
が試みられている。[Prior Art] Conventionally, it has been attempted to use the following device in order to obtain a fiber assembly made of relatively short fibers such as short fibers or whiskers.
その1つは第7図に示す遠心成形装置がある(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内に炭化珪
素ウイ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、該繊維の中空集積体26を成形することができ
る。なお、該図中22は排水口を示す。One of them is the centrifugal molding device shown in FIG.
-65200 publication). In this centrifugal molding device, the outer cylinder 21
Fibers such as silicon carbide whiskers are supplied from the supply pipe 24 into the filtration membrane 25 in the porous cylindrical container 23 arranged inside, and the hollow aggregate 26 of the fibers can be formed by the centrifugal action. Incidentally, reference numeral 22 in the figure indicates a drainage port.
又他の従来の装置として、第8図に示す吸引成形装置が
ある。この吸引成形装置では、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
せて繊維集積体を成形することができる。As another conventional device, there is a suction molding device shown in FIG. In this suction molding device, a predetermined fiber mixed liquid 34 is put in a cylinder 31, and the mixed liquid 34 is pressurized by using a pressure plunger 32 arranged on the upper portion of the cylinder 31, and the bottom portion of the cylinder 31 is By vacuum suctioning and removing the filtrate from the filter material 33 arranged in the above, the fibers can be oriented to form a fiber assembly.
しかし上記の遠心成形装置又は吸引成形装置を用いて成
形される繊維集積体は、その繊維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。従ってこの繊維集積体は、該繊維集積体を繊維強化
金属(以下FRMという。)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 assembly formed by using the above centrifugal molding apparatus or suction molding apparatus, the fibers are not one-dimensionally oriented but two-dimensionally or three-dimensionally oriented. Therefore, in this fiber assembly, the strength when the fiber assembly is made of fiber reinforced metal (hereinafter referred to as FRM) is not sufficiently strengthened in a predetermined one-dimensional direction, the fiber volume ratio is low, and the compression molding There are drawbacks such as the large spring bag.
即ちこの従来の製造装置においては、該繊維を所定の一
次元方向に配向させた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。That is, in this conventional manufacturing apparatus, although there is a desire to obtain a fiber assembly in which the fibers are oriented in a predetermined one-dimensional direction, a fiber assembly in which the fibers are one-dimensionally oriented can be obtained. However, only a two-dimensionally or three-dimensionally oriented fiber assembly was obtained.
[発明が解決しようとする問題点] 本発明は、上記欠点を克服するものであり、FRMにした
場合所定の一次元方向に高強度のFRMを提供し、繊維容
積率の高いおよびスプリングバッグの少ない、繊維が一
次元配向した繊維集積体を製造できる製造装置を提供す
ることを目的とする。[Problems to be Solved by the Invention] The present invention overcomes the above-mentioned drawbacks and provides a high-strength FRM in a predetermined one-dimensional direction when used as an FRM, and has a high fiber volume ratio and a spring bag. An object of the present invention is to provide a manufacturing apparatus capable of manufacturing a small number of fiber aggregates in which fibers are one-dimensionally oriented.
[問題点を解決するための手段] 本製造装置は、以下に述べる、配向槽と、少なくとも一
対の正負電極と、口過装置と、から成る。[Means for Solving Problems] The present manufacturing apparatus includes an orientation tank, at least a pair of positive and negative electrodes, and a mouthpiece device described below.
上記配向槽は、例えば第1図の模式図に示すように、上
方に短繊維等の繊維1が分散した誘電液体2の供給をう
け、該誘電液体を下方に供給する供給部4と、下方に該
誘電液体2を排出する排出部6と、該供給部4および該
排出部6の間に該誘電液体が下方に移動する配向部5と
をもつ。As shown in the schematic diagram of FIG. 1, for example, the orientation tank is supplied with a dielectric liquid 2 in which fibers 1 such as short fibers are dispersed upward, and a supply unit 4 for supplying the dielectric liquid downward, and a downward direction. Further, it has a discharge part 6 for discharging the dielectric liquid 2 and an orientation part 5 for moving the dielectric liquid downward between the supply part 4 and the discharge part 6.
該供給部は、例えば第1図に示すように正負電極を有す
るものとしてもよいし、例えば第3図に示すように正負
電極を有しないものとしてもよい。The supply unit may have positive and negative electrodes as shown in FIG. 1, or may have no positive and negative electrodes as shown in FIG.
なお、該供給部4の上部には、該繊維を該誘電液体中に
分散させる分散装置又は該誘電液体を供給する供給装置
3を配置した構成とすることもできる。In addition, a disperser for dispersing the fibers in the dielectric liquid or a supply device 3 for supplying the dielectric liquid may be arranged above the supply unit 4.
該排出部は、通常例えば第1図に示すように該配向部底
部に接続するドレーンパイプ61と該ドレーンパイプに接
続するドレーンコック62を有する。なお該供給部、該配
向部および該排出部の形状、大きさ等は特に限定され
ず、目的および用途により種々のものが選択される。The discharge part usually has a drain pipe 61 connected to the bottom of the orientation part and a drain cock 62 connected to the drain pipe as shown in FIG. 1, for example. The shape, size, etc. of the supply unit, the orientation unit, and the discharge unit are not particularly limited, and various ones are selected depending on the purpose and application.
上記正負電極は、該配向槽7の該配向部5に設けられそ
れぞれ垂直方向に伸び水平方向に間隔をへだてて設けら
れた少なくとも一対のものである。該正負電極は、通常
共に板状のものが用いられ、また二対以上の正負電極が
一定間隔をへだてて交互に設けられているものとするこ
ともできる。該正負電極の材質としては、通常用いられ
るものを使用でき、例えば銅等とすることができる。The positive and negative electrodes are at least a pair of electrodes provided in the alignment section 5 of the alignment tank 7 and extending in the vertical direction and spaced apart in the horizontal direction. The positive and negative electrodes are usually both plate-shaped, and two or more pairs of positive and negative electrodes may be alternately provided at regular intervals. As the material of the positive and negative electrodes, a commonly used material can be used, and for example, copper or the like can be used.
上記濾過装置は、該配向槽の該配向部と該排出部の間に
設けられ該誘電液体を通過させ、該繊維を集積させるも
のである。該濾過装置としては、多孔質セラミックフィ
ルタ等の濾過板を有するものとすることができる。The filtration device is provided between the orientation section and the discharge section of the orientation tank and allows the dielectric liquid to pass therethrough to accumulate the fibers. The filtration device may have a filtration plate such as a porous ceramic filter.
本製造装置の特徴は、上記供給部が、該供給部に注入さ
れる該繊維が分散した該誘電液体の流速を減少させるた
めの流速減少用抵抗整流体をもつことである。該抵抗整
流体は、垂直又は水平方向等の種々の方向の、該配向槽
内の液を攪拌させる比較的大きな注入流の流速を、その
攪拌をある程度防止できて、該繊維を適当に分散させる
ものである。A feature of this manufacturing apparatus is that the supply unit has a flow velocity decreasing resistance rectifying body for reducing the flow velocity of the dielectric liquid in which the fibers are injected and which is dispersed in the supply unit. The resistance rectifying body can prevent the agitation of the relatively large flow velocity of the liquid in the orientation tank in various directions such as the vertical or horizontal direction, which agitates the liquid in the orientation tank, and disperse the fibers appropriately. It is a thing.
該抵抗整流体は、上方より流入する、繊維が分散した誘
電液体の流れを水平方向に変える水平衝突板をもつもの
とすることができる。該水平衝突板の形状は特に限定さ
れず、例えば第3図に示す「く」の字形状のもの13又は
第5図に示す水平板状のもの13a等とすることができ、
またこれらの水平衝突板に所望形状の穴を有するものと
することもできる。The resistance rectifying body may have a horizontal impingement plate that changes the flow of the dielectric liquid in which the fibers are dispersed, which flows in from above, in the horizontal direction. The shape of the horizontal collision plate is not particularly limited, and may be, for example, the "V" shape 13 shown in FIG. 3 or the horizontal plate shape 13a shown in FIG.
Further, these horizontal collision plates may have holes having a desired shape.
また該抵抗整流体は例えば第3図に示すように上下方向
に多数の貫通孔14をもつ垂下整流体12bとすることもで
きる。該垂下整流体は、第3図に示すようにほぼ垂直方
向に案内された貫通孔14をもつもの12b、第2図に示す
ように左斜め方向に案内された貫通孔14aをもつもの12
a、又は第4図に示すように左斜め方向および右斜め方
向に案内された各貫通孔14a、14bの両方をもつもの12c
とすることができる。特に第4図に示すように、該繊維
が分散された誘電液体を注入口16に流入させる場合に
は、該垂下整流体12cを使用すると良い。さらに例えば
第3図に示すように該水平衝突板をもつもの12と垂下整
流体12bとを併用することもできる。この場合は、液の
垂直流速を減少させるとともに液の分散も優れるので、
より好ましい。The resistance rectifying body may be, for example, a drooping rectifying body 12b having a large number of through holes 14 in the vertical direction as shown in FIG. The hanging rectifying body has a through hole 14b guided substantially vertically as shown in FIG. 3 and a through hole 14a guided obliquely leftward as shown in FIG. 12 12
a, or 12c having both through holes 14a, 14b guided in the left diagonal direction and the right diagonal direction as shown in FIG.
Can be In particular, as shown in FIG. 4, when the dielectric liquid in which the fibers are dispersed is caused to flow into the injection port 16, the drooping rectifying body 12c may be used. Further, for example, as shown in FIG. 3, the one 12 having the horizontal collision plate and the hanging rectifying body 12b can be used together. In this case, since the vertical flow velocity of the liquid is reduced and the dispersion of the liquid is excellent,
More preferable.
また本製造装置は、第1図に示すように該正負電極8、
9間に高電圧を印加するための高電圧印加装置11を有す
るものとすることができる。なお本製造装置を用いて繊
維の多くが一次元配向した繊維集積体を製造するために
は、該高電圧印加装置等11が必要となる。In addition, as shown in FIG. 1, the manufacturing apparatus includes the positive and negative electrodes 8,
A high voltage applying device 11 for applying a high voltage may be provided between the terminals 9. The high voltage applying device 11 and the like are required to manufacture a fiber assembly in which most of the fibers are one-dimensionally oriented using the present manufacturing apparatus.
本製造装置を用いて繊維の多くが一次元配向した繊維集
積体は、例えば第1図に示すようにして製造される。A fiber assembly in which most of the fibers are one-dimensionally oriented is manufactured by using this manufacturing apparatus, for example, as shown in FIG.
まず、第1工程は、短繊維またはウイスカ等の繊維を誘
電液体に分散し、該誘電液体をビーカー3等を用いて流
速減少用抵抗整流体12の入口に流下させて、該誘電液体
中の該繊維を分散する分散工程である。First, in the first step, fibers such as short fibers or whiskers are dispersed in a dielectric liquid, and the dielectric liquid is made to flow down to the inlet of the flow velocity reducing resistance rectifying body 12 using a beaker 3 or the like, so that the dielectric liquid This is a dispersion step of dispersing the fibers.
該分散工程に用いられる該繊維としては短繊維又はウイ
スカもしくはこれらの繊維の混合繊維とすることができ
る。該ウィスカおよび該短繊維としては、各々ウィスカ
および短繊維の範疇に入るものをすべて用いることがで
き、その径および長さは特に限定されない。該繊維の材
質としては、所定の誘電液体中で高電圧を正負電極間に
印加した場合、静電配向するものであれば良い。例えば
該繊維の材質としては、アルミナ、シリカ、アルミナ−
シリカ、ベリリヤ、炭素、炭化珪素、ガラス又は各種金
属等とすることができる。又該繊維としては、これらの
うちの一材質からなる繊維の2以上の混合繊維とするこ
ともできる。The fibers used in the dispersing step may be short fibers, whiskers, or mixed fibers of these fibers. As the whiskers and the short fibers, all those within the category of whiskers and short fibers can be used respectively, and the diameter and length thereof are not particularly limited. The material of the fibers may be one that electrostatically orients when a high voltage is applied between the positive and negative electrodes in a predetermined dielectric liquid. For example, as the material of the fiber, alumina, silica, alumina-
It may be silica, beryllia, carbon, silicon carbide, glass or various metals. Further, the fiber may be a mixed fiber of two or more fibers made of one of these materials.
該誘電液体とは高電圧の印加により誘電性を示す液体を
いう。該誘電液体としては、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を用い
ることができる。該これらの誘電液体のうち四塩化炭素
が好ましい。又フッ素塩素置換炭化水素は取扱いの安全
性の点から好ましい。The dielectric liquid is a liquid that exhibits a dielectric property when a high voltage is applied. As the dielectric liquid, carbon tetrachloride, fluorinated chlorine-substituted hydrocarbon, n-hexane, cyclohexane or the like can be used. Of these dielectric liquids, carbon tetrachloride is preferred. Fluorine-chlorinated hydrocarbons are preferable from the viewpoint of handling safety.
該繊維の種類および状態によっては、該繊維の表面処理
を実施し、該繊維を解こうして該繊維の凝集状態を解除
する必要がある。該誘電液体に該繊維を分散させるには
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
することが好ましい。Depending on the type and state of the fiber, it is necessary to carry out a surface treatment of the fiber to loosen the fiber and release the aggregated state of the fiber. In order to disperse the fibers in the dielectric liquid, it is usually preferable to add an appropriate amount of a surfactant, especially a nonionic surfactant.
次の第2工程は、該繊維が分散した誘電液体を高電圧を
印加した正負電極間に配置し、該誘電液体中で個々の該
繊維をその一端が該正電極に他端が該負電極に向いた状
態の静電配向させる配向工程である。In the next second step, a dielectric liquid in which the fibers are dispersed is placed between positive and negative electrodes to which a high voltage is applied, and each of the fibers in the dielectric liquid has one end thereof as the positive electrode and the other end as the negative electrode. This is an alignment step of electrostatically aligning the film in the state of facing.
該配向工程においてはこの正負電極間に通常約1〜15KV
程度の直流高電圧を印加する。該高電圧としては、1KV
以下では繊維の静電配向力が充分でなく、又15KV程度以
上においては誘電液体が攪乱され配向された繊維を阻害
すこととなり好ましくない。該高電圧としては約1〜10
KV程度が好ましい。これは該繊維の静電気配向力に優
れ、かつ該誘電液体の攪乱も少ないからである。なお、
該高電圧の大きさとしては、用いる繊維および誘電液体
の誘電特性、および製造される繊維集積体の厚さ等によ
り最も好ましい範囲が種々設定される。In the alignment step, normally about 1 to 15 KV is applied between the positive and negative electrodes.
Apply a high DC voltage. The high voltage is 1KV
Below, the electrostatic orientation force of the fiber is not sufficient, and above about 15 KV, the dielectric liquid is disturbed to disturb the oriented fiber, which is not preferable. The high voltage is about 1 to 10
About KV is preferable. This is because the electrostatic orientation force of the fiber is excellent and the dielectric liquid is less disturbed. In addition,
As the magnitude of the high voltage, the most preferable range is set variously depending on the dielectric properties of the fibers and the dielectric liquid used, the thickness of the fiber assembly to be produced, and the like.
次いで上記により静電配向された個々の繊維はその多く
がその繊維間において該繊維の沈降方向と垂直方向(以
下正負電極方向という。)の一次元方向にブリッジング
を生じ該ブリッジングされた繊維等が下方に沈降してい
く。なお、このブリッジングされた繊維は、されない繊
維と比べて沈降速度が大きくなる。Then, most of the individual fibers electrostatically oriented as described above cause bridging between the fibers in a one-dimensional direction perpendicular to the sedimentation direction of the fibers (hereinafter referred to as positive and negative electrode directions). Etc. settle down. It should be noted that the bridging fiber has a higher sedimentation rate than the non-bridging fiber.
さらに次の第3工程は、上記により静電配向した該繊維
をその配向状態を維持した状態で集積し、該繊維が一次
元配向した繊維集積体を得る工程である。Further, the next third step is a step of accumulating the fibers electrostatically oriented as described above in a state where the orientation state is maintained to obtain a fiber assembly in which the fibers are one-dimensionally oriented.
該集積工程は、配向工程において配向した繊維を例えば
第1図に示すようにドレーンパイプ61に配置されたコッ
ク62を閉じた状態にしておくこと等により自然沈降する
ことにより行うことができる。又該集積工程は、例えば
第1図に示す装置においては、該排出部6のドレーンコ
ック62を開いた状態にすることにより、配向工程におい
て配向した繊維を含む誘電液体を該繊維の配向方向と垂
直方向に濾過し、フィルタ10上に配向した該繊維1aを集
めること等により行うことができる。この濾過する方法
によれば集積時間を短縮することができる。更に該濾過
を吸引又は真空で行うこともできる。又このフィルタを
濾過面全面に配置して自然沈降又は濾過する場合には誘
電液体を排出する際の液の乱れを抑制できるので、配向
された該繊維の配向状態を乱すことが少なく、そのため
一次元配向の状態の良い繊維集積体を得ることができ
る。なお該フィルタは多孔質セラミック等で構成される
ものとすることができる。The accumulating step can be performed by allowing the fibers oriented in the orientation step to naturally settle by, for example, keeping the cock 62 arranged in the drain pipe 61 closed as shown in FIG. Further, in the collecting step, for example, in the apparatus shown in FIG. 1, the drain cock 62 of the discharge section 6 is opened so that the dielectric liquid containing the fibers oriented in the orientation step is changed to the orientation direction of the fibers. It can be performed by filtering in the vertical direction and collecting the oriented fibers 1a on the filter 10. According to this filtering method, the integration time can be shortened. Further, the filtration can be performed by suction or vacuum. Further, when this filter is arranged on the entire filtering surface and spontaneous sedimentation or filtration is performed, the disturbance of the liquid at the time of discharging the dielectric liquid can be suppressed, and therefore the orientation state of the oriented fiber is less disturbed, and therefore the primary It is possible to obtain a fiber assembly having a good original orientation. The filter may be made of porous ceramic or the like.
上記分散工程、配向工程および集積工程を連続的に実施
するものとすることができる。The dispersion step, the orientation step and the integration step may be continuously performed.
集積工程により集積された繊維集積体は、その厚さが比
較的厚いマット形状の集積体とすることもできるし、そ
の厚さの比較的薄いフィルム形状の集積体等とすること
もできる。The fibrous aggregate accumulated in the accumulating step may be a mat-shaped aggregate having a relatively large thickness, a film-shaped aggregate having a relatively thin thickness, or the like.
上記繊維の多くが一次元配向された繊維集積体を所定の
装置から取出し、そのままの形状で又は所望形状に切断
あるいは重ね合わせてFRM用の強化繊維成形体とする。A fiber assembly in which most of the fibers are one-dimensionally oriented is taken out from a predetermined device, and cut or laminated in the same shape or in a desired shape to obtain a reinforced fiber molded body for FRM.
[発明の効果] 本発明の一次元配向繊維集積体の製造装置は、所定の供
給部、配向槽および排出部から成る配向槽と、所定の一
対の正負電極と、高電圧印加装置と、所定の濾過装置
と、から成る製造装置において、該供給部に注入される
誘電液体の流速を減少させるための流速減少用抵抗整流
体をもつことを特徴とする。[Advantageous Effects of the Invention] An apparatus for producing a one-dimensional oriented fiber assembly according to the present invention includes an orientation tank including a predetermined supply unit, an orientation tank and a discharge unit, a predetermined pair of positive and negative electrodes, a high voltage application device, and a predetermined voltage. And a manufacturing apparatus including the filtering device of (1) above, and a resistance rectifying body for reducing the flow velocity for reducing the flow velocity of the dielectric liquid injected into the supply unit.
従って本製造装置において、該誘電液体を該装置に注入
させる際、該誘電液体の流速が減少されるので、該配向
槽での液の攪乱が少ない。故に該配向槽内での配向され
た繊維の配向状態を乱すことが少なく、また該供給部で
の該繊維の分散が均一かつ良好のため、本製造装置によ
れば、該繊維の多くが良好に一次元配向し、また該繊維
の偏りが少ない均一な繊維集積体が得られるので、該繊
維集積体を用いてFRMを製造した場合その一次元配向の
方向に極めて高強度のかつ強度の均一なFRMを製造する
ことができる。Therefore, in the present manufacturing apparatus, when the dielectric liquid is injected into the apparatus, the flow velocity of the dielectric liquid is reduced, so that the liquid is not disturbed in the alignment tank. Therefore, the orientation state of the oriented fibers in the orientation tank is less disturbed, and the dispersion of the fibers in the supply section is uniform and good. Therefore, according to the present manufacturing apparatus, most of the fibers are good. Since a uniform fiber assembly with one-dimensional orientation and little deviation of the fibers can be obtained, when FRM is produced using this fiber assembly, extremely high strength and uniform strength are obtained in the direction of the one-dimensional orientation. FRM can be manufactured.
本製造装置において、該装置に流入した直後の該繊維
は、該装置の配向槽の上部である供給部に存在するた
め、該繊維の沈降時間が長くなり、そのため該繊維の一
次元配向性が向上し、また該配向槽および該電極等を小
さくしても集積効率が良い。In the present manufacturing apparatus, since the fibers immediately after flowing into the apparatus exist in the supply section which is the upper part of the orientation tank of the apparatus, the settling time of the fibers becomes long, so that the one-dimensional orientation of the fibers becomes Further, the efficiency of integration is improved even if the orientation tank and the electrodes are made smaller.
又本製造装置を用いれば、繊維の多くが良好に一次元配
向した繊維集積体が得られるので、該繊維の絡み合いが
少なく、そのため繊維容積率の高い繊維集積体を得るこ
とができる。従って該繊維集積体を用いてFRMを製造す
る場合高強度のFRMを製造することができる。Further, when the present manufacturing apparatus is used, a fiber aggregate in which most of the fibers are satisfactorily one-dimensionally oriented can be obtained, so that the entanglement of the fibers is small, and thus a fiber aggregate having a high fiber volume ratio can be obtained. Therefore, when manufacturing FRM using this fiber assembly, high strength FRM can be manufactured.
又本製造装置によれば、同様に繊維の絡み合いが少ない
のでスプリングバックの少ない繊維集積体を得ることが
できる。従って本装置を用いて製造された繊維集積体を
用いれば精度の良いFRM製品を得ることができる。Further, according to this manufacturing apparatus, since the fibers are also less entangled with each other, it is possible to obtain a fiber assembly with less springback. Therefore, an FRM product with high accuracy can be obtained by using the fiber assembly manufactured using this apparatus.
[実施例] 以下、実施例により本発明を説明する。[Examples] Hereinafter, the present invention will be described with reference to Examples.
表面処理をしないアルミナ短繊維(平均直径約3μ、長
さ10〜500μ)を、四塩化炭素の誘電液体中にごくわず
かのノニオン系界面活性剤とともに添加し、これらを攪
拌して該繊維を分散させた。Alumina short fibers without surface treatment (average diameter about 3μ, length 10-500μ) are added to a dielectric liquid of carbon tetrachloride together with a very small amount of nonionic surfactant, and these are stirred to disperse the fibers. Let
次いで第1図に示す製造装置を準備する。該装置は、該
分散液を注入する流速減少用抵抗整流体12と、 該抵抗整流体12を通じて上方に短繊維1等の繊維が分散
した誘電液体2の供給をうけ下方に該誘電液体を供給す
る供給部4と、下方に該誘電液体を2を排出する排出部
6と、該供給部4および該排出部6の間に該誘電液体2
が下方に移動する配向部5と、をもつ配向槽7と、 該配向槽7の該配向部5に設けられそれぞれ垂直方向に
伸び水平方向に間隔をへだてて設けられた一対の正電極
8および負電極9と、該配向部5と該排出部6の間に設
けられ該誘電液体を通過させ該繊維を集積させる口過装
置10と、これらの電極8、9間に高電圧を印加するため
の高電圧印加装置11と、から成る。なお該抵抗整流体12
は、ロート形状の上部とその下部に接続された水平衝突
板13をもつ。該電極間距離は40mmである。また該口過装
置10は多孔質セラミックフィルタから成る。Next, the manufacturing apparatus shown in FIG. 1 is prepared. The apparatus is supplied with a flow velocity reducing resistance rectifying body 12 for injecting the dispersion liquid, and a dielectric liquid 2 in which fibers such as short fibers 1 are dispersed upward through the resistance rectifying body 12 and supplies the dielectric liquid downward. And a discharge part 6 for discharging the dielectric liquid 2 downward, and the dielectric liquid 2 between the supply part 4 and the discharge part 6.
An alignment tank 7 having an orienting part 5 that moves downward, and a pair of positive electrodes 8 provided in the orienting part 5 of the orienting tank 7 and extending in the vertical direction and spaced apart in the horizontal direction. In order to apply a high voltage between the negative electrode 9, a penetration device 10 provided between the orientation part 5 and the discharge part 6 for passing the dielectric liquid and collecting the fibers, and a high voltage between these electrodes 8 and 9. The high voltage applying device 11 of FIG. The resistance rectifier 12
Has a funnel-shaped upper part and a horizontal impact plate 13 connected to its lower part. The distance between the electrodes is 40 mm. Further, the introducing device 10 is composed of a porous ceramic filter.
該静電配向装置内の電極間に四塩化炭素を入れて、約1K
Vの直流電圧を印加し、該装置内に上記により該繊維1
が分散した誘電液体2をビーカー3に入れて該抵抗整流
体12の上端に注入し、次いで該誘電液体は該水平衝突板
13に衝突し、その流れは水平方向に変更、分散されて、
供給部4に流入した。Put carbon tetrachloride between the electrodes in the electrostatic orientation device, and
A DC voltage of V is applied and the fiber 1
The dielectric liquid 2 dispersed in the beaker 3 is placed in the beaker 3 and injected into the upper end of the resistance rectifying body 12, and then the dielectric liquid is injected into the horizontal collision plate.
Colliding with 13, its flow was changed and dispersed horizontally,
It flowed into the supply section 4.
次いで注入された該繊維1は、該誘電液体2中で誘電分
極してその一端が該正電極8に他端が該負電極9に向い
た状態に静電配向される。この静電配向された該繊維1a
が沈降する際にその多くはブリッジングを生じ該ブリッ
ジングした繊維等が正負電極方向の一次元方向に配向さ
れた状態で沈降していく。Next, the injected fibers 1 are dielectrically polarized in the dielectric liquid 2 and electrostatically oriented so that one end thereof faces the positive electrode 8 and the other end faces the negative electrode 9. This electrostatically oriented fiber 1a
When most of them settle, bridging occurs in most of them, and the fibers and the like that have bridged settle in a state where they are oriented in a one-dimensional direction toward the positive and negative electrodes.
上記により静電配向した該繊維1aを、その配向状態を維
持した状態でドレーンパイプ61に設けられたドレーンコ
ック62を開くことにより該誘電液体をフィルタ10を介し
て濾過させるとともに、該繊維は該フィルタ10上に一次
元配向した状態で集積される。The electrostatically oriented fiber 1a as described above is filtered through the filter 10 to the dielectric liquid by opening the drain cock 62 provided in the drain pipe 61 while maintaining the orientation state, and the fiber is It is integrated on the filter 10 in a one-dimensional orientation.
そして上記分散工程、配向工程および集積工程を順次実
施し、所定の繊維集積体とした後、該装置内に残存する
誘電液体をドレーンパイプ61を通じて除去して、マット
形状の繊維集積体15を製造した。Then, the dispersion step, the orientation step, and the accumulation step are sequentially performed to form a predetermined fiber aggregate, and the dielectric liquid remaining in the apparatus is removed through the drain pipe 61 to produce a mat-shaped fiber aggregate 15. did.
本実施例の装置は、第1図に示すように、該供給部に注
入される誘電液体の流速を減少させるための、水平衝突
板13をもつ流速減少用抵抗整流体12をもつ。従って該誘
電液体を該装置に注入させる際、該誘電液体の垂直方向
の流速が減少され、かつその流れが水平方向に変えられ
るので、該繊維の分散性も良い。As shown in FIG. 1, the apparatus of this embodiment has a flow velocity reducing resistance rectifier 12 having a horizontal collision plate 13 for reducing the flow velocity of the dielectric liquid injected into the supply section. Therefore, when the dielectric liquid is injected into the device, the flow velocity of the dielectric liquid in the vertical direction is reduced, and the flow is changed in the horizontal direction, so that the dispersibility of the fiber is good.
故に本装置によれば多くの該繊維の良好に一次元配向
し、また該繊維の偏りのない均一な繊維集積体が得られ
る。Therefore, according to this apparatus, a uniform fiber assembly in which many of the fibers are well one-dimensionally oriented and the fibers are not biased can be obtained.
更に又本実施例における繊維集積体は繊維が一次元配向
した繊維集積体であるので繊維集積率は従来のものと比
べて高く、又スプリングバックの少ない繊維集積体を得
ることができ、そのため精度の高いFRMを製造すること
ができる。Furthermore, since the fiber assembly in this example is a fiber assembly in which the fibers are one-dimensionally oriented, the fiber assembly rate is higher than that of the conventional one, and a fiber assembly with less springback can be obtained, and therefore the accuracy is improved. High FRM can be manufactured.
また本製造装置は、該配向した繊維を集積する際に該装
置の底部の全面に配置された耐食性の多孔質フィルター
を有するので、本製造装置を用いれば液の排出時に生じ
る液の乱流がなく、そのため該繊維の配向が乱されるこ
とがないので該繊維の配向性の良い繊維集積体を製造す
ることができた。Further, since the present manufacturing apparatus has a corrosion-resistant porous filter disposed on the entire bottom surface of the apparatus when accumulating the oriented fibers, the turbulent flow of the liquid generated when the liquid is discharged is obtained by using the present manufacturing apparatus. Therefore, since the orientation of the fibers is not disturbed, a fiber assembly having good orientation of the fibers can be manufactured.
又本製造装置を用いれば、濾液を連続的にドレーンパイ
プを通じて排出し除去できるので短時間に繊維を集積す
ることができた。Further, since the filtrate can be continuously discharged and removed through the drain pipe by using this manufacturing apparatus, the fibers can be accumulated in a short time.
第1図は実施例に係わり、水平衝突板をもつ流速減少用
抵抗整流体を有する製造装置の説明断面図である。第2
図は垂下整流体を有する製造装置の説明断面図である。
第3図は水平衝突板をもつ流速減少用抵抗整流体および
垂下整流体を有する製造装置の説明断面図である。第4
図は繊維が分散された誘電液体の供給部への注入が横方
向から行なわれ、垂下整流体を有する製造装置の説明断
面図である。第5図は水平衝突板をもつ流速減少用抵抗
整流体の他の例を示す断面図である。 第6図は従来の、繊維が分散された誘電液体を供給部へ
注入した状態の説明断面図である。 第7図は従来の遠心成形装置の一部破断断面図である。
第8図は従来の吸引成形装置の説明断面図である。 1……繊維、1a……配向した繊維 2……誘電液体 3……繊維の分散液の供給装置 4……受給部、5……配向部 6……排出部、10……フィルタ 61……ドレーンパイプ、62……ドレーンコック 7……配向槽、8……正電極 9……負電極、11……高電圧印加装置 12……流速減少用抵抗整流体 13……水平衝突板、14……垂下整流体 15……繊維集積体、16……注入口 21……外筒、22……排水孔 23……多孔円筒容器、24……供給管 25……濾過膜 26……炭化珪素ウイスカの中空成形体 31……シリンダ 32……加圧プランジャー 33……濾過材、34……繊維混合液FIG. 1 is an explanatory cross-sectional view of a manufacturing apparatus having a flow velocity reducing resistance rectifying body having a horizontal collision plate according to the embodiment. Second
The figure is an explanatory cross-sectional view of a manufacturing apparatus having a drooping rectifying body.
FIG. 3 is an explanatory sectional view of a manufacturing apparatus having a flow velocity reducing resistance rectifying body having a horizontal collision plate and a drooping rectifying body. Fourth
The drawing is an explanatory cross-sectional view of a manufacturing apparatus in which a dielectric liquid in which fibers are dispersed is injected into a supply portion from a lateral direction and which has a hanging rectifier. FIG. 5 is a sectional view showing another example of the flow velocity reducing resistance rectifying body having a horizontal collision plate. FIG. 6 is an explanatory cross-sectional view of a state in which a conventional dielectric liquid in which fibers are dispersed is poured into a supply unit. FIG. 7 is a partially cutaway sectional view of a conventional centrifugal molding apparatus.
FIG. 8 is an explanatory sectional view of a conventional suction molding device. 1 ... Fiber, 1a ... Oriented fiber 2 ... Dielectric liquid 3 ... Fiber dispersion liquid supply device 4 ... Receiving unit, 5 ... Orientation unit 6 ... Ejection unit, 10 ... Filter 61 ... Drain pipe, 62 …… Drain cock 7 …… Orientation tank, 8 …… Positive electrode 9 …… Negative electrode, 11 …… High voltage application device 12 …… Flow rate reducing resistance rectifier 13 …… Horizontal collision plate, 14 ・ ・ ・… Suspended rectifier 15 …… Fiber aggregate, 16 …… Injection port 21 …… Outer cylinder, 22 …… Drain hole 23 …… Perforated cylindrical container, 24 …… Supply pipe 25 …… Filtration membrane 26 …… Silicon carbide whisker Hollow molded body 31 …… Cylinder 32 …… Pressurized plunger 33 …… Filtration material, 34 …… Fiber mixed liquid
Claims (3)
た誘電液体の供給をうけ、該誘電液体を下方に供給する
供給部と、下方に該誘電液体を排出する排出部と、該供
給部および該排出部の間に該誘電液体が下方に移動する
配向部と、をもつ配向槽と、 該配向槽の該配向部に設けられそれぞれ垂直方向に伸び
水平方向に間隔をへだてて設けられた少なくとも一対の
正電極および負電極と、 該配向槽の該配向部と該排出部の間に設けられ該誘電液
体を通過させ、該繊維を集積させる口過装置と、からな
る配向繊維集積体の製造装置において、 該供給部は、該供給部に注入される該誘電液体の流速を
減少させるための流速減少用抵抗整流体をもつ配向繊維
集積体の製造装置。1. A supply unit for supplying a dielectric liquid in which fibers such as whiskers and short fibers are dispersed upward and supplying the dielectric liquid downward, and a discharge unit for discharging the dielectric liquid downward, and the supply unit. And an alignment part having an alignment part in which the dielectric liquid moves downward between the discharge part and the discharge part; and an alignment part provided in the alignment part of the alignment part, each extending in the vertical direction and spaced apart in the horizontal direction. And a pair of positive electrodes and a negative electrode, and a passing device which is provided between the orientation part and the discharge part of the orientation tank and allows the dielectric liquid to pass therethrough to accumulate the fibers. 2. The manufacturing apparatus for an oriented fiber assembly, wherein the supply unit has a flow velocity decreasing resistance rectifying body for reducing the flow velocity of the dielectric liquid injected into the supply unit.
上方より流入する、繊維が分散した誘電液体の流れを水
平方向に変える水平衝突板をもつ特許請求の範囲第1項
記載の配向繊維集積体の製造装置。2. The flow velocity reducing resistance rectifying body according to claim 1, wherein the resistance rectifying body has a horizontal impinging plate for horizontally changing the flow of the dielectric liquid in which the fibers are dispersed, which flows in from above the resistance rectifying body. Equipment for manufacturing oriented fiber assembly.
の貫通孔をもつ垂下整流体である特許請求の範囲第1項
又は第2項記載の配向繊維集積体の製造装置。3. The apparatus for producing an oriented fiber assembly according to claim 1, wherein the flow velocity reducing resistance rectifying body is a drooping rectifying body having a large number of through holes in the vertical direction.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP282986A JPH0680240B2 (en) | 1986-01-09 | 1986-01-09 | Equipment for manufacturing oriented fiber aggregates |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP282986A JPH0680240B2 (en) | 1986-01-09 | 1986-01-09 | Equipment for manufacturing oriented fiber aggregates |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS62162099A JPS62162099A (en) | 1987-07-17 |
| JPH0680240B2 true JPH0680240B2 (en) | 1994-10-12 |
Family
ID=11540304
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP282986A Expired - Fee Related JPH0680240B2 (en) | 1986-01-09 | 1986-01-09 | Equipment for manufacturing oriented fiber aggregates |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0680240B2 (en) |
-
1986
- 1986-01-09 JP JP282986A patent/JPH0680240B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPS62162099A (en) | 1987-07-17 |
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