JPS625810A - Disperser for short fiber lump - Google Patents

Disperser for short fiber lump

Info

Publication number
JPS625810A
JPS625810A JP14480485A JP14480485A JPS625810A JP S625810 A JPS625810 A JP S625810A JP 14480485 A JP14480485 A JP 14480485A JP 14480485 A JP14480485 A JP 14480485A JP S625810 A JPS625810 A JP S625810A
Authority
JP
Japan
Prior art keywords
short fiber
fibers
short
dispersion
dispersed
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.)
Pending
Application number
JP14480485A
Other languages
Japanese (ja)
Inventor
金子 忠男
智敬 丸井
阿尾 和夫
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.)
JFE Steel Corp
Original Assignee
Kawasaki Steel Corp
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 Kawasaki Steel Corp filed Critical Kawasaki Steel Corp
Priority to JP14480485A priority Critical patent/JPS625810A/en
Publication of JPS625810A publication Critical patent/JPS625810A/en
Pending legal-status Critical Current

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  • Preparation Of Clay, And Manufacture Of Mixtures Containing Clay Or Cement (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 この発明は炭素繊維、ガラスmM、セラミクス系繊維な
と、無機質材料の強化用m維の短繊維塊を分散する装置
に関するもので、分散された短繊維を用いることにより
無機質材料中への繊維の均一分散を可能ならしめ、M&
維の添加廣に対する強度増加の割合を高めることができ
る。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for dispersing short fiber agglomerates of m-fibers for reinforcing inorganic materials such as carbon fibers, glass mm, ceramic fibers, etc. By using the dispersed short fibers, Enables uniform dispersion of fibers in inorganic materials, M&
The ratio of strength increase to fiber addition width can be increased.

犬、未!」Σ貞 コンクリートや石膏ボードなどに軽j政で強度の大きい
炭素m維、耐アルカリガラス繊維などを添加した強化材
料は公知である。
Dog, no! Reinforced materials are well known, such as concrete and gypsum board, to which lightweight yet strong carbon fibers, alkali-resistant glass fibers, and the like are added.

そういった強化材料の強化用m維で比較的容易に製造さ
れ安価に入手できるのは、5〜10ミリ程度の長さの短
繊維であり1代表的なものとしてピッチ系炭素m維を挙
げることができるが、これは通常綿のように繊維がから
まりあった状態で小さい塊状の形態になっている。
The reinforcing m-fibers for such reinforcing materials are short fibers with a length of about 5 to 10 mm, which are relatively easily produced and available at low cost.1 A typical example is pitch-based carbon m-fibers. However, it is usually in the form of small clumps of tangled fibers, like cotton.

この形態のままで従来のコンクリート又はモルタルミキ
サーでトライまたはウェットな状態のセメントや石膏等
に添加しても、強化用庫維はからまりあったままで、如
何に強力な混合を行っても完全な短繊維状で均一に分散
させることは困難である。そのため製造された強化材料
は、短繊維の添加量に応じて本来期待される十分な強度
を達成することができない。
Even if this form is used in a conventional concrete or mortar mixer to try or add it to wet cement or gypsum, the reinforcing fibers will remain entangled, and no matter how powerful the mixing is, it will not be completely shortened. It is fibrous and difficult to disperse uniformly. Therefore, the manufactured reinforcing material cannot achieve the originally expected sufficient strength depending on the amount of short fibers added.

この問題を解決する一つの方法として、多数の針状突起
を設けた一対の可動体を用い、交錯して相対運動する針
状突起の間で炭素短amの小塊をくしけするようにして
短繊維状にした後コンクリート、モルタル等の原材料に
混入する方法が提案されている(特開昭58−1817
60)。
One way to solve this problem is to use a pair of movable bodies equipped with a large number of needle-like protrusions, and to comb small pieces of short carbon am between the needle-like protrusions that intersect and move relative to each other. A method has been proposed in which the fibers are made into short fibers and then mixed into raw materials for concrete, mortar, etc.
60).

しかしながら、このような機械的方法では完全に短繊維
状に分散させることは期待し難い。
However, it is difficult to expect complete dispersion into short fibers using such mechanical methods.

発明が解決しようとする問題点 本発明は上述のように小塊状にからまりあった短m、*
塊を効率よく個々の短繊維に分散する装置を提供し、併
せて分散された短繊維と無機質材料とを均一に混合する
装置をも提供することを目的とする。
Problems to be Solved by the Invention The present invention solves the problems of the present invention as described above.
It is an object of the present invention to provide an apparatus for efficiently dispersing lumps into individual short fibers, and also to provide an apparatus for uniformly mixing the dispersed short fibers and an inorganic material.

発明の構成 問題点を解決するための手段 本発明に係る無機質材料への短Pa維塊の分散°混合装
置は、上部が閉鎖され底部が解放された円筒体よりなる
分散室、分散室の上部から円筒体の軸線に沿って垂直に
挿入されたガス及び短!a雄塊の供給管および該円筒体
の底部の中央に設置された円形の衝突板よりなる。
Configuration of the Invention Means for Solving the Problems The mixing device for dispersing short Pa fibers into an inorganic material according to the present invention comprises a dispersion chamber consisting of a cylindrical body with a closed top and an open bottom; Gas and short inserted vertically along the axis of the cylinder from! a) Consists of a male mass supply pipe and a circular collision plate installed at the center of the bottom of the cylindrical body.

この装置により分散された短繊維を無機質材料に混合す
るためには、上−記短繊゛維塊の分散装置の下部に、−
上記円筒体と同じ内径で且つ分散室の高さ以上の高さを
有し且つその下部側面に網状フィルターよりなるガス抜
きを設けた中空円筒及びその中空円筒と同じ内径を有し
攪拌機を内蔵する混合器を順次直結した構造を有する無
機質材料と分散された短HIA維の混合装置を設置する
In order to mix the short fibers dispersed by this device into the inorganic material, a lower part of the above-mentioned short fiber mass dispersing device is placed.
A hollow cylinder having the same inner diameter as the above-mentioned cylindrical body, having a height greater than the height of the dispersion chamber, and having a gas vent made of a mesh filter on the lower side surface thereof, and a stirrer having the same inner diameter as the hollow cylinder. A mixing device for inorganic material and dispersed short HIA fibers is installed, which has a structure in which mixers are directly connected in sequence.

これを添付図面により詳細に説明する。第1図は本発明
の短繊維塊の分散装置の下部に、分散された短繊維の混
合装置を設置した場合を側断面図で示したものである。
This will be explained in detail with reference to the accompanying drawings. FIG. 1 is a side sectional view showing a case where a mixing device for dispersed short fibers is installed below the short fiber mass dispersing device of the present invention.

上部が閉鎖され底部が解放された円筒体11よりなる分
散室12の上部から円筒体の軸線に沿って、ガス及び短
繊維塊の供給管13が垂直に挿入されており、円筒体の
底部の中央には円形の衝突板14が設置されて短繊維塊
の分散装置1を構成している。
A gas and short fiber mass supply pipe 13 is inserted vertically from the top of the dispersion chamber 12, which is made up of a cylinder 11 with a closed top and an open bottom, along the axis of the cylinder. A circular collision plate 14 is installed in the center to constitute the short fiber mass dispersing device 1.

この分散装置lの下部に、上記円筒体12と同じ内径で
1つ分散室の高さくL)以上の高さく〉L)を有し且つ
その下部側面に網状フィルター21よりなるガス抜きを
設けた中空円筒2及びその中空円筒2と同じ内径を有し
攪拌機31を内蔵する混合器3を順次直結した構造を有
する無機質材料と分散された短tawrの混合装置が改
行されている。
At the bottom of this dispersion device l, there was a dispersion chamber with the same inner diameter as the cylindrical body 12 and a height >L) greater than or equal to the height of the dispersion chamber, and a gas vent consisting of a mesh filter 21 was provided on the side surface of the lower part. A short tawr mixing device in which an inorganic material is dispersed has a structure in which a hollow cylinder 2 and a mixer 3 having the same inner diameter as the hollow cylinder 2 and containing a stirrer 31 are directly connected in sequence.

分散室12における円筒体11の上部の閉鎖部分15の
形状は、第1図に例示された截頭円錐状に限定されるも
のではなく、釣鐘状、水平プレート状その他任意の形状
に構成することができる。
The shape of the upper closed portion 15 of the cylindrical body 11 in the dispersion chamber 12 is not limited to the truncated cone shape illustrated in FIG. I can do it.

円形の衝突板14を円筒体の下端の中心に設置するため
には、第1図に例示したように円筒体の底部に網16を
張りその中心に固定するとか、円筒体の壁から支柱を出
して支えるとかの方法があるが、いずれにしても円形の
衝突板14の周囲はガス及び分散された短ja雄が自由
に通過できるように解放されている。
In order to install the circular collision plate 14 at the center of the lower end of the cylinder, as illustrated in FIG. There is a method of extending and supporting it, but in either case, the area around the circular collision plate 14 is open so that gas and dispersed short jabs can freely pass through.

また16は金属製の金網でもよいが、分散するm維の切
断笠のダメージを防ぐためには繊維材料の柔らかいネッ
トの方が望ましい。
Further, the wire mesh 16 may be a metal wire mesh, but a soft net made of fiber material is preferable in order to prevent damage to the cut hat of the dispersed m-fibers.

なお中空円筒のガス抜きを構成する網状フィルター21
には短繊維が堆積しがちなので、第2図に部分断面斜視
図として示すように、網状フィルターを内部からブラッ
シングするようにブラシ4を取り付けることにより短繊
維が網状フィルターに堆積するのを効果的に防止するこ
とができる。
Note that a mesh filter 21 constitutes a hollow cylindrical gas vent.
Since short fibers tend to accumulate on the mesh filter, as shown in the partial cross-sectional perspective view in Fig. 2, by attaching a brush 4 to brush the mesh filter from the inside, it is possible to effectively prevent short fibers from accumulating on the mesh filter. can be prevented.

ブラシ4の取付は方法としては、混合器3に設けた攪拌
fi31の回転軸32に直結されて回転するようにすれ
ば、特別のブラシ駆動機構を設ける必要がないので便利
である。
It is convenient to attach the brush 4 so that it is directly connected to the rotating shaft 32 of the stirring fi 31 provided in the mixer 3 and rotates, since there is no need to provide a special brush drive mechanism.

作用 ガス及び短ta維塊の供給管13から分散室12に送入
された高速ガス流は供給管13先端の直下にある円形の
衝突板14にあたり1反転して分散室側壁を上昇し、分
散室北部で反転して下方に向う。ガス流の一部はさらに
この反転運動を繰り返すので、分散室の内部は高度の攪
拌気流状態になる。
The high-speed gas flow fed into the dispersion chamber 12 from the supply pipe 13 of working gas and short ta fibrils hits the circular collision plate 14 located directly below the tip of the supply pipe 13, reverses once, ascends the dispersion chamber side wall, and is dispersed. It turns around in the northern part of the room and heads downward. A portion of the gas flow further repeats this reversal motion, resulting in a highly agitated gas flow state inside the dispersion chamber.

高速ガス流に伴なわれて供給管13から分散室11へ送
入された綿状にamがからまりあった短繊維塊は衝突板
14における衝撃や高度の攪拌状態にあるガス流による
分散効果を受けてばらばらにほぐされ1個々の繊維に分
散した状態になったものが網16等の空隙を通過して落
下する。
The cotton-like short fiber mass entangled with am, which is sent from the supply pipe 13 to the dispersion chamber 11 along with the high-speed gas flow, is dispersed by the impact on the collision plate 14 and the gas flow in a highly agitated state. The fibers are loosened and dispersed into individual fibers, which pass through the gaps of the net 16 and fall.

従って分散された状態の繊維を回収するには、この分散
装置の出口側(網16側)に捕集用のバー、グツイルタ
ー等を取り付ければよい。
Therefore, in order to collect the dispersed fibers, a collection bar, filter, etc. may be attached to the outlet side (net 16 side) of the dispersion device.

この〉うにして分散された短繊維を取り出し、別に設け
た無機質材料と短m!Iとの混合装置に供給してもよい
が、第1図に示す如く分散装置の下部に混合装置を直結
した構造にするのが便利である。
The short fibers dispersed in this way are taken out and mixed with a separately prepared inorganic material. Although it may be supplied to a mixing device with I, it is convenient to have a structure in which the mixing device is directly connected to the lower part of the dispersing device as shown in FIG.

混合装置における中空円筒2の径は、ガス及び短m維塊
の供給管13の径よりも太いので、ここでの気流速度は
減少し、分散した短繊維はゆるやかに流動している状態
になる。さらにガス流は網状フィルター21から外部へ
流出するので、混合器3の真上では短Iamは自由落下
の状態で、混合器内で攪拌されている無機質材料の表面
に逐次散布される。
Since the diameter of the hollow cylinder 2 in the mixing device is larger than the diameter of the gas and short fiber mass supply pipe 13, the airflow velocity here decreases, and the dispersed short fibers are in a state of gentle flow. . Further, the gas flow flows out from the mesh filter 21, so that directly above the mixer 3, the short Iam is in a free-falling state and is successively dispersed onto the surface of the inorganic material being stirred in the mixer.

中空円筒2の高さを、分散室の高さくL)以上の高さく
〉L)とするの−は、分散室で生じている攪拌気流の乱
れを回避し、また分散した短繊維が混合器内で攪拌され
ている無機質材料上の空間に均一に拡散する余裕を午え
るためである。
The height of the hollow cylinder 2 is set to be greater than or equal to the height of the dispersion chamber (L) in order to avoid turbulence in the stirring air flow occurring in the dispersion chamber, and also to prevent the dispersed short fibers from flowing into the mixer. This is to allow room for uniform diffusion in the space above the inorganic material being stirred inside.

このようにして逐次散布される短繊維、例えば炭素繊維
を混合することにより得られた無機質原料1例えば水和
により硬化するセメント原料を混合器から外部に設置し
た型等に注入し固化することにより極めて炭素N&維の
分散状態のよい炭素繊維強化コンクリートが製造される
Inorganic raw material 1 obtained by mixing the short fibers, such as carbon fiber, which are successively dispersed in this way, such as cement raw material that hardens by hydration, is poured from a mixer into a mold installed outside and solidified. Carbon fiber reinforced concrete with extremely good carbon/N/fiber dispersion is produced.

なお本発明装置において使用するガスは通常空気である
が、必要に応じて窒素その他のガスを使用してもよい。
Note that the gas used in the apparatus of the present invention is usually air, but nitrogen or other gas may be used as necessary.

口」(1 炭素繊維として比重1.63.径14.5牌。Mouth” (1 Specific gravity as carbon fiber: 1.63. Diameter 14.5 tiles.

長さ10 m m 、引張強度7800 K g / 
c m 2の重層のピッチ系炭素繊維(呉羽化学株式会
社製)を使用した。
Length 10 mm, tensile strength 7800 Kg/
cm 2 multilayer pitch-based carbon fiber (manufactured by Kureha Chemical Co., Ltd.) was used.

早強セメント、水、及び粉末珪砂を 水:早強セメント=50 + 100 (重量比)粉末
珪砂:早強セメン)=25: 100 (同)の割合で
混合したもの約500gに、第1図に示した装置を用い
て分散させた上記炭素繊維を、体積混合率l、3.及び
5%の割合で、それぞれ約10分間かけて逐次散布し混
合した。
About 500 g of a mixture of early strength cement, water, and powdered silica sand in a ratio of water: early strength cement = 50 + 100 (weight ratio) powdered silica sand: early strength cement) = 25: 100 (same) was added as shown in Figure 1. The above-mentioned carbon fibers dispersed using the apparatus shown in 3. and 5%, respectively, and were sequentially sprinkled and mixed over about 10 minutes.

比較のため同じ組成のセメント混合物に重版の未分散の
炭素m維を体積混合率1,3.及び5%び消泡剤を加え
、オムニミキサー(千代田技研工業株式会社製)で混合
したサンプルを作成した。
For comparison, reprinted undispersed carbon fibers were added to cement mixtures of the same composition at volumetric mixing ratios of 1, 3. A sample was prepared by adding 5% and antifoaming agent and mixing with an Omnimixer (manufactured by Chiyoda Giken Kogyo Co., Ltd.).

各サンプルを40X40X160mmの型枠成形後、2
4時間目に脱型し、20±3°Cで標準養生を行い、材
令70で圧縮強度の測定を行った。
After molding each sample into a 40x40x160mm mold, 2
The mold was removed after 4 hours, and standard curing was performed at 20±3°C, and the compressive strength was measured at the age of 70.

測定方法は1IsR5201に準じて実施した。The measurement method was carried out according to 1IsR5201.

結果を第3図に示す(サンプル数3の平均値)。The results are shown in Figure 3 (average value of 3 samples).

横軸は炭素繊維体積混合率(%)、縦軸は圧縮強度(K
g/cm2) 、0印は本発明により製造したサンプル
、Φ印は比較サンプルを示す。
The horizontal axis is the carbon fiber volume mixing ratio (%), and the vertical axis is the compressive strength (K
g/cm2), 0 mark indicates a sample manufactured according to the present invention, and Φ mark indicates a comparative sample.

1凡亘1」 第3図に示す如く、従来装置によるものは炭素繊維の添
加量が増加すると共に圧縮強度が低下する傾向があるの
に対し、本発明装置によるものは炭素m雄の添加量を増
加しても圧縮強度の低下が見られず、むしろ増加した。
1. As shown in Figure 3, the compressive strength tends to decrease as the amount of carbon fiber added increases with the conventional device, whereas the compressive strength of the device with the present invention decreases as the amount of carbon fiber added increases. Even when the compressive strength was increased, the compressive strength did not decrease, but rather increased.

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

第1図は本発明に係る短繊維塊の分散装置の下部に分散
された短繊維の混合器aを設置した場合断面斜視図で網
状フィルターを内部からブラッシングするようにブラシ
4を取り付けた構造を示す図、第3図は本発明装置によ
り製造したサンプルおよび比較サンプルの圧縮強度を測
定した結果を示す図で、横軸は炭素繊維体積混合率(%
)、縦軸は圧縮強度(Kg/cm2)、O印は本発明装
置により製造したサンプル、・印は比較サンプルを示す
FIG. 1 shows a structure in which a brush 4 is attached to brush the mesh filter from the inside in a cross-sectional perspective view when a mixer a of dispersed short fibers is installed at the bottom of the short fiber mass dispersion device according to the present invention. Figure 3 shows the results of measuring the compressive strength of samples manufactured by the apparatus of the present invention and comparative samples, and the horizontal axis shows the carbon fiber volume mixing ratio (%).
), the vertical axis is the compressive strength (Kg/cm2), the O mark indicates a sample manufactured by the apparatus of the present invention, and the * mark indicates a comparative sample.

Claims (1)

【特許請求の範囲】 1 上部が閉鎖され底部が解放された円筒体よりなる分
散室、分散室の上部から円筒体の軸線に沿って垂直に挿
入されたガス及び短繊維塊の供給管及び該円筒体の底部
の中央に設置された円形の衝突板よりなる短繊維塊の分
散装置。 2 下部に、上記円筒体と同じ内径で且つ分散室の高さ
以上の高さを有し且つその下部側面に網状フィルターよ
りなるガス抜きを設けた中空円筒及びその中空円筒と同
じ内径を有し攪拌機を内蔵する混合器を順次直結した構
造を有する無機質材料と分散された短繊維の混合装置を
設置したことよりなる特許請求の範囲第1項記載の短繊
維塊の分散装置。 3 分散装置の下部に設置した中空円筒の下部側面に設
けた網状フィルターを内部からブラッシングするように
取り付けられたブラシを有することよりなる特許請求の
範囲第2項記載の短繊維塊の分散装置。
[Claims] 1. A dispersion chamber consisting of a cylindrical body with a closed top and an open bottom, a gas and short fiber mass supply pipe inserted vertically from the top of the dispersion chamber along the axis of the cylinder, and A short fiber mass dispersion device consisting of a circular collision plate installed at the center of the bottom of a cylindrical body. 2. A hollow cylinder having the same inner diameter as the above-mentioned cylindrical body and a height greater than or equal to the height of the dispersion chamber, and having a gas vent made of a mesh filter on the side surface of the lower part, and having the same inner diameter as the hollow cylinder. 2. The apparatus for dispersing short fiber lumps according to claim 1, comprising a mixing apparatus for mixing an inorganic material and dispersed short fibers, which has a structure in which mixers each having a built-in stirrer are directly connected in sequence. 3. The apparatus for dispersing short fiber lumps according to claim 2, which comprises a brush attached to the lower side surface of a hollow cylinder installed at the lower part of the dispersion apparatus so as to brush the net filter from the inside.
JP14480485A 1985-07-03 1985-07-03 Disperser for short fiber lump Pending JPS625810A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14480485A JPS625810A (en) 1985-07-03 1985-07-03 Disperser for short fiber lump

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14480485A JPS625810A (en) 1985-07-03 1985-07-03 Disperser for short fiber lump

Publications (1)

Publication Number Publication Date
JPS625810A true JPS625810A (en) 1987-01-12

Family

ID=15370849

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14480485A Pending JPS625810A (en) 1985-07-03 1985-07-03 Disperser for short fiber lump

Country Status (1)

Country Link
JP (1) JPS625810A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018083388A (en) * 2016-11-25 2018-05-31 株式会社Ihi建材工業 Fiber dispersion apparatus and concrete manufacturing device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018083388A (en) * 2016-11-25 2018-05-31 株式会社Ihi建材工業 Fiber dispersion apparatus and concrete manufacturing device

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