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JPH0550965B2 - - Google Patents
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JPH0550965B2 - - Google Patents

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Publication number
JPH0550965B2
JPH0550965B2 JP63193652A JP19365288A JPH0550965B2 JP H0550965 B2 JPH0550965 B2 JP H0550965B2 JP 63193652 A JP63193652 A JP 63193652A JP 19365288 A JP19365288 A JP 19365288A JP H0550965 B2 JPH0550965 B2 JP H0550965B2
Authority
JP
Japan
Prior art keywords
powder
rotating body
fibers
raw material
small protrusions
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
JP63193652A
Other languages
Japanese (ja)
Other versions
JPH0243006A (en
Inventor
Kenzo Irie
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.)
IRIE HEKIZAI KK
Original Assignee
IRIE HEKIZAI KK
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 IRIE HEKIZAI KK filed Critical IRIE HEKIZAI KK
Priority to JP63193652A priority Critical patent/JPH0243006A/en
Publication of JPH0243006A publication Critical patent/JPH0243006A/en
Publication of JPH0550965B2 publication Critical patent/JPH0550965B2/ja
Granted legal-status Critical Current

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

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明はカーボン、アラミド等短繊維の工場生
産された原材料の状態に於ける短繊維の凝集体
を、乾状態で1本1本のモノフイラメント状に分
散すると同時に、シリカヒユーム等のサブミクロ
ン微粉体或は同径程度の微細繊維又はそれらと共
にセメント、耐火物等の粉体と前記短繊維とを均
一且つ連続的に混合するための方法及び装置に関
する。
Detailed Description of the Invention (Industrial Field of Application) The present invention is a method for converting aggregates of short fibers such as carbon and aramid fibers in the state of factory-produced raw materials into individual short fibers in a dry state. A method for uniformly and continuously mixing the short fibers with submicron fine powder such as silica fume, or fine fibers of about the same diameter, or powders such as cement and refractories together with them, while dispersing them in a filament shape, and Regarding equipment.

(従来技術) 本出願人は先に炭素短繊維の小塊又はチヨツプ
状の短繊維を1本1本分散する装置(特公昭62−
58886号公報参照)を発明した。そして、この繊
維分散装置により分散された炭素短繊維をセメン
ト、耐火物等の成型品原材料中に均一に分散混合
させ、凝集し易い特性をもつ炭素繊維の単繊維同
志が分散混合に際して互に接触して凝集を起こさ
ないようにするため、.粒径0.1μ〜1μ程度のシ
リカヒユーム等のサブミクロン微粉体或は同径程
度の微細繊維を1本1本のモノフイラメントの表
面に吸着させ各繊維間に介在させた、凝集防止処
理を施した乾状態の炭素短繊維原材料と上記成型
品原材料粉体とを混合させること、更に上記製造
方法として.炭素短繊維小塊又はチヨツプ状の
短繊維を1本1本の炭素短繊維に分散しつつ、粒
径0.1μ〜1μ程度のシリカヒユーム等のサブミクロ
ン微粉体或は同径程度の微細繊維が霧状に拡散し
ているミキサー中に逐次投入し、各炭素短繊維の
モノフイラメントの表面にサブミクロン微粉体或
は同径程度の微細繊維を吸着介在させたことを特
徴とする凝集防止処理を施した乾状態の炭素短繊
維原材料の製造方法。.炭素短繊維小塊又はチ
ヨツプ状短繊維を1本1本の炭素短繊維に分散し
つつ、粒径0.1μ〜1μ程度のシリカヒユーム等のサ
ブミクロン微粉体或は同径程度の微細繊維を前記
各炭素短繊維のモノフイラメントの表面に逐次吹
きつけて吸着させ各繊維間に介在させたことを特
徴とする凝集防止処理を施した乾状態の炭素短繊
維原材料の製造方法。.炭素短繊維小塊又はチ
ヨツプ状短繊維と粒径0.1μ〜1μ程度のシリカヒユ
ーム等のサブミクロン微粉体或は同径程度の微細
繊維とを混合した状態で繊維の分散と同時に、各
炭素短繊維1本1本のモノフイラメントの表面に
サブミクロン微粉体或は同径程度の微細繊維を吸
着介在させることを特徴とする凝集防止処理を施
した乾状態の炭素短繊維原材料の製造方法を提案
した。そして、更に前記発明による特公昭62−
58886号公報に示す繊維分散装置の問題点を解決
する方法及び手段として、.短繊維の凝集体を
1対のベルトコンベアー等の移送装置間を通して
表面に多数の小突起を有する回転体の略中心方向
に強制供給し、該移送装置先端部で挟着保持され
た凝集体を回転体表面の多数の小突起でかきとら
れ単繊維状に分散させる如くした短繊維の凝集体
を単繊維状に分散させる方法。.多数の小突起
を有する回転体の略中心に向けて1対のベルトコ
ンベアー等の移送装置を配設し、短繊維の凝集体
を該移送装置に供給する装置を有し、前記移送装
置の先端部に於いて強制移送される凝集体が挟着
保持され乍ら送り出される手段を備えた短繊維の
凝集体を単繊維状に分散させる装置を提案した。
(Prior art) The present applicant previously developed a device (Japanese Patent Publication No. 1983-1983-1) for dispersing small pieces or chop-shaped short fibers of short carbon fibers one by one.
(see Publication No. 58886). Then, the short carbon fibers dispersed by this fiber dispersion device are uniformly dispersed and mixed into the raw materials for molded products such as cement and refractories, and the carbon fiber single fibers, which tend to aggregate easily, come into contact with each other during dispersion and mixing. In order to prevent agglomeration from occurring. Submicron fine powder such as silica fume with a particle size of about 0.1μ to 1μ or fine fibers of about the same diameter are adsorbed onto the surface of each monofilament and interposed between each fiber to prevent agglomeration. The above manufacturing method includes mixing the dry short carbon fiber raw material and the above-mentioned molded product raw material powder. While carbon short fiber small lumps or chop-shaped short fibers are dispersed into individual short carbon fibers, submicron fine powder such as silica hume with a particle size of about 0.1μ to 1μ or fine fibers with the same diameter are atomized. The short carbon fibers are sequentially introduced into a mixer where they are dispersed, and subjected to agglomeration prevention treatment characterized by adsorbing and intervening submicron fine powder or fine fibers of approximately the same diameter on the surface of each short carbon monofilament. A method for producing dry short carbon fiber raw material. .. While dispersing carbon short fiber small lumps or choppy short fibers one by one into individual short carbon fibers, submicron fine powder such as silica hume with a particle size of about 0.1μ to 1μ or fine fibers with about the same diameter are added to each of the above. A method for producing a dry carbon short fiber raw material subjected to an agglomeration prevention treatment characterized by successively spraying onto the surface of a monofilament of carbon short fibers, adsorbing the fibers, and interposing them between each fiber. .. At the same time as the fibers are dispersed, each short carbon fiber is mixed with a submicron fine powder such as silica hume with a particle size of about 0.1μ to 1μ or a fine fiber with the same diameter. We proposed a method for producing dry carbon short fiber raw material that has been subjected to agglomeration prevention treatment, which is characterized by adsorbing submicron fine powder or fine fibers of about the same diameter on the surface of each monofilament. . Furthermore, the above-mentioned patent publication No. 62-
As a method and means for solving the problems of the fiber dispersion device shown in Publication No. 58886. Aggregates of short fibers are forcibly fed approximately toward the center of a rotating body that has many small protrusions on its surface through a pair of transfer devices such as belt conveyors, and the aggregates held in place at the tip of the transfer device are A method for dispersing aggregates of short fibers into single fibers, which are scraped off by a large number of small protrusions on the surface of a rotating body and dispersed into single fibers. .. A transfer device such as a pair of belt conveyors is disposed approximately toward the center of a rotating body having a large number of small protrusions, and a device for supplying aggregates of short fibers to the transfer device is provided. We have proposed an apparatus for dispersing short fiber aggregates into single fibers, which is equipped with a means for holding the aggregates forcedly transferred at the same time as sending them out.

(発明が解決しようとする問題点) 然るに、上記従来技術にあつては,の方法
及び装置によりの凝集防止処理を施した乾状態
の炭素短繊維原材料を製造しても、セメント又は
耐火物等の成型品原材料中に均一に分散混合させ
るため、それらを混合ミキサー中に投入して攪拌
する際に、 (1) 繊維径が比較的細く単位当り量の比容積が嵩
高の場合 (2) 繊維径が比較的長く単位当り量の比容積が嵩
高の場合 (3) 成型品原材料に比較して繊維混入量が多い場
合 には短繊維は回転運動を与えられる事によつて造
粒化しがちになり、分散に問題が生じる恐れを有
していた。この条件をクリアーするためには、
に於けるシリカヒユーム等のサブミクロン微粉体
或は微細繊維の添加量を増加させることによつて
或程度の調整は可能であるが、それら微粉体等の
添加量はセメント又は耐火物等の成型品原材料に
比較し原界を超えると強度低下等の影響が生じ自
ずから一定の制約を受けざるを得なかつたし、更
に前項の方法により短繊維と微粉体或は微細繊
維とを予め混合する際にも、その方法によつては
上記のミキシングによる造粒化の傾向が懸念され
ていた。又、による乾状態の炭素短繊維とセメ
ント或は耐火物等の成型品原材料とを、ミキサー
により混合するため、ミキサー容量に従つたバツ
チ方式を取らざるを得ず、製造効率からいつても
連続製造方式による方法が優ることは論を持たな
いところである。
(Problems to be Solved by the Invention) However, in the above-mentioned prior art, even if dry carbon short fiber raw materials are produced after being subjected to agglomeration prevention treatment using the method and apparatus described above, cement, refractories, etc. In order to uniformly disperse and mix the raw materials for molded products, when putting them into a mixer and stirring them, (1) the fiber diameter is relatively small and the specific volume per unit is bulky; (2) the fibers When the diameter is relatively long and the specific volume per unit is bulky (3) When the amount of fiber mixed in is large compared to the raw material of the molded product, short fibers tend to granulate due to rotational motion. Therefore, there was a risk that problems would arise in dispersion. In order to clear this condition,
It is possible to make some adjustment by increasing the amount of submicron fine powder such as silica hume or fine fibers added, but the amount of these fine powders etc. Compared to the raw material, exceeding the original limit causes effects such as a decrease in strength, which inevitably necessitates certain restrictions. However, depending on the method, there was a concern about the tendency of granulation due to the above-mentioned mixing. In addition, since dry short carbon fibers and raw materials for molded products such as cement or refractories are mixed in a mixer, it is necessary to use a batch method according to the capacity of the mixer. There is no argument that the manufacturing method is superior.

(問題点を解決するための手段) 本発明は上記種々の問題点を解決することを目
的とし、短繊維の凝集体を該原材料定量供給装
置により、1対のベルトコンベアー等の移送装置
間を通して表面に多数の小突起を有する第1の回
転体の略中心方向に定量連続強制供給し、該移送
装置先端部で挟着保持された凝集体を該回転体表
面の多数の小突起でかきとりモノフイラメント状
に分散し、第1の回転体の高速回転により生ずる
強力な空気流に従つて、回転方向先端部に行くに
つれて拡開した通路内で拡散混合し乍ら前方に設
置された表面に多数の小突起を有する第2の回転
体の表面に吹き付けると共に、粉体を第2の回転
体上部に配設した粉体定量供給装置により、第2
の回転体表面に定量連続供給し第2の回転体の高
速回転により生ずる空気流に従つて飛散させるこ
とにより、モノフイラメント状になつた短繊維と
粉体とを連続的に混合する方法。多数の小突起
を有する第1の回転体の略中心に向けて1対のベ
ルトコンベアー等の移送装置を配設し、短繊維の
凝集体を該原材料定量供給装置により該移送装置
間に定量連続供給する装置を有し、前記移送装置
先端部に於いて強制移送される凝集体が挟着保持
され乍ら送り出される手段を備え、且つ前記回転
体の回転方向先端部に行くに従つて通路を拡開し
前方に表面に多数の小突起を有する第2の回転体
を設置し、その上部に粉体の定量連続供給が可能
な粉体定量供給装置を有する短繊維の凝集体をモ
ノフイラメント状に分散し併せて該短繊維と粉体
とを連続的に混合する装置を特徴とするものであ
る。
(Means for Solving the Problems) The present invention aims to solve the various problems mentioned above, and aims to pass short fiber aggregates between a pair of transfer devices such as a belt conveyor using the raw material quantitative supply device. A fixed amount of water is continuously forcibly fed toward the approximate center of a first rotating body having a large number of small protrusions on its surface, and the aggregates held by the tip of the transfer device are scraped off by the large number of small protrusions on the surface of the rotating body. They are dispersed in a filament shape, and are diffused and mixed in a passageway that widens toward the tip in the direction of rotation according to the strong air flow generated by the high-speed rotation of the first rotating body. The powder is sprayed onto the surface of the second rotating body having small protrusions, and the powder is sprayed onto the surface of the second rotating body, and the powder is sprayed onto the surface of the second rotating body.
A method of continuously mixing monofilament-shaped short fibers and powder by continuously supplying a fixed amount onto the surface of a second rotating body and scattering the powder according to the air flow generated by the high speed rotation of a second rotating body. A transfer device such as a pair of belt conveyors is disposed approximately toward the center of a first rotating body having a large number of small protrusions, and aggregates of short fibers are continuously and quantitatively fed between the transfer devices by the raw material quantitative supply device. a feeding device, a means for feeding the aggregates forcibly transferred at the tip of the transfer device while being pinched and held, and a passageway extending toward the tip in the rotational direction of the rotating body. A second rotary body with a large number of small protrusions on the surface is installed in front of the expanded body, and a powder metering device capable of continuously supplying powder at a fixed rate is installed on the top of the second rotating body. The invention is characterized by an apparatus that continuously mixes the short fibers and the powder together with the short fibers.

(作用) 本発明は3〜25mm程度の短繊維凝集体を、該原
材料収納用ホツパー下部に設置された定量供給装
置により1対のベルトコンベアー等移送装置間に
定量連続強制供給し、該移送装置先端部に於いて
凝集体を挟着保持し乍ら第1の回転体表面の多数
の小突起でかきとられモノフイラメント状に分散
されつつ第2の回転体表面に吹付け、第2の回転
体はその上部に配設された粉体定量供給装置によ
り粒径0.1μ〜1μ程度のシリカヒユーム等の無機質
微粉体又は径0.01μ〜1μ程度の石綿テーリング等
の無機質微細繊維が該表面に定量連続供給され、
回転する表面の小突起により飛散し第1の回転体
から吹付けられてくるモノフイラメント状になつ
た短繊維と連続的に混合され乍ら後方へ排出され
る。この際、上記移送装置の移送速度及び粉体定
量供給装置による単位時間当りの供給量は目的仕
様に合せて夫々調整が可能になつており、又、場
合によつて上記微粉体等は移送装置により移送さ
れる凝集体原材料の表面から定量連続供給し、第
2の回転体上部の粉体定量供給装置からはセメン
ト或は耐火物等成型品原材料の粉体を連続チヤー
ジすることも、更に第2の回転体の回転方向前方
に同形の第3の回転体を設置し、第2の回転体上
部からは上記微粉体等を第3の回転体上部からは
成型品原材料の粉体の連続供給を行つてもよい
し、該原材料粉体の種類が複数のときは予め混合
し供給してもよい。かくして短繊維凝集体はモノ
フイラメント状となり、微粉体更に成型品原材料
粉体と均一に混合され長時間の連続加工製造を行
うことができる。
(Function) The present invention continuously forcibly supplies short fiber aggregates of about 3 to 25 mm between a pair of transfer devices such as a belt conveyor by a fixed amount supply device installed at the bottom of the raw material storage hopper. While holding the aggregate at the tip, it is scraped off by a large number of small protrusions on the surface of the first rotating body and dispersed in a monofilament shape, and then sprayed onto the surface of the second rotating body. The powder metering device installed on the top of the body continuously supplies a fixed amount of inorganic fine powder such as silica fume with a particle size of about 0.1μ to 1μ or inorganic fine fibers such as asbestos tailings with a diameter of about 0.01μ to 1μ on the surface. supplied,
The short fibers are scattered by small protrusions on the rotating surface and are discharged to the rear while being continuously mixed with monofilament-shaped short fibers blown from the first rotating body. At this time, the transfer speed of the above-mentioned transfer device and the supply amount per unit time by the powder quantitative supply device can be adjusted respectively according to the target specifications, and in some cases, the above-mentioned fine powder, etc. It is also possible to continuously supply a fixed amount from the surface of the aggregate raw material transferred by the second rotating body, and to continuously charge the powder of the raw material for molded products such as cement or refractory from the powder fixed quantity supply device on the upper part of the second rotating body. A third rotary body of the same shape is installed in front of the second rotary body in the rotational direction, and the above-mentioned fine powder, etc. is continuously supplied from the upper part of the second rotary body, and powder of molded product raw material is continuously supplied from the upper part of the third rotary body. Alternatively, when there are a plurality of types of raw material powder, they may be mixed in advance and supplied. In this way, the short fiber aggregate becomes a monofilament, which is uniformly mixed with the fine powder and the molded product raw material powder, allowing continuous processing and manufacturing over a long period of time.

(実施例) 以下、第1図に示した実施例に基づいて具体的
に説明する。1,14は表面に多数の針状突起
2,15を突設した円筒形の第1,第2の回転ド
ラムで夫々直径400mm、980,750r.p.mで矢印方向
に回転している。3は3〜25mm程度にカツトされ
たピツチ系炭素短繊維或はアラミド短繊維の凝集
体原材料、4は該原材料収納用ホツパー、5,
5′はホツパー4の下部に設けられた1対の原材
料定量供給用回転部材で夫々矢印方向に回転し、
回転速度の可変により供給量を増減なし得る機構
になつており、6は略々水平状に配設された原材
料移送供給用ベルトコンベアーで矢印方向に可動
し、ガイドローラー7,8より先端は第1の回転
ドラム1の中心に向けられ、該垂直部6′先端と
針状突起2とは僅かの間隙を設けられている。9
は前記垂直部6′と略々平行に配設された喰込用
ベルトコンベアーで矢印方向に可動し、その先端
ガイドローラー10は側面に配設されたスプリン
グによつてベルトコンベアー6の垂直部6′先端
のガイドローラー11に向つて常時押圧されてい
る。12はガイドローラー8上方に水平に配設し
た補助ベルトコンベアーで矢印方向に可動してい
る。13はケーシングでベルトコンベアー6の垂
直部6′先端より第1の回転ドラム1の回転方向
に沿つて巻回配設され、第1の回転ドラム1との
間隔が次第に広くなる構造になつており、第2の
回転ドラム14下部も同様で、且つ垂直方向上下
にスライドし間隔調整がなし得るようになつてい
る。16は粉体用ホツパー、17は粒径0.1μ〜1μ
程度のシリカヒユームの無機質粉体又は径0.01μ
〜1μ程度の石綿テーリングの無機質微細繊維、
18は粉体用ホツパー16下部に水平状に配設さ
れた粉体供給用ベルトコンベアーで矢印方向に移
送しうる様になつており、その上面と粉体用ホツ
パー16の下部とは僅かの間隔が設けられ、且つ
間隙の調整により粉体量の増減が可能になつてい
る。
(Example) Hereinafter, a detailed explanation will be given based on the example shown in FIG. Reference numerals 1 and 14 denote first and second rotating drums each having a diameter of 400 mm and rotating in the direction of the arrow at 980 and 750 rpm, respectively, each having a large number of needle-like protrusions 2 and 15 protruding from their surfaces. 3 is an aggregate raw material of pitch-based short carbon fibers or aramid short fibers cut to about 3 to 25 mm; 4 is a hopper for storing the raw material; 5;
Reference numeral 5' denotes a pair of rotary members for quantitative supply of raw materials provided at the bottom of the hopper 4, each rotating in the direction of the arrow.
The mechanism is such that the supply amount can be increased or decreased by varying the rotational speed, and reference numeral 6 is a belt conveyor for transferring and supplying raw materials that is arranged approximately horizontally and moves in the direction of the arrow. 1, and a small gap is provided between the tip of the vertical portion 6' and the needle-like protrusion 2. 9
is movable in the direction of the arrow by a biting belt conveyor disposed approximately parallel to the vertical portion 6', and its tip guide roller 10 is moved by the vertical portion 6 of the belt conveyor 6 by a spring disposed on the side surface. 'It is constantly pressed toward the guide roller 11 at the tip. Reference numeral 12 denotes an auxiliary belt conveyor disposed horizontally above the guide roller 8 and movable in the direction of the arrow. Reference numeral 13 denotes a casing, which is wound along the rotational direction of the first rotating drum 1 from the tip of the vertical portion 6' of the belt conveyor 6, and has a structure in which the distance between the casing and the first rotating drum 1 gradually increases. Similarly, the lower part of the second rotating drum 14 can be slid vertically up and down to adjust the spacing. 16 is a hopper for powder, 17 is a particle size of 0.1μ to 1μ
Inorganic powder of silica hume or diameter 0.01μ
~1μ inorganic fine fibers with asbestos tailings,
Reference numeral 18 denotes a powder supply belt conveyor which is arranged horizontally below the powder hopper 16 so that it can be transferred in the direction of the arrow, and there is a slight distance between its upper surface and the lower part of the powder hopper 16. is provided, and the amount of powder can be increased or decreased by adjusting the gap.

19は粉体供給用円筒形回転ドラム直径150mm、
250r.p.mで矢印方向に回転しその円周部には長手
方向にスリツトを設け、ベルトコンベアー18の
端部より落下されてくる粉体との摩擦抵抗を大に
し、第2の回転ドラム14表面の針状突起15に
供給し易い構造になつている。
19 is a cylindrical rotating drum for powder supply with a diameter of 150 mm;
It rotates at 250 rpm in the direction of the arrow, and its circumferential portion is provided with slits in the longitudinal direction to increase the frictional resistance with the powder falling from the end of the belt conveyor 18. It has a structure that allows easy supply to the needle-like protrusion 15 of.

次に作用について説明する。原材料収納用ホツ
パー4の下部に設置された定量供給用回転部材
5,5′の間から原材料移送供給用ベルトコンベ
アー6上に定量連続供給された原材料3は補助ベ
ルトコンベアー12に上方を押えられ、ベルトコ
ンベアー6の垂直部6′と喰込用ベルトコンベア
ー9間に上方より送り込まれた両者間を強制移送
され、先端にあるガイドローラー10,11より
挟着保持され乍ら送り出され、第1の回転ドラム
1の針状突起2により掻きとられモノフイラメン
ト状に分散される。分散された単繊維は第1の回
転ドラム1の回転により生ずる強力な空気の流れ
により、次第に広がつているケーシング13との
空隙間を通過し、次第に体積が膨張してより一層
単繊維化が促進され乍ら、第2の回転ドラム14
の表面に突設された針状突起15に吹付けられ
る。この際、第1、第2の回転ドラム1,14の
周速度に夫々差異があるため単繊維化は一段と増
進され、更に第2の回転ドラム上部より落下し飛
散される無機質粉体又は無機質微細繊維17と均
一且つ連続的に混合され乍ら後方へ排出される。
斯くの如く、短繊維凝集体原材料3の定量供給用
回転部材5,5′による供給量、原材料供給用ベ
ルトコンベアー6の供給速度、及び無機質微粉体
等17の供給量を仕様に基づき当初夫々調整を行
うことにより、カーボン、アラミド等短繊維が乾
状態で高い混入率をもつて均一に混入されたドラ
イコンパウンドを連続的に加工製造することが可
能となる。
Next, the effect will be explained. The raw material 3 is continuously supplied in a quantitative manner onto the raw material transfer and supply belt conveyor 6 from between the quantitative supply rotary members 5 and 5' installed at the lower part of the raw material storage hopper 4, and is pressed upward by the auxiliary belt conveyor 12. It is forcibly transferred between the vertical part 6' of the belt conveyor 6 and the biting belt conveyor 9 from above, and is sent out while being pinched and held by the guide rollers 10 and 11 at the tip. It is scraped off by the needle-like protrusions 2 of the rotating drum 1 and dispersed into monofilaments. Due to the strong air flow generated by the rotation of the first rotating drum 1, the dispersed single fibers pass through the gap between the casing 13 and the casing 13, which gradually expands in volume, and are further made into single fibers. While being promoted, the second rotating drum 14
The liquid is sprayed onto needle-like protrusions 15 protruding from the surface. At this time, since the circumferential speeds of the first and second rotating drums 1 and 14 are different, the formation of single fibers is further promoted, and the inorganic powder or inorganic fine particles that fall from the upper part of the second rotating drum and are scattered. It is uniformly and continuously mixed with the fibers 17 and discharged to the rear.
As described above, the supply amount of the short fiber aggregate raw material 3 by the rotating members 5, 5' for quantitative supply, the supply speed of the raw material supply belt conveyor 6, and the supply amount of the inorganic fine powder, etc. 17 are initially adjusted respectively based on the specifications. By doing this, it becomes possible to continuously process and manufacture a dry compound in which short fibers such as carbon and aramid are uniformly mixed at a high mixing rate in a dry state.

〔成型品原材料と混合する場合の一実施例〕[An example of mixing with molded product raw materials]

1 (1) ピツチ系炭素短繊維(長さ20mm)
3%(重量比) (2) 無機質微粉体(シリカヒユーム、粒径0.1μ〜
1μ) 9%( 〃 ) (3) セメント 60%( 〃 ) (4) 骨材(炭素カルシユーム粉)(粒度調整 粒
径20μ〜200μ) 28%( 〃 ) 2 (1) ピツチ系カーボン短繊維(長さ3mm)
3.8%(重量比) (2) アラミド短繊維(長さ3mm)
3.8%( 〃 ) (3) 無機質微細繊維(石綿テーリング、径0.01μ
〜1μ) 15.4%( 〃 ) (4) フエノール樹脂粉末 7.0%( 〃 ) (5) 炭酸カルシユーム粉(粒度調整 粒径10μ〜
120μ) 70.0%( 〃 ) (効果) 本発明はカーボン、アラミド等各種短繊維の凝
集体を該原材料定量供給装置により、円筒形の外
周部表面に多数の細かい突起が小間隔を置いて立
設され一定方向に回転する第1の回転体の表面の
任意の位置より、該回転体の中心に向けて設置さ
れたベルトコンベアー等の供給移送装置上に定量
連続供給し、1対のベルトコンベアー等の供給移
送装置の間を通しつつ強制供給を行ない、供給原
材料を供給移送装置先端部で強固に保持し乍ら第
1の回転体表面の細かい突起による可動部材とに
より、上記凝集体をモノフイラメント状に分散し
つつ第2の回転体表面に吹付け、該回転体上部よ
り連続的に定量づつ落下し飛散する無機質微粉
体、無機質微細繊維或はセメント等成型品原材料
粉体と均一且つ連続的に混合なし得ることを特徴
とした短繊維の凝接集体をモノフイラメント状に
分散すると同時に、粉体と均一且つ連続的に混合
する方法及び装置を要旨としているので、従来技
術による分散方法、装置に比較し次の様な長所を
有している。
1 (1) Pitch-based short carbon fiber (length 20mm)
3% (weight ratio) (2) Inorganic fine powder (silica hume, particle size 0.1μ ~
1μ) 9% (〃) (3) Cement 60% (〃) (4) Aggregate (carbon calcium powder) (particle size adjustment particle size 20μ to 200μ) 28% (〃) 2 (1) Pitch-based short carbon fiber ( length 3mm)
3.8% (weight ratio) (2) Aramid staple fiber (length 3mm)
3.8% (〃 ) (3) Inorganic fine fiber (asbestos tailing, diameter 0.01μ
~1μ) 15.4% (〃) (4) Phenol resin powder 7.0% (〃) (5) Calcium carbonate powder (particle size adjustment particle size 10μ~
120μ) 70.0% (〃) (Effects) The present invention uses aggregates of various short fibers such as carbon and aramid to form a large number of fine protrusions erected at small intervals on the cylindrical outer peripheral surface using the raw material quantitative supply device. A fixed amount is continuously supplied from any position on the surface of a first rotating body rotating in a constant direction onto a supply transfer device such as a belt conveyor installed toward the center of the rotating body, and a pair of belt conveyors etc. The raw material is forcibly fed through the feeding and transferring device, and while the raw material is firmly held at the tip of the feeding and transferring device, the agglomerate is turned into a monofilament by a movable member formed by fine protrusions on the surface of the first rotating body. The powder is sprayed on the surface of the second rotating body while being dispersed in a uniform manner, and is uniformly and continuously with the inorganic fine powder, inorganic fine fibers, cement, etc. raw material powder for molded products, which falls continuously in fixed amounts from the top of the rotating body and scatters. The gist of the present invention is a method and apparatus for dispersing an aggregate of short fibers into a monofilament shape, and at the same time uniformly and continuously mixing it with powder, so that the dispersion method and apparatus according to the prior art can be used. It has the following advantages compared to

(1) 凝集防止処理を施した乾状態の炭素短繊維の
製造が容易なこと。
(1) It is easy to produce dry short carbon fibers that have been treated to prevent agglomeration.

(2) 短繊維の凝集体とセメント及び耐火物等粉体
とのドライブレンドが容易なこと。
(2) Easy dry blending of short fiber aggregates and powders such as cement and refractories.

(3) 短繊維が高混入率のとき、或は繊維長が長く
嵩高の場合のブレンドが容易なこと。
(3) Easy blending when a high proportion of short fibers is mixed, or when the fiber length is long and bulky.

(4) 従来のバツチ方式と異なり連続加工方式がと
ることが出来るので高能率なこと。
(4) Unlike the conventional batch method, it is highly efficient because it can use a continuous processing method.

又、本発明による方法及び装置により得られた
凝集防止処理を施した乾状態のカーボン、アラミ
ド炭繊維原材料が使用され、更にセメント及び耐
火物等粉体と高い混入率をもつこれ等短繊維のド
ライコンパウンドが多方面に渡り利用されること
によつて、カーボン、アラミド短繊維等将来の可
能性を有する新素材の用途開発が社会的により一
層促進されることは確実である。
In addition, dry carbon and aramid carbon fiber raw materials subjected to agglomeration prevention treatment obtained by the method and apparatus of the present invention are used, and furthermore, these short fibers having a high mixing rate with powders such as cement and refractories are used. It is certain that the use of dry compounds in a wide range of fields will further promote the development of new materials with future potential, such as carbon and short aramid fibers.

【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正面図である。 1,14……第1回転ドラム、第2回転ドラ
ム、2,15……針状突起、3……短繊維凝集体
原材料、4……原材料収納用ホツパー、5,5′
……原材料定量供給用回転部材、6,6′……原
材料移送供給用ベルトコンベアー、7,8,1
0,11……ガイドローラー、9……喰込用ベル
トコンベアー、12……補助ベルトコンベアー、
13……ケーシング、16……粉体収納用ホツパ
ー、17……無機質微粉体又は無機質微細繊維、
18……粉体供給用ベルトコンベアー、19……
粉体供給用回転ドラム。
FIG. 1 is a front view of one embodiment of the apparatus of the present invention. 1, 14...First rotating drum, second rotating drum, 2, 15... Needle-like protrusion, 3... Short fiber aggregate raw material, 4... Hopper for storing raw material, 5, 5'
... Rotating member for quantitative supply of raw materials, 6, 6' ... Belt conveyor for transferring and supplying raw materials, 7, 8, 1
0, 11... Guide roller, 9... Belt conveyor for biting, 12... Auxiliary belt conveyor,
13...Casing, 16...Hopper for storing powder, 17...Inorganic fine powder or inorganic fine fiber,
18... Belt conveyor for powder supply, 19...
Rotating drum for powder supply.

Claims (1)

【特許請求の範囲】 1 短繊維の凝集体を該原材料定量供給装置によ
り、1対のベルトコンベアー等の移送装置間を通
して表面に多数の小突起を有する第1の回転体の
略中心方向に定量連続強制供給し、該移送装置先
端部で挟着保持された凝集体を該回転体表面の多
数の小突起でかきとりモノフイラメント状に分散
し、第1の回転体の高速回転により生ずる強力な
空気流に従つて、回転方向先端部に行くにつれて
拡開した通路内で拡散混合し乍ら前方に設置され
た表面に多数の小突起を有する第2の回転体の表
面に吹付けると共に、粉体を第2の回転体上部に
配設した粉体定量供給装置により、第2の回転体
表面に定量連続供給し第2の回転体の高速回転に
より生ずる空気流に従つて飛散させることによ
り、モノフイラメント状になつた短繊維と粉体と
を連続的に混合する方法。 2 多数の小突起を有する第1の回転体の略中心
に向けて1対のベルトコンベアー等の移送装置を
配設し、短繊維の凝集体を該原材料定量供給装置
により該移送装置間に定量連続供給する装置を有
し、前記移送装置先端部に於いて強制移送される
凝集体が挟着保持され乍ら送り出される手段を備
え、且つ、前記回転体の回転方向先端部に行くに
従つて通路を拡開し前方に表面に多数の小突起を
有する第2の回転体を設置し、その上部に粉体の
定量連続供給が可能な粉体定量供給装置を有する
短繊維の凝集体をモノフイラメント状に分散し併
せて該短繊維と粉体とを連続的に混合する装置。
[Scope of Claims] 1. The aggregate of short fibers is passed between a pair of belt conveyors or other transfer devices by the raw material quantitative supply device in a direction approximately toward the center of a first rotating body having a large number of small protrusions on its surface. The agglomerates held at the tip of the transfer device are scraped off by a large number of small protrusions on the surface of the rotary body and dispersed in a monofilament shape, using strong air generated by high-speed rotation of the first rotary body. According to the flow, the powder is diffused and mixed in a passage that widens toward the tip in the direction of rotation, and is sprayed onto the surface of a second rotating body that has many small protrusions on the surface installed in the front. A fixed amount of powder is continuously supplied to the surface of the second rotary body by a powder quantitative supply device disposed above the second rotary body, and the powder is dispersed according to the air flow generated by the high speed rotation of the second rotary body. A method of continuously mixing filament-shaped short fibers and powder. 2. A pair of transfer devices such as belt conveyors are arranged approximately toward the center of the first rotating body having a large number of small protrusions, and aggregates of short fibers are fixedly distributed between the transfer devices by the raw material quantitative supply device. a continuous supply device, a means for feeding out the aggregates forcibly transferred at the tip of the transfer device while being pinched and held; A second rotating body with a large number of small protrusions on the surface is installed in front of the passage to widen the passage, and a powder metering device capable of continuously supplying powder at a fixed rate is installed on top of the second rotating body. A device that continuously mixes the short fibers and powder by dispersing them into filaments.
JP63193652A 1988-08-03 1988-08-03 Continuously mixing method and device of powder with short fiber aggregate by dispersing in state of monofilament Granted JPH0243006A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63193652A JPH0243006A (en) 1988-08-03 1988-08-03 Continuously mixing method and device of powder with short fiber aggregate by dispersing in state of monofilament

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63193652A JPH0243006A (en) 1988-08-03 1988-08-03 Continuously mixing method and device of powder with short fiber aggregate by dispersing in state of monofilament

Publications (2)

Publication Number Publication Date
JPH0243006A JPH0243006A (en) 1990-02-13
JPH0550965B2 true JPH0550965B2 (en) 1993-07-30

Family

ID=16311508

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63193652A Granted JPH0243006A (en) 1988-08-03 1988-08-03 Continuously mixing method and device of powder with short fiber aggregate by dispersing in state of monofilament

Country Status (1)

Country Link
JP (1) JPH0243006A (en)

Also Published As

Publication number Publication date
JPH0243006A (en) 1990-02-13

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