JPH03279483A - Papermaking disaggregation machine also used as duster - Google Patents

Papermaking disaggregation machine also used as duster

Info

Publication number
JPH03279483A
JPH03279483A JP2071988A JP7198890A JPH03279483A JP H03279483 A JPH03279483 A JP H03279483A JP 2071988 A JP2071988 A JP 2071988A JP 7198890 A JP7198890 A JP 7198890A JP H03279483 A JPH03279483 A JP H03279483A
Authority
JP
Japan
Prior art keywords
raw material
chamber
foreign matter
screen
recovery chamber
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
JP2071988A
Other languages
Japanese (ja)
Inventor
Yoshihiko Aikawa
相川 叔彦
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.)
Aikawa Iron Works Co Ltd
Original Assignee
Aikawa Iron Works Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Aikawa Iron Works Co Ltd filed Critical Aikawa Iron Works Co Ltd
Priority to JP2071988A priority Critical patent/JPH03279483A/en
Publication of JPH03279483A publication Critical patent/JPH03279483A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/64Paper recycling

Abstract

PURPOSE:To increase purifying treating power, dusting ability and disaggregating ability by providing a closed casing with a screen and impeller in a specific state and dividing a fiber recovery chamber into a fine selecting chamber and a coarsely selecting chamber. CONSTITUTION:A closed casing 3 provided with a raw material feed opening 1 and a foreign matter outlet 2 is equipped with a screen 4 and divided into a fiber recovery chamber 6 and a foreign matter recovery chamber 5. An impeller 7 is rotatably set at the side of the foreign matter recovery chamber close to the screen 4, part at the outer peripheral side of the screen is made into a finely selecting part 41 and part at the inner peripheral side into a coarsely selecting part 42, which are made to correspond to a finely selecting chamber 61 and a coarsely selecting chamber 62 divided by a partition plate 10 and the chambers are provided with outlets 8 and 9, respectively.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、新生パルプ生産処理、損紙処理又は新聞、雑
誌等の故紙処理において、未離解片、異物、例えば金属
片9石、プラスチック片、スチロール片、ビニール片を
含む製紙用原料を処理し、粗大異物を優先して系外に排
棄すると共に、未離解片の離解作用を行うリジェクト処
理のための製紙用離解兼除塵機に関するものである。
Detailed Description of the Invention [Industrial Application Field] The present invention is applicable to the production of new pulp, waste paper processing, or waste paper processing such as newspapers and magazines. , related to a paper disintegration and dust removal machine for processing papermaking raw materials including styrofoam pieces and vinyl pieces, discarding coarse foreign matter from the system with priority, and disintegrating undisintegrated pieces. It is.

〔従来の技術〕[Conventional technology]

従来、新生パルプ生産処理・損紙処理・古紙処理など製
紙用設備においては原料となる繊維懸濁液中の未離解片
を離解し、かつ石、砂、金属片、樹脂片などの異物その
他のごみ排除のために用いられる各種分離機のりジェツ
トはスクリーンで処理されるのが一般的である。
Conventionally, in paper manufacturing equipment such as new pulp production processing, waste paper processing, and waste paper processing, undisintegrated pieces in the raw material fiber suspension are disintegrated, and foreign substances such as stones, sand, metal pieces, resin pieces, etc. Glue jets from various separators used for waste removal are generally treated with screens.

しかし、このリジェクト中には異物とともに多量の未離
解片が含まれているために、スクリーンは比較的大きな
孔径として未離解繊維分の回収を計っているが、スクリ
ーンを大孔径とすると、必熱的に異物も、また出口原料
側に通過するので分離能力不足となる傾向があって問題
であった。この場合、リジェクト処理系内の異物循環を
防止し、品質、マシン操業性を向上させるためにはスク
リーンの孔径を出来るだけ小さくすべきであることは言
うまでもないが、小孔径のスクリーンを使用することに
より、異物排出の際に排棄される有用繊維分の損失が大
きく、歩留低下の問題が発生する。
However, since this reject contains a large amount of undisaggregated fibers as well as foreign substances, the screen is designed to have relatively large pores in order to recover the undisaggregated fibers. However, since foreign matter also passes through to the outlet raw material side, there is a tendency for the separation capacity to be insufficient, which is a problem. In this case, it goes without saying that the pore diameter of the screen should be as small as possible in order to prevent foreign matter circulation within the reject processing system and improve quality and machine operability, but it is also recommended to use a screen with a small pore diameter. As a result, there is a large loss of useful fibers that are discarded during the discharge of foreign matter, resulting in a problem of decreased yield.

一方歩留り低下を防止するため強力なデフレーカーをテ
ールラインに使用すると、異物の破砕が起こり、スクリ
ーンにてこれらの異物を除去することが出来なくなり、
結局品質、マシン操業性に悪影響を及ぼすこととなる。
On the other hand, if a powerful deflaker is used on the tail line to prevent a decrease in yield, foreign matter will be crushed and the screen will not be able to remove these foreign matter.
Eventually, quality and machine operability will be adversely affected.

特に故紙を原料としている設備において、セパレーター
又は丸孔スクリーンをパルパー後の粗選設備として使用
するシステムにおいては多量のテールが排出され、この
テール中から有用繊維を回収するために複雑なシステム
が必要となり、操業不安定の原因となっていた。
Particularly in equipment that uses waste paper as a raw material, systems that use separators or round-hole screens as coarse selection equipment after pulping produce a large amount of tail, and a complex system is required to recover useful fibers from this tail. This caused operational instability.

このため、最近ではテール中から有用繊維を回収するた
めに離解能力と除塵能力とを合せ持つリジェクト処理機
が必要とされるようになって来ている。
For this reason, recently there has been a need for a reject processor that has both disintegration ability and dust removal ability in order to recover useful fibers from the tail.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

ところが、この従来のシステム処理機では径の孔を穿設
したスクリーンに近接されてインペラが回転自在に設け
であるタイプが多く、このためインペラのロータブレー
ドの内周側と外周側とでは周速が異なって除塵効果に違
いが生して品質が低下する。即ち、インペラの外周より
内周が遅い回転速度となるため除塵程度の格差が生しる
おそれが多いし、段ポール故紙、原料のように比較的離
解しにくい原料の場合には離解能力不足となり、そのテ
ール中に未離解片が多く混入していることとなり、排棄
粕中に多量の有用繊維が含まれることとなって粕ととも
に系外に棄てられて歩留りが低下する。
However, in many of these conventional system processing machines, the impeller is rotatably installed in close proximity to a screen with holes of the same diameter. The difference in dust removal effect results in a decrease in quality. In other words, since the rotation speed of the inner circumference of the impeller is slower than that of the outer circumference, there is a risk that there will be a difference in the degree of dust removal, and in the case of raw materials that are relatively difficult to disintegrate, such as corrugated pole waste paper and raw materials, disintegration capacity may be insufficient. , a large amount of undisaggregated pieces are mixed in the tail, and a large amount of useful fibers are included in the waste lees, which are discarded out of the system together with the lees, resulting in a decrease in yield.

特にスクリーンを通過できない未離解片によってスクリ
ーンプレー1・の目孔が詰まって処理能力が低下するほ
か、原料処理時間中に次第に未離解片が滞留してきて、
テールの負荷が上り運転の継続が困難となるし、このた
め必然的に原料処理時間が短くなり、生産量が少なくな
る欠点があった。
In particular, undisaggregated fragments that cannot pass through the screen clog the holes in the screen play 1, reducing processing capacity, and undisaggregated fragments gradually accumulate during the raw material processing time.
The load on the tail increases, making it difficult to continue operation, which inevitably shortens the raw material processing time and reduces production.

本発明は、これら従来の諸欠点を適確に排除しようとす
るもので、インペラによって回流する原料に対し乱流の
生成と、ときほぐし作用とで原料に剪断力を加えて未離
解片の離解を促進させ、原料性状、異物性状によって破
砕程度をも調節でき、リジェクト有用繊維と異物とを分
離する精選処理能力の増大が可能であり、しかも未離解
片の排出が少なく、異物の砕きも少なくして製品品質の
向上に役立つと共に、処理システムは簡素化でき、有用
繊維の回収を大幅に高められる装置を安価な形態で提供
することを目的としたものである。
The present invention aims to accurately eliminate these conventional drawbacks, and aims to disintegrate undisintegrated pieces by applying shearing force to the raw material by generating turbulent flow and loosening action on the raw material being circulated by an impeller. The degree of crushing can be adjusted according to the properties of raw materials and foreign matter, increasing the selection processing capacity for separating useful fibers from rejects and foreign matter, and reducing the amount of undisintegrated fragments and crushing of foreign matter. The purpose of this invention is to provide an inexpensive device that is useful for improving product quality, simplifies the processing system, and greatly increases the recovery of useful fibers.

〔課題を解決するための手段〕[Means to solve the problem]

本発明は、原料供給口と、異物排出口とを備えた密閉ケ
ーシング内に、原料を有用繊維分と不純物の異物分とに
分離するためのスクリーンを設けて繊維回収室と異物回
収室とに区画形成し、該異物回収室側の前記スクリーン
に近接してインペラを回転自在に備え、該スクリーンの
外周部側に小径の孔を設けた精選部と、内周部側に前記
孔より大きい開口面積の大径の孔を設けた粗選部とを備
え、この精選部と粗選部とに対応して繊維回収室が仕切
板で精選室と粗選室とに仕切られ、各室にそれぞれ連通
ずる流出口を設けたことを特徴とする製紙用離解兼除塵
機である。
The present invention provides a fiber recovery chamber and a foreign matter recovery chamber by providing a screen for separating the raw material into useful fiber components and impurity foreign matter components in a sealed casing equipped with a raw material supply port and a foreign matter discharge port. a selective part formed into a partition, rotatably equipped with an impeller close to the screen on the side of the foreign matter collection chamber, a selection part having a small diameter hole on the outer circumferential side of the screen, and an opening larger than the hole on the inner circumferential side. Corresponding to the fine selection section and the rough selection section, the fiber recovery room is divided into a selection room and a rough selection room by a partition plate. This is a disintegrator and dust remover for paper manufacturing, which is characterized by having a communicating outlet.

〔作 用〕[For production]

本発明の製紙用離解兼除塵機では、ケーシング3内に原
料供給口1から送入された原料中の良質繊維はインペラ
7で旋回され、この回転するインペラ7に接近配備され
るスクリーン4の精選部4と粗選部4□とを通過し、仕
切板10で区画された精選室6.と粗選室6、を経て流
出口8,9からそれぞれ次工程に送られる。この精選室
6.の精選部4.を通過できない未離解繊維分は異物回
収室5内においてフラットプレートのスクリーン4上を
回転するインペラ7の衝撃波及びインペラ7とスクリー
ン4との間の摩擦作用及びスクリーン4にある孔(5〜
30鶴φ)を通過する際にインペラ7との衝撃を受は離
解され、繊維回収室6の粗選室6□を経て返送路11で
原料供給口1に戻され、再度インペラ7に対応するスク
リーン4に送られ精選部4、で良を繊維を通過させる。
In the paper-making disintegrator and dust remover of the present invention, high-quality fibers in the raw material fed into the casing 3 from the raw material supply port 1 are rotated by the impeller 7, and carefully selected by the screen 4 disposed close to the rotating impeller 7. A fine selection room 6 which passes through the section 4 and the rough selection section 4□ and is divided by a partition plate 10. and rough selection chamber 6, and are sent to the next process from outlet ports 8 and 9, respectively. This selection room 6. Selected section 4. The undisaggregated fibers that cannot pass through the foreign matter collection chamber 5 are exposed to the shock wave of the impeller 7 rotating on the flat plate screen 4, the friction between the impeller 7 and the screen 4, and the holes (5 to 5) in the screen 4.
When passing through the impeller 7 (30 cranes φ), the fibers are disintegrated by the impact with the impeller 7, passed through the rough sorting chamber 6□ of the fiber recovery chamber 6, and returned to the raw material supply port 1 through the return path 11, where they are returned to the impeller 7 again. The fibers are sent to a screen 4 and passed through a screening section 4.

この作用を繰り返すことにより未離解片はほぐされ、回
収されて次第に少なくなり、原料中の異物はケーシング
3内の異物回収室5に溜まってくるので適宜時に排出流
路の弁14を開いて異物を排出口2から排除すればよい
。いずれにしても、原料は異物回収室5内において撹乱
回流されて、スクリーン4の精選部41から精選室61
にから有用繊維を通過して流し、径の大きい未離解片や
異物は粗選部4□から粗選室6□に通過させ、さらに両
スクリーンから通過せずに残されるものは異物排出口2
から系外へ間歇的に排除されて処理される。
By repeating this action, the undisaggregated pieces are loosened and collected, and the amount gradually decreases, and the foreign matter in the raw material accumulates in the foreign matter collection chamber 5 in the casing 3, so open the valve 14 of the discharge flow path at an appropriate time to remove the foreign matter. should be removed from the discharge port 2. In any case, the raw material is agitated and circulated in the foreign matter recovery chamber 5, and is passed from the screening section 41 of the screen 4 to the screening chamber 61.
Useful fibers are passed through the filter, large-diameter undisaggregated pieces and foreign matter are passed from the rough sorting section 4□ to the rough sorting chamber 6□, and those remaining without passing through both screens are passed through the foreign matter discharge port 2.
It is intermittently removed from the system and processed.

一方スクリーン4のスクリーン面を拭う様に接近させて
回転するインペラ7に対向して精選室6と粗選室6□を
対設配備したことで、送り込まれた原料はその回転方向
の旋回、渦流で乱流を生じさせて原料を離解させスクリ
ーン4を通過できない未離解片などは、インペラ7によ
り遠心力ではね飛ばされときほぐされて離解させながら
遠心力により有用繊維を精選部4.から精選室6.へ通
過させ原料中の粗大異物は異物回収室5の外周壁に飛ば
され、その周壁を旋回しながら下方の排出口2に落下集
合し、導出流路の弁14の間歇的な開閉により排除され
、一方の粗選部4□を通過したを用繊維を含む未離解片
は粗選室68を経て流出口9から返送路11で原料タン
ク12に循環させ、原料移送出管13で原料供給口lに
戻し再処理され、さらに精選室6.に入った有用wIh
維は流出口8の弁の開閉制御でケーシング系外に取り出
され原料として次工程にて処理されるものである。
On the other hand, by arranging the fine sorting chamber 6 and the coarse sorting chamber 6 □ opposite the impeller 7 which rotates close to the screen surface of the screen 4, the raw material fed into the screen undergoes swirling and swirling in the direction of rotation. Undisintegrated pieces that cannot pass through the screen 4 are flung away by centrifugal force by an impeller 7, loosened and disintegrated, and useful fibers are separated by centrifugal force into the sorting section 4. Carefully selected room 6. The coarse foreign matter in the raw material is blown to the outer peripheral wall of the foreign matter recovery chamber 5, falls and collects at the lower discharge port 2 while swirling around the peripheral wall, and is removed by intermittent opening and closing of the valve 14 of the outlet flow path. The undisaggregated pieces containing raw fibers that have passed through the rough sorting section 4□ pass through the rough sorting chamber 68, are circulated from the outlet 9 to the raw material tank 12 via the return path 11, and are transferred to the raw material tank 12 through the raw material transfer outlet pipe 13. It is returned to the room 6. Useful wIh that entered
The fibers are taken out of the casing system by controlling the opening and closing of the valve at the outlet 8 and are processed as raw materials in the next process.

即ち、原料中の未離解片は離解されて残ることが少なく
、異物はスクリーンを通過出来ず次第にケーシングの異
物回収室5内に濃縮され、出口への良質原料通過が妨げ
られてきて、タイマ又はモータの負荷、若しくは出入口
の差圧が予め設定された状態となると大口弁が閉しられ
、洗浄水がケーシング内に導入され、ケーシング内に残
留する良質m維を出口側に回収する。この良質繊維が回
収された後、ケーシング内は水と異物のみとなりリジェ
クト弁を全開することにより糸外へ異物を排棄し、これ
ら全ての動作は自動的にコントロールして運転される。
That is, undisaggregated pieces in the raw material are rarely disintegrated and remain, and foreign matter cannot pass through the screen and gradually becomes concentrated in the foreign matter collection chamber 5 of the casing, which obstructs the passage of high-quality raw material to the outlet. When the motor load or the differential pressure at the inlet and outlet reaches a preset state, the large mouth valve is closed, washing water is introduced into the casing, and high-quality m-fibers remaining in the casing are collected at the outlet side. After the high-quality fibers are collected, the inside of the casing becomes only water and foreign matter, and by fully opening the reject valve, the foreign matter is discharged to the outside of the yarn, and all these operations are automatically controlled and operated.

〔実施例] 本発明の実施例を第1〜3図例で説明すると、上方に原
料供給口1と、下方に異物排出口2とを備えた密閉ケー
シング3の一方の内側面に、原料を有用繊維分と不純物
の異物分とに分離するためのスクリーン4、例えば円板
状のフラットスクリーンプレートで異物回収室5と繊維
回収室6とに区画形成し、該スクリーン4に近接してイ
ンペラ7を回転自在に備えると共に、このインペラ7に
よって生ずる原料回流速度との相対速度差が生ずるスク
リーン4の外周部側に小径の孔を設けた精選部4.と、
内周部側に前記孔より大きい開口面積の大径の孔を設け
た粗選部43とを備え、この精選部41と粗選部4□と
に対応して繊維回収室6が仕切板10で精選室61と粗
選室6□とに仕切られ、各室6.6□にそれぞれ連通す
る流出口8.9を設け、粗選室6□の流出口9を返送路
11を介して原料タンク12に連結し、該原料タンク1
2から原料移送出管13で前記原料供給口1に連結した
循環路を密閉ケーシング3に備えた製紙用離解兼除塵機
としである。
[Example] An example of the present invention will be described with reference to FIGS. 1 to 3. A raw material is placed on one inner surface of a sealed casing 3 that has a raw material supply port 1 on the upper side and a foreign matter discharge port 2 on the lower side. A screen 4 for separating useful fibers and impurities, for example, a flat screen plate in the form of a disk, is used to divide the foreign matter recovery chamber 5 and the fiber recovery chamber 6 into a foreign matter recovery chamber 5 and a fiber recovery chamber 6, and an impeller 7 is installed adjacent to the screen 4. The screening section 4. is rotatably equipped with a small-diameter hole provided on the outer peripheral side of the screen 4, where a relative speed difference with the raw material circulating speed generated by the impeller 7 occurs. and,
A coarse selection section 43 is provided with a large-diameter hole having an opening area larger than that of the hole on the inner peripheral side, and a fiber recovery chamber 6 is provided with a partition plate 10 corresponding to the selection section 41 and the rough selection section 4□. It is divided into a fine sorting chamber 61 and a rough sorting chamber 6□, and each chamber 6.6□ is provided with an outlet 8.9 that communicates with the raw material. connected to the tank 12, and the raw material tank 1
This is a disintegrator and dust remover for paper manufacturing, which has a closed casing 3 with a circulation path connected from 2 to the raw material supply port 1 by a raw material transfer pipe 13.

この場合、前記スクリーンプレートは丸孔プレート或い
は長孔プレート若しくはスリットプレートを選んで用い
られるし、インペラ内周部側に対面する粗選部4tは外
周部側の精選部4.の孔径より開口面積を大きく、例え
ば1.1〜3.0倍としたり、内周側に行くに従って開
口面積を漸増させた配列としてもよく、孔又はスリット
サイズも同一に限らず異なる寸法のものに選定して除塵
効果と有用繊維回収率向上とをあげることが配慮される
。さらに前記スクリーン4の精選部41と粗選部4.と
は一体もので形成しであるが、分割別体ものを組合わせ
て構成してもよい。
In this case, the screen plate is selected from a round hole plate, a long hole plate, or a slit plate, and the coarse selection section 4t facing the inner circumference side of the impeller is replaced by the fine selection section 4t on the outer circumference side. The opening area may be larger than the hole diameter, for example, 1.1 to 3.0 times, or the opening area may be gradually increased toward the inner circumference, and the hole or slit size is not limited to the same size but may have different sizes. Consideration should be given to selecting the appropriate fibers to improve the dust removal effect and the recovery rate of useful fibers. Furthermore, the fine selection section 41 and the rough selection section 4 of the screen 4. Although it is formed as one piece, it may be constructed by combining separate pieces.

図中15はポンプ、16,17.18は弁、19は次工
程機器である。
In the figure, 15 is a pump, 16, 17, and 18 are valves, and 19 is a next process device.

なお、前記原料供給口1には、弁のある原料流路を、ま
た異物排出口2には弁14のある排出流路が連結され、
さらに精選原料流出口8には弁18のある導出流路とが
連結されていると共に、該原料流路又は密閉ケーシング
3に、弁のある洗浄水供給流路と必要に応じエア抜き弁
のある排気流路(図示せず)とが配備してあり、原料及
び洗浄水の供給と異物並びに精選原料の排出との各操作
を各流路に配備される弁の開閉によって行うもので、前
記密閉ケーシング3に備えた洗浄水供給用の弁を含め、
多弁は開閉操作を繰り返し、リジヱクト処理が行われる
The raw material supply port 1 is connected to a raw material flow path with a valve, and the foreign matter discharge port 2 is connected to a discharge flow path with a valve 14.
Further, the selected raw material outlet 8 is connected to a discharge flow path with a valve 18, and the raw material flow path or the sealed casing 3 is provided with a wash water supply flow path with a valve and an air bleed valve as required. An exhaust flow path (not shown) is provided, and the operations of supplying raw materials and washing water and discharging foreign matter and selected raw materials are performed by opening and closing valves provided in each flow path. Including the wash water supply valve provided in the casing 3,
The multiple valves are repeatedly opened and closed, and the rigid process is performed.

即ち、水張り工程、原料処理工程、離解工程洗浄工程、
異物排出工程を行う0例えば、ケーシング3内に異物が
溜まり過ぎるとオーバーロード。
That is, water filling process, raw material treatment process, disintegration process, washing process,
Perform the foreign matter discharge process 0 For example, if too much foreign matter accumulates inside the casing 3, it will overload.

品質低下となるので原料流路の弁を閉し、洗浄水供給流
路の弁を開き、ケーシング3内を洗浄して良質繊維を回
収したのち、導出流路の弁を閉じて、また排出流路の弁
14を開いて異物を系外に排棄する。その後、再び弁1
4を閉しケーシング3内に洗浄水供給流路の弁を開けて
水を張り、原料流路の弁と導出流路の弁とを開けて良質
繊維を含む原料を通過させるものである。
To prevent quality deterioration, close the valve of the raw material flow path, open the valve of the washing water supply flow path, wash the inside of the casing 3 to recover high-quality fibers, close the valve of the outlet flow path, and open the discharge flow path again. The valve 14 of the passage is opened to discharge foreign matter from the system. Then valve 1 again
4 is closed, the valve of the washing water supply channel is opened to fill water into the casing 3, and the valve of the raw material channel and the valve of the outlet channel are opened to allow the raw material containing high-quality fibers to pass through.

なお、異物排出の際はタイマ又はモータの負荷、若しく
は出入口の差圧が予め設定された状態となると大口弁が
閉しられ、洗浄水が密閉ケーシング3内に導入され、密
閉ケーシング3内に残留する良質繊維を出口側に回収す
る。この良質繊維が回収された後、密閉ケーシング3内
は水と異物のみとなり弁14を全開することにより糸外
へ異物を排棄する。これら全ての動作は自動的にコント
ロールされ、無人運転されるようにするのが配慮される
In addition, when discharging foreign matter, when the load of the timer or motor or the differential pressure at the entrance and exit reaches a preset state, the large mouth valve is closed, and the cleaning water is introduced into the sealed casing 3 and the remaining water remains inside the sealed casing 3. The high quality fibers are collected on the exit side. After the high-quality fibers are collected, the inside of the sealed casing 3 becomes only water and foreign matter, and by fully opening the valve 14, the foreign matter is discharged to the outside of the yarn. Consideration is given to ensuring that all these operations are automatically controlled and operated unmanned.

また、前記ケーシング3内に溜る異物排出をバッチ式に
よらずにケーシング3から少量ずつ弁を開けて連続的に
排出する形態とすることもできる。
Further, the foreign matter accumulated in the casing 3 may be discharged not in a batch manner but continuously by opening a valve little by little from the casing 3.

なお、前記インペラ7は回転軸20を介してモータ21
でコントロールされつつ駆動されるように構成しである
が、変速又は増速機構乃至クラブチ機構を介した形態と
してもよく、さらに多弁及び各検出器、タイマはデータ
処理部のコンピュータユニット(図示せず)に連絡され
、制御回路を構成してあって、原料処理量、原料種類、
原料濃度、出入口圧力差、負荷など離解条件のデータを
アナログ信号として入力してデジタル信号に変換するA
/Dコンバータ及びD/Aコンバータを含む前記コンピ
ュータユニットで内部固定データと入力データとを比較
処理して前記回転インペラ7を駆動するモータを制御し
、かつ弁の開閉を制御し連続的に表示部にデジタル表示
させながら運転するようにするのがよい。
Note that the impeller 7 is connected to a motor 21 via a rotating shaft 20.
Although it is configured to be driven while being controlled by a speed change or speed increasing mechanism or a club mechanism, the multi-valve, each detector, and the timer may be controlled by a computer unit (not shown) of the data processing section. ), and a control circuit is configured to control the raw material processing amount, raw material type,
A that inputs data on disintegration conditions such as raw material concentration, inlet and outlet pressure difference, and load as analog signals and converts them into digital signals.
The computer unit including a /D converter and a D/A converter compares and processes internal fixed data and input data, controls the motor that drives the rotary impeller 7, controls the opening and closing of the valve, and continuously displays the display unit. It is a good idea to drive while using the digital display.

〔発明の効果〕〔Effect of the invention〕

本発明は、原料供給口と、異物排出口とを備えた密閉ケ
ーシング内に、原料を有用繊維分と不純物の異物分とに
分離するためのスクリーンを設けて繊維回収室と異物回
収室とに区画形成し、該異物回収室側の前記スクリーン
に近接してインペラを回転自在に備え、該スクリーンの
外周部側に小径の孔を設けた精選部と、内層部側に前記
孔より大きい開口面積の大径の孔を設けた粗選部とを備
え、この精選部と粗選部とに対応して繊維回収室が仕切
板で精選室と粗選室とに仕切られ、各室にそれぞれ連通
する流出口を設けたことで除塵効果がアンバランスとな
ることなく効率よく行え、しかも原料に剪断力を加えて
未離解片を効率よく諦解させ、原料中に未離解片が多く
混入していても離解作用が不足することなく、有用繊維
の回収歩留りを向上できると共に、スクリーンの目詰ま
りも少なく処理能力も良好で生産量を大幅に高められる
と共に、異物は砕くことなく、14物破砕程度も調節で
きて製品品質が向上し、粗大異物はもちろん細かいごみ
をも適確に分離し、除塵能力も離解能力も大きく有用繊
維と異物とを分離する精選処理力も高い能率良い作業が
可能である。
The present invention provides a fiber recovery chamber and a foreign matter recovery chamber by providing a screen for separating the raw material into useful fiber components and impurity foreign matter components in a sealed casing equipped with a raw material supply port and a foreign matter discharge port. a selective part formed into a partition, rotatably equipped with an impeller close to the screen on the side of the foreign matter collection chamber, with a small-diameter hole provided on the outer peripheral side of the screen, and an opening area larger than the hole on the inner layer side. The fiber recovery chamber is divided into a fine sorting chamber and a rough sorting chamber by a partition plate corresponding to the fine sorting section and the rough sorting section, and communicates with each chamber. By providing an outlet to remove dust, the dust removal effect can be carried out efficiently without becoming unbalanced. Furthermore, by applying shearing force to the raw material, undisaggregated fragments are efficiently dissolved, and many undisaggregated fragments are mixed in the raw material. However, the recovery yield of useful fibers can be improved without insufficient disintegration action, and the screen is less clogged and the processing capacity is good, greatly increasing the production volume. It can be adjusted to improve product quality, accurately separate not only large foreign substances but also fine dust, and has large dust removal and disintegration capabilities, and high selection processing power to separate useful fibers from foreign substances, enabling highly efficient work. .

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

図面は本発明の実施例を示し、第1図は第2図II線に
おける正面図、第2図は縦断面図、第3図は使用状態の
系統説明図である。 1・・・原料供給口、2・・・異物排出口、3・・・密
閉ケ−タンク、4・・・スクリーン、41・・・精選部
、4□・・・粗選部、5・・・異物回収室、6・・・繊
維回収室、61・・・精選室、62・・・粗選室、7・
・・インペラ、8.9・・・流出口、10・・・仕切板
、11・・・返送路、12・・・原料タンク。
The drawings show an embodiment of the present invention, in which FIG. 1 is a front view taken along the line II in FIG. 1... Raw material supply port, 2... Foreign matter discharge port, 3... Closed tank, 4... Screen, 41... Selection section, 4□... Rough selection section, 5...・Foreign matter collection room, 6... Fiber recovery room, 61... Selection room, 62... Rough selection room, 7.
... Impeller, 8.9... Outlet, 10... Partition plate, 11... Return path, 12... Raw material tank.

Claims (2)

【特許請求の範囲】[Claims] (1)原料供給口と、異物排出口とを備えた密閉ケーシ
ング内に、原料を有用繊維分と不純物の異物分とに分離
するためのスクリーンを設けて繊維回収室と異物回収室
とに区画形成し、該異物回収室側の前記スクリーンに近
接してインペラを回転自在に備え、該スクリーンの外周
部側に小径の孔を設けた精選部と、内周部側に前記孔よ
り大きい開口面積の大径の孔を設けた粗選部とを備え、
この精選部と粗選部とに対応して繊維回収室が仕切板で
精選室と粗選室とに仕切られ、各室にそれぞれ連通する
流出口を設けたことを特徴とする製紙用離解兼除塵機。
(1) A screen is installed in a sealed casing equipped with a raw material supply port and a foreign matter discharge port to separate the raw material into useful fiber components and impurity foreign matter components, dividing the raw material into a fiber recovery chamber and a foreign matter recovery chamber. a selective part having a rotatable impeller close to the screen on the foreign matter collection chamber side, a selection part having a small diameter hole on the outer peripheral side of the screen, and an opening area larger than the hole on the inner peripheral side. and a coarse selection section with large diameter holes,
The fiber recovery chamber is divided into a fine sorting chamber and a rough sorting chamber by a partition plate corresponding to the fine sorting section and the rough sorting section, and an outlet communicating with each chamber is provided. Dust remover.
(2)前記密閉ケーシングが、粗選室の流出口を返送路
を介して原料タンクに連結し、該原料タンクから原料移
送出管で前記原料供給口に連結した循環路を備えた請求
項1記載の製紙用離解兼除塵機。
(2) Claim 1, wherein the sealed casing includes a circulation path that connects the outlet of the rough sorting chamber to the raw material tank via a return path, and connects the raw material tank to the raw material supply port with a raw material transfer outlet pipe. The paper-making disintegrator and dust remover mentioned above.
JP2071988A 1990-03-23 1990-03-23 Papermaking disaggregation machine also used as duster Pending JPH03279483A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2071988A JPH03279483A (en) 1990-03-23 1990-03-23 Papermaking disaggregation machine also used as duster

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2071988A JPH03279483A (en) 1990-03-23 1990-03-23 Papermaking disaggregation machine also used as duster

Publications (1)

Publication Number Publication Date
JPH03279483A true JPH03279483A (en) 1991-12-10

Family

ID=13476354

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2071988A Pending JPH03279483A (en) 1990-03-23 1990-03-23 Papermaking disaggregation machine also used as duster

Country Status (1)

Country Link
JP (1) JPH03279483A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010525185A (en) * 2007-04-30 2010-07-22 フォイト パテント ゲゼルシャフト ミット ベシュレンクテル ハフツング Process for producing a mesh for processing a fiber suspension suitable for paper products, in particular a hard mesh
JP2012217872A (en) * 2011-04-04 2012-11-12 Shimadzu Corp Filtration apparatus
CN106567270A (en) * 2016-10-23 2017-04-19 郑建灵 Papermaking deslagging device

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010525185A (en) * 2007-04-30 2010-07-22 フォイト パテント ゲゼルシャフト ミット ベシュレンクテル ハフツング Process for producing a mesh for processing a fiber suspension suitable for paper products, in particular a hard mesh
JP2012217872A (en) * 2011-04-04 2012-11-12 Shimadzu Corp Filtration apparatus
CN106567270A (en) * 2016-10-23 2017-04-19 郑建灵 Papermaking deslagging device

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