JP2762369B2 - Operating method of pulper for papermaking - Google Patents

Operating method of pulper for papermaking

Info

Publication number
JP2762369B2
JP2762369B2 JP22827089A JP22827089A JP2762369B2 JP 2762369 B2 JP2762369 B2 JP 2762369B2 JP 22827089 A JP22827089 A JP 22827089A JP 22827089 A JP22827089 A JP 22827089A JP 2762369 B2 JP2762369 B2 JP 2762369B2
Authority
JP
Japan
Prior art keywords
tank
foreign matter
disintegration
pulper
storage
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
JP22827089A
Other languages
Japanese (ja)
Other versions
JPH0397982A (en
Inventor
叔彦 相川
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 TETSUKO KK
Original Assignee
AIKAWA TETSUKO 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 AIKAWA TETSUKO KK filed Critical AIKAWA TETSUKO KK
Priority to JP22827089A priority Critical patent/JP2762369B2/en
Publication of JPH0397982A publication Critical patent/JPH0397982A/en
Application granted granted Critical
Publication of JP2762369B2 publication Critical patent/JP2762369B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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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

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  • Paper (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、新聞古紙,色上古紙などの故紙処理など製
紙用設備として原料を高濃度で離解し、脱墨用原料又は
その他各種原料として使用するための高濃度パルパーの
操業システム、即ち製紙用パルパーの運転方法に関する
ものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention disintegrates raw materials at a high concentration as papermaking equipment such as waste paper processing of used newspapers and colored papers, and uses them as deinking raw materials or various other raw materials. The present invention relates to a high-concentration pulper operating system for use, that is, a method for operating a papermaking pulper.

〔従来の技術〕[Conventional technology]

従来、この種のほとんどの高濃度パルパー(10〜20%
濃度)の操業はバッチ式であった。即ち、原料離解が終
了した時点で排出機構を開放して異物とともに全量の原
料をパルパーから排出し、5%程度にチェストで希釈し
て有機繊維を回収し再びパルパー内に水張り、原料投入
して離解を行うといえ工程を繰り返していた。また、原
料離解完了後に排出機構を開放してストレーナを備えた
除塵機を経由して原料を排出する方式も試みられ、この
方式ではパルパーはバッチ式運動では異物は1バッチ毎
にストレーナを備えた除塵機タブの下部バルブを開き排
出するが、バッチ式操業に変わりがなく、操業性も良く
なかった。一方連続的に運転するためにタンクの底部
に、紙料に回流を与える解離用ロータを回転可能に備
え、その周わりにストレーナなどの通孔壁で処理原料室
を区画配備し、そしてこの処理原料室に希釈水を導入し
て約5%程度の濃度に希釈しながら連続的に原料を抜き
出す方法を採られることが知られているが、この場合で
も、原料中の異物がストレーナを抜けることが出来ず、
パルパー内に異物が次第に溜まり、ロータの回転により
破砕された異物が次の工程に送られ事後処理に問題が生
じやすいほか、異物を砕いたり無駄な動力消費につなが
ら品質的にも良くならないことが知られている。
Conventionally, most of this kind of high concentration pulper (10-20%
Concentration) was a batch operation. That is, when the raw material disintegration is completed, the discharge mechanism is opened to discharge the entire raw material together with the foreign matter from the pulper, dilute it with a chest to about 5%, collect the organic fibers, fill the pulper again with water, and feed the raw material. Although the disintegration was performed, the process was repeated. In addition, a method has been attempted in which the discharge mechanism is opened and the raw material is discharged through a dust remover equipped with a strainer after the completion of the raw material disaggregation. In this method, the pulper is provided with a strainer for each batch in the batch-type movement. The lower valve of the dust remover tab was opened and discharged, but there was no change to the batch operation and the operability was not good. On the other hand, for continuous operation, a dissociation rotor that circulates the stock is rotatably provided at the bottom of the tank, and a processing material chamber is partitioned around a perforated wall such as a strainer around the periphery thereof. It is known that a method of continuously extracting a raw material while introducing dilution water into a chamber and diluting to a concentration of about 5% is used, but even in this case, foreign substances in the raw material may pass through the strainer. I ca n’t,
Foreign matter gradually accumulates in the pulper, and the foreign matter crushed by the rotation of the rotor is sent to the next step, which may cause problems in post-processing.In addition, the quality may not be improved while crushing the foreign matter and wasteful power consumption. Are known.

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

従来パルパーによる処理においては、バッチ式操業の
場合には操業時間のロスタイムがあり操業性も歩留りも
悪いものであり、パルパー型式が大きくなり、又設備モ
ータも大型化し、かつモータ始動,停止の回数が多くな
り、モータも特殊型となって高価となるという欠点があ
る。このため連続式操業としても原料中の異物は次第に
パルパー内に溜り時間の経過と共にパルパー内の異物濃
度が高まり、それに比例して原料抜き出し濃度は低くな
り、且つ異物もパルパーロータ回転に依って破砕され工
程に送られてしまい品質低下の一因となるほか、動力消
費に無駄ができ運転管理並びに経費的にも好ましくない
という問題があった。
In the conventional treatment with a pulper, the batch type operation has a loss of operation time, and the operability and yield are poor, the pulper type becomes large, the equipment motor becomes large, and the number of times of starting and stopping the motor is increased. However, there is a disadvantage that the motor becomes a special type and becomes expensive. For this reason, even in continuous operation, foreign substances in the raw material gradually accumulate in the pulper, and as the time elapses, the concentration of the foreign substance in the pulper increases, and the concentration of the raw material withdrawn decreases in proportion to the time. In addition to the above, there is a problem that power is consumed and power management is unfavorable in terms of operation management and cost.

本発明は、これらの従来の諸欠点を適確に排除しよう
とするもので、パルパー処理が効果的にでき、パルパー
中の良質繊維の有用繊維を著しく効率よく連続的に回収
し、かつ処理能力の増大が図られパルパーの操業性を向
上しうるし、パルパーによる異物破砕がなく品質低下も
なく排除すべき異物処理を含む事後処理も簡便で、異物
がパルパー内に次第に蓄積されるのを防止してパルパー
掃除が減少または不要となり、保守保安もらくで安全性
の高い合理的な運転が可能で信頼性も大幅に高められる
製紙用パルパーの運転方法を提供することを目的とする
ものである。
The present invention is intended to properly eliminate these conventional drawbacks, and can effectively treat the pulper, continuously collect useful fibers of good quality fibers in the pulper extremely efficiently and continuously, and improve the processing capacity. It is possible to improve the operability of the pulper, improve the operability of the pulper. Accordingly, it is an object of the present invention to provide a method for operating a papermaking pulper in which pulper cleaning is reduced or unnecessary, maintenance security is ensured, a safe and reasonable operation is possible, and reliability is greatly improved.

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

本発明は、製紙用原料が供給される紙料タンク内で原
料を液体とともに回転自在の解離用ロータで回流させつ
つ撹拌して液中で原料解離すると共に、このタンク内の
解離済みの良質繊維と、未離解分を含む異物とをその排
出量をそれぞれ調整しつつ系外に導出する製紙用パルパ
ーの運転方法において、良質繊維が未離解分を含む異物
とともに、排出路の排出機構で排出量を調整されつつ貯
留離解用タンクに一旦排出され、該貯留離解用タンク内
で良質繊維と、未離解分含有異物とに分離して、良質繊
維を貯留離解用タンクから連続的に導出し、かつ貯留離
解用タンク内に異物除去済で残留する未離解分を除塵用
タンクに間歇的に排出し、この除塵用タンク内に希釈水
を導入しつつ未離解分中の異物をさらに分離除去し、こ
の異物の分離された未離解分の全部又は一部を前記紙料
タンクに返送循環して再処理すると共に、貯留される異
物を除塵用タンクより間歇的に排出することを特徴とす
る製紙用パルパーの運転方法である。
The present invention relates to a stock material to which a raw material for papermaking is supplied, wherein the raw material is stirred and circulated by a rotatable dissociation rotor together with a liquid to dissociate the raw material in the liquid, and the dissociated high-quality fibers in the tank. In the method of operating a papermaking pulper that leads out of the system while adjusting the discharge amount of the foreign matter containing the undisintegrated component, the quality fiber is discharged together with the foreign material containing the undisintegrated component by the discharge mechanism in the discharge path. Is discharged once to the storage and disintegration tank while being adjusted, and in the storage and disintegration tank, the high-quality fibers are separated into undisintegrated components-containing foreign matter, and the high-quality fibers are continuously derived from the storage and disintegration tank, and The undisintegrated material remaining after the foreign matter has been removed in the storage and disintegration tank is intermittently discharged to the dust removing tank, and the foreign matter in the undisintegrated matter is further separated and removed while introducing dilution water into the dust removing tank. This foreign matter was separated All or part of the macerating min while reprocessed returned circulated to the stock tank, a papermaking pulper operating method characterized by discharging the foreign substances stored intermittently from dust tank.

〔作 用〕(Operation)

本発明の製紙用パルパーの運転方法では、パルパー内
の離解用ロータで混合撹拌された紙料が全量連続的に連
続運転用の貯留離解用タンク内に導入しつつ有用繊維を
異物類と分離して連続的に導出回収し貯留する未離解分
を含む異物は間歇的に運転される除塵用タンク内に移送
して未離解分と異物とに分離し、未離解分の一部又は全
部を前記パルパーに返送循環させて再処理すると共に、
異物は除塵用ンクから間歇的に排除し、常時良質繊維は
連続的に回収されて次工程処理に供され操業性を大幅に
向上して運転することが可能となるものであり、パルパ
ー内での異物の破砕が著しく少なく品質向上にも運転管
理上にも良好に操業することが可能となるものである。
In the method for operating the papermaking pulper of the present invention, the whole of the stock mixed and stirred by the disintegration rotor in the pulper is continuously introduced into the storage and disintegration tank for continuous operation to separate useful fibers from foreign matter. The foreign matter containing the undisintegrated components to be continuously collected and stored is transferred to a dust removal tank that is operated intermittently and separated into the undisintegrated components and the foreign materials. It is returned to the pulper and circulated for reprocessing.
Foreign matter is intermittently removed from the dust removal tank, and high-quality fibers are continuously collected and provided to the next process for operation with greatly improved operability. The crushing of foreign matter is extremely small, and it is possible to operate satisfactorily both in quality improvement and operation management.

〔実施例〕〔Example〕

本発明の実施例を第1〜3図例について説明すると、
原料AがコンベヤBで供給される紙料タンク1内で原料
Aを液体とともに回転自在の離解用ロータ2で回流させ
つつ撹拌して液中に原料離解すると共に、このタンク内
の離解済みの良質繊維と、未離解分を含む異物とを排出
路3の排出量調整機構4例えばバルブV1によってその排
出量を調整しつつ系外に導出する製紙用パルパーの運転
方法において、良質繊維が未離解分を含む異物とととも
に、排出路3の排出量調整機構4で貯留離解用タンク5
に一旦排出され、給水路11から希釈水を入れ該貯留離解
用タンク5内で良質繊維と、未離解分含有異物とに分離
して、良質繊維を貯留離解用タンク5からポンプ6のあ
る流出路7でチェストCに連続的に導出し、かつ貯留離
解用タンク5内に異物除去済で残留する未離解分を除塵
用タンク8に連通路9を経由して排出部10のバルブV2
開閉操作で間歇的に排出し、この除塵用タンク8内に希
釈水を給水路111より導入しつつ未離解分中の異物をさ
らに分離除去し、この異物の分離された未離解分の全部
又は一部をポンプ12のある返送路13で前記紙料タンク1
に返送循環し、或いはチェストCに導入して再処理する
と共に、貯留される異物を除塵用タンク8より間歇的に
異物排出路14にある排出部15のバルブV3を開放して系外
に排棄できるようになっている。
The embodiment of the present invention will be described with reference to FIGS.
The raw material A is stirred in the stock material tank 1 supplied with the conveyor B while being circulated by the rotatable rotatable rotor 2 together with the liquid to disintegrate the raw material A into the liquid. and fibers, method of operating a papermaking pulper to derive the outside the system while adjusting the emissions and foreign substances including non defibration content by the discharge amount adjusting mechanism 4, for example a valve V 1 of the discharge passage 3, good fiber Not macerating The storage and disaggregation tank 5 is controlled by the discharge amount adjusting mechanism 4 of the discharge path 3 together with the foreign matter containing
Once, the diluted water is supplied from the water supply channel 11, and the high-quality fibers are separated from the non-disintegrated portion-containing foreign matter in the storage and disintegration tank 5, and the high-quality fibers are discharged from the storage and disintegration tank 5 with the pump 6. The undisintegrated portion which is continuously led out to the chest C by the passage 7 and which has been removed after the foreign matter has been removed in the storage and disintegration tank 5 is transferred to the dust removing tank 8 via the communication passage 9 by the valve V 2 of the discharge unit 10. It opened and closed intermittently discharged at this dilution to dust removal tank 8 water supply passage 11 1 is introduced from further separating and removing foreign matters MiHanare in solution fraction with a total non defibration component separated in the foreign substance Alternatively, a part of the stock tank 1 is returned to the return path 13 having a pump 12.
And re-processed by introducing it into the chest C, and intermittently open the valve V 3 of the discharge section 15 in the foreign substance discharge path 14 from the dust removing tank 8 to remove the stored foreign substances from the system. It can be discarded.

この場合、原料は前記貯留離解用タンク5及び除塵用
タンク8内において、それぞれ回転するインペラ16,17
によって回流撹拌されつつ、通液用のスリット又は丸孔
のあるスクリーン18,19で導出分と貯留分とに分離しつ
つ最終処理手段で異物を間歇的に系外に排出除去してパ
ルパー運転するのがよい。
In this case, the raw materials are stored in the storage / disintegration tank 5 and the dust removal tank 8 by rotating impellers 16 and 17 respectively.
While being circulated and stirred, foreign substances are intermittently discharged and removed from the system by the final treatment means while the pulper operation is performed, while separating into the derived part and the reserved part by the screens 18 and 19 having slits or round holes for liquid passage. Is good.

図中、M1,M2,M3は駆動用のモータで離解用ロータ2及
びインペラ16,17をそれぞれ回転駆動するために備えら
れる。V1〜V7は電磁弁などのバルブで各流路の開閉を司
る。V8〜V9は手動バルブで返送路13並びに分岐路131
それぞれ備えられるが、分岐点に設けた三方弁で切換分
配することも可能である。20は給水源、21は脱気管で除
塵用タンク8に備えられる。
In the drawing, M 1 , M 2 , and M 3 are driving motors provided to rotationally drive the disintegration rotor 2 and the impellers 16 and 17, respectively. V 1 ~V 7 governs the opening and closing of the flow paths in the valve such as an electromagnetic valve. Although V 8 ~V 9 are respectively provided in the return passage 13 and branch passage 13 1 in manual valve, it is possible to switch distributed three-way valve provided in the branch point. Reference numeral 20 denotes a water supply source, and reference numeral 21 denotes a deaeration pipe provided in the dust removing tank 8.

しかして、第3図に示す方式にように水を所定量入れ
た紙料タンク1に原料Aを投入して離解用ロータ2のモ
ータM1をONとして運転を開始すると、給水路11中のバル
ブV7を開とすると同時に脱気管21のバルブV6を開き、か
つ給水路111のバルブV5を開とし。貯留離開用タンク5
と除塵用タンク8とに給水され、それぞれ所定時間経過
後タイマーで貯留離解用タンク5内のインペラ16のモー
タM2をONとする。次で所定時間後に排出路3の排出部4
のバルブV1を開き貯留離解用タンク5に移送し続けると
ともにポンプ6をONとして有用繊維分を連続的にタンク
5より流出路7を経て抜き出しチェストCに連続的に供
給する。この際、タイマー又はインペラ16のモータM2
負荷上限に至ると除塵用タンク8のインペラ17のモータ
M3をONとし、連絡路9の排出部10のバルブV2を開き、返
送路13のバルブV4も開としてから未離解分の返送を前記
紙料タンク1に開始するに際し、給水路111のバルブV5
を開としてポンプ12をONとして、所定時間経過後にバル
ブV2を閉じ、さらに所定時間経過してからポンプ12をOF
Fとし、バルブV5,V4を閉、バルブV6を開としてから排出
路14のバルブV3を開いて異物排出を行ったのち、バルブ
V3を閉じインペラ17のモータM3をOFFする。そしてバル
ブV6及びバルブV5を開とし、希釈水を給水路111から導
入し、満水にしてからバルブV5及びV6を閉じ、インペラ
17のモータM3をONとし次の除塵工程に備えられ、前記処
理工程を繰り返し連続的に良質の導出を流出路7で行い
うるものである。
Thus, if it the raw material A was charged to the stock tank 1 of water was placed in a predetermined amount so the system shown in Figure 3 starts operation as ON the motor M 1 of the defibration rotor 2, in water supply passage 11 When the valve V 7 opened by opening the valve V 6 of degassing tubes 21 simultaneously, and the valve V 5 of the water supply passage 11 1 opens. Storage / separation tank 5
And water is supplied into the dust tank 8, respectively, and ON the motor M 2 of the impeller 16 in the reservoir defibration tank 5 at a predetermined time has elapsed after the timer. Next, after a predetermined time, the discharge section 4 of the discharge path 3
Continuously continuously supplied to the chest C withdrawn through the outlet channel 7 from the tank 5 a useful fiber content as ON the pump 6 with opening the valve V 1 continues to transfer to the storage defibration tank 5. At this time, the motor of the impeller 17 of the dust tank 8 reaches the load limit of the motor M 2 of the timer or the impeller 16
Upon the M 3 and ON, opening the valve V 2 of the discharge portion 10 of the communication passage 9 is also started valve V 4 of the return passage 13 from the open back of the non-defibration content in the paper stock tank 1, water supply path 11 1 valve V 5
The pump 12 as ON is opened, closing the valve V 2 after a predetermined time has elapsed, the pump 12 After an additional predetermined time OF
And F, after performing the foreign matter discharge valve V 5, V 4 closed, by opening the valve V 3 of the discharge passage 14 from the valve V 6 is opened, the valve
Turning OFF the motor M 3 of the closed impeller 17 V 3. And the valve V 6 and valve V 5 is opened, introducing the diluting water from the water supply path 11 1, closing the valves V 5 and V 6 after the full level, the impeller
The motor M 3 17 and ON provided next dedusting step, in which the derivation of continuous quality repeat the processing steps may be carried out to the outflow path 7.

また、第4図例の方式のように紙料タンク1の運転は
第3図例と同様にし、貯留離解用タンク5のインペラ16
のモータM2をONとした後は、先ず脱気管21のバルブV6
開いてエア抜きをしてバルブV4,バルブV2を順に開き所
定時間経過後バルブV2を閉じ、さらにバルブV5を開いて
希釈水を供給しつつ返送路13のポンプ12をONとし、所定
運転後にバルブV5を閉じて給水を停止してからバルブV4
を閉じポンプ12をOFFし、バルブV6を開として脱気し排
出路14の排出部15のバルブV3を開いて異物を排除してか
らバルブV3を閉じインペラ17のモータM3をOFFとして次
の異物排除工程に至るまで待機することで前記離解処理
工程を各部で繰り返し連続的に良質繊維の導出を流出路
7で能率よく行い得るものである。
4, the operation of the stock tank 1 is the same as that of the embodiment shown in FIG. 3, and the impeller 16 of the storage / disintegration tank 5 is used.
After the motor M 2 and ON, the valve V 4 Bleed first by opening the valve V 6 of degassing tubes 21, closed a predetermined time has elapsed after the valve V 2 opens the valve V 2 in the order, further valves V 5 by opening the oN the pump 12 of the return path 13 while supplying dilution water, the valve V 4 stop the water supply by closing the valve V 5 after a predetermined operation
OFF the pump 12 closed, OFF the motor M 3 of the impeller 17 to close the valve V 3 from the exclusion of foreign material by opening the valve V 3 of the discharge portion 15 of the degassed valve V 6 is opened discharging path 14 By waiting until the next foreign matter removing step, the above-described disaggregation processing step can be repeated in each part, and the good-quality fibers can be continuously and efficiently discharged through the outflow path 7.

〔発明の効果〕〔The invention's effect〕

本発明は、良質繊維が未離解分を含む異物とともに、
排出路の排出機構で排出量を調整されつつ貯留離解用タ
ンクに一旦排出され、該貯留離解用タンク内で良質繊維
と、未離解分含有異物とに分離して、良質繊維を貯留離
解用タンクから連続的に導出し、かつ貯留離解用タンク
用に異物除去済で残留する未離解分を除塵用タンクに間
歇的に排出し、この除塵用タンク内に希釈水を導入しつ
つ未離解分中の異物をさらに分離除去し、この異物の分
離された未離解分の全部又は一部を前記紙料タンクに返
送循環して再処理すると共に、貯留される異物を除塵用
タンクより間歇的に排出することにより、パルパー処理
が効果的にでき、パルパー中の良質繊維の有用繊維を著
しく効率よく連続的に回収し、かつ処理能力の増大が図
られパルパーの操業性を向上しうるし、パルパーによる
異物破砕がなく品質低下もなく排除すべき異物処理を含
む事後処理も簡便で、異物がパルパー内に次第に蓄積さ
れるのを防止してパルパー掃除が減少または不要とな
り、保守保安もらくで安全性の高い合理的な運転が可能
で信頼性も大幅に高められるものであると共に、パルパ
ーが小型化され設置面積も動力も少なく設備費も節減で
きるものである。
The present invention is a high-quality fiber together with foreign matter containing undisintegrated components,
The discharge amount is adjusted by the discharge mechanism of the discharge path, and once discharged to the storage / disintegration tank, the high-quality fiber and the non-disintegrated portion-containing foreign matter are separated in the storage / disintegration tank, and the high-quality fiber is stored and disintegrated. , And the remaining undisintegrated material remaining after removal of foreign matter for the storage and disintegration tank is discharged intermittently to the dust removal tank, and diluted water is introduced into the dust removal tank while diluting water is introduced. The foreign material is further separated and removed, and all or a part of the separated undisintegrated material is returned to the stock tank, circulated and reprocessed, and the stored foreign material is intermittently discharged from the dust removing tank. By doing so, the pulper treatment can be effectively performed, useful fibers of good quality fibers in the pulper can be continuously collected extremely efficiently, and the processing capacity can be increased to improve the operability of the pulper. Good without crushing Post-treatment including foreign matter treatment that should be eliminated without reduction is also easy, preventing foreign matter from gradually accumulating in the pulper, reducing or eliminating the need for pulper cleaning. Operation is possible and the reliability is greatly improved, and the pulper is downsized, the installation area is small, the power is small, and the equipment cost can be reduced.

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

図面は本発明の実施例を示し、第1図は系統説明側面
図、第2図は第1図I−I線における切断平面図、第3
図は運転状態のフローシート、第4図は他の実施例の運
転状態のフローシートである。 1……紙料タンク、2……ロータ、3……紙料排出路、
4……排出量調整機構、5……貯留離解用タンク、6…
…ポンプ、7……流出路、8……除塵用タンク、9……
連通路、10……排出部、11,111……給水路、14……異物
排出路、15……排出部、16,17……インペラ、18,19……
スクリーン、M1〜M3……モータ、V1〜V9……バルブ。
1 shows an embodiment of the present invention, FIG. 1 is a side view for explaining a system, FIG. 2 is a sectional plan view taken along the line II in FIG.
The figure shows a flow sheet in an operating state, and FIG. 4 shows a flow sheet in an operating state of another embodiment. 1 ... stock tank, 2 ... rotor, 3 ... stock discharge path,
4 ... discharge adjustment mechanism, 5 ... storage and disintegration tank, 6 ...
... Pump, 7 ... Outflow path, 8 ... Dust removal tank, 9 ...
Communication passage, 10 discharge section, 11, 11 1 ... water supply path, 14 foreign matter discharge path, 15 discharge section, 16, 17 impeller, 18, 19 ...
Screen, M 1 ~M 3 ...... motor, V 1 ~V 9 ...... valve.

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】製紙用原料が供給される紙料タンク内で原
料を液体とともに回転自在の離解用ロータで回流させつ
つ撹拌して液中で原料離解すると共に、このタンク内の
離解済みの良質繊維と、未離解分を含む異物とをその排
出量をそれぞれ調整しつつ系外に導出する製紙用パルパ
ーの運転方法において、良質繊維が未離解分を含む異物
とともに、排出路の排出機構で排出量を調整されつつ貯
留離解用タンクに一旦排出され、該貯留離解用タンク内
で良質繊維と、未離解分含有異物とに分離して、良質繊
維を貯留離解用タンクから連続的に導出し、かつ貯留離
解用タンク内に異物除去済で残留する未離解分を除塵用
タンクに間歇的に排出し、この除塵用タンク内に希釈水
を導入しつつ未離解分中の異物をさらに分離除去し、こ
の異物の分離された未離解分の全部又は一部を前記紙料
タンクに返送循環して再処理すると共に、貯留される異
物を除塵用タンクより間歇的に排出することを特徴とす
る製紙用パルパーの運転方法。
A raw material is supplied in a stock tank to which papermaking raw material is supplied. The raw material is stirred with the liquid while being circulated by a rotatable disintegrating rotor to disintegrate the raw material in the liquid. In the method of operating a papermaking pulper in which fibers and foreign matter containing undisintegrated components are led out of the system while adjusting the discharge amount, good quality fibers are discharged together with foreign matter containing undisintegrated components by a discharge mechanism in a discharge path. Once discharged to the storage and disintegration tank while the amount is adjusted, high-quality fibers in the storage and disintegration tank, and separated into undisintegrated components-containing foreign matter, continuously deriving good quality fibers from the storage and disintegration tank, The undisintegrated material remaining after the foreign matter has been removed from the storage and disintegration tank is intermittently discharged to the dust removing tank, and diluting water is introduced into the dust removing tank to further separate and remove the foreign matter in the undisintegrated matter. , This foreign matter is separated All or part of the non-defibration min while reprocessed returned circulated to the stock tank, papermaking pulper operating method characterized by discharging the foreign substances stored intermittently from dust tank.
【請求項2】原料は前記貯留離解用タンク及び除塵用タ
ンク内において、それぞれ回転するインペラによって回
流撹拌されつつ、通液用のスリット又は丸孔のあるスク
リーンで導出分と貯留分とに分離しつつ最終処理段階で
異物を間歇的に系外に排出除去するものである請求項1
記載のパルパーの運転方法。
2. The raw material is separated and separated in a storage and disintegration tank and a dust removal tank by a rotating impeller while being circulated and stirred by a screen having a slit or a round hole for liquid passage. 2. The method according to claim 1, further comprising the step of intermittently discharging and removing foreign matter from the system in the final processing step.
Operating method of the described pulper.
【請求項3】前記紙料タンクの排出路の排出機構が、回
転する離解用ロータの所定設定時間の運転後または離解
用ロータの所定の動力負荷によって操作制御される開閉
バルブであって、連続的に紙料を除塵用タンクに排出す
るものである請求項1または2記載のパルパーの運転方
法。
3. The open / close valve, wherein the discharge mechanism of the discharge path of the stock tank is an open / close valve that is operated and controlled after a predetermined time of operation of a rotating disintegration rotor or by a predetermined power load of the disintegration rotor. 3. The method for operating a pulper according to claim 1, wherein the paper material is discharged to a dust removing tank.
JP22827089A 1989-09-05 1989-09-05 Operating method of pulper for papermaking Expired - Lifetime JP2762369B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22827089A JP2762369B2 (en) 1989-09-05 1989-09-05 Operating method of pulper for papermaking

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22827089A JP2762369B2 (en) 1989-09-05 1989-09-05 Operating method of pulper for papermaking

Publications (2)

Publication Number Publication Date
JPH0397982A JPH0397982A (en) 1991-04-23
JP2762369B2 true JP2762369B2 (en) 1998-06-04

Family

ID=16873843

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22827089A Expired - Lifetime JP2762369B2 (en) 1989-09-05 1989-09-05 Operating method of pulper for papermaking

Country Status (1)

Country Link
JP (1) JP2762369B2 (en)

Also Published As

Publication number Publication date
JPH0397982A (en) 1991-04-23

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