JP2017115259A - Waste paper recycling processing apparatus - Google Patents

Waste paper recycling processing apparatus Download PDF

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JP2017115259A
JP2017115259A JP2015250804A JP2015250804A JP2017115259A JP 2017115259 A JP2017115259 A JP 2017115259A JP 2015250804 A JP2015250804 A JP 2015250804A JP 2015250804 A JP2015250804 A JP 2015250804A JP 2017115259 A JP2017115259 A JP 2017115259A
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unit
operation mode
used paper
disaggregation
stirring
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義 寺井
Tadashi Terai
義 寺井
佳久 東本
Yoshihisa Higashimoto
佳久 東本
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Duplo Seiko Corp
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Duplo Seiko Corp
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Priority to JP2015250804A priority Critical patent/JP2017115259A/en
Priority to US15/381,257 priority patent/US20170183816A1/en
Priority to CN201611198536.4A priority patent/CN106917310B/en
Publication of JP2017115259A publication Critical patent/JP2017115259A/en
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    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21BFIBROUS RAW MATERIALS OR THEIR MECHANICAL TREATMENT
    • D21B1/00Fibrous raw materials or their mechanical treatment
    • D21B1/04Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres
    • D21B1/12Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres by wet methods, by the use of steam
    • D21B1/30Defibrating by other means
    • D21B1/34Kneading or mixing; Pulpers
    • D21B1/345Pulpers
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21BFIBROUS RAW MATERIALS OR THEIR MECHANICAL TREATMENT
    • D21B1/00Fibrous raw materials or their mechanical treatment
    • D21B1/04Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres
    • D21B1/12Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres by wet methods, by the use of steam
    • D21B1/30Defibrating by other means
    • D21B1/32Defibrating by other means of waste paper
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21BFIBROUS RAW MATERIALS OR THEIR MECHANICAL TREATMENT
    • D21B1/00Fibrous raw materials or their mechanical treatment
    • D21B1/04Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres
    • D21B1/12Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres by wet methods, by the use of steam
    • D21B1/30Defibrating by other means
    • D21B1/32Defibrating by other means of waste paper
    • D21B1/325Defibrating by other means of waste paper de-inking devices
    • 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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  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Mechanical Engineering (AREA)
  • Paper (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a waste paper recycling processing apparatus which does not affect quality of recycled paper even when paper pieces attached on an inner wall surface of a stirring tank are mixed in a pulp solution and downsizing of the apparatus is realized.SOLUTION: The waste paper recycling processing apparatus comprises a pulper part that is a processing part constituting a waste paper recycling processing system and a control part that controls the operation of the processing part. The pulper part has a stirring tank 901, a stirrer that rotatably drives a stirring blade 902 in the stirring tank 901, and a water supply part 911 that supplies water for dilution to the stirring tank 901. The control part drives the stirrer sequentially in a disintegration operation mode, a transition operation mode, and a dilution operation mode.SELECTED DRAWING: Figure 3

Description

本発明は、古紙の発生場所であるオフィス等に設置して紙を再生する古紙再生処理装置に関するものである。   The present invention relates to a used paper recycling apparatus that is installed in an office or the like where waste paper is generated to recycle the paper.

従来、古紙再生処理装置には、例えば古紙投入部、パルパー部、脱墨部、抄紙部、乾燥部や運転を制御する制御部を設けている。古紙紙投入部は、再生原料の古紙をパルパー部に供給するものであり、パルパー部は、古紙を離解して古紙パルプを含む古紙パルプ溶液を調整するものであり、脱墨部は、古紙パルプ溶液を脱墨して脱墨パルプを調製するものである。抄紙部は、脱墨された古紙パルプ溶液から湿紙を抄紙するものであり、乾燥部は、脱水された湿紙を乾燥するものである。   Conventionally, used paper recycling processing apparatuses are provided with a used paper input unit, a pulper unit, a deinking unit, a paper making unit, a drying unit, and a control unit for controlling operation. The waste paper input section supplies recycled paper as recycled raw material to the pulper section, the pulper section disaggregates waste paper and adjusts the waste paper pulp solution containing waste paper pulp, and the deinking section A deinked pulp is prepared by deinking the solution. The paper making section is for making wet paper from the deinked waste paper pulp solution, and the drying section is for drying the dehydrated wet paper.

パルパー部は、撹拌槽と撹拌槽内に配した撹拌羽根と撹拌羽根を回転駆動する駆動部を有しており、撹拌羽根の回転により撹拌槽の離解用水中で古紙を撹拌して離解処理し、調製した古紙パルプ溶液を次工程に移送する。   The pulper unit has a stirrer tank, a stirring blade disposed in the stirrer tank, and a drive unit that rotationally drives the stirrer blade. The prepared waste paper pulp solution is transferred to the next step.

図5に示すように、パルパー部では、所定量の撹拌用水を注水し(S1)、その後に古紙を投入し(S2)、次に撹拌羽根を750rpmで回転させて離解処理し(S3)、続いて希釈用水を供給しつつ撹拌し(S4)、パルプ濃度が4重量%に達した時点で(S5)で停止する(S6)。   As shown in FIG. 5, in the pulper unit, a predetermined amount of agitation water is poured (S1), then used paper is added (S2), and then the agitation blade is rotated at 750 rpm to disaggregate (S3). Then, it stirs, supplying dilution water (S4), and stops at (S5) when the pulp concentration reaches 4% by weight (S6).

また、特許文献1には、攪拌羽根によって攪拌を行う際に、攪拌槽内における古紙原料及び給水部からの水を含む液体の水位を攪拌羽根を浸漬可能な高さとして攪拌を行い、攪拌処理中に攪拌羽根の回転数が上昇するときに、給水部より給水を行って攪拌羽根を攪拌槽内の液体に浸漬させる技術が記載されている。   In addition, in Patent Document 1, when stirring is performed with a stirring blade, the water level of the liquid containing water from the waste paper raw material and the water supply unit in the stirring tank is stirred at a height at which the stirring blade can be immersed, and stirring processing is performed. A technique is described in which, when the rotation speed of the stirring blade increases, water is supplied from the water supply section so that the stirring blade is immersed in the liquid in the stirring tank.

特開2011−219893JP2011-219893

上記のパルパー部では、撹拌槽内の撹拌羽根を離解用回転数(750rpm)で回転させて所定量の離解用水中で古紙を離解処理し、離解濃度(8重量%)の古紙パルプ溶液を調製しており、その後、撹拌用回転数(400rpm)で回転させながら希釈用水を加えて所定濃度(4重量%)まで古紙パルプ溶液を希釈している。この回転数の抑制により撹拌力が過剰となって動力費に無駄が生じることや騒音の抑制を行っている。   In the above-mentioned pulper section, the agitation blade in the agitation tank is rotated at a disaggregation speed (750 rpm) to disaggregate waste paper in a predetermined amount of disaggregation water to prepare a waste paper pulp solution having a disaggregation concentration (8 wt%). After that, the waste paper pulp solution is diluted to a predetermined concentration (4% by weight) by adding dilution water while rotating at a rotational speed for stirring (400 rpm). By suppressing the number of revolutions, the stirring force becomes excessive, resulting in wasted power costs and noise.

しかし、離解操作の途中において未離解の紙片がパルパー部の撹拌槽の内壁面に付着し、付着した未離解の紙片が希釈操作時に古紙パルプ溶液中に混入する場合があり、未離解の紙片が古紙パルプ溶液とともに抄紙されて再生紙の品質を低下させる要因となる問題や、あるいは混入した紙片が液位センサに付着し、撹拌槽内の液位を検出する際に検出誤作動を招く問題があった。   However, in the middle of the disaggregation operation, undisaggregated paper pieces may adhere to the inner wall surface of the stirring tank of the pulper unit, and the adhering undisaggregated paper pieces may be mixed in the waste paper pulp solution during the dilution operation. There is a problem that causes the paper to be degraded with the waste paper pulp solution and causes the quality of the recycled paper to deteriorate, or the mixed paper piece adheres to the liquid level sensor, causing a detection malfunction when detecting the liquid level in the stirring tank. there were.

また、従来は、所定濃度の古紙パルプ溶液を次工程の脱墨部へ排出した後に、撹拌槽の開口に臨んで設けた複数のシャワーヘッドから槽内に散水し、撹拌槽の内壁面に付着した古紙パルプの繊維や未離解の紙片を洗い流して撹拌槽内を洗浄し、先に述べた不具合の原因となる紙片の付着を次回の離解処理まえに解消している。しかし、シャワーヘッドは装置構成の複雑化、大型化の要因となり、コスト高の要因となる。   Also, conventionally, after discharging the waste paper pulp solution of a predetermined concentration to the deinking part of the next process, water is sprayed into the tank from a plurality of shower heads provided facing the opening of the stirring tank, and adheres to the inner wall surface of the stirring tank The fibers of the used paper pulp and undissolved paper pieces are washed away to wash the inside of the agitation tank, and the adhesion of the paper pieces causing the above-mentioned problems is eliminated before the next disaggregation treatment. However, the shower head becomes a factor of increasing the complexity and size of the apparatus, and increases the cost.

本発明は上記課題を解決するものであり、希釈処理操作の途中において撹拌槽の内壁面に付着した紙片が古紙パルプ溶液中に混入しても再生紙の品質に影響を与えず、シャワーヘッドからの散水による洗浄を不要とし、装置の小型化を実現した古紙再生処理装置を提供することを目的とする。   The present invention solves the above-mentioned problems, and even if a piece of paper adhering to the inner wall surface of the stirring tank is mixed in the waste paper pulp solution during the dilution process operation, it does not affect the quality of the recycled paper. It is an object of the present invention to provide a used paper recycling apparatus that eliminates the need for cleaning with water spray and realizes downsizing of the apparatus.

上記課題を解決するために、本発明の古紙再生処理装置は、古紙再生処理系を構成する処理部であるパルパー部と、処理部の運転を制御する制御部を備える古紙再生処理装置において、パルパー部は、撹拌槽と、撹拌槽内で撹拌羽根を回転駆動する撹拌装置と、撹拌槽に希釈用水を供給する給水部を有し、制御部は、撹拌装置を順次に離解運転モード、遷移運転モード、希釈運転モードで運転し、離解運転モードでは、撹拌羽根を離解用回転数で回転させて撹拌槽内に貯溜した所定量の離解用水中で古紙を離解処理して古紙パルプ溶液を生成し、遷移運転モードでは、給水部から撹拌槽内の古紙パルプ溶液に希釈用水を給水しつつ、撹拌羽根を離解用回転数で回転させて古紙パルプ溶液を撹拌し、希釈運転モードでは、給水部から撹拌槽内の古紙パルプ溶液に希釈用水を給水しつつ、撹拌羽根を離解用回転数より低速の撹拌用回転数で回転させて古紙パルプ溶液を撹拌する。   In order to solve the above-described problems, a used paper recycling processing apparatus according to the present invention includes a pulper unit that is a processing unit constituting a used paper recycling processing system, and a used paper recycling processing apparatus that includes a control unit that controls operation of the processing unit. The unit has a stirring tank, a stirring device that rotationally drives the stirring blades in the stirring tank, and a water supply unit that supplies dilution water to the stirring tank, and the control unit sequentially turns the stirring device into disaggregation operation mode and transition operation. In the disaggregation operation mode, the waste paper is disaggregated in a predetermined amount of disaggregation water stored in the agitation tank by rotating the agitation blade at the disaggregation speed to generate a waste paper pulp solution. In the transition operation mode, while the dilution water is supplied from the water supply unit to the waste paper pulp solution in the stirring tank, the agitation blade is rotated at the rotational speed for disaggregation to stir the waste paper pulp solution. In the dilution operation mode, from the water supply unit In the stirring tank While water and water for dilution in the paper pulp solution, by rotating the stirring blades at a stirring rotation speed slower than the macerating rotation speed for stirring the used paper pulp solution.

本発明の古紙再生処理装置において、撹拌槽内の古紙パルプ溶液の濃度を検出する濃度検出部を備え、制御部は、古紙パルプ溶液の濃度を指標として運転モードを切り替え、遷移処理操作における遷移終期濃度で遷移運転モードから希釈運転モードに切り替え、遷移終期濃度は、離解運転モードにおける離解終期濃度よりも低く設定し、希釈運転モードの希釈処理操作における希釈終期濃度よりも高く設定することを特徴とする。   In the used paper recycling treatment apparatus of the present invention, the waste paper recycling processing apparatus includes a concentration detection unit that detects the concentration of the used paper pulp solution in the stirring tank, and the control unit switches the operation mode using the concentration of the used paper pulp solution as an index, and the transition end in the transition processing operation. Switching from the transition operation mode to the dilution operation mode by concentration, the transition end concentration is set lower than the end disaggregation concentration in the disaggregation operation mode, and set higher than the end dilution concentration in the dilution processing operation in the dilution operation mode. To do.

本発明の古紙再生処理装置において、処理部として撹拌槽へ古紙を投入する古紙投入部を備え、古紙投入部が撹拌槽に投入する古紙投入量を計測する重量センサを有し、給水部が撹拌槽に供給する水量を計測する流量センサを有し、濃度検出部が、重量センサの計測値と流量センサの計測値から古紙パルプ溶液の濃度を算出することを特徴とする。   In the used paper recycling apparatus of the present invention, the processing unit includes a used paper input unit that inputs used paper into the agitation tank, the used paper input unit has a weight sensor that measures the amount of used paper input to the agitation tank, and the water supply unit is agitated It has a flow sensor for measuring the amount of water supplied to the tank, and the concentration detector calculates the concentration of the used paper pulp solution from the measured value of the weight sensor and the measured value of the flow sensor.

本発明の古紙再生処理装置において、処理部として撹拌槽へ古紙を投入する古紙投入部を備え、古紙投入部は古紙を複数回にわたって撹拌槽へ投入し、制御部は、古紙投入部の古紙投入操作中に撹拌装置を離解準備運転モードで運転し、離解準備運転モードでは、撹拌羽根を撹拌用回転数より低速の粗裂拡散用回転数で回転させて投入した古紙を粗く引き裂くことを特徴とする。   In the used paper recycling apparatus of the present invention, the processing unit includes a used paper input unit that inputs used paper into the stirring tank, the used paper input unit inputs the used paper into the stirring tank a plurality of times, and the control unit inputs the used paper of the used paper input unit. During operation, the stirrer is operated in the disaggregation preparation operation mode, and in the disaggregation preparation operation mode, the used paper is roughly torn by rotating the stirring blade at a rotation speed for rough crack diffusion lower than the rotation speed for stirring. To do.

以上のように本発明によれば、離解運転モードと希釈運転モードとの間において遷移運転モードで撹拌装置を駆動し、遷移運転モードにおいて、古紙パルプ溶液に希釈用水を給水しつつ、撹拌羽根を離解用回転数で回転させることで、離解運転モード時に撹拌槽の内壁面に付着した古紙の紙片を槽内液位の上昇にともなって古紙パルプ溶液中に取り込み、離解用回転数下で離解処理する。このため、希釈運転モードにおいて古紙パルプ溶液中に古紙の粗い紙片が残ることを抑制でき、後工程の抄紙において紙片に起因する品質の低下を防止できる。また、槽内液位の上昇中に古紙パルプ溶液に強く撹拌作用を及ぼすことで、槽内壁面が古紙パルプ溶液で効果的に洗われて紙片が洗浄されるので、シャワーヘッドからの散水による洗浄を不要とし、装置の小型化を実現できる。   As described above, according to the present invention, the stirring device is driven in the transition operation mode between the disaggregation operation mode and the dilution operation mode, and in the transition operation mode, the stirring blade is supplied while supplying the dilution water to the waste paper pulp solution. By rotating at the speed of disaggregation, waste paper adhering to the inner wall surface of the stirring tank in the disaggregation operation mode is taken into the waste paper pulp solution as the liquid level in the tank rises, and disaggregation is performed at the speed of disaggregation. To do. For this reason, it can suppress that the paper piece with a rough used paper remains in a used paper pulp solution in dilution operation mode, and can prevent the quality fall resulting from a paper piece in papermaking of a post process. In addition, since the inner wall surface of the tank is effectively washed with the used paper pulp solution and the paper pieces are washed by strongly agitating the used paper pulp solution while the liquid level in the tank is rising, washing by watering from the shower head Can be reduced, and the size of the apparatus can be reduced.

本発明の実施の形態における古紙再生処理装置の処理フローを示すフローチャートThe flowchart which shows the processing flow of the used paper reproduction | regeneration processing apparatus in embodiment of this invention 同古紙再生処理装置を示すブロック図Block diagram showing the used paper recycling system 同古紙再生処理装置のパルパー部を示す断面図Sectional view showing the pulper unit of the used paper recycling processor 同抄紙部の構成を示す模式図Schematic diagram showing the structure of the papermaking section 従来の処理方法におけるフローチャートFlowchart in conventional processing method

以下、本発明の実施の形態を図面に基づいて説明する。図2に示すように、古紙再生処理装置は、古紙再生処理系を構成する複数の処理部を有しており、処理部には古紙投入部1、パルパー部9、脱墨部11、抄紙部13、乾燥部14、仕上部15、白水タンク部100、脱墨廃液処理装置101がある。また、古紙再生処理装置は各処理部の運転を制御する制御部700を備えている。   Hereinafter, embodiments of the present invention will be described with reference to the drawings. As shown in FIG. 2, the used paper recycling processing apparatus has a plurality of processing units constituting a used paper recycling processing system, and the processing units include a used paper feeding unit 1, a pulper unit 9, a deinking unit 11, and a paper making unit. 13, a drying unit 14, a finishing unit 15, a white water tank unit 100, and a deinking waste liquid treatment apparatus 101. In addition, the used paper recycling apparatus includes a control unit 700 that controls the operation of each processing unit.

本実施の形態において、古紙投入部1は、再生原料の枚葉紙の古紙をパルパー部9に投入するものであり、パルパー部9は、古紙を離解用水中で離解させて古紙パルプを含む古紙パルプ溶液を調整する。古紙投入部1およびパルパー部9の詳細は後述する。   In the present embodiment, the used paper input unit 1 inputs used recycled paper sheets into the pulper unit 9, and the pulper unit 9 disintegrates the used paper in the disaggregation water to contain used paper pulp. Prepare pulp solution. Details of the used paper input unit 1 and the pulper unit 9 will be described later.

脱墨部11は、脱墨槽501において古紙パルプ溶液を脱墨処理し、古紙パルプ溶液中の繊維、インク等の固形分を含んだ脱墨廃液を分離除去し、脱墨した古紙パルプ溶液を抄紙部13に送るとともに、脱墨廃液を取出し口から脱墨排水系102を通して脱墨廃液処理装置101に供給する。   The deinking unit 11 deinks the waste paper pulp solution in the deinking tank 501, separates and removes the deinking waste liquid containing solids such as fibers and ink in the waste paper pulp solution, and removes the deinked waste paper pulp solution. While being sent to the paper making unit 13, the deinking waste liquid is taken out from the outlet and supplied to the deinking waste liquid processing apparatus 101 through the deinking drainage system 102.

図4に示すように、抄紙部13は、脱墨された古紙パルプ溶液から湿紙12を抄紙するものであり、複数のローラ41に巻回されたメッシュ状のベルトからなる抄紙ワイヤー42と、脱墨された古紙パルプ溶液を抄紙ワイヤー42上に注ぐヘッドボックス43を有している。   As shown in FIG. 4, the paper making unit 13 is for making the wet paper 12 from the deinked waste paper pulp solution, and a paper making wire 42 made of a mesh-like belt wound around a plurality of rollers 41; A head box 43 for pouring the deinked waste paper pulp solution onto the paper making wire 42 is provided.

抄紙ワイヤー42の無端軌道は、ヘッドボックス43から後述する乾燥ローラ49に至るまでの往路部と、乾燥ローラ49の一部を覆う転移部と、乾燥ローラ49からヘッドボックス43に戻る復路部からなる。   The endless track of the paper making wire 42 includes an outward path portion from the head box 43 to a later-described drying roller 49, a transition portion that covers a part of the drying roller 49, and a return path portion that returns from the drying roller 49 to the head box 43. .

抄紙ワイヤー42の往路部には、抄紙ワイヤー42の下部側でヘッドボックス43の近くに、抄紙ワイヤー42の下面に摺接して抄紙ワイヤー42の下面から滴る水を払う水切り部44と、抄紙ワイヤー42を介して湿紙12から水分を吸引する吸引装置45を設けている。   In the forward path portion of the papermaking wire 42, a draining portion 44 that slides on the lower surface of the papermaking wire 42 and drops water dripping from the lower surface of the papermaking wire 42 near the head box 43 on the lower side of the papermaking wire 42, and the papermaking wire 42 A suction device 45 for sucking moisture from the wet paper 12 is provided.

さらに吸引装置45の下流側には、複数の絞りローラ41a、41bが抄紙ワイヤー42を挟んで位置しており、絞りローラ41a、41bによって双方のローラ間を通過する抄紙ワイヤー42上の湿紙12を絞る。ヘッドボックス43から抄紙ワイヤー42に供給された直後の湿紙12の含水率を100重量%とすると、絞りローラ41a、41bを通過した湿紙12は、含水率が60−65重量%である。   Further, on the downstream side of the suction device 45, a plurality of squeezing rollers 41a and 41b are located with the paper making wire 42 interposed therebetween, and the wet paper 12 on the paper making wire 42 passing between both rollers by the squeezing rollers 41a and 41b. Squeeze. When the moisture content of the wet paper 12 immediately after being supplied from the head box 43 to the papermaking wire 42 is 100% by weight, the wet paper 12 having passed through the squeezing rollers 41a and 41b has a moisture content of 60 to 65% by weight.

乾燥部14は、脱水された湿紙12を乾燥する乾燥ローラ49を備えており、乾燥ローラ49は加熱装置を内蔵している。乾燥ローラ49の一部は複数のローラ50に巻回したカンバスベルト51が無端軌道の一部で乾燥ローラ49を覆っており、乾燥部14においてカンバスベルト51と乾燥ローラ49の外周面との間に湿紙12を挟み、乾燥ローラ49で湿紙12を乾燥させる。抄紙ワイヤー42の転移部とカンバスベルト51との間には、乾燥ローラ49に湿紙12を押圧するカレンダローラ50aを設けている。   The drying unit 14 includes a drying roller 49 that dries the dehydrated wet paper 12. The drying roller 49 has a built-in heating device. A part of the drying roller 49 is covered with a canvas belt 51 wound around a plurality of rollers 50 and covers the drying roller 49 with a part of the endless track, and the drying unit 14 is provided between the canvas belt 51 and the outer peripheral surface of the drying roller 49. The wet paper 12 is sandwiched between the two, and the wet paper 12 is dried by the drying roller 49. A calender roller 50 a that presses the wet paper 12 against the drying roller 49 is provided between the transition portion of the paper making wire 42 and the canvas belt 51.

カンバスベルト51の往路終端位置でスクレーパ111が乾燥した乾紙61を乾燥ローラ49から剥離させて仕上部15に案内する。
仕上部15は、湿紙12を乾燥して得られる乾紙61に対して仕上工程を行い、得られた再生紙62を紙受部63に排出するものであり、乾紙61を所定のサイズに切断する金属製のカッター装置60およびスリッター装置112が設けられている。
The dry paper 61 dried by the scraper 111 at the forward end position of the canvas belt 51 is peeled off from the drying roller 49 and guided to the finishing unit 15.
The finishing unit 15 performs a finishing process on the dry paper 61 obtained by drying the wet paper 12, and discharges the obtained recycled paper 62 to the paper receiving unit 63. The dry paper 61 is a predetermined size. A metal cutter device 60 and a slitter device 112 are provided.

白水タンク部100は、抄紙排水系104を通して抄紙部13から流入する古紙パルプを含む排水である白水を貯留するものであり、白水を白水返送系105、106を通して古紙再生処理系の各所へ返送する。パルパー部9に連通する白水返送系106は、パルパー部9の撹拌槽901に離解用水および希釈用水として白水を供給する。   The white water tank unit 100 stores white water, which is waste water containing waste paper pulp flowing from the paper making unit 13 through the paper making drainage system 104, and returns the white water to various parts of the used paper recycling processing system through the white water return systems 105 and 106. . The white water return system 106 communicating with the pulper unit 9 supplies white water as the disaggregation water and dilution water to the stirring tank 901 of the pulper unit 9.

給水源、ここでは上水配管107から用水を供給する給水配管108が白水タンク部100に接続しており、給水配管108に電磁弁からなる緊急停止用の元弁装置109を設けている。   A water supply source 108, here, a water supply pipe 108 for supplying water from a water supply pipe 107 is connected to the white water tank section 100, and a main valve device 109 for emergency stop including an electromagnetic valve is provided in the water supply pipe 108.

脱墨廃液処理装置101は、脱墨部11から脱墨排水系102を通して供給する脱墨廃液を処理するもので、古紙パルプの繊維、インク、トナー等の固形成分と液相成分とを分離する。   The deinking waste liquid processing apparatus 101 processes the deinking waste liquid supplied from the deinking unit 11 through the deinking drainage system 102, and separates solid components and liquid phase components such as fibers, ink, and toner of waste paper pulp. .

図3に示すように、古紙投入部1は、パルパー部9の撹拌槽901の上方に位置し、再生原料の古紙を枚葉紙のままで直接にパルパー部9に投入するものである。古紙投入部1は、枚葉紙を立った姿勢に保持する姿勢保持部203を有し、姿勢保持部203が上部開口と下部開口を有する上下開放の四角形の枠体からなり、投入口をなす下部開口が撹拌槽901の上部開口に対向している。姿勢保持部203の底部をなすスライド底板206は、姿勢保持部203の下部開口を覆っており、スライド底板206は下部開口を開閉するスライド方向に移動可能である。   As shown in FIG. 3, the used paper input unit 1 is located above the stirring tank 901 of the pulper unit 9, and inputs the recycled paper used as a raw material directly into the pulper unit 9 as a sheet. The used paper feeding unit 1 has a posture holding unit 203 that holds a sheet in an upright posture, and the posture holding unit 203 is formed of a rectangular frame body having an upper opening and a lower opening and having an upper opening and a lower opening. The lower opening faces the upper opening of the stirring tank 901. A slide bottom plate 206 forming the bottom of the posture holding unit 203 covers a lower opening of the posture holding unit 203, and the slide bottom plate 206 is movable in a sliding direction for opening and closing the lower opening.

古紙投入部1は姿勢保持部203に積載した古紙の重量を計測するロードセル等からなる重量センサ(図示省略)を備えており、姿勢保持部203には姿勢保持補助板203aを設けており、姿勢保持補助板203aが姿勢保持部203の枚葉紙積載空間を複数の分室に区分している。   The used paper input unit 1 includes a weight sensor (not shown) including a load cell that measures the weight of used paper loaded on the posture holding unit 203. The posture holding unit 203 is provided with a posture holding auxiliary plate 203a. The holding auxiliary plate 203a divides the sheet stacking space of the posture holding unit 203 into a plurality of compartments.

ユーザーに対する安全性を確保するために、姿勢保持部203の上部開口を覆ってカバー部301を設けており、カバー部301は透明の扉体302を備えている。
パルパー部9は、撹拌槽901の内部に撹拌装置として撹拌羽根902と撹拌羽根902を回転駆動する回転軸903を有している。回転軸903は下端を槽底部に枢着し、撹拌槽901の上方に配置した上下二つの軸受904、905で回転自在に支持され、上下の軸受904、905の間にプーリー906を有し、プーリー906がベルト907を介して撹拌羽根駆動モータ922で駆動されることで、回転軸903および撹拌羽根902が回転する。撹拌羽根駆動モータ922はトルクセンサ923を有している。
In order to ensure safety for the user, a cover part 301 is provided to cover the upper opening of the posture holding part 203, and the cover part 301 includes a transparent door body 302.
The pulper unit 9 includes a stirring blade 902 and a rotating shaft 903 that rotationally drives the stirring blade 902 as a stirring device inside the stirring tank 901. The rotary shaft 903 is pivotally attached to the bottom of the tank, is rotatably supported by two upper and lower bearings 904 and 905 disposed above the stirring tank 901, and has a pulley 906 between the upper and lower bearings 904 and 905. The pulley 906 is driven by the stirring blade drive motor 922 via the belt 907, whereby the rotating shaft 903 and the stirring blade 902 rotate. The stirring blade drive motor 922 has a torque sensor 923.

撹拌槽901は槽底部に取出し口908を有し、取出し口908に移送部909が接続している。移送部909は撹拌槽901で離解処理した古紙パルプ溶液を脱墨部11に移送する移送経路をなし、移送ポンプとしてチューブポンプ910を有している。   The stirring tank 901 has an extraction port 908 at the bottom of the tank, and a transfer unit 909 is connected to the extraction port 908. The transfer unit 909 forms a transfer path for transferring the waste paper pulp solution disaggregated in the stirring tank 901 to the deinking unit 11 and includes a tube pump 910 as a transfer pump.

撹拌槽901の開口に臨んで設けた給水部911は希釈用水を撹拌槽901に供給するものであり、給水部911に渦式流量計や羽根車式流量計からなる流量センサ921を介して白水返送系106が接続している。また、移送部909にはチューブポンプ910の下流位置に第2給水部として白水返送系105が接続している。   A water supply unit 911 provided facing the opening of the agitation tank 901 supplies dilution water to the agitation tank 901, and white water is supplied to the water supply part 911 via a flow rate sensor 921 comprising a vortex flow meter or an impeller flow meter. A return system 106 is connected. Further, a white water return system 105 is connected to the transfer unit 909 as a second water supply unit at a downstream position of the tube pump 910.

撹拌槽901の内部には、古紙パルプ溶液の液位を検出する液位センサとして、槽内に貯溜可能な上限液位に対応する上限液位検出センサ912と、槽内の撹拌羽根902の位置に対応する下限液位検出センサ913と、古紙パルプ溶液の所定量を貯溜した際の規定残量液位に対応する規定残量液位検出センサ914を設けている。   Inside the stirring tank 901, as a liquid level sensor for detecting the liquid level of the used paper pulp solution, an upper limit liquid level detection sensor 912 corresponding to the upper limit liquid level that can be stored in the tank, and the positions of the stirring blades 902 in the tank And a lower limit liquid level detection sensor 914 corresponding to a predetermined remaining liquid level when a predetermined amount of used paper pulp solution is stored.

制御部700は濃度検出部701を有し、濃度検出部701は重量センサ207の重量計測値および流量センサ921の流量計測値に基づいて古紙パルプ溶液の濃度を算出する。   The control unit 700 has a concentration detection unit 701, and the concentration detection unit 701 calculates the concentration of the used paper pulp solution based on the weight measurement value of the weight sensor 207 and the flow rate measurement value of the flow rate sensor 921.

以下、上記した構成の作用を説明する。制御部700は、古紙投入部1とパルパー部9と脱墨部11と抄紙部13と仕上部15と白水タンク部100と脱墨廃液処理装置101とを制御し、各処理部において古紙再生処理系の運転を行う。   The operation of the above configuration will be described below. The control unit 700 controls the used paper input unit 1, the pulper unit 9, the deinking unit 11, the paper making unit 13, the finishing unit 15, the white water tank unit 100, and the deinking waste liquid processing apparatus 101. Run the system.

古紙投入部1のスライド底板206を全閉位置に配置し、この状態でカバー部301の扉体302を開放し、姿勢保持部203の枠体内に枚葉紙の束を搭載する。スライド底板206をスライド方向の開方向に移動させ、姿勢保持部203の下部開口を開放する。枚葉紙は、姿勢保持補助板203aで区分された室毎に、スライド底板206が開くに伴って立った姿勢のままに下部開口からパルパー部9の撹拌槽901に順次に投下される。撹拌槽901は、給水部911から供給する所定量の白水を離解用水として貯溜している。   The slide bottom plate 206 of the used paper input unit 1 is disposed at the fully closed position, and in this state, the door body 302 of the cover unit 301 is opened, and a bundle of sheets is mounted in the frame body of the posture holding unit 203. The slide bottom plate 206 is moved in the opening direction of the sliding direction, and the lower opening of the posture holding unit 203 is opened. The sheets are sequentially dropped from the lower opening to the agitation tank 901 of the pulper unit 9 in a standing position as the slide bottom plate 206 is opened for each chamber divided by the posture holding auxiliary plate 203a. The stirring tank 901 stores a predetermined amount of white water supplied from the water supply unit 911 as disaggregation water.

次に、制御部700は、パルパー部9の撹拌装置を順次に離解運転モード、遷移運転モード、希釈運転モードで運転する。
本実施の形態においては、古紙投入部1が古紙を複数回にわたって撹拌槽901へ投入するが、古紙の投入は1回で行うことも可能である。
Next, the control unit 700 sequentially operates the stirring device of the pulper unit 9 in the disaggregation operation mode, the transition operation mode, and the dilution operation mode.
In the present embodiment, the used paper input unit 1 inputs the used paper into the stirring tank 901 a plurality of times, but it is also possible to input the used paper once.

制御部700は古紙投入部1の古紙投入操作中に撹拌羽根902を離解準備運転モードで運転する。離解準備運転モードでは、撹拌羽根902を撹拌用回転数の750rpmより低速の粗裂拡散用回転数200rpmで回転させて投入した古紙を粗く引き裂く粗裂処理を行う。   The control unit 700 operates the stirring blade 902 in the disaggregation preparation operation mode during the used paper input operation of the used paper input unit 1. In the disaggregation preparation operation mode, a rough tearing process is performed in which the stirrer blade 902 is rotated at a rotational speed for rough crack diffusion of 200 rpm, which is lower than the rotational speed for stirring of 750 rpm, and the used paper is roughly torn.

すなわち、図1に示すように、パルパー部9では、所定量の撹拌用水を注水し(S11)、その後に古紙を投入し(S12)、続いて粗裂処理し(S13)、再び古紙を投入し(S14)、続いて粗裂処理し(S15)する。   That is, as shown in FIG. 1, in the pulper unit 9, a predetermined amount of agitation water is poured (S11), then used paper is added (S12), followed by a rough tearing process (S13), and used paper is again input. (S14), followed by rough cracking (S15).

このため、先に撹拌槽901に投入した古紙と、後で撹拌槽901に投入した古紙とが撹拌槽901の槽内で混在する場合にあっても、先に投入した古紙がその重なりをほぐされるとともに、粗く引き裂かれた紙片となっており、後で投入する古紙が離解用水中に浸漬されることを阻害せず、投入時期にかかわらず、離解処理に先だって古紙が粗く引き裂さかれた状態となり、離解処理を円滑に行うことができる。   For this reason, even when the waste paper previously fed into the stirring tank 901 and the waste paper later thrown into the stirring tank 901 are mixed in the tank of the stirring tank 901, the waste paper introduced earlier loosens the overlap. In addition, the paper was roughly torn and did not prevent the waste paper to be introduced later from being immersed in the water for disaggregation, and the waste paper was roughly torn prior to the disaggregation process regardless of the time of introduction. It will be in a state and a disaggregation process can be performed smoothly.

次に、離解運転モード(S16)では、撹拌羽根902を離解用回転数の750rpmで回転させて撹拌槽901の槽内に貯溜した所定量の離解用水中で古紙を離解処理し、離解処理操作の終期における離解終期濃度が8重量%となる古紙パルプ溶液を生成する。離解処理操作の終期は、トルクセンサ923で計測する負荷によって検知し、離解処理の進行にともなってトルクが低下し、トルクセンサ923の計測値が所定値に達した時点を離解が完了した時とする。離解処理操作の終期は、離解処理の進行にともなって上昇する古紙パルプ溶液の温度15℃から20℃によっても検知することが可能である。また、タイマー制御によっても離解処理操作の終期を検知できる。   Next, in the disaggregation operation mode (S16), the waste paper is disaggregated in a predetermined amount of disaggregation water stored in the agitation tank 901 by rotating the agitation blade 902 at a disaggregation rotation speed of 750 rpm, and the disaggregation processing operation is performed. This produces a waste paper pulp solution with a final disaggregation concentration of 8% by weight at the end of. The end of the disaggregation processing operation is detected by the load measured by the torque sensor 923, and when the disaggregation is completed when the torque decreases with the progress of the disaggregation processing and the measured value of the torque sensor 923 reaches a predetermined value. To do. The end of the disaggregation treatment operation can also be detected by a temperature of 15 ° C. to 20 ° C. of the waste paper pulp solution that rises with the progress of the disaggregation treatment. The end of the disaggregation processing operation can also be detected by timer control.

遷移運転モード(S17)では、撹拌槽901の古紙パルプ溶液に給水部911から希釈用水を給水しつつ、撹拌羽根902を離解用回転数の750rpmで回転させて古紙パルプ溶液を撹拌し、8重量%の離解終期濃度から離解処理操作の終期における6重量%の遷移終期濃度にまで希釈する。   In the transition operation mode (S17), while the dilution water is supplied from the water supply unit 911 to the waste paper pulp solution in the stirring tank 901, the stirring blade 902 is rotated at a disaggregation speed of 750 rpm, and the waste paper pulp solution is stirred to 8 weight. Dilute to a final concentration of 6% by weight at the end of the disaggregation operation.

このとき、制御部700は、投入した古紙量、つまり重量センサ207で計測した古紙量から古紙パルプ溶液を6重量%の遷移終期濃度とするのに必要な、不足する希釈水量を算出し、その算出量を給水部911から供給し、古紙パプル溶液を遷移終期濃度に調整する。遷移処理操作の終期は、タイマー制御によって検知する(S18)。   At this time, the controller 700 calculates the amount of diluted water that is insufficient to make the waste paper pulp solution 6% by weight transition end concentration from the amount of used paper that has been input, that is, the amount of used paper measured by the weight sensor 207, The calculated amount is supplied from the water supply unit 911, and the used paper pulp solution is adjusted to the transition end concentration. The end of the transition processing operation is detected by timer control (S18).

また、遷移処理操作の終期は、古紙パルプ溶液の濃度の変化によっても検知できる。すなわち、制御部700の濃度検出部701が、重量センサ207の重量計測値と流量センサ921の流量計測値から古紙パルプ溶液の濃度を算出する。制御部700は、給水部911からの給水が終了した時点で古紙パルプ溶液が遷移終期濃度の6重量%に達したとして、この古紙パルプ溶液の遷移終期濃度で遷移運転モードから希釈運転モードに切り替える。遷移処理操作の終期は、トルクセンサ923の計測値によっても検知できる。   The end of the transition processing operation can also be detected by a change in the concentration of the used paper pulp solution. That is, the concentration detection unit 701 of the control unit 700 calculates the concentration of the used paper pulp solution from the weight measurement value of the weight sensor 207 and the flow rate measurement value of the flow rate sensor 921. The controller 700 switches from the transition operation mode to the dilution operation mode at the transition end concentration of the waste paper pulp solution, assuming that the waste paper pulp solution has reached 6% by weight of the transition end concentration at the time when the water supply from the water supply unit 911 is completed. . The end of the transition processing operation can also be detected by the measured value of the torque sensor 923.

このように、離解運転モードと希釈運転モードとの間で実施する遷移運転モードにおいて、古紙パルプ溶液に希釈用水を給水しつつ、撹拌羽根902を離解用回転数で回転させることで、離解運転モード時に撹拌槽901の内壁面に付着した古紙の紙片を槽内液位の上昇にともなって古紙パルプ溶液中に取り込み、離解用回転数下で離解処理し、少なくとも脱墨部11へ供給可能な細かな形状にまで離解させることができる。   Thus, in the transition operation mode performed between the disaggregation operation mode and the dilution operation mode, the disintegration operation mode is performed by rotating the stirring blade 902 at the disaggregation rotation speed while supplying dilution water to the waste paper pulp solution. A piece of waste paper attached to the inner wall surface of the stirring tank 901 is sometimes taken into the waste paper pulp solution as the liquid level in the tank rises, is disaggregated at a disaggregation speed, and can be supplied to at least the deinking unit 11 Can be disaggregated to a simple shape.

このため、希釈運転モードにおいて古紙パルプ溶液中に古紙の粗い紙片が残ることを抑制でき、後工程の抄紙部13の抄紙において紙片に起因する品質の低下を防止できる。また、槽内液位の上昇中に古紙パルプ溶液に強く撹拌作用を及ぼすことで、槽内壁面が古紙パルプ溶液で効果的に洗われて紙片が洗浄されるので、従来のようなシャワーヘッドからの散水による洗浄を不要とし、装置の小型化を実現できる。   For this reason, it is possible to suppress the remaining waste paper pieces from remaining in the waste paper pulp solution in the dilution operation mode, and it is possible to prevent the quality from being deteriorated due to the paper pieces in the paper making of the paper making unit 13 in the subsequent process. In addition, by strongly agitating the used paper pulp solution during the rise of the liquid level in the tank, the inner wall surface of the tank is effectively washed with the used paper pulp solution and the paper pieces are washed. This eliminates the need for cleaning with water spraying, and can reduce the size of the apparatus.

希釈運転モード(S19)では、給水部911から撹拌槽901の古紙パルプ溶液に希釈用水を給水しつつ、撹拌羽根902を離解用回転数の750rpmより低速の撹拌用回転数の400rpmで回転させて古紙パルプ溶液を撹拌し、6重量%の遷移終期濃度から希釈処理操作の終期における4重量%の希釈終期濃度にまで希釈する。この希釈終期濃度は古紙パルプ溶液をチューブポンプ910で脱墨部11に供給するためであり、チューブポンプ910の仕様によって希釈終期濃度が設定される。古紙パルプ溶液の濃度が4重量%に達した時点で(S20)、終了する(S21)。   In the dilution operation mode (S19), while supplying dilution water to the waste paper pulp solution in the stirring tank 901 from the water supply unit 911, the stirring blade 902 is rotated at a rotation speed of 400 rpm, which is lower than the rotation speed of 750 rpm. The waste paper pulp solution is stirred and diluted from a 6% by weight transition end concentration to a 4% by weight end dilution concentration at the end of the dilution process operation. This final concentration of dilution is for supplying the waste paper pulp solution to the deinking unit 11 with the tube pump 910, and the final concentration of dilution is set according to the specifications of the tube pump 910. When the concentration of the used paper pulp solution reaches 4% by weight (S20), the process ends (S21).

次に、撹拌羽根902を回転させて古紙パルプ溶液を撹拌しつつ、移送部909のチューブポンプ910を駆動して撹拌槽901の取出し口908から古紙パルプ溶液を取出し、脱墨部11に移送する。   Next, while stirring the used paper pulp solution by rotating the stirring blade 902, the tube pump 910 of the transfer unit 909 is driven to take out the used paper pulp solution from the takeout port 908 of the stirring tank 901 and transfer it to the deinking unit 11. .

1 古紙投入部
9 パルパー部
11 脱墨部
12 湿紙
13 抄紙部
14 乾燥部
15 仕上部
41 ローラ
41a、41b 絞りローラ
42 抄紙ワイヤー
43 ヘッドボックス
44 水切り部
45 吸引装置
49 乾燥ローラ
50 ローラ
50a カレンダローラ
51 カンバスベルト
60 カッター装置
61 乾紙
62 再生紙
63 紙受部
100 白水タンク部
101 脱墨廃液処理装置
102 脱墨排水系
104 抄紙排水系
105、106 白水返送系
107 上水配管
108 給水配管
109 元弁装置
111 スクレーパ
112 スリッター装置
203 姿勢保持部
203a 姿勢保持補助板
206 スライド底板
207 重量センサ
301 カバー部
302 扉体
501 脱墨槽
700 制御部
701 濃度検出部
901 撹拌槽
902 撹拌羽根
903 回転軸
904、905 軸受
906 プーリー
907 ベルト
908 取出し口
909 移送部
910 チューブポンプ
911 給水部
912 上限液位検出センサ
913 下限液位検出センサ
914 規定残量液位検出センサ
921 流量センサ
922 撹拌羽根駆動モータ
923 トルクセンサ
DESCRIPTION OF SYMBOLS 1 Used paper input part 9 Pulper part 11 Deinking part 12 Wet paper 13 Paper making part 14 Drying part 15 Finishing part 41 Roller 41a, 41b Drawing roller 42 Paper making wire 43 Head box 44 Draining part 45 Suction device 49 Drying roller 50 Roller 50a Calendar roller 51 canvas belt 60 cutter device 61 dry paper 62 recycled paper 63 paper receiving unit 100 white water tank unit 101 deinking waste liquid treatment device 102 deinking drainage system 104 papermaking drainage system 105, 106 white water return system 107 water supply pipe 108 water supply pipe 109 yuan Valve device 111 Scraper 112 Slitter device 203 Posture holding unit 203a Posture holding auxiliary plate 206 Slide bottom plate 207 Weight sensor 301 Cover unit 302 Door body 501 Deinking tank 700 Control unit 701 Concentration detection unit 901 Stirring blade 902 Stirring blade 903 Rotating shaft 904 905 bearing 906 pulley 907 belt 908 outlet 909 transfer unit 910 tube pump 911 water supply unit 912 upper liquid level detection sensor 913 lower liquid level detection sensor 914 defining the remaining liquid level detection sensor 921 flow sensor 922 stirring blade driving motor 923 torque sensor

Claims (4)

古紙再生処理系を構成する処理部であるパルパー部と、処理部の運転を制御する制御部を備える古紙再生処理装置において、
パルパー部は、撹拌槽と、撹拌槽内で撹拌羽根を回転駆動する撹拌装置と、撹拌槽に希釈用水を供給する給水部を有し、
制御部は、撹拌装置を順次に離解運転モード、遷移運転モード、希釈運転モードで運転し、
離解運転モードでは、撹拌羽根を離解用回転数で回転させて撹拌槽内に貯溜した所定量の離解用水中で古紙を離解処理して古紙パルプ溶液を生成し、
遷移運転モードでは、給水部から撹拌槽内の古紙パルプ溶液に希釈用水を給水しつつ、撹拌羽根を離解用回転数で回転させて古紙パルプ溶液を撹拌し、
希釈運転モードでは、給水部から撹拌槽内の古紙パルプ溶液に希釈用水を給水しつつ、撹拌羽根を離解用回転数より低速の撹拌用回転数で回転させて古紙パルプ溶液を撹拌することを特徴とする古紙再生処理装置。
In a used paper recycling processing apparatus comprising a pulper unit, which is a processing unit constituting a used paper recycling processing system, and a control unit that controls the operation of the processing unit,
The pulper unit has a stirring tank, a stirring device that rotationally drives the stirring blade in the stirring tank, and a water supply unit that supplies dilution water to the stirring tank,
The control unit sequentially operates the stirring device in the disaggregation operation mode, the transition operation mode, and the dilution operation mode,
In the disaggregation operation mode, the waste paper is disaggregated in a predetermined amount of the disaggregation water stored in the agitation tank by rotating the stirring blade at the disaggregation rotation speed to generate a waste paper pulp solution.
In the transition operation mode, while supplying the dilution water from the water supply unit to the used paper pulp solution in the stirring tank, the stirring blade is rotated at the rotational speed for disaggregation to stir the used paper pulp solution.
In the dilution operation mode, the waste paper pulp solution is agitated by rotating the stirring blade at a lower rotation speed than the disaggregation rotation speed while supplying dilution water from the water supply section to the waste paper pulp solution in the stirring tank. Used paper recycling processing equipment.
撹拌槽内の古紙パルプ溶液の濃度を検出する濃度検出部を備え、
制御部は、古紙パルプ溶液の濃度を指標として運転モードを切り替え、遷移処理操作における遷移終期濃度で遷移運転モードから希釈運転モードに切り替え、
遷移終期濃度は、離解運転モードにおける離解終期濃度よりも低く設定し、希釈運転モードの希釈処理操作における希釈終期濃度よりも高く設定することを特徴とする請求項1に記載の古紙再生処理装置。
Provided with a concentration detector that detects the concentration of waste paper pulp solution in the stirring tank,
The control unit switches the operation mode using the concentration of the waste paper pulp solution as an index, switches from the transition operation mode to the dilution operation mode at the transition end concentration in the transition processing operation,
2. The used paper recycling apparatus according to claim 1, wherein the transition end concentration is set lower than the end disaggregation concentration in the disaggregation operation mode and is set higher than the end dilution concentration in the dilution processing operation in the dilution operation mode.
処理部として撹拌槽へ古紙を投入する古紙投入部を備え、
古紙投入部が撹拌槽に投入する古紙投入量を計測する重量センサを有し、
給水部が撹拌槽に供給する水量を計測する流量センサを有し、
濃度検出部が、重量センサの計測値と流量センサの計測値から古紙パルプ溶液の濃度を算出することを特徴とする請求項2に記載の古紙再生処理装置。
As a processing unit, equipped with a used paper input unit that inputs used paper to the stirring tank,
The used paper input unit has a weight sensor that measures the amount of used paper input into the agitation tank,
A water supply unit has a flow sensor for measuring the amount of water supplied to the stirring tank,
The used paper recycling apparatus according to claim 2, wherein the concentration detection unit calculates the concentration of the used paper pulp solution from the measured value of the weight sensor and the measured value of the flow rate sensor.
処理部として撹拌槽へ古紙を投入する古紙投入部を備え、
古紙投入部は古紙を複数回にわたって撹拌槽へ投入し、
制御部は、古紙投入部の古紙投入操作中に撹拌装置を離解準備運転モードで運転し、
離解準備運転モードでは、撹拌羽根を撹拌用回転数より低速の粗裂拡散用回転数で回転させて投入した古紙を粗く引き裂くことを特徴とする請求項1から3の何れか1項に記載の古紙再生処理装置。
As a processing unit, equipped with a used paper input unit that inputs used paper to the stirring tank,
The used paper input section inputs used paper into the agitation tank several times.
The control unit operates the stirring device in the disaggregation preparation operation mode during the waste paper feeding operation of the waste paper feeding unit,
4. In the disaggregation preparation operation mode, the used waste paper is roughly torn by rotating the stirring blade at a rotational speed for rough crack diffusion lower than the rotational speed for stirring. Waste paper recycling processor.
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