JPH04209882A - Method for controlling pulp concentration in pulper and pulp concentration controlling apparatus - Google Patents
Method for controlling pulp concentration in pulper and pulp concentration controlling apparatusInfo
- Publication number
- JPH04209882A JPH04209882A JP33756990A JP33756990A JPH04209882A JP H04209882 A JPH04209882 A JP H04209882A JP 33756990 A JP33756990 A JP 33756990A JP 33756990 A JP33756990 A JP 33756990A JP H04209882 A JPH04209882 A JP H04209882A
- Authority
- JP
- Japan
- Prior art keywords
- pulper
- pulp
- dilution water
- raw material
- supply
- 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
Links
- 238000000034 method Methods 0.000 title claims abstract description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 46
- 239000012895 dilution Substances 0.000 claims abstract description 34
- 238000010790 dilution Methods 0.000 claims abstract description 34
- 239000007788 liquid Substances 0.000 claims abstract description 14
- 238000003756 stirring Methods 0.000 claims abstract description 13
- 239000002994 raw material Substances 0.000 claims description 22
- 238000001514 detection method Methods 0.000 claims description 7
- 239000000203 mixture Substances 0.000 abstract description 4
- 230000008569 process Effects 0.000 abstract description 4
- 239000011259 mixed solution Substances 0.000 description 3
- 230000005540 biological transmission Effects 0.000 description 2
- 230000007246 mechanism Effects 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000003085 diluting agent Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 230000004044 response Effects 0.000 description 1
Landscapes
- Paper (AREA)
Abstract
Description
本発明は、パルパーにより原料パルプと水とを混合する
際におけるパルプ濃度の制御方法及びこの方法を実施す
るための装置に関する。The present invention relates to a method for controlling pulp concentration when mixing raw material pulp and water using a pulper, and an apparatus for implementing this method.
従来より、パルプの仕込み工程においてシートパルプ等
の原料パルプを離解するのは、一般に、槽の下部に撹拌
機を設けてなるパルパーと、多品種のシートパルプを品
種毎にストックする装置とを設け、製品としての再生パ
ルプに応じた濃度となるようにこのソートパルプと希釈
水をパルパーの中に供給し、これらを撹拌して希釈水中
にノートパルプを溶解させることで行なっていた1、こ
の方法では、混合液の濃度調整は、希釈水の供給量に応
じた重量のシートパルプを人手によってパルパー内へ供
給することで行なったり、ンートパルプをパルパーへ供
給する手段を設けるとともにその供給をタイマーを用し
)で一定間隔て行なつにり、あるいは予め混合液の濃度
を高めに設定しておいて、そこへ希釈水を追加すること
で行なったりしていた。Traditionally, raw material pulp such as sheet pulp in the pulp preparation process is generally disintegrated using a pulper equipped with an agitator at the bottom of a tank and a device that stocks various types of sheet pulp by type. This method was carried out by feeding this sorted pulp and dilution water into a pulper so that the concentration corresponded to the recycled pulp as a product, and stirring them to dissolve the note pulp in the dilution water1. In this case, the concentration of the mixed solution can be adjusted by manually feeding sheet pulp into the pulper in a weight corresponding to the amount of dilution water supplied, or by providing a means for feeding sheet pulp into the pulper and using a timer to control the feeding. This was done at regular intervals, or by setting the concentration of the mixed solution high in advance and adding dilution water to it.
ところが、これらの方法ではソートバルブを品種毎にス
トックする装置が必要であるために設備コストが高く、
同時に装置が大型化し、メンテナンス費用が増えるとい
う問題があった。
したがって、本発明の解決すべき技術的課題は、多品種
の原料パルプを用いる場合でも装置が大型化するのを防
止し9つ混合液の濃度を所望の値に調整できるようにす
ることである。However, these methods require equipment to stock sort valves by type, resulting in high equipment costs.
At the same time, there was a problem in that the equipment became larger and maintenance costs increased. Therefore, the technical problem to be solved by the present invention is to prevent the device from increasing in size even when using a wide variety of raw material pulps, and to be able to adjust the concentration of the 9-mixture to a desired value. .
本発明に係るパルパーにおけるバルブ濃度制御方法では
、上述の技術的課題を解決するために、パルパー内に供
給した原料バルブと希釈水とを混合する撹拌手段の負荷
を検出し、その検出値に応して原料パルプ及び希釈水そ
れぞれのパルパー内への供給もしくはその停止を制御す
ることにより、混合液の濃度か適正値となるように調整
される。
この方法を実施するにめの装置としては、原料パルプ及
び希釈水を混合するために槽と撹拌手段とで構成された
パルパーと、パルパーに原料パルプを供給する原料バル
ブ供給手段と、パルパーへ希釈水を供給する希釈水供給
手段を備え、さらに、撹拌時における撹拌手段の負荷を
検出する検出手段と、この検出手段の出力信号に応じて
、混合液の濃度が適性値となるように原料バルブ供給手
段による原料パルプの供給と希釈水供給手段による希釈
水の供給とを制御する制御手段を設けておけばよい。In order to solve the above-mentioned technical problem, in the valve concentration control method in a pulper according to the present invention, the load on the stirring means for mixing the raw material valve and dilution water supplied into the pulper is detected, and the load is adjusted according to the detected value. By controlling the supply or stopping of the raw material pulp and dilution water into the pulper, the concentration of the mixed liquid is adjusted to an appropriate value. The equipment for carrying out this method includes a pulper consisting of a tank and stirring means for mixing the raw material pulp and dilution water, a raw material valve supply means for supplying the raw material pulp to the pulper, and a diluent to the pulper. It is equipped with a dilution water supply means for supplying water, and further includes a detection means for detecting the load on the stirring means during stirring, and a raw material valve that adjusts the concentration of the mixed liquid to an appropriate value according to the output signal of this detection means. It is sufficient to provide a control means for controlling the supply of raw material pulp by the supply means and the supply of dilution water by the dilution water supply means.
この構成では、混合液のバルブ濃度によって異なる撹拌
手段の負荷か検出手段によって検出され、その検出値に
基づいて原料パルプと希釈水の供給もしくは停止が制御
手段によって制御さねる。したか−)で、原料パルプを
品種毎にストックする手段を設けて例えばその供給タイ
ミングをとるような方法を用いなくても、混合液は制御
手段によって常に適正な濃度に調整されるので、装置の
大型化やコストアンプなとの問題が生じることはない。In this configuration, the detection means detects the load on the stirring means that varies depending on the valve concentration of the mixed liquid, and the control means controls the supply or stop of the raw material pulp and dilution water based on the detected value. ), the mixed liquid can always be adjusted to an appropriate concentration by the control means, without having to stock the raw material pulp by type and, for example, adjust its supply timing. There are no problems such as an increase in the size of the amplifier or a cost amplifier.
以下に、第1図に示した本発明の1実施例について詳細
に説明する。
図において、1は大略円筒形の槽2と、その下部に設け
られた撹拌機3とからなるパルパーである。撹拌機3は
ベルト伝動機構4を介して駆動モータ5と接続されてい
る。また、パルパー1の上方には、原料パルプの供給手
段としてシートバルブ7用の投入コンベア6が設けられ
、且つ、希釈水の供給手段としてのポンプ8によって不
図示の水源から希釈水20を供給するパイプ9か設けら
れていて、パルパー1内にシートバルブ7と希釈水20
を供給できるようになっている。また、パルパー1内に
供給されて撹拌機3により混合されたノートバルブ7の
混合液を次の工程へ送るために、パルパー1の下部には
排出パイプ10か設けられており、その配管経路内に、
2個のバルブ11゜13とポンプ12か設けられている
。そして、このパイプ10を通る混合液を必要に応して
パルパー1内へ戻すために、バルブ13の下流側には切
り換えバルブ14と循環パイプ15とか設けられている
。
パルパーIには、内部の水位を検知してその水位に応じ
て希釈水20の供給量を制御するための水位検出計16
が取り付けられており、希釈水2゜の供給用パイプ9に
は、この水位検出計16からの信号を受けて希釈水20
の流量を調整するためのバルブ17が設けられている。
また、上述した撹拌機3の駆動モータ5には、この駆動
モータ5の負荷(混合液の濃度により変化する)を電流
値から検出するロードセンサ18が検出手段として接続
されており、その出力信号に応して投入コンベア6によ
るシートバルブ7の供給が行なわれるように、この投入
コンヘア6の駆動モータ19とロードセンサ18とか不
図示の制御手段を介して電気的に接続されている。
このロートセンサ18では、パルパー1内の混合液の濃
度に応じた電流値を直接に検出することかできる。した
かってこの構成では、混合液を撹拌する駆動モータ5の
負荷がロードセンサ18により検出されて、その結果、
負荷が小さいためにバルブ濃度が設定値よりも低いと検
出されると、制御手段から投入コンベア6にシートバル
ブ7の投入信号が送られて、ソートバルブ7がパルパー
1内へ自動的に投入される。逆に駆動モータ5の負荷が
大きいと検出された場合にはバルブ濃度は設定値よりも
高いので、シートバルブ7の投入は行なわれない。また
、このようにロードセンサ18により駆動モータ5の負
荷が大きいと検出された場合、及び水位検出計16によ
り水位が一定値以下であることが検出されに場合には、
バルブ17が開放されてパルパー1内への希釈水20の
供給か行なわれ、水位が一定値以上になっているとバル
ブ17か閉しられて、パルパー1内への希釈水20の供
給は行なわれない。
このように、上記構成では、ソートバルブを品種毎にス
トックする装置を設けずに多品種のノートバルブを無作
為に供給しても混合液の濃度を確実に所望の値に調整す
ることか可能であり、装置の大型化やコスト高といった
問題が生じることはない。また、所望の一定濃度の混合
液を連続的に効率よく取り出すことかできる。例えば、
パルパーの内径を約3m、高さを約2mとし、ll0k
Wの駆動モータを使用し1こ場合、タイマーを用いてノ
ートバルブの投入タイミングを制御していたものでは1
日7時間の運転で11900kgのソートバルブを離解
処理していたのに対し、本実施例の構成によれば、同し
量のンー゛トパルプを処理するのが僅か467時間で行
なえ、時間的に約3分の2に短縮することができた。し
たがって、作業者の労働時間を短縮でき、且つ装置の稼
動時間の短縮により電力消費量も大幅に節減することが
できる。
なお、この実施例では、例えば原料バルブの離解以降の
工程においてトラブルが発生したような場合、切り換え
バルブ14を切り換えてパイプ10からの排出液を再度
パルパー1内へ戻し、同時に水とソートパルプの供給を
中断することにより、復旧作業をスムーズに行なうこと
かできる。Below, one embodiment of the present invention shown in FIG. 1 will be described in detail. In the figure, 1 is a pulper consisting of a roughly cylindrical tank 2 and an agitator 3 provided at the bottom thereof. The stirrer 3 is connected to a drive motor 5 via a belt transmission mechanism 4 . Further, above the pulper 1, an input conveyor 6 for a sheet valve 7 is provided as a means for supplying raw material pulp, and a pump 8 as a means for supplying dilution water supplies dilution water 20 from a water source (not shown). A pipe 9 is provided, and a seat valve 7 and dilution water 20 are installed in the pulper 1.
is now available. In addition, a discharge pipe 10 is provided at the bottom of the pulper 1 in order to send the mixed liquid of the note valve 7 supplied into the pulper 1 and mixed by the stirrer 3 to the next process. To,
Two valves 11 and 13 and a pump 12 are provided. In order to return the liquid mixture passing through the pipe 10 into the pulper 1 as needed, a switching valve 14 and a circulation pipe 15 are provided downstream of the valve 13. The pulper I is equipped with a water level detector 16 for detecting the internal water level and controlling the supply amount of dilution water 20 according to the water level.
is attached to the dilution water 2° supply pipe 9, and the dilution water 20° is supplied in response to the signal from this water level detector 16.
A valve 17 is provided for adjusting the flow rate. Further, a load sensor 18 is connected as a detection means to the drive motor 5 of the agitator 3, which detects the load of the drive motor 5 (which changes depending on the concentration of the mixed liquid) from the current value, and its output signal is The drive motor 19 of the input conveyor 6 is electrically connected via a load sensor 18 or other control means (not shown) so that the input conveyor 6 supplies the seat valves 7 accordingly. This funnel sensor 18 can directly detect the current value according to the concentration of the mixed liquid in the pulper 1. Therefore, in this configuration, the load on the drive motor 5 for stirring the liquid mixture is detected by the load sensor 18, and as a result,
When it is detected that the valve concentration is lower than the set value due to a small load, the control means sends an input signal for the seat valve 7 to the input conveyor 6, and the sorting valve 7 is automatically input into the pulper 1. Ru. Conversely, if it is detected that the load on the drive motor 5 is large, the valve concentration is higher than the set value, so the seat valve 7 is not closed. Furthermore, when the load sensor 18 detects that the load on the drive motor 5 is large, and when the water level detector 16 detects that the water level is below a certain value,
The valve 17 is opened and the dilution water 20 is supplied into the pulper 1, and when the water level is above a certain value, the valve 17 is closed and the dilution water 20 is not supplied into the pulper 1. Not possible. In this way, with the above configuration, it is possible to reliably adjust the concentration of the mixed liquid to the desired value even if a wide variety of note valves are supplied at random without providing a device to stock sort valves for each type. Therefore, problems such as an increase in the size of the device and high cost do not occur. Further, a mixed solution having a desired constant concentration can be continuously and efficiently taken out. for example,
The inner diameter of the pulper is about 3 m, the height is about 2 m, and ll0k.
In this case, when using a W drive motor, it is not possible to use a timer to control the injection timing of the note valve.
Whereas 11,900 kg of sort valves were disintegrated in 7 hours of operation per day, with the configuration of this example, it took only 467 hours to process the same amount of raw pulp. We were able to shorten the time by approximately two-thirds. Therefore, the working time of the worker can be shortened, and the operating time of the device can be shortened, resulting in a significant reduction in power consumption. In this embodiment, for example, if a trouble occurs in the process after disintegration of the raw material valve, the switching valve 14 is switched to return the discharged liquid from the pipe 10 to the pulper 1, and at the same time, the water and sorted pulp are removed. By interrupting the supply, restoration work can be carried out smoothly.
第1図は本発明の1実施例に係るバルブ濃度制御方法を
実施するための装置の構成図である。
1・・・パルパー、2・槽、3・・・撹拌機(撹拌手段
)、4 ベルト伝動機構、訃・・駆動モータ、6・・シ
ートバルブ投入コンベア(原料バルブ供給手段)、7・
・・シートバルブ、8・・・ポンプ(希釈水供給手段)
、9 希釈水供給パイプ、10・・排出パイプ、11.
13・・バルブ、12・・・ポンプ、14・・切り換え
バルブ、15・・・循環用パイプ、16・・水位検出計
、17・・・流量調整バルブ、I8・・ロートセンサ(
検出手段)、19 ・コンベア駆動モータ、20・・・
希釈水
特 許 出 願 人 花王株式会社
代 理 人 弁理士 青白 葆 (ほか1名)第1図FIG. 1 is a block diagram of an apparatus for carrying out a valve concentration control method according to an embodiment of the present invention. DESCRIPTION OF SYMBOLS 1... Pulper, 2. Tank, 3... Stirrer (stirring means), 4 Belt transmission mechanism, End... Drive motor, 6... Seat valve input conveyor (raw material valve supply means), 7.
... Seat valve, 8... Pump (dilution water supply means)
, 9 dilution water supply pipe, 10... discharge pipe, 11.
13... Valve, 12... Pump, 14... Switching valve, 15... Circulation pipe, 16... Water level detector, 17... Flow rate adjustment valve, I8... Roto sensor (
detection means), 19 ・Conveyor drive motor, 20...
Dilution water patent Applicant Kao Corporation agent Patent attorney Aobai Ao (and 1 other person) Figure 1
Claims (2)
混合する撹拌手段の負荷を検出し、その検出値に応じて
原料パルプ及び希釈水それぞれの供給もしくはその停止
を制御して混合液の濃度を適正値となるように調整する
ことを特徴とするパルパーにおけるパルプ濃度制御方法
。(1) The load on the stirring means for mixing the raw material pulp and dilution water supplied into the pulper is detected, and the supply or stop of each of the raw material pulp and dilution water is controlled according to the detected value, and the mixed liquid is A pulp density control method in a pulper, which comprises adjusting the density to a proper value.
拌手段とで構成されたパルパーと、該パルパーに原料パ
ルプを供給する原料パルプ供給手段と、該パルパーへ希
釈水を供給する希釈水供給手段と、を備え、 さらに、撹拌時における上記撹拌手段の負荷を検出する
検出手段と、該検出手段の出力信号に応じて、混合液の
濃度が適性値となるように上記原料パルプ供給手段によ
る原料パルプの供給と上記希釈水供給手段による希釈水
の供給とを制御する制御手段を備えたことを特徴とする
パルプ濃度制御装置。(2) A pulper composed of a tank and a stirring means for mixing raw material pulp and dilution water, a raw material pulp supply means for supplying raw material pulp to the pulper, and a dilution water supplying dilution water to the pulper. a supplying means, further comprising a detection means for detecting the load on the stirring means during stirring, and a raw material pulp supplying means for controlling the concentration of the mixed liquid to an appropriate value according to the output signal of the detection means. 1. A pulp concentration control device comprising a control means for controlling the supply of raw material pulp by the dilution water supply means and the supply of dilution water by the dilution water supply means.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP33756990A JPH04209882A (en) | 1990-11-30 | 1990-11-30 | Method for controlling pulp concentration in pulper and pulp concentration controlling apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP33756990A JPH04209882A (en) | 1990-11-30 | 1990-11-30 | Method for controlling pulp concentration in pulper and pulp concentration controlling apparatus |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH04209882A true JPH04209882A (en) | 1992-07-31 |
Family
ID=18309880
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP33756990A Pending JPH04209882A (en) | 1990-11-30 | 1990-11-30 | Method for controlling pulp concentration in pulper and pulp concentration controlling apparatus |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH04209882A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006249644A (en) * | 2005-02-14 | 2006-09-21 | Yaskawa Electric Corp | Pupler control apparatus |
JP2012067424A (en) * | 2010-09-27 | 2012-04-05 | Duplo Seiko Corp | Waste paper recycling apparatus |
JP2014234555A (en) * | 2013-05-31 | 2014-12-15 | 株式会社新興テクノ | Waste paper feeding device |
JP2017125289A (en) * | 2016-01-12 | 2017-07-20 | デュプロ精工株式会社 | Pulp slurry supply apparatus and pulp slurry transfer method |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5234401U (en) * | 1975-09-01 | 1977-03-11 | ||
JPS6142039A (en) * | 1984-08-06 | 1986-02-28 | Mitsubishi Electric Corp | Data processor diagnosing system |
JPS6319595B2 (en) * | 1979-12-10 | 1988-04-23 | Yasukichi Okazaki |
-
1990
- 1990-11-30 JP JP33756990A patent/JPH04209882A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5234401U (en) * | 1975-09-01 | 1977-03-11 | ||
JPS6319595B2 (en) * | 1979-12-10 | 1988-04-23 | Yasukichi Okazaki | |
JPS6142039A (en) * | 1984-08-06 | 1986-02-28 | Mitsubishi Electric Corp | Data processor diagnosing system |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006249644A (en) * | 2005-02-14 | 2006-09-21 | Yaskawa Electric Corp | Pupler control apparatus |
JP4682755B2 (en) * | 2005-02-14 | 2011-05-11 | 株式会社安川電機 | Pulper control device |
JP2012067424A (en) * | 2010-09-27 | 2012-04-05 | Duplo Seiko Corp | Waste paper recycling apparatus |
JP2014234555A (en) * | 2013-05-31 | 2014-12-15 | 株式会社新興テクノ | Waste paper feeding device |
JP2017125289A (en) * | 2016-01-12 | 2017-07-20 | デュプロ精工株式会社 | Pulp slurry supply apparatus and pulp slurry transfer method |
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