JP2011132624A - Method for dewatering scum discharged in papermaking process - Google Patents

Method for dewatering scum discharged in papermaking process Download PDF

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JP2011132624A
JP2011132624A JP2009291548A JP2009291548A JP2011132624A JP 2011132624 A JP2011132624 A JP 2011132624A JP 2009291548 A JP2009291548 A JP 2009291548A JP 2009291548 A JP2009291548 A JP 2009291548A JP 2011132624 A JP2011132624 A JP 2011132624A
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scum
sludge
rotating body
papermaking process
dewatering
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Hidetake Sone
英丈 曽根
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Nippon Sharyo Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for dewatering scum discharged in a papermaking process without using chemicals. <P>SOLUTION: The dewatering method for the scum discharged in the papermaking process removes water from the scum containing water in sludge such as sewage separated from white water used in the papermaking process. The scum is supplied into a bottom-opened concave rotary vessel 12 through a supply pipe extended from below the vessel upward and scattered by keeping a contact with a top plate 121 of the rotating rotor 12 to deposit the sludge on the side face 122 of the rotor 12 while dropping water downward along the side face 122 of the rotor 12 to separate the sludge and the water. <P>COPYRIGHT: (C)2011,JPO&INPIT

Description

本発明は、製紙工場で使用される白水の処理に際して生じるスカムの脱水方法に関し、特に薬品を使用することなく行うスカムの脱水方法に関する。   The present invention relates to a method for dewatering scum generated during the treatment of white water used in a paper mill, and more particularly to a method for dewatering scum that is performed without using chemicals.

近年、省資源や地球環境保全の要求が高まり、古紙および損紙のリサイクル率が高くなってきており、これまで脱墨や異物除去が困難であった雑誌の他、ラミネート処理された紙容器なども紙料として用いられるようになってきている。古紙を再生するには、パルパーに投入された古紙が水に薬剤を混合した溶液によって溶解され、得られた紙料スラリからクリーナー装置によって粗い異物が除去された後、フローテーターにより脱墨処理とともに漂白処理が行われ、更にクリーナー装置によって微細な異物除去が行われる。そうしてできた液状パルプから抄紙工程を経て再生紙が作られる。   In recent years, demands for resource conservation and global environmental conservation have increased, and the recycling rate of waste paper and waste paper has increased. Magazines that have been difficult to deink and remove foreign matter, laminated paper containers, etc. Are also being used as paper stock. To recycle waste paper, waste paper put into the pulper is dissolved by a solution mixed with chemicals in water, and after removing coarse foreign substances from the resulting paper slurry by a cleaner device, the paper is deinked by a flotator. Bleaching is performed, and fine foreign matter is removed by a cleaner. Recycled paper is made from the resulting liquid pulp through a papermaking process.

ところで、製紙工場では大量の水を使用するため、抄紙工程で使用した水を循環させて再びパルパーへ送り込むようにしているが、こうした循環水(白水)も繰り返し使用した後に排水処理などが行われる。そこでは、例えば加圧浮上装置が使用され、水に空気を高圧で溶かし込んで生じる微細な気泡に白水中の微細繊維や汚泥(総称して「スラッジ」という)を付着させて浮上させる。浮上した表面のスラッジは掻き取られ、残った水は放流または再利用される。そして、掻き取られたスラッジ(これを「スカム」という)は水分を多く含んでいるため脱水処理が行われ、その後に焼却などの処理が行われる。   By the way, because a large amount of water is used in paper mills, the water used in the papermaking process is circulated and sent back to the pulper. Wastewater treatment is performed after such circulating water (white water) is also used repeatedly. . In this case, for example, a pressure levitation device is used, and fine fibers and sludge (generally referred to as “sludge”) in white water are attached to fine bubbles generated by dissolving air in water at a high pressure to float. The surface sludge that has surfaced is scraped off, and the remaining water is discharged or reused. Since the scraped sludge (referred to as “scum”) contains a lot of water, it is dehydrated, and then incinerated.

再表WO2006/022188号公報Reissue WO2006 / 022188 特開2003−119680号公報JP 2003-119680 A 特開2000−153106号公報JP 2000-153106 A

“トリプルアール株式会社 / 商品情報 / 遠心分離機 series”、[online]、[平成21年11月20日検索]、インターネット<URL:http://www.triple-r.co.jp/products/ensin/index.html>“Triple Earl Co., Ltd. / Product Information / Centrifuge series”, [online], [Searched on November 20, 2009], Internet <URL: http://www.triple-r.co.jp/products/ ensin / index.html>

ところで従来は、スクリュープレス(特許文献2参照)やベルトプレス(特許文献3参照)などを使用したスカムの脱水が行われていたが、そのままでは微細なスラッジは隙間から水分と一緒に流れてしまうため脱水処理が困難であった。そこで、特許文献1に記載するように、高分子凝集剤などの薬品を添加することによって凝集されたスカムをベルトプレスやスクリュープレスを用いて圧搾する脱水が行われていた。しかしながら、そうした脱水処理を行っていたのでは、高分子凝集剤などの薬品にかかる費用が製紙コストを引き上げてしまう原因となってしまっていた。   Conventionally, dewatering of the scum using a screw press (see Patent Document 2) or a belt press (see Patent Document 3) has been performed, but fine sludge flows together with moisture from the gap as it is. Therefore, the dehydration process was difficult. Therefore, as described in Patent Document 1, dehydration has been performed in which a scum aggregated by adding a chemical such as a polymer flocculant is squeezed using a belt press or a screw press. However, when such a dehydration process was performed, the cost of chemicals such as a polymer flocculant increased the papermaking cost.

そこで、本発明は、かかる問題点を解決すべく、薬品を使用することのない製紙過程で出たスカムの脱水方法を提供することを目的とする。   Accordingly, an object of the present invention is to provide a method for dewatering scum produced in the papermaking process without using chemicals in order to solve such problems.

本発明に係る製紙過程で出たスカムの脱水方法は、製紙過程で使用される白水から取り出した汚泥などのスラッジに水分を含んだスカムから水分を取り除くためのものであって、下方に開口した凹形状容器の回転体内に、その下方から上方に伸びた供給管を介して送り込んだ前記スカムを、回転する前記回転体の天板部に接触させて飛ばし、スラッジを前記回転体の側面に付着させる一方、水分を前記回転体の側面に沿って下方に落とすようにしてスラッジと水分とを分離するようにしたことを特徴とする。
また、本発明に係る製紙過程で出たスカムの脱水方法は、前記スカムを一定量連続して前記回転体内に送り込んだ後、前記スカムの送り込みを止めた状態で一定時間だけ前記回転体を回転させるようにしたことが好ましい。
The dewatering method of the scum produced in the papermaking process according to the present invention is for removing moisture from the scum containing moisture in sludge such as sludge extracted from white water used in the papermaking process, and opened downward. The scum fed into the rotating body of the concave container through the supply pipe extending from the lower side to the upper side of the rotating container is brought into contact with the top plate portion of the rotating body to be blown, and the sludge is attached to the side surface of the rotating body. On the other hand, the sludge and the moisture are separated by dropping the moisture downward along the side surface of the rotating body.
Also, in the method for dewatering a scum produced in the papermaking process according to the present invention, the scum is continuously fed into the rotating body by a predetermined amount, and then the rotating body is rotated for a certain time in a state where the feeding of the scum is stopped. It is preferable to make it.

よって、本発明によれば、回転体内に送り込んだスカムを天板部の回転によって飛ばし、遠心力によってスラッジを回転体の側面に付着させる一方で、水分は回転体の側面に沿って落ちることにより分離するようにしたので、薬品を使用しなくてもスカムの脱水を行うことが可能になり、その分コストを抑えることが可能になる。   Therefore, according to the present invention, the scum fed into the rotating body is blown off by the rotation of the top plate, and the sludge adheres to the side surface of the rotating body by centrifugal force, while moisture falls along the side surface of the rotating body. Since they are separated, the scum can be dehydrated without using any chemicals, and the cost can be reduced accordingly.

本実施形態の脱水方法で使用する遠心分離脱水機の概略構成を示した断面図である。It is sectional drawing which showed schematic structure of the centrifugal dehydrator used with the spin-drying | dehydration method of this embodiment. 遠心分離脱水機によるスカムの脱水方法を示した図である。It is the figure which showed the dehydration method of the scum by a centrifugal dehydrator. 遠心分離脱水機によるスカムの脱水方法を示した図である。It is the figure which showed the dehydration method of the scum by a centrifugal dehydrator.

以下、本発明に係る製紙過程で出たスカムの脱水方法について、その一実施形態を図面を参照しながら説明する。
製紙工場では、前述したように、抄紙工程で使用した水(白水)が再利用されてパルパーへと送り込まれ、繰り返し使用された白水は、ある程度使用された後、排水処理が行われて放流される。その排水処理で使用される加圧浮上装置では、使用済み白水に空気が高圧で溶かし込まれ、微細な気泡に付着させた汚泥などのスラッジを浮上させ、それを掻き取ることでスカムが得られる。
Hereinafter, an embodiment of a method for dewatering a scum produced in a papermaking process according to the present invention will be described with reference to the drawings.
In the paper mill, as described above, the water used in the paper making process (white water) is reused and sent to the pulper. After being used to some extent, the white water that has been used repeatedly is drained and discharged. The In the pressurized levitation device used in the wastewater treatment, air is dissolved in used white water at high pressure, sludge such as sludge adhering to fine bubbles is levitated, and scraped off to obtain scum. .

そのスカムは水分を多く含んでいるためこれまで薬品が使用されてきたが、本実施形態では、薬品を使用することなく遠心分離脱水機を使用してスカムから水分を除去する脱水方法を採用した。図1は、本実施形態で使用する遠心分離脱水機の概略構成を示した断面図である。遠心分離脱水機10は、箱形の本体11内に凹形容器の回転体12が回転支持されている。回転体12は、凹形状を上下逆にして配置され、上方を塞いで下方が開口している。上端の天板部121は平面であり、円筒形状の筒部122は下端部分123が内側に傾斜した形状をしている。   Since the scum contains a lot of moisture, chemicals have been used so far, but in this embodiment, a dehydration method that removes moisture from the scum using a centrifugal dehydrator without using the chemicals is adopted. . FIG. 1 is a cross-sectional view showing a schematic configuration of a centrifugal dehydrator used in the present embodiment. In the centrifugal dehydrator 10, a rotating body 12 of a concave container is rotatably supported in a box-shaped main body 11. The rotating body 12 is disposed with its concave shape turned upside down, and the upper part is closed and the lower part is opened. The top plate portion 121 at the upper end is a flat surface, and the cylindrical tube portion 122 has a shape in which the lower end portion 123 is inclined inward.

この回転体12は、本体11を上方に貫いた回転軸13に連結され、その回転軸13を介して軸受14によって回転支持されている。回転軸13にはVプーリー15が固定され、不図示のVベルトを介してモータの回転が伝達されるようになっている。例えばこの回転体12には、毎分2500回転の回転スピードが与えられる。一方、本体11の下側にはスカムを投入する供給管16が取り付けられている。供給管16は、本体側部から水平に入り、90度に折り曲げられて回転体12の回転中心に沿って立ち上がっている。供給管16の先端は、回転体12の天板部121に近接した位置にまで達し、送り込まれたスカムが先端から吹き出して天板部121に当たるようになっている。   The rotating body 12 is connected to a rotating shaft 13 penetrating the main body 11 upward, and is rotatably supported by a bearing 14 via the rotating shaft 13. A V pulley 15 is fixed to the rotary shaft 13 so that the rotation of the motor is transmitted via a V belt (not shown). For example, the rotating body 12 is given a rotational speed of 2500 revolutions per minute. On the other hand, a supply pipe 16 for introducing scum is attached to the lower side of the main body 11. The supply pipe 16 enters horizontally from the side of the main body, is bent at 90 degrees, and rises along the rotation center of the rotating body 12. The distal end of the supply pipe 16 reaches a position close to the top plate portion 121 of the rotating body 12, and the scum that has been sent blows out from the tip and hits the top plate portion 121.

この遠心分離脱水機10は、天板部121に当たったスカムが、回転によって筒部122へ飛ばされ、汚泥などのスラッジが遠心力によって筒部122に付着する一方で、水分は下方へと垂れて流れるようになっている。ところで、回転体12の下には、スカムから分離した水分を受けための受け皿17が設けられている。受け皿17は、その中心側端部に壁を立てて貫通孔171が形成され、溜まった水分が本体11に形成された排水管18を介して流れ出るようになっている。   In the centrifugal dehydrator 10, the scum that hits the top plate part 121 is blown to the cylinder part 122 by rotation, and sludge such as sludge adheres to the cylinder part 122 by centrifugal force, while moisture droops downward. Is flowing. By the way, a receiving tray 17 for receiving moisture separated from the scum is provided under the rotating body 12. The tray 17 is provided with a through hole 171 with a wall standing at the center side end portion thereof, so that accumulated water flows out through a drain pipe 18 formed in the main body 11.

回転体12内には、径方向に沿って配置され、且つその方向に移動可能なスラッジ掻板19が設けられている。スラッジ掻板19は、不図示の駆動手段によって図示する回転中心側から回転体12の筒部122へと図面右側へ移動し、回転する筒部122に付着したスラッジを掻き取るものである。そのため、回転体12からは水分の他にスラッジも落ちてくるが、受け皿17は、シャッター構造になっており、スラッジを掻き落とす時には受け皿17をスライドさせ、受け皿17に載らないようになっている。スラッジ掻板19により掻き出されたスラッジは落下し、不図示の容器に回収されるようになっている。   A sludge scraper 19 that is disposed along the radial direction and is movable in that direction is provided in the rotating body 12. The sludge scraping plate 19 is moved to the right side of the drawing from the rotation center side shown in the drawing by a driving means (not shown) to the right side of the drawing, and scrapes off the sludge adhering to the rotating cylinder portion 122. For this reason, sludge also falls from the rotating body 12 in addition to moisture, but the tray 17 has a shutter structure, and when the sludge is scraped off, the tray 17 is slid and does not rest on the tray 17. . The sludge scraped out by the sludge scraper 19 falls and is collected in a container (not shown).

次に、この遠心分離脱水機10を使用したスカムの脱水方法について説明する。図2及び図3は、遠心分離脱水機10によるスカムの脱水処理工程を示した図である。加圧浮上装置で得られたスカムは、供給管16を通して遠心分離脱水機10へと送り込まれる。供給管16を上昇して先端から吹き出したスカムは、回転する回転体12の天板部121に当たり筒部122へと飛ばされる。そのため、図2に示すように、汚泥などのスラッジSは遠心力によって筒部122に付着する一方、水分Wは下端部分123先端から垂れて受け皿17に落ち、排水管18を介して排水される。   Next, a scum dehydration method using the centrifugal dehydrator 10 will be described. FIG. 2 and FIG. 3 are diagrams showing a scum dehydration process by the centrifugal dehydrator 10. The scum obtained by the pressure levitation device is sent to the centrifugal dehydrator 10 through the supply pipe 16. The scum that rises from the supply pipe 16 and blows out from the tip of the supply pipe 16 hits the top plate portion 121 of the rotating rotating body 12 and is blown to the cylindrical portion 122. Therefore, as shown in FIG. 2, sludge S such as sludge adheres to the cylindrical portion 122 by centrifugal force, while moisture W hangs down from the tip of the lower end portion 123 and falls to the tray 17 and is drained through the drain pipe 18. .

こうして遠心分離脱水機10に対してスカムが送り込まれると、スラッジと水分との分離が行われ、回転体12の筒部122内側面に付着したスラッジSの堆積層ができあがる。そしてスカムの送り込みが所定時間行われた後、一旦供給管16からのスカムの供給を止め、その後更に一定時間の回転を続けることにより、スラッジSを遠心力で筒部122に付着させたまま、残る水分Wをより多く落として脱水効果を上げるようにする。   When the scum is sent to the centrifugal dehydrator 10 in this way, the sludge and moisture are separated, and a deposit layer of sludge S adhering to the inner surface of the cylindrical portion 122 of the rotating body 12 is formed. Then, after the scum is fed for a predetermined time, the supply of the scum from the supply pipe 16 is once stopped, and then the rotation of the scum is continued for a certain period of time. The remaining water W is dropped to increase the dehydration effect.

そうした後、回転体12の回転を継続したままスラッジ掻板19が図3に示すように矢印の径方向へと移動する。スラッジ掻板19が、筒部122内側面に付着したスラッジSに達すると、スラッジ掻板19に当たったスラッジSが掻き落とされ、本体11の回収孔11aを通って下に用意されている容器に回収される。スラッジSが掻き落とされた後は、再び供給管16からスカムが送り込まれ、こうした繰り返しによりスラッジと水分とを分離した脱水処理が行われる。   After that, the sludge scraper 19 moves in the radial direction of the arrow as shown in FIG. 3 while the rotation of the rotating body 12 is continued. When the sludge scraping plate 19 reaches the sludge S adhering to the inner surface of the cylindrical portion 122, the sludge S that has hit the sludge scraping plate 19 is scraped off, and the container prepared below through the recovery hole 11a of the main body 11 To be recovered. After the sludge S is scraped off, the scum is sent again from the supply pipe 16, and a dehydration process is performed in which the sludge and moisture are separated by such repetition.

よって、本実施形態におけるスカムの脱水方法によれば、遠心分離脱水機10を使用することにより、薬品を使用しなくてもスカムの脱水を行うことが可能になり、その分コストを抑えることが可能になった。また、脱水処理を行ったスラッジSは、運搬などに対して扱いやすいものとなり、ボイラーの燃料やセメントの原料としてそのまま再利用することもできる。   Therefore, according to the scum dehydration method in the present embodiment, by using the centrifugal dehydrator 10, it is possible to dehydrate the scum without using chemicals, thereby reducing the cost. It became possible. Further, the sludge S that has been subjected to the dehydration process becomes easy to handle for transportation and the like, and can be reused as it is as a raw material for boiler fuel or cement.

以上、本実施形態に係る製紙過程で出たスカムの脱水方法について説明したが、本発明はこれに限定されることなく、その趣旨を逸脱しない範囲で変更が可能である。   As mentioned above, although the dehydration method of the scum produced in the papermaking process according to the present embodiment has been described, the present invention is not limited to this and can be changed without departing from the spirit thereof.

10 遠心分離脱水機
11 本体
12 回転体
13 回転軸
16 供給管
17 受け皿
19 スラッジ掻板
121 天板部
122 筒部
DESCRIPTION OF SYMBOLS 10 Centrifugal dehydrator 11 Main body 12 Rotating body 13 Rotating shaft 16 Supply pipe 17 Receptacle 19 Sludge scraper 121 Top plate part 122 Cylinder part

Claims (2)

製紙過程で使用される白水から取り出した汚泥などのスラッジに水分を含んだスカムから水分を取り除くための、製紙過程で出たスカムの脱水方法において、
下方に開口した凹形状容器の回転体内に、その下方から上方に伸びた供給管を介して送り込んだ前記スカムを、回転する前記回転体の天板部に接触させて飛ばし、スラッジを前記回転体の側面に付着させる一方、水分を前記回転体の側面に沿って下方に落とすようにしてスラッジと水分とを分離するようにしたことを特徴とする製紙過程で出たスカムの脱水方法。
In the dewatering method of scum produced in the papermaking process to remove moisture from the scum containing moisture in sludge such as sludge taken out from the white water used in the papermaking process,
The scum fed through a supply pipe extending upward from below into the rotating body of the concave container opened downward is brought into contact with the top plate portion of the rotating rotating body, and sludge is removed from the rotating body. A method for dewatering scum produced in a papermaking process, wherein the sludge is separated from moisture by dropping water along the side surface of the rotating body while adhering to the side surface of the rotating body.
請求項1に記載する製紙過程で出たスカムの脱水方法において、
前記スカムを一定量連続して前記回転体内に送り込んだ後、前記スカムの送り込みを止めた状態で一定時間だけ前記回転体を回転させるようにしたことを特徴とする製紙過程で出たスカムの脱水方法。
In the method for dewatering scum produced in the papermaking process according to claim 1,
The dewatering of the scum generated in the papermaking process, wherein the scum is continuously fed into the rotating body after a predetermined amount and then the rotating body is rotated for a certain time in a state where the feeding of the scum is stopped. Method.
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014091108A (en) * 2012-11-06 2014-05-19 G-Force Japan Kk Centrifugal separator

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0317725U (en) * 1989-06-29 1991-02-21
JPH07862A (en) * 1993-06-14 1995-01-06 Hitachi Ltd Centrifugal separator
JPH11333325A (en) * 1998-05-25 1999-12-07 Chuo Seisakusho Ltd Centrifugal separator
JP2000219891A (en) * 1998-04-22 2000-08-08 Haerting Sa Highly efficient recovery of unsaponifiable matter from black liquor soap or crude tall oil
JP2003144973A (en) * 2001-11-09 2003-05-20 Horyo Corp Centrifuge
JP2004041951A (en) * 2002-07-12 2004-02-12 G-Force Japan Kk Centrifugal separator
JP2004283716A (en) * 2003-03-20 2004-10-14 Toagosei Co Ltd Method for dehydrating sludge
JP2008115052A (en) * 2006-11-07 2008-05-22 Mitsubishi Paper Mills Ltd Method of producing calcium carbonate

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0317725U (en) * 1989-06-29 1991-02-21
JPH07862A (en) * 1993-06-14 1995-01-06 Hitachi Ltd Centrifugal separator
JP2000219891A (en) * 1998-04-22 2000-08-08 Haerting Sa Highly efficient recovery of unsaponifiable matter from black liquor soap or crude tall oil
JPH11333325A (en) * 1998-05-25 1999-12-07 Chuo Seisakusho Ltd Centrifugal separator
JP2003144973A (en) * 2001-11-09 2003-05-20 Horyo Corp Centrifuge
JP2004041951A (en) * 2002-07-12 2004-02-12 G-Force Japan Kk Centrifugal separator
JP2004283716A (en) * 2003-03-20 2004-10-14 Toagosei Co Ltd Method for dehydrating sludge
JP2008115052A (en) * 2006-11-07 2008-05-22 Mitsubishi Paper Mills Ltd Method of producing calcium carbonate

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014091108A (en) * 2012-11-06 2014-05-19 G-Force Japan Kk Centrifugal separator

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