JP6991000B2 - A method for cleaning the water reservoir and a method for cleaning the circulating water system including the water reservoir. - Google Patents

A method for cleaning the water reservoir and a method for cleaning the circulating water system including the water reservoir. Download PDF

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JP6991000B2
JP6991000B2 JP2017117062A JP2017117062A JP6991000B2 JP 6991000 B2 JP6991000 B2 JP 6991000B2 JP 2017117062 A JP2017117062 A JP 2017117062A JP 2017117062 A JP2017117062 A JP 2017117062A JP 6991000 B2 JP6991000 B2 JP 6991000B2
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大揮 蔵本
昭吾 倉内
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アクアス株式会社
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本発明は、パルプおよび紙製造設備における水貯留部の洗浄方法、および、水貯留部を含む循環水系の洗浄方法に関する。 The present invention relates to a method for cleaning a water reservoir in a pulp and paper manufacturing facility, and a method for cleaning a circulating water system including the water reservoir.

製紙はパルプを水中に分散させた原料スラリーを抄紙することで行われ、その際、微細繊維や填料を含む白水が抄紙機等から多量に排出される。この白水は、水資源の有効活用や再利用の観点から、抄紙工程で循環して用いられるようになっている。しかし、白水は、填料、澱粉、サイズ剤、ラテックス、カゼイン等の有機物を多く含むため、細菌類、真菌類等の微生物の繁殖に好適であり、このような微生物に由来するスライム、スケール、ピッチ由来のデポジットが循環水系に発生しやすい。このようなデポジットは製品に付着すると欠陥となり、製品歩留まりの低下につながる懸念がある。 Papermaking is performed by making a raw material slurry in which pulp is dispersed in water, and at that time, a large amount of white water containing fine fibers and a filler is discharged from a paper machine or the like. From the viewpoint of effective utilization and reuse of water resources, this white water is circulated and used in the papermaking process. However, since white water contains a large amount of organic substances such as fillers, starches, sizing agents, latex, and casein, it is suitable for breeding microorganisms such as bacteria and fungi, and slime, scale, and pitch derived from such microorganisms. Derived deposits are likely to occur in circulating water systems. If such a deposit adheres to the product, it becomes a defect, and there is a concern that the product yield may decrease.

また、パルプおよび紙製造設備の水貯留部の底部には、沈殿物が堆積し、これが腐敗して悪臭物質が発生し、製紙工場内の臭気の原因となり、あるいは、製品に付着する可能性がある。 In addition, sediment accumulates at the bottom of the water reservoir of pulp and paper manufacturing equipment, which can spoil and generate malodorous substances, which can cause odors in paper mills or adhere to products. be.

これら問題の改善のために、例えば数週間から数箇月に1回程度の頻度で、設備の運転を止め、洗浄剤を用いて洗浄を行うことが提案されている(特許文献1参照)。具体的には、水貯留部を含む循環水系の水に対して、洗浄主剤として水酸化ナトリウム等のアルカリ性剤、および、洗浄主剤とともに洗浄剤を構成する洗浄助剤として、過酸化水素、界面活性剤、鉱物油、キレート剤などを添加して、1~3時間程度、水を循環させたのち排水する。その後、水貯留部を作業員が清掃して、残った堆積物を除去している。この際、洗浄主剤と併用する洗浄助剤の価格は洗浄主剤に比べて高く、その使用量の削減が求められていたが、抜本的な検討は行われてこなかった。 In order to improve these problems, it has been proposed to stop the operation of the equipment and perform cleaning with a cleaning agent, for example, once every few weeks to several months (see Patent Document 1). Specifically, for circulating water system water including a water reservoir, an alkaline agent such as sodium hydroxide as a cleaning main agent, and hydrogen peroxide and surfactant as a cleaning auxiliary agent constituting the cleaning agent together with the cleaning main agent. Add an agent, mineral oil, a chelating agent, etc., circulate the water for about 1 to 3 hours, and then drain the water. After that, workers clean the water reservoir to remove the remaining sediment. At this time, the price of the cleaning aid used in combination with the cleaning main agent is higher than that of the cleaning main agent, and it has been required to reduce the amount used, but no drastic study has been conducted.

特開2007-277769号公報Japanese Unexamined Patent Publication No. 2007-277769

本発明は、このような従来技術の問題点を解決することを目的としている。すなわち、本発明は、パルプおよび紙製造設備の洗浄に用いる洗浄剤の使用量の削減を可能とする水貯留部の洗浄方法、および、水貯留部を含む循環水系の洗浄方法を提供することを目的とする。 An object of the present invention is to solve such a problem of the prior art. That is, the present invention provides a method for cleaning a water reservoir and a method for cleaning a circulating water system including the water reservoir, which can reduce the amount of a cleaning agent used for cleaning pulp and paper manufacturing equipment. The purpose.

上記目的は、以下の本発明によって解決される。即ち、本発明の水貯留部の洗浄方法は、運転を停止したパルプおよび紙製造設備における水貯留部の洗浄方法であって、
水が貯留された状態の、堆積物が底部に沈積している水貯留部に洗浄剤を添加し、横向き、下向き、あるいは、斜め下向きの水流で前記水貯留部の底部またはその近傍に水流を生じさせる攪拌を行うことを特徴とする。
The above object is solved by the following invention. That is, the method for cleaning the water reservoir of the present invention is a method for cleaning the water reservoir in the pulp and paper manufacturing equipment that has stopped operation .
A cleaning agent is added to the water reservoir where the sediment is deposited at the bottom of the water reservoir, and the water flow is applied to the bottom of the water reservoir or its vicinity with a horizontal, downward, or diagonally downward water flow . It is characterized by performing agitation to generate it .

また、本発明の水貯留部の洗浄方法では、前記洗浄剤が、洗浄主剤としてアルカリ性洗浄剤を含有している構成とすることができる。 Further, in the method for cleaning the water storage portion of the present invention, the cleaning agent may be configured to contain an alkaline cleaning agent as a cleaning main agent .

本発明においては、前記水流による攪拌を、水中攪拌機にて行うことができる。 In the present invention, the agitation by the water flow can be performed by an underwater agitator.

また、本発明においては、前記水流による攪拌を、前記水貯留部への給水口に取り付けたノズルにて行うことができる。 Further, in the present invention, stirring by the water flow can be performed by a nozzle attached to the water supply port to the water storage unit.

一方、本発明の水貯留部を含む循環水系の洗浄方法は、上記本発明の水貯留部の洗浄方法により、水貯留部の洗浄を行いながら、当該水貯留部を含む循環水系に洗浄剤を含む水を循環させる攪拌・循環工程を有することを特徴とする。 On the other hand, in the method for cleaning the circulating water system including the water storage portion of the present invention, the cleaning agent is applied to the circulating water system including the water storage portion while cleaning the water storage portion by the above-mentioned cleaning method for the water storage portion of the present invention. It is characterized by having a stirring / circulation step of circulating the contained water.

また、本発明の水貯留部を含む循環水系の洗浄方法では、前記攪拌・循環工程の後に、前記循環水系の水を排水する排水工程を有することができる。 Further, in the method for cleaning a circulating water system including a water storage portion of the present invention, it is possible to have a drainage step of draining the water of the circulating water system after the stirring / circulation step.

本発明の水貯留部の洗浄方法、および、本発明の水貯留部を含む循環水系の洗浄方法によれば、パルプおよび紙製造設備における水貯留部に対し、水が貯留された状態で洗浄剤を添加し、水流による攪拌を行う攪拌洗浄工程を有する構成により、洗浄助剤の使用量の削減が可能となる。また、洗浄性が向上することから、洗浄時間の短縮や後工程の作業員による清掃作業の負担軽減あるいは省略が可能となる。 According to the method for cleaning the water reservoir of the present invention and the method for cleaning the circulating water system including the water reservoir of the present invention, the cleaning agent in a state where water is stored in the water reservoir in the pulp and paper manufacturing facility. It is possible to reduce the amount of the cleaning aid used by the configuration having a stirring cleaning step of adding water and stirring with a water stream. Further, since the cleaning property is improved, the cleaning time can be shortened and the burden of cleaning work by the worker in the post-process can be reduced or omitted.

本発明の水貯留部の洗浄方法、および、本発明の水貯留部を含む循環水系の洗浄方法が実施されるパルプおよび紙製造設備の一例を示すモデル図である。It is a model figure which shows an example of the pulp and paper manufacturing equipment which carries out the cleaning method of the water storage part of this invention, and the cleaning method of the circulating water system including the water storage part of this invention. 水中攪拌機による攪拌方法の例を示すモデル図である。It is a model figure which shows the example of the stirring method by the underwater stirrer.

本発明について以下に図面を用いて説明する。
<パルプおよび紙製造設備>
本発明の水貯留部の洗浄方法は、製紙工場におけるパルプおよび紙製造設備で実施される水貯留部の洗浄に適用されるものである。
The present invention will be described below with reference to the drawings.
<Pulp and paper manufacturing equipment>
The method for cleaning a water reservoir of the present invention is applied to cleaning a water reservoir carried out in a pulp and paper manufacturing facility in a paper mill.

本発明において、パルプおよび紙製造設備の「水貯留部」とは、パルプ精選系、原料調整系、白水循環系、白水回収系、その他のコーター周辺などの水貯留部を包含し、パルプおよび紙製造設備において多量に排出される水溶液(いわゆる「白水」等。)の回収、再利用系までを含めた水循環工程全体における全ての水貯留部を意味する。白水は、通常、紙製造時に使用する原料パルプに由来する微細繊維や、その他の製紙用薬剤等を含んでいる。 In the present invention, the "water storage unit" of the pulp and paper manufacturing equipment includes a water storage unit such as a pulp selection system, a raw material adjustment system, a white water circulation system, a white water recovery system, and other coater peripherals, and includes pulp and paper. It means all the water storage parts in the entire water circulation process including the recovery and reuse system of the aqueous solution (so-called "white water" etc.) discharged in a large amount in the manufacturing equipment. White water usually contains fine fibers derived from raw material pulp used in paper production, other paper-making chemicals, and the like.

図1に本発明の、水貯留部の洗浄方法、および、水貯留部を含む循環水系の洗浄方法について説明に使用するパルプおよび紙製造設備の一例Aのモデル図を示すが、本発明はこの例に限定されるものではない。 FIG. 1 shows a model diagram of Example A of a pulp and paper manufacturing facility used for explaining a method for cleaning a water reservoir and a method for cleaning a circulating water system including a water reservoir according to the present invention. It is not limited to an example.

まず、パルプ精選系A1として原料パルプをウォッシャー1で洗浄し、次いで濃縮脱水し、脱水により生じた水は濃縮脱水ピット2に回収される。一方、脱水されたパルプは、晒処理機3で漂白処理後、高濃度チェスト4に一時、蓄えられる。なお、図1では省略したが、このパルプ精選系A1には、使用される水を再利用できるように水系水の循環ラインが付属している。 First, as the pulp selection system A1, the raw material pulp is washed with a washer 1 and then concentrated and dehydrated, and the water generated by the dehydration is collected in the concentrated dehydration pit 2. On the other hand, the dehydrated pulp is temporarily stored in the high-concentration chest 4 after being bleached by the bleaching machine 3. Although omitted in FIG. 1, the pulp selection system A1 is provided with an aqueous water circulation line so that the water used can be reused.

原料調整槽5とマシンチェスト6とを備えた原料調整系A2で原料を調整する。すなわち、原料調整槽5に、高濃度チェスト4からのパルプを含む原料と水が供給され、さらに回収水タンク16からポンプ17により送水される水が加えられて、パルプスラリーが調整される。調整されたパルプスラリーは、マシンチェスト6に供給され、粘度調整剤や紙力増強剤等の各種製紙用薬剤等が添加された後、ポンプ7により白水循環系A3に供給される。そして、白水サイロ9からの白水(紙料成分をある程度含んだ水)と混合されて、ポンプ8によって、紙料としてインレット10に供給され、インレット10からワイヤパート11の、回転駆動されるワイヤ11aへ供給される。ワイヤパート11に供給された紙料は、脱水されてシート形状となり、プレスパート12以降の工程に送られて紙製品となる。一方、ワイヤパート11に残った水は、白水として白水サイロ9に貯留される。白水サイロ9に貯留された白水は、ポンプ7により供給された各種製紙用薬剤等を含むパルプスラリーと混合されて、ポンプ8によってインレット10に供給されて、白水循環系A3が形成される。 The raw material is adjusted by the raw material adjusting system A2 provided with the raw material adjusting tank 5 and the machine chest 6. That is, the raw material containing pulp from the high-concentration chest 4 and water are supplied to the raw material adjusting tank 5, and the water sent from the recovered water tank 16 by the pump 17 is further added to prepare the pulp slurry. The prepared pulp slurry is supplied to the machine chest 6, various paper-making chemicals such as a viscosity modifier and a paper strength enhancer are added, and then supplied to the white water circulation system A3 by the pump 7. Then, it is mixed with white water (water containing a certain amount of paper material component) from the white water silo 9, supplied to the inlet 10 as a paper material by the pump 8, and the wire 11a of the wire part 11 is rotationally driven from the inlet 10. Is supplied to. The paper material supplied to the wire part 11 is dehydrated into a sheet shape, and is sent to the processes after the press part 12 to become a paper product. On the other hand, the water remaining in the wire part 11 is stored in the white water silo 9 as white water. The white water stored in the white water silo 9 is mixed with a pulp slurry containing various paper-making chemicals supplied by the pump 7 and supplied to the inlet 10 by the pump 8 to form the white water circulation system A3.

白水サイロ9に貯留された白水の一部は、白水サイロ9から白水回収系A4のシールピット13に供給される。シールピット13に供給された白水は、ポンプ14により固液分離装置15に送られて固液分離処理される。固液分離処理された成分のうちの水は、回収水タンク16に貯留された後、その一部はポンプ17により原料調整系A2の原料調整槽5に供給されてパルプスラリーの濃度調整に利用され、また、別の一部は図示しない配管を通ってワイヤパート11のワイヤ11aやプレスパート12のフェルトを清浄に保つためのシャワー水に利用されるなど、パルプおよび紙製造の工程における各種用水として再利用される。このように白水回収系A4は、パルプ精選系A1、原料調整系A2、および、白水循環系A3とともに、パルプおよび紙製造設備の水系を構成し、水はこの循環水系内を循環している。なお、回収水タンク16内の他の一部の水は濃度調整のために系外に排出され、図示しない排水処理設備等に送られる。 A part of the white water stored in the white water silo 9 is supplied from the white water silo 9 to the seal pit 13 of the white water recovery system A4. The white water supplied to the seal pit 13 is sent to the solid-liquid separation device 15 by the pump 14 for solid-liquid separation processing. After the water among the components that have been subjected to the solid-liquid separation treatment is stored in the recovered water tank 16, a part of the water is supplied to the raw material adjusting tank 5 of the raw material adjusting system A2 by the pump 17 and used for adjusting the concentration of the pulp slurry. And another part is used for shower water to keep the wire 11a of the wire part 11 and the felt of the press part 12 clean through a pipe (not shown). Will be reused as. As described above, the white water recovery system A4 constitutes the water system of the pulp and paper manufacturing equipment together with the pulp selection system A1, the raw material adjustment system A2, and the white water circulation system A3, and water circulates in the circulation water system. Some of the other water in the recovered water tank 16 is discharged to the outside of the system for concentration adjustment, and is sent to a wastewater treatment facility (not shown).

また、パルプおよび紙製造設備A内の水が不足した場合には、この例では用水ライン19より供給されたクッションタンク18内に貯留された水がポンプ20により、シールピット13に供給される。なお、固液分離装置15で固液分離された成分のうちの固形分は製紙原料として再利用されるか、廃棄物として処理される。 When the water in the pulp and paper manufacturing equipment A is insufficient, in this example, the water stored in the cushion tank 18 supplied from the water line 19 is supplied to the seal pit 13 by the pump 20. The solid content of the components separated by the solid-liquid separation device 15 is reused as a papermaking raw material or treated as waste.

図1のパルプおよび紙製造設備Aにおいて、水が貯留される水貯留部としては、特に限定されないが、これら製紙水系内に存在する水槽等、一時的に水の滞留する箇所が対象となる。具体的には、パルプ製造設備における水系では濃縮脱水ピット2、紙製造設備における水系では、マシンチェスト6、白水サイロ9、シールピット13、回収水タンク16等、また、紙製造設備における水系に流入する水系では、クッションタンク18が挙げられるが、本発明における水貯留部はこれらに限定されない、例えば、コーター周辺の水系の水貯留部や原料調整槽に水を供給するために原料調整系内に設けられる仕込み水ピットなど、パルプおよび紙製造設備における水系および当該水系に流入する水系に存在する水貯留部は全て本発明における水貯留部に含まれる。 In the pulp and paper manufacturing equipment A of FIG. 1, the water storage portion in which water is stored is not particularly limited, but a place where water temporarily stays, such as a water tank existing in these papermaking water systems, is targeted. Specifically, in the water system in the pulp manufacturing facility, the concentrated dehydration pit 2, in the water system in the paper manufacturing facility, the machine chest 6, the white water silo 9, the seal pit 13, the recovered water tank 16, etc., and inflow into the water system in the paper manufacturing facility. The water system includes a cushion tank 18, but the water storage unit in the present invention is not limited to these, for example, in the raw material adjustment system for supplying water to the water storage unit or the raw material adjustment tank of the water system around the coater. All the water storage portions existing in the water system in the pulp and paper manufacturing equipment and the water system flowing into the water system, such as the prepared water pit, are included in the water storage unit in the present invention.

図1では、抄紙工程の循環水系に流入する用水ライン19の水をシールピット13に供給する例を示したが、供給場所はシールピット13に限定されない。例えば、パルプや各種製紙用薬剤の希釈水として上記循環水系以外の外部からの水を供給した場合には、当該外部からの水は、本発明のパルプおよび紙製造設備の循環水系に流入する水である。なお、プレスパート12等の抄紙工程よりも後の工程から排出される水を白水サイロ9やシールピット13等に回収してもよい。 FIG. 1 shows an example in which the water of the water line 19 flowing into the circulating water system in the papermaking process is supplied to the seal pit 13, but the supply location is not limited to the seal pit 13. For example, when water from an outside other than the above-mentioned circulating water system is supplied as diluting water for pulp and various paper-making chemicals, the water from the outside flows into the circulating water system of the pulp and paper manufacturing equipment of the present invention. Is. The water discharged from the process after the papermaking process of the press part 12 or the like may be collected in the white water silo 9, the seal pit 13, or the like.

[水貯留部の洗浄方法]
まず、本発明の水貯留部の洗浄方法について説明する。
[How to clean the water reservoir]
First, a method for cleaning the water storage portion of the present invention will be described.

<水貯留部>
本発明のパルプおよび紙製造設備における水貯留部の洗浄方法では、パルプ精選系(A1)、原料調整系(A2)、白水循環系(A3)、白水回収系(A4)あるいは、図示しないコーター周辺の水系(以下、これらを合わせて「製紙水系」と云う。)、さらには、これら水系に流入する水系(符号18~20)に存在する水貯留部が洗浄の対象となる。
<Water storage>
In the method for cleaning the water storage portion in the pulp and paper manufacturing equipment of the present invention, the pulp selection system (A1), the raw material adjustment system (A2), the white water circulation system (A3), the white water recovery system (A4), or the periphery of the coater (not shown). (Hereinafter, these are collectively referred to as "papermaking water system"), and further, the water storage portion existing in the water system (reference numerals 18 to 20) flowing into these water systems is subject to cleaning.

水貯留部内で、水に含まれる固形分、懸濁物質がその底部に沈積する。こうして沈積した堆積物近傍あるいは沈積物が積層して形成された堆積物層の内部は有機物が豊富なために、細菌類をはじめとする微生物の温床となると共に嫌気化が進み、微生物の代謝産物として硫化水素、メチルメルカプタン等の還元性物質が生成されるようになる。 In the water reservoir, solids and suspended solids contained in water are deposited on the bottom. Since the vicinity of the sediments deposited in this way or the inside of the sediment layer formed by stacking the sediments is rich in organic matter, it becomes a hotbed for microorganisms such as bacteria and becomes anaerobic, and is a metabolite of microorganisms. As a result, reducing substances such as hydrogen sulfide and methyl mercaptan will be produced.

これらは、製品の欠点となりうるスライムの発生を防止するために水系に添加されるスライムコントロール剤の効果を低下させる。したがって、通常は定期的に、例えば毎月1回等の頻度で、製造装置を止めて洗浄を行っている。具体的には、生産を中止し、それぞれの水系ごとに、洗浄主剤として水酸化ナトリウム等のアルカリ性洗浄剤、および、過酸化水素などの酸化剤、界面活性剤、鉱物油などを含む洗浄助剤を添加し、通常1~3時間、水系水を循環させたのちに排水する。なお、この水の循環の際に加温することもある。 These reduce the effectiveness of slime control agents added to the water system to prevent the generation of slime, which can be a drawback of the product. Therefore, the manufacturing apparatus is usually stopped and cleaned regularly, for example, once a month. Specifically, production will be discontinued, and for each water system, alkaline cleaning agents such as sodium hydroxide and cleaning aids containing oxidizing agents such as hydrogen peroxide, surfactants, mineral oils, etc. will be used as cleaning main agents. Is added, and the aqueous water system is circulated for 1 to 3 hours, and then drained. In addition, it may be heated during the circulation of this water.

このような従来技術の洗浄において、洗浄剤を含む水系水の循環にもかかわらず、水貯留部の底部には堆積物が残留してしまうことが多かった。そのため、洗浄後に作業員によって水貯留部内の清掃を行うことが一般に行われてきた。 In such conventional cleaning, deposits often remain at the bottom of the water reservoir despite the circulation of water-based water containing a cleaning agent. Therefore, it has been common practice for workers to clean the inside of the water storage section after cleaning.

<水貯留部の攪拌>
本発明の水貯留部の洗浄方法においては、水貯留部内の水系水に、水流による攪拌を行うことが特徴となっている。水貯留部内の水系水に水流を発生する手段としては特に制限はないが、水中攪拌機(水中ポンプ)を使用して攪拌を行うことが好ましい。特に、配管やホース等を取り付けずに、そのまま水中攪拌機を水貯留部に投入して駆動させるだけで、水貯留部内に水流を与えることができる。勿論、配管やホース等を取り付けて、水中で適宜これらを取回しても構わない。図1に示した例では、水貯留部である濃縮脱水ピット2、マシンチェスト6、白水サイロ9、シールピット13、回収水タンク16、および、クッションタンク18のそれぞれに水中攪拌機S(横向き噴射式のもの)が設置されている。
<Stirring of water reservoir>
The method for cleaning the water storage portion of the present invention is characterized in that the water-based water in the water storage portion is agitated by a water flow. There is no particular limitation as a means for generating a water flow in the water system water in the water reservoir, but it is preferable to perform stirring using a submersible agitator (submersible pump). In particular, it is possible to give a water flow to the water storage unit by simply putting the submersible stirrer into the water storage unit and driving it without attaching a pipe or a hose. Of course, pipes, hoses, etc. may be attached and these may be appropriately routed in water. In the example shown in FIG. 1, the submersible stirrer S (horizontal injection type) is provided in each of the concentrated dehydration pit 2, the machine chest 6, the white water silo 9, the seal pit 13, the recovered water tank 16, and the cushion tank 18, which are water storage portions. Things) are installed.

ここで、水中攪拌機は、既存の抄紙システムに大規模な改修なしに設置できると云うメリットがある。水中攪拌機としては、横向き噴射式あるいは下向き噴射式のものを用いることが好ましい。上向き噴射式の水中攪拌機を用いると、堆積物を巻き上げる水流の力が弱く、本発明の効果を得にくくなる。 Here, the submersible stirrer has the advantage that it can be installed in an existing papermaking system without major modification. As the submersible stirrer, it is preferable to use a horizontal injection type or a downward injection type. When an upward injection type submersible stirrer is used, the force of the water flow that winds up the sediment is weak, and it becomes difficult to obtain the effect of the present invention.

また、設置に際して配管工事やポンプの設置等が必要となる場合があるが、水貯留部に水を供給するラインの先端にノズルをつけることで水流を発生させて攪拌してもよく、この場合も勿論、本発明における「水流による攪拌」の範疇に含まれる。この場合において、特に、側面に周囲の水を吸い込む孔を有するノズル(例えば、いけうち社製液攪拌用ノズルEJX)を用いることが、より大きな水流を得ることができるので好ましい。 In addition, plumbing work and pump installation may be required for installation, but water flow may be generated and agitated by attaching a nozzle to the tip of the line that supplies water to the water storage section. In this case. Of course, it is included in the category of "stirring by water flow" in the present invention. In this case, it is particularly preferable to use a nozzle having a hole for sucking the surrounding water on the side surface (for example, a nozzle EJX for liquid stirring manufactured by Ikeuchi Co., Ltd.) because a larger water flow can be obtained.

本発明では、例えば、上記例において、パルプ精選系、原料調整系、白水循環系、あるいは、白水回収系により構成される水系、コーター付近の水系、このような水系に流入する水系に存在する水貯留部を攪拌しながら洗浄を行う。このような構成により、攪拌しない場合と比較して、洗浄効果が高まり、洗浄助剤の添加量の削減が可能となる。したがって、経済性等を勘案しつつ、なるべく多くの水貯蔵部、さらには、これら水系にあるすべての水貯留部で攪拌を行いながら洗浄を行うことが好ましい。 In the present invention, for example, in the above example, a water system composed of a pulp selection system, a raw material adjustment system, a white water circulation system, or a white water recovery system, a water system near a coater, and water existing in a water system flowing into such a water system. Cleaning is performed while stirring the reservoir. With such a configuration, the cleaning effect is enhanced and the amount of the cleaning aid added can be reduced as compared with the case where no stirring is performed. Therefore, it is preferable to perform cleaning while stirring as many water storage units as possible, and all water storage units in these water systems, while considering economic efficiency and the like.

本発明における水流による攪拌としては、水貯留部の底部またはその近傍に水流を生じさせる攪拌であることが好ましい。詳しくは、水貯留部の底部に向かう水流を生じさせたり、水貯留部の底部のすぐ上を略平行に進む水流を生じさせたりすることが好ましい。水貯留部の底部またはその近傍に水流を生じさせることで、水貯留部の底部に沈積している堆積物の除去・洗浄効果が発揮され、堆積物の量を低減させることができる。そのため、水貯留部の底部の洗浄効果が高まる。 As the stirring by the water flow in the present invention, it is preferable that the stirring is such that a water flow is generated at or near the bottom of the water storage portion. Specifically, it is preferable to generate a water flow toward the bottom of the water storage portion or to generate a water flow that travels substantially in parallel just above the bottom of the water storage portion. By creating a water flow at or near the bottom of the water reservoir, the effect of removing and cleaning the deposits deposited on the bottom of the water reservoir is exhibited, and the amount of deposits can be reduced. Therefore, the cleaning effect of the bottom of the water storage portion is enhanced.

ここで、水中攪拌機を用いた場合を例に挙げて、いくつかの攪拌手法、特に水貯留部の底部またはその近傍に水流を生じさせる攪拌手法の例について、図2のモデル図を用いて説明する。 Here, taking the case of using an underwater agitator as an example, some agitation methods, particularly an example of a agitation method for generating a water flow at or near the bottom of the water reservoir, will be described using the model diagram of FIG. do.

図2(a)は、水中攪拌機Sとして下向き噴射式のものを用いている例である。この例では水貯留部30の中央に水中攪拌機Sを設置しており、その直下の底部に向けて水流を生じさせている。水貯留部30の底部に向けて直接水流を生じさせているので、堆積物除去効果が高い。 FIG. 2A is an example in which a downward injection type is used as the submersible stirrer S. In this example, an underwater stirrer S is installed in the center of the water storage unit 30, and a water flow is generated toward the bottom immediately below the submersible stirrer S. Since the water flow is directly generated toward the bottom of the water storage portion 30, the effect of removing deposits is high.

図2(b)は、水中攪拌機Sとして横向き噴射式のものを用い、水貯留部30の底部よりも若干高い位置に配して、水流が斜め下方を向くように水中攪拌機Sを斜めに設置した例である。この場合も、水流が水貯留部30の底部に斜めに当たり、堆積物を払うように除去できるため、堆積物除去効果が高い。 In FIG. 2B, a horizontal injection type water stirrer S is used, arranged at a position slightly higher than the bottom of the water storage unit 30, and the water stirrer S is installed diagonally so that the water flow faces diagonally downward. This is an example. In this case as well, the water flow hits the bottom of the water storage portion 30 diagonally and can be removed so as to dispel the deposits, so that the effect of removing the deposits is high.

図2(c)は、図2(b)と同様、水中攪拌機Sとして横向き噴射式のものを用い、水流が水貯留部30の底部と略平行となるようそのまま横向きに設置した例である。この場合、水流は水貯留部30の底部に向かうわけでは無いが、その近傍を進んで堆積物を掃くように除去できるため、堆積物除去効果が高い。 FIG. 2C is an example in which, as in FIG. 2B, a horizontal injection type water stirrer S is used and the water flow is installed sideways as it is so as to be substantially parallel to the bottom of the water storage unit 30. In this case, the water flow does not go toward the bottom of the water reservoir 30, but it can be removed in the vicinity thereof as if sweeping the sediment, so that the effect of removing the sediment is high.

有底円筒形の水貯留部30に対して、図2(b)や図2(c)のように、横向き噴射式の水中攪拌機を設置する場合、図2(d)にモデル的に示すように、水流が水貯留部30の内周面に沿うように設置することが好ましい。このように設置することで、底部全体に水流を生じさせ、広い面積の堆積物除去効果を高めることができる。 When a horizontal injection type submersible stirrer is installed in the bottomed cylindrical water storage section 30 as shown in FIGS. 2 (b) and 2 (c), as shown in FIG. 2 (d) as a model. In addition, it is preferable to install the water flow along the inner peripheral surface of the water storage unit 30. By installing in this way, it is possible to generate a water flow over the entire bottom and enhance the effect of removing deposits over a wide area.

また、図2(e)にモデル的に示すように、水流が水貯留部30の底部付近における円形の直径方向に向かうように設置することも好ましい。このように設置することで、底部における中央付近を最も効率よく堆積物除去効果を高めることができ、底部全体の堆積物除去効果を高めることができる。 Further, as shown as a model in FIG. 2 (e), it is also preferable to install the water flow so as to be directed in the circular radial direction near the bottom of the water storage portion 30. By installing in this way, the sediment removal effect can be most efficiently enhanced near the center of the bottom, and the sediment removal effect of the entire bottom can be enhanced.

いずれにしても、水貯留部の容量や形状などに合わせて堆積物の洗浄や除去効果ができるだけ得られるように、水中攪拌機の種類や能力、設置位置等を適宜選択すればよい。また、これらの例では水中攪拌機Sは水貯留部30にそれぞれ1台設置されているが、必要に応じて複数台設置することもできる。また、洗浄効果を高めるために水流に空気などの気体の泡を吹き込んでもよい。水流による攪拌を行う装置として、水中攪拌機以外の物を用いる場合にも、以上に説明した内容に準じて設置することができる。 In any case, the type, capacity, installation position, etc. of the underwater agitator may be appropriately selected so that the effect of cleaning and removing the deposits can be obtained as much as possible according to the capacity and shape of the water reservoir. Further, in these examples, one submersible stirrer S is installed in each of the water storage units 30, but a plurality of submersible stirrers S can be installed as needed. Further, in order to enhance the cleaning effect, bubbles of gas such as air may be blown into the water stream. Even when a device other than the underwater agitator is used as the device for agitating by the water flow, it can be installed according to the contents described above.

水貯留部の底部に沈積している堆積物を洗浄・除去する効果を高い次元で実現するには、水貯留部における堆積物が沈積しやすい箇所の流速が例えば0.5m/秒以上となるようすることが好ましい。 In order to realize the effect of cleaning and removing the sediments deposited on the bottom of the water reservoir at a high level, the flow velocity at the place where the sediments are likely to be deposited in the water reservoir is, for example, 0.5 m / sec or more. It is preferable to do so.

<洗浄剤>
本発明で用いる洗浄剤は、パルプおよび紙製造設備の洗浄に用いられる各種洗浄剤を用いることができる。多くの洗浄剤は、洗浄主剤と洗浄助剤とから構成され、洗浄主剤として水酸化ナトリウム等のアルカリ性洗浄剤、洗浄助剤としては、過酸化水素、脂肪酸誘導体、界面活性剤、ホスホン酸などのキレート剤、鉱物油等が挙げられる。
<Cleaning agent>
As the cleaning agent used in the present invention, various cleaning agents used for cleaning pulp and paper manufacturing equipment can be used. Many cleaning agents are composed of a cleaning main agent and a cleaning auxiliary, and the cleaning main agent is an alkaline cleaning agent such as sodium hydroxide, and the cleaning auxiliary agent is hydrogen peroxide, a fatty acid derivative, a surfactant, a phosphonic acid, or the like. Examples include chelating agents and mineral oils.

ここで、過酸化水素は装置や水貯留部の壁面や底面、配管内にこびりついた堆積物を剥離させる。脂肪酸誘導体、および、界面活性剤は洗剤として機能して堆積物の塊の分解に寄与し、ホスホン酸はスケールに対してキレート剤として機能し、可溶化する。鉱物油はアルカリ性洗浄剤併存下で油汚れを除去する。 Here, hydrogen peroxide exfoliates the deposits stuck on the wall surface and bottom surface of the device and the water storage part, and in the pipe. Fatty acid derivatives and surfactants act as detergents and contribute to the decomposition of sediment masses, while phosphonic acids act as chelating agents for scale and solubilize. Mineral oil removes oil stains in the presence of an alkaline cleaner.

本発明の水貯留部の洗浄方法によれば、一般的なケースで、洗浄主剤に比して高価な洗浄助剤の使用量を従来の洗浄方法に比して1/3ないし2/3程度削減することが可能となるが、その削減量は実際の洗浄状態を確認して決定すればよい。 According to the method for cleaning the water reservoir of the present invention, in a general case, the amount of the cleaning aid, which is more expensive than the main cleaning agent, is about 1/3 to 2/3 as compared with the conventional cleaning method. It is possible to reduce the amount, but the amount of reduction may be determined by confirming the actual cleaning condition.

[循環水系の洗浄方法]
次に、本発明の水貯留部を含む循環水系の洗浄方法について説明する。
[Washing method for circulating water system]
Next, a method for cleaning the circulating water system including the water storage portion of the present invention will be described.

<水系水の循環>
従来の洗浄方法では、パルプ精選系、原料調整系、白水循環系、白水回収系により構成される水系、および、コーター付近の水系の洗浄の際、洗浄剤を添加した水系水を循環させながら洗浄を行っていたが、本発明の洗浄方法でもこのような水系水の循環を行うことが、水貯留部以外の水系部分、例えば配管、機器・装置を洗浄できる点で好ましい。ただし、水貯留部の攪拌を行っている間中、循環を継続することは必ずしも必要ない。
<Circulation of water system>
In the conventional cleaning method, when cleaning a water system composed of a pulp selection system, a raw material adjustment system, a white water circulation system, a white water recovery system, and a water system near a coater, the water system to which a cleaning agent is added is circulated for cleaning. However, even in the cleaning method of the present invention, it is preferable to perform such circulation of water-based water in that water-based parts other than the water storage portion, for example, pipes, equipment / devices can be cleaned. However, it is not always necessary to continue circulation while stirring the water reservoir.

例えば、予め水系水の循環により配管、機器・装置等の洗浄を行った後に、水貯留部のみ攪拌による洗浄を行う、あるいは、水系水の循環による洗浄と水貯留部の攪拌による洗浄とを同時に開始し、水系水の循環による洗浄により水貯留部以外の配管、機器・装置等の洗浄が終了したときに水系水の循環を停止し、水貯留部の攪拌による洗浄のみを継続する、などの例が挙げられる。 For example, after cleaning pipes, equipment / devices, etc. by circulating water-based water in advance, only the water storage unit is cleaned by stirring, or cleaning by circulating water-based water and cleaning by stirring the water storage unit are performed at the same time. When the cleaning of pipes, equipment, etc. other than the water storage part is completed by cleaning by the circulation of water-based water, the circulation of water-based water is stopped and only the cleaning by stirring of the water storage part is continued. An example is given.

<洗浄時間>
洗浄時間については、汚染状態や攪拌、循環の程度、洗浄剤の種類等に応じて、適宜検討を行って設定すればよいが、本発明の洗浄方法によれば、水貯留部の攪拌による洗浄により、通常、従来の洗浄方法による洗浄時間より、洗浄時間を短縮することが可能となる。
<Washing time>
The cleaning time may be appropriately examined and set according to the state of contamination, stirring, the degree of circulation, the type of cleaning agent, etc., but according to the cleaning method of the present invention, cleaning by stirring the water reservoir is performed. As a result, it is usually possible to shorten the cleaning time as compared with the cleaning time by the conventional cleaning method.

<洗浄後の清掃>
本発明の水貯留部の洗浄方法によれば、洗浄の効果が高いので、従来、洗浄・排水終了後に行われていた水貯留部の清掃にかかる時間を大幅に短縮することができ、あるいは、清掃自体を省略することができる。
<Cleaning after cleaning>
According to the method for cleaning the water reservoir of the present invention, the effect of cleaning is high, so that the time required for cleaning the water reservoir, which has been conventionally performed after the completion of cleaning and drainage, can be significantly shortened, or Cleaning itself can be omitted.

以上、本発明について、好ましい実施形態を挙げて説明したが、本発明の水貯留部の洗浄方法、および、水貯留部を含む循環水系の洗浄方法は、上記実施形態の構成に限定されるものではない。 Although the present invention has been described above with reference to preferred embodiments, the method for cleaning the water reservoir and the method for cleaning the circulating water system including the water reservoir of the present invention are limited to the configuration of the above embodiment. is not it.

当業者は、従来公知の知見に従い、本発明の水貯留部の洗浄方法、および、水貯留部を含む循環水系の洗浄方法を適宜改変することができる。このような改変によってもなお、本発明の水貯留部の洗浄方法、および、水貯留部を含む循環水系の洗浄方法の構成を具備する限り、もちろん、本発明の範疇に含まれるものである。 Those skilled in the art can appropriately modify the method for cleaning the water reservoir of the present invention and the method for cleaning the circulating water system including the water reservoir according to the conventionally known knowledge. Even with such a modification, it is, of course, included in the category of the present invention as long as it has the configuration of the method for cleaning the water storage portion of the present invention and the method for cleaning the circulating water system including the water storage portion.

以下に、実施例を挙げて本発明をより具体的に説明するが、本発明の水貯留部の洗浄方法、および、水貯留部を含む循環水系の洗浄方法は、この実施例に限定されない。
なお、以下の実施例では、既存のパルプおよび紙製造プラントにて、適宜装置を改造して、装置を止めたり稼働させたりして、各種実験を行った。
Hereinafter, the present invention will be described in more detail with reference to examples, but the method for cleaning the water reservoir and the method for cleaning the circulating water system including the water reservoir of the present invention are not limited to this embodiment.
In the following examples, various experiments were conducted in an existing pulp and paper manufacturing plant by appropriately modifying the equipment and stopping or operating the equipment.

≪水中攪拌機による検討≫
(実施例1)
水系の洗浄のために運転を停止したパルプおよび紙製造設備において、白水サイロ(水量:20m3)を有する4つの条件の白水循環系(後記表1における条件I~IV)で、以下の試験を実施した。なお、パルプおよび紙製造設備は、図1を用いて説明した通りであり、本実施例では、図1における白水循環系(A3)の洗浄により、実験した。水中攪拌機は図1における白水サイロ9に設置した。
≪Examination by submersible stirrer≫
(Example 1)
In a pulp and paper manufacturing facility that was shut down for cleaning the water system, the following tests were performed with a white water circulation system (conditions I to IV in Table 1 below) having a white water silo (water volume: 20 m 3 ). Carried out. The pulp and paper manufacturing equipment was as described with reference to FIG. 1, and in this example, the experiment was carried out by washing the white water circulation system (A3) in FIG. The underwater stirrer was installed in the white water silo 9 in FIG.

<攪拌機>
上記白水サイロのうち白水循環系IおよびIIIの白水サイロIおよびIIIの底部にそれぞれ水中攪拌機(フジ機械社製SHG-101HS6)を水流が白水サイロの底面に平行となるように設置した。
<Stirrer>
Of the white water silos, a submersible stirrer (SHG-101HS6 manufactured by Fuji Machinery Co., Ltd.) was installed at the bottom of the white water silos I and III of the white water circulation system I and III so that the water flow was parallel to the bottom surface of the white water silo.

<水系水の循環>
白水循環系I~IVで通常の洗浄時と同じように、全て同一の条件でそれぞれ水系水を循環させた。
<Circulation of water system>
In the white water circulation system I to IV, the water system water was circulated under the same conditions as in the normal washing.

<洗浄剤>
水系水の循環を維持しながら、洗浄主剤として48質量%水酸化ナトリウム水溶液(以下、「48%NaOH」とも云う。)を100L(リットル)、洗浄助剤として35質量%過酸化水素水(以下、「35%H22」と云う。)、および、アクアス社製洗浄剤(脂肪酸誘導体、界面活性剤、ホスホン酸、鉱物油を含有。以下、「洗浄剤」と云う。)をこの順で、下記表1に示す薬剤量となるように添加した。
<Cleaning agent>
While maintaining the circulation of aqueous water, 100 L (liter) of 48% by mass sodium hydroxide aqueous solution (hereinafter, also referred to as "48% NaOH") as a cleaning main agent, and 35% by mass hydrogen peroxide solution (hereinafter, also referred to as "48% NaOH") as a cleaning aid. , "35% H 2 O 2 "), and a cleaning agent manufactured by Aquas (containing a fatty acid derivative, a surfactant, a phosphonic acid, and a mineral oil; hereinafter referred to as a "cleaning agent") in this order. Then, it was added so as to have the amount of the drug shown in Table 1 below.

<洗浄>
上記の薬品の添加後、2時間、各水系水の循環を継続して洗浄を行った。この間、白水循環系IおよびIIIでは白水サイロ内の水中攪拌機を運転した。
<Washing>
After the addition of the above chemicals, the water system water was continuously circulated for 2 hours for washing. During this period, the underwater stirrer in the white water silo was operated in the white water circulation systems I and III.

<評価>
これら白水循環系I~IV内の水系水の排水後、これら白水循環系の白水サイロの底面を観察し、堆積物の有無、および、洗浄後の作業員による清掃の要否を調べた。結果を下記表1にまとめて示す。
<Evaluation>
After draining the water system water in the white water circulation system I to IV, the bottom surface of the white water silo of the white water circulation system was observed, and the presence or absence of deposits and the necessity of cleaning by the worker after cleaning were investigated. The results are summarized in Table 1 below.

なお、I~IVの条件は、下記を目的とした条件である。
白水循環系I:従来(II)と同条件で本発明を適用。
白水循環系II:従来の循環洗浄方式。
白水循環系III:従来(II)から洗浄助剤の量を半減させた上で本発明を適用。
白水循環系IV:従来(II)の循環洗浄方式のまま洗浄助剤の量を半減。
The conditions I to IV are for the following purposes.
White water circulation system I: The present invention is applied under the same conditions as the conventional (II).
White water circulation system II: Conventional circulation cleaning method.
White water circulation system III: The present invention is applied after halving the amount of cleaning aid from the conventional (II).
White water circulation system IV: The amount of cleaning aid is halved with the conventional (II) circulation cleaning method.

Figure 0006991000000001
Figure 0006991000000001

表1に示したように、白水サイロの水中攪拌機を運転して洗浄を行った白水循環系IおよびIIIでは、洗浄により堆積物が除去されたため、洗浄後の作業員による清掃作業が不要となった。また、白水循環系IIIでも十分な洗浄性が確認されたことから、洗浄助剤の使用量を半分に減らすことができることが判る。これに対して、水中攪拌機を設置しなかった白水循環系IIおよびIVでは、洗浄後の清掃作業が必要であった。なお、洗浄助剤の量を半減させた白水循環系IVでは、白水循環系IIに比して、残存堆積物が多く、洗浄後の清掃作業にかかった時間がより長かった。 As shown in Table 1, in the white water circulation systems I and III, which were washed by operating the underwater stirrer of the white water silo, the deposits were removed by the washing, so that the cleaning work by the worker after the washing became unnecessary. rice field. In addition, since sufficient detergency was confirmed in the white water circulation system III, it can be seen that the amount of the cleaning aid used can be reduced by half. On the other hand, in the white water circulation system II and IV in which the underwater stirrer was not installed, cleaning work after cleaning was required. The white water circulation system IV, in which the amount of the cleaning aid was halved, had more residual deposits than the white water circulation system II, and the cleaning work after cleaning took longer.

(実施例2)
上記実験後、白水循環系IおよびIIIの次回の洗浄時に、これら白水循環系で実施例1と同様にして、ただし、洗浄助剤の35%H22、および、洗浄剤の添加量のみをそれぞれ6.6kg、および、6kgに減らし、さらに白水循環系IIIでは洗浄時間を90分として、ともに水中攪拌機を運転しながら洗浄を行ったところ、これら2つの白水循環系IおよびIIIで、ともに白水サイロ内の堆積物が除去され、洗浄後の清掃が不要だった。これにより洗浄助剤の使用量を2/3削減できること、および、洗浄時間の短縮が可能であることが判った。
(Example 2)
After the above experiment, at the next cleaning of the white water circulation systems I and III, the same as in Example 1 in these white water circulation systems, but only 35% H 2 O 2 of the cleaning aid and the amount of the cleaning agent added. Was reduced to 6.6 kg and 6 kg, respectively, and the washing time was set to 90 minutes in the white water circulation system III, and both were washed while operating the underwater stirrer. Both of these two white water circulation systems I and III were washed. The deposits in the white water silo were removed and no cleaning was required after cleaning. It was found that this can reduce the amount of cleaning aid used by 2/3 and shorten the cleaning time.

A パルプおよび紙製造設備の一例
A1 パルプ精選系
A2 原料調整系
A3 白水循環系
A4 白水回収系
1 ウォッシャー
2 濃縮脱水ピット
3 晒処理機
4 高濃度チェスト
5 原料調整槽
6 マシンチェスト
7、8、14、17、20 ポンプ
9 白水サイロ
10 インレット
11 ワイヤパート
11a ワイヤ
12 プレスパート
13 シールピット
15 固液分離装置
16 回収水タンク
18 クッションタンク
19 用水ライン
30 水貯留部
A Example of pulp and paper manufacturing equipment A1 Pulp selection system A2 Raw material adjustment system A3 White water circulation system A4 White water recovery system 1 Washer 2 Concentrated dehydration pit 3 Bleaching machine 4 High concentration chest 5 Raw material adjustment tank 6 Machine chest 7, 8, 14 , 17, 20 Pump 9 White water silo 10 Inlet 11 Wire part 11a Wire 12 Press part 13 Seal pit 15 Solid-liquid separator 16 Recovery water tank 18 Cushion tank 19 Water line 30 Water storage

Claims (6)

運転を停止したパルプおよび紙製造設備における水貯留部の洗浄方法であって、
水が貯留された状態の、堆積物が底部に沈積している水貯留部に洗浄剤を添加し、横向き、下向き、あるいは、斜め下向きの水流で前記水貯留部の底部またはその近傍に水流を生じさせる攪拌を行うことを特徴とする水貯留部の洗浄方法。
It is a method of cleaning the water storage part in the pulp and paper manufacturing equipment that has stopped operation .
A cleaning agent is added to the water storage part where the sediment is deposited at the bottom of the water storage part, and the water flow is applied to the bottom of the water storage part or its vicinity with a horizontal, downward, or diagonally downward water flow . A method for cleaning a water reservoir, which comprises performing agitation to generate the water.
前記洗浄剤が、洗浄主剤としてアルカリ性洗浄剤を含有していることを特徴とする請求項1に記載の水貯留部の洗浄方法。The method for cleaning a water reservoir according to claim 1, wherein the cleaning agent contains an alkaline cleaning agent as a cleaning main agent. 前記水流による攪拌を、水中攪拌機にて行うことを特徴とする請求項1または請求項2に記載の水貯留部の洗浄方法。 The method for cleaning a water storage portion according to claim 1 or 2, wherein the stirring by the water flow is performed by an underwater stirrer. 前記水流による攪拌を、前記水貯留部への給水口に取り付けたノズルにて行うことを特徴とする請求項1または請求項2に記載の水貯留部の洗浄方法。 The method for cleaning a water storage unit according to claim 1 or 2, wherein stirring by the water flow is performed by a nozzle attached to a water supply port to the water storage unit. 請求項1~請求項4のいずれかに記載の水貯留部の洗浄方法により、水貯留部の洗浄を行いながら、当該水貯留部を含む循環水系に洗浄剤を含む水を循環させる攪拌・循環工程を有することを特徴とする水貯留部を含む循環水系の洗浄方法。 By the method for cleaning the water storage unit according to any one of claims 1 to 4, the water storage unit is cleaned, and the water containing the cleaning agent is circulated in the circulating water system including the water storage unit. A method for cleaning a circulating water system including a water reservoir, which comprises a step. 前記攪拌・循環工程の後に、前記循環水系の水を排水する排水工程を有することを特徴とする請求項5に記載の水貯留部を含む循環水系の洗浄方法。 The method for cleaning a circulating water system including a water storage unit according to claim 5, further comprising a drainage step of draining the water of the circulating water system after the stirring / circulation step.
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