JP2002194688A - Method for cleaning in papermaking and screening process - Google Patents

Method for cleaning in papermaking and screening process

Info

Publication number
JP2002194688A
JP2002194688A JP2000385450A JP2000385450A JP2002194688A JP 2002194688 A JP2002194688 A JP 2002194688A JP 2000385450 A JP2000385450 A JP 2000385450A JP 2000385450 A JP2000385450 A JP 2000385450A JP 2002194688 A JP2002194688 A JP 2002194688A
Authority
JP
Japan
Prior art keywords
caustic soda
paper
limonene
cleaning
aqueous dispersion
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
Application number
JP2000385450A
Other languages
Japanese (ja)
Inventor
Takayuki Hiratsuka
高行 平塚
Kenji Manabe
健司 真部
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Paper Mills Ltd
Original Assignee
Mitsubishi Paper Mills Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mitsubishi Paper Mills Ltd filed Critical Mitsubishi Paper Mills Ltd
Priority to JP2000385450A priority Critical patent/JP2002194688A/en
Publication of JP2002194688A publication Critical patent/JP2002194688A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide a method for cleaning in a paper making and screening process, having high safety and slight influence on drain, with which impurities of chemicals consisting essentially of a sizing agent in a screening process can be effectively removed. SOLUTION: This method for cleaning in the paper making and screening process, an aqueous dispersion liquid consisting essentially of D-limonene and caustic soda is added to a screening system and circulated to remove impurities derived from each chemical consisting essentially of the sizing agent. Preferably the weight ratio of the caustic soda to the D-limonene in the aqueous dispersion liquid is 5-50 wt.%.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、抄紙精選工程内の
サイズ剤を主体とした各薬品の不純物を効果的に除去す
ることのできる抄紙精選工程における洗浄方法に関する
ものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a cleaning method in a paper making process which can effectively remove impurities of various chemicals, mainly sizing agents, in the paper making process.

【0002】[0002]

【従来の技術】(1) 精選工程は、主にタンク、異物
を除去するスクリーン、クリーナー、配管、ポンプから
構成され、開口部がほとんどない工程である。その為、
今迄は、精選工程内を洗浄する方法は、水(温水)によ
ってポンプで回流しパイプ内の流速で汚れを除去する方
法であった。 (2)工程内の汚れが、紙に配合されている薬品に起因
するものの場合は、水(温水)に濃度0.5〜2重量%
位の苛性ソーダを混合し、同様に回流することで洗浄し
ていた。 (3)苛性ソーダによる洗浄効率を上げるために、濃度
を2〜5重量%程度に濃くする方法を施したが、排水規
制、安全性の問題で実現性はなかった。 (4)よって、上記の方法では、汚れ(異物)が除去さ
れないことが多く、配管などを取り外すことにより物理
的に洗浄していたため、生産時間に弊害を及ぼす例があ
った。
2. Description of the Related Art (1) The selection process is a process mainly including a tank, a screen for removing foreign substances, a cleaner, piping, and a pump, and having almost no opening. For that reason,
Until now, the method of cleaning the inside of the fine selection process has been a method of removing dirt at a flow rate in a pipe by circulating with a pump using water (hot water). (2) When the stain in the process is caused by the chemical compounded in the paper, the concentration is 0.5 to 2% by weight in water (hot water).
The caustic soda was mixed and washed similarly by circulating. (3) In order to increase the washing efficiency with caustic soda, a method of increasing the concentration to about 2 to 5% by weight was applied, but there was no feasibility due to drainage regulations and safety issues. (4) Therefore, in the above method, dirt (foreign matter) is often not removed, and physical cleaning is performed by removing pipes and the like.

【0003】従来の苛性ソーダによる洗浄では、紙に配
合されている各種薬品の混合による不純物の除去には、
必ずしも効果的でなかった。また、苛性ソーダの濃度を
上げると、排水への影響、安全性の問題などの弊害が起
こった。
[0003] In the conventional washing with caustic soda, for removing impurities by mixing various chemicals contained in paper,
Not always effective. In addition, when the concentration of caustic soda was increased, adverse effects such as effects on drainage and safety problems occurred.

【0004】上述したとおり、これらの問題を解決すべ
き有効な洗浄薬品がなく、その解決が待たれていた。
As mentioned above, there is no effective cleaning chemical to solve these problems, and the solution has been awaited.

【0005】[0005]

【発明が解決しようとする課題】本発明の目的は、安全
性が高く、排水への影響が少なく、かつ抄紙精選工程内
のサイズ剤を主体とした各薬品の不純物を効果的に除去
することのできる抄紙精選工程における洗浄方法を提供
するものである。
SUMMARY OF THE INVENTION It is an object of the present invention to provide a high-safety, low-impact effect on wastewater, and to effectively remove impurities of various chemicals, mainly sizing agents, in a paper-making process. It is intended to provide a washing method in a paper making selection step that can be performed.

【0006】[0006]

【課題を解決するための手段】本発明者は、上記に鑑み
鋭意検討した結果、本発明の抄紙精選工程における洗浄
方法を発明するに至った。
Means for Solving the Problems As a result of intensive studies in view of the above, the present inventor has invented a washing method in the paper making selective step of the present invention.

【0007】即ち、本発明の抄紙精選工程における洗浄
方法は、精選系に主としてD−リモネンおよび苛性ソー
ダからなる水性分散液を添加し、回流させてサイズ剤を
主体とした各薬品に由来する不純物を除去することを特
徴とするものである。
That is, in the washing method in the papermaking screening step of the present invention, an aqueous dispersion mainly composed of D-limonene and caustic soda is added to a screening system, and the mixture is circulated to remove impurities derived from various chemicals mainly containing a sizing agent. It is characterized by being removed.

【0008】本発明において、水性分散液における苛性
ソーダの重量比としては、D−リモネンに対して5〜5
0重量%であることが好ましい。
In the present invention, the weight ratio of caustic soda in the aqueous dispersion is 5 to 5 with respect to D-limonene.
It is preferably 0% by weight.

【0009】[0009]

【発明の実施の形態】本発明における抄紙精選工程は、
抄紙の白水を循環している工程であり、クリーナー、ス
クリーンによって異物を除去する工程でもある。精選工
程で不純物が発生し、クリーナーおよびスクリーンで除
去されない場合には、紙製品に不純物が付着して欠点と
なり、製品としての機能を果たさなくなる。そのため、
抄紙精選工程の不純物を極力抑えることが必要である
が、紙の品質安定化のために、各有機薬品が配合されて
いることから、それらの混合物をある一定期間で洗浄、
除去する必要がある。本発明では、洗浄剤として、D−
リモネンと苛性ソーダの水性分散液を添加することによ
り、従来、効果のなかった各薬品の混合不純物について
の溶解除去が効率よく行われることを見出した。
BEST MODE FOR CARRYING OUT THE INVENTION In the present invention, the paper-making selection step
This is the step of circulating the white water of the paper making, and also the step of removing foreign substances by a cleaner and a screen. If impurities are generated during the selection process and are not removed by the cleaner and the screen, the impurities adhere to the paper product, resulting in a defect and failing to function as a product. for that reason,
It is necessary to minimize impurities in the papermaking process, but since the organic chemicals are blended to stabilize the quality of the paper, the mixture is washed for a certain period of time.
Need to be removed. In the present invention, D-
It has been found that by adding an aqueous dispersion of limonene and caustic soda, dissolution and removal of mixed impurities of various chemicals, which have been ineffective conventionally, can be efficiently performed.

【0010】本発明において、D−リモネンと苛性ソー
ダの重量比としては、D−リモネンに対して苛性ソーダ
が5〜50重量%であることで、効率的に除去すること
ができる。ここで、苛性ソーダが5重量%未満では、除
去率が、低下する。また、50重量%を超えて多くなる
と、回流後の排水および安全性に支障をきたす。
In the present invention, the weight ratio of D-limonene to caustic soda is 5 to 50% by weight of D-limonene, so that it can be efficiently removed. Here, if the amount of caustic soda is less than 5% by weight, the removal rate decreases. On the other hand, when the content exceeds 50% by weight, drainage after circulation and safety are hindered.

【0011】D−リモネンに苛性ソーダを混合するの
は、D−リモネンの溶解効果を促進させる目的である。
The purpose of mixing caustic soda with D-limonene is to promote the dissolving effect of D-limonene.

【0012】ここで、D−リモネンによって除去される
不純物は、組成として有機物が80%以上含有している
ことが分析結果から認められている。不純物の発生状況
としては、酸性紙と中性紙を相互抄造している系で多く
認められ、特にサイズ剤が、酸性紙でケン化ロジンサイ
ズ、中性紙でアルキルケテンダイマーの相互抄造してい
る系に特に認められている。
Here, it has been confirmed from analysis results that impurities removed by D-limonene contain 80% or more of organic substances in composition. Regarding the generation of impurities, it is often observed in systems where acid paper and neutral paper are mutually formed.In particular, the sizing agent is obtained by mutual papermaking of saponified rosin size with acid paper and alkyl ketene dimer with neutral paper. Is specifically recognized in certain systems.

【0013】本発明における実施に当たって、まず、抄
紙精選工程内に水を充満しておく。D−リモネンと苛性
ソーダを所定比率で混合した水性分散液を抄紙精選工程
内に投入する。その際 水性分散液の水に対する固形濃
度は1〜2重量%とする。水性分散液投入後、抄紙精選
工程のポンプを運転し、該分散液を回流させることによ
り、該分散液を抄紙精選工程内全体に行き渡らせる。続
いて、数時間回流させて後、該分散液を排水し、排水完
了後に排水弁を閉め、再び水(温水)を抄紙精選工程内
に充満させて回流する。水(温水)回流を2〜3回繰り
返すことによって抄紙精選工程外に除去する。水性分散
液が系内に残っていると、生産時、薬品を分解して工程
に弊害を起こす可能性があるため、水(温水)回流を実
施することは必須の作業である。ここで、回流における
ポンプの出力は、洗浄効果を上げるために、配管内の流
速を速くすることが効果的であり、できるだけ最大出力
にすることが望ましい。
In the practice of the present invention, first, water is filled in the paper making process. An aqueous dispersion obtained by mixing D-limonene and caustic soda at a predetermined ratio is fed into the papermaking screening process. At this time, the solid concentration of the aqueous dispersion in water is set to 1 to 2% by weight. After the introduction of the aqueous dispersion, the pump in the paper-making process is operated to circulate the dispersion, thereby distributing the dispersion throughout the paper-making process. Subsequently, the mixture is allowed to flow for several hours, and then the dispersion is drained. After drainage is completed, the drain valve is closed, and water (warm water) is filled again in the paper-making process and is circulated. The water (warm water) circulation is repeated two or three times to remove the water outside the paper making process. If the aqueous dispersion remains in the system, the chemicals may be decomposed at the time of production, which may cause an adverse effect on the process. Therefore, it is essential to carry out circulation of water (hot water). Here, it is effective to increase the flow rate in the piping in order to increase the cleaning effect, and it is desirable that the output of the pump in the circulating flow be maximized as much as possible.

【0014】[0014]

【実施例】以下、本発明について、実施例を挙げて説明
する。
The present invention will be described below with reference to examples.

【0015】実施例1〜6および比較例1〜2 精選工程30m3の保有量に水を充満させ、続いて、サ
イロに下記表1に示す苛性ソーダを含む水性液1000
リットルとD−リモネン100リットル(有効成分10
0%)からなる水性分散液を投入した。その後、精選工
程のポンプを運転し、2〜3時間回流し、回流後、水性
分散液を排水した。排水完了後、精選工程内に再度水を
充満させ、水のみで回流を30分程度実施して後、排水
した。この水による回流を2〜3回実施し、苛性ソーダ
とD−リモネンの水性分散液を精選工程外に除外した。
このようにして、精選工程の洗浄後、下記のようにし
て、書籍用紙を抄造した。
Examples 1 to 6 and Comparative Examples 1 to 2 The water held in the cleaning step 30 m 3 was filled with water, and the aqueous solution containing caustic soda shown in Table 1 below was added to the silo.
Liters and 100 liters of D-limonene (active ingredient 10
0%). Thereafter, the pump in the selection process was operated to circulate for 2-3 hours, and after circulating, the aqueous dispersion was drained. After the drainage was completed, water was filled again in the selection process, and circulating was performed with only water for about 30 minutes, and then drained. This circulation with water was performed two or three times, and the aqueous dispersion of caustic soda and D-limonene was excluded from the outside of the selection process.
After washing in the selection process in this way, book paper was made as described below.

【0016】濾水度400mlまで叩解したLBKPと
濾水度480mlまで叩解したNBKPを重量比7:3
に混合して得た叩解パルプ100部に、カチオン澱粉
(Cato308、日本エヌエスシー製)6.0部 ア
ルキルケテンダイマーサイズ剤(AS263、日本PM
C製)1.5部 ポリメタクリル酸エステル(ハイホル
ダー301、栗田工業製)0.3部を添加した。このよ
うに配合した紙料を長網抄紙機により抄造し、書籍用紙
を製造した。長網抄紙機の構成は、ワイヤー→プレス→
ドライヤー→サイズプレス→ドライヤー→カレンダー→
リーラーである。
LBKP beaten to a freeness of 400 ml and NBKP beaten to a freeness of 480 ml were in a weight ratio of 7: 3.
Into 100 parts of beaten pulp obtained by mixing the above, 6.0 parts of cationic starch (Cato 308, manufactured by NSC) Alkyl ketene dimer sizing agent (AS263, PM of Japan)
C) 1.5 parts Polymethacrylate (High Holder 301, manufactured by Kurita Kogyo) 0.3 part was added. The stock thus blended was machined by a fourdrinier machine to produce book paper. The configuration of Fourdrinier is as follows: wire → press →
Dryer → size press → dryer → calendar →
It is a reeler.

【0017】上記実施例1〜6および比較例1〜2によ
り、精選工程における洗浄後の抄造した紙について下記
の評価方法により評価し、その結果を下記表1に示す。
According to the above Examples 1 to 6 and Comparative Examples 1 and 2, the paper made after the washing in the selection step was evaluated by the following evaluation method. The results are shown in Table 1 below.

【0018】<紙の欠点の個数>紙の欠点の個数は、オ
ムロン製電子検紙機(型式KP24YW14,NVPD
Fi)を用い、蛍光灯を光源として測定した。洗浄前後
の数字は、1000m2当の紙における欠点(異物)の
個数を示している。また、除去率(%)は、紙の欠点の
個数について、洗浄前後の該個数差を洗浄前の該個数で
割り算した値(%)である。
<Number of paper defects> The number of paper defects is determined by an OMRON electronic paper inspection machine (model KP24YW14, NVPD).
Using Fi), the measurement was performed using a fluorescent lamp as a light source. The numbers before and after washing indicate the number of defects (foreign matter) in 1000 m 2 paper. The removal rate (%) is a value (%) obtained by dividing the difference between before and after cleaning by the number before and after cleaning for the number of paper defects.

【0019】[0019]

【表1】 [Table 1]

【0020】上記実施例1〜6および比較例1〜2の結
果より、Dリモネンに対する苛性ソーダの重量を5重量
%以上とすることにより約40%位の異物の除去率を増
加できる。さらに、苛性ソーダの重量が50重量%以上
では、臨界線に達している。このため、苛性ソーダの重
量として、5〜50重量%の範囲が、コスト、安全性を
考慮した場合、適切であることが確認できた。一方、比
較例1、2では、それぞれD−リモネン、苛性ソーダが
単独の場合であるが、いずれも除去率が低い結果であっ
た。
From the results of Examples 1 to 6 and Comparative Examples 1 and 2, it is possible to increase the foreign matter removal rate of about 40% by setting the weight of caustic soda to D limonene to 5% by weight or more. Further, when the weight of caustic soda is 50% by weight or more, the critical line is reached. For this reason, it was confirmed that the range of 5 to 50% by weight as the weight of caustic soda was appropriate in consideration of cost and safety. On the other hand, in Comparative Examples 1 and 2, D-limonene and caustic soda were used alone, respectively, but both had low removal rates.

【0021】[0021]

【発明の効果】本発明の抄紙精選工程における洗浄方法
は、従来では充分除去できなかったサイズ剤を主体とす
る各薬品の不純物を効率よく除去することができ、紙の
品質向上と生産性向上に大きく寄与するものである。さ
らに、苛性ソーダとD−リモネンの重量比特定値とする
ことにより、除去効果も高い。
According to the cleaning method of the present invention, the impurities of various chemicals, mainly sizing agents, which could not be sufficiently removed in the past can be efficiently removed, thereby improving the quality and productivity of the paper. It greatly contributes to Furthermore, by setting the weight ratio of caustic soda to D-limonene to a specific value, the removal effect is also high.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 抄紙精選工程における洗浄方法におい
て、精選系に主としてD−リモネンおよび苛性ソーダか
らなる水性分散液を添加し、回流させてサイズ剤を主体
とした各薬品に由来する不純物を除去することを特徴と
する抄紙精選工程における洗浄方法。
In a washing method in a papermaking screening step, an aqueous dispersion mainly composed of D-limonene and caustic soda is added to a screening system, and the mixture is circulated to remove impurities derived from various chemicals mainly containing a sizing agent. A washing method in a papermaking screening step, characterized by the following.
【請求項2】 水性分散液における苛性ソーダの重量比
が、D−リモネンに対して5〜50重量%であることを
特徴とする請求項1記載の抄紙精選工程における洗浄方
法。
2. The method according to claim 1, wherein the weight ratio of caustic soda in the aqueous dispersion is 5 to 50% by weight based on D-limonene.
JP2000385450A 2000-12-19 2000-12-19 Method for cleaning in papermaking and screening process Pending JP2002194688A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000385450A JP2002194688A (en) 2000-12-19 2000-12-19 Method for cleaning in papermaking and screening process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000385450A JP2002194688A (en) 2000-12-19 2000-12-19 Method for cleaning in papermaking and screening process

Publications (1)

Publication Number Publication Date
JP2002194688A true JP2002194688A (en) 2002-07-10

Family

ID=18852710

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000385450A Pending JP2002194688A (en) 2000-12-19 2000-12-19 Method for cleaning in papermaking and screening process

Country Status (1)

Country Link
JP (1) JP2002194688A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008007862A (en) * 2006-06-27 2008-01-17 Kurita Water Ind Ltd Pitch controlling agent and pitch controlling method
EP2130434A3 (en) * 2008-04-16 2012-08-29 Acquaflex S.r.l. Biocidal and dispersing composition and use thereof in a method for controlling the biological contamination and the formation of deposits in a system for the production of paper and/or of wood pulp

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008007862A (en) * 2006-06-27 2008-01-17 Kurita Water Ind Ltd Pitch controlling agent and pitch controlling method
EP2130434A3 (en) * 2008-04-16 2012-08-29 Acquaflex S.r.l. Biocidal and dispersing composition and use thereof in a method for controlling the biological contamination and the formation of deposits in a system for the production of paper and/or of wood pulp

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