JP2000015267A - Treatment of wastewater from paper manufacturing - Google Patents

Treatment of wastewater from paper manufacturing

Info

Publication number
JP2000015267A
JP2000015267A JP10315278A JP31527898A JP2000015267A JP 2000015267 A JP2000015267 A JP 2000015267A JP 10315278 A JP10315278 A JP 10315278A JP 31527898 A JP31527898 A JP 31527898A JP 2000015267 A JP2000015267 A JP 2000015267A
Authority
JP
Japan
Prior art keywords
wastewater
treatment
flocculant
polymer flocculant
chelating polymer
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
JP10315278A
Other languages
Japanese (ja)
Inventor
Hitoshi Hatano
倫 波多野
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.)
Nihon Solid Co Ltd
Original Assignee
Nihon Solid Co 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 Nihon Solid Co Ltd filed Critical Nihon Solid Co Ltd
Priority to JP10315278A priority Critical patent/JP2000015267A/en
Publication of JP2000015267A publication Critical patent/JP2000015267A/en
Pending legal-status Critical Current

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  • Separation Of Suspended Particles By Flocculating Agents (AREA)

Abstract

PROBLEM TO BE SOLVED: To make treated water reusable and lower the load of the wastewater treatment thereafter by using a chelating polymer flocculant of maceration and steam maceration wastewater in paper manufacturing process and adjusting the wastewater neutral or acidic. SOLUTION: After waste paper 6 is macerated by a macerator 1, a chelating polymer flocculant 2 is added to control pH at neutral or lower. In this case, the addition amount is preferably controlled to adjust the pH around 6. After that, the resultant macerated waste paper is washed in a concentrated wastewater washing apparatus (a thickener) 3 and divided to a paper manufacturing substance 4 and washing wastewater 5. By such treatment, COD and BD in the wastewater are significantly lowered and pH adjustment is made unnecessary and the SS and the COD values in the separated water is remarkably decreased and flocculation and precipitation treatment is easily carried out, so that repeat use of the treated water is made possible. Further, dewatering efficiency of cellulose is greatly increased and recovery efficiency is heightened. Furthermore, PVA is made reusable. As the chelating polymer flocculant 2, a mixture of a chlorine type inorganic flocculant and a polyamine type flocculant is especially preferable.

Description

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

【0001】[0001]

【発明の属する利用分野】本発明は、製紙工程におけ
る、製造工程および排水の処理方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a manufacturing process and a method for treating wastewater in a papermaking process.

【0002】[0002]

【従来の技術】従来、古紙の離解工程で、印刷インキや
塗布剤等の剥離に、苛性ソーダと高温蒸気、または温水
でセルロースと分離し、濃縮排水洗浄装置(シックナ
ー)でセルロースを回収して、抄造プロセスで再使用す
る方法がとられているが、シックナーからの分離水は、
アルカリ度が高くPHも10以上で、溶解性の物質が多
く粘性も高いので、洗浄のために多量の加注水(場合に
よっては温水)が必要とされている。またシックナーか
らの高濃度分離水には、PVAやインキ、糊剤などの溶
解性物質が多く、C.O.D.、B.O.D.の排水数
値が高く、生物処理を必要とするため、処理に時間がか
かり、生物処理されない状況下では、排水は、放置時間
が長いほど益々安定して、離解性の高い排水性状となっ
ている。またこれらの高濃度廃液は、排水処理装置で処
理するが、通常はPHコントロールにより中性で処理さ
れる沈澱処理だけでは、溶解性物質が処理されないま
ま、一般排水で希釈され、未処理数値のまま排出されて
いた。特にC.O.D.値は、20〜25p.p.m.
放流されている。基準値ではクリアしているが、総合排
水量が極めて多く、総量値では膨大な数値として河川、
海域に放流されている現状である。
2. Description of the Related Art Conventionally, in the process of disintegrating waste paper, cellulose is separated from caustic soda and high-temperature steam or hot water to separate printing ink and coating agent, and the cellulose is recovered by a concentrated wastewater washing device (thickener). Although the method of reuse in the papermaking process has been adopted, the water separated from the thickener is
Since it has a high alkalinity, a pH of 10 or more, a large amount of soluble substances and a high viscosity, a large amount of pouring water (in some cases, hot water) is required for washing. The high-concentration water separated from the thickener contains many soluble substances such as PVA, ink and paste. O. D. , B. O. D. The wastewater has a high numerical value and requires biological treatment, so it takes a long time to process.Unless the biological treatment is performed, the wastewater has a more stable and longer disintegrating drainage property as the standing time is longer. . In addition, these high-concentration waste liquids are treated by a wastewater treatment device. Normally, only precipitation treatment, which is neutralized by pH control, is diluted with general wastewater without dissolving soluble substances, and the untreated numerical value Was discharged as it was. In particular, C.I. O. D. Values are 20-25 p. p. m.
Has been released. Although it is clear by the standard value, the total drainage is extremely large, and the total
It is currently being released into the sea.

【0003】[0003]

【発明が解決しようとする課題】本発明者は、これら従
来の欠点を解消すべく種々検討を重ねた結果、離解、蒸
解廃液にキレート高分子凝集剤を加え、中性以下とする
ことで、粘性の低下や溶解物質の抽出がなされ、シック
ナーでの脱水効率とセルロース回収率が大幅に高まり、
分離洗浄排水のC.O.D.、B.O.D.、色素など
が著しく低下し、また処理水等の再利用などを可能と
し、その後の排水処理の負荷を大幅に低減する方法を完
成するに至った。
The inventor of the present invention has conducted various studies in order to solve these conventional drawbacks. As a result, by adding a chelating polymer flocculant to the disintegration and digestion waste liquid to make it neutral or less, The viscosity is reduced and the dissolved substances are extracted, and the dehydration efficiency in the thickener and the cellulose recovery rate are greatly increased.
C. of separation washing wastewater O. D. , B. O. D. In addition, the pigment and the like have been remarkably reduced, and the reuse of the treated water and the like has been made possible, thereby completing a method of greatly reducing the load of the subsequent wastewater treatment.

【0004】[0004]

【発明を解決するための手段】本発明を図面を参照しな
がら説明するが、本発明は以下の説明に限定されるもの
ではない。図1は本発明の浄化工法を利用した、製紙排
水処理のフローシートである。従来、離解機に集められ
た古紙は、蒸気や苛性ソーダなどを加えて離解された
後、濃縮廃水洗浄装置(シックナー)に送られるが、本
発明では、離解機1内で離解後、キレート高分子凝集剤
2を加えて中性以下にする。この場合PH6前後に調整
する量を注入することが望ましい。その後濃縮廃水洗浄
装置(シックナー)3において洗浄し、抄造物4と洗浄
廃液5に分けられるが、本発明においては、廃液中の
C.O.D.、B.O.D.などが著しく低下、PH調
整が不要となり、分離水のSS、C.O.D.値が大幅
に減り、凝集沈殿処理が容易なため、処理水の再利用も
可能となる。またセルロースの脱水効率が大幅にあが
り、回収効率もよくなる。さらにPVAは、従来廃液中
に含まれてしまうため廃棄物として排出され、抄造時に
は新たに加えられていたが、本発明では抄造物4内にと
どまるため、PVAの再利用が可能となるなど、抄造工
程における効率アップやコスト削減が可能となる。
The present invention will be described with reference to the drawings, but the present invention is not limited to the following description. FIG. 1 is a flow sheet for papermaking wastewater treatment using the purification method of the present invention. Conventionally, waste paper collected in a disintegrator is disintegrated by adding steam, caustic soda, and the like, and then sent to a concentrated wastewater cleaning device (thickener). Add coagulant 2 to neutrality or less. In this case, it is desirable to inject an amount to be adjusted around PH6. Thereafter, the concentrated wastewater is washed in a concentrated wastewater washing device (thickener) 3 to be separated into a papermaking product 4 and a washing wastewater 5. O. D. , B. O. D. Etc. decrease significantly, PH adjustment becomes unnecessary, and SS, C.I. O. D. Since the value is greatly reduced and the coagulation-sedimentation treatment is easy, it is possible to reuse the treated water. In addition, the dehydration efficiency of cellulose is greatly increased, and the recovery efficiency is also improved. Further, PVA is conventionally discharged as waste because it is contained in a waste liquid, and newly added during papermaking. However, in the present invention, PVA remains in the paperwork 4, so that PVA can be reused. It is possible to increase efficiency and reduce costs in the papermaking process.

【0005】従来希釈温水や無機系硫酸バンドを注入し
ているが、希釈や無機凝集剤だけでは、溶解性のC.
O.D.は、除去しにくいことが知られている。通常は
パックなどを加えた後、凝集剤を使用するため、フロッ
クの表面に架橋して、強度の弱い付着効果しか得られな
かったが、本キレート凝集剤(例えば、NTフロック0
5:日本ソリッド製)においては、凝集分解と架橋が同
時に行なわれるため、凝集がフロック内外で行われ、フ
ロックの内部にまで作用するため、溶解性物質の除去に
優れている。
Conventionally, diluted hot water or an inorganic sulfuric acid band has been injected.
O. D. Is known to be difficult to remove. Usually, after adding a pack or the like, since a flocculant is used, the floc surface is cross-linked to obtain a weak adhesion effect. However, the present chelate flocculant (for example, NT floc 0)
5: made by Nippon Solid Co., Ltd.), since coagulation decomposition and cross-linking are performed simultaneously, coagulation is performed inside and outside the floc and acts even inside the floc, so that the removal of soluble substances is excellent.

【0006】本発明におけるキレート高分子凝集剤は、
無機系(カチオン)と同系のカチオン性アクリルアマイ
ド、ポリアミン、ポリイミン等と配合したものいい、無
機系には、硫酸鉄、硫酸アルミニウム、塩化鉄、ポリ塩
化アルミニウムなどがある。さらに、混合高分子とは、
ポリアミン、ポリイミン、アクリルアマイドポリマー、
とを混合したものをいう。本発明においては特に塩化系
の無機凝集剤とポリアミン系を混合したものがよい。こ
れらは、濃厚廃液と抄造排水処理に使用することも含ま
れる。
The chelating polymer flocculant in the present invention comprises:
It may be blended with cationic acrylamide, polyamine, polyimine and the like, which are the same as inorganic (cation). Examples of the inorganic include iron sulfate, aluminum sulfate, iron chloride, and polyaluminum chloride. Furthermore, the mixed polymer is
Polyamine, polyimine, acrylic amide polymer,
Means a mixture of In the present invention, a mixture of a chloride-based inorganic coagulant and a polyamine-based compound is particularly preferable. These include use in concentrated waste liquids and papermaking wastewater treatment.

【発明の効果】本発明により、シックナーでの脱水効率
とセルロース回収率が大幅に高まり、分離洗浄排水の
C.O.D.、B.O.D.、色素などが著しく低下
し、また処理水等の再利用などを可能とし、その後の排
水処理の負荷を大幅に低減するなど、製紙排水処理工程
における効率アップとコスト削減等が可能となる。
According to the present invention, the dewatering efficiency and the cellulose recovery rate in the thickener are greatly increased, and the C.I. O. D. , B. O. D. In addition, the pigment and the like are remarkably reduced, the reuse of the treated water and the like is enabled, and the load of the subsequent wastewater treatment is greatly reduced.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明における製紙排水処理のフローシートFIG. 1 is a flow sheet for papermaking wastewater treatment in the present invention.

【符号の説明】[Explanation of symbols]

1.離解機 2.キレート高分子凝集剤 3.濃縮排水洗浄装置 4.抄造物 5.洗浄廃液 6.古紙 1. Disintegrator 2. 2. Chelating polymer flocculant Concentrated wastewater washing device 4. Papermaking 5. Wash liquid 6. used paper

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 製紙工程における離解、蒸解廃液に、キ
レート高分子凝集剤を使用し、中性以下に調整すること
を特徴とした処理方法。
1. A treatment method characterized by using a chelating polymer flocculant as a disintegration and digestion waste liquid in a papermaking process and adjusting the waste liquid to neutral or lower.
JP10315278A 1998-10-02 1998-10-02 Treatment of wastewater from paper manufacturing Pending JP2000015267A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10315278A JP2000015267A (en) 1998-10-02 1998-10-02 Treatment of wastewater from paper manufacturing

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10315278A JP2000015267A (en) 1998-10-02 1998-10-02 Treatment of wastewater from paper manufacturing

Publications (1)

Publication Number Publication Date
JP2000015267A true JP2000015267A (en) 2000-01-18

Family

ID=18063492

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10315278A Pending JP2000015267A (en) 1998-10-02 1998-10-02 Treatment of wastewater from paper manufacturing

Country Status (1)

Country Link
JP (1) JP2000015267A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005110931A1 (en) * 2004-05-13 2005-11-24 Hansu Ltd. Method for removing suspension contained in cooling water for spray used in iron works
CN104986841A (en) * 2015-07-30 2015-10-21 李平兰 Treatment agent for paper-making waste fluid

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005110931A1 (en) * 2004-05-13 2005-11-24 Hansu Ltd. Method for removing suspension contained in cooling water for spray used in iron works
CN104986841A (en) * 2015-07-30 2015-10-21 李平兰 Treatment agent for paper-making waste fluid

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