JPH05317899A - Treatment of sludge - Google Patents

Treatment of sludge

Info

Publication number
JPH05317899A
JPH05317899A JP4160341A JP16034192A JPH05317899A JP H05317899 A JPH05317899 A JP H05317899A JP 4160341 A JP4160341 A JP 4160341A JP 16034192 A JP16034192 A JP 16034192A JP H05317899 A JPH05317899 A JP H05317899A
Authority
JP
Japan
Prior art keywords
sludge
pva
water content
treatment
added
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
JP4160341A
Other languages
Japanese (ja)
Inventor
Teruhisa Yoshida
輝久 吉田
Hideaki Hamada
英明 浜田
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.)
Hitachi Kiden Kogyo Ltd
Original Assignee
Hitachi Kiden Kogyo 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 Hitachi Kiden Kogyo Ltd filed Critical Hitachi Kiden Kogyo Ltd
Priority to JP4160341A priority Critical patent/JPH05317899A/en
Publication of JPH05317899A publication Critical patent/JPH05317899A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To improve the handleability of sludge by adding an aq. PVA soln. to the sludge, preparing a uniform liq. mixture, adding inorg. salts to the mixture, flocculating and treating the sludge. CONSTITUTION:An aq. PVA soln. and inorg. salts are added to raw sludge or excess sludge produced at the time of treating sewage to rapidly flocculate the sludge. This sludge is allowed to stand and kneaded. By this kneading, the shrinking action of the sludge is promoted and the sludge solidifies to a rubbery state and becomes nonsticky. The water content of the sludge is reduced to about 76.4% corresponding to a degree attained by dehydration with a dehydrator such as a centrifugal dehydrator or a belt press. The malodor of the sludge is removed and excellent handleability can be imparted.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は生汚泥、余剰汚泥、特に
浮遊汚泥の凝集、集泥、固液分離、及び取扱性のよい汚
泥を製造する汚泥処理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 sludge treatment method for producing raw sludge, surplus sludge, particularly flocculation of sludge, collecting sludge, solid-liquid separation, and sludge having good handleability.

【0002】[0002]

【従来の技術】下水処理に際して水と汚泥とを動分離
し、上澄水は分離除去した後の固形物の下水汚泥は含水
率が極めて高く、そのままでは埋立等に用いることはで
きない。このため下水処理等において発生した汚泥は、
濃縮を行った後、さらにを遠心脱水、またはベルトプレ
ス脱水機にて所望の含水率まで脱水処理している。
2. Description of the Related Art Sewage sludge, which is a solid after the water and sludge are dynamically separated and the supernatant water is separated and removed during sewage treatment, has an extremely high water content and cannot be used as it is for landfilling. Therefore, sludge generated in sewage treatment, etc.
After concentrating, it is further dehydrated by centrifugal dehydration or a belt press dehydrator to a desired water content.

【0003】[0003]

【発明が解決しようとする課題】しかし、下水処理にお
いて単に水と固形物とを分離するには時間を要し、かつ
非能率である。このため、固液を分離する際、濃縮汚泥
中に高分子凝集剤を添加して汚泥フロックを増大し、脱
水に供している。この場合、汚泥の各性状に適した凝集
剤を選定し、かつ適正に使用するために非常に限られた
濃度範囲で薬剤を汚泥中に注入することが必要で、この
技術が充分でないと、脱水ケーキの含水率が高くなり、
ベトつき、後の脱水処理においての取扱性が悪くなる。
However, in the treatment of sewage, it takes time and is inefficient to simply separate water and solids. Therefore, when the solid-liquid is separated, a polymer flocculant is added to the concentrated sludge to increase sludge flocs, which is then used for dehydration. In this case, it is necessary to select a flocculant suitable for each property of the sludge, and to inject the chemical into the sludge in a very limited concentration range for proper use, and if this technique is not sufficient, The water content of the dehydrated cake becomes high,
Stickiness and poor handleability in the subsequent dehydration treatment.

【0004】本発明は下水汚泥を簡易に凝集せしめ、得
られた汚泥を簡易に脱水するのみで、取扱性を向上させ
ることを目的とする。
An object of the present invention is to improve the handleability by simply coagulating the sewage sludge and simply dehydrating the obtained sludge.

【0005】[0005]

【課題を解決するための手段】本発明は上記目的を達成
するためになしたもので、水処理において発生する生汚
泥、余剰汚泥等の汚泥に、ポリビニルアルコール(以下
PVAと略す)水溶液を添加して均一状態とした混合液
に無機塩類を加えて汚泥を凝集して処理することを特徴
とすることを要旨とする。
Means for Solving the Problems The present invention has been made to achieve the above object, and an aqueous solution of polyvinyl alcohol (hereinafter abbreviated as PVA) is added to sludge such as raw sludge and excess sludge generated in water treatment. The gist is that the sludge is treated by adding inorganic salts to the mixed solution which has been made uniform by adding inorganic salts.

【0006】[0006]

【作用】下水処理に際して発生する生汚泥、余剰汚泥に
安価に入手できるポリビニルアルコール水溶液に無機塩
類を加えるのみで、下水汚泥は速やかに凝集する。これ
をさらに静置した後、混練すると、汚泥の収縮作用を助
長してゴム状にまで固化し、ベトつきがなくなる。含水
率は76.4%位となるので、円心脱水機やベルトプレ
ス機による脱水機で脱水した程度となり、汚泥の処理が
迅速簡易に行えるものとなる。
The sewage sludge is rapidly aggregated by simply adding inorganic salts to an aqueous polyvinyl alcohol solution that can be obtained at low cost from raw sludge and surplus sludge generated during sewage treatment. When this is left to stand still and then kneaded, the contraction action of the sludge is promoted and the sludge is solidified into a rubber-like form, and stickiness disappears. Since the water content is about 76.4%, it is about dehydrated by a dewatering machine such as a concentric dewatering machine or a belt press machine, and sludge can be treated quickly and easily.

【0007】[0007]

【実施例】以下本発明を実施例により説明する。EXAMPLES The present invention will be described below with reference to examples.

【0008】〔実施例1〕活性汚泥100mlに15%
PVA水溶液10mlを添加し、継いで10%硫酸ナト
リウム溶液400mlを添加した後、60分間静置す
る。その後、集泥及び混練し、汚泥の水切りをした後、
含水率を計測したら含水率は76.4%であった。上記
操作において、硫酸ナトリウム水溶液を添加すると汚泥
は速やかに凝集浮上する。次の60分静置後の集泥操作
段階では汚泥は充分に収縮されており、強度的にもピン
セット等で挟んで取出可能な状態に達する。さらに汚泥
を混練して収縮作用を助長すると汚泥はゴム状にまで固
化し、ベトつき、悪臭のない取扱性に優れた性状に改善
される。表面水を水切りした汚泥の含水率は76.4%
であり、円心脱水やベルトプレス脱水とほぼ同等の性能
を有する。
[Example 1] 15% per 100 ml of activated sludge
After adding 10 ml of an aqueous PVA solution and subsequently adding 400 ml of a 10% sodium sulfate solution, the mixture is allowed to stand for 60 minutes. After that, after collecting and kneading the mud and draining the sludge,
When the water content was measured, the water content was 76.4%. In the above operation, when the sodium sulfate aqueous solution is added, the sludge rapidly flocculates and floats. In the next sludge collection operation stage after standing for 60 minutes, the sludge is sufficiently shrunk, and in terms of strength, it reaches a state where it can be taken out by being sandwiched with tweezers or the like. Further, when the sludge is kneaded to promote the contraction action, the sludge is solidified into a rubber-like state, and the sludge is improved to a property that is not sticky and has no bad odor and is excellent in handleability. The water content of the sludge drained from the surface water is 76.4%.
Therefore, it has almost the same performance as the circle-center dehydration and the belt press dehydration.

【0009】〔実施例2〕活性汚泥50ml(推定ML
SS3000mg/l)に5%PVA水溶液を2mlよ
り12mlまで2mlづつ、その添加量を変えて添加
し、さらにこれに10%硫酸ナトリウム200mlを添
加し、一日静置した後、汚泥の凝集性を確認した。実施
例2においては、重合度4000の高粘度性PVAを用
いて、その使用量を実施例1に比して4/5〜2/15
に減量して汚泥の凝集性を観察した。その結果、もっと
もPVAの使用量が少ない2mlの添加試験区でも汚泥
は凝集し、高分子凝集剤で得られるフロックより大きな
ものを形成した。またその後の操作でゴム状汚泥を製造
するには4ml以上の試験区において可能であった。汚
水50ml当たりの使用PVA量は4ml添加の場合、
0.2gとわずかであった。
[Example 2] 50 ml of activated sludge (estimated ML
5% PVA aqueous solution was added to SS3000mg / l) from 2ml to 12ml in 2ml increments, and the addition amount was changed, and 200ml of 10% sodium sulfate was further added to the mixture. confirmed. In Example 2, high-viscosity PVA having a degree of polymerization of 4000 was used, and the amount used was 4/5 to 2/15 as compared with Example 1.
The amount was reduced to 0 and the cohesiveness of the sludge was observed. As a result, the sludge aggregated even in the 2 ml addition test area where the amount of PVA used was the smallest, and the sludge formed was larger than the floc obtained by the polymer flocculant. Further, it was possible to produce rubbery sludge in the subsequent operation in a test area of 4 ml or more. The amount of PVA used per 50 ml of waste water is 4 ml,
The amount was as small as 0.2 g.

【0010】従来の高分子凝集剤は水に溶かすと分子が
分解されて汚泥の凝集性を低下させるため使用毎に、し
かも汚泥の濃度や性状に応じて調整することが必要であ
るが、本発明に使用されるPVAは水溶液中においても
化学的に安定しており、数%程度の水溶液とした場合で
もゲル化することなく、30日以上保存できる共に、安
価に入手できるもので、下水処理に際して好適である。
Since the conventional polymer flocculant decomposes molecules when dissolved in water to reduce the coagulability of sludge, it is necessary to adjust the coagulant for each use and according to the concentration and properties of the sludge. The PVA used in the invention is chemically stable even in an aqueous solution, can be stored for 30 days or more without gelation even when made into an aqueous solution of about several%, and can be obtained at low cost. In that case, it is suitable.

【0011】〔実施例3〕MLSS3000mg/lの
汚泥50mlに対して、表−1のようにPVA添加量を
変化させ、次に硫酸ナトリウム以外の無機塩類として、
硫酸カリウム〔K2SO4〕、硫酸アンモニウム〔(NH
a)2SO4〕について、種々の濃度に調整し、200m
lを加えて、汚泥の凝集性、固化性を確認した。
Example 3 With respect to 50 ml of MLSS 3000 mg / l sludge, the addition amount of PVA was changed as shown in Table 1, and then, as inorganic salts other than sodium sulfate,
Potassium sulfate [K2SO4], ammonium sulfate [(NH
a) 2SO4] is adjusted to various concentrations, and 200m
1 was added to confirm sludge cohesiveness and solidification.

【0012】[0012]

【表1】 [Table 1]

【0013】本試験より、無機塩類の種類によって、そ
の使用量に差があるものの、汚泥の凝集、あるいは固化
に、PVAと硫酸塩の組み合わせが有効であることが確
認された。固化汚泥の水切後の含水率は、PVA10m
l添加試験区において、15%硫酸ナトリウムの場合、
76.8%、25%硫酸アンモニウムの場合、78.2
%であり、硫酸ナトリウムとほぼ同等の性能を示した。
From this test, it was confirmed that the combination of PVA and sulfate is effective for agglomeration or solidification of sludge, although the amount used varies depending on the type of inorganic salt. The water content of the solidified sludge after draining is 10 m of PVA.
In the 1 addition test section, in the case of 15% sodium sulfate,
78.2% for 76.8% and 25% ammonium sulfate
%, Which was almost equivalent to that of sodium sulfate.

【0014】[0014]

【発明の効果】本発明汚泥処理方法は水処理において発
生する生汚泥、余剰汚泥等の汚泥に、ポリビニルアルコ
ール(以下PVAと略す)水溶液を添加して均一状態と
した混合液に無機塩類を加えて汚泥を凝集して処理する
ことを特徴とするようになしているため、使用する薬剤
の単価が高分子凝集剤に比べ安価なる故、下水処理のラ
ンニングコストを安価に抑えると共に、MLSS300
0mg/l程度の比較的汚泥濃度が低い液に対して使用
可能であるため、最終沈澱池から引き抜いた汚泥を直接
処理することができ、従来の汚泥濃縮槽、及び貯留槽が
不要となる。また添加濃度も上限値と下限値を正確に保
持しなければならない高分子凝集剤に比べ、PVAは凝
集に必要な下限値のみを制御すればよく、しかも化学的
に安定しているので、非常に使いやすく、高度な特別の
技術を要することなく下水処理を簡易、かつ確実に行え
る。さらにPVAを添加して得られた汚泥は簡易な水切
りで、含水率76.4%が達成でき、従来の脱水機を必
要としないため、装置が単純でコストが安くなり、また
得られた汚泥はゴム状でベトつき・悪臭がないため、運
搬に対しても有利であるし、炭素・水素・酸素より構成
される物質であるので焼却処分しても有害物質を生成し
ない等の利点を有する。
INDUSTRIAL APPLICABILITY According to the sludge treatment method of the present invention, inorganic salts are added to a mixed solution which is made uniform by adding an aqueous solution of polyvinyl alcohol (hereinafter abbreviated as PVA) to sludge such as raw sludge and surplus sludge generated in water treatment. Since the sludge is treated by aggregating the sludge by using the MLSS300, the unit cost of the chemicals used is lower than that of the polymer flocculant, and the running cost of the sewage treatment is kept low and the MLSS300 is used.
Since it can be used for a liquid having a relatively low sludge concentration of about 0 mg / l, the sludge drawn out from the final settling tank can be directly treated, and the conventional sludge thickening tank and storage tank are unnecessary. In addition, PVA needs to control only the lower limit necessary for aggregation, and is chemically stable, as compared with polymer flocculants that must maintain the upper and lower limits accurately, and therefore is extremely stable. Easy to use, sewage treatment can be performed easily and surely without the need for advanced special technology. Furthermore, the sludge obtained by adding PVA can be easily drained to achieve a water content of 76.4%, and since a conventional dehydrator is not required, the device is simple and the cost is low. Is a rubber-like substance that is not sticky or has a bad odor, so it is advantageous for transportation, and because it is a substance composed of carbon, hydrogen, and oxygen, it does not produce harmful substances even when incinerated. ..

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 水処理において発生する生汚泥、余剰汚
泥等の汚泥に、ポリビニルアルコール(以下PVAと略
す)水溶液を添加して均一状態とした混合液に無機塩類
を加えて汚泥を凝集して処理することを特徴とする汚泥
処理方法。
1. An inorganic salt is added to a mixed solution obtained by adding an aqueous solution of polyvinyl alcohol (hereinafter abbreviated as PVA) to a sludge such as raw sludge and surplus sludge generated in water treatment to aggregate the sludge. A sludge treatment method characterized by treating the sludge.
【請求項2】 前記無機塩類が硫酸ナトリウム、硫酸カ
リウム等の硫酸塩である請求項1記載の汚泥処理方法。
2. The sludge treatment method according to claim 1, wherein the inorganic salts are sulfates such as sodium sulfate and potassium sulfate.
JP4160341A 1992-05-26 1992-05-26 Treatment of sludge Pending JPH05317899A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4160341A JPH05317899A (en) 1992-05-26 1992-05-26 Treatment of sludge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4160341A JPH05317899A (en) 1992-05-26 1992-05-26 Treatment of sludge

Publications (1)

Publication Number Publication Date
JPH05317899A true JPH05317899A (en) 1993-12-03

Family

ID=15712893

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4160341A Pending JPH05317899A (en) 1992-05-26 1992-05-26 Treatment of sludge

Country Status (1)

Country Link
JP (1) JPH05317899A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004060819A1 (en) * 2003-05-07 2004-07-22 Ciba Specialty Chemicals Water Treatments Limited Treatment of aqueous suspensions
AU2006100744B4 (en) * 2003-05-07 2007-06-14 Ciba Specialty Chemicals Water Treatments Limited Treatment of Aqueous Suspensions
JP2007275848A (en) * 2006-04-11 2007-10-25 Toyokazutada Kk Composite material utilizing industrial waste liquid, solid-liquid separation method of industrial waste liquid and storage method of industrial waste liquid
WO2012132521A1 (en) * 2011-03-25 2012-10-04 栗田工業株式会社 Method for modifying slurry of coal and/or iron ore
CN108147631A (en) * 2017-12-23 2018-06-12 郭舒洋 A kind of compound sludge curing agent

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004060819A1 (en) * 2003-05-07 2004-07-22 Ciba Specialty Chemicals Water Treatments Limited Treatment of aqueous suspensions
AU2006100744B4 (en) * 2003-05-07 2007-06-14 Ciba Specialty Chemicals Water Treatments Limited Treatment of Aqueous Suspensions
EA011444B1 (en) * 2003-05-07 2009-02-27 Циба Спешиалти Кемикэлз Уотер Тритментс Лимитед Treatment of aqueous suspensions
US7901583B2 (en) 2003-05-07 2011-03-08 Ciba Specialty Chemicals Water Treatments Ltd. Treatment of aqueous suspensions
JP2007275848A (en) * 2006-04-11 2007-10-25 Toyokazutada Kk Composite material utilizing industrial waste liquid, solid-liquid separation method of industrial waste liquid and storage method of industrial waste liquid
JP4649361B2 (en) * 2006-04-11 2011-03-09 豊和直 株式会社 Composite material utilizing industrial waste liquid, solid-liquid separation method of industrial waste liquid, and storage method of industrial waste liquid
WO2012132521A1 (en) * 2011-03-25 2012-10-04 栗田工業株式会社 Method for modifying slurry of coal and/or iron ore
JP2012214292A (en) * 2011-03-25 2012-11-08 Kurita Water Ind Ltd Method for modifying slurry of coal and/or iron ore
CN103392015A (en) * 2011-03-25 2013-11-13 栗田工业株式会社 Method for modifying slurry of coal and/or iron ore
KR20140048847A (en) * 2011-03-25 2014-04-24 쿠리타 고교 가부시키가이샤 Method for modifying slurry of coal and/or iron ore
CN108147631A (en) * 2017-12-23 2018-06-12 郭舒洋 A kind of compound sludge curing agent

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