JP2001286900A - Method for flocculating organic sludge and polymer flocculating agent - Google Patents
Method for flocculating organic sludge and polymer flocculating agentInfo
- Publication number
- JP2001286900A JP2001286900A JP2000106189A JP2000106189A JP2001286900A JP 2001286900 A JP2001286900 A JP 2001286900A JP 2000106189 A JP2000106189 A JP 2000106189A JP 2000106189 A JP2000106189 A JP 2000106189A JP 2001286900 A JP2001286900 A JP 2001286900A
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- polymer
- general formula
- equivalent value
- following general
- 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.)
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Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、下水、し尿或いは有機
性産業廃水より生じる有機性汚泥を遠心脱水機やベルト
プレス脱水機などで脱水処理する際の前操作として行わ
れる凝集方法および該凝集方法に用いる高分子凝集剤に
関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a coagulation method and a coagulation method which are carried out as a pre-operation when dewatering an organic sludge generated from sewage, human waste or organic industrial wastewater by a centrifugal dehydrator or a belt press dehydrator. The present invention relates to a polymer flocculant used in the method.
【0002】[0002]
【従来の技術】従来、有機性汚泥の脱水処理には、カチ
オン性高分子凝集剤および両性高分子凝集剤或いはカチ
オンポリマーと両性ポリマーを混合した凝集剤を汚泥中
に添加して有機物を凝集してフロックを得、該フロック
を脱水機にかけて脱水するようにしている。2. Description of the Related Art Conventionally, in the dehydration treatment of organic sludge, a cationic polymer coagulant and an amphoteric polymer coagulant or a coagulant obtained by mixing a cationic polymer and an amphoteric polymer are added to sludge to coagulate organic substances. To obtain a floc, and the floc is dewatered by a dehydrator.
【0003】[0003]
【発明が解決しようとする課題】しかしながら、従来の
凝集剤は、有機物含有量が多く、汚泥の表面の負電荷の
大きい難脱水性汚泥を凝集しても、強度の弱いフロック
しか得られず、従って、脱水機にかけると該フロックが
壊れ易くなり、該フロックの含水率を低下できず、ベル
トプレス脱水機による脱水操作においては剥離性に問題
があった。また、汚泥濃度の変動、有機物含有量の変動
等に追従することが難しく安定した脱水処理操作が困難
でもある。However, the conventional flocculant has a large amount of organic matter and can only obtain floc having a low strength even when flocculating hardly dewaterable sludge having a large negative charge on the sludge surface. Therefore, when the floc is applied to a dehydrator, the floc is easily broken, the water content of the floc cannot be reduced, and there is a problem in the releasability in the dehydrating operation by the belt press dehydrator. Further, it is difficult to follow the fluctuation of the sludge concentration, the fluctuation of the organic matter content, and the like, and it is also difficult to perform a stable dehydration treatment operation.
【0004】本発明は、有機物含有量が多く、汚泥の表
面の負電荷が大きい難脱水性汚泥で汚泥濃度および有機
物含有量の変動のある汚泥を安定して脱水処理するため
鋭意検討した結果、創案し得たものである。The present invention has been made as a result of intensive studies to stably dehydrate sludge having a large amount of organic matter and a sludge with a large negative charge on the surface of the sludge and having a variable sludge concentration and organic matter content. It was invented.
【0005】[0005]
【課題を解決するための手段】(カオチン当量値CV)
/(アニオン当量値AV)の比が1.0〜1.4である
下記一般式(1)で示される両性ポリマーと下記一般式
(2)で示されるカチオンポリマーを、カチオンポリマ
ーを25〜80重量%の割合で有機性汚泥中に添加混合
することにある。[Means for Solving the Problems] (Chaotin equivalent value C V )
The ratio of / (anion equivalent value A V ) is 1.0 to 1.4, and the amphoteric polymer represented by the following general formula (1) and the cationic polymer represented by the following general formula (2) are used. It is to add and mix the organic sludge at a ratio of 80% by weight.
【0006】[0006]
【化3】 Embedded image
【0007】添加混合に際し、両性ポリマーとカチオン
ポリマーを相前後して有機性汚泥中に添加するようにし
ても良いが、各ポリマーを混合して凝集剤と成し、該凝
集剤が粉末の場合は水で溶かし、液状の場合は水で希釈
して添加混合するようにすると凝集操作が円滑に行われ
る。At the time of addition and mixing, the amphoteric polymer and the cationic polymer may be added to the organic sludge immediately before and after, but each polymer is mixed to form a flocculant, and when the flocculant is a powder, Is dissolved in water, and if liquid, it is diluted with water and added and mixed, so that the coagulation operation is performed smoothly.
【0008】従って、(カオチン当量値CV)/(アニ
オン当量値AV)の比が1.0〜1.4である前記一般
式(1)で示される両性ポリマーと前記一般式(2)で
示されるカチオンポリマーを、カチオンポリマーを25
〜80重量%の割合で混合した高分子凝集剤と成し、殊
に、該高分子凝集剤を液状とすることにより有機性汚泥
の凝集操作上好適な製品を提供できる。Accordingly, the amphoteric polymer represented by the general formula (1) wherein the ratio of (chaotin equivalent value C V ) / (anion equivalent value A V ) is 1.0 to 1.4, and the above-mentioned general formula (2) The cationic polymer represented by
A polymer coagulant mixed at a ratio of up to 80% by weight can be provided. In particular, by making the polymer coagulant liquid, a product suitable for coagulation operation of organic sludge can be provided.
【0009】なお、前記一般式(1)で示される両性ポ
リマーならびに前記一般式(2)で示されるカチオンポ
リマーは水溶液重合法、乳化重合法、塊状重合法、懸濁
重合法により製造できる。The amphoteric polymer represented by the general formula (1) and the cationic polymer represented by the general formula (2) can be produced by an aqueous solution polymerization method, an emulsion polymerization method, a bulk polymerization method, or a suspension polymerization method.
【0010】本発明の高分子凝集剤は単独で汚泥脱水に
使用しても良いが、無機凝集剤として硫酸バンド、塩化
第二鉄、硫酸第一鉄、ポリ硫酸第二鉄と併用すること
で、脱水性、濾布剥離性においてより良い効果が得られ
る。Although the polymer flocculant of the present invention may be used alone for sludge dewatering, it can be used in combination with a sulfate band, ferric chloride, ferrous sulfate and ferric polysulfate as an inorganic flocculant. A better effect can be obtained in terms of dehydration and filter cloth releasability.
【0011】汚泥に対する本発明の高分子凝集剤の添加
量は通常1.0〜1.5%/汚泥TS当たり、であり、
無機凝集剤の添加量は、汚泥の荷電量を測定し、その荷
電量の約1/2を中和する程度の無機凝集剤を添加する
ことが望ましい。The amount of the polymer flocculant of the present invention to be added to sludge is usually 1.0 to 1.5% / per sludge TS.
The amount of the inorganic flocculant to be added is preferably such that the amount of charge of the sludge is measured, and the amount of the inorganic flocculant that neutralizes about の of the charge is added.
【0012】[0012]
【実施例】以下、実施例により本発明を詳細に説明する
が、本発明はこれに限定されるものではない。EXAMPLES The present invention will be described in detail below with reference to examples, but the present invention is not limited to these examples.
【0013】アクリロイルオキシエチルトリメチルアン
モニウムクロライド80mol%、アクリルアミド20
mol%を組成分とするカチオンポリマーK−1と、ア
クリロイルオキシエチルトリメチルアンモニウムクロラ
イド14mol%、アクリル酸10mol%、アクリル
アミド76mol%を組成分とする両性ポリマーKA−
1およびコロイド滴定値より推定してメタアクリロイル
オキシエチルトリメチルアンモニウムクロライド30m
ol、アクリル酸10mol%、アクリルアミド60m
ol%を組成分とする市販の両性ポリマーR−1のそれ
ぞれを表−1及び表−2に示す重量%にして、有機物含
有量の多い下水消化汚泥(VTS/TS:74.8%)
にポリ硫酸第二鉄3%/TSを添加後、高分子凝集剤を
加え、遠心脱水しケーキ含水率を測定した。Acryloyloxyethyltrimethylammonium chloride 80 mol%, acrylamide 20
mol% of the cationic polymer K-1 and acryloyloxyethyltrimethylammonium chloride 14 mol%, acrylic acid 10 mol%, and acrylamide 76 mol% of the amphoteric polymer KA-.
1 and methacryloyloxyethyltrimethylammonium chloride 30 m
ol, acrylic acid 10mol%, acrylamide 60m
ol% of each component of the commercially available amphoteric polymer R-1 having a composition as shown in Tables 1 and 2, and the sewage digested sludge having a high organic content (VTS / TS: 74.8%).
After adding ferric polysulfate 3% / TS to the mixture, a polymer flocculant was added, and the mixture was centrifugally dehydrated to measure the water content of the cake.
【0014】比較例として、カチオンポリマーK−1単
独、市販両性ポリマーR−1単独、及びカチオンポリマ
ーK−1 10%,R−1 90%の混合品についても
試験した。As comparative examples, a test was also conducted on a cationic polymer K-1 alone, a commercially available amphoteric polymer R-1 alone, and a mixture of 10% cationic polymer K-1 and 90% R-1.
【0015】結果は表−1のように実施例は比較例と比
べケーキ含水率を低下することができた。As shown in Table 1, the water content of the cake was reduced in the example as compared with the comparative example.
【0016】実施例5及び比較例7は高分子凝集剤を
1.5%/TSと多量に添加した試験において、比較例
7はフロックが再分散して小さくなり、含水率が上昇し
たが、実施例5はフロックの再分散は殆どなく安定して
処理できた。In Example 5 and Comparative Example 7, a test was conducted in which a large amount of a polymer flocculant was added at 1.5% / TS. In Comparative Example 7, the floc was redispersed and became smaller, and the water content increased. In Example 5, the floc was hardly redispersed, and the treatment could be performed stably.
【0017】[0017]
【表1】 [Table 1]
【0018】[0018]
【表2】 [Table 2]
【0019】[0019]
【発明の効果】本発明方法は従来脱水が困難であった有
機物含有量の多い難脱水性汚泥に対してフロック強度が
強い凝集操作を行うことができ、従って、脱水ケーキの
含水率を低下でき、濾布剥離性も良い為、スクリューデ
カンター、ベルトプレス等の脱水機において優れた脱水
処理を可能にした。また、本発明の高分子凝集剤は、過
剰添加によっておこるフロックの再分散が起こり難く最
適添加量範囲が広い為、汚泥濃度及び有機物含有量の変
動にも安定した処理を可能にした。According to the method of the present invention, a flocculation operation having a high floc strength can be performed on a hardly dewaterable sludge having a large amount of organic matter, which has conventionally been difficult to dewater, so that the water content of the dewatered cake can be reduced. Since the filter fabric has good releasability, excellent dehydration treatment is possible in a dehydrator such as a screw decanter or a belt press. Further, the polymer flocculant of the present invention makes it difficult to re-disperse floc caused by excessive addition and has a wide optimum addition amount range, so that a stable treatment can be performed even when the sludge concentration and the organic matter content fluctuate.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) C08L 33/00 C08L 33/00 Fターム(参考) 4D015 BA05 BA06 BA11 BA12 BA19 BB06 BB14 BB17 CA12 DA05 DA13 DA15 DA16 DB07 DB13 DB15 DC02 DC06 DC07 EA03 FA03 FA19 4D059 AA01 AA03 AA23 BE16 BE37 BE55 BE56 BE57 DA17 DA23 DA24 DB24 DB26 EB20 4J002 BG01W BG07W BG07X BG13W BG13X FD200 GD05 4J100 AJ02R AL08P AM15Q BA32P CA04 CA05 JA18 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification symbol FI theme coat ゛ (reference) C08L 33/00 C08L 33/00 F term (reference) 4D015 BA05 BA06 BA11 BA12 BA19 BB06 BB14 BB17 CA12 DA05 DA13 DA15 DA16 DB07 DB13 DB15 DC02 DC06 DC07 EA03 FA03 FA19 4D059 AA01 AA03 AA23 BE16 BE37 BE55 BE56 BE57 DA17 DA23 DA24 DB24 DB26 EB20 4J002 BG01W BG07W BG07X BG13W BG13X FD200 GD05 4J100 AJ02R AL08P AL15P ALQPAMQ
Claims (2)
量値AV)の比が1.0〜1.4である下記一般式
(1)で示される両性ポリマーと下記一般式(2)で示
されるカチオンポリマーを、カチオンポリマーを25〜
80重量%の割合で有機性汚泥中に添加混合することを
特徴とする有機性汚泥の凝集方法。 【化1】 1. An amphoteric polymer represented by the following general formula (1) having a ratio of (chaotin equivalent value C V ) / (anion equivalent value A V ) of 1.0 to 1.4, and the following general formula (2) A cationic polymer represented by
A method for coagulating organic sludge, comprising adding and mixing 80% by weight into organic sludge. Embedded image
量値AV)の比が1.0〜1.4である下記一般式
(1)で示される両性ポリマーと下記一般式(2)で示
されるカチオンポリマーを、カチオンポリマーを25〜
80重量%の割合で混合した高分子凝集剤。 【化2】 2. An amphoteric polymer represented by the following general formula (1) having a ratio of (chaotin equivalent value C V ) / (anion equivalent value A V ) of 1.0 to 1.4, and the following general formula (2): A cationic polymer represented by
A polymer flocculant mixed at a ratio of 80% by weight. Embedded image
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2000106189A JP2001286900A (en) | 2000-04-07 | 2000-04-07 | Method for flocculating organic sludge and polymer flocculating agent |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2000106189A JP2001286900A (en) | 2000-04-07 | 2000-04-07 | Method for flocculating organic sludge and polymer flocculating agent |
Publications (1)
Publication Number | Publication Date |
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JP2001286900A true JP2001286900A (en) | 2001-10-16 |
Family
ID=18619407
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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JP2000106189A Pending JP2001286900A (en) | 2000-04-07 | 2000-04-07 | Method for flocculating organic sludge and polymer flocculating agent |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008200597A (en) * | 2007-02-20 | 2008-09-04 | Daiyanitorikkusu Kk | Amphoteric polymer flocculant and method for treating sludge by using the same |
JP2012091079A (en) * | 2010-10-25 | 2012-05-17 | Daiyanitorikkusu Kk | Organic coagulant |
CN103772604A (en) * | 2014-01-23 | 2014-05-07 | 中国海洋石油总公司 | Cationic polymer |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0231899A (en) * | 1988-07-19 | 1990-02-01 | Dia Furotsuku Kk | Method for dehydrating sludge |
JPH0615299A (en) * | 1992-07-04 | 1994-01-25 | Sanyo Chem Ind Ltd | Sludge dehydrating agent |
JPH07256300A (en) * | 1994-03-24 | 1995-10-09 | Nippon Gesuido Jigyodan | Dehydration of sludge using both inorganic flocculant and amphoteric polymeric flocculant |
JPH08112504A (en) * | 1994-10-17 | 1996-05-07 | Sanyo Chem Ind Ltd | Polymer flocculant |
JPH0957299A (en) * | 1995-08-24 | 1997-03-04 | Kurita Water Ind Ltd | Sludge dehydrating agent |
-
2000
- 2000-04-07 JP JP2000106189A patent/JP2001286900A/en active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0231899A (en) * | 1988-07-19 | 1990-02-01 | Dia Furotsuku Kk | Method for dehydrating sludge |
JPH0615299A (en) * | 1992-07-04 | 1994-01-25 | Sanyo Chem Ind Ltd | Sludge dehydrating agent |
JPH07256300A (en) * | 1994-03-24 | 1995-10-09 | Nippon Gesuido Jigyodan | Dehydration of sludge using both inorganic flocculant and amphoteric polymeric flocculant |
JPH08112504A (en) * | 1994-10-17 | 1996-05-07 | Sanyo Chem Ind Ltd | Polymer flocculant |
JPH0957299A (en) * | 1995-08-24 | 1997-03-04 | Kurita Water Ind Ltd | Sludge dehydrating agent |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008200597A (en) * | 2007-02-20 | 2008-09-04 | Daiyanitorikkusu Kk | Amphoteric polymer flocculant and method for treating sludge by using the same |
JP2012091079A (en) * | 2010-10-25 | 2012-05-17 | Daiyanitorikkusu Kk | Organic coagulant |
CN103772604A (en) * | 2014-01-23 | 2014-05-07 | 中国海洋石油总公司 | Cationic polymer |
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