JPH07328323A - High molecular coagulant - Google Patents

High molecular coagulant

Info

Publication number
JPH07328323A
JPH07328323A JP6156823A JP15682394A JPH07328323A JP H07328323 A JPH07328323 A JP H07328323A JP 6156823 A JP6156823 A JP 6156823A JP 15682394 A JP15682394 A JP 15682394A JP H07328323 A JPH07328323 A JP H07328323A
Authority
JP
Japan
Prior art keywords
sludge
polymer
dewatering
vinylformamide
coagulant
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.)
Granted
Application number
JP6156823A
Other languages
Japanese (ja)
Other versions
JP3478871B2 (en
Inventor
Shigeru Sato
茂 佐藤
Masayuki Murano
正幸 村野
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.)
Kurita Water Industries Ltd
Original Assignee
Kurita Water Industries 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 Kurita Water Industries Ltd filed Critical Kurita Water Industries Ltd
Priority to JP15682394A priority Critical patent/JP3478871B2/en
Publication of JPH07328323A publication Critical patent/JPH07328323A/en
Application granted granted Critical
Publication of JP3478871B2 publication Critical patent/JP3478871B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

PURPOSE:To obtain a coagulant which, when used for dewatering of sludge, has a good coagulation effect, gives a coagulated block with high strength and a low water content by mechanical dewatering, and is capable of stable dewatering of sludge by preparing it from a polymer which has benzyl vinylamine monomeric units of a specified structure in a specified ratio. CONSTITUTION:A coagulant is prepared from a polymer having 2-30 mole % of a benzyl vinylamine unit expressed by the formula as a monomeric unit. The polymer is a benzylated product of hydrolyzate of poly-N-vinylformamide or copolymer of N-vinylformamide and other vinyl monomer. The high molecular coagulant when used for dewatering of sludge, has a good coagulation effect, gives a coagulated block with high strength, a low water content by mechanical dewatering, and peelable dewatered cake, enabling stable dewatering of sludge.

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、新規な高分子凝集剤、
さらに詳しくは、汚泥の脱水処理に用いた場合、凝集力
に優れ、強度の高い凝集フロックを与え、機械脱水によ
り含水率が低く、かつ剥離性の良い脱水ケーキを得るこ
とができ、安定した汚泥の脱水処理が可能な高分子凝集
剤に関するものである。
The present invention relates to a novel polymer flocculant,
More specifically, when used in the sludge dewatering treatment, it gives a flocculated floc with excellent cohesive strength and high strength, and it is possible to obtain a dehydrated cake with a low water content and good peelability by mechanical dehydration, and a stable sludge. The present invention relates to a polymer flocculant capable of being dehydrated.

【0002】[0002]

【従来の技術】近年、都市下水し尿処理や工場排水など
の活性汚泥処理が広く行われているが、発生する有機汚
泥は含水率が高いので、廃棄、焼却及び肥料化するため
に、効率よく脱水処理することが必要である。従来、汚
泥の脱水処理には、脱水剤として主に高分子量のカチオ
ン性ポリマー、例えばジメチルアミノエチル(メタ)ア
クリレートの塩酸塩や硫酸塩などの三級塩又は塩化メチ
ル四級化物などの四級アンモニウム塩の単独重合体やア
クリルアミドなどとの共重合体が用いられている。しか
しながら、近年、下水道の整備などにより、汚泥の発生
量が増加していることや、汚泥中の有機物量の増加、腐
敗などによる汚泥性状の悪化が進んでいることから、汚
泥の脱水処理に上記のような従来のカチオン性ポリマー
を用いた場合、(1)凝集フロックは大きいものの、強
度が弱いために、(イ)ろ布からのケーキの剥離が悪
く、脱水機の運転トラブルを起こしやすい、(ロ)ろ過
性が悪いために、汚泥の処理量が上がらない、(ハ)汚
泥中のSS分が分離液中に漏出する、(2)脱水ケーキ
の含水率が高いために、(イ)ケーキの埋め立て処分の
場合、その運搬費用が高くつく、(ロ)焼却処分の場
合、燃料費が高くつくとともに、焼却炉のトラブルが発
生しやすい、(3)汚泥の脱水処理が安定しない、など
の問題が生じ、処理方法の改善が求められていた。
2. Description of the Related Art In recent years, activated sludge treatment such as municipal sewage treatment and sewage treatment and industrial wastewater has been widely performed. However, since the organic sludge generated has a high water content, it can be efficiently disposed of for disposal, incineration and fertilization. It is necessary to perform dehydration treatment. Conventionally, sludge is dehydrated mainly by using a high molecular weight cationic polymer as a dehydrating agent, for example, tertiary salts such as dimethylaminoethyl (meth) acrylate hydrochloride and sulfate, or quaternary salts such as methyl chloride quaternary. A homopolymer of an ammonium salt or a copolymer with acrylamide is used. However, in recent years, the amount of sludge generated has increased due to the development of sewer systems, the amount of organic matter in sludge has increased, and sludge properties have deteriorated due to decay, etc. When a conventional cationic polymer such as (1) is used, (1) the flocculation flocs are large, but the strength is weak, so (a) peeling of the cake from the filter cloth is poor, and operating problems of the dehydrator are likely to occur. (B) Due to poor filterability, the sludge treatment amount does not increase, (c) SS content in the sludge leaks into the separated liquid, (2) because the dehydrated cake has a high water content, (a) In the case of cake landfill disposal, the transportation cost is high, (b) In the case of incineration disposal, the fuel cost is high and troubles in the incinerator are likely to occur, (3) Sludge dewatering process is not stable, etc. The problem of Improvement of the method has been demanded.

【0003】[0003]

【発明が解決しようとする課題】本発明は、このような
従来のカチオン性ポリマーが有する欠点を克服し、汚泥
の脱水処理に用いた場合、凝集力に優れ、強度の高い凝
集フロックを与え、機械脱水により含水率が低く、かつ
剥離性の良い脱水ケーキを得ることができ、安定した汚
泥の脱水処理が可能な高分子凝集剤を提供することを目
的としてなされたものである。
DISCLOSURE OF THE INVENTION The present invention overcomes the drawbacks of such conventional cationic polymers, and when used for sludge dewatering treatment, provides floc with excellent cohesive force and high strength. The purpose of the present invention is to provide a polymer flocculant capable of obtaining a dehydrated cake having a low water content and good peelability by mechanical dehydration and capable of performing stable dehydration treatment of sludge.

【0004】[0004]

【課題を解決するための手段】本発明者らは、前記の好
ましい性質を有する高分子凝集剤を開発すべく鋭意研究
を重ねた結果、構成単位として、ベンジル化ビニルアミ
ン単位を特定の割合で含有するポリマーから成る高分子
凝集剤が、その目的に適合しうることを見い出し、この
知見に基づいて本発明を完成するに至った。すなわち、
本発明は、 (1)構成単量体単位として、式
Means for Solving the Problems As a result of intensive studies to develop a polymer flocculant having the above-mentioned preferable properties, the present inventors have found that a specific proportion of a benzylated vinylamine unit is contained as a constitutional unit. It has been found that a polymer flocculant composed of the above polymer can meet the purpose, and the present invention has been completed based on this finding. That is,
The present invention provides the following formula (1) as a constituent monomer unit:

【化2】 で表されるベンジル化ビニルアミン単位2〜30モル%
を含有するポリマーから成る高分子凝集剤、及び、 (2)ポリマーが、N−ビニルホルムアミドの単独重合
体又はN−ビニルホルムアミドと他のビニル系単量体と
の共重合体の加水分解物をベンジル化したものである第
(1)項記載の高分子凝集剤を提供するものである。
[Chemical 2] 2-30 mol% of benzylated vinylamine unit represented by
And a polymer flocculant comprising a polymer containing (2) a polymer, a hydrolyzate of a homopolymer of N-vinylformamide or a copolymer of N-vinylformamide and another vinyl-based monomer. Benzylated one
The polymer coagulant according to the item (1) is provided.

【0005】以下、本発明を詳細に説明する。本発明の
高分子凝集剤は、構成単量体単位として、式
The present invention will be described in detail below. The polymer flocculant of the present invention has the formula:

【化3】 で表されるベンジル化ビニルアミン単位2〜30モル%
を含有するポリマーから成るものであって、前記式
[1]で表されるベンジル化ビニルアミン単位以外の構
成単量体単位としては、ビニルアミン単位及び/又は共
重合可能な他のビニル系単量体単位などを挙げることが
できる。該ポリマーにおいて、ベンジル化ビニルアミン
単位の含有量が2モル%未満ではベンジル化の効果が発
揮されにくく、本発明の目的が十分に達せられないし、
30モル%を超えると疎水性が強くなりすぎて、汚泥脱
水剤としての効果がむしろ低下する傾向がみられる。本
発明の高分子凝集剤の製造方法については特に制限はな
いが、例えば以下に示す方法によって、該高分子凝集剤
を好ましく製造することができる。まず、N−ビニルホ
ルムアミド若しくはN−ビニルアセトアミドの単独重合
体、N−ビニルホルムアミドとN−ビニルアセトアミド
の共重合体、又はN−ビニルホルムアミド若しくはN−
ビニルアセトアミドと他のビニル系単量体との共重合体
を製造する。この際用いられる共重合可能なビニル系単
量体としては、例えばアクリルアミド、メタクリルアミ
ド、スチレン、アクリル酸メチル、メタクリル酸メチ
ル、アクリル酸エチル、メタクリル酸エチル、酢酸ビニ
ル、アクリロニトリル、N−ビニルピロリドンなどのノ
ニオン性単量体;アクリル酸、メタクリル酸又はこれら
のアルカリ金属塩、ビニルスルホン酸、2−アクリルア
ミド−2−メチルプロパンスルホン酸、スチレンスルホ
ン酸などのスルホン基を有する化合物又はそのアルカリ
金属塩などのアニオン性単量体;ジメチルアミノエチル
アクリレート、ジメチルアミノエチルメタクリレート、
ジメチルアミノプロピルアクリルアミド、ジメチルアミ
ノプロピルメタクリルアミドなどの三級塩若しくは四級
アンモニウム塩などのカチオン性単量体を挙げることが
できるが、もちろんこれらに限定されるものではない。
これらの共重合可能なビニル系単量体は1種用いてもよ
いし、2種以上を組み合わせて用いてもよい。
[Chemical 3] 2-30 mol% of benzylated vinylamine unit represented by
And a vinylamine unit and / or another copolymerizable vinyl-based monomer as a constituent monomer unit other than the benzylated vinylamine unit represented by the formula [1]. A unit etc. can be mentioned. In the polymer, when the content of benzylated vinylamine unit is less than 2 mol%, the effect of benzylation is difficult to be exhibited, and the object of the present invention cannot be sufficiently achieved.
If it exceeds 30 mol%, the hydrophobicity becomes too strong and the effect as a sludge dehydrating agent tends to be rather lowered. The method for producing the polymer flocculant of the present invention is not particularly limited, but the polymer flocculant can be preferably produced by, for example, the method described below. First, a homopolymer of N-vinylformamide or N-vinylacetamide, a copolymer of N-vinylformamide and N-vinylacetamide, or N-vinylformamide or N-
A copolymer of vinylacetamide and another vinyl monomer is produced. Examples of the copolymerizable vinyl monomer used at this time include acrylamide, methacrylamide, styrene, methyl acrylate, methyl methacrylate, ethyl acrylate, ethyl methacrylate, vinyl acetate, acrylonitrile, N-vinylpyrrolidone, etc. Nonionic monomers; acrylic acid, methacrylic acid or alkali metal salts thereof, vinyl sulfonic acid, 2-acrylamido-2-methylpropane sulfonic acid, styrene sulfonic acid and other compounds having a sulfone group, or alkali metal salts thereof, etc. Anionic monomer of dimethylaminoethyl acrylate, dimethylaminoethyl methacrylate,
Examples thereof include, but are not limited to, cationic monomers such as tertiary salts such as dimethylaminopropyl acrylamide and dimethylaminopropyl methacrylamide, or quaternary ammonium salts.
These copolymerizable vinyl monomers may be used alone or in combination of two or more.

【0006】また、重合方法については特に制限はな
く、例えば溶液重合法、懸濁重合法、乳化重合法など、
一般に用いられる方法を採用することができる。次い
で、このようにして得られたベースポリマーに、加水分
解率に応じた量の塩酸などの酸性物質又は水酸化ナトリ
ウムなどのアルカリ性物質を加え、通常40〜100℃
程度の温度において反応させることにより、加水分解し
てカチオン化、すなわち一級アミノ基を有するポリマー
を得る。この際、加水分解率(カチオン化率)は、N−
ビニルホルムアミド単位若しくはN−ビニルアセトアミ
ド単位に対し、20〜95モル%の範囲が好ましい。次
に、前記一級アミノ基を有するポリマーに、アルカリ性
条件下で塩化ベンジルや臭化ベンジルなどのハロゲン化
ベンジルを、通常40〜100℃程度の温度において反
応させることにより、一級アミノ基をベンジル化して、
ベンジル化ビニルアミン単位2〜30モル%を含有する
ポリマーを製造する。このようにして得られた反応液
は、そのまま高分子凝集剤として用いてもよいし、塩酸
などの酸を加えてアミン部分を塩酸塩などにし、高分子
凝集剤として用いてもよく、あるいはこれらをアセトン
やメタノールなどの適当な溶媒中に投入し、粉末状のポ
リマーを取り出して、高分子凝集剤として用いてもよ
い。本発明の高分子凝集剤として用いられる前記ポリマ
ーの分子量は、処理対象(汚泥)の性状や汚泥脱水の機
械条件などにより適宜選ばれるが、その指標となる0.
1N−塩化ナトリウム水溶液中において温度30℃で測
定した固有粘度で8dl/g以上が好ましい。なお、該ポ
リマーの構造決定は、定性的には赤外分光分析法(IR
法)でもよいが、ベンジル化率を正確に知るには核磁気
共鳴吸収法(NMR法)を用いるのがよい。本発明の高
分子凝集剤は、特に汚泥脱水剤として好適に用いられ、
この際、必要に応じて塩化第二鉄、ポリ硫酸鉄、ポリ塩
化アルミニウム、硫酸バンドなどの無機系凝集剤や、そ
の他の有機系高分子凝集剤と併用することができる。ま
た、本発明の高分子凝集剤を汚泥脱水剤として用いる場
合、対象となる汚泥としては、有機性汚泥であればよ
く、汚泥種や汚泥性状については特に制限されず、例え
ば下水の混合生汚泥、下水の消化汚泥、し尿処理汚泥、
一般産業排水処理で生じる余剰汚泥などが挙げられる。
また、汚泥の脱水に用いられる脱水機としては、例えば
ベルトプレス脱水機、遠心脱水機、フィルタープレス脱
水機、スクリュープレス脱水機、真空脱水機などが挙げ
られる。
The polymerization method is not particularly limited, and examples thereof include solution polymerization method, suspension polymerization method and emulsion polymerization method.
A commonly used method can be adopted. Then, to the base polymer thus obtained, an acidic substance such as hydrochloric acid or an alkaline substance such as sodium hydroxide is added in an amount according to the hydrolysis rate, and the temperature is usually 40 to 100 ° C.
By reacting at a moderate temperature, hydrolysis is performed to cationize, that is, a polymer having a primary amino group is obtained. At this time, the hydrolysis rate (cationization rate) is N-
The range of 20 to 95 mol% is preferable with respect to the vinylformamide unit or the N-vinylacetamide unit. Next, the primary amino group is benzylated by reacting the polymer having a primary amino group with a benzyl halide such as benzyl chloride or benzyl bromide at a temperature of about 40 to 100 ° C. under alkaline conditions. ,
A polymer containing 2 to 30 mol% benzylated vinylamine units is prepared. The reaction solution thus obtained may be used as a polymer flocculant as it is, or may be used as a polymer flocculant by adding an acid such as hydrochloric acid to convert the amine moiety into a hydrochloride or the like. Alternatively, the powdery polymer may be put into an appropriate solvent such as acetone or methanol and taken out to be used as a polymer flocculant. The molecular weight of the polymer used as the polymer flocculant of the present invention is appropriately selected depending on the properties of the object to be treated (sludge), the mechanical conditions for sludge dewatering, etc.
The intrinsic viscosity measured at a temperature of 30 ° C. in a 1N sodium chloride aqueous solution is preferably 8 dl / g or more. The structure of the polymer is qualitatively determined by infrared spectroscopic analysis (IR
Method), but it is preferable to use the nuclear magnetic resonance absorption method (NMR method) in order to know the benzylation rate accurately. The polymer flocculant of the present invention is particularly preferably used as a sludge dehydrating agent,
At this time, if necessary, an inorganic flocculant such as ferric chloride, polyferric sulfate, polyaluminum chloride, and a sulfuric acid band, or other organic polymer flocculant can be used in combination. When the polymer flocculant of the present invention is used as a sludge dehydrating agent, the target sludge may be an organic sludge, and the sludge species and sludge properties are not particularly limited, and for example, mixed raw sludge of sewage. , Sewage digested sludge, human waste treatment sludge,
Examples include surplus sludge generated by general industrial wastewater treatment.
Examples of the dehydrator used for dehydrating sludge include a belt press dehydrator, a centrifugal dehydrator, a filter press dehydrator, a screw press dehydrator, a vacuum dehydrator and the like.

【0007】[0007]

【実施例】次に、実施例により本発明をさらに詳細に説
明するが、本発明はこれらの例によってなんら限定され
るものではない。 製造例1 (1)ベースポリマーの製造 N−ビニルホルムアミド204.8gを蒸留水に溶解し
て1000mlとし、pHを約7に調整した。窒素ガス導入
管、ジムロート冷却管を備えた1000mlセパラブルフ
ラスコに、前記モノマー水溶液を移し、30分間窒素バ
ブリングを行ったのち、2,2'−アゾビスシアノアミジ
ノプロパン・塩酸塩0.54gを加え、50℃にて10
時間重合を行った。次いで、生成した含水ゲル状ポリマ
ーを多量のアセトン中に投入し、脱水、粉砕後、白色粉
末のポリ(N−ビニルホルムアミド)を得た。収率は1
00.1%であった。 (2)ポリ(N−ビニルホルムアミド)の加水分解 前記(1)で得たポリ(N−ビニルホルムアミド)4
0.0gを、撹拌機、冷却管を備えたセパラブルフラス
コに入れ、さらに蒸留水800mlを加え撹拌して、溶解
させた。次いで、35wt%濃塩酸117.2gを加え、
60℃に昇温して撹拌下24時間加水分解を行った。反
応物を多量のアセトンに投入し、脱水、粉砕後、白色粉
末のポリ(N−ビニルホルムアミド)の部分加水分解物の
塩酸塩を得た。収率は100.2%で、コロイド滴定よ
り求めた加水分解率は84モル%であった。 (3)ベンジル化 前記(2)で得られたポリ(N−ビニルホルムアミド)の
部分加水分解物の塩酸塩5.0gを、撹拌機、冷却管を
備えたセパラブルフラスコに入れ、水200mlを加えて
均一溶液とし、15wt%水酸化ナトリウム水溶液25ml
を加えたのち、50℃に昇温し、所定量の塩化ベンジル
を加え、ポリマーA、B、C及びDの4種を得た。 ポリマーの種類 塩化ベンジルの量 A 0.41g B 0.81g C 2.0g D 3.0g 反応終了後は、前記(1)、(2)と同様にアセトンで
精製し、粉末化した。得られたポリマーA〜Dのベンジ
ル化率を、プロトンNMR測定を行って、8ppm付近の
ベンゼン環のプロトンのシグナルと2ppm付近の主鎖メ
チレンのプロトンのシグナルの面積比より測定した。第
1表に、製造例1で得られたポリマーA〜D及び他の供
試ポリマーE、F、Gの物性を示す。
The present invention will be described in more detail by way of examples, which should not be construed as limiting the invention thereto. Production Example 1 (1) Production of Base Polymer 204.8 g of N-vinylformamide was dissolved in distilled water to 1000 ml, and the pH was adjusted to about 7. The monomer aqueous solution was transferred to a 1000 ml separable flask equipped with a nitrogen gas introduction tube and a Dimroth condenser tube, and after nitrogen bubbling for 30 minutes, 0.52 g of 2,2′-azobiscyanoamidinopropane · hydrochloride was added. 10 at 50 ° C
Polymerization was carried out for a time. Next, the produced hydrogel polymer was put into a large amount of acetone, dehydrated and pulverized to obtain white powder of poly (N-vinylformamide). Yield is 1
It was 0.1%. (2) Hydrolysis of poly (N-vinylformamide) Poly (N-vinylformamide) 4 obtained in (1) above
0.0 g was placed in a separable flask equipped with a stirrer and a condenser, and 800 ml of distilled water was further added and stirred to dissolve it. Then, 117.2 g of 35 wt% concentrated hydrochloric acid was added,
The temperature was raised to 60 ° C. and hydrolysis was performed for 24 hours with stirring. The reaction product was poured into a large amount of acetone, dehydrated and pulverized to obtain a hydrochloride of a partial hydrolyzate of poly (N-vinylformamide) as white powder. The yield was 100.2%, and the hydrolysis rate determined by colloid titration was 84 mol%. (3) Benzylation 5.0 g of the hydrochloride of the partial hydrolyzate of poly (N-vinylformamide) obtained in (2) above was placed in a separable flask equipped with a stirrer and a condenser, and 200 ml of water was added. Add a uniform solution to the solution, and add 15 wt% sodium hydroxide aqueous solution 25 ml.
Then, the temperature was raised to 50 ° C. and a predetermined amount of benzyl chloride was added to obtain 4 kinds of polymers A, B, C and D. Polymer type Amount of benzyl chloride A 0.41 g B 0.81 g C 2.0 g D 3.0 g After completion of the reaction, the product was purified with acetone and powdered in the same manner as in the above (1) and (2). The benzylation ratios of the obtained polymers A to D were measured by proton NMR, and were measured from the area ratio of the signal of the proton of the benzene ring at around 8 ppm and the signal of the proton of the main chain methylene at around 2 ppm. Table 1 shows the physical properties of the polymers A to D obtained in Production Example 1 and the other test polymers E, F and G.

【0008】[0008]

【表1】 [Table 1]

【0009】1)pH3でのコロイド当量値。 2)0.1N−NaCl水溶液を溶媒とする30℃での
固有粘度、ただし( )内は1N−NaCl水溶液を溶
媒とする30℃での固有粘度。 3)ジメチルアミノエチルメタクリレートの塩化メチル
四級化物ホモポリマー。 4)ジメチルアミノエチルアクリレートの塩化メチル四
級化物/アクリルアミドコポリマー。 実施例1〜3、比較例1〜4 汚泥として、下水混合生汚泥(pH6.1、SS1.36
%、VSS/SS78.7%、繊維分/SS18.6%、
電導度1420μs/cm)を用い、以下に示す方法によ
り評価した。汚泥200mlを300mlポリビーカーに採
り、0.2重量%濃度に調製したポリマー溶液を、シリ
ンジを用いて所定量汚泥に加え、タービン羽根を備えた
撹拌機で250rpm、30秒間撹拌を行った。その際の
フロック径を測定したのち、ナイロンろ布を敷いたヌッ
チェロートに、内径50mmのポリ塩化ビニルの円筒をお
き、その中へ凝集した汚泥を注ぎ込み、メスシリンダー
を用いて10秒後のろ液量を測定した。次に、ろ布上に
残った凝集汚泥をベルトプレス用のポリエステルろ布に
一定量とり、1.0kg/cm2で1分間圧搾したのち、ろ布
上のケーキをヘラでかき取り、含水率を測定した。ろ布
に付着した汚泥は高圧水で洗い落とし、固形物量を測定
することにより、ろ布剥離性を評価した。これらの結果
を第2表に示す。
1) Colloid equivalent value at pH 3. 2) Intrinsic viscosity at 30 ° C. using 0.1N-NaCl aqueous solution as a solvent, however, () shows intrinsic viscosity at 30 ° C. using 1N-NaCl aqueous solution as a solvent. 3) A methyl chloride quaternary homopolymer of dimethylaminoethyl methacrylate. 4) Methyl chloride quaternary / acrylamide copolymer of dimethylaminoethyl acrylate. Examples 1 to 3 and Comparative Examples 1 to 4 As sludge, sewage mixed raw sludge (pH 6.1, SS1.36)
%, VSS / SS78.7%, fiber content / SS18.6%,
The conductivity was 1420 μs / cm), and the evaluation was performed by the following method. 200 ml of sludge was placed in a 300 ml polybeaker, a predetermined amount of the polymer solution prepared to have a concentration of 0.2% by weight was added to the sludge by a predetermined amount using a syringe, and the mixture was stirred at 250 rpm for 30 seconds with a stirrer equipped with a turbine blade. After measuring the floc diameter at that time, place a polyvinyl chloride cylinder with an inner diameter of 50 mm on a Nutcheroth covered with a nylon filter cloth, pour the agglomerated sludge into it, and use a graduated cylinder to filter it after 10 seconds. The liquid volume was measured. Next, a certain amount of the coagulated sludge remaining on the filter cloth was put on a polyester filter cloth for belt press and squeezed at 1.0 kg / cm 2 for 1 minute, and the cake on the filter cloth was scraped off with a spatula to obtain a water content. Was measured. The sludge adhering to the filter cloth was washed off with high-pressure water, and the amount of solid matter was measured to evaluate the filter cloth releasability. The results are shown in Table 2.

【0010】[0010]

【表2】 [Table 2]

【0011】実施例4〜6、比較例5〜8 汚泥として、し尿余剰汚泥と三次処理汚泥との混合汚泥
(pH7.0、SS2.3%、VSS/SS72.7%、繊
維分/SS3.4%、電導度2160μs/cm)を用
い、前記下水混合生汚泥の場合と同様にして評価した。
その結果を第3表に示す。
Examples 4 to 6 and Comparative Examples 5 to 8 As sludge, a mixed sludge (pH 7.0, SS 2.3%, VSS / SS 72.7%, fiber content / SS 3.) of human waste surplus sludge and tertiary treated sludge was used. 4%, conductivity 2160 μs / cm) was used and evaluated in the same manner as in the case of the sewage mixed raw sludge.
The results are shown in Table 3.

【0012】[0012]

【表3】 [Table 3]

【0013】[0013]

【発明の効果】本発明の高分子凝集剤は、汚泥脱水処理
に用いた場合、凝集力に優れ、強度の高い凝集フロック
を与え、機械脱水により含水率が低く、かつ剥離性の良
い脱水ケーキが得られ、安定した汚泥の脱水処理が可能
である。
Industrial Applicability The polymer flocculant of the present invention, when used for sludge dewatering treatment, gives a flocculating floc having excellent cohesive force and high strength, a low water content by mechanical dewatering, and a good delaminating cake. Is obtained, and stable dehydration treatment of sludge is possible.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】構成単量体単位として、式 【化1】 で表されるベンジル化ビニルアミン単位2〜30モル%
を含有するポリマーから成る高分子凝集剤。
1. A constitutional monomer unit as a constituent monomer unit: 2-30 mol% of benzylated vinylamine unit represented by
A polymer flocculant comprising a polymer containing
【請求項2】ポリマーが、N−ビニルホルムアミドの単
独重合体又はN−ビニルホルムアミドと他のビニル系単
量体との共重合体の加水分解物をベンジル化したもので
ある請求項1記載の高分子凝集剤。
2. The polymer according to claim 1, wherein the hydrolyzate of a homopolymer of N-vinylformamide or a copolymer of N-vinylformamide and another vinyl monomer is benzylated. Polymer flocculant.
JP15682394A 1994-06-15 1994-06-15 Polymer flocculant Expired - Lifetime JP3478871B2 (en)

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JP15682394A JP3478871B2 (en) 1994-06-15 1994-06-15 Polymer flocculant

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JPH07328323A true JPH07328323A (en) 1995-12-19
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008533224A (en) * 2005-03-11 2008-08-21 アトーテヒ ドイッチュラント ゲゼルシャフト ミット ベシュレンクテル ハフツング Polyvinylammonium compound, method for producing polyvinylammonium compound, acidic solution containing polyvinylammonium compound and method for electrolytically depositing copper plating
JP2011131166A (en) * 2009-12-24 2011-07-07 Daiyanitorikkusu Kk Method for flocculating waste water
JP2011131164A (en) * 2009-12-24 2011-07-07 Daiyanitorikkusu Kk Method for treating oil-containing waste water

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58137500A (en) * 1982-02-12 1983-08-15 Hitachi Plant Eng & Constr Co Ltd Assistant for dehydrating sludge
JPH04293600A (en) * 1991-03-20 1992-10-19 Kurita Water Ind Ltd Dehydration of sludge
JPH04298300A (en) * 1991-03-27 1992-10-22 Kurita Water Ind Ltd Sludge dehydrating agent and method for dehydrating sludge by using this agent
JPH04300700A (en) * 1991-03-28 1992-10-23 Kurita Water Ind Ltd Sludge dehydrating agent

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58137500A (en) * 1982-02-12 1983-08-15 Hitachi Plant Eng & Constr Co Ltd Assistant for dehydrating sludge
JPH04293600A (en) * 1991-03-20 1992-10-19 Kurita Water Ind Ltd Dehydration of sludge
JPH04298300A (en) * 1991-03-27 1992-10-22 Kurita Water Ind Ltd Sludge dehydrating agent and method for dehydrating sludge by using this agent
JPH04300700A (en) * 1991-03-28 1992-10-23 Kurita Water Ind Ltd Sludge dehydrating agent

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008533224A (en) * 2005-03-11 2008-08-21 アトーテヒ ドイッチュラント ゲゼルシャフト ミット ベシュレンクテル ハフツング Polyvinylammonium compound, method for producing polyvinylammonium compound, acidic solution containing polyvinylammonium compound and method for electrolytically depositing copper plating
KR101242879B1 (en) * 2005-03-11 2013-03-13 아토테크더치랜드게엠베하 Polyvinylammonium compound, method of manufacturing same, acidic solution containing said compound and method of electrolytically depositing a copper deposit
EP1856167B1 (en) * 2005-03-11 2015-05-06 Atotech Deutschland GmbH Acidic solution containing a polyvinylammonium compound and method of electrolytically depositing a copper deposit
JP2011131166A (en) * 2009-12-24 2011-07-07 Daiyanitorikkusu Kk Method for flocculating waste water
JP2011131164A (en) * 2009-12-24 2011-07-07 Daiyanitorikkusu Kk Method for treating oil-containing waste water

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