JP2000140509A - Novel flocculant and sludge treatment using the same - Google Patents

Novel flocculant and sludge treatment using the same

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Publication number
JP2000140509A
JP2000140509A JP10324780A JP32478098A JP2000140509A JP 2000140509 A JP2000140509 A JP 2000140509A JP 10324780 A JP10324780 A JP 10324780A JP 32478098 A JP32478098 A JP 32478098A JP 2000140509 A JP2000140509 A JP 2000140509A
Authority
JP
Japan
Prior art keywords
chitin
chitosan
flocculant
sludge
produced
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.)
Withdrawn
Application number
JP10324780A
Other languages
Japanese (ja)
Inventor
Koreatsu Ito
維厚 伊藤
Arinori Fukita
有紀 吹田
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.)
Kansai Kako Co Ltd
Original Assignee
Kansai Kako 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 Kansai Kako Co Ltd filed Critical Kansai Kako Co Ltd
Priority to JP10324780A priority Critical patent/JP2000140509A/en
Publication of JP2000140509A publication Critical patent/JP2000140509A/en
Withdrawn legal-status Critical Current

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  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Treatment Of Sludge (AREA)

Abstract

PROBLEM TO BE SOLVED: To obtain a novel flocculant safe to animals and plants and not bringing about environmental pollution without using an acrylamide polymer generating an aluminum salt or a carcinogenic substance being a cause substance of Alzheimer's desease as a flocculant in the sludge treatment of urban sewage/ factory waste water, and a sludge treatment method using the same. SOLUTION: Safety and environment purifying properties are ensured by selecting a substance produced by an organism as a flucculant added at a time of sludge treatment. That is, a flocculant to be used is constituted of a microbiologically produced flocculant and chitin/chitosan obtained from a shell of a crab or a lobster. Especially, a flocculation active substance based on glycoprotein produced by Gram-positive bacteria containing Rhodococcus erythropolis or a flocculation active substance based on acidic polysaccharide produced by a strain of the genus Aureobasidium is used as the microbiologically produced flocculant. Further, as the chitin/chitosan, a chitin/ chitosan obtained by deacetylating 80% or more of chitin is used.

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、都市下水、農業集
落排水、畜産排水、工場排水等から発生する汚泥や土木
・建築汚泥等を凝集沈殿させる凝集剤に関し、更に詳細
には、微生物産生凝集剤とバイオマス資源から得られた
キチン・キトサンを凝集剤として使用して、動植物に対
して安全でしかも環境汚染を生じない凝集沈殿効率の高
い凝集剤およびそれを用いる汚泥処理方法に関する。
The present invention relates to a coagulant for coagulating and sedimenting sludge generated from municipal sewage, agricultural settlement drainage, livestock drainage, factory drainage, etc., civil engineering / building sludge, etc. More particularly, the present invention relates to a coagulant produced by microorganisms. The present invention relates to a flocculant which uses chitin and chitosan obtained from a biomass resource as a flocculant and which is safe for animals and plants and has high flocculation and sedimentation efficiency without causing environmental pollution, and a sludge treatment method using the flocculant.

【0002】[0002]

【従来の技術】一般に、有機物を含む各種排水の処理方
法としては、大方において活性汚泥法が採用されてい
る。この活性汚泥法は効率の高い排水処理方法であり、
良質の処理水が経済的に得られる特徴を持っているの
で、もっとも広く普及している。
2. Description of the Related Art In general, an activated sludge method is generally used as a method for treating various kinds of wastewater containing organic matter. This activated sludge method is a highly efficient wastewater treatment method,
It is the most widely used because of the economical characteristics of high quality treated water.

【0003】この活性汚泥法で処理した後の余剰汚泥や
土木・建築汚泥を凝集・沈殿・濾過・脱水しなければな
らないが、これに当たり、浮遊汚泥に後述の凝集剤を添
加攪拌して凝集を起こさせ、これを常法により濾過分離
して、清澄な処理水と含水汚泥ケーキに分離している。
清澄な処理水は滅菌後放流されるが、含水汚泥ケーキは
埋め立てなどの方法で自然環境にリターンされるのが常
法である。
[0003] Excess sludge and civil engineering / building sludge after treatment by this activated sludge method must be coagulated, settled, filtered and dewatered. In this case, a flocculant described later is added to the suspended sludge to stir the coagulation. This is separated by filtration by a conventional method to separate clear treated water and a hydrated sludge cake.
Clear treated water is discharged after sterilization, but it is customary to return the hydrous sludge cake to the natural environment by landfilling.

【0004】例えば、下水処理の一連の工程で説明する
と、まず流入下水から砂などを沈砂除去した後、最初沈
殿池で懸濁物質を沈殿分離し、次の生物酸化処理工程で
活性汚泥法や生物膜処理法により有機物を酸化分解し、
最後に最終沈殿池で残留浮遊している懸濁物質を沈殿除
去して清澄水を最終処理水として放流している。そし
て、分離された含水汚泥の容積および重量の減少化を図
るために、凝集剤が使用されている。このように水分を
極力少なくした含水汚泥ケーキを埋め立て処分してい
る。
[0004] For example, a series of processes of sewage treatment will be described. First, sand and the like are removed from inflowing sewage by sedimentation, and suspended substances are first settled and separated in a sedimentation basin. Oxidative decomposition of organic matter by biofilm treatment method,
Finally, the suspended solids remaining in the final sedimentation basin are removed by settling and the clear water is discharged as final treated water. In order to reduce the volume and weight of the separated hydrous sludge, a flocculant is used. The hydrated sludge cake whose water content is reduced as much as possible is landfilled.

【0005】この凝集処理工程では、無機系凝集剤や合
成高分子系凝集剤が大量に使用されてきた。無機系凝集
剤には、硫酸バンド、ポリ塩化アルミニウム等のアルミ
ニウム塩や、塩化第2鉄、硫酸第2鉄、ポリ硫酸第2鉄
(通称、ポリ鉄)等の鉄塩からなる水溶性の多価金属塩
が多く使用されている。合成高分子系凝集剤には、ポリ
ジメチルアミノエチルアクリレート等のカチオン系合成
高分子や、ポリアクリルアミド、その加水分解物、ポリ
アクリル酸等のアニオン系合成高分子、その他のノニオ
ン系合成高分子が好んで使用されてきた。
In this coagulation treatment step, a large amount of an inorganic coagulant or a synthetic polymer coagulant has been used. Inorganic coagulants include aluminum salts such as sulfuric acid bands and polyaluminum chloride, and water-soluble polysulfates such as iron salts such as ferric chloride, ferric sulfate, and ferric polysulfate (commonly referred to as polyiron). Valent metal salts are often used. Synthetic polymer-based flocculants include cationic synthetic polymers such as polydimethylaminoethyl acrylate, anionic synthetic polymers such as polyacrylamide, hydrolysates thereof, and polyacrylic acid, and other nonionic synthetic polymers. It has been used favorably.

【0006】これらの凝集剤により分離された汚泥は、
埋め立てにより建設用造成地や農地等として活用され
る。しかし、特に農地として活用された場合には重大な
安全性阻害や環境汚染の問題が生じる。第1に無機系凝
集剤では、多価金属塩であるため含水汚泥ケーキの重量
を重くするだけでなく、土壌中に多価金属イオンを持ち
込むため植物の生育に不適切な土壌に改質してしまう。
その中でもアルミニウムイオンはアルツハイマー病の原
因物質とも云われており、農産物を介して人間に蓄積す
る危険性を有している。第2に合成高分子凝集剤では、
その生分解性が悪いために土壌に蓄積され、植物の生育
を阻害する要因となる。特に、ポリアクリルアミドのモ
ノマーであるアクリルアミドは発ガン性と神経毒性を有
しているため、アクリルアミドモノマーの残留が大きく
危惧されている。
[0006] The sludge separated by these flocculants is
Reclaimed land is used as land for construction and agricultural land. However, when used as agricultural land, serious safety problems and environmental pollution problems arise. First, the inorganic coagulant not only increases the weight of the hydrated sludge cake because it is a polyvalent metal salt, but also introduces polyvalent metal ions into the soil to modify it into soil that is unsuitable for plant growth. Would.
Among them, aluminum ion is also said to be a causative substance of Alzheimer's disease, and has a risk of accumulating in humans through agricultural products. Second, in the case of a synthetic polymer flocculant,
Due to its poor biodegradability, it accumulates in soil and inhibits plant growth. In particular, since acrylamide, which is a monomer of polyacrylamide, has carcinogenicity and neurotoxicity, there is great concern that acrylamide monomer remains.

【0007】[0007]

【発明が解決しようとする課題】このような化学凝集剤
の有する欠点を打開するために開発されてきたのが、近
年のバイオテクノロジーを利用した微生物産生凝集剤で
ある。例えば、特開平8−256782号公報には、ロ
ードコッカス・エリスロポリス(Rhodococus ery-throp
olis)KR―S−1株(FERM BP−4913)の
発酵法による増殖方法が記載されている。この増殖過程
で菌体外の培地中に微生物産生凝集剤が排出産生される
のである。日本化学会誌1992年第5号によれば、ロ
ードコッカスが産生する微生物産生凝集剤はNOC−1
として報告されており、生化学的分析から糖蛋白質であ
ることが明らかにされた。
In order to overcome the drawbacks of such a chemical flocculant, a microbial flocculant produced by utilizing recent biotechnology has been developed. For example, Japanese Patent Application Laid-Open No. 8-256787 discloses Rhodococus erythropolis.
olis) KR-S-1 strain (FERM BP-4913) is described. During this growth process, the microorganism-producing coagulant is excreted and produced in the extracellular medium. According to the Chemical Society of Japan, No. 5, 1992, the microbial coagulant produced by Rhodococcus is NOC-1.
And biochemical analysis revealed that it was a glycoprotein.

【0008】これらの公報および報告書には、NOC−
1は生分解性に優れた安全性の高い物質で、二次公害の
おそれがない凝集剤と記載されている。しかも無機汚泥
から有機汚泥に亘る広範囲の浮遊汚泥に対し強力な凝集
作用を有すると報告されている。そこで、本発明者はこ
のNOC−1を実際の農業集落排水の凝集沈殿に適用し
てみたところ、NOC−1単独ではほとんど凝集活性を
示さないことを確認するに至った。しかも、このNOC
−1は使用すべきではないカルシウム等の無機系凝集剤
(Ca2+、Mg2+、Fe2+、Al3+等を多価イ
オンとする)を同時使用して初めて凝集効果を示すとい
うことが分かった。また、NOC−1は、単独で凝集効
果を発揮できるのはカオリンなどの無機汚泥に限定さ
れ、広い範囲の有機汚泥に対しては単独での凝集効果は
小さいことが分かった。
[0008] These publications and reports contain NOC-
No. 1 is a highly safe substance excellent in biodegradability and described as a flocculant having no risk of secondary pollution. In addition, it is reported that it has a strong flocculating effect on a wide range of suspended sludge ranging from inorganic sludge to organic sludge. Thus, the present inventor has applied this NOC-1 to actual coagulation sedimentation of agricultural settlement drainage, and has found that NOC-1 alone shows almost no coagulation activity. And this NOC
It was found that -1 exhibited an aggregating effect only when an inorganic aggregating agent such as calcium (Ca2 +, Mg2 +, Fe2 +, Al3 +, etc. was used as a polyvalent ion) which should not be used was used at the same time. In addition, it was found that NOC-1 alone can exert the coagulation effect only on inorganic sludge such as kaolin, and the coagulation effect by itself is small for a wide range of organic sludge.

【0009】他方、特開平8−81501号公報には、
オーレオバシジウム(Aureobasidium )属に属する菌株
(FERM P−14228)が産生する酸性多糖につ
いて報告されている。この酸性多糖は凝集活性を有し、
毒性を有しない廃水処理剤と記載されているから、微生
物産生凝集剤の一種であることが分かる。しかもこの酸
性多糖は後述するように商品名アミーして市販されてお
り、実用化された微生物産生凝集剤がほとんど見あたら
ない中で、実用化されている希な例である。
On the other hand, Japanese Patent Application Laid-Open No. Hei 8-81501 discloses that
An acidic polysaccharide produced by a strain belonging to the genus Aureobasidium (FERM P-14228) has been reported. This acidic polysaccharide has aggregating activity,
Since it is described as a non-toxic wastewater treatment agent, it can be understood that it is a kind of microbial coagulant. In addition, this acidic polysaccharide is commercially available under the trade name Amy as described below, and is a rare example that has been put to practical use while practically no microorganism-producing coagulant has been found.

【0010】本発明者等はこのアミーの凝集効果を確認
するために、上述した農業集落排水の凝集沈殿に適用し
てみたところ、アミー単独では凝集活性がないことが判
明した。また、このアミーもポリ鉄などの無機系凝集剤
を同時使用して初めて凝集効果を示すことも分かった。
従って、この酸性多糖も前記ロードコッカス・エリスロ
ポリスの糖蛋白質と同様の性格を有している。
[0010] The present inventors applied the above-mentioned coagulation and sedimentation of agricultural settlement drainage to confirm the coagulation effect of Amy and found that Amy alone did not have coagulation activity. In addition, it was also found that this Amy exhibited the coagulation effect only when an inorganic coagulant such as polyiron was used simultaneously.
Therefore, this acidic polysaccharide also has the same properties as the glycoprotein of Rhodococcus erythropolis.

【0011】また、特開昭59−160509号公報に
は、キチン・キトサンが汚泥脱水用の凝集剤として機能
することが述べられている。その脱アセチル化率が67
〜75モル%のときに凝集効果が格段によくなると記載
されている。ところが、本発明者等の試験によれば、こ
のキチン・キトサンの凝集性能も単独では小さく、実用
に耐えないことが判明した。
Japanese Patent Application Laid-Open No. 59-160509 discloses that chitin / chitosan functions as a flocculant for dewatering sludge. Its deacetylation rate is 67
It is described that the coagulation effect is remarkably improved when the content is ~ 75 mol%. However, according to a test conducted by the present inventors, it has been found that the aggregation performance of chitin / chitosan alone is small and cannot be put to practical use.

【0012】[0012]

【課題を解決するための手段】本発明は上記欠点を解消
するためになされたものであり、本発明に係る新規な凝
集剤は、微生物産生凝集剤とキチン・キトサンを併用し
た点に特徴を有する。また、前記微生物産生凝集剤とし
てロードコッカス・エリスロポリスを含むグラム陽性菌
が産生する糖蛋白質を主成分とする凝集活性物質または
オーレオバシジウム属の菌株が産生する酸性多糖を主成
分とする凝集活性物質を用い、前記キチン・キトサンと
してキチン質を80%以上に脱アセチル化して得られた
キチン・キトサンを用いる凝集剤を提案する。
DISCLOSURE OF THE INVENTION The present invention has been made to solve the above-mentioned disadvantages, and a novel flocculant according to the present invention is characterized in that a microorganism-producing flocculant is used in combination with chitin / chitosan. Have. In addition, an agglutinating active substance mainly composed of a glycoprotein produced by Gram-positive bacteria including Rhodococcus erythropolis as the microorganism-producing flocculant or an agglutinating activity mainly composed of an acidic polysaccharide produced by a strain of Aureobasidium. A coagulant using chitin / chitosan obtained by deacetylating chitin to 80% or more as the chitin / chitosan using the substance is proposed.

【0013】更に、微生物産生凝集剤とキチン・キトサ
ンの併用重量比を1:9〜5:5とした凝集剤を提案す
る。前記した各凝集剤を、被処理水に添加して汚泥を凝
集沈殿させるか、又は含水汚泥に添加して汚泥を脱水す
る汚泥処理方法を提案する。
Further, the present invention proposes a flocculant wherein the combined weight ratio of the microorganism-produced flocculant and chitin / chitosan is 1: 9 to 5: 5. The present invention proposes a sludge treatment method in which each of the above-mentioned coagulants is added to the water to be treated to cause coagulation and sedimentation of the sludge, or is added to hydrous sludge to dewater the sludge.

【0014】[0014]

【発明の実施の形態】本発明者等は、従来の微生物産生
凝集剤が単独で有機汚泥を凝集させる効果は小さいもの
の、多価金属カチオンを生じる無機系凝集剤を添加した
場合には、有機汚泥に対して強力な凝集作用を発現する
ことに着目した。即ち、微生物産生凝集剤には他のカチ
オン系凝集剤との相乗効果によって強力な凝集性能を発
揮する性質があると考えたのである。従って、本発明者
は前記無機系凝集剤と同様の作用効果を有する他の安全
な凝集剤を発見するために鋭意研究した結果、カチオン
官能基を有するキチン・キトサンを発見するに至った。
BEST MODE FOR CARRYING OUT THE INVENTION The present inventors have found that, although the conventional microorganism-producing coagulant has a small effect of coagulating organic sludge by itself, when an inorganic coagulant that generates polyvalent metal cations is added, an organic coagulant is used. We focused on the fact that it exerts a strong coagulation action on sludge. That is, it was considered that the microorganism-produced flocculant had a property of exhibiting a strong flocculating performance by a synergistic effect with other cationic flocculants. Accordingly, the present inventors have conducted intensive studies to find another safe flocculant having the same action and effect as the inorganic flocculant, and as a result, have found chitin / chitosan having a cationic functional group.

【0015】このキチン・キトサンを微生物産生凝集剤
と共に被処理水に同時に添加した場合でも、逐次に添加
した場合でも汚泥に対し強力な凝集効果を発揮する。逐
次添加とは、微生物産生凝集剤を添加した後にキチン・
キトサンを添加する場合、又はキチン・キトサンを先に
添加して微生物産生凝集剤を後から添加する場合の両者
を包含している。
[0015] Even when this chitin / chitosan is added simultaneously with the microorganism-producing coagulant to the water to be treated, or when it is added sequentially, a strong coagulation effect is exerted on sludge. Sequential addition means that after adding the microorganism-producing coagulant,
Both the case where chitosan is added and the case where chitin / chitosan is added first and the microorganism-producing coagulant is added later are included.

【0016】キチン質とは、カニ・エビ等の甲殻類や昆
虫の外殻・細胞壁の主要成分で、カルシウムや蛋白質と
の複合体を構成している。地球上で生物生成されるバイ
オマス資源としては、セルロースに次いで第2の分量を
占める。このキチン質からカルシウムおよび蛋白質を除
去したものをキチンと呼び、このキチンを脱アセチル化
したものをキトサンと云い、キチンとキトサンは共に天
然高分子である。しかし、キチンを100%脱アセチル
化することは困難で、キトサンと称する物質でもキチン
とキトサンが所定率で複合している。このような複合物
質を本発明ではキチン・キトサンと呼ぶ。
Chitin is a major component of shells and cell walls of crustaceans such as crabs and shrimps and insects, and forms a complex with calcium and proteins. As a biomass resource that is bio-generated on earth, it accounts for the second amount after cellulose. A substance obtained by removing calcium and protein from the chitin is called chitin, and a substance obtained by deacetylating the chitin is called chitosan. Both chitin and chitosan are natural polymers. However, it is difficult to deacetylate chitin by 100%, and even with a substance called chitosan, chitin and chitosan are complexed at a predetermined ratio. In the present invention, such a composite substance is called chitin / chitosan.

【0017】学名では、キチンはβ―(1→4)―2―
アセトアミドー2―デオキシーβ―D―グルコースであ
り、キトサンはβ―(1→4)―2―アミノー2―デオ
キシーβ―D―グルコースである。キチン・キトサンは
この2種の構造が共存した分子構造を有する。
In the scientific name, chitin is β- (1 → 4) -2-
Acetamide-2-deoxy-β-D-glucose, and chitosan is β- (1 → 4) -2-amino-2-deoxy-β-D-glucose. Chitin / chitosan has a molecular structure in which these two types coexist.

【0018】本発明で使用するキチン・キトサンとして
は甲陽ケミカル株式会社が販売する粉体の商品名コーヨ
ーキトサンが用いられる。このキチン・キトサンは天然
バイオマス資源から製造された物質であるから、人や動
物への安全性は極めて高い。また、微生物に対する変異
原性は勿論なく、逆に強い抗変異原性があることが報告
されている。
As the chitin / chitosan used in the present invention, Koyo Chitosan, a trade name of a powder sold by Koyo Chemical Co., Ltd., is used. Since chitin / chitosan is a substance produced from natural biomass resources, its safety for humans and animals is extremely high. In addition, it is reported that, of course, it has not only mutagenicity against microorganisms but also strong antimutagenicity.

【0019】前述したように、特開昭59−16050
9号公報には、キチン・キトサンは汚泥脱水用の凝集剤
として機能することが述べられている。しかし、本発明
者等の試験により、単独使用では凝集性能が小さいこと
が判明した。このような単独凝集性能の小さなキチン・
キトサンを同様な性格の微生物産生凝集剤と併用したと
きに、何故強力な凝集性能が発現するのかについては、
いまだに実証的な解明は進んでいない。しかし、本発明
者等は現在、キチン・キトサンがカチオン官能基を有す
る点から、このカチオン官能基が微生物産生凝集剤に対
し多価金属カチオンと同様の凝集促進効果を発現するの
ではないかと考えている。いずれにしても、本発明者ら
が発見したキチン・キトサンと微生物産生凝集剤との相
乗効果により、安全で強力な凝集剤を完成するに至っ
た。
As described above, Japanese Patent Application Laid-Open No. 59-16050
No. 9 describes that chitin / chitosan functions as a flocculant for sludge dewatering. However, tests by the present inventors have revealed that the cohesion performance is small when used alone. Chitin with such small coagulation performance
The reason why strong coagulation performance is exhibited when chitosan is used in combination with a microorganism-producing coagulant of a similar character, is as follows.
Empirical elucidation has not progressed yet. However, the present inventors now believe that chitin / chitosan has a cationic functional group, and that this cationic functional group may exert the same aggregation promoting effect on microbial aggregating agents as polyvalent metal cations. ing. In any case, the synergistic effect of the chitin / chitosan and the microbial coagulant discovered by the present inventors has led to the completion of a safe and powerful coagulant.

【0020】また、微生物産生凝集剤と併用した場合に
凝集効果を効率的に発揮させるには、キチン・キトサン
の脱アセチル化率は80%以上が好適であることが明ら
かとなった。この点は、前述した67〜75%とは重な
っておらず、本発明者によって初めて発見されたことで
ある。従って、前記コーヨーキトサンの中で、品名とし
てSK−10(85%以上)、SK−50(80%以
上)、SK−200(80%以上)、SK−400(8
0%以上)等が本発明に適用できる。括弧内は脱アセチ
ル化率を示す。
In addition, it has been found that a deacetylation ratio of chitin / chitosan is preferably 80% or more in order to efficiently exert the flocculating effect when used in combination with a microbial flocculant. This point does not overlap with the above-mentioned 67 to 75%, and is the first discovery by the present inventors. Therefore, among the KOYO chitosans, SK-10 (85% or more), SK-50 (80% or more), SK-200 (80% or more), SK-400 (8
0% or more) can be applied to the present invention. The figures in parentheses indicate the deacetylation rate.

【0021】本発明の一成分である微生物産生凝集剤と
しては、公知の微生物産生凝集剤が利用できる。この微
生物産生凝集剤は微生物産生菌が増殖過程で菌体外また
は菌体内に産生するものである。菌体外とは培地中に産
生することであり、例えば液体培地、即ち培養液であれ
ばその液体自体が凝集剤溶液となる。菌体内に産生され
る場合には、菌体から培地に凝集剤を放出させることが
必要になる。例えば、菌体を破裂させたり、特定の薬剤
で菌体外へ溶出させたりする等の手段をとる。培養液か
ら菌体を凝集分離させてもよいし、菌体を薬剤で死滅化
処理してもよい。菌体に毒性がない場合にはそのまま培
養液中に残存させる場合もある。
As the microorganism-producing coagulant which is one component of the present invention, a known microorganism-producing coagulant can be used. The microorganism-producing coagulant is produced by a microorganism-producing bacterium extracellularly or intracellularly during the growth process. The term "extracellular" refers to production in a medium. For example, in the case of a liquid medium, that is, a culture solution, the liquid itself becomes a flocculant solution. When produced in cells, it is necessary to release the flocculant from the cells into the medium. For example, a means such as rupture of the cells or elution of the cells with a specific agent is used. The cells may be aggregated and separated from the culture solution, or the cells may be killed with a drug. If the cells are not toxic, they may remain in the culture solution as they are.

【0022】凝集剤を産生するグラム陽性菌としては、
ロードコッカス・エリスロポリス、ノカルディア・レス
トゥリクタ、ノカルディア・カルカレア、ノカルディア
・ロードニイ、コリネバクテリウム属、オーレオバクテ
リウム属、オエルスコビア属などが利用できる。またグ
ラム陰性菌としては、アルカリゲネス・ラトゥス、アル
カリゲネス・クピドゥス、シュードモナス属、アシネト
バクター属、エンテロバクター属などが利用できる。
[0022] Gram-positive bacteria that produce flocculants include:
Rhodococcus erythropolis, Nocardia restricta, Nocardia calcarea, Nocardia rhodny, Corynebacterium, Aureobacterium, Oerskovia and the like can be used. Examples of gram-negative bacteria include Alcaligenes ratus, Alcaligenes cupidus, Pseudomonas, Acinetobacter, Enterobacter and the like.

【0023】特に本発明で活用できるグラム陽性菌は、
ロードコッカス・エリスロポリスKR−S−1株(FE
RM BP−4913)、オーレオバクテリウムKYM
−6株(FERM P−11357)、オエルスコビア
KYM−7株(FERM P−11358)等である。
括弧内は工業技術院生命工学工業技術研究所への寄託番
号であり、所定条件の下に菌株を入手することができ
る。ロードコッカス・エリスロポリスに代表されるよう
に、グラム陽性菌のいくつかは微生物産生凝集剤として
糖蛋白質を産生する。特に、ロードコッカス・エリスロ
ポリスはNOC−1と名付けられた糖蛋白質を産生し、
このNOC−1を微生物産生凝集剤として後述の実施例
で使用する。
In particular, Gram-positive bacteria that can be used in the present invention include:
Rhodococcus erythropolis KR-S-1 strain (FE
RM BP-4913), Aureobacterium KYM
-6 strain (FERM P-11357), Oerskovia KYM-7 strain (FERM P-11358) and the like.
The numbers in parentheses are the deposit numbers with the National Institute of Bioscience and Human-Technology, National Institute of Advanced Industrial Science and Technology, and strains can be obtained under predetermined conditions. As represented by Rhodococcus erythropolis, some gram-positive bacteria produce glycoproteins as microbial aggregating agents. In particular, Rhodococcus erythropolis produces a glycoprotein named NOC-1,
This NOC-1 is used as a microorganism-producing coagulant in Examples described later.

【0024】これらの微生物産生凝集剤は商品としては
未だに市場に流通していない。そこで、本発明者は各種
の菌株を入手し、液体培地または固体培地にて所定条件
で培養し、微生物産生凝集剤を培地中に生産した。微生
物の培養方法は各種の微生物に共通している側面が強
い。例えばNOC−1を生産するために、ロードコッカ
ス・エリスロポリスKR―S−1株の培養方法を述べる
と、液体培地に種菌を接種して30℃で2〜4日間振と
う培養する。この培養液中に前記NOC−1が蓄積され
る。
These microorganism-producing coagulants have not yet been marketed as commercial products. Then, the inventor obtained various strains, cultured them in a liquid medium or solid medium under predetermined conditions, and produced a microorganism-producing flocculant in the medium. Microbial culture methods have a strong aspect common to various microorganisms. For example, in order to produce NOC-1, a method of culturing Rhodococcus erythropolis KR-S-1 is described. A liquid medium is inoculated with a seed bacterium and cultured at 30 ° C. with shaking for 2 to 4 days. The NOC-1 is accumulated in the culture solution.

【0025】ロードコッカス・エリスロポリスKR―S
−1株は菌体外、即ち培養液中にNOC−1を排出しな
がら生産するから、培養液自体を微生物産生凝集剤とし
て使用することができる。
Lord Coccus erythropolis KR-S
Since the -1 strain is produced extracellularly, that is, while excreting NOC-1 in the culture solution, the culture solution itself can be used as a microorganism-producing flocculant.

【0026】その他の微生物産生菌として、前述したオ
ーレオバシジウム属の菌株(FERM P−1422
8)が利用でき、その産生する凝集剤は酸性多糖であ
る。微生物産生凝集剤が商品化される例は極めて希れで
あるが、この酸性多糖は商品名アミーとして株式会社ソ
フィから販売されている。アミーの性状は酸性多糖培養
液で、精製しない培養液自体が商品として販売されてい
る。従って、本発明で使用する場合には、培養液自体
か、又はそれを希釈して使用する。
As another microorganism-producing bacterium, the aforementioned strain of the genus Aureobasidium (FERM P-1422) is used.
8) is available and the coagulant produced is an acidic polysaccharide. It is extremely rare that a microorganism-producing coagulant is commercialized, but this acidic polysaccharide is sold by Sophie Co., Ltd. under the trade name Amy. Amy is an acidic polysaccharide culture, and the unpurified culture itself is sold as a commercial product. Therefore, when used in the present invention, the culture solution itself or a diluted solution thereof is used.

【0027】本発明において、微生物産生凝集剤/キチ
ン・キトサンの分数比で表される併用重量比は1/9〜
5/5の範囲にあることが望ましい。この範囲内では高
い凝集効果が得られる。また、微生物産生凝集剤とキチ
ン・キトサンを同時に凝集・脱水対象である被処理液・
含水汚泥に添加してもよいし、逐次に添加してもよい。
逐次添加では、微生物産生凝集剤を先に添加してもよい
し、キチン・キトサンを先に添加してもよく、添加順序
にかかわらず、両剤の相乗効果として凝集・脱水効果が
発揮できる。
In the present invention, the combined weight ratio represented by the fractional ratio of the microorganism-producing coagulant / chitin / chitosan is from 1/9 to
It is desirable to be in the range of 5/5. Within this range, a high aggregation effect can be obtained. In addition, the microbe-produced coagulant and chitin / chitosan are simultaneously coagulated and dehydrated.
It may be added to hydrous sludge or may be added sequentially.
In the sequential addition, the microorganism-producing coagulant may be added first, or chitin / chitosan may be added first, and the coagulation / dehydration effect can be exhibited as a synergistic effect of both agents regardless of the order of addition.

【0028】本発明に係る汚泥処理方法とは、対象とす
る被処理水から懸濁物質である浮遊汚泥を凝集沈殿させ
て固液分離を行ったり、また分離された含水率の高い汚
泥を脱水して含水率を低下させることである。被処理水
は極めて広範囲に亘り、都市下水、農業集落排水、畜産
排水、工場排水、土木・建築排水などがある。更に具体
的には、上水道・中水道の造水分野、発酵工業における
発酵液と培養菌体との分離、食品工業や土木浚渫工事で
の清澄処理など広範囲に亘る。また、脱水対象となる含
水汚泥には、生汚泥、余剰汚泥、消化汚泥やそれらの混
合汚泥などがあり、汚泥全般に対して本発明を適用でき
る。
The sludge treatment method according to the present invention means that the suspended sludge, which is a suspended substance, is coagulated and settled from the target water to be subjected to solid-liquid separation, and the separated sludge having a high water content is dewatered. To reduce the water content. The water to be treated covers a very wide area, including urban sewage, agricultural settlement drainage, livestock drainage, factory drainage, civil engineering and construction drainage. More specifically, it covers a wide range of fields, such as the water freshening field of water supply and middle water supply, the separation of fermented liquid and cultured cells in the fermentation industry, and the clarification treatment in the food industry and civil engineering dredging. The wet sludge to be dehydrated includes raw sludge, surplus sludge, digested sludge and mixed sludge thereof, and the present invention can be applied to sludge in general.

【0029】前記の汚泥処理液の具体例からも分かるよ
うに、本発明に云う汚泥は無機汚泥、有機汚泥、それら
の混合汚泥を含む。無機汚泥は無機物質からなる汚泥
で、例えば地上でできる泥水、金属や硫黄などの分散コ
ロイド、水酸化鉄などの会合コロイド等多種類からな
る。有機汚泥は有機物質からなる汚泥で、例えば下水中
の屎尿や食品汚泥、また発酵液中の培養菌体など広範囲
の有機物が含まれる。
As can be seen from the specific examples of the above-mentioned sludge treatment liquid, the sludge according to the present invention includes inorganic sludge, organic sludge, and mixed sludge thereof. Inorganic sludge is a sludge made of an inorganic substance, for example, muddy water formed on the ground, dispersed colloids of metals and sulfur, and associated colloids such as iron hydroxide. Organic sludge is a sludge made of organic substances, and includes a wide range of organic substances such as human waste and sewage in sewage, and cultured cells in fermentation liquor.

【0030】[0030]

【実施例】以下に、本発明に係る新規な凝集剤およびそ
れを用いる汚泥処理方法の実施例を説明する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of the novel flocculant according to the present invention and a sludge treatment method using the same will be described below.

【0031】[実施例1:酸性多糖アミーとキチン・キ
トサンの併用]この実施例では、原料汚泥として農業集
落排水を活性汚泥法で処理した後の余剰汚泥を用い、こ
の余剰汚泥が懸濁した被処理水を凝集沈殿させた。この
被処理水の性質として、被処理水1リットル中の固形分
量(mg)、即ちMLSSは17000mg/Lであ
り、そのPHは6.2であった。
Example 1 Combination of Acidic Polysaccharide Amy and Chitin / Chitosan In this example, surplus sludge obtained by treating agricultural settlement wastewater by the activated sludge method was used as raw material sludge, and the surplus sludge was suspended. The water to be treated was coagulated and precipitated. As the properties of the water to be treated, the solid content in 1 liter of the water to be treated (mg), that is, MLSS was 17000 mg / L, and its PH was 6.2.

【0032】微生物産生凝集剤は、株式会社ソフィーか
ら商品名アミーで販売されている凝集剤を用い、この凝
集剤は黒酵母の一種であるオーレオバシジウム属の菌株
(FERM P−14228)が培養液中に産生する酸
性多糖である。商品のアミーは濃度不明な培養液として
提供されるから、この培養液の入荷時の原液またはその
水による希釈液(以後、アミーと略称し、希釈度で区別
する)を本発明の微生物産生凝集剤として使用した。
As the microorganism-producing flocculant, a flocculant sold by Sophie Co. under the trade name Amy is used. This flocculant is cultured by a strain of the genus Aureobasidium (FERM P-14228), a kind of black yeast. It is an acidic polysaccharide produced in liquid. Since the Amy of the product is provided as a culture solution of unknown concentration, the stock solution at the time of receipt of this culture solution or a dilution of the same with water (hereinafter abbreviated as Amy and distinguished by the degree of dilution) is used for the production of microorganisms according to the present invention. Used as an agent.

【0033】キチン・キトサンとしては、甲陽ケミカル
株式会社が販売する商品名コーヨーキトサンの中から標
準的なSK−400を使用した。このSK−400は淡
黄白色の粉末で、脱アセチル化率が80%以上の高分子
キチン・キトサンである。このSK−400の0.5%
酢酸酸性水溶液を調製し、この0.5%水溶液またはそ
の水による希釈液(以後、キトサンと略称し、希釈度で
区別する)をキチン・キトサンとして使用した。
As the chitin / chitosan, standard SK-400 from Koyo Chitosan sold by Koyo Chemical Co., Ltd. was used. This SK-400 is a pale yellowish white powder and is a high molecular weight chitin / chitosan having a deacetylation ratio of 80% or more. 0.5% of this SK-400
An aqueous acetic acid solution was prepared, and this 0.5% aqueous solution or a diluted solution thereof with water (hereinafter, abbreviated as chitosan and distinguished by dilution) was used as chitin-chitosan.

【0034】凝集沈殿の実験方法は、図1に示すよう
に、500mLのガラスビーカー2(98mmφ×12
0mmh)に汚泥処理液4を300mL投入し、このと
き液深は60mmになる。このビーカー2にアミーとキ
トサンの所定量を同時に、または逐次にピペットで添加
した。表1でアミーとキトサンを2段並記してある場合
には同時添加を意味し、第1(段階)・第2(段階)と
記載の場合はその順に逐次添加したことを意味する。ア
ミーおよび/またはキトサンを添加した後、料理用の卵
の泡立て器を攪拌機6として人手でビーカー液中にほぼ
垂直に挿入し、所定時間だけ攪拌した。速度切り換えス
イッチと変圧器8を手動で調節して、急速攪拌では約1
00rpm、緩速攪拌では約60rpmとなるように調
節した。
As shown in FIG. 1, the experimental method of the coagulation and sedimentation was as follows: 500 mL glass beaker 2 (98 mmφ × 12 mm).
At 0 mmh), 300 mL of the sludge treatment liquid 4 is introduced, and at this time, the liquid depth becomes 60 mm. Predetermined amounts of Amy and chitosan were simultaneously or sequentially added to this beaker 2 with a pipette. In Table 1, when Amy and chitosan are listed in two stages, this means simultaneous addition, and when described as first (stage) and second (stage), it means that they were sequentially added in that order. After the addition of the amy and / or chitosan, a cooking egg whisk was manually inserted almost vertically into the beaker liquid as a stirrer 6 and stirred for a predetermined time. The speed change switch and the transformer 8 are manually adjusted, and about 1
It was adjusted so as to be 00 rpm and about 60 rpm with slow stirring.

【0035】凝集フロックの形成状態は、上記の凝集沈
殿操作終了後、肉眼観察を続けながら20分静置したあ
と行った。第一次判定として、内容物を2号濾紙を用い
て自然濾過し、その濾過速度と濾液の清澄度から判断し
た。この第一次判定で凝集状態がよいとみなされた実施
例については、第二次判定をおこなった。即ち、水流ポ
ンプとヌッチェに5A濾紙を敷いて減圧濾過し、残った
含水汚泥ケーキの含水率を株式会社ケット科学研究所製
の赤外線水分計FD−600を用いて測定した。測定は
試料を105℃で1時間加熱して行われた。実施例と比
較例の判定結果は表1にあり、それぞれ実1や比1のよ
うに記載する。
The formation state of the flocculated floc was performed after the completion of the flocculating and sedimentation operation, and after standing for 20 minutes while continuing to observe with the naked eye. As a first judgment, the content was subjected to natural filtration using No. 2 filter paper, and judgment was made from the filtration speed and the clarity of the filtrate. For the examples in which the primary state was considered to be good in the primary determination, a secondary determination was performed. That is, 5A filter paper was spread on a water-jet pump and Nutsche and filtered under reduced pressure, and the water content of the remaining water-containing sludge cake was measured using an infrared moisture meter FD-600 manufactured by Kett Science Laboratory Co., Ltd. The measurement was performed by heating the sample at 105 ° C. for 1 hour. The determination results of the example and the comparative example are shown in Table 1, and are described as “real 1” and “ratio 1”, respectively.

【0036】[0036]

【表1】 [Table 1]

【0037】実施例1−1および実施例1−2は、アミ
ーとキトサンを被処理水に逐次に添加する場合を示し、
その添加順序に拘わらず、汚泥の凝集沈殿またはフロッ
ク形成とその濾過に成功している。実施例1−3〜実施
例1−8はアミーとキトサンを被処理水に同時に添加し
た場合を示し、急速または緩速攪拌に拘わらず、しかも
両凝集剤の添加量をかなり低減しても、全体に大きなフ
ロックが形成されている。また濾過性が良いために濾液
が透明であり、脱水汚泥ケーキの含水率も比較的低かっ
た。これに反し、比較例1−1および比較例1−2で示
すように、アミーまたはキトサンを単独で使用した場合
には、凝集しなかったり、フロックがかなり小さいため
に濾過性が良くてもケーキの含水率がかなり高くなるこ
とが分かる。
Example 1-1 and Example 1-2 show the case where Amy and chitosan are sequentially added to the water to be treated,
Regardless of the order of addition, flocculation and floc formation of sludge and filtration thereof have been successful. Examples 1-3 to 1-8 show the case where Amy and chitosan were added to the water to be treated at the same time, irrespective of rapid or slow stirring, and even if the amount of both coagulants was considerably reduced, Large flocs are formed throughout. In addition, the filtrate was transparent because of good filterability, and the water content of the dewatered sludge cake was relatively low. On the other hand, as shown in Comparative Examples 1-1 and 1-2, when Amy or chitosan is used alone, cake does not coagulate or has a very small floc, so that the cake has good filterability. It can be seen that the water content of the.

【0038】また、表1からも分かるように、アミーや
キトサンを希釈して被処理水に添加した方が、原液のま
ま添加するよりも凝集効果が上がる。希釈すると粘性が
低下して被処理水と混じり易くなり、少量でも凝集効果
が発現し易くなる。従って、凝集剤の使用量を減量で
き、極めて経済的である。また、粘性の小さい分だけ攪
拌時間も短くでき、希釈倍率が高いほど多くの点で効果
的である。
As can be seen from Table 1, the coagulation effect is higher when diluting the amy or chitosan to the water to be treated than when adding it undiluted. When diluted, the viscosity is reduced and the water is easily mixed with the water to be treated. Therefore, the amount of the coagulant used can be reduced, which is extremely economical. In addition, the stirring time can be shortened by the lower viscosity, and the higher the dilution ratio, the more effective in many respects.

【0039】[実施例2:糖蛋白質NOC−1とキチン
・キトサンの併用]工業技術院生命工学工業技術研究所
に寄託されているロードコッカス・エリスロポリスKR
−S−1(FERM BP−4913)と同一の菌株を
入手し、本発明者が液体培地にて培養し、その培養原液
のみを微生物産生凝集剤のNOC−1として使用した。
[Example 2: Combined use of glycoprotein NOC-1 and chitin / chitosan] Rhodococcus erythropolis KR deposited at the Institute of Biotechnology and Industrial Technology, National Institute of Advanced Industrial Science and Technology
The same strain as that of -S-1 (FERM BP-4913) was obtained and cultured by the present inventors in a liquid medium, and only the undiluted culture solution was used as NOC-1 of a microorganism-producing coagulant.

【0040】この液体培地の組成は下記の通りであり、
この液体培地に種菌を接種して30℃で2日間振とう培
養した。炭素源としてはグルコースとフラクトースを使
用した。この培養液中にNOC−1が蓄積されている 炭素源 10g/L K2HPO4 5g/L KH2PO4 2g/L MgSO4 0.2g/L ウレア 0.5g/L イースト抽出物 0.5g/L NaCl 0.1g/L 精製水 1L(リットル)
The composition of this liquid medium is as follows:
This liquid medium was inoculated with a seed bacterium and cultured with shaking at 30 ° C. for 2 days. Glucose and fructose were used as carbon sources. NOC-1 is accumulated in this culture solution Carbon source 10 g / L K2HPO4 5 g / L KH2PO4 2 g / L MgSO4 0.2 g / L Urea 0.5 g / L Yeast extract 0.5 g / L NaCl 0.1 g / L purified water 1L (liter)

【0041】前記NOC−1の培養液の性状は、PHが
7.0〜8.0、凝集活性値は1.0〜1.5であっ
た。この活性値は1/OD550サンプルー1/OD5
50ブランクで与えられ、無機汚泥のカオリン凝集特性
から得られる。
The culture solution of NOC-1 had a pH of 7.0 to 8.0 and an agglutinating activity of 1.0 to 1.5. This activity value is 1 / OD550 sample-1 / OD5
Given in 50 blanks, it is obtained from the kaolin flocculation properties of inorganic sludge.

【0042】上記活性値の測定方法は下記の通りであ
る。培養したNOC−1を100mLのメスシリンダー
に1mL取り、純水9mLを加えて希釈する。これに、
カオリンを5000ppmの濃度で含む懸濁水を80m
Lと塩化カルシウムの10%水溶液10mLを加えて合
計100mLにする。この溶液に対しゆっくりした上下
転倒攪拌を3回行った後、10分間静置する。その後、
メスシリンダー内の液を液面下10cmの位置からサン
プルとして1mL採取し、吸光度測定用のセルに封入す
る。株式会社島津製作所製の分光光度計にて、波長55
0nmにおける吸光度OD550を測定する。なお、ブ
ランクとして、上記操作の内NOC−1の部分を純水に
置き換えたものを別途作成し、それについても吸光度を
測定する。
The method for measuring the above activity value is as follows. Take 1 mL of the cultured NOC-1 in a 100 mL graduated cylinder and add 9 mL of pure water for dilution. to this,
80m of suspension water containing kaolin at a concentration of 5000ppm
Add L and 10 mL of a 10% aqueous solution of calcium chloride to make a total of 100 mL. This solution is slowly stirred upside down three times, and then allowed to stand for 10 minutes. afterwards,
1 mL of the liquid in the measuring cylinder is sampled from a position 10 cm below the liquid surface as a sample, and sealed in a cell for measuring absorbance. With a spectrophotometer manufactured by Shimadzu Corporation, wavelength 55
The absorbance OD550 at 0 nm is measured. A blank in which the NOC-1 portion of the above operation was replaced with pure water was separately prepared, and the absorbance was measured for the blank.

【0043】キチン・キトサンとしては、甲陽ケミカル
株式会社が販売する商品名コーヨーキトサンの中から標
準的なSK−400を使用した。実施例1と同様に、こ
のSK−400の0.5%酢酸酸性水溶液を調製し、こ
の0.5%水溶液またはその水による希釈液(以後、キ
トサンと略称し、希釈度で区別する)をキチン・キトサ
ンとして使用した。実際にはキトサンの希釈液は使用し
なかった。
As chitin / chitosan, standard SK-400 from Koyo Chitosan (trade name, sold by Koyo Chemical Co., Ltd.) was used. In the same manner as in Example 1, a 0.5% aqueous solution of SK-400 in acetic acid was prepared, and this 0.5% aqueous solution or a diluent thereof (hereinafter abbreviated as chitosan and distinguished by the degree of dilution) was used. Used as chitin and chitosan. In practice, no chitosan diluent was used.

【0044】凝集沈殿の実験方法と判定方法は、実施例
1と同様であるから、その説明を省略する。実施例およ
び比較例の結果は表2に示されており、実2および比2
のように表される。
The experimental method and the method of judging the coagulation and sedimentation are the same as those in Example 1, and the description thereof will be omitted. The results of the examples and comparative examples are shown in Table 2 and show the results of the actual 2 and the ratio 2
It is represented as

【0045】[0045]

【表2】 [Table 2]

【0046】比較例1および2から、キトサン単独では
汚泥は凝集するが、フロックは小さく、濾過性は悪かっ
た。また比較例3から、NOC−1単独では十分に多い
量を添加しても汚泥を凝集沈殿させることはできなかっ
た。これに反し、実施例1から分かるように、NOC−
1とキトサンを順次添加した場合には凝集性は良くな
る。実施例2〜6はNOC−1とキトサンを同時に添加
した場合を示し、急速攪拌や緩速攪拌に拘わらず、どの
ケースでも凝集沈殿し、かつ濾過性も良い。実施例1〜
5は汚泥処理水を中和せず、実施例6は汚泥処理水を事
前に中和している。つまり中和の有無に関係なく、同時
添加では凝集効果が高くなる。また、添加量を少なくし
ても、ごく短時間の攪拌で大きなフロックを形成し、濾
過性も良く、含水汚泥ケーキの含水率も良好であった。
From Comparative Examples 1 and 2, chitosan alone aggregated sludge, but the floc was small and the filterability was poor. Further, from Comparative Example 3, it was not possible to coagulate and settle sludge even if NOC-1 alone was added in a sufficiently large amount. On the contrary, as can be seen from Example 1, NOC-
When 1 and chitosan are sequentially added, the cohesiveness is improved. Examples 2 to 6 show the case where NOC-1 and chitosan were added at the same time. In any case, irrespective of the rapid stirring or the slow stirring, coagulation and sedimentation were observed and the filterability was good. Example 1
5 does not neutralize the sludge treated water, and Example 6 neutralizes the sludge treated water in advance. That is, regardless of the presence or absence of neutralization, the co-addition enhances the aggregation effect. In addition, even if the addition amount was reduced, a large floc was formed by stirring for a very short time, the filterability was good, and the water content of the hydrous sludge cake was also good.

【0047】本発明は上記実施例に限定されるものでは
なく、本発明の技術的思想を逸脱しない範囲における種
々の変形例、設計変更などをその技術的範囲内に包含す
るものである。
The present invention is not limited to the above-described embodiment, but includes various modifications and design changes within the technical scope thereof without departing from the technical concept of the present invention.

【0048】[0048]

【発明の効果】本発明は以上詳述したように、近年に至
って急速に増加した都市下水、農業集落排水、畜産排
水、工場排水、土木建築汚泥水などの汚泥処理水を効率
的に清浄化することができる。しかも、微生物が産生す
る凝集剤と、バイオマス資源から得られたキチン・キト
サン複合体を併用した凝集剤であるから、人間を含む生
物に対し安全で、かつ自然環境を汚染することなく、汚
泥処理水から汚泥を効率的に凝集沈殿させる効果を有す
る。従って、従来から大量に使用されてきた凝集剤、即
ちアルツハイマー病の原因物質であるアルミニウム塩や
モノマーが発ガン物質・神経毒といわれるアクリルアミ
ド重合体に替わる凝集剤が提供されたのである。本発明
が近未来において、土壌を環境汚染から守る効果には極
めて大きいものがある。
As described in detail above, the present invention efficiently purifies sludge treated water such as urban sewage, agricultural settlement drainage, livestock drainage, factory drainage, civil engineering and construction sludge which has increased rapidly in recent years. can do. In addition, since the coagulant uses a coagulant produced by microorganisms and a chitin-chitosan complex obtained from biomass resources, it is safe for living organisms, including humans, and without polluting the natural environment. It has the effect of efficiently coagulating and settling sludge from water. Accordingly, a coagulant that has been used in large quantities in the past, that is, a coagulant that replaces an acrylamide polymer in which an aluminum salt or monomer that is a causative substance of Alzheimer's disease is called a carcinogen or neurotoxin, has been provided. In the near future, the effect of the present invention to protect soil from environmental pollution is extremely large.

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

【図1】図1は本発明に係る新規な凝集剤の凝集試験方
法を説明する斜視図である。
FIG. 1 is a perspective view for explaining a novel aggregating test method for an aggregating agent according to the present invention.

【符号の説明】[Explanation of symbols]

2はビーカー、4は汚泥処理液、6は攪拌機、8は変圧
器である。
2 is a beaker, 4 is a sludge treatment liquid, 6 is a stirrer, and 8 is a transformer.

───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 4D015 BA05 BB08 BB09 BB17 CA02 DB32 DB34 EA04 EA32 EA35 4D059 AA02 BE60 BE61 DB18 DB31 EB11  ──────────────────────────────────────────────────続 き Continued on the front page F term (reference) 4D015 BA05 BB08 BB09 BB17 CA02 DB32 DB34 EA04 EA32 EA35 4D059 AA02 BE60 BE61 DB18 DB31 EB11

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 微生物産生凝集剤とキチン・キトサンを
併用したことを特徴とする凝集剤。
1. A flocculant comprising a combination of a microorganism-producing flocculant and chitin / chitosan.
【請求項2】 前記微生物産生凝集剤としてロードコッ
カス・エリスロポリスを含むグラム陽性菌が産生する糖
蛋白質を主成分とする凝集活性物質またはオーレオバシ
ジウム属の菌株が産生する酸性多糖を主成分とする凝集
活性物質を用い、前記キチン・キトサンとしてキチン質
を80%以上に脱アセチル化して得られたキチン・キト
サンを用いる請求項1記載の凝集剤。
2. An agglutinating agent mainly containing a glycoprotein produced by a Gram-positive bacterium containing Rhodococcus erythropolis as the microorganism-producing flocculant or an acidic polysaccharide produced by a strain of Aureobasidium genus as a main component. The flocculant according to claim 1, wherein a chitin / chitosan obtained by deacetylating chitin to 80% or more is used as the chitin / chitosan.
【請求項3】 微生物産生凝集剤とキチン・キトサンの
併用重量比を1:9〜5:5とした請求項2記載の凝集
剤。
3. The coagulant according to claim 2, wherein the combined weight ratio of the microorganism-produced coagulant and chitin / chitosan is 1: 9 to 5: 5.
【請求項4】 微生物産生凝集剤とキチン・キトサンを
凝集剤として被処理水に添加して汚泥を凝集沈殿させる
か、又は含水汚泥に添加して汚泥を脱水することを特徴
とする汚泥処理方法。
4. A method for treating sludge, comprising adding a microorganism-producing coagulant and chitin / chitosan as coagulants to water to be treated to coagulate and settle sludge, or adding it to hydrous sludge to dewater sludge. .
【請求項5】 前記微生物産生凝集剤としてロードコッ
カス・エリスロポリスを含むグラム陽性菌が産生する糖
蛋白質を主成分とする凝集活性物質またはオーレオバシ
ジウム属の菌株が産生する酸性多糖を主成分とする凝集
活性物質を用い、前記キチン・キトサンとしてキチン質
を80%以上に脱アセチル化して得られたキチン・キト
サンを用いる請求項4記載の汚泥処理方法。
5. An agglutinating substance mainly composed of a glycoprotein produced by a Gram-positive bacterium including Rhodococcus erythropolis as the microorganism-producing flocculant or an acidic polysaccharide produced by a strain of the genus Aureobasidium. 5. The sludge treatment method according to claim 4, wherein a chitin / chitosan obtained by deacetylating chitin to 80% or more is used as the chitin / chitosan.
【請求項6】 微生物産生凝集剤とキチン・キトサンの
併用重量比を1:9〜5:5とし、両剤を同時一括添加
するか又は逐次添加し、逐次添加では添加順序に制限が
ない請求項5記載の汚泥処理方法。
6. The combined weight ratio of the microorganism-producing coagulant and chitin / chitosan is 1: 9 to 5: 5, and both agents are added simultaneously or sequentially, and the order of addition is not limited in the sequential addition. 6. The method for treating sludge according to 5.
JP10324780A 1998-11-16 1998-11-16 Novel flocculant and sludge treatment using the same Withdrawn JP2000140509A (en)

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001247601A (en) * 2000-03-03 2001-09-11 Marine Biotechnol Inst Co Ltd Extracellular polysaccharide produced by bacteria belonging to genus rhodococcus and clarification method of marine environment using the same
JP2005529191A (en) * 2002-02-12 2005-09-29 キトツィーム・エス・アー Cell wall derivatives from biomass and their preparation
CN115611436A (en) * 2022-09-30 2023-01-17 北京城市排水集团有限责任公司 Modified composite material and application thereof, and sewage biological treatment standard-improving and efficiency-improving method
US11866354B2 (en) 2016-09-16 2024-01-09 Dexerials Corporation Extract of plant powder, and water purifier
US11952297B2 (en) 2016-09-16 2024-04-09 Dexerials Corporation Extract of plant powder, and water purifier

Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63126596A (en) * 1986-11-14 1988-05-30 Agency Of Ind Science & Technol Decoloring method for soluble dye by microorganism
JPH0290903A (en) * 1988-09-26 1990-03-30 Agency Of Ind Science & Technol Flocculant derived from microbe and flocculation method
JPH0292273A (en) * 1988-09-29 1990-04-03 Agency Of Ind Science & Technol Production enhancing medium of bacterium flocculating agent and production enhancement
JPH03249909A (en) * 1990-02-28 1991-11-07 Agency Of Ind Science & Technol Production of microbial flocculant and method for recovering useful matter
JPH05345180A (en) * 1992-06-12 1993-12-27 Umehara Jiro Improving method of water quality
JPH06114208A (en) * 1992-06-18 1994-04-26 Osaka City Flocculant
JPH0775561A (en) * 1991-05-15 1995-03-20 Agency Of Ind Science & Technol Medium for producing microbial coagulant and production method
JPH07100304A (en) * 1993-09-30 1995-04-18 Nippon Synthetic Chem Ind Co Ltd:The Flocculating method for suspension liquid
JPH0881501A (en) * 1994-03-22 1996-03-26 Agawamura Acidic polysaccharide
JPH08322547A (en) * 1995-05-30 1996-12-10 Otsuka Chem Co Ltd Protein separation from liquid material

Patent Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63126596A (en) * 1986-11-14 1988-05-30 Agency Of Ind Science & Technol Decoloring method for soluble dye by microorganism
JPH0290903A (en) * 1988-09-26 1990-03-30 Agency Of Ind Science & Technol Flocculant derived from microbe and flocculation method
JPH0292273A (en) * 1988-09-29 1990-04-03 Agency Of Ind Science & Technol Production enhancing medium of bacterium flocculating agent and production enhancement
JPH03249909A (en) * 1990-02-28 1991-11-07 Agency Of Ind Science & Technol Production of microbial flocculant and method for recovering useful matter
JPH0775561A (en) * 1991-05-15 1995-03-20 Agency Of Ind Science & Technol Medium for producing microbial coagulant and production method
JPH05345180A (en) * 1992-06-12 1993-12-27 Umehara Jiro Improving method of water quality
JPH06114208A (en) * 1992-06-18 1994-04-26 Osaka City Flocculant
JPH07100304A (en) * 1993-09-30 1995-04-18 Nippon Synthetic Chem Ind Co Ltd:The Flocculating method for suspension liquid
JPH0881501A (en) * 1994-03-22 1996-03-26 Agawamura Acidic polysaccharide
JPH08322547A (en) * 1995-05-30 1996-12-10 Otsuka Chem Co Ltd Protein separation from liquid material

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001247601A (en) * 2000-03-03 2001-09-11 Marine Biotechnol Inst Co Ltd Extracellular polysaccharide produced by bacteria belonging to genus rhodococcus and clarification method of marine environment using the same
JP4657414B2 (en) * 2000-03-03 2011-03-23 範之 岩淵 Extracellular polysaccharides produced by bacteria belonging to the genus Rhodococcus and methods for purification of marine environment using the same
JP2005529191A (en) * 2002-02-12 2005-09-29 キトツィーム・エス・アー Cell wall derivatives from biomass and their preparation
US11866354B2 (en) 2016-09-16 2024-01-09 Dexerials Corporation Extract of plant powder, and water purifier
US11952297B2 (en) 2016-09-16 2024-04-09 Dexerials Corporation Extract of plant powder, and water purifier
CN115611436A (en) * 2022-09-30 2023-01-17 北京城市排水集团有限责任公司 Modified composite material and application thereof, and sewage biological treatment standard-improving and efficiency-improving method

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