JPH0732920B2 - Enzymatic modification and concentration method of organic sludge - Google Patents

Enzymatic modification and concentration method of organic sludge

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Publication number
JPH0732920B2
JPH0732920B2 JP63171473A JP17147388A JPH0732920B2 JP H0732920 B2 JPH0732920 B2 JP H0732920B2 JP 63171473 A JP63171473 A JP 63171473A JP 17147388 A JP17147388 A JP 17147388A JP H0732920 B2 JPH0732920 B2 JP H0732920B2
Authority
JP
Japan
Prior art keywords
sludge
enzyme
organic
organic sludge
lysozyme
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.)
Expired - Lifetime
Application number
JP63171473A
Other languages
Japanese (ja)
Other versions
JPH0222000A (en
Inventor
明夫 岡田
三雄 川瀬
安子 吉田
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.)
NGK Insulators Ltd
Original Assignee
NGK Insulators 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 NGK Insulators Ltd filed Critical NGK Insulators Ltd
Priority to JP63171473A priority Critical patent/JPH0732920B2/en
Publication of JPH0222000A publication Critical patent/JPH0222000A/en
Publication of JPH0732920B2 publication Critical patent/JPH0732920B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Treatment Of Sludge (AREA)

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は都市下水汚泥のような有機質分を多量に含む汚
泥を無薬注で改質するとともに容易に濃縮することがで
きる酵素による有機性汚泥の改質及び濃縮方法に関する
ものである。
DETAILED DESCRIPTION OF THE INVENTION (Industrial field of application) The present invention is an enzyme-based organic substance capable of reforming sludge containing a large amount of organic matter such as municipal sewage sludge without chemical injection and easily concentrating it. The present invention relates to a method for reforming and concentrating sludge.

(従来の技術) 多量の有機質分を含有する有機性汚泥を凝集させるため
には、助剤として消石灰、塩化第二鉄、高分子凝集剤等
を汚泥に添加し混合し、凝集させるのが普通である。し
かし消石灰、塩化第二鉄等を添加すると脱水ケーキのボ
リュームが増加するほか、設備の配管内部等にスケール
が付着するという欠点があり、また高分子凝集剤を用い
た場合には脱水ケーキの含水率を低下させることが困難
であるという欠点があった。
(Prior Art) In order to coagulate organic sludge containing a large amount of organic matter, it is common to add slaked lime, ferric chloride, polymer coagulant, etc. to the sludge as an auxiliary agent and mix them to coagulate. Is. However, the addition of slaked lime, ferric chloride, etc. increases the volume of the dehydrated cake, and has the disadvantage that scale adheres to the inside of the piping of the equipment, etc. There was a drawback that it was difficult to reduce the rate.

このため、これらの助剤を使用せず無薬注で汚泥処理を
行う方法が求められており、例えば特開昭61−278400号
公報には汚泥を電気分解処理することによって汚泥の改
質を図る方法が示されている。しかしこの方法は多くの
電力を要するためにコスト高となる欠点がある。
Therefore, there is a demand for a method of performing sludge treatment by chemical injection without using these auxiliaries, and for example, in JP-A-61-278400, sludge is reformed by electrolysis treatment. It shows how to do it. However, this method has a drawback that the cost is high because a lot of power is required.

(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問題を解決して、有機性汚泥
を無薬注で、しかも低コストで迅速に改質し、また濃縮
することができる酵素による有機性汚泥の改質及び濃縮
方法を目的として完成されたものである。
(Problems to be Solved by the Invention) The present invention solves such a conventional problem by using an enzyme capable of rapidly modifying and concentrating organic sludge without chemical injection and at low cost. It was completed for the purpose of reforming and concentrating organic sludge.

(課題を解決するための手段) 上記の課題を達成するためになされ第1の発明は有機性
汚泥にリゾチーム等の溶菌酵素を接触させ、10〜50℃の
温度条件下で撹拌することにより汚泥を分解、改質する
ことを特徴とするものであり、第2の発明は有機性汚泥
にリゾチーム等の溶菌酸素を接触させ、撹拌することに
よって汚泥を凝集させ、これを沈澱濃縮することを特徴
とするものである。
(Means for Solving the Problem) The first invention made to achieve the above object is to bring sludge into contact with a lytic enzyme such as lysozyme by contacting the organic sludge with stirring at a temperature of 10 to 50 ° C. The second invention is characterized in that organic sludge is brought into contact with lysing oxygen such as lysozyme and agitated to agglomerate the sludge to precipitate and concentrate it. It is what

第1の発明においては、生物処理汚泥のような有機性汚
泥(TS値が1〜5%程度)に溶菌酵素を接触させ、その
触媒作用によって有機性汚泥中の菌体の細胞壁を溶解さ
せることにより汚泥の改質を図る。溶菌酵素としてはリ
ゾチームが代表的なものであるが、ザイモリエース等の
その他の溶菌酵素を用いることもできる。溶菌酵素は遊
離状態で汚泥中に添加し撹拌して反応させても、また担
体に固定化し汚泥と接触させてもよい。前者の場合には
溶菌酵素の添加量は30U/以上とするものとし、撹拌は
汚泥と酸素とが十分接触できる程度の弱撹拌とすればよ
い。また後者の場合には溶菌酵素をセピオライト担体の
ようなセラミックス担体に固定化し、これをカラム内に
充填して上向流式もしくは下向流式で汚泥を通泥して接
触反応させればよく、この場合の滞留時間は1時間とす
れば十分である。なお反応温度は溶菌酵素の活性が大き
くなる10〜50℃、より好ましくは30〜40℃が適当であ
り、10℃未満では活性が低下し、また50℃を超えると加
温のためのエネルギーコストが高くつくうえに悪臭発生
の原因ともなるので実用的ではない。
In the first invention, a lytic enzyme is contacted with an organic sludge (TS value of about 1 to 5%) such as biologically treated sludge, and the cell wall of the microbial cells in the organic sludge is dissolved by its catalytic action. To improve sludge. Lysozyme is a typical lytic enzyme, but other lytic enzymes such as zymolyase can also be used. The lytic enzyme may be added to sludge in a free state and reacted by stirring, or may be immobilized on a carrier and brought into contact with sludge. In the former case, the addition amount of the lytic enzyme is 30 U / or more, and the stirring may be weak stirring so that the sludge and oxygen can be sufficiently brought into contact with each other. In the latter case, the lytic enzyme may be immobilized on a ceramics carrier such as a sepiolite carrier, which may be packed in a column and sludge may be passed through the column in an upflow or downflow system to cause a catalytic reaction. In this case, the residence time of 1 hour is sufficient. It should be noted that the reaction temperature is 10 to 50 ° C at which the activity of the lytic enzyme becomes large, and more preferably 30 to 40 ° C. It is not practical because it is expensive and causes a bad odor.

第2の発明においても同様に有機性汚泥にリゾチーム等
の溶菌酵素を接触させるが、この場合の溶菌酵素の添加
量は1U/以上とすればよく、第1の発明に比較してわ
ずかである。本発明においては溶菌酵素は菌体の細胞壁
を完全に溶解するには至らないが、遊離状態にある菌体
を相互に集合させるバインダーとしての役割を演じ、難
脱水性汚泥をも速やかに凝集させることができる。凝集
した汚泥を重力濃縮させれば、高濃度の汚泥を得ること
ができる。
In the second invention as well, a lytic enzyme such as lysozyme is brought into contact with the organic sludge in the same manner. In this case, the addition amount of the lytic enzyme may be 1 U / or more, which is small compared to the first invention. . In the present invention, the lytic enzyme does not completely dissolve the cell wall of the microbial cell, but plays a role as a binder for assembling the microbial cells in a free state with each other, and also rapidly agglomerates the non-dehydrating sludge. be able to. If the aggregated sludge is gravity-concentrated, a high-concentration sludge can be obtained.

以下に各発明を実施例により更に詳細に説明する。Hereinafter, each invention will be described in more detail with reference to Examples.

(実施例) 実施例1−汚泥の改質方法 1m×1m×1.5mの改質槽に有機性汚泥を入れ、リゾチーム
を遊離状態で種々の濃度となるように添加し、35℃で1
時間撹拌した。撹拌は汚泥とリゾチームの接触を目的と
し、100rpm以下の弱い撹拌とした。このようにして改質
された汚泥をベルトプレス脱水機で脱水した。脱水条件
は濾布速度0.75m/分、濾布緊張圧力2kg/cm2である。な
おベルトプレスによる濾過速度は余剰汚泥の場合50kg/m
・Hr、混合汚泥の場合120kg/m・Hrであった。
(Example) Example 1-Sludge reforming method Put organic sludge into a 1 m x 1 m x 1.5 m reforming tank, add lysozyme to various concentrations in a free state, and perform 1 at 35 ° C.
Stir for hours. The stirring was for the purpose of contacting sludge and lysozyme, and was weak stirring at 100 rpm or less. The sludge thus modified was dehydrated with a belt press dehydrator. The dehydration conditions are a filter cloth speed of 0.75 m / min and a filter cloth tension pressure of 2 kg / cm 2 . The filtration rate by the belt press is 50 kg / m for excess sludge.
・ Hr, 120 kg / m ・ Hr for mixed sludge.

第1図はこのようにして得られた脱水汚泥の含水率と酵
素量との関係を示すグラフであり、特に混合汚泥の場合
には酵素量が30U/以上となると含水率が70%にまで低
下し、余剰汚泥の場合含水率が83%にまで低下すること
が分かる。また第2図は脱水前の汚泥の濾過性の指標で
あるCST値と酵素量との関係を示すグラフであり、30U/g
以上の酵素を添加すると汚泥が改質され、CST値が20〜5
0秒にまで低下することが分かる。
Fig. 1 is a graph showing the relationship between the water content of dehydrated sludge and the amount of enzyme obtained in this way. Especially in the case of mixed sludge, when the amount of enzyme is 30 U / or more, the water content reaches 70%. It can be seen that the water content decreases to 83% in the case of excess sludge. Fig. 2 is a graph showing the relationship between the CST value, which is an index of the filterability of sludge before dehydration, and the amount of enzyme, 30 U / g
When the above enzymes are added, the sludge will be modified and the CST value will be 20-5.
It can be seen that it drops to 0 seconds.

これに対して従来の高分子凝集剤を用いたベルトプレス
による脱水処理の含水率は混合汚泥の場合78%、余剰汚
泥の場合86%であるのと比例すると、次表に示すように
乾燥汚泥(DS)当たりの付着水分量は混合汚泥の場合21
%、余剰汚泥の場合34%も低下している。
On the other hand, if the water content of dehydration treatment by a belt press using a conventional polymer coagulant is 78% for mixed sludge and 86% for excess sludge, it is proportional to dry sludge as shown in the following table. The amount of attached water per (DS) is 21 for mixed sludge.
%, And in the case of excess sludge, it has decreased by 34%.

また直径0.5m、高さ1mのカラムにリゾチームを固定化し
た担体をカラム中に充填する担体数を変化させて充填し
たものを用いて同様の測定を行った結果を第3図と第4
図に示す。このように遊離酵素を用いた場合にも、固定
化された酵素を用いた場合にも同様の汚泥改質効果が確
認された。このように本発明によれば無薬注で有機性汚
泥の改質を図ることができる。
In addition, the same measurement was carried out using a column having a diameter of 0.5 m and a height of 1 m, in which the carrier in which lysozyme was immobilized was packed while varying the number of carriers packed in the column.
Shown in the figure. Thus, the same sludge reforming effect was confirmed when the free enzyme was used and when the immobilized enzyme was used. As described above, according to the present invention, the organic sludge can be reformed without chemical injection.

実施例2−汚泥の凝集方法 濃度が0.52%の希釈された難脱水性の有機質汚泥に0.1U
/の種々の量のリゾチームを添加し、約1分間200rpm
の急速撹拌を行い、その後1時間重力濃縮を行わせた。
この結果、リゾチームがバインダとして作用して汚泥が
凝集したのでその濃縮汚泥の濃度をJISに規定される方
法によって測定したところ、第5図のとおりの結果が得
られた。第5図からも明らかなように、1U/以上の溶
菌酵素の添加により濃縮汚泥濃度は3%以上にまで上昇
し、以下の脱水が容易に行えるようになった。
Example 2-Sludge flocculation method 0.1 U for diluted non-dewatering organic sludge with a concentration of 0.52%
Add various amount of / of lysozyme, 200 rpm for about 1 minute
Was rapidly stirred, followed by gravity concentration for 1 hour.
As a result, lysozyme acted as a binder to agglomerate the sludge, and the concentration of the concentrated sludge was measured by the method specified in JIS. The results shown in FIG. 5 were obtained. As is clear from FIG. 5, the concentration of the concentrated sludge increased to 3% or more by the addition of 1 U / or more lytic enzyme, and the following dehydration could be easily performed.

また、通常の重力濃縮方により前記汚泥を24時間濃縮し
たところ、濃縮汚泥濃度は1.5%であった。この結果か
らも通常の重量濃縮方に比較して、短時間に約2倍の濃
度にまで濃縮が行われていることが明らかである。
When the sludge was concentrated for 24 hours by the usual gravity concentration method, the concentration of the concentrated sludge was 1.5%. From this result, it is clear that the concentration is approximately doubled in a short time as compared with the usual weight concentration method.

(発明の効果) 本発明は以上に説明したとおり、リゾチームのような溶
菌酵素を有機性汚泥と接触させることによって汚泥の改
質あるいは凝集を行わせることができるものであって、
無薬注で汚泥処理が可能であるので、従来のように消石
灰や塩化第二鉄を添加する方法とは異なり脱水ケーキの
ボリュームが増加することがなく、短時間に高濃度まで
濃縮でき、また配管内部等にスケールが付着することも
ない。更に本発明によれば脱水ケーキの含水率を低下さ
せることができるうえ、汚泥の電気分解法に比較して汚
泥処理コストを引下げることができる。よって本発明は
従来の問題点を一掃した酵素による有機性汚泥の改質及
び濃縮方法として、産業の発展に寄与するところは極め
て大である。
(Effect of the invention) As described above, the present invention is capable of reforming or agglomerating sludge by contacting a lytic enzyme such as lysozyme with organic sludge,
Since sludge treatment is possible without chemical injection, unlike the conventional method of adding slaked lime or ferric chloride, the volume of the dehydrated cake does not increase, and it can be concentrated to a high concentration in a short time. No scale adheres to the inside of the pipe. Further, according to the present invention, the water content of the dehydrated cake can be reduced, and the sludge treatment cost can be reduced as compared with the sludge electrolysis method. Therefore, the present invention, as a method for modifying and concentrating an organic sludge with an enzyme that eliminates the conventional problems, is extremely important in contributing to industrial development.

【図面の簡単な説明】 第1図は第1の発明における遊離酵素量と脱水ケーキの
含水率との関係を示すグラフ、第2図は遊離酵素量とCS
T値との関係を示すグラフ、第3図は固定化酵素量と含
水率との関係を示すグラフ、第4図は固定化酵素量とCS
T値との関係を示すグラフ、第5図は第2の発明におけ
る酵素量と重力濃縮された汚泥濃度との関係を示すグラ
フである。
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a graph showing the relationship between the amount of free enzyme and the water content of dehydrated cake in the first invention, and FIG. 2 is the amount of free enzyme and CS.
Graph showing the relationship with T value, Fig. 3 is a graph showing the relationship between the amount of immobilized enzyme and water content, and Fig. 4 is the amount of immobilized enzyme and CS
FIG. 5 is a graph showing the relationship with the T value, and FIG. 5 is a graph showing the relationship between the enzyme amount and the gravity-concentrated sludge concentration in the second invention.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】有機性汚泥にリゾチーム等の溶菌酵素を接
触させ、10〜50℃の温度条件下で撹拌することにより汚
泥を分解、改質することを特徴とする酵素による有機性
汚泥の改質方法。
1. A method for modifying an organic sludge with an enzyme, which comprises decomposing and modifying the sludge by bringing a lysing enzyme such as lysozyme into contact with the organic sludge and stirring the mixture under a temperature condition of 10 to 50 ° C. Quality method.
【請求項2】有機性汚泥にリゾチーム等の溶菌酵素を接
触させ、撹拌することによって汚泥を凝集させ、これを
沈澱濃縮することを特徴とする酵素による汚泥の濃縮方
法。
2. A method for concentrating sludge with an enzyme, which comprises contacting a lysing enzyme such as lysozyme with organic sludge and stirring to agglomerate the sludge to precipitate and concentrate the sludge.
JP63171473A 1988-07-08 1988-07-08 Enzymatic modification and concentration method of organic sludge Expired - Lifetime JPH0732920B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63171473A JPH0732920B2 (en) 1988-07-08 1988-07-08 Enzymatic modification and concentration method of organic sludge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63171473A JPH0732920B2 (en) 1988-07-08 1988-07-08 Enzymatic modification and concentration method of organic sludge

Publications (2)

Publication Number Publication Date
JPH0222000A JPH0222000A (en) 1990-01-24
JPH0732920B2 true JPH0732920B2 (en) 1995-04-12

Family

ID=15923757

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63171473A Expired - Lifetime JPH0732920B2 (en) 1988-07-08 1988-07-08 Enzymatic modification and concentration method of organic sludge

Country Status (1)

Country Link
JP (1) JPH0732920B2 (en)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2572334B2 (en) * 1992-09-28 1997-01-16 株式会社荏原製作所 Method and apparatus for microbiological reduction of excess sludge
CA2620659C (en) * 2005-09-02 2015-10-27 Novozymes North America, Inc. Methods for enhancing the dewaterability of sludge with -alpha-amylase treatment
JP2008012476A (en) * 2006-07-07 2008-01-24 Honda Motor Co Ltd Wastewater treatment system
KR100967639B1 (en) * 2008-03-26 2010-07-07 지에스건설 주식회사 METHOD FOR REDUCING EXCESS SLUDGE USING THERMOMONAS SP. GSlyso-1 STRAIN
CN102566101A (en) * 2012-02-17 2012-07-11 深圳市华星光电技术有限公司 Fixing device of liquid crystal panel and liquid crystal display of fixing device
KR20220160028A (en) * 2020-03-26 2022-12-05 스미또모 가가꾸 가부시키가이샤 Protein having peptidoglycan degradation activity and DNA encoding the protein, microbial degradation agent and microbial degradation method
CN113880394B (en) * 2021-08-31 2023-10-13 芜湖海创环保科技有限责任公司 Plant enzyme sludge dehydrating agent and method for dehydrating sludge

Also Published As

Publication number Publication date
JPH0222000A (en) 1990-01-24

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