JPH0218905B2 - - Google Patents

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Publication number
JPH0218905B2
JPH0218905B2 JP2161087A JP2161087A JPH0218905B2 JP H0218905 B2 JPH0218905 B2 JP H0218905B2 JP 2161087 A JP2161087 A JP 2161087A JP 2161087 A JP2161087 A JP 2161087A JP H0218905 B2 JPH0218905 B2 JP H0218905B2
Authority
JP
Japan
Prior art keywords
enzymes
enzyme
sewage
organic
treatment
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
Application number
JP2161087A
Other languages
Japanese (ja)
Other versions
JPS63190690A (en
Inventor
Masahiro Kon
Tatsuo Sumino
Shozo Harada
Ichiro Nakajima
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hitachi Ltd
Original Assignee
Hitachi Plant Engineering and Construction 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 Hitachi Plant Engineering and Construction Co Ltd filed Critical Hitachi Plant Engineering and Construction Co Ltd
Priority to JP2161087A priority Critical patent/JPS63190690A/en
Publication of JPS63190690A publication Critical patent/JPS63190690A/en
Publication of JPH0218905B2 publication Critical patent/JPH0218905B2/ja
Granted legal-status Critical Current

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  • Treatment Of Sludge (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

〔産業上の利用分野〕 本発明は、下水処理に係り、特に下水処理場に
流入する下水やビル廃水等の低濃度有機廃水等中
の浮遊有機物質を酵素により可溶化する方法に関
する。 〔従来の技術〕 河川や湖沼の富栄養化、水質源確保が困難とな
るに伴い、下水の高効率処理技術の開発が社会的
に要求されている。その一環として、下水の窒素
除去が望まれている。窒素除去方法としては、大
別して物理化学的方法及び生物学的方法の2種類
があるが、前者はアンモニア態窒素しか除去でき
ないのに対し、後者は有機態窒素も除去できるの
で、下水のように有機態窒素を含む廃水の処理に
は、生物学的方法が適していると考えられる。 生物学的窒素除去方法は、硝化工程及び脱窒工
程から成り、脱窒工程に必要な有機炭素源として
下水中のBODが消費されるため、合理的プロセ
スである。 〔発明が解決しようとする問題点〕 ところで、生物学的処理における脱窒工程に必
要な有機炭素源は、理論的には、硝酸態窒素の
2.86倍以上であるが、将来、処理水の向上及び処
理の高速化へ移行する伴い、有機炭素源である
BODの不足が懸念され、BOD補給が必要とな
る。 このBOD源を系内から供給する方法として、
下水中の浮遊有機物質を可溶化して有機炭素源を
補給することが考えられる。可溶化方法として
は、(1)熱処理、(2)酸及びアルカリ処理、(3)熱と酸
又はアルカリ処理の組み合わせ、(4)酵素処理が考
えられる。(1)〜(3)は種々研究され、いくつかの報
告がされているが、生物処理が困難なものまで分
解してしまう傾向がある。他方、(4)の酵素処理
は、生物処理しやすい範囲まで穏和に分解すると
予想されるが、未だ、適用例がない。 従つて、本発明は、前記従来技術の欠点を解消
し、生物酸化処理しやすい範囲まで下水中の有機
性浮遊物質を分解、可溶化しうる酵素処理法を提
供することを目的とする。 〔問題点を解決するための手段〕 本発明は、酵素を特別の順序で添加することに
よつて前記の問題点を解決したものである。 即ち、本発明は、酵素の添加順序をまず、澱粉
分解酵素、次に、蛋白質分解酵素、そしてその他
の有機物分解酵素とすることを特徴とする下水中
の有機性浮遊物質の酵素処理法に関する。 下水に2種以上の酵素を同時に添加しても、下
水中の浮遊性有機物質は、酵素を個々に添加した
場合と同等又はそれ以下でしか分解されないが、
本発明により、まず澱粉分解酵素、次に、蛋白質
分解酵素を添加し、その後、残りの酵素を添加す
ると、効率よく有機物質が分解される。三番目に
添加される酵素としては、セルロース分解酵素、
脂肪分解酵素、細胞壁分解酵素等があるが、これ
らはどのような添加順序で添加しても、効果に影
響はない。 澱粉分解酵素は、α−及びβ−アミラーゼであ
り、動物の膵液及び唾液、カビ、細菌等に存在
し、また、生産される。また、蛋白質分解酵素と
しては、例えばペプシン、トリプシン、キモトリ
プシン、及びカビ、酵母又は細菌のプロテアーゼ
が挙げられる。脂肪分解酵素としては、リパーゼ
があり、これは動物の膵液或いは胃液中、又はヒ
マの種子、ナタネナの種子、カビ、酵母、細菌中
に存在し、また、これらによつて生産される。セ
ルロース分解酵素はセルラーゼであり、カビ、細
菌、原虫、植物等に存在し、生産される。更に、
細胞壁分解酵素として、リゾチームが挙げられ
る。リゾチームは、卵白やイチジクの乳液から得
られるもので、細菌の細胞壁のムコ多糖類の加水
分解を接触する酵素である。 それぞれの酵素を添加し、反応させる際の反応
条件は、酵素の種類及びその起源によつて変動す
るが、当業者は各酵素に関する反応最的条件を適
宜選択することができる。 酵素処理によつて可溶化された有機物は、
TOCの増加分として測定することができる。 〔実施例〕 次に、実施例に基づいて本発明を詳述するが、
本発明はこれに限定されるものではない。 参考例 1 分流式のK処理場に流入する下水を採取し、α
−アミラーゼ(起源:枯草菌)、中性プロテアー
ゼ(起源:放線菌)、リパーゼ(クモノスカビ)、
セルラーゼ(起源:糸状菌)及び卵白リゾチーム
をそれぞれ単独で用いて処理した。 その際の処理条件は、下記のとおりである:
[Industrial Application Field] The present invention relates to sewage treatment, and particularly to a method for solubilizing suspended organic substances in low-concentration organic wastewater such as sewage or building wastewater flowing into a sewage treatment plant using an enzyme. [Conventional technology] As rivers and lakes become eutrophic and it becomes difficult to secure water sources, there is a social demand for the development of highly efficient sewage treatment technology. As part of this effort, it is hoped that nitrogen will be removed from sewage. There are two types of nitrogen removal methods: physicochemical methods and biological methods.The former can only remove ammonia nitrogen, while the latter can also remove organic nitrogen, so it can be Biological methods are considered suitable for treating wastewater containing organic nitrogen. The biological nitrogen removal method consists of a nitrification process and a denitrification process, and it is a rational process because BOD in sewage is consumed as an organic carbon source necessary for the denitrification process. [Problems to be solved by the invention] By the way, the organic carbon source necessary for the denitrification process in biological treatment is theoretically nitrate nitrogen.
This is more than 2.86 times, but in the future, with the transition to improved and faster processing of treated water, it will become an organic carbon source.
There are concerns about a lack of BOD, and BOD replenishment will be necessary. As a method of supplying this BOD source from within the system,
One possibility is to solubilize suspended organic matter in sewage to replenish organic carbon sources. Possible solubilization methods include (1) heat treatment, (2) acid and alkali treatment, (3) combination of heat and acid or alkali treatment, and (4) enzyme treatment. Various studies have been conducted on (1) to (3), and several reports have been made, but they tend to degrade even those that are difficult to biologically treat. On the other hand, enzyme treatment (4) is expected to gently decompose to the extent that it can be easily biotreated, but there are no examples of its application yet. Therefore, it is an object of the present invention to provide an enzyme treatment method capable of eliminating the drawbacks of the prior art and capable of decomposing and solubilizing organic suspended substances in sewage to the extent that they can be easily biooxidized. [Means for Solving the Problems] The present invention solves the above problems by adding enzymes in a particular order. That is, the present invention relates to a method for enzymatically treating organic suspended solids in sewage, which is characterized in that the order of addition of enzymes is first a starch degrading enzyme, then a protease degrading enzyme, and then other organic matter degrading enzymes. Even if two or more enzymes are added to sewage at the same time, the suspended organic matter in the sewage will be degraded at the same rate or less than when the enzymes are added individually.
According to the present invention, organic substances are efficiently decomposed by first adding a starch-degrading enzyme, then a protease, and then adding the remaining enzymes. The third enzyme added is cellulolytic enzyme,
There are lipolytic enzymes, cell wall degrading enzymes, etc., but no matter what order these are added, the effect will not be affected. Starch degrading enzymes are α- and β-amylases, and are present or produced in pancreatic juice and saliva of animals, molds, bacteria, and the like. Examples of proteases include pepsin, trypsin, chymotrypsin, and fungal, yeast, or bacterial proteases. Lipolytic enzymes include lipase, which exists in pancreatic or gastric juice of animals, or in castor seeds, rapeseed seeds, molds, yeasts, and bacteria, and is produced by these. Cellulose-degrading enzymes are cellulases, which exist and are produced by molds, bacteria, protozoa, plants, and the like. Furthermore,
Lysozyme is an example of a cell wall degrading enzyme. Lysozyme, obtained from egg whites and fig milk, is an enzyme that catalyzes the hydrolysis of mucopolysaccharides in bacterial cell walls. The reaction conditions for adding and reacting each enzyme vary depending on the type of enzyme and its origin, but those skilled in the art can appropriately select the optimal reaction conditions for each enzyme. Organic matter solubilized by enzyme treatment is
It can be measured as an increase in TOC. [Examples] Next, the present invention will be described in detail based on Examples.
The present invention is not limited to this. Reference example 1 Sewage flowing into a separate type K treatment plant is collected, and α
- amylase (origin: Bacillus subtilis), neutral protease (origin: actinobacteria), lipase (arachnoid fungus),
Cellulase (origin: filamentous fungi) and egg white lysozyme were each used alone for treatment. The processing conditions at that time are as follows:

【表】 処理結果を第1表に示す。 第1表 酵素名 TOC増加率(%) α−アミラーゼ 26 中性プロテアーゼ 9 リパーゼ 11 セルラーゼ 8 リゾチーム 7 TOC増加率の最も高いのは、α−アミラーゼ
であつた。 実施例 1 参考例1に記載したのと同じ下水を採取し、ま
ず、α−アミラーゼを用いて参考例1に記載した
のと同じ条件で処理し、次いで、残りの酵素で
個々に処理した結果、第2表に示す結果を得た。
[Table] Table 1 shows the processing results. Table 1 Enzyme name TOC increase rate (%) α-amylase 26 Neutral protease 9 Lipase 11 Cellulase 8 Lysozyme 7 The enzyme with the highest TOC increase rate was α-amylase. Example 1 The same sewage as described in Reference Example 1 was collected and first treated with α-amylase under the same conditions as described in Reference Example 1, and then treated individually with the remaining enzymes. , the results shown in Table 2 were obtained.

【表】 この中で最も高いTOC増加率を示したのは、
中性プロテアーゼを添加した場合であり、他の場
合には、ほとんど差が見られなかつた。 次に、最初にα−アミラーゼ、次に中性プロテ
アーゼで処理した後、リパーゼ、セルラーゼ又は
リゾチームでそれぞれ単独で処理した結果を第3
表に示す。第3表から明らかなとおり、TOC増
分は、三番目に添加する酵素の種類によつてほと
んど差を示さなかつた。
[Table] Among these, the one with the highest TOC increase rate was
This was the case when neutral protease was added, and almost no difference was observed in other cases. Next, after first treating with α-amylase and then with neutral protease, the results of treating each with lipase, cellulase, or lysozyme alone were compared with the third treatment.
Shown in the table. As is clear from Table 3, the TOC increment showed almost no difference depending on the type of enzyme added third.

〔発明の効果〕〔Effect of the invention〕

本発明により、初めに澱粉分解酵素、次いで、
蛋白質分解酵素で処理し、その後、他の酵素で処
理することにより、下水中の有機性浮遊物質の酵
素処理が効率良く進行し、有機性浮遊物質を生物
処理しやすい程度まで可溶化することができる。
According to the invention, first the amylolytic enzyme, then the
By treating with proteolytic enzymes and then with other enzymes, the enzymatic treatment of organic suspended solids in sewage can proceed efficiently, and the organic suspended solids can be solubilized to the extent that they can be easily processed biologically. can.

Claims (1)

【特許請求の範囲】[Claims] 1 下水中に酵素を添加して浮遊有機物質を可溶
化する際に、酵素の添加順序をまず澱粉分解酵
素、次に、蛋白質分解酵素、そしてその他の有機
物分解酵素とすることを特徴とする下水中の有機
性浮遊物質の酵素処理法。
1. A sewage system characterized in that when enzymes are added to sewage to solubilize suspended organic matter, the enzymes are added in the order of starch-degrading enzymes, then proteolytic enzymes, and then other organic matter-degrading enzymes. Enzyme treatment method for organic suspended solids inside.
JP2161087A 1987-01-30 1987-01-30 Enzyme treatment method for organic suspended solids in sewage Granted JPS63190690A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2161087A JPS63190690A (en) 1987-01-30 1987-01-30 Enzyme treatment method for organic suspended solids in sewage

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2161087A JPS63190690A (en) 1987-01-30 1987-01-30 Enzyme treatment method for organic suspended solids in sewage

Publications (2)

Publication Number Publication Date
JPS63190690A JPS63190690A (en) 1988-08-08
JPH0218905B2 true JPH0218905B2 (en) 1990-04-27

Family

ID=12059806

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2161087A Granted JPS63190690A (en) 1987-01-30 1987-01-30 Enzyme treatment method for organic suspended solids in sewage

Country Status (1)

Country Link
JP (1) JPS63190690A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4936994A (en) * 1989-03-13 1990-06-26 Nalco Chemical Company Application of cellulase to control industrial slime

Also Published As

Publication number Publication date
JPS63190690A (en) 1988-08-08

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