JPH07328691A - Nitrification reaction accelerating method utilizing sedimentation tank sludge of sewage treating equipment by immersed filter bed method - Google Patents
Nitrification reaction accelerating method utilizing sedimentation tank sludge of sewage treating equipment by immersed filter bed methodInfo
- Publication number
- JPH07328691A JPH07328691A JP15909494A JP15909494A JPH07328691A JP H07328691 A JPH07328691 A JP H07328691A JP 15909494 A JP15909494 A JP 15909494A JP 15909494 A JP15909494 A JP 15909494A JP H07328691 A JPH07328691 A JP H07328691A
- Authority
- JP
- Japan
- Prior art keywords
- tank
- nitrogen
- filter bed
- sludge
- contact aeration
- 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.)
- Pending
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
- Biological Treatment Of Waste Water (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】この発明は、生物膜法の一方法で
ある浸漬ろ床法を利用した汚水処理施設で、窒素の高度
処理設備を有する施設に利用できる硝化反応促進方法で
す。[Field of Industrial Application] The present invention is a method for promoting nitrification reaction which can be used in a sewage treatment facility that uses a submerged filter method, which is one of the biofilm methods, and that has facilities for advanced nitrogen treatment.
【0002】[0002]
【従来の技術】浸漬ろ床法を利用した窒素除去の高度処
理法は、接触ばっ気槽内で、アンモニア態窒素が硝酸態
窒素に変わる硝化反応を利用し、硝酸態化した窒素を脱
窒反応が進行する嫌気性ろ床槽に返送して脱窒をはかる
ことになっている。しかし、接触ばっ気槽内での硝化活
性が低く、硝化反応が進みにくいため、嫌気性ろ床槽内
での窒素除去率が低い。2. Description of the Related Art A high-level treatment method for nitrogen removal using a dipping filter method is to denitrify nitrated nitrogen by utilizing a nitrification reaction in which ammonia nitrogen is converted to nitrate nitrogen in a contact aeration tank. It is supposed to be returned to the anaerobic filter tank where the reaction progresses for denitrification. However, since the nitrification activity in the contact aeration tank is low and the nitrification reaction is difficult to proceed, the nitrogen removal rate in the anaerobic filter tank is low.
【0003】[0003]
【発明が解決しようとする課題】この発明は、いままで
硝化反応が進みにくかった点を解消して、窒素除去の高
度処理を確実にすることを目的としている。DISCLOSURE OF THE INVENTION The present invention aims to solve the problem that the nitrification reaction has been difficult to proceed until now, and to ensure a high degree of nitrogen removal treatment.
【0004】[0004]
【課題を解決するための手段】この発明の硝化促進方法
は、沈澱槽汚泥の持つ硝化活性を利用するために、接触
ばっ気槽に沈澱槽汚泥を返送して、嫌気性ろ床槽から送
られてくるアンモニア態窒素を含んだ汚水と混合、浮遊
せしめ、接触ばっ気槽内の硝化反応を高めることを特徴
とする。The method for promoting nitrification of the present invention utilizes the nitrification activity of the sludge in the sedimentation tank, so that the sludge in the sedimentation tank is returned to the contact aeration tank and is sent from the anaerobic filter bed tank. It is characterized in that it is mixed with the sewage containing ammonia nitrogen and is floated to enhance the nitrification reaction in the contact aeration tank.
【0005】[0005]
【作用】接触ばっ気槽は、ろ材に付着した生物膜のみ
で、硝化活性が低いため、アンモニア態窒素の硝化が進
みにくい。このため、本来は、汚泥濃縮貯留槽へ移送す
る沈澱槽汚泥の持つ硝化活性に着目し、沈澱槽汚泥を接
触ばっ気槽に返送して浮遊せしめ、接触ばっ気槽内の硝
化活性を高めることにより、硝化反応の促進が可能とな
り、接触ばっ気槽内で硝酸態化した窒素を嫌気性ろ床槽
に返送する工程を経て、窒素除去の高度処理が確実にで
きるようになった。[Function] The contact aeration tank has only a biofilm attached to the filter medium and has a low nitrification activity, so that nitrification of ammonia nitrogen is difficult to proceed. Therefore, originally, paying attention to the nitrifying activity of the sedimentation tank sludge that is transferred to the sludge concentration storage tank, the sedimentation tank sludge is returned to the contact aeration tank and floated to enhance the nitrification activity in the contact aeration tank. As a result, the nitrification reaction can be promoted, and the advanced treatment of nitrogen removal can be ensured through the process of returning the nitrated nitrogen in the contact aeration tank to the anaerobic filter tank.
【0006】[0006]
【実施例】沈澱槽汚泥を接触ばっ気槽第1室に返送する
経路を設置し、接触ばっ気槽内の活性汚泥沈澱率を、硝
化活性が最も発現する20%程度になるよう制御して実
施した。従前の水質状況は、流入原水のアンモニア態窒
素 24mg/l、亜硝酸態窒素<0、01mg/l、
硝酸態窒素 0、5mg/l、に対して、沈澱槽流出水
質は、アンモニ態窒素 19、5mg/l、亜硝酸態窒
素 0、36mg/l、硝酸態窒素4、3mg/lであ
った。本発明の設備を設置した後の水質状況は、流入原
水のアンモニア態窒素 29、4mg/l亜硝酸態窒素
<0、01mg/l、硝酸態窒素 <0、5mg/
l、に対して、沈澱槽流出水質は、アンモニア態窒素
<0、1mg/l、亜硝酸態窒素 0、11mg/l、
硝酸態窒素 17、5mg/lとなり、硝化反応が確実
に進むことが、確認できた。[Example] A route for returning the sludge from the settling tank to the first chamber of the contact aeration tank was set up, and the sedimentation rate of the activated sludge in the contact aeration tank was controlled to about 20% at which the nitrification activity was most expressed. Carried out. The conventional water quality was as follows: Ammonia nitrogen 24 mg / l, Nitrite nitrogen <0, 01 mg / l,
With respect to nitrate nitrogen of 0 and 5 mg / l, the effluent quality of the precipitation tank was ammonia nitrogen of 19 and 5 mg / l, nitrite nitrogen of 0 and 36 mg / l, and nitrate nitrogen of 4 and 3 mg / l. The water quality after installing the equipment of the present invention is as follows: ammonium nitrogen 29, 4 mg / l nitrite nitrogen <0, 01 mg / l, nitrate nitrogen <0, 5 mg /
1, the water quality of the settling tank is ammonia nitrogen.
<0, 1 mg / l, nitrite nitrogen 0, 11 mg / l,
It was confirmed that the nitrate nitrogen was 17, 5 mg / l, and the nitrification reaction proceeded reliably.
【0007】[0007]
【発明の効果】この発明は、従来、汚水処理方法の一方
法である浸漬ろ床法による脱窒効果には、限界があると
されていたが、本発明をシステム化することにより、浮
遊生物法と遜色ない程度にまで、高めることができ、既
設汚水処理場への適用はもとより、新設施設への適用に
より、公共水域への栄養塩類の負荷の削減が図れ、環境
保全に大きく寄与できる。According to the present invention, the denitrification effect of the immersion filter method, which is one of the methods for treating wastewater, has been limited in the past. However, by systematizing the present invention, floating organisms are suspended. It can be increased to a level comparable to the law, and it can be applied not only to existing sewage treatment plants, but also to new facilities, reducing the load of nutrient salts on public water bodies and contributing greatly to environmental conservation.
【図1】 生物膜法の一方法である浸漬ろ床法を利用し
た汚水処理施設処理フロー図[Fig. 1] Flow chart of sewage treatment facility treatment using the immersion filter method, which is one of the biofilm methods
Claims (1)
触ばっ気槽内の硝化反応の促進を図り、嫌気性ろ床槽内
での窒素除去を高める方法1. A method for enhancing the removal of nitrogen in an anaerobic filter bed tank by utilizing the nitrification activity of a settling tank sludge to promote the nitrification reaction in the contact aeration tank.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15909494A JPH07328691A (en) | 1994-06-06 | 1994-06-06 | Nitrification reaction accelerating method utilizing sedimentation tank sludge of sewage treating equipment by immersed filter bed method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15909494A JPH07328691A (en) | 1994-06-06 | 1994-06-06 | Nitrification reaction accelerating method utilizing sedimentation tank sludge of sewage treating equipment by immersed filter bed method |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH07328691A true JPH07328691A (en) | 1995-12-19 |
Family
ID=15686113
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP15909494A Pending JPH07328691A (en) | 1994-06-06 | 1994-06-06 | Nitrification reaction accelerating method utilizing sedimentation tank sludge of sewage treating equipment by immersed filter bed method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH07328691A (en) |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH02284695A (en) * | 1989-04-26 | 1990-11-22 | Unitika Ltd | Treatment of waste water |
-
1994
- 1994-06-06 JP JP15909494A patent/JPH07328691A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH02284695A (en) * | 1989-04-26 | 1990-11-22 | Unitika Ltd | Treatment of waste water |
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