JPH08155491A - Biological denitrification apparatus - Google Patents

Biological denitrification apparatus

Info

Publication number
JPH08155491A
JPH08155491A JP30073594A JP30073594A JPH08155491A JP H08155491 A JPH08155491 A JP H08155491A JP 30073594 A JP30073594 A JP 30073594A JP 30073594 A JP30073594 A JP 30073594A JP H08155491 A JPH08155491 A JP H08155491A
Authority
JP
Japan
Prior art keywords
sludge
denitrification
tank
pipe
denitrification tank
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
Application number
JP30073594A
Other languages
Japanese (ja)
Inventor
Masaichiro Mita
匡一郎 三田
Shozo Nishikawa
正三 西川
Masako Kagiwada
正子 鍵和田
Tetsuro Fukase
哲朗 深瀬
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 JP30073594A priority Critical patent/JPH08155491A/en
Publication of JPH08155491A publication Critical patent/JPH08155491A/en
Pending legal-status Critical Current

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  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)

Abstract

PURPOSE: To prevent sludge in a denitrification tank from floating and to enable stable and efficient denitrification by removing sludge which floated from the denitrification tank in which dirty water is passed through a sludge bed added with elemental sulfur in a upward current, adding a surface active agent to the sludge in a reaction vessel, mixing them, and returning liquid in the reaction vessel to the denitrification tank. CONSTITUTION: In a denitrification apparatus, raw water is introduced from a raw water inflow pipe 2 to the bottom part of a denitrification tank 1 in which a fluidized bed 1A added with elementary sulfur as an electron donor is formed to be denitrified in an upward current. The treated water is removed from the upper part of the tank through a treated water take off pipe 3. In this process, an extraction pipe 4 for floating sludge is placed near the upper part of the fluidized bed 1A, sludge extracted from the pipe 4, after being added with a surfactant in a surfactant storage tank 6 by a pipe 5, is modified in a reaction vessel 7, and the modified sludge is refluxed to the bottom part of the denitrification tank 1 through a pipe 8. In this way, the sludge is prevented from floating and flowing out so that the amount of sludge held in the denitrification tank 1 is kept high.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は硝酸性窒素及び/又は亜
硝酸性窒素を含む汚水(原水)を生物学的に脱窒処理す
る装置に係り、特に、電子供与体として元素状硫黄を添
加した汚泥床に上向流で原水を通水して脱窒処理する装
置において、保持汚泥量を高く維持する生物学的脱窒装
置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a device for biologically denitrifying sewage (raw water) containing nitrate nitrogen and / or nitrite nitrogen, and more particularly to adding elemental sulfur as an electron donor. The present invention relates to a biological denitrification device for maintaining a high retained sludge amount in a device for performing denitrification treatment by passing raw water through an upstream sludge bed.

【0002】[0002]

【従来の技術】従来、し尿、都市下水、その他の窒素含
有有機性廃水を処理する方法として、生物学的硝化脱窒
処理が行われてきた。この生物学的硝化脱窒処理は、原
水中の窒素成分を硝酸イオン又は亜硝酸イオンに生物学
的に硝化する硝化工程と、硝酸イオン又は亜硝酸イオン
を窒素(N2 )に生物学的に還元する脱窒工程とを有し
ている。従来、生物学的脱窒装置としては、脱窒槽内に
汚泥床を形成して原水を上向流通水し、処理水を槽上部
から取り出すものが一般的である。
2. Description of the Related Art Conventionally, biological nitrification denitrification has been performed as a method for treating human waste, municipal wastewater, and other nitrogen-containing organic wastewater. This biological nitrification / denitrification treatment is a nitrification step of biologically nitrifying nitrogen components in raw water into nitrate ions or nitrite ions, and biologically converting nitrate ions or nitrite ions into nitrogen (N 2 ). And a denitrification step of reducing. Conventionally, as a biological denitrification apparatus, a sludge bed is generally formed in a denitrification tank, raw water is upwardly circulated, and treated water is taken out from the upper part of the tank.

【0003】ところで、生物学的脱窒処理においては、
脱窒反応に必要な電子供与体として、メタノール、エタ
ノール、酢酸等の有機物を添加して脱窒細菌の増殖を行
っている。
By the way, in the biological denitrification process,
As electron donors necessary for the denitrification reaction, organic substances such as methanol, ethanol and acetic acid are added to grow the denitrifying bacteria.

【0004】しかし、有機物は、適正な添加量となるよ
うに制御を行う必要がある、余剰汚泥の発生量が多いな
どの不具合があることから、有機物に代る電子供与体と
して、元素状硫黄を添加する方法が提案されている(特
公昭53−9469号公報)。
[0004] However, since the organic matter has such problems that it is necessary to control so that the amount of addition is appropriate and that the amount of excess sludge generated is large, elemental sulfur is used as an electron donor instead of the organic matter. Is proposed (Japanese Patent Publication No. 53-9469).

【0005】[0005]

【発明が解決しようとする課題】前記上向流式脱窒装置
において、電子供与体として元素状硫黄を添加すると、
添加した元素状硫黄に脱窒細菌が付着して増殖し、汚泥
を形成するようになるが、この場合において、汚泥が原
水の上向流で浮上し易くなり、処理水と共に流出し易
く、このため、脱窒槽内の汚泥保持量を高く維持するこ
とができないという問題があった。
In the above-mentioned upflow type denitrification device, when elemental sulfur is added as an electron donor,
Denitrifying bacteria adhere to the added elemental sulfur and proliferate to form sludge, but in this case, the sludge easily floats in the upward flow of raw water and easily flows out together with the treated water. Therefore, there is a problem that the sludge holding amount in the denitrification tank cannot be maintained high.

【0006】本発明は上記従来の問題点を解決し、電子
供与体として元素状硫黄を添加する上向流式脱窒装置に
おいて、汚泥の浮上を防止して、脱窒槽内の汚泥保持量
を高く維持することができる生物学的脱窒装置を提供す
ることを目的とする。
The present invention solves the above-mentioned conventional problems and prevents the sludge from floating in an upflow type denitrification device in which elemental sulfur is added as an electron donor, thereby increasing the sludge retention amount in the denitrification tank. An object of the present invention is to provide a biological denitrification device that can be maintained at a high level.

【0007】[0007]

【課題を解決するための手段】本発明の生物学的脱窒装
置は、元素状硫黄を添加した汚泥床に上向流で硝酸性窒
素及び/又は亜硝酸性窒素を含む汚水を通水する脱窒槽
と、該脱窒槽から浮上した汚泥を取り出す手段と、取り
出した汚泥に界面活性剤を添加混合する反応槽と、該反
応槽の液を脱窒槽に戻す手段とを有することを特徴とす
る。
The biological denitrification device of the present invention passes sewage containing nitrate nitrogen and / or nitrite nitrogen upflow through a sludge bed containing elemental sulfur. A denitrification tank, a means for taking out sludge floating from the denitrification tank, a reaction tank for adding and mixing a surfactant to the taken out sludge, and a means for returning the liquid in the reaction tank to the denitrification tank. .

【0008】[0008]

【作用】元素状硫黄を添加する上向流式脱窒装置におい
て、汚泥が浮上する機構は、脱窒によって発生した窒素
ガスが、疎水性の高い元素状硫黄に付着することによ
り、元素状硫黄を含む汚泥が浮上し易くなるものである
と考えられる。
[Function] In the upward flow type denitrification device for adding elemental sulfur, the mechanism of floating sludge is that the nitrogen gas generated by denitrification adheres to highly hydrophobic elemental sulfur and It is considered that the sludge containing is easily floated.

【0009】本発明においては、浮上した汚泥を脱窒槽
から取り出し、界面活性剤と混合して脱窒槽に返送する
ことにより、界面活性剤の有する湿潤作用で元素状硫黄
に脱窒反応で発生した窒素ガスが付着しにくくなり、汚
泥の浮上が防止される。
In the present invention, the floating sludge is taken out from the denitrification tank, mixed with the surfactant and returned to the denitrification tank, and the elemental sulfur is generated by the denitrification reaction due to the wetting action of the surfactant. Nitrogen gas is less likely to adhere and sludge is prevented from floating.

【0010】[0010]

【実施例】以下、図面を参照して本発明を詳細に説明す
る。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described in detail below with reference to the drawings.

【0011】図1は本発明の生物学的脱窒装置の一実施
例を示す系統図である。
FIG. 1 is a system diagram showing an embodiment of the biological denitrification apparatus of the present invention.

【0012】この脱窒装置は、原水流入配管2より、槽
内に流動床1Aが形成された脱窒槽1の槽底部に原水を
導入して、上向流にて脱窒処理し、処理水を槽上部より
処理水取出配管3を経て取り出すものであり、流動床1
Aの上部近傍位置には浮上汚泥の引抜き配管4が設けら
れている。この引抜き配管4より引き抜かれた汚泥は、
配管5より、界面活性剤貯槽6内の界面活性剤が添加さ
れた後、反応槽7内で界面活性剤と十分に混合される。
反応槽7内で界面活性剤により改質された汚泥は、配管
8を経て原水と共に脱窒槽1の底部に戻される。
In this denitrification apparatus, raw water is introduced from a raw water inflow pipe 2 to the bottom of the denitrification tank 1 in which a fluidized bed 1A is formed in the tank, and the denitrification treatment is performed in an upward flow to obtain treated water. Is taken out from the upper part of the tank through the treated water taking-out pipe 3, and the fluidized bed 1
At a position near the upper part of A, a floating sludge extraction pipe 4 is provided. The sludge drawn from this drawing pipe 4
After the surfactant in the surfactant storage tank 6 is added from the pipe 5, it is sufficiently mixed with the surfactant in the reaction tank 7.
The sludge modified with the surfactant in the reaction tank 7 is returned to the bottom of the denitrification tank 1 together with the raw water via the pipe 8.

【0013】このようにして、浮上した汚泥に界面活性
剤を混合して再び脱窒槽に戻すことにより、汚泥の浮上
及び流出を防止して、脱窒槽内の汚泥保持量を高く維持
することができる。
In this way, by mixing the surface-active agent with the floating sludge and returning it to the denitrification tank again, it is possible to prevent the sludge from floating and flowing out, and to maintain a high sludge retention amount in the denitrification tank. it can.

【0014】なお、ここで添加する界面活性剤としては
特に制限はないが、ポリオキシエチレンソルビタンモノ
オレエート等のノニオン系界面活性剤が好ましく、その
添加量は汚泥容量に対して10mg/l以上、特に20
〜200mg/lとするのが好ましい。
The surfactant to be added here is not particularly limited, but nonionic surfactants such as polyoxyethylene sorbitan monooleate are preferable, and the addition amount thereof is 10 mg / l or more relative to the sludge volume. , Especially 20
It is preferably set to 200 mg / l.

【0015】また、本発明において、電子供与体として
添加する元素状硫黄としては、粒径10〜100μm程
度の硫黄粉末が好適に使用される。硫黄粉末は予め脱窒
槽に種汚泥と共に添加しておくが、脱窒の進行に伴って
消費されるため、必要に応じて随時脱窒槽に補充する。
硫黄粉末の添加量は、通常の場合、除去する窒素の総量
に対して2〜3倍(重量比)程度の割合で添加するのが
好ましい。
In the present invention, as the elemental sulfur added as an electron donor, sulfur powder having a particle size of about 10 to 100 μm is preferably used. Sulfur powder is added to the denitrification tank together with the seed sludge in advance, but it is consumed as the denitrification progresses, so it is replenished to the denitrification tank as needed.
In the usual case, it is preferable to add the sulfur powder in a ratio of about 2 to 3 times (weight ratio) with respect to the total amount of nitrogen to be removed.

【0016】以下に具体的な実施例及び比較例を挙げ
て、本発明をより詳細に説明する。
The present invention will be described in more detail with reference to specific examples and comparative examples.

【0017】実施例1 図1に示す脱窒装置により原水の処理を行った。Example 1 Raw water was treated by the denitrification apparatus shown in FIG.

【0018】脱窒槽(6リットル)内には下水処理場の
活性汚泥3000mg/lを種汚泥として入れると共
に、硫黄粉末(粒径10〜100μm)を200g添加
し、1カ月間脱窒処理を継続した。原水の流量は20m
l/分とし、また、脱窒処理中、浮上汚泥を300ml
/日の割合で取り出し、反応槽にてノニオン系界面活性
剤(ポリオキシエチレンソルビタンモノオレエート)を
100mg/lの割合で添加して混合した後、脱窒槽に
戻した。
In the denitrification tank (6 liters), 3000 mg / l of activated sludge from the sewage treatment plant was added as seed sludge, and 200 g of sulfur powder (particle size 10 to 100 μm) was added to continue denitrification treatment for 1 month. did. The flow rate of raw water is 20m
1 / min, 300 ml of floating sludge during denitrification
The mixture was taken out at a rate of / day, and the nonionic surfactant (polyoxyethylene sorbitan monooleate) was added at a rate of 100 mg / l in the reaction tank and mixed, and then returned to the denitrification tank.

【0019】脱窒処理開始時の脱窒槽内の汚泥量と1ケ
月経過後の脱窒槽内の汚泥量を表1に示す。また、原水
水質及び1ケ月間の処理水の平均水質を表1に示す。
Table 1 shows the amount of sludge in the denitrification tank at the start of denitrification treatment and the amount of sludge in the denitrification tank after one month. Table 1 shows the raw water quality and the average quality of treated water for one month.

【0020】比較例1 実施例1において、汚泥の循環を行わず、即ち、汚泥を
取り出して界面活性剤を添加して返送することなく、そ
の他は同様の条件で処理を行った。
Comparative Example 1 In Example 1, the sludge was not circulated, that is, the sludge was not taken out and the surfactant was added and returned, and the other conditions were the same.

【0021】脱窒処理開始時の脱窒槽内の汚泥量と1ケ
月経過後の脱窒槽内の汚泥量を表1に示す。また、原水
水質及び1ケ月間の処理水の平均水質を表1に示す。
Table 1 shows the amount of sludge in the denitrification tank at the start of denitrification treatment and the amount of sludge in the denitrification tank after 1 month. Table 1 shows the raw water quality and the average quality of treated water for one month.

【0022】[0022]

【表1】 [Table 1]

【0023】表1より、本発明の生物学的脱窒装置によ
れば、汚泥の浮上が防止され、脱窒槽内の汚泥保持量を
高く維持して高水質処理水を得ることができることが明
らかである。
From Table 1, it is clear that according to the biological denitrification apparatus of the present invention, floating of sludge can be prevented, and the sludge retention amount in the denitrification tank can be maintained high to obtain high quality treated water. Is.

【0024】[0024]

【発明の効果】以上詳述した通り、本発明の生物学的脱
窒装置によれば、脱窒槽内の汚泥の浮上を効果的に防止
して脱窒槽内の汚泥保持量を高く維持することができる
ため、安定かつ効率的な脱窒を行うことができる。
As described in detail above, according to the biological denitrification apparatus of the present invention, it is possible to effectively prevent the sludge from floating in the denitrification tank and maintain a high sludge retention amount in the denitrification tank. Therefore, stable and efficient denitrification can be performed.

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

【図1】本発明の生物学的脱窒装置の一実施例を示す系
統図である。
FIG. 1 is a system diagram showing an embodiment of a biological denitrification device of the present invention.

【符号の説明】[Explanation of symbols]

1 脱窒槽 6 界面活性剤貯槽 7 反応槽 1 Denitrification tank 6 Surfactant storage tank 7 Reaction tank

───────────────────────────────────────────────────── フロントページの続き (72)発明者 深瀬 哲朗 東京都新宿区西新宿3丁目4番7号 栗田 工業株式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Tetsuro Fukase 3-4-7 Nishishinjuku, Shinjuku-ku, Tokyo Kurita Industry Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 元素状硫黄を添加した汚泥床に上向流で
硝酸性窒素及び/又は亜硝酸性窒素を含む汚水を通水す
る脱窒槽と、該脱窒槽から浮上した汚泥を取り出す手段
と、取り出した汚泥に界面活性剤を添加混合する反応槽
と、該反応槽の液を脱窒槽に戻す手段とを有することを
特徴とする生物学的脱窒装置。
1. A denitrification tank for passing sewage containing nitrate nitrogen and / or nitrite nitrogen in an upward flow to a sludge bed to which elemental sulfur has been added, and means for removing the sludge floating from the denitrification tank. A biological denitrification apparatus comprising: a reaction tank for adding and mixing a surfactant to the taken out sludge; and means for returning the liquid in the reaction tank to the denitrification tank.
JP30073594A 1994-12-05 1994-12-05 Biological denitrification apparatus Pending JPH08155491A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP30073594A JPH08155491A (en) 1994-12-05 1994-12-05 Biological denitrification apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP30073594A JPH08155491A (en) 1994-12-05 1994-12-05 Biological denitrification apparatus

Publications (1)

Publication Number Publication Date
JPH08155491A true JPH08155491A (en) 1996-06-18

Family

ID=17888478

Family Applications (1)

Application Number Title Priority Date Filing Date
JP30073594A Pending JPH08155491A (en) 1994-12-05 1994-12-05 Biological denitrification apparatus

Country Status (1)

Country Link
JP (1) JPH08155491A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002159993A (en) * 2000-11-27 2002-06-04 Nitchitsu Co Ltd Nitric acid removal treatment equipment
JP2018094553A (en) * 2016-12-14 2018-06-21 一般財団法人畜産環境整備機構 Sulfur material for denitrification

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002159993A (en) * 2000-11-27 2002-06-04 Nitchitsu Co Ltd Nitric acid removal treatment equipment
JP2018094553A (en) * 2016-12-14 2018-06-21 一般財団法人畜産環境整備機構 Sulfur material for denitrification

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