JP2904005B2 - Apparatus and method for removing nitrogen from wastewater - Google Patents
Apparatus and method for removing nitrogen from wastewaterInfo
- Publication number
- JP2904005B2 JP2904005B2 JP11394494A JP11394494A JP2904005B2 JP 2904005 B2 JP2904005 B2 JP 2904005B2 JP 11394494 A JP11394494 A JP 11394494A JP 11394494 A JP11394494 A JP 11394494A JP 2904005 B2 JP2904005 B2 JP 2904005B2
- Authority
- JP
- Japan
- Prior art keywords
- tank
- wastewater
- nitrogen
- denitrification
- nitrification
- 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.)
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Description
【0001】[0001]
【産業上の利用分野】本発明は、廃水中から窒素及びB
OD成分を同時に生物学的に除去する装置及び方法に関
する。BACKGROUND OF THE INVENTION The present invention relates to a method for producing nitrogen and B from wastewater.
An apparatus and method for simultaneously biologically removing OD components.
【0002】[0002]
【従来の技術】廃水中から窒素とBODを同時に除去す
る方法としては、従来、図2に示したように、原水を原
水流入管1から最初沈殿池2に流入させ、ここで固液分
離を行った後、脱窒槽3及び硝化槽5から成る反応槽で
処理するのであるが、硝化槽5で硝化処理された硝化循
環液は硝化液循環ライン9により脱窒槽3へ循環され、
脱窒処理を受け、最終的には窒素成分は窒素ガスとして
廃水中から除去される。処理液は最終沈殿池10で固液
分離された後、処理水11として放流される。2. Description of the Related Art Conventionally, as a method for simultaneously removing nitrogen and BOD from wastewater, as shown in FIG. 2, raw water is introduced from a raw water inflow pipe 1 into a first sedimentation tank 2 where solid-liquid separation is performed. After that, the treatment is performed in a reaction tank consisting of the denitrification tank 3 and the nitrification tank 5. The nitrification circulating liquid nitrified in the nitrification tank 5 is circulated to the denitrification tank 3 by the nitrification liquid circulation line 9,
After being subjected to the denitrification treatment, the nitrogen component is finally removed from the wastewater as nitrogen gas. The treatment liquid is solid-liquid separated in the final sedimentation tank 10 and then discharged as treated water 11.
【0003】都市部の若干の大規模な下水処理場におけ
る流入下水量と、有機物(BOD)や全窒素(T−N)
といった水質成分の濃度を調べたところ、一般に、図3
に例示するように、それらが時間的に同様の変化をして
いることが判った。すなわち、流入水量が多いときに
は、BOD濃度もT−N濃度も高いことが判った。その
ため、従来の方法においては、図4に示すように、流入
下水量及びT−N濃度が最も高くなる時間帯に原水を流
入させ、反応槽の滞留時間分だけ遅れて脱窒槽へ循環さ
れる硝酸態窒素は、既に流量、濃度ともに低下した有機
物(BOD)によって脱窒されることとなり、窒素及び
有機物負荷のそれぞれの1日の平均値では脱窒に必要な
BOD/N比を満たしていても、時間によって有機物の
不足による脱窒不良が発生するという問題があった。[0003] Inflow sewage, organic matter (BOD) and total nitrogen (TN) in some large-scale sewage treatment plants in urban areas
Investigation of the concentration of water quality components such as
It was found that they had similar changes in time as exemplified in FIG. That is, when the amount of inflow water was large, it was found that both the BOD concentration and the TN concentration were high. Therefore, in the conventional method, as shown in FIG. 4, the raw water flows into the denitrification tank at a time when the inflow sewage amount and the TN concentration are highest, and is delayed by the residence time of the reaction tank. Nitrate nitrogen is already denitrified by organic matter (BOD) whose flow rate and concentration have both decreased, and the daily average values of nitrogen and organic matter load satisfy the BOD / N ratio required for denitrification. However, there is a problem that the denitrification failure due to a shortage of organic substances occurs depending on time.
【0004】[0004]
【発明が解決しようとする課題】本発明は、前段の脱窒
槽と後段の硝化槽から成る反応槽で、硝化槽の硝化液を
脱窒槽に循環することにより、廃水中の窒素を生物学的
に除去する廃水の処理において、流入するBOD、T−
Nの負荷が日変動することに起因する、硝酸態窒素が脱
窒されるために必要なBODが脱窒槽において一時的に
不足する現象を解消し、安定して効率的な窒素除去を可
能にすることを目的とする。DISCLOSURE OF THE INVENTION The present invention is a reaction tank comprising a first-stage denitrification tank and a second-stage nitrification tank. By circulating a nitrification solution in the nitrification tank to the denitrification tank, nitrogen in wastewater is biologically removed. BOD, T-
Eliminates the temporary shortage of BOD required for denitrification of nitrate nitrogen in the denitrification tank due to daily fluctuation of N load, and enables stable and efficient nitrogen removal The purpose is to do.
【0005】[0005]
【課題を解決するための手段】本発明による廃水中の窒
素除去装置は、最初沈殿池に流入した廃水を脱窒槽と硝
化槽から成る反応槽で処理し、硝化槽の硝化液を脱窒槽
に循環することにより、廃水中の窒素を生物学的に除去
する廃水中の窒素除去装置において、原水流入管に流量
計を備え、さらに、最初沈殿池をバイパスして脱窒槽へ
原水を直接流入させうるバイパスラインを付設したこと
を特徴とする。The apparatus for removing nitrogen from wastewater according to the present invention treats wastewater that first flows into a sedimentation basin in a reaction tank consisting of a denitrification tank and a nitrification tank, and converts the nitrification liquid in the nitrification tank into a denitrification tank. In a wastewater nitrogen removal device that biologically removes nitrogen in wastewater by circulating, a raw water inflow pipe is equipped with a flow meter, and the raw water is directly introduced into the denitrification tank, bypassing the first sedimentation basin. And a bypass line.
【0006】また、本発明による廃水中の窒素除去方法
は、最初沈殿池に流入した廃水を脱窒槽と硝化槽から成
る反応槽で処理し、硝化槽の硝化液を脱窒槽に循環する
ことにより、廃水中の窒素を生物学的に除去する廃水中
の窒素除去方法において、原水流入量を常時測定して、
測定流入量から脱窒に必要な有機物の不足時間帯を予測
し、その時間帯にバイパスラインにより原水を脱窒槽へ
直接流入させるバイパス流量を制御することを特徴とす
る。In addition, the method for removing nitrogen from wastewater according to the present invention comprises treating wastewater that first flows into a sedimentation basin in a reaction tank comprising a denitrification tank and a nitrification tank, and circulating the nitrification liquid in the nitrification tank to the denitrification tank. In a nitrogen removal method for wastewater that biologically removes nitrogen in wastewater, the amount of raw water inflow is constantly measured,
It is characterized in that a shortage time period of the organic matter necessary for denitrification is predicted from the measured inflow amount, and a bypass flow rate in which the raw water flows directly into the denitrification tank by the bypass line during that time period.
【0007】[0007]
【実施例】次に、図面を参照して、本発明の実施例につ
いて説明する。図1は、本発明の一実施例を示す廃水中
の窒素除去装置の系統図である。図1に示した装置にお
いて、窒素及びBOD成分を含む廃水は、原水流入管1
より最初沈殿池2で固液分離を受ける。このときBOD
成分に比較して窒素成分は、大部分が溶存態であるた
め、除去率は低い。その後、廃水は、下部に散気装置6
を有する硝化槽5内で硝化され、硝化循環液は硝化液循
環ライン9により脱窒槽3に戻される。廃水は、脱窒槽
3で脱窒され、窒素成分は窒素ガスとして除去される。
窒素を除去された廃水は、最終沈殿池10で固液分離さ
れ、処理水11として放流される。Next, an embodiment of the present invention will be described with reference to the drawings. FIG. 1 is a system diagram of an apparatus for removing nitrogen from wastewater showing one embodiment of the present invention. In the apparatus shown in FIG. 1, wastewater containing nitrogen and BOD components is supplied to a raw water inflow pipe 1.
First, solid-liquid separation is performed in the sedimentation tank 2. At this time BOD
Since the nitrogen component is mostly in a dissolved state as compared with the component, the removal rate is low. After that, the waste water is placed in the lower part of the diffuser 6
The nitrification circulating liquid is returned to the denitrification tank 3 through the nitrification liquid circulating line 9. Wastewater is denitrified in the denitrification tank 3, and nitrogen components are removed as nitrogen gas.
The wastewater from which nitrogen has been removed is solid-liquid separated in the final sedimentation basin 10 and discharged as treated water 11.
【0008】都市部の大規模な下水処理場の場合、図3
に示したとおり、廃水の流入量と、窒素及びBOD成分
の濃度は同時に上昇するため、本発明においては、図1
に示したように、原水流入管1に流量計4を設置し、こ
の流量計4で流入量を測定することにより、過去の廃水
流入量データによって流入量の時間的なピークを推定す
ることを可能とした。これと、過去の変動パターンの結
果から、脱窒槽3における有機物不足の時間帯(図3に
おける斜線部分)を予測し、この時間帯にバイパスライ
ン7により最初沈殿池2をバイパスさせることにより必
要な有機物量を補うことができる。最初沈殿池での窒素
除去率は、元来、比較的低いため、バイパスによる窒素
負荷の上昇は起こらない。これにより、流入水質の負荷
変動に係わらず、終日安定した窒素除去及びBOD除去
を効率よく行うことが可能となる。In the case of a large-scale sewage treatment plant in an urban area, FIG.
As shown in FIG. 1, since the inflow of wastewater and the concentrations of nitrogen and BOD components increase simultaneously, in the present invention, FIG.
As shown in the figure, by installing a flow meter 4 in the raw water inflow pipe 1 and measuring the inflow with the flow meter 4, it is possible to estimate the temporal peak of the inflow from past wastewater inflow data. Made it possible. From this and the results of the past fluctuation patterns, a time zone in which the organic matter is insufficient in the denitrification tank 3 (shaded area in FIG. 3) is predicted, and during this time, the first sedimentation basin 2 is required to be bypassed by the bypass line 7. The amount of organic matter can be supplemented. Since the nitrogen removal rate in the primary sedimentation basin is relatively low by nature, no increase in nitrogen load due to bypass occurs. This makes it possible to efficiently perform stable nitrogen removal and BOD removal throughout the day irrespective of load fluctuations in the inflow water quality.
【0009】最終沈殿池10の底部に沈殿する汚泥は、
一部は返送汚泥ライン12より脱窒槽3へ返送し、残り
は、余剰汚泥排出管13より排出する。The sludge settled at the bottom of the final settling basin 10 is:
A part is returned to the denitrification tank 3 from the return sludge line 12, and the rest is discharged from an excess sludge discharge pipe 13.
【0010】[0010]
【発明の効果】流入廃水量、廃水中の窒素及びBOD成
分濃度の変動が、相乗的に作用して、日平均や時間平均
の水質から計算すれば化学量論的な脱窒への必要有機物
量を満足している廃水でも、時間的に脱窒が不十分な部
分が発生する現象を防止し、安定して効率のよい窒素除
去を行うことができる。According to the present invention, fluctuations in the amount of inflowing wastewater, the concentration of nitrogen and BOD components in the wastewater act synergistically, and when calculated from daily or hourly average water quality, necessary organic substances for stoichiometric denitrification are obtained. Even if the amount of wastewater satisfies the amount, the phenomenon that a portion where denitrification is insufficient in time is prevented from occurring, and stable and efficient nitrogen removal can be performed.
【図1】本発明の一実施例を示す廃水中の窒素除去装置
の系統図である。FIG. 1 is a system diagram of an apparatus for removing nitrogen from wastewater showing one embodiment of the present invention.
【図2】従来の廃水中の窒素除去装置の系統図である。FIG. 2 is a system diagram of a conventional apparatus for removing nitrogen from wastewater.
【図3】一般的下水処理場における下水流入量とBOD
及びT−N濃度の経時変化を示すグラフである。Fig. 3 Sewage inflow and BOD in a general sewage treatment plant
6 is a graph showing the change over time of the TN concentration.
【図4】流入BOD及びT−Nと必要BODの経時変化
を示すグラフである。FIG. 4 is a graph showing changes over time of inflow BOD and TN and required BOD.
1 原水流入管 2 最初沈殿池 3 脱窒槽 4 流量計 5 硝化槽 7 バイパスライン 9 硝化液循環ライン 10 最終沈殿池 11 処理水 DESCRIPTION OF SYMBOLS 1 Raw water inflow pipe 2 First settling tank 3 Denitrification tank 4 Flow meter 5 Nitrification tank 7 Bypass line 9 Nitrification liquid circulation line 10 Final settling tank 11 Treated water
───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 昭62−132597(JP,A) (58)調査した分野(Int.Cl.6,DB名) C02F 3/28 - 3/34 ──────────────────────────────────────────────────続 き Continuation of the front page (56) References JP-A-62-132597 (JP, A) (58) Field surveyed (Int. Cl. 6 , DB name) C02F 3/28-3/34
Claims (2)
化槽から成る反応槽で処理し、硝化槽の硝化液を脱窒槽
に循環することにより、廃水中の窒素を生物学的に除去
する廃水中の窒素除去装置において、原水流入管に流量
計を備え、さらに、最初沈殿池をバイパスして脱窒槽へ
原水を直接流入させうるバイパスラインを付設したこと
を特徴とする廃水中の窒素除去装置。1. Nitrogen in wastewater is biologically removed by treating wastewater flowing into a sedimentation basin in a reaction tank comprising a denitrification tank and a nitrification tank, and circulating a nitrification solution in the nitrification tank to the denitrification tank. A nitrogen removal device for wastewater, comprising a flow meter in a raw water inflow pipe, and a bypass line capable of directly flowing raw water into a denitrification tank by bypassing a sedimentation tank. Removal device.
化槽から成る反応槽で処理し、硝化槽の硝化液を脱窒槽
に循環することにより、廃水中の窒素を生物学的に除去
する廃水中の窒素除去方法において、原水流入量を常時
測定して、測定流入量から脱窒に必要な有機物の不足時
間帯を予測し、その時間帯にバイパスラインにより原水
を脱窒槽へ直接流入させるバイパス流量を制御すること
を特徴とする廃水中の窒素除去方法。2. Nitrogen in biological wastewater is biologically removed by treating wastewater flowing into a sedimentation basin in a reaction tank comprising a denitrification tank and a nitrification tank, and circulating a nitrification solution in the nitrification tank to the denitrification tank. In the method of removing nitrogen from wastewater, the raw water inflow is constantly measured, and the time of shortage of the organic matter required for denitrification is predicted from the measured inflow, and during that time, the raw water flows directly into the denitrification tank via the bypass line A method for removing nitrogen from wastewater, comprising controlling a bypass flow rate to be removed.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11394494A JP2904005B2 (en) | 1994-04-28 | 1994-04-28 | Apparatus and method for removing nitrogen from wastewater |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11394494A JP2904005B2 (en) | 1994-04-28 | 1994-04-28 | Apparatus and method for removing nitrogen from wastewater |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH07290089A JPH07290089A (en) | 1995-11-07 |
JP2904005B2 true JP2904005B2 (en) | 1999-06-14 |
Family
ID=14625121
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP11394494A Expired - Fee Related JP2904005B2 (en) | 1994-04-28 | 1994-04-28 | Apparatus and method for removing nitrogen from wastewater |
Country Status (1)
Country | Link |
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JP (1) | JP2904005B2 (en) |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP5467837B2 (en) * | 2009-10-09 | 2014-04-09 | 三菱電機株式会社 | Control device for biological water treatment equipment |
JP5651384B2 (en) * | 2010-06-18 | 2015-01-14 | 株式会社クボタ | Sewage treatment equipment, sewage treatment method, and method for renovating sewage treatment equipment |
JP5575211B2 (en) * | 2012-11-29 | 2014-08-20 | 三菱電機株式会社 | Control device for biological water treatment equipment |
JP5826328B2 (en) * | 2014-05-26 | 2015-12-02 | 三菱電機株式会社 | Control device for biological water treatment equipment |
JP5791762B2 (en) * | 2014-05-26 | 2015-10-07 | 三菱電機株式会社 | Control device for biological water treatment equipment |
JP5791763B2 (en) * | 2014-05-26 | 2015-10-07 | 三菱電機株式会社 | Control device for biological water treatment equipment |
-
1994
- 1994-04-28 JP JP11394494A patent/JP2904005B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
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JPH07290089A (en) | 1995-11-07 |
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