JPS62155999A - Method for controlling biological nitrification and denitrification process - Google Patents

Method for controlling biological nitrification and denitrification process

Info

Publication number
JPS62155999A
JPS62155999A JP29844185A JP29844185A JPS62155999A JP S62155999 A JPS62155999 A JP S62155999A JP 29844185 A JP29844185 A JP 29844185A JP 29844185 A JP29844185 A JP 29844185A JP S62155999 A JPS62155999 A JP S62155999A
Authority
JP
Japan
Prior art keywords
nitrogen
denitrification
nitrification
denitrification process
waste water
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
JP29844185A
Other languages
Japanese (ja)
Inventor
Tsuneo Suzuki
恒雄 鈴木
Moriyuki Sumiyoshi
住吉 盛幸
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 Plant Technologies Ltd
Original Assignee
Hitachi Plant Technologies 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 Technologies Ltd filed Critical Hitachi Plant Technologies Ltd
Priority to JP29844185A priority Critical patent/JPS62155999A/en
Publication of JPS62155999A publication Critical patent/JPS62155999A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To permit stable and adequate nitrification and denitrification process by detecting the electrical conductivity in waste water and/or the liquid mixture in a denitrification stage and adjusting the rate of the dilute water to be injected and/or the rate of the waste water to be supplied according to a preset target value. CONSTITUTION:The liquid mixture of a nitrification tank 4 which nitrifies org. or ammonia nitrogen to nitrate nitrogen or nitrite nitrogen is circulated in a denitrification tank 3 which makes denitrification by reducing the nitrogen in the waste water to gaseous nitrogen, by which the nitrogen removal is execut ed. The degree of electrolytic dissociation in the liquid mixture of the tank 3 is detected by an electrical conductivity meter 8 in this stage and a waste water pump 2 is run by a motor revolution control device 9. The device 9 compares the electric signal from the meter 8 and the target value, makes calculation such as proportional integration with the deviation signal there between and controls the speed of a motor. As a result, the ammonia concn. is adjusted to be constant and the nitrification and denitrification process is stably and adequately executed.

Description

【発明の詳細な説明】 1棗上夏程朋分肚 本発明は、廃水中の窒素化合物を生物学的に除去する硝
化脱窒プロセスを好適に進行させる制御方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a control method for suitably proceeding with a nitrification-denitrification process for biologically removing nitrogen compounds from wastewater.

従】顎l支舌 都市下水、畜産汚水等に含まれている窒素化合物を除去
するため、しばしば生物学的硝化脱窒プロセスが利用さ
れている。特に、畜産汚水は高濃度の窒素化合物を含み
、その濃度の変動が激しいのが特徴である。そのため、
大容量の設備で濃度の変動を吸収させるか、又は適度の
希釈水を用いて濃度の調節を行っている。
Biological nitrification-denitrification processes are often used to remove nitrogen compounds contained in municipal sewage, livestock sewage, etc. In particular, livestock wastewater contains a high concentration of nitrogen compounds, and is characterized by large fluctuations in the concentration. Therefore,
Fluctuations in concentration are absorbed by large-capacity equipment, or the concentration is adjusted using appropriate dilution water.

<1゛シよ゛と るI 占 しかし、大容量の設備で濃度を吸収させる場合には、広
い敷地面積を必要とし、不経済である。
However, when absorbing the concentration using large-capacity equipment, a large site area is required, which is uneconomical.

また、希釈水を用いて濃度を調整するのは、煩雑である
ばかりでなく、不安定である。
Further, adjusting the concentration using dilution water is not only complicated but also unstable.

従って、本発明は、廃水の水質の変動に自動的に対応す
ることのでき、硝化脱窒プロセスを安定して好適に行う
ことのできる制御方法を提供することを目的とする。
Therefore, an object of the present invention is to provide a control method that can automatically respond to changes in the quality of wastewater and can perform the nitrification-denitrification process stably and suitably.

刹ILを一゛ るための   び 本発明は、廃水及び脱窒工程の混合液中に存在するアン
モニア濃度が電導度と比例することを見い出し、電導度
が予め設定した目標値になるように希釈水又は原廃水を
供給して、廃水又は脱窒槽内の混合液を一定のアンモニ
ア濃度に調節することによって前記の問題点を解決した
ものである。
In order to increase the IL, the present invention has discovered that the ammonia concentration present in the wastewater and the mixed liquid of the denitrification process is proportional to the electrical conductivity, and the present invention is diluted so that the electrical conductivity reaches a preset target value. This problem is solved by supplying water or raw wastewater and adjusting the ammonia concentration of the wastewater or the mixed liquid in the denitrification tank to a constant ammonia concentration.

即ち、本発明による生物学的硝化脱窒プロセスの制御方
法は、廃水中の窒素を窒素ガスに還元し、脱窒する工程
に、有機性又はアンモニア性窒素を硝酸性窒素或いは亜
硝酸性窒素に硝化する工程の混合液を循環させて、窒素
除去を行う生物学的硝化脱窒プロセスにおいて、廃水及
び/又は脱窒工程の混合液中の電導度を検出し、予め設
定した目標値により希釈水注入量及び/又は廃水の供給
量を調節することを特徴とする。
That is, the biological nitrification-denitrification process control method according to the present invention reduces nitrogen in wastewater to nitrogen gas and converts organic or ammonia nitrogen into nitrate nitrogen or nitrite nitrogen during the denitrification process. In the biological nitrification-denitrification process, in which nitrogen is removed by circulating the mixed solution from the nitrification process, the electrical conductivity in the wastewater and/or the mixed solution from the denitrification process is detected, and the dilution water is adjusted according to a preset target value. It is characterized by adjusting the amount of injection and/or the amount of waste water supplied.

本発明においては、電導度肝を用いて廃水及び/又は脱
窒工程の混合液の電導度を常に測定し、その測定値に応
じて、予め設定した目標型導度になるまで、廃水及び/
又は希釈水を供給できるように制御装置を設ける。
In the present invention, the conductivity of the wastewater and/or the mixed liquid in the denitrification process is constantly measured using a conductivity meter, and according to the measured value, the conductivity of the wastewater and/or the mixed liquid in the denitrification process is measured until the conductivity reaches a preset target type.
Or provide a control device to supply dilution water.

災胤皿 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。
Next, the present invention will be described in detail based on Examples, but the present invention is not limited thereto.

図面は、本発明の実施例を示すものである。The drawings illustrate embodiments of the invention.

第1図は本発明方法の一実施例を示すフローシートであ
る。
FIG. 1 is a flow sheet showing one embodiment of the method of the present invention.

従来の循環型硝化脱窒プロセスにおいては、まず、廃水
貯留槽1に蓄えられた廃水を廃水ポンプ2で脱窒槽3に
流入させ、硝化槽4から循環ポンプ5で戻された硝酸性
又は亜硝酸性の窒素を有機性炭素の存在下に窒素ガスに
還元させる。次に、脱窒槽3で分解されない廃水中に存
在する有機性或いはアンモニア性窒素は、硝化槽4で硝
酸性又は亜硝酸性の窒素に硝化され、脱窒1.曹3へ循
環することにより窒素ガスとして除去される。窒素が除
去された硝化液は、沈澱槽6で固液分離分離され、処理
水は放流され、汚泥は脱窒槽3へ返送ポンプ7で送られ
る。一部の汚泥は余剰汚泥として系外に排出される。
In the conventional circulation type nitrification and denitrification process, first, wastewater stored in a wastewater storage tank 1 is made to flow into a denitrification tank 3 using a wastewater pump 2, and nitrate or nitrous acid is returned from the nitrification tank 4 using a circulation pump 5. The organic nitrogen is reduced to nitrogen gas in the presence of organic carbon. Next, organic or ammonia nitrogen present in the wastewater that is not decomposed in the denitrification tank 3 is nitrified to nitrate or nitrite nitrogen in the nitrification tank 4, and denitrification 1. It is removed as nitrogen gas by circulating to Sodium 3. The nitrified liquid from which nitrogen has been removed is subjected to solid-liquid separation in a settling tank 6, treated water is discharged, and sludge is sent to a denitrification tank 3 by a return pump 7. Some of the sludge is discharged outside the system as surplus sludge.

本発明の循環型硝化脱窒プロセスでは、脱窒槽3の混合
液中の電導度を電導度肝8で検出し、モーター回転制御
装置9を介して廃水ポンプ2を運転する。モーター回転
制御装置9は、電導度肝8からの電気信号と目標値とを
比較し、その偏差信号について比例積分等の演算を行い
、モーターのスピードを制御するものである。この操作
は、0N−OFF動作でも良いが、その場合にはアンモ
ニア負荷の変動が大きくなる。
In the circulating nitrification and denitrification process of the present invention, the conductivity in the mixed liquid in the denitrification tank 3 is detected by the conductivity gauge 8, and the wastewater pump 2 is operated via the motor rotation control device 9. The motor rotation control device 9 compares the electrical signal from the conductivity gauge 8 with a target value, performs calculations such as proportional integral on the deviation signal, and controls the speed of the motor. This operation may be an ON-OFF operation, but in that case, fluctuations in the ammonia load will become large.

第1図に示した装置において、養豚場汚水を処理した時
の脱窒槽3中の混合液の電導度とアンモニア濃度との関
係を調べ、第2図に示す。
In the apparatus shown in FIG. 1, the relationship between the electrical conductivity and ammonia concentration of the mixed liquid in the denitrification tank 3 when pig farm wastewater was treated was investigated and is shown in FIG.

第3図は、本発明の別の実施例を示すもので、第1図に
示した実施例と異なる点は、廃水中の電導度を電導度肝
8で検出し、予め設定した目標値により希釈水量を調節
できるように、電導度肝8を調節計10を介して希釈水
注入弁11と電気的に連動させたことである。
FIG. 3 shows another embodiment of the present invention, which differs from the embodiment shown in FIG. The conductivity gauge 8 is electrically linked to the dilution water injection valve 11 via the controller 10 so that the amount of water can be adjusted.

第4図には、養豚場汚水の電導度とアンモニア濃度との
関係を示す。
FIG. 4 shows the relationship between the electrical conductivity and ammonia concentration of pig farm wastewater.

なお、本発明方法において、第1図に示した方式と第3
図に示した方式を併用してもよく、この場合には更に精
度が向上する。
In addition, in the method of the present invention, the method shown in FIG.
The methods shown in the figure may be used together, and in this case, the accuracy is further improved.

発1F榎近果 本発明方法によれば、取り扱い易いセンサーを用いて、
アンモニア濃度を一定に調節することによって、安定し
た処理水質が得られ、広い敷地面積を必要とせず、簡単
な装置で自動制御できるので、維持管理が容易となる。
According to the method of the present invention, using an easy-to-handle sensor,
By adjusting the ammonia concentration to a constant level, stable treated water quality can be obtained, and since it does not require a large site area and can be automatically controlled with a simple device, maintenance is easy.

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

第1図は、本発明の1実施例を示すフローシート、第2
図は第1図の脱窒槽中の混合液の電導度とアンモニア濃
度との関係図、第3図は本発明の他の実施例を示すフロ
ーシート、第4図は養豚場の汚水の電導度とアンモニア
濃度との関係図である。
FIG. 1 is a flow sheet showing one embodiment of the present invention;
The figure shows the relationship between the electrical conductivity and ammonia concentration of the mixed liquid in the denitrification tank shown in Fig. 1, Fig. 3 is a flow sheet showing another embodiment of the present invention, and Fig. 4 shows the electrical conductivity of sewage from a pig farm. It is a relationship diagram between and ammonia concentration.

Claims (1)

【特許請求の範囲】[Claims] (1)廃水中の窒素を窒素ガスに還元し、脱窒する工程
に、有機性又はアンモニア性窒素を硝酸性窒素或いは亜
硝酸性窒素に硝化する工程の混合液を循環させて、窒素
除去を行う生物学的硝化脱窒プロセスにおいて、廃水及
び/又は脱窒工程の混合液中の電導度を検出し、予め設
定した目標値により希釈水注入量及び/又は廃水の供給
量を調節することを特徴とする生物学的硝化脱窒プロセ
スの制御方法。
(1) In the process of reducing nitrogen in wastewater to nitrogen gas and denitrifying it, circulate the mixed solution of the process of nitrifying organic or ammonia nitrogen to nitrate nitrogen or nitrite nitrogen to remove nitrogen. In the biological nitrification and denitrification process carried out, the electrical conductivity in wastewater and/or the mixed liquid of the denitrification process is detected, and the dilution water injection amount and/or wastewater supply amount is adjusted according to a preset target value. Characteristic control method of biological nitrification-denitrification process.
JP29844185A 1985-12-27 1985-12-27 Method for controlling biological nitrification and denitrification process Pending JPS62155999A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP29844185A JPS62155999A (en) 1985-12-27 1985-12-27 Method for controlling biological nitrification and denitrification process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP29844185A JPS62155999A (en) 1985-12-27 1985-12-27 Method for controlling biological nitrification and denitrification process

Publications (1)

Publication Number Publication Date
JPS62155999A true JPS62155999A (en) 1987-07-10

Family

ID=17859748

Family Applications (1)

Application Number Title Priority Date Filing Date
JP29844185A Pending JPS62155999A (en) 1985-12-27 1985-12-27 Method for controlling biological nitrification and denitrification process

Country Status (1)

Country Link
JP (1) JPS62155999A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0683139A3 (en) * 1994-05-17 1995-11-29 Bfi Entsorgungstech
JP2000015231A (en) * 1998-07-06 2000-01-18 Kubota Corp Method for methane fermentation of organic waste
JP2003024986A (en) * 2001-07-16 2003-01-28 Kurita Water Ind Ltd Biological denitrification method and biological denitrification apparatus
JP2003047990A (en) * 2001-08-02 2003-02-18 Kurita Water Ind Ltd Biological denitrifier
JP2012206017A (en) * 2011-03-29 2012-10-25 Kubota Kankyo Service Kk Method and apparatus for treating wastewater

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0683139A3 (en) * 1994-05-17 1995-11-29 Bfi Entsorgungstech
JP2000015231A (en) * 1998-07-06 2000-01-18 Kubota Corp Method for methane fermentation of organic waste
JP2003024986A (en) * 2001-07-16 2003-01-28 Kurita Water Ind Ltd Biological denitrification method and biological denitrification apparatus
JP2003047990A (en) * 2001-08-02 2003-02-18 Kurita Water Ind Ltd Biological denitrifier
JP2012206017A (en) * 2011-03-29 2012-10-25 Kubota Kankyo Service Kk Method and apparatus for treating wastewater

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