JP2833888B2 - Operating method of aeration device - Google Patents
Operating method of aeration deviceInfo
- Publication number
- JP2833888B2 JP2833888B2 JP27000591A JP27000591A JP2833888B2 JP 2833888 B2 JP2833888 B2 JP 2833888B2 JP 27000591 A JP27000591 A JP 27000591A JP 27000591 A JP27000591 A JP 27000591A JP 2833888 B2 JP2833888 B2 JP 2833888B2
- Authority
- JP
- Japan
- Prior art keywords
- aerobic
- anaerobic
- aerator
- aerators
- sewage
- 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 - Lifetime
Links
- 238000005273 aeration Methods 0.000 title claims description 19
- 238000011017 operating method Methods 0.000 title 1
- 238000005276 aerator Methods 0.000 claims description 35
- 238000000034 method Methods 0.000 claims description 7
- 239000010865 sewage Substances 0.000 description 14
- 230000002093 peripheral effect Effects 0.000 description 6
- 239000010802 sludge Substances 0.000 description 6
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 238000013019 agitation Methods 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 238000009423 ventilation Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 238000010564 aerobic fermentation Methods 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 230000001546 nitrifying effect Effects 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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
- Activated Sludge Processes (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は複数台の曝気機を個別的
に運転制御することにより無終端水路内に好気と嫌気と
の状態を形成して汚水の硝化、脱窒を効率的に行う曝気
装置の運転方法に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention efficiently controls nitrification and denitrification of sewage by controlling the operation of a plurality of aerators individually to form aerobic and anaerobic conditions in an endless waterway. The present invention relates to a method of operating an aeration apparatus.
【0002】[0002]
【従来の技術】生活汚水、産業廃棄汚水等の有機物質を
含有する汚水の処理において、長円形・円形等の二重円
形水路の如く、循環水路、いわゆる無終端水路を形成し
た曝気槽内に1または複数の曝気装置を設置し、この槽
内の汚水中に空気を強制的に供給し、空気中の酸素を汚
水中に溶存させて、かつ汚水をこの空気と混合しつつ撹
拌して曝気、即ち好気性発酵処理を行う方法が提案され
ている。そしてこの曝気により有機物の分解を行い、汚
水を浄化している。2. Description of the Related Art In the treatment of sewage containing organic substances such as domestic sewage and industrial waste sewage, an aeration tank having a circulating water channel, that is, a so-called non-terminal water channel, such as a double circular water channel such as an ellipse or a circle. One or more aeration devices are installed, air is forcibly supplied to the sewage in the tank, oxygen in the air is dissolved in the sewage, and the sewage is mixed with the air and stirred to aerate. That is, a method of performing an aerobic fermentation treatment has been proposed. The aeration decomposes organic matter to purify sewage.
【0003】[0003]
【発明が解決しようとする課題】従って汚水中の有機物
を好気性発酵にて処理できても、汚水中の窒素分の除
去、即ち脱窒をも行うためには常に酸素を供給するだけ
でなく、嫌気状態とすることも必要である。同一の曝気
槽内で曝気、即ち好気状態と嫌気状態を形成するには槽
内に於ける曝気機の運転を制御する必要がある。このた
め、一台の曝気機に通気弁を設け、この弁を開閉操作す
ることにより好気と嫌気との運転を可能としている。し
かしこの好気・嫌気兼用機では好気運転から嫌気運転へ
の切り替えには曝気機の運転を停止して行っているた
め、汚水の撹拌も停止し、汚泥が沈降する。このうち汚
泥が槽底に沈降すると硝化液と流入水中の炭素源と活性
汚泥の効率は接触が行えず、充分な脱窒が行えない。ま
た好気・嫌気兼用機で、その通気弁の開閉にて好気と嫌
気とを切り換える場合には単に弁の開閉操作のみであ
る。このため、好気運転時に比べ、嫌気運転時には汚水
の撹拌は強くなくてもよいが、一台の曝気機では好気運
転に合わせて同じ撹拌力にて嫌気運転をするため、動力
の損失が大となる。Therefore, even if organic matter in sewage can be treated by aerobic fermentation, not only oxygen is always supplied but also nitrogen is removed in sewage to remove nitrogen, that is, denitrify. It is also necessary to be in an anaerobic state. In order to form aeration in the same aeration tank, that is, to form an aerobic state and an anaerobic state, it is necessary to control the operation of the aerator in the tank. For this reason, a ventilation valve is provided in one aerator, and aerobic and anaerobic operation is enabled by opening and closing this valve. However, in this aerobic / anaerobic combined machine, the operation of the aerator is stopped when switching from the aerobic operation to the anaerobic operation, so that the agitation of the sewage is stopped and the sludge settles. When the sludge settles at the bottom of the tank, the efficiency of the nitrifying liquid, the carbon source in the influent and the activated sludge cannot be brought into contact, and sufficient denitrification cannot be performed. When switching between aerobic and anaerobic by opening and closing the ventilation valve in the aerobic / anaerobic combined machine, it is merely an opening and closing operation of the valve. Therefore, compared to the aerobic operation, the sewage does not need to be strongly agitated during the anaerobic operation, but a single aerator performs the anaerobic operation with the same agitation power in accordance with the aerobic operation. It will be great.
【0004】本発明は好気・嫌気運転の撹拌力を調整
し、各運転状況に最適な撹拌力で運転することを目的と
する。[0004] It is an object of the present invention to adjust the agitation power for aerobic / anaerobic operation and to operate with an agitation power optimal for each operation situation.
【0005】[0005]
【課題を解決するための手段】本発明は上記目的を達成
するためになしたもので、好気運転と嫌気運転とを切替
可能な曝気機と、好気運転のみを行う好気専用曝気機と
を組み合わせて曝気槽内に設けると共に、好気運転時に
は双方の曝気機を好気運転し、嫌気運転時には切替可能
な曝気機を嫌気運転とし、他の好気専用曝気機を停止す
ることにより、脱窒を促進するようになしたことを要旨
とする。SUMMARY OF THE INVENTION The present invention has been made to achieve the above object, and has an aerator capable of switching between aerobic operation and anaerobic operation, and an aerobic exclusive aerator for performing only aerobic operation. In addition to installing in the aeration tank in combination with aerobic operation, aerobic operation of both aerators during aerobic operation, anaerobic operation of switchable aerators during anaerobic operation, and stopping other aerobic dedicated aerators The point is that denitrification is promoted.
【0006】[0006]
【作用】一つの曝気槽に好気専用の曝気機と、好気・嫌
気切替可能な曝気機を一組として設置する。そして好気
運転時には双方の曝気機を好気運転し、嫌気運転時には
切替可能な曝気機を嫌気運転とし、他の好気専用曝気機
を停止する。これにより嫌気運転時にも最小の動力にて
槽底に所要流速を得られ、汚泥が沈降するのを防止し、
硝化液と流入水中の炭素源と活性汚泥の効率は接触が行
えるので効率的に、かつ安定した脱窒が行える。[Function] A single aeration tank is provided with an aerator dedicated to aerobic and an aerator capable of switching between aerobic and anaerobic. During the aerobic operation, both aerators are aerobically operated, and during the anaerobic operation, the switchable aerator is set as the anaerobic operation, and the other aerobic-dedicated aerators are stopped. This allows the required flow velocity to be obtained at the bottom of the tank with minimum power even during anaerobic operation, preventing sludge from settling,
The efficiency of the nitrification liquid, the carbon source in the influent water, and the activated sludge can be brought into contact, so that efficient and stable denitrification can be performed.
【0007】[0007]
【実施例】以下本発明曝気装置の運転方法を図示の実施
例に基づいて説明する。図において1は図示の如く円形
をした、もしくは長円形をした無終端水路を形成した曝
気槽で、この所要容量を有する曝気槽1の任意位置に、
例えば円形曝気槽1の中心を通る半径線上に、かつ水路
方向に平行にして水路の内周側に好気・嫌気運転兼用型
の曝気機3を、外周側に好気専用型の曝気機2を配設す
る。BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a block diagram showing the operation of an aeration apparatus according to the present invention. In the drawing, reference numeral 1 denotes an aeration tank having a circular or oval endless channel formed as shown in the figure.
For example, an aerator 3 for both aerobic and anaerobic operation is provided on the inner peripheral side of the water channel on a radial line passing through the center of the circular aeration tank 1 and parallel to the water channel direction, and an aerial device 2 for aerobic only is provided on the outer peripheral side. Is arranged.
【0008】上述の如く2台の曝気機2,3を一組とし
て配置する場合、この2台の曝気機2,3を同時に運転
または同時に停止して運転すると図2に示すような溶存
酸素(DO)の変化を示す。また2台の曝気機2,3の
うち一方を連続運転し、他方を運転・停止を繰り返す
と、図3のようなDO変化を示す。しかし嫌気運転時に
は好気専用機2を停止し、兼用機3の通気弁を閉じて運
転すると図4に示すようなDO変化を得る。When the two aerators 2 and 3 are arranged as a set as described above, if the two aerators 2 and 3 are simultaneously operated or stopped and operated at the same time, the dissolved oxygen (FIG. 2) shown in FIG. DO). When one of the two aerators 2 and 3 is continuously operated and the other is repeatedly operated and stopped, a DO change as shown in FIG. 3 is exhibited. However, during the anaerobic operation, when the aerobic dedicated machine 2 is stopped and the ventilation valve of the combined use machine 3 is closed to operate, a DO change as shown in FIG. 4 is obtained.
【0009】このようにして2台の曝気機2,3を運転
する場合、好気時間比をT−N除去率を示したグラフを
図5に示す。従って従来の運転方法に比べ、脱窒速度は
1.2〜1.5倍となり、脱窒率は80%以上となる。FIG. 5 is a graph showing the aerobic time ratio and the TN removal rate when the two aerators 2 and 3 are operated in this manner. Accordingly, the denitrification rate becomes 1.2 to 1.5 times and the denitrification rate becomes 80% or more as compared with the conventional operation method.
【0010】好気・嫌気兼用型の曝気機3を無終端水路
の内周側に設置する場合、槽内を好気または嫌気いずれ
の運転時でも水路内周側の汚水は常に撹拌されているの
で、内周側にも所定流速を常に確保でき、汚泥の沈澱を
未然に防止できる利点がある。しかし長円形等の水路で
は、いずれ側に設置してもよいし、また円形水路でも汚
水の種別によっては兼用型を外周側に設置することも可
能である。When the aerobic / anaerobic type aerator 3 is installed on the inner peripheral side of the endless water channel, the sewage on the inner peripheral side of the water channel is constantly stirred regardless of whether the inside of the tank is operated aerobically or anaerobically. Therefore, there is an advantage that a predetermined flow rate can always be secured on the inner peripheral side, and sludge sedimentation can be prevented. However, in the case of an elliptical channel or the like, it may be installed on any side, and in the case of a circular channel, a combined type may be installed on the outer peripheral side depending on the type of sewage.
【0011】[0011]
【発明の効果】本発明曝気装置の運転方法は好気運転と
嫌気運転とを切替可能な曝気機と、好気運転のみを行う
好気専用曝気機とを組み合わせて曝気槽内に設けると共
に、好気運転時には双方の曝気機を好気運転し、嫌気運
転時には切替可能な曝気機を嫌気運転とし、他の好気専
用曝気機を停止するようになしているため、槽底に汚泥
が沈澱することなく、安定して効率的に脱窒が行える利
点を有する。According to the method of operating the aeration apparatus of the present invention, a combination of an aerator capable of switching between aerobic operation and anaerobic operation and an aerator dedicated to aerobic operation is provided in an aeration tank. During aerobic operation, both aerators are operated aerobically, during anaerobic operation, switchable aerators are set to anaerobic operation, and other aerobic-only aerators are stopped. This has the advantage that denitrification can be performed stably and efficiently without performing.
【図1】本発明曝気装置の運転方法を説明する一実施例
の平面図である。FIG. 1 is a plan view of one embodiment for explaining a method of operating an aeration apparatus of the present invention.
【図2】2台の曝気機を同時に運転または停止した場合
のDO変化を示すグラフ図である。FIG. 2 is a graph showing a change in DO when two aerators are simultaneously operated or stopped.
【図3】2台の曝気機の一方を連続、他方を間歇運転し
た場合のDO変化を示すグラフ図である。FIG. 3 is a graph showing DO changes when one of two aerators is operated continuously and the other is operated intermittently.
【図4】本発明曝気装置の運転方法によるDO変化を示
すグラフ図である。FIG. 4 is a graph showing a DO change according to a method of operating the aeration apparatus of the present invention.
【図5】T−N除去率を示すグラフ図である。FIG. 5 is a graph showing a TN removal rate.
1 曝気槽 2 好気・嫌気兼用型曝気機 3 好気専用型曝気機 DESCRIPTION OF SYMBOLS 1 Aeration tank 2 Aerobic / anaerobic combined type aerator 3 Aerobic exclusive type aerator
Claims (1)
機と、好気運転のみを行う好気専用曝気機とを組み合わ
せて曝気槽内に設けると共に、好気運転時には双方の曝
気機を好気運転し、嫌気運転時には切替可能な曝気機を
嫌気運転とし、他の好気専用曝気機を停止することによ
り、脱窒を促進するようになしたことを特徴とする曝気
装置の運転方法。An aerator capable of switching between aerobic operation and anaerobic operation and an aerobic exclusive aerator for performing only aerobic operation are provided in an aeration tank in combination, and both aerators are used during aerobic operation. Operation of an aeration apparatus characterized in that aerobic operation is performed, and an aerator that can be switched during an anaerobic operation is set as an anaerobic operation, and denitrification is promoted by stopping other aerobic-dedicated aerators. Method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP27000591A JP2833888B2 (en) | 1991-09-20 | 1991-09-20 | Operating method of aeration device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP27000591A JP2833888B2 (en) | 1991-09-20 | 1991-09-20 | Operating method of aeration device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH05104091A JPH05104091A (en) | 1993-04-27 |
| JP2833888B2 true JP2833888B2 (en) | 1998-12-09 |
Family
ID=17480230
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP27000591A Expired - Lifetime JP2833888B2 (en) | 1991-09-20 | 1991-09-20 | Operating method of aeration device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2833888B2 (en) |
-
1991
- 1991-09-20 JP JP27000591A patent/JP2833888B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH05104091A (en) | 1993-04-27 |
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