JPS587359B2 - Denitrification equipment for water treatment - Google Patents
Denitrification equipment for water treatmentInfo
- Publication number
- JPS587359B2 JPS587359B2 JP54096248A JP9624879A JPS587359B2 JP S587359 B2 JPS587359 B2 JP S587359B2 JP 54096248 A JP54096248 A JP 54096248A JP 9624879 A JP9624879 A JP 9624879A JP S587359 B2 JPS587359 B2 JP S587359B2
- Authority
- JP
- Japan
- Prior art keywords
- tank
- nitrogen
- water
- detected value
- oxidation
- 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
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
- Biological Treatment Of Waste Water (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Description
【発明の詳細な説明】
本発明は、窒素加合物を酸化した後還元して窒素ガスと
して除去する反応を同時的に行なわせる水処理用脱窒装
置に関し、所望の脱窒処理の制御を容易確実に行なわせ
られるようにする事を目的とする。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a denitrification device for water treatment that simultaneously performs a reaction in which a nitrogen compound is oxidized and then reduced to be removed as nitrogen gas. The purpose is to make it easy and reliable.
次に、本発明の実施例を図面に基いて詳述する。Next, embodiments of the present invention will be described in detail based on the drawings.
窒素加合物を含有する被処理水の供給管1を処理槽2の
長手方向一端側に接続すると共に、槽2の他端側に脱窒
処理水をオーバーフローによって取出す管3を接続し、
前記処理槽2の内部に、その底部で連通する隔壁4……
を槽2の長手方向に間隔をへだてて設けて、直列的に接
続された複数の区画空間5……を槽2の内部に形成し、
それら区画空間5……の夫々に、上向きのガス吐出ノズ
ルを備えたパイプ6をその底部側でかつ一側壁寄りに配
設すると共に、酸素ガス含有の空気供給装置7からの分
岐供給管8……を前記パイプ6の夫夫に接続して、もっ
て酸素含有ガスの供給によって窒素含有水を槽内で一方
向に旋回させると共に、取出管3からの処理水の取出し
によって窒素含有水を取出管3側に流動させるようにし
、かつその旋回流動する窒素含有水に酸素ガスを溶存さ
せるようにしてある。A supply pipe 1 for water to be treated containing a nitrogen compound is connected to one longitudinal end of a treatment tank 2, and a pipe 3 for taking out denitrified water by overflow is connected to the other end of the tank 2.
A partition wall 4 communicating with the inside of the processing tank 2 at its bottom...
are provided at intervals in the longitudinal direction of the tank 2 to form a plurality of compartment spaces 5 connected in series inside the tank 2,
A pipe 6 equipped with an upward gas discharge nozzle is disposed in each of the divided spaces 5 on the bottom side and near one side wall, and a branch supply pipe 8 from an oxygen gas-containing air supply device 7 is provided. ... is connected to the husband and wife of the pipe 6, whereby the nitrogen-containing water is swirled in one direction in the tank by supplying oxygen-containing gas, and the nitrogen-containing water is taken out by taking out the treated water from the take-out pipe 3. The nitrogen-containing water is made to flow toward the third side, and oxygen gas is dissolved in the nitrogen-containing water flowing in a swirling manner.
そして、前記供給管8……の夫々に酸素含有ガスの供給
量を制御する弁9を介装すると共に、各区画空間5……
の夫々においてその槽内の窒素含有水の酸化還元電位(
以下ORPと略称する。A valve 9 for controlling the supply amount of oxygen-containing gas is installed in each of the supply pipes 8, and each compartment space 5...
The oxidation-reduction potential of the nitrogen-containing water in the tank (
Hereinafter, it will be abbreviated as ORP.
)を検出する装置10を配設して、この酸化還元電位検
出装置10からの検出値に基く前記弁9の制御装置11
によって酸素含有ガスの供給量を調節させて、前記酸化
還元電位検出装置10によるORP検出値を設定範囲に
自動的に維持させるように構成してある。), and a control device 11 for the valve 9 based on the detected value from the oxidation-reduction potential detection device 10.
The supply amount of the oxygen-containing gas is adjusted by the oxidation-reduction potential detection device 10 to automatically maintain the ORP detection value within a set range.
第1と第2および第3の区画空間5……に、前記取出管
3からの処理水を返送供給する管12を接続すると共に
、各供給管12に処理水の返送量を制御する弁13を介
装し、かつ各区画空間5……の夫々においてその槽内の
窒素含有水の水素指数(以下pHと略称する。A pipe 12 for returning and supplying the treated water from the take-out pipe 3 is connected to the first, second and third compartment spaces 5..., and a valve 13 for controlling the amount of returned treated water is connected to each supply pipe 12. interposed, and in each compartment space 5, the hydrogen index (hereinafter abbreviated as pH) of the nitrogen-containing water in the tank is determined.
)を検出する装置14を設けて、水素指数検出装置14
からの検出値に基く前記制御弁13の制御装置15によ
って処理水の返送量を調節させて、前記水素指数検出装
置14によるpH検出値を設定範囲に自動的に維持させ
るように構成してある。) is provided, and a hydrogen index detection device 14 is provided.
The control device 15 of the control valve 13 adjusts the amount of returned treated water based on the value detected by the hydrogen index detector 14, and the pH value detected by the hydrogen index detector 14 is automatically maintained within a set range. .
前記区画空間5……の夫々に、前記パイプ6からの供給
空気に対する上向き流路を形成する状態で、かつ槽底壁
との間に間隔を形成する状態で網状体16を張設し、こ
の網状体16による区画域に、見掛け容積当りの接液面
積を可及的大にする例えばプラスチック製などの板状や
筒状の多数の担体を充填し、かつその担体に活性汚泥を
付着させておき、もって前記制御装置11,15によっ
て窒素含有水のORP並びにpHを自動的に設定範囲に
維持させる条件下において、活性汚泥を付着させた担体
の充填層に窒素含有水を繰返し旋回接触させる事により
、その間に同一担体に付着の活性汚泥によって含有窒素
分の酸化及びその酸化窒素の還元の両方を同時に進行さ
せて、水中の窒素加合物を確実容易に窒素ガスとして水
から除去させるようにしてある。A net-like body 16 is stretched in each of the divided spaces 5 to form an upward flow path for the air supplied from the pipe 6 and to form a gap with the bottom wall of the tank. A large number of plate-shaped or cylindrical carriers made of plastic or the like are filled in the divided area formed by the net-like body 16 to maximize the area in contact with the liquid per apparent volume, and activated sludge is attached to the carriers. Then, under conditions where the control devices 11 and 15 automatically maintain the ORP and pH of the nitrogen-containing water within the set range, the nitrogen-containing water is repeatedly brought into contact with the packed bed of the carrier to which the activated sludge is adhered. During this time, the activated sludge adhering to the same carrier causes both the oxidation of the nitrogen content and the reduction of the nitrogen oxides to proceed at the same time, so that the nitrogen additives in the water are surely and easily removed from the water as nitrogen gas. There is.
即ち、充填担体に付着の活性汚泥によって、その液相側
の好気性条件下にある活性汚泥層部分で酸化の反応を行
なわせると共に、担体側の嫌気性条件下にある活性汚泥
層部分において還元の反応を行なわせるもので、その窒
素含有水のORPレベルを酸化反応にとって好条件下に
おく事によって窒素含有水の十分な酸化処理を促進させ
、以後の良好な脱窒処理を行なわせられ、勿論、ORP
レベルが低い値であっても、担体の充填固定床に対する
水の相対接触効率が高いので、実質的に液相側の活性汚
泥層部分におけるORPのレベルが高い条件下になって
いて、良好な酸化反応を行なわせられ、単に活性汚泥を
遊流動させる酸化処理ではORPを極めてシビアに設定
する制御が必要であるが、それに比べてORPの制御範
囲を顕著に拡大でき、制御上極めて有利な状態で酸化反
応処理を行なわせられる。In other words, the activated sludge adhering to the packed carrier causes an oxidation reaction to occur in the activated sludge layer under aerobic conditions on the liquid phase side, and reduction in the activated sludge layer under anaerobic conditions on the carrier side. By placing the ORP level of the nitrogen-containing water under favorable conditions for the oxidation reaction, sufficient oxidation treatment of the nitrogen-containing water is promoted, and subsequent good denitrification treatment can be performed. Of course, ORP
Even if the level is low, the relative contact efficiency of water with the packed fixed bed of carrier is high, so the ORP level in the activated sludge layer part on the liquid phase side is substantially high, resulting in a favorable condition. Oxidation treatment in which an oxidation reaction is carried out and activated sludge is simply allowed to flow freely requires very strict control of ORP, but compared to this, the control range of ORP can be significantly expanded, and this is an extremely advantageous state in terms of control. An oxidation reaction treatment can be performed.
そして、pHレベルの変動は脱窒処理にとって悪影響を
及ぼすが、処理水の返送供給によってpHレベルを設定
範囲に維持させる事によって、前述の活性汚泥による脱
窒処理を確実容易に行なわせられ、その上、pHレベル
並びにORPレベルを設定通りに自動的に維持させるの
で、何ら人為操作を要する事なく適確な処理を所望通り
に行なわせられる。Fluctuations in pH level have a negative effect on denitrification treatment, but by maintaining the pH level within the set range by returning treated water, the denitrification treatment using activated sludge described above can be carried out reliably and easily. Moreover, since the pH level and ORP level are automatically maintained as set, appropriate treatment can be performed as desired without any manual operation.
尚、窒素含有水としてゴミ埋立浸出汚水を対象にし、そ
して第1区画空間5におけるORPを−50〜±0mv
にかつpHを7. 0 〜7. 5に設定し、第2区画
空間5におけるORPを±5.0mvにかつpHを7.
0〜8.0に設定し、第3区画空間5におけるORPを
+50〜+100mVにかつpHを6,5〜7.5に設
定し、第4区画空間5におけるORPを+100mv以
上にかつpHを6. 5 〜7. 0に設定したところ
、所望通りの十分な脱窒結果が得られた。Note that the nitrogen-containing water is wastewater leached from a garbage landfill, and the ORP in the first compartment space 5 is set to -50 to ±0 mv.
and pH 7. 0 to 7. 5, the ORP in the second compartment space 5 is set to ±5.0 mv, and the pH is set to 7.0 mv.
0 to 8.0, the ORP in the third compartment space 5 is set to +50 to +100 mV and the pH is set to 6.5 to 7.5, and the ORP in the fourth compartment space 5 is set to +100 mV or more and the pH is set to 6. .. 5-7. When it was set to 0, sufficient denitrification results were obtained as desired.
また、pH調整のための処理水の返送として、窒素含有
水の供給量に対してそれの0.5〜5倍量の範囲で制御
した時に安定的効率の良い処理が行なえたもので、好ま
しくはその範囲を制御範囲に設定する。In addition, when returning treated water for pH adjustment, stable and efficient treatment was possible when the amount of nitrogen-containing water supplied was controlled within the range of 0.5 to 5 times the supplied amount, which is preferable. sets that range as the control range.
尚、隔壁4による槽2の区画にあって、それの区画数に
制限は無く、また区画する事なく実施するも良く、そし
て区画を施す場合、区画空間5に対して各別にあるいは
所定のものに選択的に検出装置10,14及び自動制御
装置11.15を付設すれば良い。Note that there is no limit to the number of divisions in the tank 2 by the partition wall 4, and it may be done without partitioning, and when partitioning is done, each partition space 5 may be divided separately or in a predetermined manner. Detection devices 10, 14 and automatic control devices 11, 15 may be selectively attached to the device.
また、担体を充填固定床としたが、それを槽内で窒素含
有水とともに対流する流動床とするも良く、またその床
厚さを調節するように構成するも良く、このように固定
床あるいは流動床にした担体に活性汚泥を付着させる事
によって、活性汚泥を浮遊させるタイプのように活性汚
泥の返送が不要になり、運転が容易になると共にランニ
ングコストの節減を図れる。In addition, although the carrier is a packed fixed bed, it may also be a fluidized bed that convects with nitrogen-containing water in a tank, or it may be configured to adjust the bed thickness. By adhering the activated sludge to a carrier in the form of a fluidized bed, there is no need to return the activated sludge unlike the type in which activated sludge is suspended, making operation easier and reducing running costs.
以上要するに本発明による水処理用脱窒装置は、活性汚
泥を付着させた担体を槽内に収容させ、前記槽内の窒素
含有水の酸化還元電位及び水素指数を検出する装置を設
け、前記酸化還元電位検出装置からの検出値に基いてそ
の検出値を設定範囲に維持すべく前記槽内の窒素含有水
への酸素含有ガス供給量を自動的に制御する装置を設け
、前記水素指数検出装置からの検出値に基いてその検出
値を設定範囲に維持すべく前記槽への処理水返送量を自
動的に制御する装置を設けてある事を特徴とする。In summary, the denitrification device for water treatment according to the present invention accommodates a carrier to which activated sludge is attached in a tank, is provided with a device for detecting the oxidation-reduction potential and hydrogen index of the nitrogen-containing water in the tank, and A device is provided for automatically controlling the amount of oxygen-containing gas supplied to the nitrogen-containing water in the tank in order to maintain the detected value within a set range based on the detected value from the reduction potential detecting device, and the hydrogen index detecting device The apparatus is characterized in that a device is provided for automatically controlling the amount of treated water returned to the tank based on the detected value from the tank in order to maintain the detected value within a set range.
即ち、活性汚泥を担体に付着させて窒素含有水に接触さ
せて、酸化還元電位の制御範囲を顕著に拡大させると共
に、その酸化還元電位と水素指数を、所望の反応を良好
に維持させるに足る条件に自動的に設定させる事によっ
て、殊に酸化還元電位の制御を容易にした状態で十分な
酸化処理を行なわせるとともに、水素指数の制御により
良好な脱窒処理を促進させられるようになり、その上、
従来必要とした活性汚泥の返送を省略でき、処理工程の
簡略化も図れるようになった。That is, by adhering activated sludge to a carrier and bringing it into contact with nitrogen-containing water, the control range of redox potential can be significantly expanded, and the redox potential and hydrogen index can be maintained at a level sufficient to maintain the desired reaction. By automatically setting the conditions, it is possible to perform sufficient oxidation treatment with easy control of the oxidation-reduction potential in particular, and to promote good denitrification treatment by controlling the hydrogen index. On top of that,
This eliminates the need to return activated sludge, which was previously required, and simplifies the treatment process.
図面は本発明に係る水処理用脱窒装置の実施例を示し、
第1図は全体縦断側面図、第2図は第1図の■−■線断
面図である。
2……槽、5……区画空間、10……酸化還元電位検出
装置、11……酸素含有ガス供給量自動制御装置、14
……水素指数検出装置、15……処理水返送量自動制御
装置。The drawings show an embodiment of the denitrification device for water treatment according to the present invention,
FIG. 1 is an overall longitudinal sectional side view, and FIG. 2 is a sectional view taken along the line ■--■ in FIG. 1. 2...tank, 5...compartment space, 10...oxidation-reduction potential detection device, 11...oxygen-containing gas supply amount automatic control device, 14
...Hydrogen index detection device, 15...Automatic control device for the amount of returned treated water.
Claims (1)
記槽2内の窒素含有水の酸化還元電位及び水素指数を検
出する装置10,14を設け、前記酸化還元電位検出装
置10からの検出値に基いてその検出値を設定範囲に維
持すべく前記槽2内の窒素含有水への酸素含有ガス供給
量を自動的に制御する装置11を設け、前記水素指数検
出装置14からの検出値に基いてその検出値を設定範囲
に維持すべく前記槽2への処理水返送量ネ自動的に制御
する装置15を設けてある事を特徴とする水処理用脱窒
装置。 2 前記槽2の内部に、直列に接続された複数の区画空
間5……を形成し、前記両検出装置10,14及び両自
動制御装置11,15を前記区画空間5……に対して各
別に付設してある事を特徴とする特許請求の範囲第1項
に記載の水処理用脱窒装置。[Scope of Claims] 1. A carrier to which activated sludge is attached is housed in a tank 2, and devices 10 and 14 are provided for detecting the oxidation-reduction potential and hydrogen index of the nitrogen-containing water in the tank 2, and the oxidation-reduction A device 11 is provided that automatically controls the amount of oxygen-containing gas supplied to the nitrogen-containing water in the tank 2 based on the detected value from the potential detection device 10 in order to maintain the detected value within a set range, and the hydrogen index The dewatering device for water treatment is characterized in that it is equipped with a device 15 that automatically controls the amount of treated water returned to the tank 2 based on the detected value from the detection device 14 in order to maintain the detected value within a set range. Nitrogen equipment. 2 A plurality of compartment spaces 5 connected in series are formed inside the tank 2, and both the detection devices 10 and 14 and both automatic control devices 11 and 15 are connected to each compartment space 5. The denitrification device for water treatment according to claim 1, characterized in that it is separately attached.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP54096248A JPS587359B2 (en) | 1979-07-27 | 1979-07-27 | Denitrification equipment for water treatment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP54096248A JPS587359B2 (en) | 1979-07-27 | 1979-07-27 | Denitrification equipment for water treatment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5621688A JPS5621688A (en) | 1981-02-28 |
| JPS587359B2 true JPS587359B2 (en) | 1983-02-09 |
Family
ID=14159909
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP54096248A Expired JPS587359B2 (en) | 1979-07-27 | 1979-07-27 | Denitrification equipment for water treatment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS587359B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0773706B2 (en) * | 1987-03-17 | 1995-08-09 | 新日本製鐵株式会社 | Wastewater treatment method |
| JP5097024B2 (en) * | 2008-06-17 | 2012-12-12 | シャープ株式会社 | Water treatment apparatus and water treatment method |
-
1979
- 1979-07-27 JP JP54096248A patent/JPS587359B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5621688A (en) | 1981-02-28 |
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