JPH0919698A - Advanced treatment of waste water - Google Patents

Advanced treatment of waste water

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Publication number
JPH0919698A
JPH0919698A JP19113895A JP19113895A JPH0919698A JP H0919698 A JPH0919698 A JP H0919698A JP 19113895 A JP19113895 A JP 19113895A JP 19113895 A JP19113895 A JP 19113895A JP H0919698 A JPH0919698 A JP H0919698A
Authority
JP
Japan
Prior art keywords
activated carbon
tank
organic matter
denitrification
wastewater
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
JP19113895A
Other languages
Japanese (ja)
Inventor
Tetsuji Miyabayashi
哲司 宮林
Naomichi Mori
直道 森
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 JP19113895A priority Critical patent/JPH0919698A/en
Publication of JPH0919698A publication Critical patent/JPH0919698A/en
Pending legal-status Critical Current

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

Abstract

PROBLEM TO BE SOLVED: To provide an advanced treatment method capable of simultaneously and efficiently removing organic matters and nitrogen from waste water without adding a hydrogen donor from the outside in a denitrifying process even though a denitrifying tank following a nitration tank is installed. SOLUTION: In a method for removing organic matters and nitrogen from the waste water containing organic matters and nitrogen with a nitration process and subsequently with a denitrifying process, the organic matters in the waste water is preliminarily adsorbed with activated carbon in a organic matter adsorbing tank 3 and the waste water is introduced into the nitration tank 4 and the activated carbon adsorbed the organic matters is introduced into the denitrifying tank 6, and the organic matters adsorbed on the activated carbon is utilized as the hydrogen donor required for the denitrification.

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、有機物及び窒素を含有
する廃水の高度処理法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an advanced treatment method for wastewater containing organic matter and nitrogen.

【0002】[0002]

【従来の技術】廃水中の有機物及び窒素の処理方法とし
ては、生物学的方法である循環式硝化脱窒法が一般的で
ある。反応槽は、脱窒槽及び硝化槽から構成され、有機
物及び窒素を含有する廃水は、脱窒槽に流入する。脱窒
槽流出槽は硝化槽に流入し、廃水中のアンモニア性窒素
(NH4 −N)は硝化細菌により硝酸性窒素(NO3
N)に変換(硝化)される。硝化された混合液は脱窒槽
に循環され、そこで混合液中のNO3 −Nは脱窒細菌に
より廃水中の有機物を水素供与体として窒素ガスに変換
され、廃水から窒素は除去される。また、廃水中の有機
物は、脱窒槽で脱窒に利用されると共に、硝化槽で酸化
分解され、廃水から除去される。しかしながら、この方
法では脱窒槽の後段に硝化槽が設置されているため、N
3 −Nを完全に脱窒することはできず、処理水中にN
3 −Nが残留する。
2. Description of the Related Art As a method for treating organic matters and nitrogen in wastewater, a circulation type nitrification denitrification method which is a biological method is generally used. The reaction tank is composed of a denitrification tank and a nitrification tank, and wastewater containing organic matter and nitrogen flows into the denitrification tank. The denitrification tank outflow tank flows into the nitrification tank, and the ammonia nitrogen (NH 4 —N) in the wastewater is converted into nitrate nitrogen (NO 3 −) by nitrifying bacteria.
N) is converted (nitrification). The nitrified mixed liquid is circulated to a denitrification tank, where NO 3 -N in the mixed liquid is converted into nitrogen gas by denitrifying bacteria using organic matter in the wastewater as a hydrogen donor, and nitrogen is removed from the wastewater. Further, the organic matter in the wastewater is used for denitrification in the denitrification tank, and is also oxidized and decomposed in the nitrification tank to be removed from the wastewater. However, in this method, since the nitrification tank is installed after the denitrification tank, N
O 3 -N cannot be completely denitrified, and N 3
O 3 -N remains.

【0003】同様に生物学的方法である内生脱窒法は、
硝化槽の後段に脱窒槽が設置されている。この方法で
は、循環式硝化脱窒法より処理水中の総窒素濃度、すな
わちNH4 −N、NO3 −N及びNO2 −Nの総和を低
くすることができるが、脱窒に必要な有機物が前段の硝
化槽で酸化処理されてしまい、脱窒速度が小さくなると
いう問題点があった。そこで、脱窒速度を大きくするた
めにメタノール等を添加する場合もある。
The endogenous denitrification method, which is also a biological method, is
A denitrification tank is installed after the nitrification tank. In this method, the total nitrogen concentration in the treated water, that is, the sum of NH 4 —N, NO 3 —N and NO 2 —N, can be made lower than in the circulating nitrification denitrification method, but the organic matter necessary for denitrification is However, there was a problem that the denitrification rate was reduced because the nitrification tank was oxidized. Therefore, methanol or the like may be added to increase the denitrification rate.

【0004】[0004]

【発明が解決しようとする課題】本発明は、硝化槽の後
に脱窒槽を設置した廃水の処理装置においても、脱窒工
程において外部から水素供与体を添加することなく廃水
から有機物及び窒素を同時に効率よく除去しうる廃水の
高度処理法を提供することを目的とする。
DISCLOSURE OF THE INVENTION The present invention is also applicable to a wastewater treatment apparatus having a denitrification tank installed after a nitrification tank, in which organic substances and nitrogen are simultaneously discharged from the wastewater without adding a hydrogen donor from the outside in the denitrification process. It is an object to provide an advanced treatment method for wastewater that can be efficiently removed.

【0005】[0005]

【課題を解決するための手段】本発明は、廃水を硝化処
理する前に活性炭により有機物を吸着させ、この有機物
吸着活性炭を脱窒処理に供給し、その有機物を脱窒に必
要な水素供与体として利用することによって上記課題を
解決したものである。すなわち、本発明による廃水の高
度処理法は、有機物及び窒素を含有する廃水から硝化工
程、次いで脱窒工程によって有機物及び窒素を除去する
方法において、廃水中の有機物を予め活性炭に吸着さ
せ、この有機物を吸着した活性炭を脱窒工程に導入し、
活性炭に吸着された有機物を脱窒に必要な水素供与体と
して利用することを特徴とする。
According to the present invention, an organic substance is adsorbed by activated carbon before nitrification treatment of wastewater, the activated carbon adsorbing the organic substance is supplied to a denitrification treatment, and the hydrogen donor necessary for denitrification of the organic substance. The above problem is solved by using the above. That is, the advanced treatment method of wastewater according to the present invention is a method of removing organic matter and nitrogen from wastewater containing organic matter and nitrogen by a nitrification step, and then a denitrification step, by adsorbing organic matter in the wastewater to activated carbon in advance, Introduce the activated carbon that has absorbed the denitrification process,
It is characterized in that the organic matter adsorbed on the activated carbon is used as a hydrogen donor necessary for denitrification.

【0006】本発明による廃水の高度処理法を実施する
際には、有機物吸着槽、硝化槽及び脱窒槽をこの順序に
設置した処理装置を使用する。有機物吸着槽には活性炭
を充填しておき、ここで有機物を活性炭に吸着除去した
廃水を硝化槽に導入する。硝化槽内では硝化処理により
有機性窒素及びアンモニア性窒素は、酸化されて硝酸性
窒素となる。次いで、硝化混合液を脱窒槽へ導入し、脱
窒菌により硝酸性窒素を窒素ガスに変え、脱窒するが、
脱窒には水素供与体として有機物の存在が必要である。
そこで、本発明においては、有機物吸着槽で有機物を吸
着した活性炭を脱窒槽へ投入し、この活性炭に吸着され
ていた有機物を脱窒に必要な水素供与体として利用す
る。
When carrying out the advanced treatment method of wastewater according to the present invention, a treatment apparatus in which an organic matter adsorption tank, a nitrification tank and a denitrification tank are installed in this order is used. Activated carbon is filled in the organic matter adsorption tank, and the wastewater in which the organic matter is adsorbed and removed by the activated carbon is introduced into the nitrification tank. In the nitrification tank, organic nitrogen and ammonia nitrogen are oxidized to nitric acid by nitrification. Next, the nitrification mixture is introduced into a denitrification tank, and nitrate nitrogen is changed to nitrogen gas by denitrifying bacteria to denitrify,
Denitrification requires the presence of organic matter as a hydrogen donor.
Therefore, in the present invention, activated carbon that has adsorbed the organic substance in the organic substance adsorption tank is put into the denitrification tank, and the organic substance adsorbed by the activated carbon is used as a hydrogen donor necessary for denitrification.

【0007】本発明によれば、硝化槽の後段に脱窒槽が
設置されているため、理論的には処理水窒素濃度をゼロ
にすることができる。また、脱窒に必要な有機物は硝化
槽の前段で活性炭に吸着され、脱窒槽に投入されるた
め、脱窒速度は内生脱窒法の脱窒速度より大きく、循環
式硝化脱窒法の脱窒速度と同程度である。しかも、硝化
の後で脱窒を効率良く進行させることができ、その際脱
窒槽に有機物を添加する必要がない。
According to the present invention, since the denitrification tank is installed in the latter stage of the nitrification tank, theoretically, the nitrogen concentration of the treated water can be made zero. In addition, since the organic substances necessary for denitrification are adsorbed on the activated carbon in the front stage of the nitrification tank and put into the denitrification tank, the denitrification rate is higher than the denitrification rate of the endogenous denitrification method, Similar to speed. Moreover, denitrification can be efficiently advanced after nitrification, and at that time, it is not necessary to add an organic substance to the denitrification tank.

【0008】また、脱窒槽で使用された活性炭は、有機
物吸着槽へ返送して再使用することができる。このと
き、返送する活性炭になお有機物が多量に残存すること
が考えられる場合には、活性炭を直接、有機物吸着槽へ
返送しないで、一旦硝化槽へ返送し、ここで残留有機物
を酸化分解した後、有機物吸着槽へ返送するのが好まし
い。これにより活性炭の吸着能が充分に回復してから有
機物吸着槽へ返送されるので、活性炭の破過を防止する
ことができる。
The activated carbon used in the denitrification tank can be returned to the organic matter adsorption tank for reuse. At this time, if it is considered that a large amount of organic matter still remains in the activated carbon to be returned, the activated carbon is not directly returned to the organic matter adsorption tank, but is once returned to the nitrification tank where the residual organic matter is oxidatively decomposed. It is preferable to return it to the organic substance adsorption tank. As a result, the adsorbing ability of the activated carbon is sufficiently recovered and then returned to the organic substance adsorption tank, so that the breakthrough of the activated carbon can be prevented.

【0009】さらに、本発明の高度処理法は、活性炭を
有機物吸着槽と脱窒槽の両方に充填しておき、廃水の流
下方向を切り替えることによって有機物及び窒素を効率
よく除去することもできる。すなわち、処理槽を第1活
性炭槽、硝化槽及び第2活性炭槽の順序に配列し、第1
活性炭槽で有機物を吸着させ、硝化槽で硝化処理し、次
いで第2活性炭槽で脱窒処理を行い、所定時間経過後に
原水を第2活性炭槽に導入し、ここで活性炭に有機物を
吸着させ、次いで硝化処理し、第1活性炭槽で脱窒処理
を行う。このように廃水の流下方向を所定時間毎に切り
替えることによって活性炭を移動することなく、廃水中
の有機物及び窒素を効率よく除去することができる。
Further, according to the advanced treatment method of the present invention, activated carbon is filled in both the organic matter adsorption tank and the denitrification tank, and the flowing direction of the wastewater can be switched to efficiently remove the organic matter and nitrogen. That is, the treatment tanks are arranged in the order of the first activated carbon tank, the nitrification tank, and the second activated carbon tank.
Organic matter is adsorbed in the activated carbon tank, nitrification is performed in the nitrification tank, and then denitrification is performed in the second activated carbon tank. After a predetermined time, raw water is introduced into the second activated carbon tank, where the organic matter is adsorbed by the activated carbon, Next, nitrification is performed, and denitrification is performed in the first activated carbon tank. In this way, by switching the flow direction of the wastewater every predetermined time, it is possible to efficiently remove the organic matter and nitrogen in the wastewater without moving the activated carbon.

【0010】[0010]

【実施例】次に、図面を参照して本発明を実施例に基づ
いて詳細に説明する。図1は、本発明の廃水の高度処理
法の第一の実施例を示す系統図である。図1において、
廃水は、原水導入管1により活性炭2が充填されている
有機物吸着槽3に導入される。有機物を吸着除去された
廃水は、次いで硝化槽4に導入され、廃水中の有機性窒
素及びアンモニア性窒素は酸化されて硝酸性窒素とな
る。有機物吸着槽3で廃水中の有機物を吸着した活性炭
2は、活性炭移送管5により硝化槽4の後段にもっちさ
れた脱窒槽6に移送される。脱窒槽6において、脱窒菌
は硝化槽4から流入する硝酸性窒素を、活性炭2に吸着
されている有機物を利用して脱窒する。脱窒された廃水
は、排水管7から処理水として排水される。一方、有機
物を脱窒に利用した活性炭2は、活性炭返送管8により
有機物吸着槽3に返送される。この実施例によれば、脱
窒槽に有機物を添加することなく、高い脱窒速度で効率
よく脱窒を行うことができる。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Next, the present invention will be described in detail based on embodiments with reference to the drawings. FIG. 1 is a system diagram showing a first embodiment of the advanced wastewater treatment method of the present invention. In FIG.
The waste water is introduced into the organic matter adsorption tank 3 filled with the activated carbon 2 through the raw water introduction pipe 1. The wastewater from which the organic substances have been adsorbed and removed is then introduced into the nitrification tank 4, and the organic nitrogen and ammonia nitrogen in the wastewater are oxidized to nitrate nitrogen. The activated carbon 2 that has adsorbed the organic matter in the wastewater in the organic matter adsorption tank 3 is transferred by the activated carbon transfer pipe 5 to the denitrification tank 6 provided at the subsequent stage of the nitrification tank 4. In the denitrification tank 6, the denitrification bacteria denitrify the nitrate nitrogen flowing from the nitrification tank 4 by using the organic matter adsorbed on the activated carbon 2. The denitrified waste water is discharged from the drain pipe 7 as treated water. On the other hand, the activated carbon 2 used for denitrifying the organic matter is returned to the organic matter adsorption tank 3 through the activated carbon return pipe 8. According to this example, denitrification can be efficiently performed at a high denitrification rate without adding an organic substance to the denitrification tank.

【0011】図2は、本発明の廃水の高度処理法の第二
の実施例を示す系統図であり、図1に示した実施例と異
なる点は、活性炭を脱窒槽6から直接有機物吸着槽3に
返送するのではなく、活性炭第1返送管9により硝化槽
4へ返送し、ここで活性炭に吸着されて残留する有機物
を酸化分解した後、活性炭第2返送管10により有機物
吸着槽3に導入することである。これにより活性炭の破
過を防止することができる。
FIG. 2 is a system diagram showing a second embodiment of the advanced treatment method for wastewater according to the present invention. The difference from the embodiment shown in FIG. 1 is that activated carbon is directly denitrified from an organic matter adsorption tank 6 3 is returned to the nitrification tank 4 through the activated carbon first return pipe 9, and the organic matter remaining on the activated carbon adsorbed by the activated carbon is oxidatively decomposed and then returned to the organic matter adsorption tank 3 through the activated carbon second return pipe 10. It is to introduce. This makes it possible to prevent breakthrough of the activated carbon.

【0012】図3は、本発明の廃水の高度処理法の第三
の実施例を示す系統図である。この実施例では、廃水の
流下方向を切り替えることにより、硝化槽の両側の反応
槽を有機物吸着槽及び脱窒槽とする。廃水は、実線の矢
印で示したように、第1原水導入管11により活性炭1
2が充填されている第1活性炭充填槽13に導入され
る。第1活性炭充填槽13においては活性炭12への有
機物の吸着が進行する。有機物を吸着除去された廃水
は、次いで硝化槽14に導入され、廃水中の有機性窒素
及びアンモニア性窒素は酸化され、硝酸性窒素となる。
硝化された廃水は、活性炭15が充填された第2活性炭
充填槽16に導入され、脱窒される。脱窒された廃水
は、第1排水管17から排水される。所定時間経過後、
バルブを切り替えて点線の矢印で示したように、廃水は
第2原水導入管18により第2活性炭充填槽16に導入
される。この場合には第2活性炭充填槽16において活
性炭15への有機物の吸着が進行する。有機物を吸着さ
れた廃水は、次いで硝化槽14に導入され、さらに第1
活性炭充填槽13に導入される。第1活性炭充填槽13
では、バルブ切り替え前に吸着した有機物を利用して脱
窒が進行する。脱窒された廃水は、第2排水管19より
排水される。
FIG. 3 is a system diagram showing a third embodiment of the advanced treatment method for wastewater according to the present invention. In this embodiment, the reaction tanks on both sides of the nitrification tank are used as an organic matter adsorption tank and a denitrification tank by switching the flow direction of the wastewater. The wastewater is discharged from the activated carbon 1 through the first raw water introduction pipe 11 as indicated by the solid arrow.
It is introduced into the first activated carbon filling tank 13 filled with 2. In the first activated carbon filling tank 13, the adsorption of organic substances on the activated carbon 12 proceeds. The waste water from which the organic substances have been adsorbed and removed is then introduced into the nitrification tank 14, and the organic nitrogen and ammonia nitrogen in the waste water are oxidized to form nitrate nitrogen.
The nitrified wastewater is introduced into the second activated carbon filling tank 16 filled with activated carbon 15 and denitrified. The denitrified waste water is discharged from the first drain pipe 17. After a predetermined time,
The wastewater is introduced into the second activated carbon filling tank 16 through the second raw water introducing pipe 18 as indicated by the dotted line arrow by switching the valve. In this case, the adsorption of organic substances on the activated carbon 15 proceeds in the second activated carbon filling tank 16. The wastewater in which the organic substances have been adsorbed is then introduced into the nitrification tank 14, and the first
It is introduced into the activated carbon filling tank 13. First activated carbon filling tank 13
Then, denitrification proceeds using the organic matter adsorbed before switching the valve. The denitrified waste water is discharged from the second drain pipe 19.

【0013】第三の実施例によれば、第一の実施例と同
様の効果を達成するのに、バルブの切り替えのみで、活
性炭を移送することがないため、動力費を低減でき、ま
た、活性炭移送装置が不要になるため構造が簡単にな
る。しかし、第三の実施例においても、第二の実施例の
場合と同様に所定時間経過後に、第1活性炭充填槽ある
いは第2活性炭充填槽中の活性炭を硝化槽14へ移送す
ることにより、吸着されて残留する有機物を酸化分解し
た後、第1活性炭充填槽あるいは第2活性炭充填槽へ返
送することができる。これにより活性炭の破過を防止す
ることができる。
According to the third embodiment, in order to achieve the same effect as that of the first embodiment, it is possible to reduce the power cost because the activated carbon is not transferred only by switching the valve, and the activated carbon is not transferred. The structure is simple because no activated carbon transfer device is required. However, also in the third embodiment, as in the case of the second embodiment, after a predetermined time has passed, the activated carbon in the first activated carbon filling tank or the second activated carbon filling tank is transferred to the nitrification tank 14 to cause adsorption. The organic matter remaining after being subjected to oxidative decomposition can be returned to the first activated carbon filling tank or the second activated carbon filling tank. This makes it possible to prevent breakthrough of the activated carbon.

【0014】[0014]

【発明の効果】本発明によれば、硝化槽の後に脱窒槽が
設置されている場合でも、廃水中の有機物を脱窒に利用
しうるので、脱窒のために有機物を添加する必要はな
く、脱窒速度を大きくすることができ、廃水中の有機物
及び窒素を効率よく除去することができる。
According to the present invention, even if a denitrification tank is installed after the nitrification tank, the organic matter in the wastewater can be utilized for denitrification, so that it is not necessary to add the organic matter for denitrification. The denitrification rate can be increased, and organic matter and nitrogen in wastewater can be efficiently removed.

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

【図1】本発明の廃水の高度処理法の第一の実施例を示
す系統図である。
FIG. 1 is a system diagram showing a first embodiment of an advanced treatment method for wastewater according to the present invention.

【図2】本発明の廃水の高度処理法の第二の実施例を示
す系統図である。
FIG. 2 is a system diagram showing a second embodiment of the advanced treatment method for wastewater of the present invention.

【図3】本発明の廃水の高度処理法の第三の実施例を示
す系統図である。
FIG. 3 is a system diagram showing a third embodiment of the advanced treatment method for wastewater of the present invention.

【符号の説明】[Explanation of symbols]

1 原水導入管 2 活性炭 3 有機物吸着槽 4 硝化槽 5 活性炭移送管 6 脱窒槽 7 排水管 8 活性炭返送管 9 活性炭第1返送管 10 活性炭第2返送管 11 第1原水導入管 12 活性炭 13 第1活性炭充填槽 14 硝化槽 15 活性炭 16 第2活性炭充填槽 17 第1排水管 18 第2原水導入管 19 第2排水管 1 Raw water introduction pipe 2 Activated carbon 3 Organic substance adsorption tank 4 Nitrification tank 5 Activated carbon transfer pipe 6 Denitrification tank 7 Drain pipe 8 Activated carbon return pipe 9 Activated carbon 1st return pipe 10 Activated carbon 2nd return pipe 11 1st Raw water introduction pipe 12 Activated carbon 13 1st Activated carbon filling tank 14 Nitrification tank 15 Activated carbon 16 Second activated carbon filling tank 17 First drainage pipe 18 Second raw water introduction pipe 19 Second drainage pipe

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 有機物及び窒素を含有する廃水から硝化
工程、次いで脱窒工程によって有機物及び窒素を除去す
る方法において、廃水中の有機物を予め活性炭に吸着さ
せ、この有機物を吸着した活性炭を脱窒工程に導入し、
活性炭に吸着された有機物を脱窒に必要な水素供与体と
して利用することを特徴とする廃水の高度処理法。
1. A method for removing organic matter and nitrogen from wastewater containing organic matter and nitrogen by a nitrification step and then a denitrification step, wherein the organic matter in the wastewater is adsorbed on activated carbon in advance, and the activated carbon adsorbing the organic matter is denitrified. Introduced into the process,
A high-level treatment method for wastewater, which uses organic matter adsorbed on activated carbon as a hydrogen donor necessary for denitrification.
【請求項2】 脱窒工程に使用した活性炭を硝化工程へ
移送して、残留有機物を酸化分解した後、廃水中の有機
物の吸着に再使用する請求項1記載の廃水の高度処理
法。
2. The advanced treatment method for wastewater according to claim 1, wherein the activated carbon used in the denitrification step is transferred to a nitrification step to oxidize and decompose residual organic matter, and then reused for adsorption of organic matter in wastewater.
【請求項3】 処理槽を第1活性炭槽、硝化槽及び第2
活性炭槽の順序に配列し、所定時間毎に原水の導入を第
1活性炭槽側あるいは第2活性炭槽側から切り替えて行
い、有機物の吸着、硝化処理及び脱窒処理を順次行うこ
とを特徴とする廃水の高度処理法。
3. A treatment tank comprising a first activated carbon tank, a nitrification tank and a second tank.
Characterized by arranging in an order of activated carbon tanks and switching the introduction of raw water from the first activated carbon tank side or the second activated carbon tank side at predetermined time intervals to sequentially perform adsorption of organic matter, nitrification treatment and denitrification treatment. Advanced wastewater treatment method.
【請求項4】 脱窒処理に使用した活性炭を予め硝化槽
に返送して残留有機物を酸化分解した後、第1活性炭槽
あるいは第2活性炭槽へ返送する請求項3記載の廃水の
高度処理法。
4. The advanced treatment method of waste water according to claim 3, wherein the activated carbon used for the denitrification treatment is previously returned to the nitrification tank to oxidize and decompose the residual organic matter, and then returned to the first activated carbon tank or the second activated carbon tank. .
JP19113895A 1995-07-04 1995-07-04 Advanced treatment of waste water Pending JPH0919698A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19113895A JPH0919698A (en) 1995-07-04 1995-07-04 Advanced treatment of waste water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19113895A JPH0919698A (en) 1995-07-04 1995-07-04 Advanced treatment of waste water

Publications (1)

Publication Number Publication Date
JPH0919698A true JPH0919698A (en) 1997-01-21

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
JP19113895A Pending JPH0919698A (en) 1995-07-04 1995-07-04 Advanced treatment of waste water

Country Status (1)

Country Link
JP (1) JPH0919698A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007260549A (en) * 2006-03-28 2007-10-11 Dowa Holdings Co Ltd Water cleaning method and apparatus
JP2008155085A (en) * 2006-12-21 2008-07-10 Ihi Corp Waste water treatment method and apparatus
TWI466480B (en) * 2007-01-10 2014-12-21 Qualcomm Inc Transmission of information using cyclically shifted sequences

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007260549A (en) * 2006-03-28 2007-10-11 Dowa Holdings Co Ltd Water cleaning method and apparatus
JP2008155085A (en) * 2006-12-21 2008-07-10 Ihi Corp Waste water treatment method and apparatus
TWI466480B (en) * 2007-01-10 2014-12-21 Qualcomm Inc Transmission of information using cyclically shifted sequences

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