JP2000051883A - Method for treating activated sludge of drainage - Google Patents

Method for treating activated sludge of drainage

Info

Publication number
JP2000051883A
JP2000051883A JP22553698A JP22553698A JP2000051883A JP 2000051883 A JP2000051883 A JP 2000051883A JP 22553698 A JP22553698 A JP 22553698A JP 22553698 A JP22553698 A JP 22553698A JP 2000051883 A JP2000051883 A JP 2000051883A
Authority
JP
Japan
Prior art keywords
sludge
reaction tank
bio
sewage
drainage
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
JP22553698A
Other languages
Japanese (ja)
Inventor
Hideaki Hamada
英明 浜田
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 Kiden Kogyo Ltd
Original Assignee
Hitachi Kiden Kogyo 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 Kiden Kogyo Ltd filed Critical Hitachi Kiden Kogyo Ltd
Priority to JP22553698A priority Critical patent/JP2000051883A/en
Publication of JP2000051883A publication Critical patent/JP2000051883A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Activated Sludge Processes (AREA)
  • Treatment Of Sludge (AREA)

Abstract

PROBLEM TO BE SOLVED: To reduce excess sludge discharged from a sewage treatment plant and others remarkably and to enable stable bio-treatment in a bio-reaction tank by a method in which sludge discharged from the bio-reaction tank with treated water is separated into solid and liquid, and the separated sludge is crushed and returned to the bio-reaction tank. SOLUTION: Drainage charged into an apparatus is introduced from a drainage pit 1 into a bio-reaction tank 3 through a drainage pump 2. The bio-reaction tank 3 is equipped with an aerator 4 for aerating the drainage, the introduced drainage is aerated, agitated to activate microorganisms in activated sludge, organic substances in the drainage is subjected to aerobic fermentation and anaerobic fermentation, the sludge is separated from treated water. Part or the whole separated sludge, after being crushed through a sludge pump 6 and a mechanical crusher 7, is returned to the bio-reaction tank 3. In this way, the decomposition of the sludge in the bio-reaction tank 3 is promoted to reduce excess sludge so that bio-treatment in the bio-reaction tank 3 can be performed stably.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、汚水の活性汚泥処
理方法に関し、特に、生物反応槽より処理水と共に流出
した汚泥を固液分離した後、生物反応槽へ戻すようにす
ることにより、下水処理場等から排出される余剰汚泥を
減少させるとともに、生物反応槽における生物処理を安
定して行うことができるようにした汚水の活性汚泥処理
方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for treating activated sludge of sewage, and more particularly to a method for separating sewage sludge flowing out of a biological reaction tank together with treated water into solid and liquid and returning the sludge to the biological reaction tank. The present invention relates to an activated sludge treatment method for sewage, in which excess sludge discharged from a treatment plant or the like is reduced and biological treatment in a biological reaction tank can be performed stably.

【0002】[0002]

【従来の技術】従来、下水処理場等においては、曝気槽
等の生物反応槽において、下水等の有機性汚水を活性汚
泥により生物処理する活性汚泥処理方法が採用されてい
る。この汚水の活性汚泥処理方法においては、生物反応
槽より処理水と共に流出した汚泥を固液分離した後、分
離した汚泥の一部又は全部を、そのまま生物反応槽へ戻
すようにすることにより、下水処理場等から排出される
余剰汚泥を減少させるとともに、生物反応槽における生
物処理を安定して行うことができるようにしていた。
2. Description of the Related Art Conventionally, in a sewage treatment plant or the like, an activated sludge treatment method in which organic wastewater such as sewage is biologically treated with activated sludge in a biological reaction tank such as an aeration tank. In this activated sludge treatment method for wastewater, after solid-liquid separation of the sludge flowing out together with the treated water from the biological reaction tank, part or all of the separated sludge is returned to the biological reaction tank as it is, thereby reducing the sewage. Surplus sludge discharged from a treatment plant or the like is reduced, and biological treatment in a biological reaction tank can be stably performed.

【0003】[0003]

【発明が解決しようとする課題】ところで、従来の汚水
の活性汚泥処理方法においては、生物反応槽より処理水
と共に流出した汚泥を固液分離した後、分離した汚泥
を、そのまま生物反応槽へ戻すようにしているが、この
分離した汚泥は、汚水に可溶な微細な粒径のものから容
易に汚水中に溶けない大きな粒径のものまでが混在した
状態にあるため、これをそのまま生物反応槽へ戻すよう
にしても、汚水中に溶けない大きな粒径のものは、生物
処理に寄与せず、分解されずにそのまま再度生物反応槽
より処理水と共に流出し、最終的には余剰汚泥として廃
棄されることとなる。余剰汚泥は、含水率が高い(汚泥
濃度は1%程度)ため、これを直接焼却したり、埋立地
に投棄することができず、通常、濃縮して脱水ケーキと
した後、焼却したり、埋立地に投棄するようにしてお
り、このため、その処理に費用がかかるだけでなく、近
年の環境保護の気運の高まりや埋立地の不足によって、
処理自体に困難を伴うようになってきている。
By the way, in the conventional activated sludge treatment method for wastewater, the sludge flowing out of the biological reaction tank together with the treated water is separated into solid and liquid, and the separated sludge is returned to the biological reaction tank as it is. However, the separated sludge has a mixture of fine particles that are soluble in sewage and large particles that are not easily dissolved in sewage. Even if it is returned to the tank, those with a large particle size that does not dissolve in the wastewater do not contribute to biological treatment and flow out of the biological reaction tank again without being decomposed together with the treated water, and eventually as excess sludge It will be discarded. Since excess sludge has a high moisture content (sludge concentration is about 1%), it cannot be directly incinerated or dumped in landfills. They are dumped in landfills, which is not only expensive to treat, but also due to the recent rise in environmental protection and lack of landfills,
The processing itself is becoming difficult.

【0004】本発明は、上記従来の汚水の活性汚泥処理
方法の有する余剰汚泥の処理の問題に鑑み、下水処理場
等から排出される余剰汚泥を著しく減少させるととも
に、生物反応槽における生物処理を安定して行うことが
できるようにした汚水の活性汚泥処理方法を提供するこ
とを目的とする。
[0004] In view of the problem of the treatment of excess sludge of the conventional method for treating activated sludge, the present invention remarkably reduces excess sludge discharged from a sewage treatment plant and the like, and reduces biological treatment in a biological reaction tank. An object of the present invention is to provide a method for treating activated sludge of sewage, which can be performed stably.

【0005】[0005]

【課題を解決するための手段】上記目的を達成するた
め、本発明の汚水の活性汚泥処理方法は、生物反応槽よ
り流出した汚泥を、生物反応槽へ戻して汚水を浄化する
汚水の活性汚泥処理方法において、生物反応槽より処理
水と共に流出した汚泥を固液分離した後、分離した汚泥
を破砕後、生物反応槽へ戻すようにすることを特徴とす
る。
In order to achieve the above object, the method for treating activated sludge of sewage of the present invention is characterized in that activated sludge of sewage for purifying sewage by returning sludge discharged from a biological reaction tank to a biological reaction tank. The treatment method is characterized in that the sludge flowing out of the biological reaction tank together with the treated water is subjected to solid-liquid separation, and then the separated sludge is crushed and returned to the biological reaction tank.

【0006】この汚水の活性汚泥処理方法は、生物反応
槽より流出した汚泥を、固液分離した後、分離した汚泥
を破砕することにより、汚泥中の容易に汚水中に溶けな
い大きな粒径のものを可溶な微細な粒径のものにした
後、生物反応槽へ戻すようしているので、生物反応槽に
おける汚泥の分解が促進され、下水処理場等から排出さ
れる余剰汚泥を著しく減少又は余剰汚泥が発生しないよ
うにすることができるとともに、生物反応槽における生
物処理を安定して行うことができる。
In this method for treating activated sludge, the sludge flowing out of a biological reaction tank is separated into solid and liquid, and then the separated sludge is crushed, so that the sludge having a large particle size that is not easily dissolved in the sludge in the sludge. Since the waste is reduced to a soluble fine particle size and then returned to the biological reaction tank, the decomposition of sludge in the biological reaction tank is promoted, and surplus sludge discharged from sewage treatment plants is significantly reduced. Alternatively, excess sludge can be prevented from being generated, and the biological treatment in the biological reaction tank can be stably performed.

【0007】この場合において、汚泥の破砕を、機械式
破砕機、超音波式破砕機等の破砕機により行うようにす
ることができる。
[0007] In this case, the sludge can be crushed by a crusher such as a mechanical crusher or an ultrasonic crusher.

【0008】これにより、汚泥の破砕を確実に行うこと
ができる。
Thus, the sludge can be crushed reliably.

【0009】また、汚泥の破砕を、汚水ポンプ、曝気機
等の既存の設備により行うようにすることができる。
Further, the sludge can be crushed by existing equipment such as a sewage pump and an aerator.

【0010】これにより、設備の構築コストを低廉にす
ることができる。
As a result, the construction cost of the equipment can be reduced.

【0011】[0011]

【発明の実施の形態】以下、本発明の汚水の活性汚泥処
理方法の実施の形態を図面に基づいて説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the method for treating activated sludge of wastewater of the present invention will be described below with reference to the drawings.

【0012】図1に、本発明の汚水の活性汚泥処理方法
を実施する下水処理場等に設置される活性汚泥処理設備
の第1実施例を示す。
FIG. 1 shows a first embodiment of an activated sludge treatment facility installed in a sewage treatment plant or the like for implementing the activated sludge treatment method of the present invention.

【0013】この活性汚泥処理設備に流入した汚水は、
汚水ピット1から汚水ポンプ2を介して曝気槽等の生物
反応槽3内に導入される。
The sewage flowing into the activated sludge treatment facility is:
The sewage pit 1 is introduced into a biological reaction tank 3 such as an aeration tank via a sewage pump 2.

【0014】この生物反応槽3には、汚水を曝気処理す
るための曝気機4が設置されており、生物処理槽3内に
導入された汚水を、曝気、撹拌して、活性汚泥中の微生
物(バクテリア)を活性化して、汚水中の有機物を好気
性発酵及び嫌気性発酵を繰り返すことにより処理するよ
うにしている。
An aerator 4 for aerating sewage is installed in the biological reaction tank 3, and the sewage introduced into the biological treatment tank 3 is aerated and agitated to remove microorganisms in the activated sludge. (Bacteria) are activated to treat organic matter in wastewater by repeating aerobic fermentation and anaerobic fermentation.

【0015】そして、生物処理槽3で生物処理された汚
泥を含む処理水は、沈澱槽5へ導入され、重力による自
然沈降等による固液分離を行うことにより、処理水から
汚泥を分離し、上澄水は、殺菌処理した後、河川等へ放
流するようにする。
The treated water containing the sludge biologically treated in the biological treatment tank 3 is introduced into the sedimentation tank 5 and separated from the treated water by solid-liquid separation by gravity sedimentation or the like. The supernatant water is discharged to rivers and the like after sterilization.

【0016】一方、分離した汚泥は、その一部又は全部
を、返送汚泥ポンプ6により返送汚泥配管8を介して生
物反応槽3に戻すようにしている。
On the other hand, part or all of the separated sludge is returned to the biological reaction tank 3 by the return sludge pump 6 via the return sludge pipe 8.

【0017】ところで、この分離した汚泥は、汚水に可
溶な微細な粒径のものから容易に汚水中に溶けない大き
な粒径のものまでが混在した状態にあるため、これをそ
のまま生物反応槽へ戻すようにしても、汚水中に溶けな
い大きな粒径のものは、生物処理に寄与せず、分解され
ずにそのまま再度生物反応槽3より処理水と共に流出
し、最終的には余剰汚泥として廃棄されることとなる。
Incidentally, the separated sludge is in a mixed state of fine particles having a fine particle size soluble in sewage and large particles which are not easily dissolved in sewage. Even if it is returned to the wastewater, those having a large particle size that does not dissolve in the sewage do not contribute to biological treatment and flow out again from the biological reaction tank 3 together with the treated water without being decomposed, and eventually as excess sludge. It will be discarded.

【0018】このため、返送汚泥配管8に機械式破砕機
7を介在し、汚泥を破砕後、生物反応槽3へ戻すように
する。このように、汚泥中の容易に汚水中に溶けない大
きな粒径のものを可溶な微細な粒径のものにした後、生
物反応槽3へ戻すようにすることにより、生物反応槽3
における汚泥の分解が促進され、排出される余剰汚泥を
著しく減少又は余剰汚泥が発生しないようにすることが
できるとともに、生物反応槽3における生物処理を安定
して行うことができるものとなる。
For this reason, a mechanical crusher 7 is interposed in the return sludge pipe 8 so that the sludge is crushed and then returned to the biological reaction tank 3. As described above, the sludge having a large particle size that is not easily dissolved in the sludge is converted into a fine particle having a soluble size, and then returned to the biological reaction tank 3.
The decomposition of sludge in the above is promoted, the excess sludge to be discharged can be remarkably reduced or surplus sludge is not generated, and the biological treatment in the biological reaction tank 3 can be stably performed.

【0019】ところで、本実施例においては、汚泥の破
砕を、返送汚泥配管8に介在した機械式破砕機7により
行うようにしたが、汚泥の破砕方式は、これに限定され
ず、例えば、汚泥を大気放出する際に生じる圧力差及び
衝撃力で破砕する方式のほか、20kHz程度の高周波
により生じるキャビテーション中の衝撃力で汚泥を破砕
する超音波式破砕機を使用することができる。
In this embodiment, the sludge is crushed by the mechanical crusher 7 interposed in the return sludge pipe 8, but the crushing method of the sludge is not limited to this. In addition to the method of crushing by the pressure difference and the impact force generated when air is released to the atmosphere, an ultrasonic crusher that crushes sludge by the impact force during cavitation generated by high frequency of about 20 kHz can be used.

【0020】このような、機械破砕方式、超音波破砕方
式のいずれの方式によっても、汚泥中の容易に汚水中に
溶けない大きな粒径のものを可溶な微細な粒径のものに
することができるとともに、さらに、バクテリアを主体
とする汚泥の細胞壁の破壊が可能となり、細胞内物質を
可溶化できるものとなる。また、これらの破砕方式は、
酸、アルカリ等を用いた薬液分解やオゾンによる酸化分
解と異なり、処理水に薬液やオゾンが残留せず、このた
め、処理水の2次処理が不要となり、さらに、汚水処理
のために必要とされる微生物の量は減少しないため、生
物反応槽3における生物処理を安定して行うことができ
るものとなる。
In any of the mechanical crushing method and the ultrasonic crushing method, a large particle size that is not easily dissolved in the sludge in the sludge is converted into a fine particle size that is soluble. And the cell wall of sludge mainly composed of bacteria can be destroyed, so that intracellular substances can be solubilized. Also, these crushing methods
Unlike chemical solution decomposition using acid or alkali or oxidative decomposition using ozone, no chemical solution or ozone remains in the treated water, so that the secondary treatment of the treated water becomes unnecessary, and furthermore, it is necessary for the sewage treatment. Since the amount of microorganisms to be removed does not decrease, the biological treatment in the biological reaction tank 3 can be stably performed.

【0021】このように、分離した汚泥は、可溶な微細
な粒径のものにした後、生物反応槽3へ戻され、生物処
理が行われるが、通常、汚泥は有機物量が70%前後で
あり、しかも、オキシデーションディッチ法や長時間曝
気法での有機物の汚泥転換率が70%程度であることか
ら、この汚水の活性汚泥処理方法においては、生物反応
槽3の汚泥濃度が49%増加した時点で発生する汚泥量
と分解処理される汚泥量が等しくなり、見掛け上、余剰
汚泥が発生しない活性汚泥処理方法となる。
As described above, the separated sludge is converted into a fine one having a soluble fine particle diameter, and then returned to the biological reaction tank 3, where biological treatment is performed. Usually, the sludge has an organic matter content of about 70%. In addition, since the sludge conversion rate of organic matter by the oxidation ditch method or the long-time aeration method is about 70%, in this activated sludge treatment method, the sludge concentration in the biological reaction tank 3 is 49%. The amount of sludge generated at the time of the increase and the amount of sludge to be decomposed are equalized, so that the activated sludge treatment method apparently does not generate excess sludge.

【0022】また、上記実施例では、返送汚泥配管8に
機械式破砕機7を介在し、汚泥を破砕後、生物反応槽3
へ戻すようにしたが、図2に示す本発明の汚水の活性汚
泥処理方法を実施する下水処理場等に設置される活性汚
泥処理設備の第2実施例のように、返送汚泥配管8を汚
水ピット1に接続し、汚泥を汚水と共に汚水ピット1か
ら汚水ポンプ2を介して生物反応槽3内に導入すると
き、汚水ポンプ2により汚泥を破砕するように構成した
り、図3に示す本発明の汚水の活性汚泥処理方法を実施
する下水処理場等に設置される活性汚泥処理設備の第3
実施例のように、返送汚泥配管8を生物反応槽3の曝気
機4の近傍位置に接続し、汚泥を生物反応槽3内に導入
するとき、曝気機4により汚泥を破砕するように構成す
ることができる。
In the above embodiment, a mechanical crusher 7 is interposed in the return sludge pipe 8 to crush the sludge.
However, as in the second embodiment of the activated sludge treatment facility installed in a sewage treatment plant or the like that performs the activated sludge treatment method of the present invention shown in FIG. When the sludge is connected to the pit 1 and introduced into the biological reaction tank 3 via the sewage pump 2 from the sewage pit 1 together with the sewage, the sludge is crushed by the sewage pump 2 or the present invention shown in FIG. Of activated sludge treatment equipment installed in a sewage treatment plant or the like that implements the activated sludge treatment method for sewage in Japan
As in the embodiment, the return sludge pipe 8 is connected to a position near the aerator 4 in the biological reaction tank 3, and the sludge is crushed by the aerator 4 when the sludge is introduced into the biological reaction tank 3. be able to.

【0023】[0023]

【発明の効果】本発明の汚水の活性汚泥処理方法によれ
ば、生物反応槽より流出した汚泥を、固液分離した後、
分離した汚泥を破砕することにより、汚泥中の容易に汚
水中に溶けない大きな粒径のものを可溶な微細な粒径の
ものにした後、生物反応槽へ戻すようしているので、生
物反応槽における汚泥の分解が促進され、下水処理場等
から排出される余剰汚泥を著しく減少又は余剰汚泥が発
生しないようにすることができるとともに、生物反応槽
における生物処理を安定して行うことができ、余剰汚泥
の処理に付随する問題を一挙に解消することができる。
According to the activated sludge treatment method of the present invention, the sludge flowing out of the biological reaction tank is subjected to solid-liquid separation.
By crushing the separated sludge, the sludge with a large particle size that is not easily dissolved in the sewage is converted into a fine particle size that is soluble, and then returned to the biological reaction tank. Decomposition of sludge in the reaction tank is promoted, surplus sludge discharged from sewage treatment plants and the like can be significantly reduced or surplus sludge is not generated, and biological treatment in the biological reaction tank can be stably performed. Thus, problems associated with the treatment of excess sludge can be eliminated at a glance.

【0024】また、汚泥の破砕を、機械式破砕機、超音
波式破砕機等の破砕機により行うようにすることによ
り、汚泥の破砕を確実に行うことができる。
Further, by crushing the sludge using a crusher such as a mechanical crusher or an ultrasonic crusher, the sludge can be reliably crushed.

【0025】また、汚泥の破砕を、汚水ポンプ、曝気機
等の既存の設備により行うようにすることにより、設備
の構築コストを低廉にすることができる。
[0025] In addition, since the sludge is crushed by existing equipment such as a sewage pump and an aerator, the construction cost of the equipment can be reduced.

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

【図1】本発明の汚水の活性汚泥処理方法を実施する下
水処理場等に設置される活性汚泥処理設備の第1実施例
の説明図である。
FIG. 1 is an explanatory diagram of a first embodiment of an activated sludge treatment facility installed in a sewage treatment plant or the like for implementing the activated sludge treatment method of the present invention.

【図2】本発明の汚水の活性汚泥処理方法を実施する下
水処理場等に設置される活性汚泥処理設備の第2実施例
の説明図である。
FIG. 2 is an explanatory view of a second embodiment of the activated sludge treatment facility installed in a sewage treatment plant or the like for implementing the activated sludge treatment method for wastewater of the present invention.

【図3】本発明の汚水の活性汚泥処理方法を実施する下
水処理場等に設置される活性汚泥処理設備の第3実施例
の説明図である。
FIG. 3 is an explanatory view of a third embodiment of an activated sludge treatment facility installed in a sewage treatment plant or the like for implementing the activated sludge treatment method of the present invention.

【符号の説明】[Explanation of symbols]

1 汚水ピット 2 汚水ポンプ 3 生物反応槽 4 曝気機 5 沈澱槽 6 返送汚泥ポンプ 7 機械式破砕機 8 返送汚泥配管 Reference Signs List 1 sewage pit 2 sewage pump 3 biological reaction tank 4 aerator 5 sedimentation tank 6 return sludge pump 7 mechanical crusher 8 return sludge piping

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 生物反応槽より流出した汚泥を、生物反
応槽へ戻して汚水を浄化する汚水の活性汚泥処理方法に
おいて、生物反応槽より処理水と共に流出した汚泥を固
液分離した後、分離した汚泥を破砕後、生物反応槽へ戻
すようにすることを特徴とする汚水の活性汚泥処理方
法。
1. An activated sludge treatment method for sewage in which sludge flowing out of a biological reaction tank is returned to a biological reaction tank to purify sewage. A method for treating activated sludge in sewage, wherein the crushed sludge is returned to a biological reaction tank after crushing.
【請求項2】 汚泥の破砕を、機械式破砕機、超音波式
破砕機等の破砕機により行うようにしたことを特徴とす
る請求項1記載の汚水の活性汚泥処理方法。
2. The activated sludge treatment method according to claim 1, wherein the sludge is crushed by a crusher such as a mechanical crusher or an ultrasonic crusher.
【請求項3】 汚泥の破砕を、汚水ポンプ、曝気機等の
既存の設備により行うようにしたことを特徴とする請求
項1記載の汚水の活性汚泥処理方法。
3. The activated sludge treatment method according to claim 1, wherein the sludge is crushed by an existing facility such as a sewage pump and an aerator.
JP22553698A 1998-08-10 1998-08-10 Method for treating activated sludge of drainage Pending JP2000051883A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22553698A JP2000051883A (en) 1998-08-10 1998-08-10 Method for treating activated sludge of drainage

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22553698A JP2000051883A (en) 1998-08-10 1998-08-10 Method for treating activated sludge of drainage

Publications (1)

Publication Number Publication Date
JP2000051883A true JP2000051883A (en) 2000-02-22

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
JP22553698A Pending JP2000051883A (en) 1998-08-10 1998-08-10 Method for treating activated sludge of drainage

Country Status (1)

Country Link
JP (1) JP2000051883A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002018470A (en) * 2000-07-07 2002-01-22 Matsushita Environment Airconditioning Eng Co Ltd Method and apparatus for treating organic wastewater
JP2007021285A (en) * 2005-07-12 2007-02-01 Mitsubishi Rayon Eng Co Ltd Method and apparatus for reducing volume of excess sludge
JP2009028673A (en) * 2007-07-30 2009-02-12 Miike Iron Works Co Ltd Apparatus for reducing sludge volume

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002018470A (en) * 2000-07-07 2002-01-22 Matsushita Environment Airconditioning Eng Co Ltd Method and apparatus for treating organic wastewater
JP2007021285A (en) * 2005-07-12 2007-02-01 Mitsubishi Rayon Eng Co Ltd Method and apparatus for reducing volume of excess sludge
JP2009028673A (en) * 2007-07-30 2009-02-12 Miike Iron Works Co Ltd Apparatus for reducing sludge volume

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