JPH0999294A - Waste water treating equipment - Google Patents

Waste water treating equipment

Info

Publication number
JPH0999294A
JPH0999294A JP7258618A JP25861895A JPH0999294A JP H0999294 A JPH0999294 A JP H0999294A JP 7258618 A JP7258618 A JP 7258618A JP 25861895 A JP25861895 A JP 25861895A JP H0999294 A JPH0999294 A JP H0999294A
Authority
JP
Japan
Prior art keywords
tank
membrane
biological treatment
separation
treatment
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
JP7258618A
Other languages
Japanese (ja)
Inventor
Kazuo Suzuki
和夫 鈴木
Kensuke Matsui
謙介 松井
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.)
Kurita Water Industries Ltd
Original Assignee
Kurita Water Industries 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 Kurita Water Industries Ltd filed Critical Kurita Water Industries Ltd
Priority to JP7258618A priority Critical patent/JPH0999294A/en
Publication of JPH0999294A publication Critical patent/JPH0999294A/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

  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Activated Sludge Processes (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

PROBLEM TO BE SOLVED: To prevent deterioration of membrane performance due to the insolubilization of nutrient salts and increase in load at the time of performing membrane separation of a treated liquid with biological treatment and flocculation. SOLUTION: This equipment is provided with a biological treatment tank 1 for biologically treating organic waste water, a separation membrane tank 2 into which the biologically treated liquid is introduced and in which a membrane module 7 is immersed, a means 3 for adding nutrient salts to the biological treatment tank 1 and a means 6 for adding a flocculant to the separation membrane tank 2. Accordingly, since this equipment is divided into two tanks, namely the biological treatment tank 1 and the separation membrane tank 2 for subjecting the biologically treated liquid to flocculation and then, to solid-liquid separation with the membrane module 7, the nutrient salts are prevented from being insolubilized by the flocculant to inhibit wasteful consumption of the flocculant due to the insolubilization of the nutrient salts from occurring. Thus, membranes of the membrane module 7 are prevented from being contaminated with BOD causative substances or intermediate products and by using this equipment, stable and effective treatment of waste water can be performed over a long period.

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】本発明は排水処理装置に係
り、特に、栄養塩が不足した有機性排水にリン成分等の
栄養塩を添加して生物処理した後凝集処理し、凝集処理
液を膜分離して処理する場合に好適な排水処理装置に関
する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a wastewater treatment apparatus, and more particularly, to organic wastewater lacking nutrient salts, which is biologically treated by adding a nutrient salt such as a phosphorus component and then coagulated to form a coagulated liquid. The present invention relates to a wastewater treatment device suitable for separate treatment.

【0002】[0002]

【従来の技術】従来、生物処理や凝集処理における固液
分離手段として膜分離手段を適用する例は数多く提案さ
れており、例えば、図3のような装置がある。図3に示
す装置において、原水は、まず、ブロワ32及び散気管
33よりなる曝気手段が設けられた生物(活性汚泥)処
理槽31に導入され、好気性生物処理される。生物処理
液は、ポンプ34で膜分離装置35に導入され、膜濃縮
水の一部は循環水として生物処理槽31に返送され、残
部は系外へ排出される。膜分離装置35の膜透過水は、
凝集槽36に導入され、凝集剤により溶解性の難生物分
解性有機物が凝集、不溶化される。凝集処理液はポンプ
37により膜分離装置38に導入されて固液分離され
る。この膜分離装置38の膜濃縮水の一部は循環水とし
て凝集槽36に返送され、残部は系外へ排出される。一
方、膜透過水は処理水として系外へ排出される。
2. Description of the Related Art Conventionally, many examples of applying a membrane separation means as a solid-liquid separation means in biological treatment or coagulation treatment have been proposed, for example, there is an apparatus shown in FIG. In the apparatus shown in FIG. 3, raw water is first introduced into a living organism (activated sludge) treatment tank 31 provided with an aeration means including a blower 32 and an air diffusing pipe 33, and treated for aerobic organisms. The biological treatment liquid is introduced into the membrane separation device 35 by the pump 34, a part of the membrane concentrated water is returned to the biological treatment tank 31 as circulating water, and the rest is discharged out of the system. The permeated water of the membrane separator 35 is
The coagulant is introduced into the coagulation tank 36 to coagulate and insolubilize soluble poorly biodegradable organic matter. The coagulation treatment liquid is introduced into the membrane separation device 38 by the pump 37 and is subjected to solid-liquid separation. A part of the membrane concentrated water of the membrane separator 38 is returned to the coagulation tank 36 as circulating water, and the rest is discharged out of the system. On the other hand, the membrane permeated water is discharged out of the system as treated water.

【0003】図3の排水処理装置は、2槽の処理槽と、
2機の膜分離装置とを必要とし、設備が複雑であること
から、この生物処理及び膜分離工程と、凝集処理及び膜
分離工程とを一工程にまとめ、処理設備を簡素化したも
のとして、図4に示す装置が提案されている(特公平6
−83837号公報)。
The wastewater treatment equipment of FIG. 3 has two treatment tanks,
Since two membrane separation devices are required and the equipment is complicated, the biological treatment and membrane separation steps and the coagulation treatment and membrane separation steps are combined into one step to simplify the treatment equipment. The device shown in FIG. 4 has been proposed (Japanese Patent Publication 6).
-83837).

【0004】図4に示す装置は、生物処理槽31内の散
気管33上方に浸漬型膜モジュール40を浸漬設置し、
また、凝集剤添加手段を設け、生物処理槽31で好気性
生物処理すると共に凝集処理し、生物処理及び凝集処理
液を吸引ポンプ41で吸引することにより、膜モジュー
ル40で濾過して固液分離するものである。
In the apparatus shown in FIG. 4, an immersion type membrane module 40 is installed by immersion above the air diffuser 33 in the biological treatment tank 31.
Further, a flocculant addition means is provided to perform aerobic biological treatment and coagulation treatment in the biological treatment tank 31, and the biological treatment and aggregation treatment liquid is sucked by the suction pump 41 to be filtered by the membrane module 40 for solid-liquid separation. To do.

【0005】[0005]

【発明が解決しようとする課題】図4に示す装置であれ
ば、図3に示す装置に比べて、大幅な装置設備の簡略化
が図れるが、次のような問題がある。
The apparatus shown in FIG. 4 can greatly simplify the equipment of the apparatus as compared with the apparatus shown in FIG. 3, but has the following problems.

【0006】即ち、一般に有機性排水の生物処理に当っ
ては、排水中の栄養塩(リン,窒素)が生物処理に不足
するために、これらの栄養塩を排水に添加して生物処理
する場合が多い。
[0006] In general, in the biological treatment of organic wastewater, when nutrient salts (phosphorus, nitrogen) in the wastewater are insufficient for biological treatment, when these nutrient salts are added to the wastewater for biological treatment. There are many.

【0007】この場合、栄養塩、特にリン成分と凝集剤
とを同じ処理槽に添加すると、微生物が栄養塩を吸収利
用する前に、栄養塩と凝集剤とが化学的に反応して、微
生物に吸収利用され難い不溶性の塩を生成する。例え
ば、リン塩と凝集剤の鉄化合物は、下記式で速やかに反
応し、不溶化する。このため、栄養塩が有効に利用され
ないという問題がある。
In this case, if the nutrient salt, especially the phosphorus component and the flocculant are added to the same treatment tank, the nutrient salt and the flocculant chemically react with each other before the microorganism absorbs and utilizes the nutrient salt, and It produces an insoluble salt that is difficult to be absorbed and utilized by the. For example, the phosphorus salt and the iron compound of the aggregating agent react quickly and become insoluble according to the following formula. Therefore, there is a problem that nutrient salts are not effectively used.

【0008】 PO4 3- +Fe3+ → FePO4 (不溶化) また、この場合には、栄養塩のみならず、凝集剤も無駄
に消費され、溶解性の難生物分解性有機物の凝集、不溶
化に有効利用されなくなる。
PO 4 3− + Fe 3+ → FePO 4 (insolubilization) Further, in this case, not only the nutrient salt but also the coagulant is wastefully consumed, resulting in the coagulation and insolubilization of the soluble biodegradable organic substance. It will not be used effectively.

【0009】しかも、固液分離のための分離膜を、好気
性生物処理(酸化処理)を行う生物処理槽に浸漬設置す
ると、急速に膜の差圧が上昇し、必要な透過量が得られ
なくなる例が多々ある。これは、過負荷によりBODや
中間生成物が残留し、これらが膜面で濃縮したり膜面に
付着したりすることにより、膜が汚染するためであるこ
とが判明した。また、膜面に微生物が付着増殖し、接触
酸化における生物膜様のものを膜面に形成することによ
り、膜の差圧を増加させる場合もある。
Moreover, when the separation membrane for solid-liquid separation is immersed and installed in a biological treatment tank for aerobic biological treatment (oxidation treatment), the differential pressure of the membrane is rapidly increased to obtain the required permeation amount. There are many cases that disappear. It was found that this is because the BOD and the intermediate product remained due to the overload, and the membrane was contaminated by condensing these on the membrane surface or adhering to the membrane surface. In some cases, a microorganism adheres to and grows on the membrane surface to form a biofilm-like substance in the catalytic oxidation on the membrane surface, thereby increasing the differential pressure of the membrane.

【0010】本発明は上記従来の問題点を解決し、有機
性排水を生物処理及び凝集処理し、凝集処理液を膜分離
処理する排水処理装置であって、栄養塩の不溶化、及
び、負荷増加等による膜性能の劣化を防止して、長期に
わたり安定かつ効率的な処理を行える排水処理装置を提
供することを目的とする。
The present invention solves the above-mentioned conventional problems, and is a wastewater treatment apparatus for subjecting organic wastewater to biological treatment and coagulation treatment, and a coagulation treatment liquid to a membrane separation treatment, wherein the nutrient salt is insolubilized and the load is increased. It is an object of the present invention to provide a wastewater treatment device capable of performing stable and efficient treatment for a long period of time by preventing deterioration of membrane performance due to the above.

【0011】[0011]

【課題を解決するための手段】本発明の排水処理装置
は、有機性排水を生物処理する生物処理槽と、該生物処
理槽の流出液が導入される分離膜槽と、該分離膜槽内に
浸漬設置された膜モジュールと、前記生物処理槽に栄養
塩を添加する栄養塩添加手段と、前記分離膜槽内の液又
は前記流出液に凝集剤を添加する凝集剤添加手段と、前
記膜モジュールの透過水を処理水として取り出す処理水
取出手段とを備えてなることを特徴とする。
The wastewater treatment equipment of the present invention comprises a biological treatment tank for biologically treating organic wastewater, a separation membrane tank into which the effluent of the biological treatment tank is introduced, and the inside of the separation membrane tank. A membrane module dipped and installed in the biological treatment tank, a nutrient salt adding means for adding a nutrient salt to the biological treatment tank, a coagulant adding means for adding a coagulant to the liquid in the separation membrane tank or the effluent, and the membrane It is characterized by comprising a treated water extracting means for taking out permeated water of the module as treated water.

【0012】本発明の排水処理装置では、有機性排水を
生物処理するための水槽と、凝集処理して膜モジュール
で固液分離するための水槽とを分けたため、生物処理槽
に添加されたリン成分等の栄養塩は、凝集剤と反応して
不溶化することなく、微生物に有効に利用吸収される。
また、栄養塩の不溶化に凝集剤が無駄に消費されること
もなく、凝集剤は溶解性の難生物分解性有機物の凝集、
不溶化に有効に利用される。
In the wastewater treatment equipment of the present invention, the water tank for biological treatment of organic wastewater and the water tank for solid-liquid separation in the membrane module after coagulation treatment are separated, and therefore phosphorus added to the biological treatment tank is separated. Nutrient salts such as components are effectively used and absorbed by microorganisms without reacting with the flocculant to insolubilize them.
In addition, the coagulant is not wastefully consumed for insolubilizing the nutrient salts, and the coagulant is a coagulant of the soluble biodegradable organic matter,
It is effectively used for insolubilization.

【0013】しかも、生物処理槽で生物処理を完全に行
い、BODや中間生成物の残留が殆どない、生物処理槽
流出液を膜モジュールで膜濾過するため、膜汚染が防止
され、長期にわたり安定かつ効率的な膜分離を行える。
Moreover, since the biological treatment is completely carried out in the biological treatment tank, and the BOD and the intermediate product are hardly left, the effluent of the biological treatment tank is membrane-filtered by the membrane module, so that the membrane contamination is prevented and the stable for a long time. And efficient membrane separation can be performed.

【0014】[0014]

【発明の実施の形態】以下、図面を参照して本発明を詳
細に説明する。
DETAILED DESCRIPTION OF THE INVENTION The present invention will be described in detail below with reference to the drawings.

【0015】図1,2は本発明の排水処理装置の一実施
例方法を示す系統図である。
1 and 2 are system diagrams showing a method of an embodiment of the waste water treatment equipment of the present invention.

【0016】図1に示す排水処理装置は、生物処理槽1
と分離膜槽2とを備え、生物処理槽1には、配管3より
栄養塩が添加される。また、生物処理槽1には散気管4
が設けられており、ブロワ5で曝気がなされる。
The wastewater treatment equipment shown in FIG.
And a separation membrane tank 2 are provided, and nutrient salts are added to the biological treatment tank 1 through a pipe 3. Also, the biological treatment tank 1 has an air diffuser 4
Is provided, and aeration is performed by the blower 5.

【0017】分離膜槽2には、配管6より凝集剤が添加
される。この分離膜槽2には膜モジュール7が浸漬設置
されており、この膜モジュール7の透過水は、吸引ポン
プ8を備える配管9で抜き出される。この膜モジュール
7の下部には散気管10が設けられ、ブロワ5による曝
気で生じた上昇流で槽内液が流動し、凝集処理及び膜分
離処理が促進するように構成されている。
A coagulant is added to the separation membrane tank 2 through a pipe 6. A membrane module 7 is immersed in the separation membrane tank 2, and the permeated water of the membrane module 7 is extracted through a pipe 9 equipped with a suction pump 8. An air diffuser 10 is provided in the lower part of the membrane module 7, and is configured so that the ascending flow generated by the aeration by the blower 5 causes the liquid in the tank to flow, thereby promoting the coagulation treatment and the membrane separation treatment.

【0018】11〜15の各符号は液移送配管、16,
17はポンプである。
Reference numerals 11 to 15 denote liquid transfer pipes, 16,
17 is a pump.

【0019】本実施例の排水処理装置では、配管11よ
り生物処理槽1に導入された有機性排水(原水)は、配
管3から栄養塩が添加され、散気管4からの曝気下、好
気性生物処理される。
In the waste water treatment apparatus of this embodiment, the organic waste water (raw water) introduced into the biological treatment tank 1 through the pipe 11 is added with nutrient salts through the pipe 3 and aerated under the aeration from the air diffuser 4. Biologically processed.

【0020】生物処理液は、配管12より分離膜槽2に
導入され、配管6から鉄塩、アルミニウム塩等の凝集剤
が添加されて凝集処理される。そして、吸引ポンプ8に
よる吸引で凝集処理液が膜濾過され、膜モジュール7か
ら取り出される清澄な透過水は、処理水として配管9よ
り系外へ排出される。
The biological treatment liquid is introduced into the separation membrane tank 2 through the pipe 12, and the flocculating agent is added through the pipe 6 with a coagulant such as iron salt or aluminum salt. Then, the coagulation treatment liquid is subjected to membrane filtration by suction by the suction pump 8, and the clear permeated water taken out from the membrane module 7 is discharged from the system through the pipe 9 as treated water.

【0021】この分離膜槽2の汚泥は配管13より抜き
出され、一部が余剰汚泥として配管15より系外に排出
され、残部は返送汚泥として配管14より生物処理槽1
に返送される。
The sludge in the separation membrane tank 2 is extracted from the pipe 13, a part of the sludge is discharged to the outside of the system through the pipe 15 as surplus sludge, and the rest is returned sludge through the pipe 14 through the biological treatment tank 1.
Will be returned to.

【0022】図2に示す排水処理装置は、凝集処理のた
めの水槽と、膜分離のための水槽を分割し、生物処理槽
1と分離膜槽2との間に凝集槽20を設け、生物処理槽
1から流出する生物処理液を配管12Aより一旦凝集槽
20に受け、この凝集槽20で配管6より凝集剤を添加
して凝集処理し、凝集処理液を配管12Bを経て分離膜
槽2に導入して膜モジュール7で膜濾過するようにした
点が、図1に示す排水処理装置と異なる。なお、この凝
集槽20にも散気管21が設けられ、ブロワ5により曝
気が行われるように構成されている。その他の構成は、
図1に示す排水処理装置と同様であり、図1に示すもの
と同一機能を奏する部材には同一符号を付してある。
In the waste water treatment apparatus shown in FIG. 2, a water tank for coagulation treatment and a water tank for membrane separation are divided, and a coagulation tank 20 is provided between the biological treatment tank 1 and the separation membrane tank 2 to remove biological matter. The biological treatment liquid flowing out from the treatment tank 1 is once received in the coagulation tank 20 through the pipe 12A, the coagulant is added from the pipe 6 in the coagulation tank 20 to perform the coagulation treatment, and the coagulation treatment liquid is passed through the pipe 12B to the separation membrane tank 2 It is different from the waste water treatment apparatus shown in FIG. 1 in that the membrane module 7 is introduced into the membrane module 7 for membrane filtration. An air diffuser 21 is also provided in the coagulation tank 20 so that the blower 5 performs aeration. Other configurations are
Members similar to those of the waste water treatment apparatus shown in FIG. 1 and having the same functions as those shown in FIG. 1 are designated by the same reference numerals.

【0023】このような本発明の排水処理装置によれ
ば、栄養塩は凝集剤が添加されない生物処理槽1に添加
されるため、不溶化することなく、微生物に有効に利用
吸収され、効率的な生物処理を行える。一方、分離膜槽
2又は凝集槽20に添加された凝集剤は、溶解性の難生
物分解性有機物の凝集、不溶化に有効に利用される。ま
た、過負荷の場合でも、この生物処理槽1で生物処理を
完全に行うことができるため、BODや中間生成物が流
出せず、これが分離膜を汚染することがない。また、膜
面での生物膜の成長の問題もない。このため、膜性能の
低下を防止して、長期にわたり安定かつ効率的な膜分離
処理を行える。
According to the waste water treatment apparatus of the present invention as described above, since the nutrient salt is added to the biological treatment tank 1 to which no coagulant is added, the nutrient salt is effectively used and absorbed by the microorganisms without being insolubilized, and is efficient. Biological treatment is possible. On the other hand, the aggregating agent added to the separation membrane tank 2 or the aggregating tank 20 is effectively used for aggregating and insolubilizing soluble biodegradable organic substances. Further, even in the case of overload, the biological treatment can be completely carried out in this biological treatment tank 1, so that BOD and intermediate products do not flow out, and this does not contaminate the separation membrane. Also, there is no problem of biofilm growth on the membrane surface. Therefore, it is possible to prevent deterioration of the membrane performance and perform stable and efficient membrane separation treatment for a long period of time.

【0024】[0024]

【発明の効果】以上詳述した通り、本発明の排水処理装
置によれば、栄養塩が不足している有機性排水に栄養塩
を添加して生物処理した後、凝集処理及び膜分離処理す
るに当り、栄養塩と凝集剤との反応の問題を解消し、添
加した栄養塩を微生物に有効に吸収利用させると共に、
凝集剤を凝集処理に有効に利用することができる。ま
た、過負荷の場合においても、BODや中間生成物、更
には生物膜で分離膜面が汚染されることが殆どなく、膜
性能の低下を防止して、長期にわたり安定かつ効率的な
処理を行える。これにより、有機性排水を効率的に処理
して、高水質処理水を安定に得ることができる。
As described in detail above, according to the wastewater treatment apparatus of the present invention, the organic wastewater lacking nutrient salts is biologically treated by adding the nutrient salt, and then subjected to the coagulation treatment and the membrane separation treatment. In doing so, the problem of the reaction between the nutrient salt and the flocculant is solved, and the added nutrient salt is effectively absorbed and utilized by the microorganisms,
The flocculant can be effectively used for the flocculation treatment. Further, even in the case of overload, the separation membrane surface is hardly contaminated with BOD, intermediate products, and further biofilms, preventing deterioration of membrane performance and performing stable and efficient treatment for a long time. You can do it. As a result, the organic wastewater can be efficiently treated and the high-quality treated water can be stably obtained.

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

【図1】本発明の排水処理装置の一実施例を示す系統図
である。
FIG. 1 is a system diagram showing an embodiment of a wastewater treatment device of the present invention.

【図2】本発明の排水処理装置の他の実施例を示す系統
図である。
FIG. 2 is a system diagram showing another embodiment of the wastewater treatment equipment of the present invention.

【図3】従来の装置を示す系統図である。FIG. 3 is a system diagram showing a conventional device.

【図4】従来の装置を示す系統図である。FIG. 4 is a system diagram showing a conventional device.

【符号の説明】[Explanation of symbols]

1 生物処理槽 2 分離膜槽 4,10,21 散気管 5 ブロワ 7 膜モジュール 8 吸引ポンプ 20 凝集槽 1 Biological treatment tank 2 Separation membrane tank 4,10,21 Air diffuser 5 Blower 7 Membrane module 8 Suction pump 20 Coagulation tank

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 有機性排水を生物処理する生物処理槽
と、該生物処理槽の流出液が導入される分離膜槽と、該
分離膜槽内に浸漬設置された膜モジュールと、前記生物
処理槽に栄養塩を添加する栄養塩添加手段と、前記分離
膜槽内の液又は前記流出液に凝集剤を添加する凝集剤添
加手段と、前記膜モジュールの透過水を処理水として取
り出す処理水取出手段とを備えてなることを特徴とする
排水処理装置。
1. A biological treatment tank for biologically treating organic wastewater, a separation membrane tank into which the effluent of the biological treatment tank is introduced, a membrane module immersed in the separation membrane tank, and the biological treatment. Nutrient salt adding means for adding nutrient salt to the tank, coagulant adding means for adding a coagulant to the liquid in the separation membrane tank or the effluent, and treated water extraction for taking out permeated water of the membrane module as treated water A wastewater treatment device comprising:
JP7258618A 1995-10-05 1995-10-05 Waste water treating equipment Pending JPH0999294A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7258618A JPH0999294A (en) 1995-10-05 1995-10-05 Waste water treating equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7258618A JPH0999294A (en) 1995-10-05 1995-10-05 Waste water treating equipment

Publications (1)

Publication Number Publication Date
JPH0999294A true JPH0999294A (en) 1997-04-15

Family

ID=17322787

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7258618A Pending JPH0999294A (en) 1995-10-05 1995-10-05 Waste water treating equipment

Country Status (1)

Country Link
JP (1) JPH0999294A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002273462A (en) * 2001-03-22 2002-09-24 Asahi Kasei Corp Method and device for treating waste water
JP2006026636A (en) * 2005-10-07 2006-02-02 Ebara Corp Solid-liquid separation method for activated sludge
JP2007160233A (en) * 2005-12-14 2007-06-28 Kurita Water Ind Ltd Organic matter-containing wastewater treatment apparatus and method
JPWO2006009125A1 (en) * 2004-07-16 2008-05-01 株式会社クラレ Wastewater treatment method with little excess sludge extraction
JP2009214082A (en) * 2008-03-13 2009-09-24 Kurita Water Ind Ltd Method and apparatus of biological treatment for organic material-containing water
WO2009140892A1 (en) * 2008-05-20 2009-11-26 北京汉青天朗水处理科技有限公司 Apparatus and process for treating wastewater
JP4680403B2 (en) * 2001-03-09 2011-05-11 住友重機械エンバイロメント株式会社 Wastewater treatment method and apparatus

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4680403B2 (en) * 2001-03-09 2011-05-11 住友重機械エンバイロメント株式会社 Wastewater treatment method and apparatus
JP2002273462A (en) * 2001-03-22 2002-09-24 Asahi Kasei Corp Method and device for treating waste water
JPWO2006009125A1 (en) * 2004-07-16 2008-05-01 株式会社クラレ Wastewater treatment method with little excess sludge extraction
JP4958551B2 (en) * 2004-07-16 2012-06-20 株式会社クラレ Wastewater treatment method with little excess sludge extraction
JP2006026636A (en) * 2005-10-07 2006-02-02 Ebara Corp Solid-liquid separation method for activated sludge
JP2007160233A (en) * 2005-12-14 2007-06-28 Kurita Water Ind Ltd Organic matter-containing wastewater treatment apparatus and method
JP2009214082A (en) * 2008-03-13 2009-09-24 Kurita Water Ind Ltd Method and apparatus of biological treatment for organic material-containing water
WO2009140892A1 (en) * 2008-05-20 2009-11-26 北京汉青天朗水处理科技有限公司 Apparatus and process for treating wastewater

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