JPS60187396A - Apparatus for biologically removing nitrogen in waste water - Google Patents

Apparatus for biologically removing nitrogen in waste water

Info

Publication number
JPS60187396A
JPS60187396A JP59041279A JP4127984A JPS60187396A JP S60187396 A JPS60187396 A JP S60187396A JP 59041279 A JP59041279 A JP 59041279A JP 4127984 A JP4127984 A JP 4127984A JP S60187396 A JPS60187396 A JP S60187396A
Authority
JP
Japan
Prior art keywords
zone
wastewater
aerobic zone
nitrogen
anaerobic zone
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.)
Granted
Application number
JP59041279A
Other languages
Japanese (ja)
Other versions
JPH0137988B2 (en
Inventor
Hironori Nakamura
裕紀 中村
Yasutomo Otake
康友 大竹
Tatsuo Sumino
立夫 角野
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 Construction Co Ltd
Hitachi Plant Technologies Ltd
Original Assignee
Hitachi Plant Construction Co Ltd
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 Construction Co Ltd, Hitachi Plant Technologies Ltd filed Critical Hitachi Plant Construction Co Ltd
Priority to JP59041279A priority Critical patent/JPS60187396A/en
Publication of JPS60187396A publication Critical patent/JPS60187396A/en
Publication of JPH0137988B2 publication Critical patent/JPH0137988B2/ja
Granted 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

Abstract

PURPOSE:To remove the nitrogen in the untreated water with a small-sized apparatus in a short time by immobilizing denitrifying bacteria and nitrifying bacteria on a carrier in high concn., and packing the carriers on which denitrifying bacteria are immobilized into the lower aeration zone of a single vessel which is separated into the upper and lower parts with a mesh screen. CONSTITUTION:The carriers 6 on which denitrifying bacteria are immobilized are packed and floated in an anaerobic zone 5 which is separated with a porous supporting material 3 which is fixed to a vessel body 1 above an inflow pipe 2 and a mesh screen 4 which is fixed at the middle part of the vessel body 1. The untreated water flows into the vessel body 1 from the inflow pipe 2, and flows into an aerobic zone 7 through the anaerobic zone 5. The nitrogen component in the waste water is oxidized to nitrous or nitric acid in the aerobic zone 7. A part of said oxidized nitrogen is returned to the anaerobic zone 5 by a pump 12, and denitrified by using organic materials in the waste water as a carbon source. The treated water flows out from an outflow pipe 10.

Description

【発明の詳細な説明】 〔発明の属する分野〕 この発明は、有機性廃水中の窒素外を生物学的気性ゾー
ンと嫌気性ゾーンにわたって、活性汚泥を含む廃水を循
環させ、窒素外を、好気性ゾーンにおいて活性汚泥中の
硝化菌を用いて硝化し、嫌気性ゾーンにおいて活性汚泥
中の脱窒菌を用いて脱窒することにより除去するよう構
成されている。
[Detailed Description of the Invention] [Field to which the invention pertains] This invention circulates wastewater containing activated sludge through a biological aerobic zone and an anaerobic zone to remove nitrogen from organic wastewater. It is configured to perform nitrification using nitrifying bacteria in activated sludge in the aerobic zone, and denitrify by using denitrifying bacteria in activated sludge in the anaerobic zone.

第1図は、従来の代表的な廃水の生物学的窒素除去装置
のフローシートを示す。原廃水は嫌気性ゾーン5から流
入し1次に好気性ゾーン7に流入する。廃水中の窒素分
は好気性ゾーン7において硝化菌によって亜硝酸あるい
は硝酸に酸化される。
FIG. 1 shows a flow sheet of a typical conventional wastewater biological nitrogen removal device. The raw wastewater flows from the anaerobic zone 5 and firstly flows into the aerobic zone 7. Nitrogen in the wastewater is oxidized to nitrite or nitric acid by nitrifying bacteria in the aerobic zone 7.

この酸化態窒素を含む活性汚泥混合液の一部は嫌気性ゾ
ーン5に戻され、脱窒菌によって窒素ガスに還元され、
残りの混合液は沈殿槽14に流入する。沈殿槽14の上
澄水は放流され、沈殿汚泥は。
A part of the activated sludge mixture containing this oxidized nitrogen is returned to the anaerobic zone 5, where it is reduced to nitrogen gas by denitrifying bacteria.
The remaining mixed liquid flows into the settling tank 14. The supernatant water in the settling tank 14 is discharged, and the settled sludge is removed.

一部引き抜かれ残りは嫌気性ゾーン5に返送される。A portion is pulled out and the rest is returned to anaerobic zone 5.

このように、従来装置においては、硝化菌と脱ゾーンに
浮遊する活性汚泥中の硝化菌は窒素の除去に関与するこ
とができない。また、好気性ゾーンに硝化菌を、嫌気性
ゾーンに脱窒菌をそれぞれ高濃度に保持することが困難
である。特に水温の低下する冬期には、増殖速度の遅い
硝化菌が活性汚泥中にごくわずかしか存在しない状態と
なる。
Thus, in the conventional apparatus, the nitrifying bacteria and the nitrifying bacteria in the activated sludge floating in the dezoning cannot participate in the removal of nitrogen. Furthermore, it is difficult to maintain high concentrations of nitrifying bacteria in the aerobic zone and high concentrations of denitrifying bacteria in the anaerobic zone. Particularly in the winter when the water temperature drops, only a small number of nitrifying bacteria, which grow slowly, exist in activated sludge.

そのため窒素除去のために大容積の装置で長時間処理し
なければならない欠点があった。さらに処理水を得るた
めに、最終工程で浮遊汚泥を沈殿させるために大型の沈
殿槽を設けなければならないことも大きな欠点であった
For this reason, there was a drawback that the process had to be carried out for a long time using a large-capacity device in order to remove nitrogen. Another major drawback was that in order to obtain treated water, a large settling tank had to be installed in order to settle floating sludge in the final step.

〔発明の目的] この発明の目的は、前記従来技術の欠点を解消し、沈殿
池が不要でコン・ξクトな装置で、短時間で廃水の窒素
除去が可能な生物学的窒素除去装置を提供することにあ
る。
[Object of the Invention] The object of the present invention is to eliminate the drawbacks of the prior art described above, and to provide a biological nitrogen removal device that does not require a sedimentation tank and is a compact device that can remove nitrogen from wastewater in a short time. It is about providing.

〔発明の要点〕[Key points of the invention]

この発明は、脱窒菌および硝化菌をそれぞれ積極的に高
濃度に担体に固定し、網目スクリーンによって上下に仕
切られた単槽の下部嫌気性ゾーンに脱窒菌の固定化担体
を充填し、散気装置により曝気される上部好気性ゾーン
に硝化菌の固定化担体を保持し、有機性廃水を下部嫌気
性ゾーンよシ流入させ処理水を上部好気性ゾーンよシ流
出させるよう構成したものである。
This invention actively immobilizes denitrifying bacteria and nitrifying bacteria on carriers at high concentrations, fills the lower anaerobic zone of a single tank divided into upper and lower parts with a mesh screen, and then diffuses air. The structure is such that immobilized carriers of nitrifying bacteria are held in the upper aerobic zone that is aerated by the device, organic wastewater flows into the lower anaerobic zone, and treated water flows out through the upper aerobic zone.

〔発明の実施例〕[Embodiments of the invention]

第2図および第3図は、担体としてポリアクリルアミド
ゲルを用い、その内部にそれぞれ硝化菌と脱窒菌を包括
してNT(4−N含有廃水、 NO3−N含有廃水をそ
れぞれ単独に処理した場合の処理性能即ち滞留時間と処
理水質の関係を示したものである。いずれの場合も短時
間で処理可能なことがわかる。
Figures 2 and 3 show the case where NT (4-N-containing wastewater and NO3-N-containing wastewater were treated separately) using polyacrylamide gel as a carrier and enclosing nitrifying bacteria and denitrifying bacteria, respectively. This figure shows the relationship between treatment performance, that is, residence time, and treated water quality.It can be seen that treatment is possible in a short time in either case.

第4図はこの発明に係る廃水の生物学的窒素除去装置の
一実施例の断面図を示す。
FIG. 4 shows a sectional view of an embodiment of the biological nitrogen removal device for wastewater according to the present invention.

槽体1の下部に流入管2を付設する。An inflow pipe 2 is attached to the lower part of the tank body 1.

流入管2の上方に槽体1に固定された多孔の支網目スク
リーン4の一ヒ方に区劃された好気性ゾーン7に散気装
置8を付設し空気または酸素を吹込んで好気性に保つ。
An aeration device 8 is attached to an aerobic zone 7 separated on one side of a porous branch mesh screen 4 fixed to the tank body 1 above the inflow pipe 2, and air or oxygen is blown into the aerobic zone to maintain aerobic conditions. .

好気性ゾーン7に硝化菌を固定した担体9を充填して浮
遊させる。
The aerobic zone 7 is filled with a carrier 9 on which nitrifying bacteria are fixed and suspended.

好気性ゾーン7の上部には流出管lOを付設する。好気
性ゾーン7と嫌気性ゾーン5とを連結する配管工lの途
中にポンプ12を付設する。
An outflow pipe IO is attached to the upper part of the aerobic zone 7. A pump 12 is attached in the middle of a plumber 1 that connects an aerobic zone 7 and an anaerobic zone 5.

槽体lの下部に汚泥引抜管13を付設する。A sludge drawing pipe 13 is attached to the lower part of the tank body l.

廃水は流入管2から槽体1に流入し嫌気性ゾーン5を経
て好気性ゾーン7に流入する。
Wastewater flows into the tank body 1 from the inflow pipe 2, passes through the anaerobic zone 5, and flows into the aerobic zone 7.

好気性ゾーン7において、廃水中の窒素分は亜硝酸ある
いは硝酸に酸化される。
In the aerobic zone 7, nitrogen in the wastewater is oxidized to nitrite or nitric acid.

これらの酸化態窒素の一部は、ポンプ12によって嫌気
性ゾーン5に戻され、廃水中の有機物を炭素源として脱
窒される。処理された処理水は流出管10より流出する
A portion of these oxidized nitrogen is returned to the anaerobic zone 5 by the pump 12 and denitrified using organic matter in the wastewater as a carbon source. The treated water flows out from the outflow pipe 10.

廃水中の沈殿性の固形成分および固定化担体内おいては
、硝化菌と脱窒菌をそれぞれ積極的に高濃度に担体に保
持し、さらにそれらを別々の好気性および嫌気性ゾーン
に保持することによって。
In the precipitable solid components and immobilized carriers of wastewater, nitrifying bacteria and denitrifying bacteria are actively retained in the carrier at high concentrations, and furthermore, they are retained in separate aerobic and anaerobic zones. By.

硝化、脱窒の機能を有効に発揮させることができるので
、廃水の窒素除去をごく短時間に行うことができる。特
に、水温が低下し、硝化、脱窒の反応速度および菌体の
増殖速度が遅くなる冬期においても、菌体が担体に高濃
度に保持されるので十分な処理が可能である。
Since the functions of nitrification and denitrification can be effectively exhibited, nitrogen can be removed from wastewater in a very short time. In particular, even in the winter when the water temperature is low and the reaction rates of nitrification and denitrification and the growth rate of bacterial cells are slow, sufficient treatment is possible because the bacterial cells are retained in the carrier at a high concentration.

また、菌体を担体に固定することにより、従来のような
浮遊型の活性汚泥法による窒素除去装置において生成す
る膨大な量の余剰汚泥をごくわずかに抑えることができ
る。これは、菌体の増殖を伴わない酵素反応が主となっ
て廃水が処理されるためだと考えられる。このように余
剰汚泥量が微量であるので従来のような大型の沈殿槽を
必要とせず、コンパクトな単槽で廃水の処理が可能であ
20〜:v1my7tの下水を用いた。硝化菌及び脱窒
菌の固定化担体として、直径3叫長さ4聴の円柱状のポ
リアクリルアミドゲルを用いた。嫌気性ゾーンに脱窒菌
の固定化担体を充填率55%で充填し、好気性ゾーンに
硝化菌の固定化担体を充填率40%で充填して、第4図
に示す装置により第1表に示す条件で処理を行った。
Furthermore, by immobilizing the bacterial cells on a carrier, the enormous amount of surplus sludge produced in a conventional nitrogen removal device using the floating activated sludge method can be suppressed to a very small amount. This is thought to be because wastewater is treated mainly by enzymatic reactions that do not involve the growth of bacterial cells. Since the amount of surplus sludge is thus small, there is no need for a large sedimentation tank like in the past, and the wastewater can be treated with a compact single tank, and sewage of 20 to 15 tons was used. A cylindrical polyacrylamide gel with a diameter of 3 cm and a length of 4 cm was used as a carrier for immobilizing nitrifying bacteria and denitrifying bacteria. The anaerobic zone was filled with denitrifying bacteria immobilized carriers at a filling rate of 55%, and the aerobic zone was filled with nitrifying bacteria immobilized carriers at a filling rate of 40%. Treatments were performed under the conditions shown.

第 1 表 第2表 比較のため、同じ原廃水を用いて第1図に示す装置によ
り処理した。その際の条件を従来例1゜従来例2として
示す。 ゛ 第2表は、約2ケ月連続処理したときの処理水質を示す
。従来例では硝化あるいは脱窒が不十分であり、 NH
4NあるいはN03−Nが多く残存する。これに対して
、この発明に係る廃水の生物学的窒素除去装置によれば
、従来装置より短い滞留時間で良好な処理水質が得られ
る。
Table 1 Table 2 For comparison, the same raw wastewater was treated with the apparatus shown in Figure 1. The conditions at that time are shown as Conventional Example 1 and Conventional Example 2.゛Table 2 shows the quality of treated water after continuous treatment for about two months. In conventional methods, nitrification or denitrification is insufficient, and NH
A large amount of 4N or N03-N remains. On the other hand, according to the biological nitrogen removal device for wastewater according to the present invention, good treated water quality can be obtained with a shorter residence time than the conventional device.

〔発明の変形例、応用例〕[Modifications and application examples of the invention]

前記実施例においては、硝化菌あるいは脱窒菌を固定す
る担体としてポリアクリルアミドゲルを用いたが、その
他アルギン酸カルシウム、に−カし、膜を透過する流出
水を処理水とすることにより、浮遊固形物をほぼ完全に
除去することができる。膜材質としては、スルホン化ポ
リスルホン。
In the above examples, polyacrylamide gel was used as a carrier to immobilize nitrifying bacteria or denitrifying bacteria, but other materials such as calcium alginate and gel were used to treat suspended solids by using the effluent that passed through the membrane as treated water. can be almost completely removed. The membrane material is sulfonated polysulfone.

多孔質ガラス、セラミック、多孔質金属などを用いるこ
とができる。
Porous glass, ceramic, porous metal, etc. can be used.

〔発明の効果〕〔Effect of the invention〕

この発明によれば、コンパクトな装置で短時間で廃水中
の窒素を除去することができる。
According to this invention, nitrogen in wastewater can be removed in a short time using a compact device.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は従来の生物学的窒素除去装置のフローシート、
第2図は硝化菌固定アクリルアミドゲルによるNF(4
−N の処理性能、第3図は脱窒菌固定アクリルアミド
ゲルによるNO3−N の処理性能。 第4図はこの発明に係る廃水の生物学的窒素除去装置の
1実施例の断面図を示す。 1・・・槽体 2・・・流入管 3・・・支持材 4・・・網目スクリーン5・・・嫌気
性ゾーン 6・・・脱窒菌を固定した担体7・・・好気
性ゾーン 8・・散気装置9・・・硝化菌を固定した担
体 10・・・流出管11・・・配 管 12・・・ポ
ンプ 13・・・汚泥引抜管。 第1図 −iV時間(h) 第4図 沸V時間(h)
Figure 1 is a flow sheet of a conventional biological nitrogen removal device.
Figure 2 shows NF (4
Figure 3 shows the treatment performance of NO3-N using denitrifying bacteria-immobilized acrylamide gel. FIG. 4 shows a sectional view of one embodiment of the biological nitrogen removal device for wastewater according to the present invention. 1... Tank body 2... Inflow pipe 3... Support material 4... Mesh screen 5... Anaerobic zone 6... Carrier with fixed denitrifying bacteria 7... Aerobic zone 8. - Air diffuser 9...Carrier with fixed nitrifying bacteria 10...Outflow pipe 11...Piping 12...Pump 13...Sludge drawing pipe. Figure 1 - iV time (h) Figure 4 Boiling V time (h)

Claims (1)

【特許請求の範囲】 l、有機性廃水を好気性ゾーンと嫌気性ゾーンとを循環
させて窒素外を硝化脱窒する廃水の生物学的窒素除去装
置において、槽体の下部に付設した流入管と、この流入
管の上方に槽体に固定された支持材と、この支持材と槽
体の中部に固定された網目スクリーンとによって区劃さ
れた嫌気性ゾーンに充填されて脱窒菌を固定した担体と
、前記網目スクリーンの上方に区劃されて散気装置を備
えた好気性ゾーンに充填されて硝化菌を固定した担体と
。 前記好気性ゾーンの上部に付設された流出管と、前記好
気性ゾーンと嫌気性ゾーンとを連結する配管と、この配
管の途中に付設されたポンプとより成ることを特徴とす
る廃水の生物学的窒素除去装置。 2、好気性ゾーンに中空糸膜を設置して、この中空糸膜
を流出管に接続したことを特徴とする特許請求の範囲第
1項記載の廃水の生物学的窒素除去装置。
[Claims] l. In a biological nitrogen removal device for wastewater that circulates organic wastewater between an aerobic zone and an anaerobic zone to nitrify and denitrify nitrogen, an inflow pipe attached to the lower part of a tank body. Then, an anaerobic zone defined by a support material fixed to the tank body above the inflow pipe, and a mesh screen fixed to the support material and the middle part of the tank body was filled with denitrifying bacteria. a carrier; and a carrier having nitrifying bacteria immobilized thereon, which is filled in an aerobic zone that is partitioned above the mesh screen and equipped with an air diffuser. Wastewater biology characterized by comprising an outflow pipe attached to the upper part of the aerobic zone, a pipe connecting the aerobic zone and the anaerobic zone, and a pump attached in the middle of this pipe. Nitrogen removal equipment. 2. The biological nitrogen removal device for wastewater according to claim 1, characterized in that a hollow fiber membrane is installed in the aerobic zone and this hollow fiber membrane is connected to an outflow pipe.
JP59041279A 1984-03-06 1984-03-06 Apparatus for biologically removing nitrogen in waste water Granted JPS60187396A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59041279A JPS60187396A (en) 1984-03-06 1984-03-06 Apparatus for biologically removing nitrogen in waste water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59041279A JPS60187396A (en) 1984-03-06 1984-03-06 Apparatus for biologically removing nitrogen in waste water

Publications (2)

Publication Number Publication Date
JPS60187396A true JPS60187396A (en) 1985-09-24
JPH0137988B2 JPH0137988B2 (en) 1989-08-10

Family

ID=12604006

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59041279A Granted JPS60187396A (en) 1984-03-06 1984-03-06 Apparatus for biologically removing nitrogen in waste water

Country Status (1)

Country Link
JP (1) JPS60187396A (en)

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63171697A (en) * 1986-10-01 1988-07-15 オー・テ・ヴエ(オムニオン・ドウ・トレトマン・エ・ドウ・ヴアロリザシオン) Waste water purifying method used for biological treatment in granular material bed
JPH0248198U (en) * 1988-09-30 1990-04-03
JPH03258396A (en) * 1990-03-08 1991-11-18 Ebara Infilco Co Ltd Sewage treating device
JPH0461993A (en) * 1990-06-28 1992-02-27 Ebara Infilco Co Ltd Method and apparatus for biological nitration and denitrification of organic polluted water
EP0489626B1 (en) * 1990-12-03 1994-03-30 Degremont Reactor for biological oxidation and reduction; process for biofiltration and process for rinsing the reactor
JPH06142668A (en) * 1992-11-02 1994-05-24 Ebara Infilco Co Ltd Purifying treatment device for organic sewage
KR20010103887A (en) * 2000-05-09 2001-11-24 김홍렬 Waste water processing device used as the device for eliminating nitrogen and organic materials
JP4581211B2 (en) * 2000-10-05 2010-11-17 栗田工業株式会社 Biological denitrification equipment
JP2010269203A (en) * 2009-05-19 2010-12-02 Nikkiso Co Ltd Waste water treatment apparatus and method of controlling the same
CN104609550A (en) * 2013-11-05 2015-05-13 中国石油化工股份有限公司 Method for removing ammonia nitrogen in wastewater by use of immobilized sludge particles
JP2020028836A (en) * 2018-08-21 2020-02-27 積水化学工業株式会社 Waste water treatment apparatus

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005005327A1 (en) * 2003-07-10 2005-01-20 Ebara Corporation Water purification high-level treatment method and apparatus

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63171697A (en) * 1986-10-01 1988-07-15 オー・テ・ヴエ(オムニオン・ドウ・トレトマン・エ・ドウ・ヴアロリザシオン) Waste water purifying method used for biological treatment in granular material bed
JPH0450880B2 (en) * 1986-10-01 1992-08-17 Oo Te Ue Omunion Do Toretoman E Do Uarorizashion
JPH0248198U (en) * 1988-09-30 1990-04-03
JPH03258396A (en) * 1990-03-08 1991-11-18 Ebara Infilco Co Ltd Sewage treating device
JPH0461993A (en) * 1990-06-28 1992-02-27 Ebara Infilco Co Ltd Method and apparatus for biological nitration and denitrification of organic polluted water
EP0489626B1 (en) * 1990-12-03 1994-03-30 Degremont Reactor for biological oxidation and reduction; process for biofiltration and process for rinsing the reactor
JPH06142668A (en) * 1992-11-02 1994-05-24 Ebara Infilco Co Ltd Purifying treatment device for organic sewage
KR20010103887A (en) * 2000-05-09 2001-11-24 김홍렬 Waste water processing device used as the device for eliminating nitrogen and organic materials
JP4581211B2 (en) * 2000-10-05 2010-11-17 栗田工業株式会社 Biological denitrification equipment
JP2010269203A (en) * 2009-05-19 2010-12-02 Nikkiso Co Ltd Waste water treatment apparatus and method of controlling the same
CN104609550A (en) * 2013-11-05 2015-05-13 中国石油化工股份有限公司 Method for removing ammonia nitrogen in wastewater by use of immobilized sludge particles
JP2020028836A (en) * 2018-08-21 2020-02-27 積水化学工業株式会社 Waste water treatment apparatus

Also Published As

Publication number Publication date
JPH0137988B2 (en) 1989-08-10

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