JP2002143895A - Decomposition method for excess sludge - Google Patents

Decomposition method for excess sludge

Info

Publication number
JP2002143895A
JP2002143895A JP2000344638A JP2000344638A JP2002143895A JP 2002143895 A JP2002143895 A JP 2002143895A JP 2000344638 A JP2000344638 A JP 2000344638A JP 2000344638 A JP2000344638 A JP 2000344638A JP 2002143895 A JP2002143895 A JP 2002143895A
Authority
JP
Japan
Prior art keywords
sludge
microorganisms
contact
excess sludge
tank
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
JP2000344638A
Other languages
Japanese (ja)
Inventor
Masahiko Nihei
正彦 二瓶
Megumi Nishida
恵 西田
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.)
JOBAN KAIHATSU KK
Original Assignee
JOBAN KAIHATSU KK
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 JOBAN KAIHATSU KK filed Critical JOBAN KAIHATSU KK
Priority to JP2000344638A priority Critical patent/JP2002143895A/en
Publication of JP2002143895A publication Critical patent/JP2002143895A/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
    • Y02W10/20Sludge processing

Landscapes

  • Treatment Of Sludge (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a decomposition method for excess sludge mainly composed of lower microorganisms, such as bacteria which entirely eliminates the discharge of the excess sludge by decomposing the excess sludge by the food chain of higher microorganisms, such as Protozoa and Metazoa. SOLUTION: The excess sludge 11 mainly composed of the lower microorganisms generated and propagated by biological treatment of sewage 2 is introduced to contact aerators 15A and 15B provided with contact materials 18 and air diffusion pipes 5 for ejecting air bubbles where the higher microorganisms, such as the Protozoa and Metazoa, living in the contact materials 18 of the contact aerators 15A and 15B prey on the sludge and the sludge is decomposed by the food chain. The treated water thereof is introduced to a settling tank 16 from which the supernatant 8 is drained. The residues 20, such as the settled microorganisms, is returned to the contact aerator 15A and the sludge is repetitively treated.

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】本発明は細菌類などの低級微
生物を主体とする余剰汚泥を、原生動物、後生動物など
の高級微生物の食物連鎖により分解処理する方法に関す
るものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for decomposing excess sludge mainly composed of low-grade microorganisms such as bacteria by a food chain of higher-grade microorganisms such as protozoa and metazoa.

【0002】[0002]

【従来の技術】一般に汚水に含まれている有機物を微生
物により浄化する活性汚泥処理法が行なわれているが、
これは処理した汚水を沈殿槽で沈殿させて、上澄液を排
水した後に、沈殿した余剰汚泥を処理する必要がある。
2. Description of the Related Art An activated sludge treatment method for purifying organic substances contained in sewage by microorganisms has been generally performed.
In this method, it is necessary to settle the treated sewage in a settling tank, drain the supernatant, and then treat the settled excess sludge.

【0003】従来この余剰汚泥の処理方法としては、汚
泥濃縮槽などで濃縮した後、脱水機で脱水してから埋め
立て処分や焼却処分などを行なっている。しかしながら
この処分方法は手間がかかり処理コストが高く、しかも
埋め立て処分場や二酸化炭素の大量排出の問題がある。
Conventionally, as a method of treating excess sludge, the sludge is concentrated in a sludge concentration tank or the like, then dewatered by a dehydrator, and then landfilled or incinerated. However, this disposal method is laborious and expensive, and has the problems of landfill sites and the emission of large amounts of carbon dioxide.

【0004】また最近注目されてきている余剰汚泥の処
理方法として、汚泥の主体である細菌類などの低級微生
物を取り出して、オゾン酸化や薬品により酸化して微生
物を可溶化し、再び有機物として微生物処理を行なう方
法がある。また取り出した低級微生物をミルですり潰
し、可溶化させて微生物処理する方法もある。しかしな
がらこれらの低級微生物を取り出して処理する方法は手
間やコストがかかる問題がある。
As a method for treating excess sludge, which has recently attracted attention, low-grade microorganisms such as bacteria, which are the main components of sludge, are taken out, oxidized by ozone oxidation or chemicals to solubilize the microorganisms, and converted into microorganisms again as organic matter. There is a method of performing processing. There is also a method in which the low-grade microorganisms taken out are ground by a mill, solubilized, and treated with microorganisms. However, the method of taking out and treating these low-grade microorganisms has a problem that it is troublesome and costly.

【0005】[0005]

【発明が解決しようとする課題】本発明は上記問題点を
改善し、後生動物などの高級微生物の食物連鎖により細
菌類などの低級微生物を主体とする余剰汚泥を分解して
その排出を大幅に削減した余剰汚泥の分解処理方法を提
供するものである。
DISCLOSURE OF THE INVENTION The present invention solves the above-mentioned problems, and decomposes excess sludge mainly composed of low-grade microorganisms such as bacteria by the food chain of higher-grade microorganisms such as metazoans to greatly reduce the discharge. An object of the present invention is to provide a method of decomposing excess sludge that has been reduced.

【0006】[0006]

【課題を解決するための手段】本発明の請求項1記載の
余剰汚泥の分解処理方法は、汚水を生物処理して発生増
殖した細菌類などの低級微生物を主体とする余剰汚泥
を、接触材と水中に気泡を噴出する曝気手段とを設けた
接触曝気槽に導き、この接触曝気槽の接触材に生息して
いる原生動物、後生動物などの高級微生物により余剰汚
泥の低級微生物を捕食する食物連鎖により前記汚泥を分
解し、この処理水を沈殿槽に導いて、上澄液を排水する
と共に、ここで沈殿した微生物などの残渣を前記接触曝
気槽に戻して繰り返し処理することを特徴とするもので
ある。
According to a first aspect of the present invention, there is provided a method for decomposing excess sludge, comprising the steps of: treating excess sludge mainly composed of low-grade microorganisms such as bacteria generated and grown by biologically treating sewage with a contact material; And a contact aeration tank provided with aeration means for ejecting air bubbles into the water, and food that feeds on lower-grade microorganisms of excess sludge by high-grade microorganisms such as protozoa and metazoans living in the contact material of the contact aeration tank. The sludge is decomposed by a chain, the treated water is guided to a sedimentation tank, the supernatant is drained, and residues such as microorganisms precipitated here are returned to the contact aeration tank and repeatedly treated. Things.

【0007】本発明の請求項2記載の余剰汚泥の分解処
理方法は、接触材が、表面に多数の突起を取付けた紐状
の芯材で形成され、これを螺旋状に巻回して表面に原生
動物、後生動物などの高級微生物を付着繁殖させること
を特徴とするものである。
According to a second aspect of the present invention, in the method for decomposing excess sludge, the contact material is formed of a cord-like core material having a large number of protrusions attached to the surface, and the contact material is spirally wound on the surface. It is characterized in that higher-grade microorganisms such as protozoa and metazoans are attached and propagated.

【0008】[0008]

【発明の実施の形態】以下本発明の実施の一形態を図1
を参照して詳細に説明する。図において1は調整槽で、
ここに流入した汚水2を貯水するものである。この調整
槽1に隣接して曝気槽3が設けられ、調整槽1からポン
プ4で汚水2が送り込まれるようになっている。曝気槽
3の底部側には、汚水2中に気泡を噴出する散気管5が
設けられている。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS One embodiment of the present invention is shown in FIG.
This will be described in detail with reference to FIG. In the figure, 1 is an adjustment tank,
The sewage 2 that has flowed in here is stored. An aeration tank 3 is provided adjacent to the adjustment tank 1, and sewage 2 is sent from the adjustment tank 1 by a pump 4. On the bottom side of the aeration tank 3, there is provided an air diffuser 5 for ejecting bubbles into the wastewater 2.

【0009】また曝気槽3に隣接して沈殿槽6が設けら
れ、上澄液8は隣接する消毒槽10に排水され、沈殿し
た余剰汚泥11の一部を前記曝気槽3に戻すようになっ
ている。消毒槽10では上澄液8に消毒液供給装置12
から消毒液を添加して殺菌した処理水9を外部に排水す
るようになっている。ここまでの装置は従来の活性汚泥
処理装置と同様である。
A settling tank 6 is provided adjacent to the aeration tank 3, and the supernatant 8 is drained to an adjacent disinfecting tank 10, and a part of the settled excess sludge 11 is returned to the aeration tank 3. ing. In the disinfecting tank 10, the supernatant 8 is supplied to the disinfecting solution supply device 12.
The treated water 9 sterilized by adding an antiseptic solution is drained to the outside. The apparatus up to this point is the same as the conventional activated sludge treatment apparatus.

【0010】本発明では、上記沈殿槽6で沈殿した余剰
汚泥11の大部分を、汚泥貯槽13に送り、ここに貯め
られた余剰汚泥11を汚泥処理装置14に供給するよう
になっている。この汚泥処理装置14は、2槽の接触曝
気槽15A、15Bが併設され、更にこれに隣接して沈
殿槽16が設けられている。
In the present invention, most of the excess sludge 11 settled in the settling tank 6 is sent to a sludge storage tank 13 and the excess sludge 11 stored therein is supplied to a sludge treatment device 14. This sludge treatment apparatus 14 is provided with two contact aeration tanks 15A and 15B, and further provided with a settling tank 16 adjacent thereto.

【0011】また前記接触曝気槽15A、15Bは、水
中に気泡を噴出する散気管5が底部側に設けられている
と共に、槽内に可撓性を有する紐状の芯材の表面に多数
の突起を取付けて、これを螺旋状に巻回した多数の接触
材18が支持フレーム19に支持されている。この接触
材18の表面には原生動物、後生動物などの高級微生物
が付着して生息している。また沈殿槽16には一段目の
接触曝気槽15に残渣20を戻す残渣返送管21が設け
られている。
In the contact aeration tanks 15A and 15B, a diffuser tube 5 for ejecting air bubbles into water is provided on the bottom side, and a large number of flexible cord-like core members are provided in the tank. A large number of contact members 18 having projections attached and spirally wound around the projections are supported by a support frame 19. High-grade microorganisms such as protozoa and metazoans adhere to the surface of the contact material 18 and inhabit. The settling tank 16 is provided with a residue return pipe 21 for returning the residue 20 to the first-stage contact aeration tank 15.

【0012】上記構成の装置により汚水2を生物処理し
て発生した余剰汚泥11を処理する方法について説明す
る。先ず下水や工場廃水などの汚水2を調整槽1に導き
ここに貯水する。ここに貯水された汚水2はポンプ4に
より隣接する曝気槽3に供給される。曝気槽3では汚水
2中に気泡を噴出する散気管5が設けられ、ここから空
気が汚水2中に噴出し、汚水2は対流しながら、図2に
示すようにイオウ菌や糸状菌、ズーグレアなど細菌類に
より汚水2に含まれている有機物が炭酸ガスと水に分解
される。この分解された水と、有機物を栄養として増殖
した細菌類は、隣接する沈殿槽6に送られる。
A method of treating the excess sludge 11 generated by biologically treating the sewage 2 with the above-described apparatus will be described. First, sewage 2 such as sewage or factory wastewater is led to the regulating tank 1 and stored therein. The sewage 2 stored here is supplied to an adjacent aeration tank 3 by a pump 4. The aeration tank 3 is provided with an air diffuser 5 for blowing air bubbles into the sewage 2 from which air is blown into the sewage 2, and the sewage 2 is convectively flowing, as shown in FIG. Organic matter contained in the sewage 2 is decomposed into carbon dioxide and water by bacteria. The decomposed water and the bacteria grown using the organic matter as nutrients are sent to the adjacent settling tank 6.

【0013】沈殿槽6では上澄液8と、汚水2を生物処
理して発生増殖した低級微生物を主成分とする余剰汚泥
11とに分離される。上澄液8は消毒槽10に送られ
て、ここで消毒液供給装置12から消毒液を添加して殺
菌し、殺菌された処理水9は外部に排水される。
In the sedimentation tank 6, the supernatant 8 and the excess sludge 11 mainly composed of low-grade microorganisms generated and grown by biological treatment of the wastewater 2 are separated. The supernatant liquid 8 is sent to a disinfecting tank 10, where the disinfecting liquid is added from a disinfecting liquid supply device 12 to sterilize, and the sterilized treated water 9 is drained to the outside.

【0014】また沈殿槽6で沈殿した、低級微生物を主
成分とする余剰汚泥11の一部は汚泥返送管7で曝気槽
3に戻されて、再び汚水2の生物処理に利用される。ま
た残りの余剰汚泥11は汚泥貯槽13に送られてここに
貯められる。この余剰汚泥11は汚泥貯槽13からポン
プ4で汚泥処理装置14の一段目の接触曝気槽15Aに
送られる。
A part of the excess sludge 11 mainly composed of low-grade microorganisms settled in the sedimentation tank 6 is returned to the aeration tank 3 by a sludge return pipe 7 and reused for biological treatment of the wastewater 2. The remaining excess sludge 11 is sent to a sludge storage tank 13 where it is stored. The surplus sludge 11 is sent from the sludge storage tank 13 by the pump 4 to the first-stage contact aeration tank 15A of the sludge treatment device 14.

【0015】接触曝気槽15A、15Bには、支持フレ
ーム19に多数の接触材18が支持され、この接触材1
8の表面にはゾウリムシやツリガネムシなどの原生動物
や、ワムシなどの後生動物など高級微生物が付着して生
息している。更に接触曝気槽15A、15Bの底部側に
は散気管5が設けられ、ここから余剰汚泥11中に気泡
が噴出し、余剰汚泥11は対流しながら、接触材18に
付着して生息している原生動物や後生動物などの高級微
生物により余剰汚泥11中に含まれる細菌類などの低級
微生物が捕食されて炭酸ガスと水に分解される。
In the contact aeration tanks 15A and 15B, a large number of contact members 18 are supported by a support frame 19.
Higher-grade microorganisms such as protozoa such as Paramecium and Vinebug and metazoans such as rotifer adhere to the surface of No. 8 and inhabit. Further, a diffuser 5 is provided on the bottom side of the contact aeration tanks 15A and 15B, from which bubbles are blown out into the excess sludge 11, and the excess sludge 11 adheres to the contact material 18 while convectively flowing. Higher-grade microorganisms such as protozoa and metazoans prey on lower-grade microorganisms such as bacteria contained in the excess sludge 11 and are decomposed into carbon dioxide and water.

【0016】一段目の接触曝気槽15Aでは図2に示す
ように先ず、余剰汚泥11の主成分である細菌類が、ゾ
ウリムシやツリガネムシなどの原生動物により捕食さ
れ、更に原生動物がワムシなどの後生動物に捕食され
る。増殖した原生動物や後生動物などの高級微生物と、
分解していない低級微生物は更に隣接して設けた二段目
の接触曝気槽15Bに供給される。接触曝気槽15Bの
接触材18には、主として原生動物や後生動物、ミミ
ズ、ミジンコなどの高級微生物が付着して生息してい
る。
In the first-stage contact aeration tank 15A, first, as shown in FIG. 2, bacteria which are the main components of the excess sludge 11 are preyed on by protozoa such as paramecium and vorticella. Preyed by animals. High-grade microorganisms such as protozoa and metazoans that have multiplied,
The low-grade microorganisms that have not been decomposed are supplied to a second-stage contact aeration tank 15B provided adjacently. The contact material 18 of the contact aeration tank 15B is inhabited by high-grade microorganisms such as protozoa and metazoa, earthworms, and daphnia.

【0017】この二段目の接触曝気槽15B内で、散気
管5から噴出する気泡により対流しながら、接触材18
に付着して生息している原生動物により未分解の低級微
生物が捕食され、増殖した原生動物は後生動物に捕食さ
れ、更に増殖した原生動物はミミズやミジンコなどに捕
食されて、食物連鎖を繰り返して余剰汚泥11は次第に
水に分解されていく。
In the contact aeration tank 15B of the second stage, the contact material 18
Undegraded low-grade microorganisms are eaten by protozoa that inhabit and inhabit, and protozoa that have proliferated are eaten by metazoans, and protozoa that have proliferated are preyed on by earthworms and daphnia, repeating the food chain. The surplus sludge 11 is gradually decomposed into water.

【0018】この分解した水と、未分解の原生動物や後
生動物などの高級微生物は沈殿槽16に送られて、ここ
で分離した上澄液8は外部に排水され、沈殿した未分解
の原生動物や後生動物などの高級微生物は残渣返送管2
1により一段目の接触曝気槽15Aに戻される。
The decomposed water and high-grade microorganisms such as undegraded protozoa and metazoan are sent to a sedimentation tank 16, and the supernatant liquid 8 separated here is drained to the outside, and For high-grade microorganisms such as animals and metazoans, return pipe 2
1 returns to the first stage contact aeration tank 15A.

【0019】一段目の接触曝気槽15Aに戻された原生
動物や後生動物などの高級微生物は接触材18に付着し
て生息し、以下、捕食量と流入細菌量(余剰汚泥投入
量)のバランスをとることにより、同様の食物連鎖を繰
り返えして余剰汚泥11を水に分解して処理することが
できる。従って、余剰汚泥11を埋め立て処分や焼却処
分していた従来方法に比べて、本発明は簡単な汚泥処理
装置14を付加するだけで、余剰汚泥11をほぼ完全に
分解処理して処理コストを大幅に削減することができ
る。
High-grade microorganisms such as protozoa and metazoans returned to the first-stage contact aeration tank 15A adhere to the contact material 18 and inhabit, and the balance between the amount of predation and the amount of inflowing bacteria (the amount of surplus sludge input) is described below. By repeating the same food chain, surplus sludge 11 can be decomposed into water and treated. Therefore, compared with the conventional method in which the surplus sludge 11 is disposed of by landfill or incineration, the present invention only requires the addition of a simple sludge treatment device 14 to substantially completely disassemble the surplus sludge 11 and greatly increase the treatment cost. Can be reduced.

【0020】本発明の汚泥処理装置14を用いて分解処
理実験を行なった。31,000mg/Lの懸濁物質
(SS)を含む余剰汚泥11を分解処理したところ、4
日間で18,000mg/Lに減少し、1日当たり10
%以上低減させることができた。5日目からは接触曝気
槽15Aに余剰汚泥11を毎日供給しながら連続的に処
理を行なったところ、10日目からはほぼ一定の状態に
達し、供給した余剰汚泥11はほぼ完全に処理されて水
に分解されていることが確認された。また接触曝気槽1
5Bの接触材18にはミミズが生息していた。つまり高
級な微生物であるミミズが生息していることは食物連鎖
が行なわれていることの証拠である。
A decomposition treatment experiment was performed using the sludge treatment apparatus 14 of the present invention. When excess sludge 11 containing 31,000 mg / L of suspended solids (SS) was decomposed,
Reduced to 18,000 mg / L per day, 10 per day
% Or more. From the fifth day, surplus sludge 11 was continuously supplied to the contact aeration tank 15A while being supplied every day. From the tenth day, the treatment reached a substantially constant state, and the supplied surplus sludge 11 was almost completely treated. Was decomposed into water. Contact aeration tank 1
Earthworms inhabited the contact material 18 of 5B. In other words, the presence of the earthworm, a high-grade microorganism, is evidence that the food chain is in operation.

【0021】なお上記説明では汚泥処理装置14に2個
の接触曝気槽15A、15Bを併設した場合について示
したが、1個または3個以上併設した構造でも良い。
In the above description, the case where two contact aeration tanks 15A and 15B are provided in the sludge treatment device 14 is shown, but a structure in which one or three or more contact aeration tanks are provided may be used.

【0022】[0022]

【発明の効果】以上説明した如く本発明に係る請求項1
記載の余剰汚泥の分解処理方法によれば、汚水を生物処
理して発生増殖した細菌類などの低級微生物を主体とす
る余剰汚泥を、接触材と水中に気泡を噴出する曝気手段
とを設けた接触曝気槽に導き、この接触曝気槽の接触材
に生息している原生動物、後生動物などの高級微生物に
より細菌類などの低級微生物を捕食して食物連鎖により
汚泥を分解し、この処理水を沈殿槽に導いて、上澄液を
排水すると共に、ここで沈殿した微生物などの残渣を前
記接触曝気槽に戻して繰り返し処理することにより、余
剰汚泥をほぼ完全に分解処理することができ、従来の余
剰汚泥の処分方法に比べてコストを大幅に削減すること
ができる。
As described above, claim 1 according to the present invention.
According to the method for decomposing excess sludge described, the excess sludge mainly composed of low-grade microorganisms such as bacteria generated and grown by biological treatment of wastewater is provided with a contact material and aeration means for blowing bubbles into water. It is led to the contact aeration tank, and higher-grade microorganisms such as protozoa and metazoans living in the contact material of this contact aeration tank prey on lower-grade microorganisms such as bacteria, decompose sludge by a food chain, and dispose of this treated water. By guiding the supernatant to a sedimentation tank and draining the supernatant, and returning the residue such as microorganisms precipitated here to the contact aeration tank and repeating the treatment, the excess sludge can be almost completely decomposed and treated. The cost can be significantly reduced as compared with the method for disposing of excess sludge.

【0023】更に本発明の請求項2記載の余剰汚泥の分
解処理方法は、紐状の芯材の表面に多数の突起を取付け
て、これを螺旋状に巻回した接触材を接触曝気槽に設け
ることにより、この表面が原生動物、後生動物などの高
級微生物の住みかとなって大量に生息させることがで
き、食物連鎖を有効に継続させて余剰汚泥の分解を速め
ることができる。
Further, in the method for decomposing excess sludge according to the second aspect of the present invention, a large number of projections are attached to the surface of a cord-like core material, and the contact material obtained by spirally winding the projections into a contact aeration tank. By providing this, the surface can be a habitat for high-grade microorganisms such as protozoa and metazoans and can be inhabited in large quantities, and the food chain can be effectively continued to accelerate the decomposition of excess sludge.

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

【図1】本発明の実施の一形態による余剰汚泥の分解装
置を示す説明図である。
FIG. 1 is an explanatory view showing an apparatus for decomposing excess sludge according to an embodiment of the present invention.

【図2】食物連鎖の状態を示す説明図である。FIG. 2 is an explanatory diagram showing a state of a food chain.

【符号の説明】[Explanation of symbols]

1 調整槽 2 汚水 3 曝気槽 4 ポンプ 5 散気管 6 沈殿槽 7 汚泥返送管 8 上澄液 9 処理水 10 消毒槽 11 余剰汚泥 12 消毒液供給装置 13 汚泥貯槽 14 汚泥処理装置 15A 接触曝気槽 16 沈殿槽 18 接触材 19 支持フレーム 20 残渣 21 残渣返送管 DESCRIPTION OF SYMBOLS 1 Adjustment tank 2 Sewage 3 Aeration tank 4 Pump 5 Aeration tube 6 Settling tank 7 Sludge return pipe 8 Supernatant 9 Treatment water 10 Disinfection tank 11 Excess sludge 12 Disinfectant supply device 13 Sludge storage tank 14 Sludge treatment device 15A Contact aeration tank 16 Settling tank 18 Contact material 19 Support frame 20 Residue 21 Residue return pipe

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 汚水を生物処理して発生増殖した細菌類
などの低級微生物を主体とする余剰汚泥を、接触材と水
中に気泡を噴出する曝気手段とを設けた接触曝気槽に導
き、この接触曝気槽の接触材に生息している原生動物、
後生動物などの高級微生物により余剰汚泥の低級微生物
を捕食する食物連鎖により前記汚泥を分解し、この処理
水を沈殿槽に導いて、上澄液を排水すると共に、ここで
沈殿した微生物などの残渣を前記接触曝気槽に戻して繰
り返し処理することを特徴とする余剰汚泥の分解処理方
法。
1. Excess sludge mainly composed of low-grade microorganisms such as bacteria generated and grown by biological treatment of sewage is led to a contact aeration tank provided with a contact material and aeration means for blowing air bubbles into water. Protozoa living in the contact material of the contact aeration tank,
The sludge is decomposed by a food chain that preyes on lower-grade microorganisms of surplus sludge by higher-grade microorganisms such as metazoans, the treated water is guided to a sedimentation tank, and the supernatant is drained, and the residue of microorganisms and the like precipitated here. Is returned to the contact aeration tank and is repeatedly treated.
【請求項2】 接触材が、表面に多数の突起を取付けた
紐状の芯材で形成され、、これを螺旋状に巻回して表面
に原生動物、後生動物などの高級微生物を付着繁殖させ
ることを特徴とする請求項1記載の余剰汚泥の分解処理
方法。
2. A contact material is formed of a cord-like core material having a large number of projections attached to a surface thereof, which is spirally wound to adhere and propagate high-grade microorganisms such as protozoa and metazoans on the surface. 2. The method for decomposing excess sludge according to claim 1, wherein:
JP2000344638A 2000-11-13 2000-11-13 Decomposition method for excess sludge Pending JP2002143895A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000344638A JP2002143895A (en) 2000-11-13 2000-11-13 Decomposition method for excess sludge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000344638A JP2002143895A (en) 2000-11-13 2000-11-13 Decomposition method for excess sludge

Publications (1)

Publication Number Publication Date
JP2002143895A true JP2002143895A (en) 2002-05-21

Family

ID=18818805

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000344638A Pending JP2002143895A (en) 2000-11-13 2000-11-13 Decomposition method for excess sludge

Country Status (1)

Country Link
JP (1) JP2002143895A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006061743A (en) * 2004-08-24 2006-03-09 Asahi Kasei Clean Chemical Co Ltd Method and apparatus for treating excess sludge
JPWO2006011241A1 (en) * 2004-07-30 2008-05-01 永和国土環境株式会社 Wastewater purification equipment
CN100460340C (en) * 2006-07-07 2009-02-11 汪群慧 Process for high performance treatment of organic sewage and reduction of excess sludge output
JP2011101879A (en) * 2009-10-14 2011-05-26 Nanshin Kankyo Kanri Center Kk System for treating sewage and/or sludge
CN102887587A (en) * 2012-11-05 2013-01-23 哈尔滨北方环保工程有限公司 Method for treating sewage by adopting multi-stage type bio-aeration pool
KR101547804B1 (en) * 2014-08-28 2015-08-27 재단법인차세대융합기술연구원 Organic waste treatment method using marine protozoa, and waste treatment apparatus using the same
CN109179861A (en) * 2018-08-28 2019-01-11 广州市市政工程设计研究总院有限公司 A kind of pulling flow type coupling sewage-treatment plant and technique
JP2019181325A (en) * 2018-04-03 2019-10-24 三菱ケミカルアクア・ソリューションズ株式会社 Reduction method of sludge, wastewater treatment facility, culture method and culture facility of aquatic crustacean, and conversion method of carbon source

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59225793A (en) * 1983-06-06 1984-12-18 Masanori Takahashi Sewage purifying apparatus
JPS61129098A (en) * 1984-11-27 1986-06-17 Nishihara Environ Sanit Res Corp Method for reducing quantity of sludge
JPS61192400A (en) * 1985-02-21 1986-08-26 Kubota Ltd Treatment of excessive sludge
JPH0471700A (en) * 1990-07-13 1992-03-06 Mitsubishi Kakoki Kaisha Ltd Sludge treating device
JPH0839092A (en) * 1994-07-29 1996-02-13 Tonen Corp Method and apparatus for treating excessive sludge
JPH0985271A (en) * 1995-09-26 1997-03-31 Sanbetsuku:Kk Sewage purifying method utilizing biological membrane, immersion filter bed used therein and its production
JPH10216799A (en) * 1997-02-10 1998-08-18 Hitachi Kiden Kogyo Ltd Treatment method for excess sludge
JPH10272483A (en) * 1997-03-28 1998-10-13 Joban Kaihatsu Kk Sewage cleaning device
JP2000229297A (en) * 1998-12-10 2000-08-22 Japan Organo Co Ltd Biological water treating device

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59225793A (en) * 1983-06-06 1984-12-18 Masanori Takahashi Sewage purifying apparatus
JPS61129098A (en) * 1984-11-27 1986-06-17 Nishihara Environ Sanit Res Corp Method for reducing quantity of sludge
JPS61192400A (en) * 1985-02-21 1986-08-26 Kubota Ltd Treatment of excessive sludge
JPH0471700A (en) * 1990-07-13 1992-03-06 Mitsubishi Kakoki Kaisha Ltd Sludge treating device
JPH0839092A (en) * 1994-07-29 1996-02-13 Tonen Corp Method and apparatus for treating excessive sludge
JPH0985271A (en) * 1995-09-26 1997-03-31 Sanbetsuku:Kk Sewage purifying method utilizing biological membrane, immersion filter bed used therein and its production
JPH10216799A (en) * 1997-02-10 1998-08-18 Hitachi Kiden Kogyo Ltd Treatment method for excess sludge
JPH10272483A (en) * 1997-03-28 1998-10-13 Joban Kaihatsu Kk Sewage cleaning device
JP2000229297A (en) * 1998-12-10 2000-08-22 Japan Organo Co Ltd Biological water treating device

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPWO2006011241A1 (en) * 2004-07-30 2008-05-01 永和国土環境株式会社 Wastewater purification equipment
US7972500B2 (en) 2004-07-30 2011-07-05 Eiwa Land Environment Co., Ltd Waste water purification apparatus
JP2006061743A (en) * 2004-08-24 2006-03-09 Asahi Kasei Clean Chemical Co Ltd Method and apparatus for treating excess sludge
CN100460340C (en) * 2006-07-07 2009-02-11 汪群慧 Process for high performance treatment of organic sewage and reduction of excess sludge output
JP2011101879A (en) * 2009-10-14 2011-05-26 Nanshin Kankyo Kanri Center Kk System for treating sewage and/or sludge
CN102887587A (en) * 2012-11-05 2013-01-23 哈尔滨北方环保工程有限公司 Method for treating sewage by adopting multi-stage type bio-aeration pool
KR101547804B1 (en) * 2014-08-28 2015-08-27 재단법인차세대융합기술연구원 Organic waste treatment method using marine protozoa, and waste treatment apparatus using the same
JP2019181325A (en) * 2018-04-03 2019-10-24 三菱ケミカルアクア・ソリューションズ株式会社 Reduction method of sludge, wastewater treatment facility, culture method and culture facility of aquatic crustacean, and conversion method of carbon source
CN109179861A (en) * 2018-08-28 2019-01-11 广州市市政工程设计研究总院有限公司 A kind of pulling flow type coupling sewage-treatment plant and technique
CN109179861B (en) * 2018-08-28 2024-01-23 广州市市政工程设计研究总院有限公司 Plug-flow type coupling sewage treatment device and process

Similar Documents

Publication Publication Date Title
JP3335500B2 (en) Wastewater treatment device and wastewater treatment method
JP4892917B2 (en) Biological treatment method and apparatus for organic wastewater
JP2006231295A (en) Wastewater treatment apparatus and wastewater treatment method
JP2007069091A (en) Organic wastewater treatment method
JP2006297374A (en) Method and apparatus for wastewater treatment
JP2003275796A (en) Method and apparatus for treating sludge by making good use of sludge pretreating unit and membrane separation type bioreactor
JP2002143895A (en) Decomposition method for excess sludge
JP4787814B2 (en) Organic wastewater purification method and apparatus
JP4644215B2 (en) Waste water treatment apparatus and waste water treatment method
JP2003053378A (en) Method and device for treating water by using separation membrane
JP2000218290A (en) Sewage treatment and sewage treating device
CN112830627B (en) Domestic sewage treatment method and integrated treatment equipment
JP2007229599A (en) Sewage treating apparatus
JPH05337479A (en) Aerobic treatment plant
JPH11128977A (en) Night soil treatment apparatus
JP2006088116A (en) Method and device for waste water treatment
JPH1099892A (en) Sewage treatment method and apparatus therefor
JP3271322B2 (en) Treatment of wastewater containing dimethyl sulfoxide
JP2003190987A (en) Method for cleaning lakes and marshes
JP2001096291A (en) Treatment process of sewage and sludge
JP3525458B2 (en) Aerobic treatment of organic wastewater
WO1995005346A1 (en) Process for purifying contaminated liquids utilizing ozone
JP2004141802A (en) Equipment and method for sludge treatment
JP2000233192A (en) Septic tank and its method
KR100297550B1 (en) Advanced Oxidation System of Wastewater Discharge Tank

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20071029

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20100212

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20100301

A02 Decision of refusal

Free format text: JAPANESE INTERMEDIATE CODE: A02

Effective date: 20100624