JPS6012193A - Fluidized bed type biological treatment apparatus - Google Patents

Fluidized bed type biological treatment apparatus

Info

Publication number
JPS6012193A
JPS6012193A JP58120279A JP12027983A JPS6012193A JP S6012193 A JPS6012193 A JP S6012193A JP 58120279 A JP58120279 A JP 58120279A JP 12027983 A JP12027983 A JP 12027983A JP S6012193 A JPS6012193 A JP S6012193A
Authority
JP
Japan
Prior art keywords
sponge
tank
carrier
substance
fluidized bed
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
JP58120279A
Other languages
Japanese (ja)
Inventor
Mikio Kitagawa
幹夫 北川
Kazuo Suzuki
和夫 鈴木
Makiko Miyahara
宮原 真紀子
Arimasa Miyaji
宮地 有正
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 JP58120279A priority Critical patent/JPS6012193A/en
Publication of JPS6012193A publication Critical patent/JPS6012193A/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

  • Biological Treatment Of Waste Water (AREA)

Abstract

PURPOSE:To efficiently remove an organism adhered to and penetrated into a sponge carrier, by intermittently taking out a part of the sponge carrier having the organism adhered thereto from a treating tank to bring the same into contact with an acidic liquid. CONSTITUTION:A porous sponge like substance 2 is introduced into the treating tank 1 of a fluidized bed type biological treatment apparatus as a microorganism carrier and fluidized by diffusing air from an air diffusing apparatus 3 provided to the bottom of the tank 1 to treat sewage supplied into and stayed in the treating tank 1 with the organism adhered to the sponge like substance 2. A discharge means 4 comprising a drum for discharging the sponge like substance 2 while rotated by a horizontal drive shaft is provided to the treating tank 1 while the discharged sponge substance 2 is taken out from a flooding port 1' and drained by a screen apparatus 5 to be fallen in an immersion tank 7 into which an acidic liquid is introduced. The sponge like substance 2 is stirred by rotating a rake 7' and successively discharged out of the tank 7 to be squeezed through a squeezing apparatus 8. The squeezed sponge like substance 2, from which the microorganism is removed, is neutralized in a neutralization tank 10 before returned to the treating tank 1 through a conduit 12.

Description

【発明の詳細な説明】 この発明は多孔質の海綿状物質なiしスポンジ状物質(
単にスポンジとも配子。)を微生物の担体として用い、
これを処理槽内で流動化させ、槽内に供給させる汚水中
のBOD成分や有害物質を担体が・保持する微生物で生
物的に酸化、還元等して除去する流動床式生物処理装置
に関する。
DETAILED DESCRIPTION OF THE INVENTION This invention provides a porous spongy material (i.e.
Just a sponge and also a mandrel. ) as a carrier for microorganisms,
The present invention relates to a fluidized bed biological treatment device that fluidizes wastewater in a treatment tank and removes BOD components and harmful substances in the wastewater supplied to the tank by biologically oxidizing, reducing, etc. using microorganisms held by carriers.

この様に微生物を用いた好気性或いは嫌気性の流動床式
処理装置は処理槽の単位容量当りの処理能力が高く、又
、バルキング問題を起さないばかりか沈澱池の省略も可
能であると言った利点がある反面、担体に付着した生物
は運転時間の経過に伴−増殖し、成る蓋取上になると担
体から剥離し、剥離した生物は微細化して処理水に混入
し、処理水の水質を悪化させる。従って、担体に付着し
た生物の量が成る程度に力ると、生*’t−担体から強
制的に剥離し、余剰汚泥として系外に排出することが必
要である。
In this way, aerobic or anaerobic fluidized bed treatment equipment using microorganisms has a high processing capacity per unit capacity of the treatment tank, and not only does it not cause bulking problems, but it is also possible to omit the settling tank. On the other hand, the organisms attached to the carrier multiply as the operating time passes, and when it reaches the top of the lid, it detaches from the carrier, and the detached organisms become microscopic and mix into the treated water, causing Deteriorate water quality. Therefore, if enough force is applied to the amount of organisms attached to the carrier, it is necessary to forcibly separate them from the raw *'t- carrier and discharge them as excess sludge to the outside of the system.

従来、担体にスポンジを使用している場合、生物の剥離
は槽内から担体を数出し、ロールなどで絞り、圧搾して
行っている。しかし、圧搾では担体表面に付着する汚泥
は剥離できても、内部の汚泥は殆ど剥離できず、絞って
は槽内に戻して循環使用すると、そのうちにスポンジの
内部は閉塞し、このような状態になるとBOD成分や有
害物質を処理するのはスポンジの表面の汚泥だけになる
ので処理槽内の汚泥濃度は低下し、とf’LK伴i装置
の処理能力も低下し且処理水の水質は悪化する。
Conventionally, when a sponge is used as a carrier, detachment of organisms is carried out by taking several carriers out of a tank, squeezing them with a roll, etc., and squeezing them. However, although the sludge adhering to the surface of the carrier can be removed by squeezing, the sludge inside can hardly be removed, and when the sponge is squeezed and returned to the tank for circulation, the inside of the sponge eventually becomes clogged, resulting in this condition. When this happens, only the sludge on the surface of the sponge is treated for BOD components and harmful substances, so the sludge concentration in the treatment tank decreases, and the treatment capacity of the f'LK-i device also decreases, and the quality of the treated water decreases. Getting worse.

本発明者等はスポンジからの生物の剥離音種々試みた結
果、生物が付着したスポンジ?I:酸性液に接触させる
と、生物は表面に膜状に付着したものも、スポンジ内部
に浸入したものも変質してスポンジから容易に離nるこ
とを見出し、不発8A′9tな丁に至ったのでるって、
生物が付着したスポンジ担体を一部宛処理槽から取出丁
排出手段と、嘔出したスポンジ担体を酸性液に接触させ
る酸処理装置と、酸処理したスポンジ担体を脱水する手
段と、脱水したスポンジ担体を処理槽に返送する返送手
段を処理槽に設けたこと管特徴とする。以下、図示の実
施例を参照して本発明を説明する。
The inventors of the present invention have tried various sounds of detachment of living things from sponges, and have found that sponges with living things attached to them? I: It was discovered that when brought into contact with an acidic liquid, living organisms, both those attached to the surface in a film form and those that have penetrated into the sponge, change in quality and easily separate from the sponge, leading to the unexploded 8A'9T. It's coming out,
A means for removing and discharging a portion of the sponge carriers with living organisms attached thereto from a treatment tank, an acid treatment device for contacting the vomited sponge carriers with an acidic liquid, a means for dehydrating the acid-treated sponge carriers, and a dehydrated sponge carrier. The processing tank is characterized by a pipe that is provided with return means for returning the water to the processing tank. The invention will now be described with reference to illustrated embodiments.

lは汚水が供給される処理槽で、槽内には比重−が/、
θ付近、多孔質の孔口の径が0.1””39位、体積が
t −1000a11位の球状、角状等任意の形態の圧
搾に耐えられるスポンジ担体コ・・・を無数に入n1槽
底部の全面から散気装置3で散気してスポンジ担体を槽
内で流動化し、槽内に供給さnる汚水を例えば、2グ時
間滞流させてその間に汚水中のBOD成分、有害物質を
スポンジ担体に付着した生物で処理し、良好な水質の処
理水として浴出口l′から排出する。
l is a treatment tank to which wastewater is supplied, and the specific gravity in the tank is -/,
In the vicinity of θ, the porous pore diameter is about 0.1''39, the volume is about t-1000a11, and an infinite number of sponge carriers that can withstand compression, such as spherical or angular shapes, are inserted. The sponge carrier is fluidized in the tank by aeration from the entire surface of the bottom of the tank with the aeration device 3, and the wastewater supplied into the tank is allowed to linger for, for example, 2 hours, during which time BOD components and harmful components in the wastewater are removed. The substances are treated with organisms attached to the sponge carrier and discharged from the bath outlet l' as treated water of good quality.

処理槽の液面近傍には垂直駆動軸で回転するレーキ (
破線で示す)或いは外周からピンが突出し、水平駆動軸
で回転するドラム(実線で示す)などの排出手段qヶ設
け、槽内のスポンジ担体を一部宛浴出口l′から外に取
出丁。排出手段ダは、処理槽の平面形状が円筒形のとき
はレーキが適し、回転ドラムは円筒形、方形、多角形の
どれにも適する。
Near the liquid level of the treatment tank, there is a rake (
A discharging means q such as a drum (indicated by a broken line) or a drum (indicated by a solid line) with a pin protruding from the outer periphery and rotated by a horizontal drive shaft is provided, and some of the sponge carriers in the bath are taken out from the bath outlet l'. As the discharge means, a rake is suitable when the planar shape of the processing tank is cylindrical, and the rotating drum is suitable for any of cylindrical, square, and polygonal shapes.

こうして隘出口/′からは処理水とスポンジ担体が排出
さnるので、こrL’t−スポンジ担体ヲ通さ方A籟装
置Sに供給して分離し、処理水は篩装置の下の水受は乙
に集めて放流し、スポンジ担体は酸性液を入f′L72
.浸漬槽7に落下させ、酸性液tスポンジ担体に含滲さ
せる。 ・ 酸性液はPHが3以下のものが好ましく、通常の塩酸、
硫酸の5tir程度の水溶液でもよいし、p’6 塩、
AL塩などそn自体が酸性を有するもの\水溶液でよ―
し、そnらの混合溶液でもより。そして、上記の様な金
属塩を含んで−ると後述の中和工程で金属塩は縦集剤と
して機能するので最も好ましい。と\での浸漬時間に約
13〜9分であるが、酸液がダO〜bo’cに加温して
あれば浸漬時間はS〜io分間に短縮するので好ましい
が、必ずしもその必狭はな埴。 ・この浸漬槽中で酸性
液をスポンジ担体に含滲させると、担体の表面の膜状の
生物は勿論、多孔、な内部に浸入した生物も酸で変質し
、スポンジから離n易い状態になる。 □ そこで浸漬槽の液面近傍でレーキ71y、回転し、担体
を攪拌すると同時に、担体を逐次槽外に排出し、圧搾装
置gに通してスポンジ担体を圧搾する。
In this way, the treated water and the sponge carrier are discharged from the outlet /', so the sponge carrier is passed through and separated by the sieving device S, and the treated water is sent to the water receiver under the sieving device. is collected and discharged into B, and the sponge carrier is filled with acidic liquid f'L72.
.. It is dropped into the dipping tank 7, and the acidic liquid is impregnated into the sponge carrier.・The acidic liquid preferably has a pH of 3 or less, such as ordinary hydrochloric acid,
An aqueous solution of about 5 tir of sulfuric acid may be used, or a p'6 salt,
Things that are acidic in themselves, such as AL salts, can be used in aqueous solutions.
However, a mixed solution of these is also better. It is most preferable to include the metal salts mentioned above, since the metal salts function as a collecting agent in the neutralization step described later. The immersion time is approximately 13 to 9 minutes at 1 and 2, but if the acid solution is heated to 20 to 20 minutes, the immersion time is preferably shortened to 5 to 10 minutes, but this is not necessarily necessary. Hanahani. - When the sponge carrier is impregnated with an acidic solution in this soaking tank, not only the membrane-like organisms on the surface of the carrier but also the organisms that have penetrated into the porous interior are denatured by the acid and become easily separated from the sponge. . □Therefore, the rake 71y rotates near the liquid surface of the dipping tank to stir the carrier, and at the same time, the carrier is successively discharged from the tank and passed through the squeezing device g to squeeze the sponge carrier.

圧搾装置gは上下二本の対をな丁ロールでもよいし、例
えば簡易なスクリュープレス、ぺ/l/)プレスその他
、スポンジ担体を圧搾し、内部の水分を搾シ出せるもの
であればよい。
The squeezing device g may be a pair of upper and lower rolls, or may be a simple screw press, a P/l/) press, or any other device that can squeeze the sponge carrier and squeeze out the moisture inside.

これによ夕変質した担体表面の生物は剥離すると共に、
担体内部の生物も搾り出さnる水と一緒に担体の外に出
、且つスポンジ担体は水會切らnる。 ・ 担体から搾シ出した水分は圧搾装置の下の水受け9に受
け、担体に中和装置10に導き、と\でアルカリ溶液に
て含滲している酸性液を中和する。
As a result, the organisms on the surface of the carrier that have changed in quality are peeled off, and
The living organisms inside the carrier also come out of the carrier together with the squeezed water, and the sponge carrier is also squeezed out with water. - The water squeezed out from the carrier is received in a water receiver 9 under the squeezing device, and introduced into the carrier into a neutralization device 10, where the acidic liquid contained in the carrier is neutralized with an alkaline solution.

中和装置10は、この実施例でに担体全通さない篩10
 aと、篩IOa上にアルカリ溶液を噴射するシャワー
管・106からなり、圧搾装置If通過しタスポンシ担
体は篩10α上全転動する際にアルカリ溶液の噴射を受
けて中和される様になっている。そして、中和さnfc
担体は&!/θαの傾斜した下端部から水41//中に
落下し、例えば水槽//の水面下に上から一端が突入し
、他端は処理槽l上に位置するエアリフト管7.2で処
理槽中に返送される。尚、ljはエアリフト管の水槽中
に上から突入した一端内部に空気を吹込む送気管を示す
。水槽//から処理m/にスポンジ担体を返送するのは
エアリフトによらず、水槽から掬い出して移送する様に
してもよい。
In this embodiment, the neutralization device 10 is a sieve 10 through which the carrier does not pass through.
a, and a shower pipe 106 that sprays an alkaline solution onto the sieve IOa, so that the Tasponsi carrier is neutralized by being sprayed with the alkaline solution as it passes through the squeezing device If and completely rolls over the sieve 10α. ing. and neutralized nfc
The carrier is &! It falls into the water 41 // from the inclined lower end of /θα, for example, one end plunges below the water surface of the water tank // from above, and the other end is connected to the treatment tank by the air lift pipe 7.2 located above the treatment tank l. It will be sent back inside. Note that lj indicates an air supply pipe that blows air into the interior of one end of the air lift pipe that protrudes into the water tank from above. The sponge carrier may be returned from the water tank // to the treatment m/ by scooping it out from the water tank and transferring it instead of using an air lift.

そして、浸漬槽7の酸性液中にはスポンジ担体から離n
yt生物が混入している。又、圧搾装置Sで担体から搾
9出した酸性液を受ける水受ワ中にも担体から離nfc
生物が混入している。このため浸漬槽中の酸性液と水受
はデ中の酸性液を抜出丁と共に、中和装置10が担体に
噴射したアルカリ溶液を受ける水受けio cからもア
ルカリ溶液を抜出し、この両方の液を混合槽/JVc入
れて中和することで凝集させ、これにより生物を汚泥と
して沈降させ、沈降した汚泥は混合槽の底から排出し、
上置液は処理槽lに汚水ケ供給する供給管/4Iにポン
プlS1返送管16で返送し、汚水に混ぜて処理槽に供
給する。
The sponge carrier is separated from the acidic liquid in the immersion tank 7.
yt organisms are mixed in. In addition, during the water receiving vessel that receives the acidic liquid squeezed out from the carrier by the squeezing device S, NFC is released from the carrier.
Contains living organisms. For this reason, the acidic liquid in the immersion tank and the water receiver are used to extract the acidic liquid in the tank, and the alkaline solution is also extracted from the water receiver IOC which receives the alkaline solution sprayed onto the carrier by the neutralization device 10. The liquid is put into the mixing tank/JVc and neutralized to cause flocculation, which causes the organisms to settle as sludge, and the settled sludge is discharged from the bottom of the mixing tank.
The overlying liquid is returned to the supply pipe /4I for supplying wastewater to the treatment tank 1 by the pump 1S1 return pipe 16, mixed with the wastewater, and supplied to the treatment tank.

中の酸性液がP’e塩、AJ 塩を含むときはとf’L
らが凝集剤として作用するので凝集効果がよい。
When the acidic liquid inside contains P'e salt and AJ salt, and f'L
Since these act as flocculants, the flocculating effect is good.

勿論、混合槽には必要に応じ高分子凝集剤1、FeCハ
・6H20などの凝集剤を加えてもよい。
Of course, a flocculant such as polymer flocculant 1 or FeC 6H20 may be added to the mixing tank if necessary.

以上、図示のフローシートに則シ、酸性液を含滲したス
ポンジ担体を圧搾装置ざで圧搾し、そnから中和装VI
Ltoでアルカリ溶液により中和するものとして説明し
たが、これに限定されず、敵性液七含滲したスポンジ担
体を中和装置でアルカリ溶液により中和し、その後に圧
搾装置で圧搾してもよい。この場合は中和したスポンジ
担体を圧搾Tるので圧搾装置の材質を耐酸性にしなくて
もよいと言う利点かめる。
As described above, according to the illustrated flow sheet, the sponge carrier impregnated with the acidic liquid is squeezed using a squeezing device, and then the neutralization device VI
Although it has been explained that the sponge carrier impregnated with the hostile liquid is neutralized with an alkaline solution in Lto, it is not limited to this, but the sponge carrier impregnated with the hostile liquid may be neutralized with an alkaline solution in a neutralization device, and then squeezed with a compression device. . In this case, since the neutralized sponge carrier is squeezed, there is an advantage that the material of the squeezing device does not need to be made acid-resistant.

又、酸性液を含滲した担体を圧搾する場合、搾り出し7
clli性液r水受はデから浸漬槽7に返送して循環使
用する様にすると酸性液の使用量の節減が図nると言う
別の見地からの利点がある。勿論、この場合は浸漬槽中
からだけ酸性液を混合槽/JK抜出し、中和装置からの
アルカリ溶液と混合して中和、凝菓丁ればよい。
In addition, when squeezing the carrier impregnated with acidic liquid, squeeze out 7
Another advantage is that the amount of acidic liquid used can be reduced by returning the liquid to the dipping tank 7 for circulation. Of course, in this case, it is only necessary to extract the acidic liquid from the dipping tank into the mixing tank/JK, mix it with the alkaline solution from the neutralizer, and neutralize it.

次に本発明の実験例を示す。Next, an experimental example of the present invention will be shown.

容量Jj1底面全面から散気を行う処理槽中にポリエチ
レン系のスポンジ担体(比重へ〇付近多孔の孔口の直径
約0.1〜コ、0txa、形状は約/−の正六面体)を
処理槽の容量の2s%にめたる体S<O・75L)入f
L、散気しながらグルコースを主体と丁;bBOD !
r00WVJ−の汚水を滞流時間コφ時間で流入させた
Capacity Jj1 A polyethylene sponge carrier (with a specific gravity of approximately 0.1 to 0, the diameter of the pore opening is approximately 0.1 to 0, and the shape is a regular hexahedron of approximately /-) is placed in a treatment tank that diffuses air from the entire bottom surface. 2s% of the capacity of f
L, mainly glucose while diffused; bBOD!
Sewage of r00WVJ- was allowed to flow in for a residence time of φ hours.

運転の開始から一週間の間は僅かな種汚泥を加えたが、
その後は汚泥を加えるのt止め、スポンジ担体の表面及
び内部に付着している生物のみで処理を行った。
A small amount of seed sludge was added during the first week of operation, but
After that, the addition of sludge was stopped and the treatment was carried out using only the organisms attached to the surface and inside of the sponge carrier.

その生物t−構属する微生qylJはカビが優占稚とな
って居シ、正常な活性汚泥(ズーグレアタイプ)と原生
動物も化1゛シていた。
The microorganism QylJ belonging to the organism T-component was dominated by mold, and normal activated sludge (Zooglaia type) and protozoa were also deformed.

スポンジ担体′を篩目の9HT! 4’、りlのダメッ
シュの篩で濾過した結果、p液の水質BB10”fA以
下、BOD s %/J以下でめった。
Sponge carrier' is sieved with 9HT! As a result of filtration through a Damesh sieve with a size of 4', the water quality of the p liquid was found to be below BB10''fA and below BOD s %/J.

生物の付着したスポンジ担体’(1−F$CJ、・6H
20が70%溶解している塩酸(5%)液中に浸した後
圧搾した結果付着した生物は容易に担体から剥離した。
Sponge carrier with attached organisms' (1-F$CJ, 6H
After immersing the carrier in hydrochloric acid (5%) in which 70% of 20 was dissolved, the attached organisms were easily peeled off from the carrier.

その塩酸液を中和すると、水酸化鉄の汚泥中に剥離した
汚泥が含in、良好な凝集を示した。
When the hydrochloric acid solution was neutralized, the exfoliated sludge was contained in the iron hydroxide sludge and showed good flocculation.

尚、汚水の水質や濃度、処理槽の負荷などによって余剰
な生物の発生量は異なり、又、時には余剰には発生し々
いこともめる。従って、実施に際してはスポンジ担体に
生じる生物の量を観淡し、そnに応じて処理槽から外に
取出し、酸液に浸漬するスポンジ担体の′Mt調整する
ことか好ましφ。
The amount of surplus organisms generated varies depending on the quality and concentration of sewage, the load on the treatment tank, etc., and in some cases, there may be no surplus. Therefore, in carrying out the process, it is preferable to consider the amount of organisms generated on the sponge carrier, and adjust the Mt of the sponge carrier taken out from the treatment tank and immersed in the acid solution accordingly.

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

図面は本発明の一実施例のフローシートで、図中、lは
処理槽、−はスポンジ担体、3は散気装置、7は峡処理
装置として例示した酸性液の入っている浸漬槽、10は
中和装置、12は返送手段として例示したエアリフト管
を示す。
The drawing is a flow sheet of an embodiment of the present invention, in which l is a treatment tank, - is a sponge carrier, 3 is an aeration device, 7 is an immersion tank containing an acidic liquid illustrated as a gorge treatment device, and 10 Reference numeral 12 indicates a neutralization device, and 12 indicates an air lift pipe as an example of a return means.

Claims (1)

【特許請求の範囲】 処理槽内に微生物担体として多孔質の海綿状物質を入n
て槽底からの散気で流動させ、処理槽中に供給さnて滞
流する汚水中を担体に付着した生物で処理する流動床式
生物処理装置において、 処理槽には槽内から担体を排出する排出手段を設けると
共に、排出さA*担体t−酸性溶液に接触させる酸処理
装置と、酸処理装置で処理した担体を脱水する脱水手段
と、脱水した担体・を処理槽に返送する返送手段を処理
槽に付属させたことを特徴とする流動床式生物処理装置
[Claims] A porous spongy material is placed in the treatment tank as a microbial carrier.
In a fluidized bed biological treatment equipment, wastewater is fluidized by air diffused from the bottom of the tank, and the sewage that stagnates in the treatment tank is treated with organisms attached to the carrier. In addition to providing a discharge means for discharging, an acid treatment device for bringing the discharged A* carrier into contact with an acidic solution, a dehydration means for dehydrating the carrier treated with the acid treatment device, and a return transport for returning the dehydrated carrier to the treatment tank. A fluidized bed biological treatment device characterized in that a means is attached to a treatment tank.
JP58120279A 1983-07-04 1983-07-04 Fluidized bed type biological treatment apparatus Pending JPS6012193A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58120279A JPS6012193A (en) 1983-07-04 1983-07-04 Fluidized bed type biological treatment apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58120279A JPS6012193A (en) 1983-07-04 1983-07-04 Fluidized bed type biological treatment apparatus

Publications (1)

Publication Number Publication Date
JPS6012193A true JPS6012193A (en) 1985-01-22

Family

ID=14782302

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58120279A Pending JPS6012193A (en) 1983-07-04 1983-07-04 Fluidized bed type biological treatment apparatus

Country Status (1)

Country Link
JP (1) JPS6012193A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2422147A (en) * 2005-01-15 2006-07-19 Geoffrey Kevin Ellison Method of treating effluent comprising the provision of a plurality of bacteria supporting elements
US11685675B2 (en) 2013-10-22 2023-06-27 Nuvoda Llc Reduction of substances in contaminated fluids using a naturally occurring biological growth media

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2422147A (en) * 2005-01-15 2006-07-19 Geoffrey Kevin Ellison Method of treating effluent comprising the provision of a plurality of bacteria supporting elements
US11685675B2 (en) 2013-10-22 2023-06-27 Nuvoda Llc Reduction of substances in contaminated fluids using a naturally occurring biological growth media

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