JPS60139394A - Biological treatment of waste water by employing fluidized bed - Google Patents

Biological treatment of waste water by employing fluidized bed

Info

Publication number
JPS60139394A
JPS60139394A JP58248809A JP24880983A JPS60139394A JP S60139394 A JPS60139394 A JP S60139394A JP 58248809 A JP58248809 A JP 58248809A JP 24880983 A JP24880983 A JP 24880983A JP S60139394 A JPS60139394 A JP S60139394A
Authority
JP
Japan
Prior art keywords
particles
fluidized bed
liquid
wastewater
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.)
Granted
Application number
JP58248809A
Other languages
Japanese (ja)
Other versions
JPH0144395B2 (en
Inventor
Susumu Matsui
進 松井
Kiyoshi Takada
清 高田
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.)
Osaka Gas Co Ltd
Original Assignee
Osaka Gas Co 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 Osaka Gas Co Ltd filed Critical Osaka Gas Co Ltd
Priority to JP58248809A priority Critical patent/JPS60139394A/en
Publication of JPS60139394A publication Critical patent/JPS60139394A/en
Publication of JPH0144395B2 publication Critical patent/JPH0144395B2/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 eliminate the damage of particles and the abrasion of a pump, by allowing a part of waste water containing microorganism adhered grown particles to pass through the liquid cyclone on the recirculation line provided to the outside of a fluidized bed while taking out the same through said line. CONSTITUTION:Microorganism adhered particles grown by the propagation of microorganisms are floated above the interface 7 of a fluidized bed 2 and a solid-liquid separation zone 3. These particles are taken out of a tank along with a part of recirculated waste water through a recirculation line 5 and allowed to forcibly pass through the liquid cyclone 8 provided on the way of the recirculation line 5 by the sucking action of a recirculation pump 9 to peel off adhered microorganisms from grown particles mainly in the liquid cyclone 8. The particles are fallen into a precipitation type hermetically closed separation tank 11 and further fallen into a hermitically closed particle storage tank 14 through a falling pipe 13 under their own wt. and accumulated therein.

Description

【発明の詳細な説明】 本発明は、微生物付着粒子により構成される流動層生物
膜法の改良に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improvement in a fluidized bed biofilm process comprised of microbially attached particles.

微生物を付着させた粒子により流動層を形成させ、流動
層内で廃水を処理し、流動層上方で微生物付着粒子と処
理済水との分離を行なう流動層生物膜法は公知であり、
このような流動層生物脱法においては、粒子に付着した
微生物が生長し肥大化し過ぎると粒子が処理槽から流出
するので、過剰付着の微生物を粒子から剥離しなければ
ならない。この際、従来法には、以下の如き欠点がある
A fluidized bed biofilm method is known, in which a fluidized bed is formed by particles to which microorganisms are attached, wastewater is treated within the fluidized bed, and the microorganism-adhered particles and treated water are separated above the fluidized bed.
In such a fluidized bed biological removal method, if the microorganisms attached to the particles grow and become too large, the particles will flow out of the treatment tank, so the excessively attached microorganisms must be peeled off from the particles. In this case, the conventional method has the following drawbacks.

(i) 粒子をポンプ内に吸引通過させる場合には、粒
子が破損され、またポンプも摩耗される。
(i) When particles are sucked through the pump, they are damaged and the pump is also worn.

(11) 処理槽上部に撹拌機を取付け、機械的に付着
微生物を剥離する場合には、やはり粒子の破損及び撹拌
機の摩耗を生ずる。
(11) When attaching a stirrer to the upper part of the treatment tank and mechanically removing attached microorganisms, particle breakage and abrasion of the stirrer also occur.

本発明はこのような従来の問題を一掃することを目的と
してなされたもので、即ち本発明は、微生物を付着させ
た粒子により処理槽内に流動層を形成させ、流動層内で
廃水を処理し、流動層上方で微生物付着肥大粒子と処理
済水との分離を行なう廃水の流動層生物処理方法におい
て、処理槽の上部から微生物付着肥大粒子を含む廃水の
一部を層外付設の循環ラインを通じて取り出しながら、
該ライン上に設置した液体サイクロン内を通過させるこ
とにより、上記粒子より付着微生物を剥離させ、液体サ
イクロンの上部出口よりの剥離微生物混合液は循環ライ
ンを通じて処理槽下部に戻し、一方正部出口よりの粒子
混合液は、密閉沈降式固液分離槽において固液分離し、
分離液は液体サイクロン上部出口よりの液に合流させ、
一方沈降粒子は、密閉型粒子溜槽に堆積させ、溜槽内に
所定量の粒子が堆積した後は、循環ポンプを通過した後
の循環液の一部を、溜槽内を通過させ、これに堆積粒子
を随伴しつつ処理槽下部に返送することを特徴とする廃
水の流動層処理法に係る。
The present invention was made with the aim of eliminating such conventional problems. Specifically, the present invention forms a fluidized bed in a treatment tank using particles to which microorganisms are attached, and treats wastewater within the fluidized bed. In a fluidized bed biological treatment method for wastewater that separates enlarged microorganism-adhered particles from treated water above the fluidized bed, a portion of the wastewater containing enlarged microorganism-adhered particles is passed from the top of the treatment tank through a circulation line installed outside the layer. While taking it out through
The adhering microorganisms are separated from the particles by passing through a liquid cyclone installed on the line, and the separated microorganism mixture from the upper outlet of the liquid cyclone is returned to the lower part of the processing tank through the circulation line, while the liquid from the main outlet is The particle mixture is subjected to solid-liquid separation in a closed settling type solid-liquid separation tank,
The separated liquid is combined with the liquid from the upper outlet of the hydrocyclone,
On the other hand, the sedimented particles are deposited in a closed particle storage tank, and after a predetermined amount of particles have been deposited in the storage tank, a part of the circulating fluid that has passed through the circulation pump is passed through the tank, and the sedimented particles are deposited in this tank. The present invention relates to a fluidized bed treatment method for wastewater, which is characterized in that wastewater is returned to the lower part of a treatment tank while being accompanied by wastewater.

以下図面に示すフローダイヤグラムを参照しつつ本発明
の詳細な説明する。
The present invention will be described in detail below with reference to flow diagrams shown in the drawings.

第1図において、廃水処理槽(1)には流動層ゾーン(
2)及び固液分離ゾーン(3)が形成されている。流動
層は、予め微生物を砂、活性炭、コークス、アンスラサ
イト、プラスチック、ガラス、シリカゲル、シリカ−ア
ルミナ等の粒子に付着させ、馴致させたものを浮遊させ
ることにより、形成されている。微生物付着用粒子の粒
径は、その材質により種々異なるが、コスト、入手の容
易さ、微生物付着の容易さ等の点で最適である砂の場合
、通常0.1〜3a+m程度である。廃水処理槽(1)
内に保持さるべき粒子の量は、粒子に対する微生物付着
量等により異なるが、通常槽内汚泥濃度(MLvSS)
が5000〜4000IIlΩ/Q程度となる様にする
のが良い。廃水は供給ライン(4)から循環ライン(5
)を経て処理槽(1)内に供給され、処理槽(1)内に
おいて、流動層ゾーン(2)を上昇する間に流動層を形
成している微生物付着粒子にそのBOD成分及び/又は
窒素成分を与え、更にその一部は、固液分離ゾーン(3
)内を上昇してライン(6)から処理済水として系外に
取り出される。微生物の生成により肥大した微生物付着
粒子は、流動層(2)と固液分離ゾーン(3)との界面
(7)の上方に浮上するので、これを循環される廃水の
一部と一緒に循環ライン(5)を通じて構外に取り出し
、循環ライン(5)の途中に設置された液体サイクロン
(8)内を、該サイクロン(8)より後方設置の循環ポ
ンプ(9)の吸引作用により強制的に通過させ、主に液
体サイクロン(8)内で肥体粒子より付着微生物を剥離
させる。液体サイクロン(8)の上部へは、剥離微生物
を含有する液が上昇するので、これを上部出口から循環
ライン(5)を通じて処理槽(1)の下部に戻し、一方
液体サイクロン(8)の下部へは粒子が降下するので、
これを一部の液と一緒に下部出口より降下管(1o)を
経て、沈降式の密閉分離槽(11)内に自重降下させる
。分離槽(11)においては、液は構内を上昇するので
、これをライン(12)を通じて、サイクロン(8)よ
り後方の循環ライン(5)に合流させ、一方粒子は槽内
を降下するので、これを降下管(13)を通じて、密閉
型の粒子溜槽(14)内に自動降下し堆積させる。溜槽
(14)内に所定量の粒子が堆積した後は、降下管(1
3)に備えたバルブ(13a)を閉じ、粒子の自動降下
を停止する一方、循環ポンプ(9)を通過した後の循環
液の一部を、分岐ライン(15)を通じて、溜槽(14
)内を上部から下部へ通過させ、堆積粒子をこの循環液
に随伴させて、降下管(16)より循環ライン(5)を
経て処理槽(1)の下部に返送させる。堆積粒子の返送
を終えた後は、分岐ライン(15)のバルブ(15a)
及び降下管(16)のバルブ(16a)を閉じ粒子返送
を停止する一方、降下管(13)のバルブ(13a)を
開き、粒子の堆積を再開させる。このような粒子の返送
操作を繰返し行なうことにより、粒子を再生しつつ循環
使用できる。尚粒子返送操作におけるバルブ(13a)
、(15a)及び(16a)の開閉切替え操作は、電磁
弁とタイマーの組合せにより周期的に行なうことができ
る。
In Figure 1, the wastewater treatment tank (1) has a fluidized bed zone (
2) and a solid-liquid separation zone (3) are formed. The fluidized bed is formed by adhering microorganisms to particles of sand, activated carbon, coke, anthracite, plastic, glass, silica gel, silica-alumina, etc. in advance and suspending them. The particle size of the particles for microbial adhesion varies depending on the material, but in the case of sand, which is optimal in terms of cost, ease of availability, ease of microbial adhesion, etc., it is usually about 0.1 to 3 a+m. Wastewater treatment tank (1)
The amount of particles that should be retained in the tank varies depending on the amount of microorganisms attached to the particles, but usually the sludge concentration in the tank (MLvSS)
It is preferable that the resistance is about 5000 to 4000 IIlΩ/Q. The wastewater flows from the supply line (4) to the circulation line (5).
), and in the treatment tank (1), the BOD components and/or nitrogen are added to the microorganism-adhered particles forming the fluidized bed while rising through the fluidized bed zone (2). components, and a part of them is also transferred to the solid-liquid separation zone (3
) and is taken out of the system as treated water through line (6). The microorganism-attached particles enlarged due to the production of microorganisms float above the interface (7) between the fluidized bed (2) and the solid-liquid separation zone (3), so they are circulated together with part of the recycled wastewater. It is taken out of the premises through the line (5) and forced to pass through the liquid cyclone (8) installed in the middle of the circulation line (5) by the suction action of the circulation pump (9) installed behind the cyclone (8). The attached microorganisms are separated from the manure particles mainly in the liquid cyclone (8). The liquid containing detached microorganisms rises to the upper part of the liquid cyclone (8), so it is returned to the lower part of the treatment tank (1) from the upper outlet through the circulation line (5), while the liquid containing the detached microorganisms rises to the upper part of the liquid cyclone (8). As particles fall to
This, along with some of the liquid, is lowered under its own weight from the lower outlet through the downcomer pipe (1o) into the sedimentation type sealed separation tank (11). In the separation tank (11), as the liquid rises within the premises, it is made to join the circulation line (5) behind the cyclone (8) through the line (12), while the particles descend within the tank. The particles are automatically lowered and deposited in a closed particle storage tank (14) through a downcomer pipe (13). After a predetermined amount of particles have accumulated in the reservoir tank (14), the downcomer pipe (14)
3) is closed to stop the automatic descent of particles, while a part of the circulating liquid after passing through the circulation pump (9) is sent to the reservoir tank (14) through the branch line (15).
) from the upper part to the lower part, and the deposited particles are entrained in this circulating liquid and returned to the lower part of the processing tank (1) via the downcomer pipe (16) and the circulation line (5). After returning the accumulated particles, close the valve (15a) of the branch line (15).
Then, the valve (16a) of the downcomer pipe (16) is closed to stop particle return, while the valve (13a) of the downcomer pipe (13) is opened to restart particle deposition. By repeatedly performing such a particle return operation, the particles can be regenerated and recycled. Valve (13a) in particle return operation
, (15a) and (16a) can be periodically performed by a combination of a solenoid valve and a timer.

また溜槽(14)内を流通される循環液の液量増加を目
的として、分岐ライン(15)と降下管(16)の間の
循環ライン(5)の途中に、絞り部(図示せず)を形成
することができる。
In addition, for the purpose of increasing the amount of circulating fluid flowing through the reservoir tank (14), a constriction part (not shown) is installed in the middle of the circulation line (5) between the branch line (15) and the downcomer pipe (16). can be formed.

本発明処理法によれば、液体サイクロン(8)にて再生
された粒子を、循環液の一部をうまく利用して、循環ポ
ンプ(9)を何等経由させることなしに、処理4!(1
)の下部に返送でき、粒子破損やポンプ磨損などの問題
を一掃できる。
According to the treatment method of the present invention, the particles regenerated in the hydrocyclone (8) can be processed 4! without passing through the circulation pump (9) by making good use of a part of the circulating liquid. (1
), which eliminates problems such as particle damage and pump wear.

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

第1図は本発明の一実施態様を示すフローダイヤグラム
、第2図は第1図の要部拡大図である。 図に於いて、(1)は処理槽、(2)は流動層ゾーン、
(3)は固液分離ゾーン、(4)は廃水の供給ライン、
(5)は循環ライン、(6)はライン、(7)は界面、
(8)は液体サイクロン、(9)は循環ポンプ、(10
)は降下管、(11)は固液分離槽、(12)はライン
、(13)は降下管、(14)は溜槽、(15)は分岐
ライン、(16)は降下管である。 (以 上) 第1図 第2図
FIG. 1 is a flow diagram showing one embodiment of the present invention, and FIG. 2 is an enlarged view of the main part of FIG. In the figure, (1) is a treatment tank, (2) is a fluidized bed zone,
(3) is a solid-liquid separation zone, (4) is a wastewater supply line,
(5) is a circulation line, (6) is a line, (7) is an interface,
(8) is a hydrocyclone, (9) is a circulation pump, (10
) is a downcomer, (11) is a solid-liquid separation tank, (12) is a line, (13) is a downcomer, (14) is a reservoir, (15) is a branch line, and (16) is a downcomer. (That's all) Figure 1 Figure 2

Claims (1)

【特許請求の範囲】[Claims] ■ 微生物を付着させた粒子により処理槽内に流動層を
形成させ、流動層内で廃水を処理し、流動層上方で微生
物付着肥大粒子と処理済水との分離を行なう廃水の流動
滞生物処理方法において、処理槽の上部から微生物付着
肥大粒子を含む廃水の一部を層外付設の循環ラインを通
じて取り出しながら、該ライン上に設置した液体サイク
ロン内を通過させることにより、上記粒子より付着微生
物を剥離させ、液体サイクロンの上部出口よりの剥離微
生物混合液は循環ラインを通じて処理槽下部に戻し、一
方正部出口よりの粒子混合液は、密閉沈降式固液分離槽
において固液分離し、分離液は液体サイクロン上部出口
よりの液に合流させ、一方沈降粒子は、密閉型粒子溜槽
に堆積させ、溜槽内に所定量の粒子が堆積した後は、循
環ポンプを通過した後の循環液の一部を、溜槽内を通過
させ、これに堆積粒子を随伴しつつ処理槽下部に返送す
ることを特徴とする廃水の流動層処理法。
■ Fluidized biological treatment of wastewater in which a fluidized bed is formed in the treatment tank using particles with microorganisms attached, the wastewater is treated in the fluidized bed, and the treated water is separated from the enlarged microorganism-adhered particles above the fluidized bed. In this method, a part of the wastewater containing enlarged microorganism-adhering particles is removed from the upper part of the treatment tank through a circulation line installed outside the layer, and the wastewater is passed through a liquid cyclone installed on the line, thereby removing the adhering microorganisms from the particles. The separated microorganism mixture from the upper outlet of the hydrocyclone is returned to the lower part of the treatment tank through the circulation line, while the particle mixture from the main outlet is separated into solid and liquid in a closed sedimentation type solid-liquid separation tank, and the separated microorganisms are separated into separated liquid. The particles are mixed with the liquid from the upper outlet of the hydrocyclone, while the sedimented particles are deposited in a closed particle reservoir, and after a predetermined amount of particles have accumulated in the reservoir, part of the circulating fluid after passing through the circulation pump is A fluidized bed treatment method for wastewater, characterized in that the wastewater is passed through a storage tank and returned to the lower part of the treatment tank while being accompanied by deposited particles.
JP58248809A 1983-12-27 1983-12-27 Biological treatment of waste water by employing fluidized bed Granted JPS60139394A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58248809A JPS60139394A (en) 1983-12-27 1983-12-27 Biological treatment of waste water by employing fluidized bed

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58248809A JPS60139394A (en) 1983-12-27 1983-12-27 Biological treatment of waste water by employing fluidized bed

Publications (2)

Publication Number Publication Date
JPS60139394A true JPS60139394A (en) 1985-07-24
JPH0144395B2 JPH0144395B2 (en) 1989-09-27

Family

ID=17183726

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58248809A Granted JPS60139394A (en) 1983-12-27 1983-12-27 Biological treatment of waste water by employing fluidized bed

Country Status (1)

Country Link
JP (1) JPS60139394A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6279896A (en) * 1985-10-03 1987-04-13 Kurita Water Ind Ltd Sewage treatment device
JP2003080284A (en) * 2001-09-14 2003-03-18 Sumitomo Heavy Ind Ltd Wastewater treatment equipment
WO2003045569A1 (en) 2001-11-27 2003-06-05 Takahashi Co., Ltd. Filter device
JP2015205278A (en) * 2011-03-01 2015-11-19 株式会社東芝 Solid-liquid separation apparatus

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6279896A (en) * 1985-10-03 1987-04-13 Kurita Water Ind Ltd Sewage treatment device
JP2003080284A (en) * 2001-09-14 2003-03-18 Sumitomo Heavy Ind Ltd Wastewater treatment equipment
WO2003045569A1 (en) 2001-11-27 2003-06-05 Takahashi Co., Ltd. Filter device
KR100645345B1 (en) * 2001-11-27 2006-11-14 가부시키가이샤 다카하시 Filter device
US7909990B2 (en) 2001-11-27 2011-03-22 Takahashi Co., Ltd. Filter device
JP2015205278A (en) * 2011-03-01 2015-11-19 株式会社東芝 Solid-liquid separation apparatus

Also Published As

Publication number Publication date
JPH0144395B2 (en) 1989-09-27

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