JPH03213128A - Wastewater treatment equipment - Google Patents
Wastewater treatment equipmentInfo
- Publication number
- JPH03213128A JPH03213128A JP2008819A JP881990A JPH03213128A JP H03213128 A JPH03213128 A JP H03213128A JP 2008819 A JP2008819 A JP 2008819A JP 881990 A JP881990 A JP 881990A JP H03213128 A JPH03213128 A JP H03213128A
- Authority
- JP
- Japan
- Prior art keywords
- membrane
- sludge
- membrane surface
- tank
- ultrasonic
- 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
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D65/00—Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
- B01D65/02—Membrane cleaning or sterilisation ; Membrane regeneration
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2321/00—Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
- B01D2321/20—By influencing the flow
- B01D2321/2033—By influencing the flow dynamically
- B01D2321/2058—By influencing the flow dynamically by vibration of the membrane, e.g. with an actuator
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2321/00—Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
- B01D2321/20—By influencing the flow
- B01D2321/2066—Pulsated flow
- B01D2321/2075—Ultrasonic treatment
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Activated Sludge Processes (AREA)
- Physical Water Treatments (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
産業上の利用分野
本発明は浄化槽汚泥、生活系排水汚泥、し尿等の有機性
廃水の廃水処理設備に関する。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to wastewater treatment equipment for organic wastewater such as septic tank sludge, domestic wastewater sludge, and human waste.
従来の技術
従来、浄化槽汚泥、生活系排水汚泥、し尿等の有機性廃
水を処理する設備として膜分離方式がある。この方式は
硝化槽などの処理槽に膜分離装置を浸漬して配置し、混
合液などの懸濁液を膜分離装置で固液分離して透過液を
処理水として抽出するものである。そして、処理槽内に
空気を曝気することにより、廃水中に含まれるを機物の
酸化に必要な酸素を供給するとともに、空気のエアリフ
ト作用によって生じる上昇撹拌流により膜分離装置の膜
面の洗浄を行っていた。2. Description of the Related Art Conventionally, membrane separation systems have been used as equipment for treating organic wastewater such as septic tank sludge, domestic wastewater sludge, and human waste. In this method, a membrane separator is immersed in a treatment tank such as a nitrification tank, and a suspension such as a mixed liquid is separated into solid and liquid by the membrane separator, and the permeate is extracted as treated water. By aerating air into the treatment tank, the oxygen necessary for oxidizing the wastewater contained in the wastewater is supplied, and the membrane surface of the membrane separator is cleaned by the upward stirring flow generated by the air lift effect. was going on.
発明が解決しようとする課題
しかし、上記した構成においては、膜面に対する上昇撹
拌流の洗浄力を高めるために曝気強度を強くすると、微
生物が生息する汚泥フロックが破壊され、生物学的処理
能力が低下するので、膜面に付着したゲル槽などを上昇
攪拌流だけでは十分に洗浄除去することができず、定期
的に膜分離装置を処理槽外に取り出して洗浄する必要が
あり、稼働効率を高める上で問題点とされていた。Problems to be Solved by the Invention However, in the above configuration, if the aeration intensity is increased in order to increase the cleaning power of the upward agitation flow on the membrane surface, the sludge flocs in which microorganisms live will be destroyed, and the biological treatment capacity will be reduced. As a result, it is not possible to sufficiently wash and remove gels and other substances that adhere to the membrane surface with the upward agitation flow alone, and it is necessary to periodically take the membrane separation device out of the processing tank for cleaning, which reduces operating efficiency. This was seen as a problem in raising the level.
本発明は上記課題を解決するもので、汚泥フロックを破
壊することなく確実に膜面の洗浄を行うことができる廃
水処理設備を提供することを目的とする。The present invention solves the above problems, and aims to provide wastewater treatment equipment that can reliably clean the membrane surface without destroying sludge flocs.
課題を解決するための手段
上記課題を解決するために本発明は、生物学的処理槽に
膜分離装置を浸漬して配置した廃水処理設備において、
膜分離装置の膜面に超音波振動を与える超音波洗浄装置
を設けた構成としたものである。Means for Solving the Problems In order to solve the above problems, the present invention provides a wastewater treatment facility in which a membrane separation device is immersed in a biological treatment tank.
The structure includes an ultrasonic cleaning device that applies ultrasonic vibration to the membrane surface of the membrane separator.
作用
上記した構成により、生物学的処理槽に貯留された原水
中に含まれる有機物は槽内に滞留する汚泥フロックの活
性汚泥生物に消化される。また、原水は膜分離装置で固
液分離され、膜分離装置の濾過膜を透過した透過水が処
理水として抽出されるとともに、濾過膜に捕捉された固
形分が槽内に残留する。そして、超音波洗浄装置によっ
て膜分離装置の濾過膜の膜面に超音波振動を与え、膜面
の振動および振動する膜面と原水の干渉によって膜面に
付着したゲル層などの付着物を洗浄除去する。したがっ
て、膜面の洗浄に際して汚泥フロックに何ら影響を与え
ず、汚泥フロックの破壊などによる生物学的処理能力の
低下を来すことなく確実に膜面の洗浄が行なわれる。Operation With the above-described configuration, organic matter contained in the raw water stored in the biological treatment tank is digested by activated sludge organisms of sludge flocs staying in the tank. Further, the raw water is subjected to solid-liquid separation in a membrane separator, and the permeated water that has passed through the filtration membrane of the membrane separator is extracted as treated water, and the solid content captured by the filtration membrane remains in the tank. Then, ultrasonic vibration is applied to the membrane surface of the filtration membrane of the membrane separation device using an ultrasonic cleaning device to clean the gel layer and other deposits that have adhered to the membrane surface due to the vibration of the membrane surface and the interference between the vibrating membrane surface and raw water. Remove. Therefore, when cleaning the membrane surface, the membrane surface is reliably cleaned without affecting the sludge flocs and without deteriorating the biological treatment capacity due to destruction of the sludge flocs.
実施例
以下本発明の一実施例を図面に基づいて説明する。第1
図において、脱窒紫檀1は密閉されて嫌気性環境に形成
されており、脱窒紫檀1には原水2の供給管3が夾雑物
・し膜分離装置4を介して連通している。また、脱窒紫
檀1には混合液5の水面上に浮上分離する浮遊物を排出
する排出装置6が設けられている。そして、脱窒紫檀1
の適当水深下に位置して送水管7が開口しており、送水
管7は硝化槽8に連通している。この硝化槽8は内部に
膜分離装置9が浸漬して配置されており、膜分離装置9
の負圧側は吸引ポンプIOに連通している。この膜分離
装置9の分離膜IIはUFもしくはMFで形成されてい
る。EXAMPLE An example of the present invention will be described below based on the drawings. 1st
In the figure, a denitrifying rosewood 1 is sealed and formed in an anaerobic environment, and a supply pipe 3 for raw water 2 is communicated with the denitrifying rosewood 1 via a contaminant/diaphragm separation device 4. Further, the denitrifying rosewood 1 is provided with a discharge device 6 for discharging floating matter floating and separating on the water surface of the mixed liquid 5. And denitrifying rosewood 1
A water pipe 7 is opened at a suitable depth below the water, and the water pipe 7 communicates with a nitrification tank 8. This nitrification tank 8 has a membrane separator 9 immersed therein.
The negative pressure side of is connected to the suction pump IO. The separation membrane II of this membrane separation device 9 is formed of UF or MF.
そして、膜分離装置9には超音波端子部I2が取り付け
られており、超音波端子部12は超音波発振器I3に接
続されている。また、硝化槽8の底部には散気管14が
配置されており、散気管14はブロワ−15の吐出側に
連通している。そして、硝化槽8には余剰汚泥16を排
出するための汚泥吸引ポンプ!7が余剰汚泥排出管I8
を介して接続されるとともに、硝化循環液19を循環さ
せるための循環ポンプ20が循環管21を介して接続さ
れており、循環管21の先端は脱窒紫檀1に連通してい
る。An ultrasonic terminal section I2 is attached to the membrane separation device 9, and the ultrasonic terminal section 12 is connected to an ultrasonic oscillator I3. Further, an aeration pipe 14 is arranged at the bottom of the nitrification tank 8, and the aeration pipe 14 communicates with the discharge side of the blower 15. The nitrification tank 8 is equipped with a sludge suction pump for discharging excess sludge 16! 7 is excess sludge discharge pipe I8
A circulation pump 20 for circulating the nitrification circulating liquid 19 is connected via a circulation pipe 21 , and the tip of the circulation pipe 21 communicates with the denitrification rosewood 1 .
以下、上記構成における作用について説明する。Hereinafter, the effects of the above configuration will be explained.
供給管3から脱窒紫檀1に流入した原水2は脱窒紫檀1
の内部に滞留する活性汚泥と混合されて混合液5となり
、原水2とともに供給された有機物が活性汚泥に培養さ
れている脱窒素菌の硝酸呼吸および亜硝酸呼吸により酸
化分解される。The raw water 2 flowing into the denitrifying rosewood 1 from the supply pipe 3 is the denitrifying rosewood 1.
is mixed with the activated sludge that stays inside to form a mixed solution 5, and the organic matter supplied together with the raw water 2 is oxidized and decomposed by nitrate respiration and nitrite respiration of denitrifying bacteria cultured in the activated sludge.
そして、混合液5は送水管7を通して硝化槽8に送られ
る。硝化槽8においては、ブロワ−15から供給される
空気が散気管lはり混合液5に散気され、混合液5に含
まれる窒素化合物が活性汚泥に培養されている硝化菌に
より硝酸化合物、亜硝酸化合物まで酸化される。さらに
、硝化槽8の硝酸化合物、亜硝酸化合物は硝化循環液1
9として活性汚泥とともに循環ポンプ20により循環管
21を通して脱窒紫檀1に戻され、脱窒素菌の硝酸呼吸
および亜硝酸呼吸によって窒素ガス、酸化窒素ガスに還
元される。The mixed liquid 5 is then sent to the nitrification tank 8 through the water pipe 7. In the nitrification tank 8, the air supplied from the blower 15 is diffused into the mixed liquid 5 using an aeration pipe, and the nitrogen compounds contained in the mixed liquid 5 are converted into nitrate compounds and nitrogen by the nitrifying bacteria cultured in the activated sludge. Oxidized to nitrate compounds. Furthermore, the nitrate compounds and nitrite compounds in the nitrification tank 8 are removed from the nitrification circulating fluid 1.
As 9, the activated sludge is returned to the denitrifying rosewood 1 through the circulation pipe 21 by the circulation pump 20, and is reduced to nitrogen gas and nitrogen oxide gas by the nitric acid respiration and nitrite respiration of the denitrifying bacteria.
そして、脱窒紫檀1および硝化槽8を循環した混合液5
は膜分離装置9を通して吸引ポンプtoiこ吸引される
ことにより固液分離され、分離膜11を透過した透過液
が処理水22として抽出されるとともに、分i!il膜
11に捕捉されて硝化槽8に残留した活性汚泥は返送汚
泥として硝化循環液19とともに脱窒紫檀1に戻される
。また、余剰汚泥は汚泥吸引ポンプ17により余剰汚泥
排出管18を通して硝化槽8の外部に排出される。Then, the mixture 5 circulated through the denitrification rosewood 1 and the nitrification tank 8
is separated into solid and liquid by being sucked through the membrane separator 9 by a suction pump, and the permeate that has passed through the separation membrane 11 is extracted as treated water 22. The activated sludge captured by the il membrane 11 and remaining in the nitrification tank 8 is returned to the denitrification rosewood 1 together with the nitrification circulating fluid 19 as return sludge. Further, the surplus sludge is discharged to the outside of the nitrification tank 8 by the sludge suction pump 17 through the surplus sludge discharge pipe 18.
そして、散気管14から散気された空気のエアリフト作
用により生じた上昇撹拌流が分離膜11の膜面に付着し
たゲル層などを洗浄除去する。さらに、超音波洗浄装置
を構成する超音波発振器13で発振した超音波を超音波
端子部12から膜分離装置9に発信し、膜分離装置9の
濾過膜11の膜面に超音波振動を与え、濾過1ullの
膜面の振動および振動する膜面と混合液5の干渉によっ
て膜面に付着したゲル層などの付着物を洗浄除去する。Then, the upward agitation flow generated by the air lift effect of the air diffused from the aeration tube 14 washes away the gel layer and the like attached to the membrane surface of the separation membrane 11. Further, the ultrasonic waves generated by the ultrasonic oscillator 13 constituting the ultrasonic cleaning device are transmitted from the ultrasonic terminal section 12 to the membrane separation device 9, and ultrasonic vibrations are applied to the membrane surface of the filtration membrane 11 of the membrane separation device 9. , the gel layer and other deposits adhering to the membrane surface due to the vibration of the membrane surface of the filtration 1 μl and the interference between the vibrating membrane surface and the mixed liquid 5 are washed and removed.
したがって、膜面の洗浄に際して汚泥フロックに何ら影
響を与えず、汚泥フロックの破壊などによる生物学的処
理能力の低下を来すことなく確実に膜面の洗浄が行なわ
れる。Therefore, when cleaning the membrane surface, the membrane surface is reliably cleaned without affecting the sludge flocs and without deteriorating the biological treatment capacity due to destruction of the sludge flocs.
発明の効果
以上述べたように本発明によれば、超音波洗浄装置によ
って膜分離装置の濾過膜の膜面に超音波振動を与えるこ
とによって、膜面の振動および振動する膜面と原水の干
渉によって膜面に付着したゲル層などの付着物を洗浄除
去することができ、膜面の洗浄に際して汚泥フロックに
何ら影響を与えず、汚泥フロックの破壊などによる生物
学的処理能力の低下を来すことなく確実に膜面の洗浄を
行うことができる。Effects of the Invention As described above, according to the present invention, by applying ultrasonic vibration to the membrane surface of a filtration membrane of a membrane separation device using an ultrasonic cleaning device, vibration of the membrane surface and interference between the vibrating membrane surface and raw water are reduced. The gel layer and other deposits on the membrane surface can be washed and removed, and the cleaning of the membrane surface does not have any effect on the sludge flocs, resulting in a decrease in biological treatment capacity due to destruction of the sludge flocs, etc. The membrane surface can be reliably cleaned without any problems.
第1図は本発明・の一実施例を示す全体構成図である。
8・・・硝化槽、9・・・膜分離装置、11・・・分離
膜、12・・・超音波端子部、13・・・超音波発振器
。FIG. 1 is an overall configuration diagram showing an embodiment of the present invention. 8... Nitrification tank, 9... Membrane separation device, 11... Separation membrane, 12... Ultrasonic terminal section, 13... Ultrasonic oscillator.
Claims (1)
水処理設備において、膜分離装置の膜面に超音波振動を
与える超音波洗浄装置を設けたことを特徴とする廃水処
理設備。1. A wastewater treatment facility in which a membrane separator is immersed in a biological treatment tank, characterized in that it is equipped with an ultrasonic cleaning device that applies ultrasonic vibrations to the membrane surface of the membrane separator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2008819A JPH03213128A (en) | 1990-01-18 | 1990-01-18 | Wastewater treatment equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2008819A JPH03213128A (en) | 1990-01-18 | 1990-01-18 | Wastewater treatment equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH03213128A true JPH03213128A (en) | 1991-09-18 |
Family
ID=11703418
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2008819A Pending JPH03213128A (en) | 1990-01-18 | 1990-01-18 | Wastewater treatment equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH03213128A (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH05154354A (en) * | 1991-12-11 | 1993-06-22 | Ebara Infilco Co Ltd | Membrane filtration apparatus |
| JP2006239627A (en) * | 2005-03-04 | 2006-09-14 | Mitsubishi Heavy Ind Ltd | Nitrogen-containing organic wastewater treatment system |
| WO2010073442A1 (en) | 2008-12-25 | 2010-07-01 | 志摩環境事業協業組合 | Immersion-type membrane separation apparatus |
| JP2011183393A (en) * | 2011-05-23 | 2011-09-22 | Mitsubishi Heavy Industries Environmental & Chemical Engineering Co Ltd | Apparatus for post-treatment of methane fermentation, system for post-treatment of methane fermentation, and method thereof |
| JP2011189327A (en) * | 2010-03-17 | 2011-09-29 | Shima Kankyo Jigyo Kyogyo Kumiai | Flat plate-like membrane element and immersion type membrane separator using this element |
| JP2014057966A (en) * | 2013-12-28 | 2014-04-03 | Shima Kankyo Jigyo Kyogyo Kumiai | Plate membrane element and immersing type membrane separator using the same |
| JP2014057965A (en) * | 2013-12-28 | 2014-04-03 | Shima Kankyo Jigyo Kyogyo Kumiai | Plate membrane element and immersing type membrane separator using the same |
| CN104147936A (en) * | 2014-08-06 | 2014-11-19 | 江苏大学 | Rolled membrane ultrasonic wave filtration auxiliary device and experimental method |
| JP2017056447A (en) * | 2015-09-18 | 2017-03-23 | 王子ホールディングス株式会社 | Water treatment system and method |
-
1990
- 1990-01-18 JP JP2008819A patent/JPH03213128A/en active Pending
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH05154354A (en) * | 1991-12-11 | 1993-06-22 | Ebara Infilco Co Ltd | Membrane filtration apparatus |
| JP2006239627A (en) * | 2005-03-04 | 2006-09-14 | Mitsubishi Heavy Ind Ltd | Nitrogen-containing organic wastewater treatment system |
| WO2010073442A1 (en) | 2008-12-25 | 2010-07-01 | 志摩環境事業協業組合 | Immersion-type membrane separation apparatus |
| JP2010149064A (en) * | 2008-12-25 | 2010-07-08 | Shima Kankyo Jigyo Kyogyo Kumiai | Immersion type membrane separation apparatus |
| US9073012B2 (en) | 2008-12-25 | 2015-07-07 | Shimakankyoujigyou Kyougyoukumiai | Immersion-type membrane separation apparatus |
| JP2011189327A (en) * | 2010-03-17 | 2011-09-29 | Shima Kankyo Jigyo Kyogyo Kumiai | Flat plate-like membrane element and immersion type membrane separator using this element |
| JP2011183393A (en) * | 2011-05-23 | 2011-09-22 | Mitsubishi Heavy Industries Environmental & Chemical Engineering Co Ltd | Apparatus for post-treatment of methane fermentation, system for post-treatment of methane fermentation, and method thereof |
| JP2014057966A (en) * | 2013-12-28 | 2014-04-03 | Shima Kankyo Jigyo Kyogyo Kumiai | Plate membrane element and immersing type membrane separator using the same |
| JP2014057965A (en) * | 2013-12-28 | 2014-04-03 | Shima Kankyo Jigyo Kyogyo Kumiai | Plate membrane element and immersing type membrane separator using the same |
| CN104147936A (en) * | 2014-08-06 | 2014-11-19 | 江苏大学 | Rolled membrane ultrasonic wave filtration auxiliary device and experimental method |
| JP2017056447A (en) * | 2015-09-18 | 2017-03-23 | 王子ホールディングス株式会社 | Water treatment system and method |
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