JP2001087635A - Active sludge treatment device using dynamic filtration membrane - Google Patents
Active sludge treatment device using dynamic filtration membraneInfo
- Publication number
- JP2001087635A JP2001087635A JP27349499A JP27349499A JP2001087635A JP 2001087635 A JP2001087635 A JP 2001087635A JP 27349499 A JP27349499 A JP 27349499A JP 27349499 A JP27349499 A JP 27349499A JP 2001087635 A JP2001087635 A JP 2001087635A
- Authority
- JP
- Japan
- Prior art keywords
- dynamic filtration
- dynamic
- filtration membrane
- membrane
- sludge treatment
- 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
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
- Activated Sludge Processes (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、ダイナミックろ過
膜を使用した活性汚泥処理装置に関し、下水、し尿、産
業廃水等の活性汚泥処理において汚泥をダイナミックろ
過膜でろ過する技術に係る。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an activated sludge treatment apparatus using a dynamic filtration membrane, and to a technique for filtering sludge with a dynamic filtration membrane in activated sludge treatment of sewage, human waste, industrial wastewater, and the like.
【0002】[0002]
【従来の技術】従来の生物学的窒素除去方法において、
生物反応槽における微生物濃度を高く維持する方法とし
てダイナミックろ過膜を使用するものがある。ダイナミ
ックろ過膜は、支持体の表面に網等によって形成するス
ペーサを配置し、スペーサを覆って不織布を配置したも
のであり、不織布の表面に活性汚泥粒子のダイナミック
層を形成し、このダイナミック層(ケーキ層)をろ過層
として利用するものである。BACKGROUND OF THE INVENTION In conventional biological nitrogen removal methods,
As a method for maintaining a high concentration of microorganisms in a biological reaction tank, there is a method using a dynamic filtration membrane. The dynamic filtration membrane is obtained by arranging a spacer formed by a net or the like on the surface of a support, and arranging a nonwoven fabric covering the spacer. A dynamic layer of activated sludge particles is formed on the surface of the nonwoven fabric. The cake layer) is used as a filtration layer.
【0003】[0003]
【発明が解決しようとする課題】上記したダイナミック
ろ過膜を使用する活性汚泥処理においては、生物反応槽
内に配置した散気装置から曝気空気を散気し、エアリフ
ト作用によって槽内に旋回流を発生させ、この旋回流に
よって槽内の活性汚泥混合液をろ過層の表面に沿ってク
ロスフローで供給し、ダイナミックろ過膜の内外の圧力
差を駆動圧力としてろ過を行なっている。In the activated sludge treatment using the above-mentioned dynamic filtration membrane, aerated air is diffused from a diffuser disposed in a biological reaction tank, and a swirling flow is generated in the tank by an air lift action. The activated sludge mixed liquid in the tank is supplied by cross-flow along the surface of the filtration layer by this swirling flow, and filtration is performed using a pressure difference between the inside and outside of the dynamic filtration membrane as a driving pressure.
【0004】ところで、クロスフローの流速が速すぎる
と不織布上にダイナミック層がろ過に必要な十分な厚さ
に形成されず、遅すぎるとダイナミック層の厚さが過剰
となって流束が低下することなり、流速の制御がろ過操
作を安定して行なううえで重要な要素となっている。し
かし、曝気空気によって生起する旋回流は乱流であり、
槽内に浸漬した複数のダイナミックろ過膜に対して、槽
内の活性汚泥混合液を常に均一な流れで供給することは
困難であった。[0004] By the way, if the flow velocity of the cross flow is too high, the dynamic layer is not formed on the nonwoven fabric to a thickness sufficient for filtration, and if it is too slow, the dynamic layer becomes excessively thick and the flux decreases. In other words, the control of the flow rate is an important factor for stably performing the filtration operation. However, the swirling flow caused by the aerated air is turbulent,
It has been difficult to always supply the activated sludge mixture in the tank with a uniform flow to a plurality of dynamic filtration membranes immersed in the tank.
【0005】本発明は上記した課題を解決するものであ
り、ダイナミックろ過膜に安定してダイナミック層を形
成し、ろ過を安定して行なうことができるダイナミック
ろ過膜を使用した活性汚泥処理装置を提供することを目
的とする。The present invention has been made to solve the above-mentioned problems, and provides an activated sludge treatment apparatus using a dynamic filtration membrane capable of stably forming a dynamic layer on a dynamic filtration membrane and performing stable filtration. The purpose is to do.
【0006】[0006]
【課題を解決するための手段】上記課題を解決するため
に、本発明のダイナミックろ過膜を使用した活性汚泥処
理装置は、生物反応槽内の一側に散気装置を配置すると
ともに、他側に鉛直方向に沿って配置する複数のダイナ
ミックろ過膜を、適当間隙をあけて平行に配置し、隣接
するダイナミックろ過膜間に平行な複数の整流板を鉛直
方向に沿って配置し、各ダイナミックろ過膜に連通して
処理水管を設けたものである。In order to solve the above-mentioned problems, an activated sludge treatment apparatus using a dynamic filtration membrane according to the present invention is provided with an air diffuser on one side in a biological reaction tank and another on the other side. A plurality of dynamic filtration membranes arranged along the vertical direction are arranged in parallel with an appropriate gap, and a plurality of straightening plates parallel to each other between adjacent dynamic filtration membranes are arranged along the vertical direction. A treated water pipe is provided in communication with the membrane.
【0007】[0007]
【発明の実施の形態】以下、本発明の実施の形態を図面
に基づいて説明する。図1〜図3において、生物反応槽
1は流入する原水2を活性汚泥処理する好気槽をなすも
のであり、槽の内部には、槽の一側に散気装置3を配置
し、槽の他側に膜分離装置4を浸漬し、散気装置3には
曝気空気を供給するブロア5を接続している。Embodiments of the present invention will be described below with reference to the drawings. In FIG. 1 to FIG. 3, a biological reaction tank 1 forms an aerobic tank for treating an inflowing raw water 2 with activated sludge. Inside the tank, an air diffuser 3 is arranged on one side of the tank. A membrane separator 4 is immersed on the other side, and a blower 5 for supplying aerated air is connected to the diffuser 3.
【0008】膜分離装置4は、鉛直方向に沿って配置す
る複数のダイナミックろ過膜6をケーシング7で保持し
てモジュール化しており、各ダイナミックろ過膜6は適
当間隙をあけて平行に配置し、隣接するダイナミックろ
過膜6の間に複数の整流板8を平行に、かつ鉛直方向に
沿って配置している。各ダイナミックろ過膜6は、支持
板9の表面に網材等のスペーサ10を配置し、スペーサ
10を覆って不織布11を配置し、不織布11の周囲を
シール材12で水密に封止しており、支持板9に透過液
流路13を形成している。The membrane separation device 4 is modularized by holding a plurality of dynamic filtration membranes 6 arranged in a vertical direction by a casing 7, and each of the dynamic filtration membranes 6 is arranged in parallel with an appropriate gap. A plurality of straightening plates 8 are arranged in parallel between the adjacent dynamic filtration membranes 6 and along the vertical direction. In each dynamic filtration membrane 6, a spacer 10 such as a net material is disposed on the surface of the support plate 9, a nonwoven fabric 11 is disposed so as to cover the spacer 10, and the periphery of the nonwoven fabric 11 is sealed with a sealant 12 in a watertight manner. The permeated liquid channel 13 is formed in the support plate 9.
【0009】各ダイナミックろ過膜6の透過液流路13
に連通する処理水管14は、槽外において生物反応槽1
の液面より所定距離Δhだけ下方において開口してい
る。以下、上記した構成における作用を説明する。ブロ
ア5によって供給する曝気空気を散気装置3から槽内の
活性汚泥混合液中に散気し、曝気によって活性汚泥処理
に必要な酸素を供給する。生物反応槽1の内部には曝気
空気のエアリフト作用によって旋回流を発生させ、この
旋回流によって槽内の活性汚泥混合液を膜分離装置4に
クロスフローで供給する。[0009] Permeate flow path 13 of each dynamic filtration membrane 6
The treatment water pipe 14 communicating with the biological reaction tank 1 outside the tank
Is opened below the liquid level by a predetermined distance Δh. Hereinafter, the operation of the above configuration will be described. The aerated air supplied by the blower 5 is diffused from the diffuser 3 into the activated sludge mixture in the tank, and oxygen required for activated sludge treatment is supplied by the aeration. A swirling flow is generated inside the biological reaction tank 1 by an air lift action of aerated air, and the activated sludge mixed liquid in the tank is supplied to the membrane separation device 4 by a cross flow using the swirling flow.
【0010】膜分離装置4に流入する活性汚泥混合液
は、整流板8で規制されて鉛直方向に沿った流れとな
り、隣接する整流板8間の流路を均一な流れとなって流
下する。この状態で、ダイナミックろ過膜6に作用する
水頭差Δhを駆動圧力として活性汚泥混合液をろ過し、
ろ過した処理水を処理水管14を通して取り出す。この
ように、ダイナミックろ過膜6には槽内の活性汚泥混合
液が整流板8に規制されて常に均一な流れで供給される
ので、その流速はブロア5を制御して散気装置3から散
気する空気量およびその流速を調整することにより、容
易に制御することができ、不織布11の表面に活性汚泥
粒子のダイナミック層をろ過に必要な厚さに安定して形
成することができ、このダイナミック層をろ過層として
安定したろ過性能を得ることができる。The activated sludge mixture flowing into the membrane separation device 4 is regulated by the flow straightening plates 8 and flows vertically, and flows down the flow path between the adjacent straightening plates 8 as a uniform flow. In this state, the activated sludge mixture is filtered using the head difference Δh acting on the dynamic filtration membrane 6 as a driving pressure,
The filtered treated water is taken out through the treated water pipe 14. As described above, since the activated sludge mixed liquid in the tank is always supplied to the dynamic filtration membrane 6 by the regulating plate 8 and is supplied in a uniform flow, the flow rate thereof is controlled by the blower 5 and diffused from the air diffuser 3. By adjusting the amount of air and the flow rate thereof, it can be easily controlled, and a dynamic layer of activated sludge particles can be stably formed on the surface of the nonwoven fabric 11 to a thickness required for filtration. A stable filtration performance can be obtained using the dynamic layer as a filtration layer.
【0011】[0011]
【発明の効果】以上のように、本発明によれば、隣接す
るダイナミックろ過膜間に平行な複数の整流板を鉛直方
向に沿って配置し、膜面に沿ってクロスフローで供給す
る槽内の活性汚泥混合液を、整流板で規制して常に均一
な流れで供給することにより、その流速を散気装置の調
整によって容易に制御することができ、不織布の表面に
形勢する活性汚泥粒子のダイナミック層をろ過に必要な
十分な厚さに安定して維持することができる。As described above, according to the present invention, a plurality of straightening plates parallel to each other between adjacent dynamic filtration membranes are arranged in the vertical direction, and the tank is supplied in a cross flow along the membrane surface. By controlling the activated sludge mixed solution with a flow straightening plate and always supplying it in a uniform flow, the flow rate can be easily controlled by adjusting the air diffuser, and the activated sludge particles forming on the surface of the nonwoven fabric can be easily controlled. The dynamic layer can be stably maintained at a sufficient thickness required for filtration.
【図1】本発明の実施の形態における活性汚泥処理装置
を示す模式図である。FIG. 1 is a schematic diagram showing an activated sludge treatment apparatus according to an embodiment of the present invention.
【図2】同実施の形態におけるダイナミックろ過膜の配
置構造を示す平面図である。FIG. 2 is a plan view showing an arrangement structure of a dynamic filtration membrane in the embodiment.
【図3】同実施の形態におけるダイナミックろ過膜の断
面図である。FIG. 3 is a cross-sectional view of the dynamic filtration membrane according to the embodiment.
1 生物反応槽 2 原水 3 散気装置 4 膜分離装置 5 ブロア 6 ダイナミックろ過膜 7 ケーシング 8 整流板 9 支持板 10 スペーサ 11 不織布 12 シール材 13 透過液流路 14 処理水管 DESCRIPTION OF SYMBOLS 1 Biological reaction tank 2 Raw water 3 Aeration device 4 Membrane separation device 5 Blower 6 Dynamic filtration membrane 7 Casing 8 Rectifier plate 9 Support plate 10 Spacer 11 Nonwoven fabric 12 Seal material 13 Permeate flow path 14 Treatment water pipe
───────────────────────────────────────────────────── フロントページの続き (72)発明者 吉崎 健 大阪府大阪市浪速区敷津東一丁目2番47号 株式会社クボタ内 (72)発明者 福原 真一 大阪府大阪市浪速区敷津東一丁目2番47号 株式会社クボタ内 (72)発明者 大井 裕亮 大阪府大阪市浪速区敷津東一丁目2番47号 株式会社クボタ内 Fターム(参考) 4D006 GA02 HA42 HA93 JA01A JA14A JA18A KA13 KA31 KA44 KB22 KE01Q MA03 MA16 MA40 PA01 PB08 PC62 4D028 BC17 CA09 ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Ken Yoshizaki 2-47, Shikitsu-Higashi 1-chome, Naniwa-ku, Osaka-shi, Osaka (72) Inventor Shinichi Fukuhara Shin-ichi Fukuhara, Osaka-shi, Osaka No. 2-47, Kubota Co., Ltd. (72) Inventor Yusuke Oi 1-47, Shishitsuhigashi, Naniwa-ku, Osaka-shi, Osaka F-term (reference) 4D006 GA02 HA42 HA93 JA01A JA14A JA18A KA13 KA31 KA44 KB22 KE01Q MA03 MA16 MA40 PA01 PB08 PC62 4D028 BC17 CA09
Claims (1)
るとともに、他側に鉛直方向に沿って配置する複数のダ
イナミックろ過膜を、適当間隙をあけて平行に配置し、
隣接するダイナミックろ過膜間に平行な複数の整流板を
鉛直方向に沿って配置し、各ダイナミックろ過膜に連通
して処理水管を設けたことを特徴とするダイナミックろ
過膜を使用した活性汚泥処理装置。An aeration device is arranged on one side in a biological reaction tank, and a plurality of dynamic filtration membranes arranged along the vertical direction on the other side are arranged in parallel with an appropriate gap therebetween.
Activated sludge treatment equipment using a dynamic filtration membrane, characterized in that a plurality of straightening plates parallel to each other between adjacent dynamic filtration membranes are arranged in the vertical direction, and a treated water pipe is provided in communication with each dynamic filtration membrane. .
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP27349499A JP2001087635A (en) | 1999-09-28 | 1999-09-28 | Active sludge treatment device using dynamic filtration membrane |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP27349499A JP2001087635A (en) | 1999-09-28 | 1999-09-28 | Active sludge treatment device using dynamic filtration membrane |
Publications (1)
Publication Number | Publication Date |
---|---|
JP2001087635A true JP2001087635A (en) | 2001-04-03 |
Family
ID=17528695
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP27349499A Pending JP2001087635A (en) | 1999-09-28 | 1999-09-28 | Active sludge treatment device using dynamic filtration membrane |
Country Status (1)
Country | Link |
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JP (1) | JP2001087635A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006021075A (en) * | 2004-07-06 | 2006-01-26 | Yoshiaki Kiso | Weight reduction method for organic surplus sludge and its device |
CN1317207C (en) * | 2003-10-21 | 2007-05-23 | 中国科学院生态环境研究中心 | Sewage treating apparatus with baffling, aerating, boosting and gravitationally outflowing membrane bioreactor |
CN101786772A (en) * | 2010-03-24 | 2010-07-28 | 哈尔滨工业大学 | Efficient biological treatment method for polymer-containing sewage in oil field |
CN104229985A (en) * | 2014-10-17 | 2014-12-24 | 苏州新协力环保科技有限公司 | Activated sludge purifying and processing method for wastewater |
WO2023239680A1 (en) * | 2022-06-08 | 2023-12-14 | Xylem Water Solutions Zelienople Llc | Chemical dosing of dynamic membrane systems and methods thereof |
-
1999
- 1999-09-28 JP JP27349499A patent/JP2001087635A/en active Pending
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1317207C (en) * | 2003-10-21 | 2007-05-23 | 中国科学院生态环境研究中心 | Sewage treating apparatus with baffling, aerating, boosting and gravitationally outflowing membrane bioreactor |
JP2006021075A (en) * | 2004-07-06 | 2006-01-26 | Yoshiaki Kiso | Weight reduction method for organic surplus sludge and its device |
CN101786772A (en) * | 2010-03-24 | 2010-07-28 | 哈尔滨工业大学 | Efficient biological treatment method for polymer-containing sewage in oil field |
CN104229985A (en) * | 2014-10-17 | 2014-12-24 | 苏州新协力环保科技有限公司 | Activated sludge purifying and processing method for wastewater |
WO2023239680A1 (en) * | 2022-06-08 | 2023-12-14 | Xylem Water Solutions Zelienople Llc | Chemical dosing of dynamic membrane systems and methods thereof |
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