JP2000189998A - Method and device for concentrating sludge - Google Patents

Method and device for concentrating sludge

Info

Publication number
JP2000189998A
JP2000189998A JP11000245A JP24599A JP2000189998A JP 2000189998 A JP2000189998 A JP 2000189998A JP 11000245 A JP11000245 A JP 11000245A JP 24599 A JP24599 A JP 24599A JP 2000189998 A JP2000189998 A JP 2000189998A
Authority
JP
Japan
Prior art keywords
sludge
tank
membrane
filtrate
concentration
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.)
Withdrawn
Application number
JP11000245A
Other languages
Japanese (ja)
Inventor
Mitsuaki Nuno
光昭 布
Takeshi Yoshizaki
健 吉崎
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.)
Kubota Corp
Original Assignee
Kubota Corp
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 Kubota Corp filed Critical Kubota Corp
Priority to JP11000245A priority Critical patent/JP2000189998A/en
Publication of JP2000189998A publication Critical patent/JP2000189998A/en
Withdrawn legal-status Critical Current

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  • Separation Using Semi-Permeable Membranes (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Treatment Of Sludge (AREA)

Abstract

PROBLEM TO BE SOLVED: To concentrate sludge into high concentration by using a membrane. SOLUTION: At the time of flocculating by adding an aluminum based flocculant in a water treating process and taking out settled sludge to concentrate, the sludge 6 is charged to a concentration tank 4, in which a membrane module 5 is mounted to be dipped, is adjusted to a prescribed acidic pH range with sulfuric acid, filtered with the membrane module 5 and concentrated by discharging the filtrate 16 outside the tank. As a result, the filtration is performed by decreasing the viscosity of the sludge? 6 to make easily flowable, metal oxides or microorganisms are hardly stuck to the membrane surface, which is kept acidic, and then, the clogging of the membrane module 5 and the plugging of the flow passage between membranes are prevented and the sludge is highly concentrated.

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、浄水や下水などの
水処理分野で発生した凝集沈殿汚泥、濾過池逆洗排水汚
泥等の汚泥を濃縮する汚泥濃縮方法および装置に関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and an apparatus for concentrating sludge such as coagulated sediment sludge generated in the field of water treatment such as purified water and sewage, and sludge such as filter pond backwash drainage sludge.

【0002】[0002]

【従来の技術】浄水や下水などの水処理分野で発生した
凝集沈殿汚泥、濾過池逆洗排水汚泥等の汚泥は従来、濃
縮した後に脱水処理している。汚泥濃縮の装置として
は、自然沈降を利用した自然沈降式濃縮槽や、濾過膜な
どを利用した機械濃縮装置がある。
2. Description of the Related Art Conventionally, sludge such as coagulated sediment sludge generated in the field of water treatment such as purified water and sewage, and sludge such as filtration pond backwash drainage sludge are concentrated and then dewatered. As an apparatus for sludge concentration, there are a natural sedimentation type concentration tank using natural sedimentation, and a mechanical concentration apparatus using a filtration membrane or the like.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、浄水場
などの凝集沈殿池で発生する汚泥は近年、原水水質の悪
化による有機物の増加や、それに伴うアルミニウム系凝
集剤(硫酸バンド、PACなど)の添加率の増加によっ
て、濃縮性が悪くなってきている。特に、アルミニウム
系凝集剤は汚泥中でAl(OH)3 の水和フロックを形
成し、このフロックが周囲に水分子を保持し易いため、
濃縮性を悪化させる要因となっている。
However, in recent years, sludge generated in coagulation sedimentation ponds such as water purification plants has increased organic matter due to deterioration of raw water quality, and added aluminum-based coagulant (sulfuric acid band, PAC, etc.). Increasing rates have led to poor enrichment. In particular, an aluminum-based flocculant is used in sludge in Al (OH) 3 Forms a hydrated floc, and since this floc easily holds water molecules around,
This is a factor that deteriorates the concentration.

【0004】その結果、自然沈降式濃縮槽では、汚泥濃
縮濃度が低くなり、脱水機での脱水性も低くなるため、
脱水設備を増大せざるをえない。また濾過膜を利用した
濃縮装置では、処理時間の短縮や装置設置面積の低減な
どの利点はあるものの、汚泥濃縮濃度の上昇につれて粘
性が著しく増大し、それによる濾過膜の目づまりや膜間
の流路閉塞など、運転に支障をきたす事態が生じること
があるため、高濃度濃縮が困難である。
[0004] As a result, in the natural sedimentation type thickening tank, the concentration of sludge becomes low, and the dewatering property of the dewatering machine becomes low.
Dehydration equipment must be increased. Concentration devices that use filtration membranes have the advantages of shortening the processing time and reducing the installation area of the device.However, the viscosity increases significantly as the concentration of sludge increases, resulting in clogging of the filtration membrane and inter-membrane space. Since a situation that hinders the operation such as blockage of the flow path may occur, it is difficult to concentrate at a high concentration.

【0005】本発明は上記問題を解決するもので、濾過
膜を利用して汚泥の高濃度濃縮を行えるようにすること
を目的とするものである。
An object of the present invention is to solve the above-mentioned problems, and an object of the present invention is to enable sludge to be concentrated at a high concentration using a filtration membrane.

【0006】[0006]

【課題を解決するための手段】上記問題を解決するため
に、本発明の汚泥濃縮方法は、水処理工程においてアル
ミニウム系凝集剤の添加により凝集し、沈殿した汚泥を
引き抜いて濃縮するに際し、分離膜を浸漬設置した濃縮
槽に汚泥を投入し、酸により所定の酸性側pH域に調整
しつつ前記分離膜により濾過して、濾液を槽外へ導出す
ることにより濃縮することを特徴とする。
Means for Solving the Problems To solve the above problems, the sludge concentrating method of the present invention is characterized in that, in the water treatment step, an agglomeration agent is added by adding an aluminum-based coagulant, and the separated sludge is extracted and concentrated. Sludge is put into a concentration tank in which the membrane is immersed and installed, filtered by the separation membrane while adjusting the pH to a predetermined acidic side with an acid, and concentrated by drawing the filtrate out of the tank.

【0007】また、濾液を、凝集処理設備に流入する原
水に注入することを特徴とする。
[0007] The present invention is characterized in that the filtrate is injected into raw water flowing into the coagulation treatment facility.

【0008】本発明の汚泥濃縮装置は、上記した汚泥濃
縮方法を実施する汚泥濃縮装置であって、アルミニウム
系凝集剤を添加した汚泥が投入される濃縮槽と、槽内に
浸漬設置された分離膜と、前記分離膜の膜透過側に連通
した濾液導出系と、槽内の汚泥のpHを測定するpH測
定手段と、槽内の汚泥にpH調整剤を注入する薬品注入
手段と、前記pH測定手段と薬品注入手段とに接続して
設けられ、pH測定手段により測定されたpH測定値に
基いて薬品注入手段によるpH調整剤の注入量を制御す
る制御装置とを備えたことを特徴とする。
The sludge concentrating apparatus of the present invention is a sludge concentrating apparatus for performing the above-described sludge concentrating method, and comprises a thickening tank into which sludge to which an aluminum-based coagulant is added is placed, and a separating tank immersed in the tank. A membrane, a filtrate discharge system communicating with the membrane permeation side of the separation membrane, a pH measuring means for measuring the pH of the sludge in the tank, a chemical injecting means for injecting a pH adjusting agent into the sludge in the tank, and the pH A controller provided to be connected to the measuring means and the chemical injecting means, and controlling the injection amount of the pH adjusting agent by the chemical injecting means based on the pH measurement value measured by the pH measuring means, I do.

【0009】ここで、所定の酸性側pH域とは、アルミ
ニウム系凝集剤により汚泥中に形成されたAl(OH)
3 フロックがAl3+として再溶解する酸性側pH域であ
り、pH3〜5程度である。これより高いと再溶解が不
十分になり、これより低くするのはpH調整剤の無駄で
ある。
Here, the predetermined acidic pH range is defined as Al (OH) formed in the sludge by the aluminum-based flocculant.
Three It is an acidic pH range where the floc is redissolved as Al 3+ , and has a pH of about 3 to 5. If it is higher than this, re-dissolution becomes insufficient, and if it is lower than this, the pH adjuster is wasted.

【0010】酸は硫酸や塩酸など、pH調整剤として作
用するものであればよい。
The acid may be any one that acts as a pH adjuster, such as sulfuric acid or hydrochloric acid.

【0011】分離膜としてはセラミック膜、有機膜な
ど、上記した酸性側pH域で損傷しない耐酸性分離膜を
使用する。
As the separation membrane, an acid-resistant separation membrane which is not damaged in the above-mentioned acidic pH range, such as a ceramic membrane and an organic membrane, is used.

【0012】上記したような汚泥濃縮方法および装置に
よれば、Al(OH)3 フロックがAl3+に変化するこ
とで、汚泥の粘性が低下して流動し易い状態となって濾
過が容易になるとともに、膜面が酸性域に保たれること
で金属酸化物や微生物などが付着しにくいこともあっ
て、分離膜の目詰まりを防止することができ、分離膜の
エレメントが複数設置されている場合には膜間の流路閉
塞も生じにくいため、効率よく高濃度濃縮を行える。
According to the method and apparatus for concentrating sludge as described above, Al (OH) 3 By changing the floc to Al 3+ , the sludge becomes less viscous and flows more easily, making filtration easier, and the membrane surface is kept in an acidic region, so that metal oxides and microorganisms are reduced. Because it is difficult to adhere, clogging of the separation membrane can be prevented, and when multiple elements of the separation membrane are installed, it is difficult to block the flow path between the membranes. I can do it.

【0013】また濾液を、凝集処理設備に流入する原水
に注入することにより、分離膜を透過した濾液中に含ま
れているAl3+を再利用して原水中の濁質や藻類などを
凝集させることができ、凝集処理設備における凝集剤の
注入量を低減できる。
[0013] Further, by injecting the filtrate into the raw water flowing into the coagulation treatment equipment, Al 3+ contained in the filtrate permeating the separation membrane is reused to coagulate turbidity and algae in the raw water. And the amount of coagulant injected into the coagulation treatment equipment can be reduced.

【0014】[0014]

【発明の実施の形態】以下、本発明の実施形態を図面を
参照しながら説明する。
Embodiments of the present invention will be described below with reference to the drawings.

【0015】図1に示した汚泥濃縮装置は、浄水場にお
いて、原水が着水井1を経て導入される凝集沈殿池2で
アルミニウム系凝集剤の添加により凝集沈殿した汚泥を
濃縮するものであり、凝集沈殿池2からの給泥管3が上
部に開口した濃縮槽4に、膜モジュール5が内設されて
おり、汚泥6を引き抜く汚泥引抜管7が下部に開口して
いる。
The sludge concentrating apparatus shown in FIG. 1 is for condensing sludge that has been coagulated and settled by adding an aluminum-based coagulant in a coagulation settling tank 2 into which raw water is introduced via a landing well 1 in a water purification plant. A membrane module 5 is provided in a concentration tank 4 in which a sludge supply pipe 3 from the coagulation sedimentation tank 2 is opened at an upper part, and a sludge extraction pipe 7 for extracting sludge 6 is opened at a lower part.

【0016】膜モジュール5は、たとえば図2に示した
ようなものであり、上下が開口したケーシング8の内部
に管状セラミック膜などの耐酸性膜エレメント9が互い
に間隔をおいて、かつケーシング8に形成された集水室
10の内部に開口して配列されていて、槽底部との間に
適当間隙をおいて、汚泥6中に浸漬するように複数段に
積層されている。
The membrane module 5 is, for example, as shown in FIG. 2, in which an acid-resistant membrane element 9 such as a tubular ceramic membrane is provided inside a casing 8 having an opening at the top and bottom and spaced apart from each other. The openings are arranged inside the formed water collecting chamber 10, and are stacked in a plurality of stages so as to be immersed in the sludge 6 with an appropriate gap between the tank and the bottom.

【0017】各膜モジュール5の集水室10に一端にお
いて連通した濾液導出管11はポンプ装置12を介装
し、処理水槽13に導かれている。膜モジュール5の下
方には、ブロワ14などの給気手段より供給される空気
などの攪拌ガスを噴出する散気装置15が設けられてい
る。
A filtrate outlet pipe 11 connected at one end to a water collecting chamber 10 of each membrane module 5 is provided with a pump device 12 and guided to a treated water tank 13. Below the membrane module 5, there is provided an air diffuser 15 for jetting a stirring gas such as air supplied from an air supply means such as a blower 14.

【0018】処理水槽13には、槽内の濾液16を後段
の処理工程へ導く処理水管17と、ポンプ装置18を介
装し上述した着水井1に至る返送管19と、ポンプ装置
20を介装し濾液導出管7の管路途中に至る洗浄水管2
1とが設けられている。
In the treated water tank 13, a treated water pipe 17 for guiding the filtrate 16 in the tank to a subsequent treatment step, a return pipe 19 provided with a pump device 18 and reaching the above-mentioned landing well 1, and a pump device 20 are provided. Washing water pipe 2 which is installed in the middle of the filtrate outlet pipe 7
1 is provided.

【0019】濃縮槽4にはまた、硫酸22などの酸を入
れた薬品タンク23より導かれ薬注ポンプ24を介装し
た薬注管25が開口するとともに、槽内の汚泥6のpH
を測定するpH計26が設けられている。
The concentrating tank 4 is also opened with a chemical injection pipe 25 guided from a chemical tank 23 containing an acid such as sulfuric acid 22 and provided with a chemical injection pump 24, and the pH of the sludge 6 in the tank.
Is provided.

【0020】pH計26と薬注ポンプ24とに接続して
設けられた制御装置27は、pH計26により測定され
たpH測定値に基いて薬注ポンプ24の吐出量を制御す
るものである。
A control device 27 connected to the pH meter 26 and the chemical injection pump 24 controls the discharge amount of the chemical injection pump 24 based on the pH measured by the pH meter 26. .

【0021】上記した構成における作用を説明する。The operation of the above configuration will be described.

【0022】凝集沈殿池2より給泥管3を通じて濃縮槽
4に導入された汚泥6は、散気装置15より噴出する攪
拌ガスによって膜モジュール5のケーシング8の内外を
流動し、その間にポンプ装置12より濾液導出管11を
通じて膜エレメント9に作用する吸引圧によって膜面に
おいて濾過され、膜面を透過した濾液16が集水室1
0,濾液導出管11を通じて処理水槽13へ導出され、
それにより濃縮された汚泥6が槽底部に蓄積する。処理
水槽13の内部の濾液16は処理水管17を通じて後段
の処理工程へ導かれる。
The sludge 6 introduced into the concentration tank 4 from the coagulation sedimentation tank 2 through the supply pipe 3 flows through the inside and outside of the casing 8 of the membrane module 5 by the agitated gas ejected from the air diffuser 15, while the pump device The filtrate 16 is filtered from the membrane surface by the suction pressure acting on the membrane element 9 through the filtrate outlet pipe 11, and the filtrate 16 that has passed through the membrane surface is collected by the collection chamber 1.
0, led out to the treated water tank 13 through the filtrate outlet pipe 11,
Thereby, the concentrated sludge 6 accumulates at the bottom of the tank. The filtrate 16 inside the treatment water tank 13 is guided to a subsequent treatment step through a treatment water pipe 17.

【0023】このとき、濃縮槽4内の汚泥6のpHがp
H計26により測定され、そのpH測定値に基いて制御
装置27により薬注ポンプ24の吐出量が制御され、薬
品タンク23内の硫酸22が薬注管25を通じて適量だ
け注入されるという動作が適宜に行われ、汚泥6は常時
pH3〜5に調整される。
At this time, the pH of the sludge 6 in the concentration tank 4 is
The discharge amount of the chemical injection pump 24 is controlled by the control device 27 based on the measured pH value by the H meter 26, and the sulfuric acid 22 in the chemical tank 23 is injected through the chemical injection tube 25 by an appropriate amount. The sludge 6 is constantly adjusted to pH 3 to 5 as appropriate.

【0024】それにより、汚泥6中に形成されていたA
l(OH)3 フロックがAl3+となって再溶解して汚泥
6の粘性が低下し、攪拌ガスによる汚泥攪拌が十分に行
われ、膜エレメント9間の流路閉塞が防止されるととも
に、膜エレメント9の膜面が酸性域に保たれ金属酸化物
や微生物などが付着しにくいこともあって、膜エレメン
ト9の目詰まりが防止されるため、高い濾過流束が維持
され、効率よく高濃度濃縮が行われる。
Thus, the A formed in the sludge 6
l (OH) 3 The floc is converted to Al 3+ and redissolved, the viscosity of the sludge 6 is reduced, the sludge is sufficiently stirred by the stirring gas, the flow passage between the membrane elements 9 is prevented, and the membrane of the membrane element 9 is prevented. Since the surface is kept in an acidic region and metal oxides and microorganisms are unlikely to adhere thereto, clogging of the membrane element 9 is prevented, so that a high filtration flux is maintained and high concentration is efficiently performed. .

【0025】なお、流入原水中の濁質や藻類の量によっ
ては、処理水槽13より流出した濾液16の一部をポン
プ装置18により返送管19を通じて着水井1に注入す
る。これにより、濾液16中に含まれているAl3+(A
2 (SO4)3)が凝集作用を発揮して流入原水中の濁質
や藻類を凝集させるため、凝集沈殿池2における凝集剤
の使用量を低減できる。
Depending on the amount of turbidity and algae in the inflowing raw water, a part of the filtrate 16 flowing out of the treated water tank 13 is injected into the landing well 1 through the return pipe 19 by the pump device 18. As a result, the Al 3+ (A
l 2 Since (SO 4 ) 3 ) exerts a flocculating action to flocculate turbidity and algae in the inflowing raw water, the amount of flocculant used in the flocculating sedimentation basin 2 can be reduced.

【0026】濾液16を着水井1ではなく凝集沈殿池2
に返送しても濾液16中のAl3+の凝集作用を利用でき
るが、その場合は濾液16による流動変動が悪影響を及
ぼさないように考慮する必要がある。
The filtrate 16 is used not in the landing well 1 but in the flocculation settling tank 2
Although the agglomerating action of Al 3+ in the filtrate 16 can be used even if the flow is returned to the above, it is necessary to consider that the flow fluctuation caused by the filtrate 16 does not have an adverse effect.

【0027】また、定期的に、あるいは膜エレメント9
における透過流束が低下した時には、処理水槽13内の
濾液16をポンプ装置20と洗浄水管21とにより、必
要に応じて次亜塩素酸ソーダなどの洗浄薬液を添加した
うえで、濾液導出管7の内部に送り込み、膜エレメント
9の透過側に圧送して、目詰まり物質を化学的、物理的
に除去する逆洗という操作を行なう。しかし、上記した
ように濃縮処理中も膜エレメント9の目詰まりは生じに
くいので、洗浄頻度が少なくて済み、膜寿命も長くな
る。
Also, periodically or with the membrane element 9
When the permeation flux at the time is lowered, the filtrate 16 in the treatment water tank 13 is added to the filtrate outlet pipe 7 by the pump device 20 and the washing water pipe 21 after adding a washing reagent such as sodium hypochlorite as necessary. , And pressure-fed to the permeation side of the membrane element 9 to perform an operation of backwashing for chemically and physically removing clogging substances. However, as described above, clogging of the membrane element 9 hardly occurs even during the concentration process, so that the frequency of cleaning is reduced and the life of the membrane is prolonged.

【0028】[0028]

【発明の効果】以上のように本発明によれば、アルミニ
ウム系凝集剤を含んだ汚泥を濃縮するに際し、所定の酸
性側pH域に調整しつつ汚泥中に浸漬設置した分離膜に
より濾過し、濾液を槽外へ導出するようにしたので、A
l(OH)3 フロックに起因する汚泥の粘性を低下さ
せ、分離膜の目詰まりや膜間の流路閉塞を防止して、高
い濾過流束で効率よく濃縮することができ、高濃度の濃
縮汚泥を得ることができる。したがって従来に比べて、
分離膜の洗浄頻度を低減し、膜寿命を長くできるだけで
なく、装置設計段階において膜面積を低減することも可
能である。
As described above, according to the present invention, when condensing sludge containing an aluminum-based flocculant, the sludge is filtered through a separation membrane immersed and installed in the sludge while being adjusted to a predetermined acidic pH range. Since the filtrate was led out of the tank, A
l (OH) 3 It reduces the viscosity of sludge caused by flocs, prevents clogging of separation membranes and blockages of channels between membranes, enables efficient concentration with high filtration flux, and enables high-concentration sludge to be obtained. it can. Therefore, compared to the past,
Not only can the frequency of cleaning the separation membrane be reduced and the life of the membrane can be extended, but also the membrane area can be reduced at the stage of designing the apparatus.

【0029】また、Al3+を含んだ濾液を、凝集処理設
備に流入する原水に注入することにより、Al3+を再利
用して凝集処理設備における凝集剤の使用量を低減でき
る。
Further, by injecting the filtrate containing Al 3+ into the raw water flowing into the coagulation treatment equipment, the amount of the coagulant used in the coagulation treatment equipment can be reduced by recycling Al 3+ .

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

【図1】本発明の一実施形態における汚泥凝集装置の概
略全体構成を示した説明図である。
FIG. 1 is an explanatory diagram showing a schematic overall configuration of a sludge aggregation device according to an embodiment of the present invention.

【図2】同汚泥凝集装置に設置される従来の膜モジュー
ルの構成を示した説明図である。
FIG. 2 is an explanatory diagram showing a configuration of a conventional membrane module installed in the sludge flocculation apparatus.

【符号の説明】[Explanation of symbols]

4 濃縮槽 5 膜モジュール 6 汚泥 11 濾液導出管 24 薬注ポンプ 25 薬注管 26 pH計 27 制御装置 4 Concentration tank 5 Membrane module 6 Sludge 11 Filtrate discharge pipe 24 Chemical injection pump 25 Chemical injection pipe 26 pH meter 27 Controller

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) C02F 1/44 C02F 1/44 K 1/52 1/52 E Fターム(参考) 4D006 GA02 HA21 HA93 HA95 KA33 KA43 KB13 KB30 KC03 KC16 KD11 KD24 KE15R MA02 MB12 MC03X PA02 PB08 PC64 4D015 BA04 CA01 CA14 DA04 DA06 EA32 FA12 FA17 FA28 4D059 AA06 AA30 BE03 BE14 BE42 BE49 BF12 BJ09 CA24 CA28 CB08 CB17 DA33 DA45 EA05 EB05 EB11 4D062 BA04 CA01 CA14 DA04 DA06 EA32 FA12 FA17 FA28 ──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 7 Identification symbol FI theme coat ゛ (reference) C02F 1/44 C02F 1/44 K 1/52 1/52 EF term (reference) 4D006 GA02 HA21 HA93 HA95 KA33 KA43 KB13 KB30 KC03 KC16 KD11 KD24 KE15R MA02 MB12 MC03X PA02 PB08 PC64 4D015 BA04 CA01 CA14 DA04 DA06 EA32 FA12 FA17 FA28 4D059 AA06 AA30 BE03 BE14 BE42 BE49 BF12 BJ09 CA24 CA28 CB08 CA14 EB17 DA04 DA05 DA04 FA17 FA28

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 水処理工程においてアルミニウム系凝集
剤の添加により凝集し、沈殿した汚泥を引き抜いて濃縮
するに際し、分離膜を浸漬設置した濃縮槽に汚泥を投入
し、酸により所定の酸性側pH域に調整しつつ前記分離
膜により濾過し、濾液を槽外へ導出することにより濃縮
することを特徴とする汚泥濃縮方法。
Claims: 1. In the water treatment step, when extracting and concentrating sludge that has been coagulated and precipitated by adding an aluminum-based coagulant, the sludge is put into a concentration tank in which a separation membrane is immersed and installed, and a predetermined acid-side pH is set with an acid. A method for concentrating sludge, wherein the sludge is filtered by the separation membrane while being adjusted to an area, and the filtrate is concentrated by drawing it out of the tank.
【請求項2】 濾液は、凝集処理設備に流入する原水に
注入することを特徴とする請求項1記載の汚泥濃縮方
法。
2. The sludge concentration method according to claim 1, wherein the filtrate is injected into raw water flowing into the coagulation treatment facility.
【請求項3】 アルミニウム系凝集剤を添加した汚泥が
投入される濃縮槽と、槽内に浸漬設置された分離膜と、
前記分離膜の膜透過側に連通した濾液導出系と、槽内の
汚泥のpHを測定するpH測定手段と、槽内の汚泥にp
H調整剤を注入する薬品注入手段と、前記pH測定手段
と薬品注入手段とに接続して設けられ、pH測定手段に
より測定されたpH測定値に基いて薬品注入手段による
pH調整剤の注入量を制御する制御装置とを備えたこと
を特徴とする汚泥濃縮装置。
3. A concentration tank into which sludge to which an aluminum-based flocculant has been added is charged, and a separation membrane immersed and installed in the tank.
A filtrate discharge system connected to the membrane permeation side of the separation membrane, a pH measuring means for measuring the pH of the sludge in the tank,
A chemical injecting means for injecting the H adjusting agent, and an amount of the pH adjusting agent to be injected by the chemical injecting means based on the pH measured by the pH measuring means, the amount being provided connected to the pH measuring means and the chemical injecting means; And a control device for controlling the sludge concentration.
JP11000245A 1999-01-05 1999-01-05 Method and device for concentrating sludge Withdrawn JP2000189998A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11000245A JP2000189998A (en) 1999-01-05 1999-01-05 Method and device for concentrating sludge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11000245A JP2000189998A (en) 1999-01-05 1999-01-05 Method and device for concentrating sludge

Publications (1)

Publication Number Publication Date
JP2000189998A true JP2000189998A (en) 2000-07-11

Family

ID=11468578

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11000245A Withdrawn JP2000189998A (en) 1999-01-05 1999-01-05 Method and device for concentrating sludge

Country Status (1)

Country Link
JP (1) JP2000189998A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE10217418A1 (en) * 2002-04-18 2003-11-13 Fraunhofer Ges Forschung Sewage sludge tank with a device for sludge pre-dewatering
JP2006263650A (en) * 2005-03-25 2006-10-05 Ngk Insulators Ltd Ceramic membrane purified water making equipment and its operation method
JP2008188498A (en) * 2007-02-01 2008-08-21 Kobelco Eco-Solutions Co Ltd Treatment method and treatment equipment for water to be treated
KR102055267B1 (en) * 2019-03-20 2019-12-13 의림환경에너텍 주식회사 One tank type wastewater treatment apparatus
JP2020108874A (en) * 2019-01-07 2020-07-16 オルガノ株式会社 Membrane filtration apparatus and membrane filtration method

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE10217418A1 (en) * 2002-04-18 2003-11-13 Fraunhofer Ges Forschung Sewage sludge tank with a device for sludge pre-dewatering
JP2006263650A (en) * 2005-03-25 2006-10-05 Ngk Insulators Ltd Ceramic membrane purified water making equipment and its operation method
JP2008188498A (en) * 2007-02-01 2008-08-21 Kobelco Eco-Solutions Co Ltd Treatment method and treatment equipment for water to be treated
JP4536740B2 (en) * 2007-02-01 2010-09-01 株式会社神鋼環境ソリューション Treatment method and treatment equipment for treated water
JP2020108874A (en) * 2019-01-07 2020-07-16 オルガノ株式会社 Membrane filtration apparatus and membrane filtration method
JP7270383B2 (en) 2019-01-07 2023-05-10 オルガノ株式会社 MEMBRANE FILTRATION DEVICE AND MEMBRANE FILTRATION METHOD
KR102055267B1 (en) * 2019-03-20 2019-12-13 의림환경에너텍 주식회사 One tank type wastewater treatment apparatus

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