JPH07195100A - Sludge treating device - Google Patents

Sludge treating device

Info

Publication number
JPH07195100A
JPH07195100A JP6001131A JP113194A JPH07195100A JP H07195100 A JPH07195100 A JP H07195100A JP 6001131 A JP6001131 A JP 6001131A JP 113194 A JP113194 A JP 113194A JP H07195100 A JPH07195100 A JP H07195100A
Authority
JP
Japan
Prior art keywords
pipe
sludge
stirring
air
raw water
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
JP6001131A
Other languages
Japanese (ja)
Other versions
JP3410533B2 (en
Inventor
Akira Matsuo
章 松尾
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.)
Chemical Grouting Co Ltd
Original Assignee
Chemical Grouting 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 Chemical Grouting Co Ltd filed Critical Chemical Grouting Co Ltd
Priority to JP00113194A priority Critical patent/JP3410533B2/en
Publication of JPH07195100A publication Critical patent/JPH07195100A/en
Application granted granted Critical
Publication of JP3410533B2 publication Critical patent/JP3410533B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PURPOSE:To continuously treat a large amt. of sludge by combining a sludge force feed pipe, a polymer flocculating agent soln. injecting pipe joining therewith, an air adding pipe joining therewith, a stirring pipe continuous with the press feed pipe and a separating pipe continuous therewith with each other. CONSTITUTION:Sludge raw water A is forcibly fed from the force feed pipe 1 and a polymer flocculating agent soln. B is injected from the injecting pipe 2. Air C is added to the air adding pipe 4. The polymer flocculating agent soln. B flowing from a tangent direction to the sludge raw water A and the air C are then added and mixed in the adding section X and the mixture D composed thereof is transported to the stirring section Y. The mixture D is turned in a direction a in the stirring section Y and is prevented from being arrested by the wall of the stirring pipe 6 by the added air C. The sludge raw water A is adequately flocculated by the polymer flocculating agent soln. B and is transported to the separating section Z. Further, the air C is made to escape and the sludge raw water A is separated and discharged to flocs E and separated excess water F in the separating section Z.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、例えばコラムジェット
グラウト工法において発生するスライム等の汚泥処理装
置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for treating sludge generated in a column jet grout method.

【0002】[0002]

【従来の技術】環境問題が重視される昨今、産業廃棄物
の扱いが困難になってきており、特にコラムジェット工
法で発生するスライム等の汚泥の減量化処理が要求され
る。
2. Description of the Related Art In recent years, environmental problems have been emphasized, and it has become difficult to handle industrial waste. In particular, reduction treatment of sludge such as slime generated by the column jet method is required.

【0003】これに対し従来の処理は、バッチミキシン
グが主であり、専用の水槽に汚泥原水を貯留し、薬液を
添加し、攪拌して分離する手順で処理を行っている。し
たがって、これらのステップをバッチで行うため、処理
能力には限界があって低い。これに対し薬液の添加、攪
拌及び分離を一本の管中で連続して行い、大流量を処理
するラインミキシングが知られている。しかし、従来の
ラインミキシングでは、管中に攪拌能力を向上させるた
めに乱流発生用の突起を設けている。しかし、セメント
等を含む汚泥の場合は、汚泥が突起に引っかかり、突起
の裏側(下流側)に滞溜し凝固してしまう可能性があ
り、好ましくない。
On the other hand, the conventional treatment is mainly batch mixing, in which the raw water of sludge is stored in a dedicated water tank, a chemical solution is added, and the mixture is stirred and separated. Therefore, since these steps are performed in batch, the throughput is limited and low. On the other hand, line mixing is known in which the addition, stirring, and separation of a chemical solution are continuously performed in a single pipe to process a large flow rate. However, in the conventional line mixing, a turbulent flow generation projection is provided in the pipe in order to improve the stirring ability. However, in the case of sludge containing cement or the like, the sludge may be caught by the protrusions and may accumulate on the back side (downstream side) of the protrusions and solidify, which is not preferable.

【0004】本発明は、大流量の汚泥を連続して処理す
ることができる汚泥処理装置を提供することを目的とし
ている。
An object of the present invention is to provide a sludge treatment device capable of continuously treating a large amount of sludge.

【0005】[0005]

【課題を解決するための手段】本発明は、汚泥原水を圧
送する汚泥原水圧送管と、該汚泥原水圧送管に斜行し接
線方向から合流して薬液を注入する薬液注入管と該薬液
注入管に斜行し接線方向から合流してエアを添加するエ
ア添加管と、前記汚泥原水圧送管に連続する撹拌管と、
該撹拌管に連続する分離管とからなっている。
The present invention is directed to a sludge raw water pressure feed pipe for feeding sludge raw water, a chemical liquid injection pipe for obliquely joining the sludge raw water pressure feed pipe, and joining the sludge raw water with a tangential direction to inject a chemical liquid, and the chemical liquid injection. An air addition pipe that obliquely joins the pipe and joins from the tangential direction to add air, and a stirring pipe that is continuous with the sludge raw water pressure feed pipe,
It consists of a separation tube continuous to the stirring tube.

【0006】上記攪拌管は、撹拌能力を高めるために、
管長を長くし、又は、途中に曲り部を設けるのが好まし
い。
The agitating tube has the following features to enhance the agitating ability.
It is preferable to lengthen the pipe or provide a bent portion in the middle.

【0007】また、分離管は、分離能力を高めるため
に、管径を太く、例えば撹拌管径の2.5倍程度に形成
するのが好ましい。
Further, in order to enhance the separating ability, it is preferable that the separation tube has a large diameter, for example, about 2.5 times the diameter of the stirring tube.

【0008】[0008]

【作用】上記のように構成された汚泥処理装置において
は、エアを添加することにより、撹拌管内の汚泥及び薬
液の混合物が撹拌管壁に引っかかることがなく、撹拌能
力が向上される。したがって、薬液添加、撹拌及び分離
が単一の管路内で連続して行われ、大流量の処理が可能
になる。
In the sludge treatment apparatus configured as described above, by adding air, the mixture of sludge and the chemical solution in the stirring pipe is not caught on the wall of the stirring pipe, and the stirring ability is improved. Therefore, chemical addition, stirring, and separation are continuously performed in a single conduit, and a large flow rate can be processed.

【0009】[0009]

【実施例】以下図面を参照して本発明の実施例を説明す
る。図1において、汚泥Aを圧送する汚泥圧送管1の中
程には、薬液すなわち高分子凝集剤溶液Bを注入する高
分子凝集剤溶液注入管2が下流側に斜行し接線方向から
合流されている。その注入管2の上流側には、ボールバ
ルブ3が設けられ、下流側には、エアCを添加するボー
ルバルブ5を備えたエア添加管4が下流側に斜行し接線
方向から合流されている。そして、圧送管1の注入管2
の下流側には、長さL1の添加部Xが形成されている。
Embodiments of the present invention will be described below with reference to the drawings. In FIG. 1, in the middle of the sludge pumping pipe 1 for pumping the sludge A, a polymer flocculant solution injection pipe 2 for injecting a chemical solution, that is, a polymer flocculant solution B, obliquely joins to the downstream side and joins from a tangential direction. ing. A ball valve 3 is provided on the upstream side of the injection pipe 2, and an air addition pipe 4 equipped with a ball valve 5 for adding air C is provided on the downstream side obliquely to the downstream side and joined from the tangential direction. There is. And the injection pipe 2 of the pressure feed pipe 1
An addition portion X having a length L1 is formed on the downstream side of the.

【0010】前記圧送管1の下流側には、圧送管1と同
径の撹拌管6が接続され、その撹拌管6の下流側には、
分離管7が接続されている。この分離管7の小径部7a
は、撹拌管6と同径に形成され、その小径部7aには、
拡径部7bを介し撹拌管6より大径(例えば2.5倍)
の大径部7cが接続されている。そして、撹拌管6と分
離管7の小径部7a及び拡径部7bにより長さL2の撹
拌部Yが形成され、大径部7cにより長さL3の分離部
Zが形成されている。
A stirring pipe 6 having the same diameter as that of the pressure feeding pipe 1 is connected to the downstream side of the pressure feeding pipe 1, and the downstream side of the stirring pipe 6 is
The separation pipe 7 is connected. The small diameter portion 7a of the separation tube 7
Is formed to have the same diameter as the stirring tube 6, and the small diameter portion 7a thereof has
Larger diameter (eg, 2.5 times) than the stirring tube 6 via the expanded diameter portion 7b
The large-diameter portion 7c of is connected. The small diameter portion 7a and the large diameter portion 7b of the stirring pipe 6 and the separation pipe 7 form a stirring portion Y having a length L2, and the large diameter portion 7c forms a separation portion Z having a length L3.

【0011】次に、作用について説明する。Next, the operation will be described.

【0012】処理に際し、圧送管1から汚泥原水Aを圧
送すると共に、注入管2から高分子凝集剤溶液Bを注入
し、エア添加管4からエアCを添加する。すると、添加
部Xにおいて、汚泥原水Aに斜めに接線方向から流入し
た高分子凝集剤溶液BとエアCとが添加混合され、それ
らA、B及びCの混合物Dは、撹拌部Yに送られる。そ
の撹拌部Yにおいて、混合物Dは矢印方向aに旋回され
ると共に、添加されたエアCにより、撹拌管6の管壁に
引っかかることなく、汚泥原水Aは高分子凝集剤溶液B
により好適に凝集され、分離部Zに送られる。その分離
部Zにおいて、エアCは逃がされ、凝集物すなわちフロ
ックEと分離余剰水Fとに分離排出される。
During the treatment, the sludge raw water A is pressure-fed through the pressure feed pipe 1, the polymer coagulant solution B is injected through the injection pipe 2, and the air C is added through the air addition pipe 4. Then, in the addition section X, the polymer flocculant solution B and the air C, which obliquely flowed into the sludge raw water A from the tangential direction, are added and mixed, and the mixture D of A, B, and C is sent to the stirring section Y. . In the stirring section Y, the mixture D is swirled in the direction of the arrow a, and the added sludge C does not catch the sludge raw water A on the polymer coagulant solution B by the added air C.
Are preferably aggregated by and are sent to the separating section Z. In the separating section Z, the air C is released and separated into flocculates, that is, flocs E and separated surplus water F and discharged.

【0013】前記撹拌部Yの撹拌能力は、汚泥原水の圧
送ポンプの能力、撹拌管6の管径及び長さL2により決
まる。しかし、長さL2がスペースの関係から制約され
る場合は、撹拌管の途中に図2に示すような曲管8を介
装するのが好ましい。
The stirring capacity of the stirring section Y is determined by the capacity of the sludge raw water pressure pump, the diameter of the stirring tube 6 and the length L2. However, when the length L2 is restricted by the space, it is preferable to interpose a curved pipe 8 as shown in FIG. 2 in the middle of the stirring pipe.

【0014】[0014]

【発明の効果】本発明は、以上説明したように構成され
ているので、エアの添加により撹拌能力を高めラインミ
キシングにより連続的に大流量の汚泥を処理することが
できる。
EFFECTS OF THE INVENTION Since the present invention is constructed as described above, it is possible to continuously treat a large flow rate of sludge by line mixing by increasing the stirring ability by adding air.

【0015】また、添加エアにより混合物が撹拌管内で
引っかかることなく好適に撹拌されるので、ジェットグ
ラウト工法のスライムの他に、粉粒体同士の混合や流体
と粉粒体との混合などにも好適に実施することができ
る。
Further, since the mixture is appropriately stirred by the added air without being caught in the stirring tube, it can be used not only for the slime of the jet grout method, but also for the mixing of powdery particles or the mixing of fluid and powdery particles. It can be suitably implemented.

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

【図1】本発明の一実施例を示す側断面図。FIG. 1 is a side sectional view showing an embodiment of the present invention.

【図2】曲管の一例を示す側面図。FIG. 2 is a side view showing an example of a curved pipe.

【符号の説明】[Explanation of symbols]

A・・・汚泥原水 B・・・高分子凝集剤溶液 C・・・エア D・・・混合物 E・・・フロック F・・・分離余剰水 X・・・添加部 Y・・・撹拌部 Z・・・分離部 1・・・汚泥圧送管 2・・・高分子凝集剤溶液注入管 3、5・・・ボールバルブ 4・・・エア添加管 6・・・撹拌管 7・・・分離管 7a・・・小径部 7b・・・拡径部 7c・・・大径部 8・・・曲管 A ... Raw sludge water B ... Polymer flocculant solution C ... Air D ... Mixture E ... Floc F ... Separation surplus water X ... Addition part Y ... Stirring part Z・ ・ ・ Separator 1 ・ ・ ・ Sludge pumping tube 2 ・ ・ ・ Polymer flocculant solution injection tube 3, 5 ・ ・ ・ Ball valve 4 ・ ・ ・ Air addition tube 6 ・ ・ ・ Stirring tube 7 ・ ・ ・ Separation tube 7a ... small diameter part 7b ... expanded part 7c ... large diameter part 8 ... curved pipe

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 汚泥原水を圧送する汚泥原水圧送管と、
該汚泥原水圧送管に斜行し接線方向から合流して薬液を
注入する薬液注入管と該薬液注入管に斜行し接線方向か
ら合流してエアを添加するエア添加管と、前記汚泥原水
圧送管に連続する撹拌管と、該撹拌管に連続する分離管
とからなることを特徴とする汚泥処理装置。
1. A sludge raw water pressure feed pipe for feeding sludge raw water under pressure,
The sludge raw water pressure-feeding pipe obliquely joins from the tangential direction to inject the chemical liquid, the chemical liquid injection pipe diagonally joins the chemical liquid injection pipe and joins from the tangential direction to add air, and the sludge raw water pressure-feeding pipe A sludge treatment device comprising a stirring tube continuous with the tube and a separation tube continuous with the stirring tube.
JP00113194A 1994-01-11 1994-01-11 Sludge treatment equipment Expired - Fee Related JP3410533B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP00113194A JP3410533B2 (en) 1994-01-11 1994-01-11 Sludge treatment equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP00113194A JP3410533B2 (en) 1994-01-11 1994-01-11 Sludge treatment equipment

Publications (2)

Publication Number Publication Date
JPH07195100A true JPH07195100A (en) 1995-08-01
JP3410533B2 JP3410533B2 (en) 2003-05-26

Family

ID=11492897

Family Applications (1)

Application Number Title Priority Date Filing Date
JP00113194A Expired - Fee Related JP3410533B2 (en) 1994-01-11 1994-01-11 Sludge treatment equipment

Country Status (1)

Country Link
JP (1) JP3410533B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100436392B1 (en) * 2001-06-20 2004-06-16 주식회사 포스코건설 A supply apparatus for a coagulating agent of water treatment sludge
JP2006521195A (en) * 2003-03-06 2006-09-21 コンストラクション リサーチ アンド テクノロジー ゲーエムベーハー Method for dewatering slurry mixture from jet grout operation and aqueous suspension used therefor

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100436392B1 (en) * 2001-06-20 2004-06-16 주식회사 포스코건설 A supply apparatus for a coagulating agent of water treatment sludge
JP2006521195A (en) * 2003-03-06 2006-09-21 コンストラクション リサーチ アンド テクノロジー ゲーエムベーハー Method for dewatering slurry mixture from jet grout operation and aqueous suspension used therefor
JP4680178B2 (en) * 2003-03-06 2011-05-11 コンストラクション リサーチ アンド テクノロジー ゲーエムベーハー Method for dewatering slurry mixture from jet grout operation and aqueous suspension used therefor

Also Published As

Publication number Publication date
JP3410533B2 (en) 2003-05-26

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