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JP2008173571A - Muddy water treatment tank and muddy water treatment equipment - Google Patents

Muddy water treatment tank and muddy water treatment equipment Download PDF

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JP2008173571A
JP2008173571A JP2007009846A JP2007009846A JP2008173571A JP 2008173571 A JP2008173571 A JP 2008173571A JP 2007009846 A JP2007009846 A JP 2007009846A JP 2007009846 A JP2007009846 A JP 2007009846A JP 2008173571 A JP2008173571 A JP 2008173571A
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water
bubble
tank
floating
suspended
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Takashi Nomoto
岳志 野本
Satoru Kimura
哲 木村
Tsutomu Nakayama
努 中山
Haruhisa Nakada
晴久 中田
Toru Hirano
亨 平野
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Nishimatsu Construction Co Ltd
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Abstract

【課題】支保用の吹付けコンクリートなどによるセメント微粒子を浮遊物質として含む濁水を浄化する際に、セメント微粒子の固化により弊害を防止する。
【解決手段】浮遊物質としてセメント微粒子を含む濁水を貯留する貯水槽12と、貯水槽12内に配置されたバブル発生装置14と、貯水槽12内のバブル発生装置14の上方に配置されて、バブル発生装置14から発生したバブルおよび浮遊物質を通過させる複数の貫通穴17を有する浮遊物質造粒促進板16と、浮遊物質造粒促進板16の各貫通穴17の下方に配置された凝集浮遊物質を蓄積するための回収容器18を備える。貯水槽12に導入された濁水W中の浮遊物質SSは、貫通穴17を通って沈降し、バブル発生装置14からのバブルBが貫通穴17を通過する際に浮遊物質SSがバブルBに捕捉され、これを繰り返す間に凝集浮遊物質Cとなって回収容器18内に蓄積される。
【選択図】図1
An object of the present invention is to prevent adverse effects by solidifying cement fine particles when purifying turbid water containing cement fine particles as floating substances by supporting shotcrete or the like.
A water storage tank 12 for storing turbid water containing cement fine particles as a suspended substance, a bubble generator 14 disposed in the water tank 12, and a bubble generator 14 in the water tank 12 are disposed above the water tank 12. The floating material granulation promoting plate 16 having a plurality of through holes 17 through which bubbles and floating substances generated from the bubble generating device 14 pass, and the aggregated floating placed below each through hole 17 of the floating material granulation promoting plate 16 A collection container 18 for accumulating substances is provided. The suspended matter SS in the turbid water W introduced into the water storage tank 12 settles through the through hole 17, and the suspended matter SS is captured by the bubble B when the bubble B from the bubble generator 14 passes through the through hole 17. While this is repeated, the aggregated floating substance C is accumulated in the collection container 18.
[Selection] Figure 1

Description

本発明は、トンネル掘削工事等において発生した処理濁水中に含まれるセメント微粒子を分離除去するための濁水処理槽およびこれを利用した濁水処理装置に関する。   The present invention relates to a muddy water treatment tank for separating and removing cement fine particles contained in treated muddy water generated in tunnel excavation work and the like, and a muddy water treatment apparatus using the muddy water treatment tank.

トンネル掘削工事においては、湧水が発生しやすく、この湧水に工事により発生した土砂が混じって濁水となる。この濁水は、工事の妨げとなるので排出されなければならず、そのまま排出したのでは河川等を汚染することになるので、濁水処理装置により排出に適した水質に処理してから河川等に放流される。図6はこのような濁水処理装置の一例を示している。図6において、原水槽1には、トンネル工事により発生した濁水が、後工程における連続処理が可能なように一定量貯留される。原水槽1に貯留された濁水は、中和槽2へ送られ、中和槽2において炭酸ガスの供給を受けて中和される。中和された濁水は、凝集反応槽3に送られ、ここでポリ塩化アルミニウムおよび高分子凝集剤の注入を受けて、濁水中のスラリーが凝集される。凝集されたスラリーを含む濁水は、続いてシックナー4に送られ、ここで上層の上水と下層の凝集されたスラリーとに分離される。上層の上水はシックナー4からオーバフローして処理水槽5には入り、ここで一旦貯留された後、河川等に放流される。シックナー4の下層に沈殿したスラリーを含む濁水は、スラリー槽6に一旦貯留された後、フィルタープレス7に送られる。フィルタープレス7では、凝集されたスラリーが圧縮ろ過されて脱水ケーキとなり、所定の場所に排出されるとともに、そのとき搾り出されたろ液が原水槽1に戻される。   In tunnel excavation work, spring water is likely to be generated, and this spring water is mixed with earth and sand generated by the work to become muddy water. This turbid water must be discharged because it interferes with the construction work. If it is discharged as it is, it will contaminate rivers, etc., and it will be discharged into rivers after being treated with muddy water treatment equipment to a quality suitable for discharge. Is done. FIG. 6 shows an example of such a muddy water treatment apparatus. In FIG. 6, a certain amount of muddy water generated by tunnel construction is stored in the raw water tank 1 so that it can be continuously processed in a subsequent process. The muddy water stored in the raw water tank 1 is sent to the neutralization tank 2 where it is neutralized by receiving the supply of carbon dioxide gas. The neutralized turbid water is sent to the agglomeration reaction tank 3, where the polyaluminum chloride and the polymer flocculant are injected, and the slurry in the turbid water is agglomerated. The turbid water containing the agglomerated slurry is then sent to the thickener 4 where it is separated into upper layer top water and lower layer agglomerated slurry. The upper water from the upper layer overflows from the thickener 4 and enters the treated water tank 5, where it is temporarily stored and then discharged into a river or the like. The muddy water containing the slurry precipitated in the lower layer of the thickener 4 is temporarily stored in the slurry tank 6 and then sent to the filter press 7. In the filter press 7, the agglomerated slurry is compressed and filtered to form a dehydrated cake, which is discharged to a predetermined location, and the filtrate squeezed at that time is returned to the raw water tank 1.

一方、濁水処理の基本技術として、バブル(気泡)を利用して濁水中の浮遊物質(Suspended Solid:SS、懸濁物質ともいう。)を除去し浄化する装置が知られている(例えば、特許文献1参照)。これは、水質活性浄化剤を池等の水域の汚濁物質を含む原水中に注入して混合攪拌することにより、主として水中に懸濁し溶解している有機物や栄養塩類を凝集物化して、その中に微細気泡を噴射して微細気泡によりその凝集物を水面上に浮上分離させることにより、水中から汚濁物質を分離除去させるものである。また、水質活性浄化剤を使用せずに、処理槽に貯留した汚水を電解装置により電気分解することにより、汚水に含まれる有機物等の汚れ成分を分離するとともに、その汚水中に微細気泡を発生させて汚れ成分を浮上分離させる装置も知られている(例えば、特許文献2参照)。
特開2003−117562号公報 特開2006−136767号公報
On the other hand, as a basic technique for turbid water treatment, there is known an apparatus for removing and purifying suspended solids (SS, also called suspended solids) using turbid water (for example, patents). Reference 1). This is because water quality active purifiers are injected into raw water containing pollutants in water bodies such as ponds and mixed and stirred to agglomerate organic substances and nutrient salts that are suspended and dissolved mainly in water. Then, fine bubbles are jetted and the aggregates are floated and separated on the water surface by the fine bubbles to separate and remove the pollutant from the water. In addition, electrolyzing the sewage stored in the treatment tank using an electrolysis device without using a water quality purification agent separates the soil components such as organic matter contained in the sewage and generates fine bubbles in the sewage. An apparatus is also known that floats and separates dirt components (see, for example, Patent Document 2).
JP 2003-117562 A JP 2006-136767 A

上記従来の汚水処理装置においては、有機物等の汚濁物質を主に分離除去の対象としているが、トンネル工事等における濁水中には有機物以外の汚濁物質が含まれている。例えば、トンネル工事において支保部材として使用される吹付けコンクリートや補助工法におけるセメント系注入材、アジテーター車の洗い水等により発生するセメント微粒子である。このようなセメント微粒子が濁水中に含まれると、上記のような濁水処理装置においては、セメント微粒子がシックナー下部やシックナーからスラリー槽への配管内において固まり、装置の濁水処理が不能になることがある。このため、清掃およびメンテナンスのため、濁水処理装置の運転を停止させなければならないことがあり、結果として工程の遅延につながる問題があった。また、バキューム清掃やハツリ清掃が必要となり、その労力が必要となり、清掃費用もかかることになる。さらに、フィルタープレスのろ布が目詰まりを起こし、濁水処理が不能となることがあり、このため、ろ布の交換頻度が多くなり、コスト高につながっていた。さらに、強アルカリのセメント粒子が濁水内に混入することによって、中和槽における中和処理のための薬剤(炭酸ガス、塩酸または硫酸)の量が多くなり、コスト高になるという問題があった。   In the above-described conventional sewage treatment apparatus, pollutants such as organic substances are mainly targeted for separation and removal, but turbid water in tunnel construction and the like contains pollutants other than organic substances. For example, sprayed concrete used as a supporting member in tunnel construction, cement-based injection material in the auxiliary method, cement fine particles generated by washing water of an agitator car, and the like. When such cement fine particles are contained in muddy water, in the muddy water treatment apparatus as described above, the cement fine particles may be solidified in the lower part of the thickener or in the pipe from the thickener to the slurry tank, and the muddy water treatment of the apparatus may become impossible. is there. For this reason, the operation of the muddy water treatment apparatus may have to be stopped for cleaning and maintenance, resulting in a problem that leads to a delay in the process. In addition, vacuum cleaning and chip cleaning are required, which requires labor and cleaning costs. In addition, the filter cloth of the filter press may be clogged, making it impossible to treat muddy water, which increases the frequency of replacement of the filter cloth, leading to high costs. Furthermore, there is a problem that the amount of chemicals (carbon dioxide, hydrochloric acid or sulfuric acid) for neutralization treatment in the neutralization tank increases due to the mixing of strong alkali cement particles in the turbid water, which increases the cost. .

本発明は、このような従来の課題を解決するためになされたもので、処理濁水中に含まれるセメント微粒子を容易かつ効率的に分離除去することのできる濁水処理槽および濁水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 such a conventional problem, and provides a turbid water treatment tank and a turbid water treatment apparatus capable of separating and removing cement fine particles contained in treated muddy water easily and efficiently. For the purpose.

本発明の濁水処理槽は、浮遊物質としてセメント微粒子を含む濁水を貯留する貯水槽と、前記貯水槽内に配置されたバブル発生装置と、前記貯水槽内の前記バブル発生装置の上方に配置されて、前記バブル発生装置から発生したバブルおよび前記浮遊物質を通過させる複数の貫通穴を有する浮遊物質造粒促進板とを備えたことを特徴とする。   The turbid water treatment tank of the present invention is disposed above a water storage tank for storing turbid water containing cement fine particles as a suspended substance, a bubble generating device disposed in the water storage tank, and the bubble generating device in the water storage tank. And a floating material granulation promoting plate having a plurality of through holes through which the bubble generated from the bubble generating device and the floating material pass.

貯水槽内に上部から浮遊物質としてセメント微粒子を含む濁水を導入すると、濁水は浮遊物質造粒促進板の貫通穴を通って流下し貯水槽内を満たす。そこで、貯水槽内下部に配置されたバブル発生装置によりバブルを発生させると、バブルは浮遊物質造粒促進板の貫通穴を通過して上昇し、その際にセメント微粒子を含む浮遊物質を捕捉しながら上昇する。浮遊物質造粒促進板の上部に浮上した浮遊物質は、貯水槽内に導入された濁水とともに再び浮遊物質造粒促進板の貫通穴を沈降し、またバブルに捕捉されながら浮遊物質造粒促進板の貫通穴を浮上する。この浮上沈降作用を繰り返す間に、セメント微粒子は水和反応により固化する性質があるため次第に結合して造粒化し、自重による自然沈降力がバブルの浮上力を上回った時点で浮遊物質造粒促進板の貫通穴を降下し、貯水槽内に堆積する。したがって、一定期間経過後に貯水槽内の堆積した凝集浮遊物質を回収することにより、濁水中のセメント微粒子を容易かつ効率的に分離除去することができる。   When turbid water containing cement fine particles as floating substance is introduced into the reservoir from above, the turbid water flows down through the through hole of the suspended substance granulation promoting plate and fills the reservoir. Therefore, when a bubble is generated by a bubble generator arranged in the lower part of the water tank, the bubble rises through the through hole of the floating material granulation promoting plate, and traps the floating material containing cement fine particles. While rising. The suspended matter floating on the floating material granulation promotion plate settles again in the through-hole of the suspended matter granulation promotion plate together with the muddy water introduced into the water tank, and is also trapped in the bubble and suspended matter granulation promotion plate Levitate the through hole. During repeated levitation and sedimentation, cement fine particles solidify due to hydration reaction, so they are gradually combined and granulated, and granulation of suspended matter is promoted when the natural sedimentation force due to its own weight exceeds the levitation force of the bubble. It drops through the plate's through hole and accumulates in the water tank. Therefore, by collecting the aggregated suspended solids accumulated in the water storage tank after a certain period of time, the cement fine particles in the muddy water can be separated and removed easily and efficiently.

また、本発明の濁水処理槽は、前記浮遊物質造粒促進板の各貫通穴の下方に、前記バブルと前記浮遊物質とが結合して造粒化した凝集浮遊物質を蓄積するための回収容器を備えたことを特徴とする。造粒化した凝集浮遊物質は、貯水槽にバキューム等の回収装置が備えられている場合には、その回収装置により貯水槽から回収することができるが、そのような回収装置がない場合には、浮遊物質造粒促進板の各貫通穴の下方に回収容器を配置することにより、回収容器内に蓄積した凝集浮遊物質を回収容器から回収することができる。   Further, the turbid water treatment tank of the present invention is a collection container for accumulating the aggregated floating substance that is granulated by combining the bubble and the floating substance below each through hole of the floating substance granulation promoting plate. It is provided with. The granulated agglomerated suspended solids can be recovered from the storage tank by the recovery device if the storage tank is equipped with a recovery device such as vacuum, but if there is no such recovery device By arranging the recovery container below each through hole of the floating substance granulation promoting plate, the aggregated floating substance accumulated in the recovery container can be recovered from the recovery container.

また、本発明の濁水処理槽は、前記回収容器が、前記浮遊物質造粒促進板の各貫通穴の下方に対向する位置に設けられたガイドパイプと、前記ガイドパイプを支持する容器本体とからなることを特徴とする。浮遊物質造粒促進板の各貫通穴を下降した凝集浮遊物質は、ガイドパイプに導かれて容器本体内に蓄積され、凝集浮遊物質をとともに流下した濁水は、容器本体から溢れて出てゆくため、容器本体内に凝集浮遊物質のみを容易かつ効率的に蓄積することができる。   Moreover, the muddy water treatment tank of the present invention includes a guide pipe provided at a position where the collection container faces below each through hole of the floating substance granulation promoting plate, and a container main body that supports the guide pipe. It is characterized by becoming. Agglomerated suspended matter descending through each through hole of the suspended matter granulation promoting plate is guided to the guide pipe and accumulated in the container body, and the turbid water that flows down together with the aggregated suspended matter overflows from the container body. Only the aggregated suspended solids can be easily and efficiently stored in the container body.

また、本発明の濁水処理槽は、前記浮遊物質造粒促進板および前記回収容器が前記貯水槽に着脱可能に取り付けられていることを特徴とする。浮遊物質造粒促進板および回収容器を貯水槽に着脱可能に取り付けることにより、凝集浮遊物質の回収の際には、浮遊物質造粒促進板および回収容器を貯水槽から取り外すことにより、凝集浮遊物質の回収を容易に行うことができる。   The muddy water treatment tank of the present invention is characterized in that the floating substance granulation promoting plate and the recovery container are detachably attached to the water storage tank. By attaching the floating material granulation promoting plate and the recovery container to the water tank so that they can be attached and detached, the aggregated floating material can be removed by removing the floating material granulation promoting plate and the recovery container from the water tank when collecting the aggregated floating material. Can be easily recovered.

また、本発明の濁水処理槽の別の実施態様では、浮遊物質としてセメント微粒子を含む濁水を貯留する貯水槽と、前記貯水槽内に配置されたバブル発生装置と、前記貯水槽内の前記バブル発生装置の上方に配置されて、上下方向に貫通する複数の差し込み穴を有する浮遊物質造粒促進板と、前記浮遊物質造粒促進板の各差し込み穴に着脱可能に差し込まれて、前記バブル発生装置から発生したバブルおよび前記浮遊物質を通過させる貫通穴を有する複数のプラグ部材と、前記プラグ部材と同径以下でその下方に前記プラグ部材との間に空間を設けて連結され、前記バブルと前記浮遊物質とが前記プラグ部材の貫通穴を通る間に結合して造粒化した凝集浮遊物質を蓄積するための回収容器とを備えたことを特徴とする。この構成により、回収容器と連結されたプラグ部材を浮遊物質造粒促進板から取り外すことにより、浮遊物質造粒促進板を貯水槽に固定した状態で回収容器を取り出すことができ、回収容器内部に蓄積された凝集浮遊物質を容易に回収することができる。   In another embodiment of the turbid water treatment tank of the present invention, a water storage tank for storing turbid water containing cement fine particles as a suspended substance, a bubble generator disposed in the water storage tank, and the bubble in the water storage tank The floating material granulation promotion plate disposed above the generator and having a plurality of insertion holes penetrating in the vertical direction, and the bubble generation is detachably inserted into each insertion hole of the floating material granulation promotion plate A plurality of plug members having a bubble generated from the apparatus and a through-hole through which the floating substance passes, and a space between the plug member and a diameter equal to or less than the plug member and below the plug member; And a collection container for accumulating the aggregated floating substance that is granulated by combining with the floating substance while passing through the through hole of the plug member. With this configuration, by removing the plug member connected to the collection container from the suspended material granulation promotion plate, the collection container can be taken out with the suspended material granulation promotion plate fixed to the water storage tank. Accumulated aggregated suspended solids can be easily recovered.

また、本発明の濁水処理装置は、上記した濁水処理槽を原水槽として備え、前記原水槽からの濁水を処理して浄化するための複数のプロセスを有する。より詳しくは、この濁水処理装置は、浮遊物質としてセメント微粒子を含む濁水を一定量貯留してセメント微粒子を凝集除去する原水槽と、原水槽から送られた濁水を中和する中和ユニットと、中和された濁水にポリ塩化アルミニウムおよび高分子凝集剤を供給して濁水中のスラリーを凝集させる凝集反応槽と、濁水中の凝集されたスラリーを沈降させてスラリーと上水とを分離するシックナーと、分離された上水を貯留して放流する放流処理水槽と、沈降したスラリーを含む濁水を貯留するスラリー槽と、スラリー槽に貯留された濁水を圧縮ろ過して脱水ケーキとろ液に分離するフィルタープレスとを備えている。   Moreover, the muddy water processing apparatus of this invention is equipped with the above-mentioned muddy water processing tank as a raw water tank, and has a several process for processing and purifying muddy water from the said raw water tank. More specifically, the turbid water treatment apparatus includes a raw water tank that stores a certain amount of turbid water containing cement fine particles as a suspended substance and aggregates and removes the cement fine particles, a neutralization unit that neutralizes turbid water sent from the raw water tank, An agglomeration reaction vessel for agglomerating slurry in muddy water by supplying polyaluminum chloride and a polymer flocculant to neutralized muddy water, and a thickener for separating the slurry and clean water by settling the agglomerated slurry in muddy water And a release treatment water tank that stores and discharges the separated water, a slurry tank that stores muddy water containing the settled slurry, and compresses and filters the muddy water stored in the slurry tank into a dehydrated cake and a filtrate. It has a filter press.

本発明の濁水処理槽は、浮遊物質としてセメント微粒子を含む濁水を貯留する貯水槽と、貯水槽内に配置されたバブル発生装置と、貯水槽内のバブル発生装置の上方に配置されて、バブル発生装置から発生したバブルおよび浮遊物質を通過させる小径の複数の貫通穴を有する浮遊物質造粒促進板とを備えているので、貯水槽内に導入された濁水が、浮遊物質造粒促進板の貫通穴を通って流下し、またバブル発生装置により発生したバブルにより浮遊物質が浮遊物質造粒促進板の貫通穴を通過して浮上沈降作用を繰り返す間に、セメント微粒子が結合して造粒化し、自重により下降して貯水槽内に堆積するので、濁水中のセメント微粒子を容易かつ効率的に捕捉除去することができる。   The turbid water treatment tank of the present invention includes a water tank for storing turbid water containing cement fine particles as a suspended substance, a bubble generator disposed in the water tank, and a bubble generator disposed in the water tank. The suspended matter granulation promoting plate having a plurality of small-diameter through holes that allow bubbles and suspended matter to pass through from the generator, so that the turbid water introduced into the water storage tank The cement fine particles are combined and granulated while flowing down through the through-holes, and the suspended matter passes through the through-holes of the suspended solids granulation promotion plate and repeats the rising and sinking action due to the bubbles generated by the bubble generator. Since it descends by its own weight and accumulates in the water storage tank, the cement fine particles in the muddy water can be easily and efficiently captured and removed.

また、この濁水処理槽を濁水処理装置の原水槽として利用することにより、原水槽下流において、セメント微粒子がシックナー下部やシックナーからスラリー槽への配管内において固まり、装置の濁水処理が不能になる問題を回避することができ、バキューム清掃やハツリ清掃が不要となり、その労力と清掃費用を削減することができる。さらに、フィルタープレスのろ布が目詰まりを起こし、濁水処理が不能となることを回避することができ、さらに、強アルカリのセメント粒子が濁水内に混入することによる中和槽における中和処理のための多量の薬剤(炭酸ガス、塩酸または硫酸)が不要となる等の効果を有する。   In addition, by using this turbid water treatment tank as a raw water tank of the turbid water treatment apparatus, cement fine particles are solidified in the lower part of the thickener or in the pipe from the thickener to the slurry tank, and the turbid water treatment of the apparatus becomes impossible. Therefore, vacuum cleaning and chip cleaning are not required, and labor and cleaning costs can be reduced. Furthermore, it is possible to avoid clogging of the filter cloth of the filter press and impairing muddy water treatment, and further, neutralization treatment in the neutralization tank by mixing strong alkali cement particles in muddy water. For example, a large amount of chemicals (carbon dioxide, hydrochloric acid or sulfuric acid) is unnecessary.

(実施の形態1)
以下、本発明の実施の形態について、図面を用いて説明する。本発明における濁水処理装置の全体の構成は図6に示したものと同じであるので、以下には原水槽としての濁水処理槽に限って説明する。図1(a)は本実施の形態における濁水処理槽の概略断面図、図1(b)はその平面図である。図1において、濁水処理槽10は、浮遊物質SSとしてセメント微粒子を含む濁水Wを貯留する貯水槽12と、貯水槽12内の底部に配置されたバブル発生装置14と、貯水槽12内のバブル発生装置14の上方に配置されて、バブル発生装置14から発生したバブルBおよび浮遊物質SSを通過させる小径の複数の貫通穴17を有する浮遊物質造粒促進板16と、浮遊物質造粒促進板16の各貫通穴17の下方に、バブルBと浮遊物質SSとが結合して造粒化した凝集浮遊物質C(一部のみを図示)を蓄積するための回収容器18とを備えている。浮遊物質SSとしてセメント微粒子を含む濁水Wは、貯水槽12の上方から供給管20を通じて導入され、排水ポンプ22により排出管24を通じて排出される。
(Embodiment 1)
Hereinafter, embodiments of the present invention will be described with reference to the drawings. Since the whole structure of the turbid water treatment apparatus in the present invention is the same as that shown in FIG. 6, the following description will be limited to the turbid water treatment tank as the raw water tank. Fig.1 (a) is a schematic sectional drawing of the muddy water processing tank in this Embodiment, FIG.1 (b) is the top view. In FIG. 1, a muddy water treatment tank 10 includes a water storage tank 12 that stores muddy water W containing cement fine particles as a suspended substance SS, a bubble generator 14 that is disposed at the bottom of the water storage tank 12, and a bubble in the water storage tank 12. A floating material granulation promoting plate 16 which is disposed above the generating device 14 and has a plurality of small-diameter through holes 17 through which the bubbles B and the floating material SS generated from the bubble generating device 14 pass. Under each of the 16 through holes 17, a collection container 18 is provided for accumulating aggregated suspended matter C (only a part of which is shown in the figure) formed by combining bubbles B and suspended matter SS. The turbid water W containing cement fine particles as the suspended matter SS is introduced from above the water storage tank 12 through the supply pipe 20 and discharged through the discharge pipe 24 by the drain pump 22.

バブル発生装置14は、例えば加圧ポンプにより水を送り出し、空気を負圧により吸引して、直径がマイクロからミリオーダーのバブルを発生させるタイプのものであり、ここでは直径が数十ミクロン程度のマイクロバブル発生装置が使用されているが、発生させるバブルの直径は、濁水に含まれているセメント微粒子の粒径に応じて決定される。バブル発生装置は、濁水処理槽の稼動中は常時動作している。他のバブル発生装置としては、キャビテーション方式、旋回方式、加圧溶解方式、ベンチュリー方式などが使用可能である。   The bubble generating device 14 is of a type that generates water with a pressure of, for example, a water pump and sucks air with a negative pressure to generate a bubble with a diameter of micro to millimeter order. Here, the diameter is about several tens of microns. Although the microbubble generator is used, the diameter of the bubble to be generated is determined according to the particle size of the cement fine particles contained in the muddy water. The bubble generator is always operating during operation of the muddy water treatment tank. As other bubble generating devices, a cavitation method, a swiveling method, a pressure dissolution method, a venturi method, and the like can be used.

浮遊物質造粒促進板16は、厚さが15cm程度のポリプロピレンまたはアクリル樹脂製のもので、貯水槽12の左右の両壁面にそれぞれ設けられた2個ずつの支持片11に載せられて着脱可能になっている。また、図1(b)に示すように、貯水槽12の両側長辺側において、貯水槽12の壁面との間に間隔を設けてある。この間隔は、供給管20を通じて大量の濁水が供給された場合に、浮遊物質造粒促進板16が障害となって溢流するのを防ぐためである。貫通穴17は、バブルBおよび浮遊物質SSが通過しやすいように、上部および下部がR面取りされている。貫通穴17の直径は、数mmから数cm程度、ここでは直径が2cm程度の貫通穴17が、互いに20cm程度の間隔を設けて形成されている。浮遊物質造粒促進板16の材料としては、他には鋼やアルミニウム等の金属材料が使用可能であり、表面に塗装などの処理を施してもよい。   The floating substance granulation promotion plate 16 is made of polypropylene or acrylic resin having a thickness of about 15 cm, and is detachably mounted on the two support pieces 11 provided on both the left and right wall surfaces of the water storage tank 12, respectively. It has become. Moreover, as shown in FIG.1 (b), the space | interval is provided between the wall surfaces of the water storage tank 12 in the both-side long side side of the water storage tank 12. As shown in FIG. This interval is for preventing the floating material granulation promoting plate 16 from overflowing when a large amount of muddy water is supplied through the supply pipe 20. The through-hole 17 is chamfered at the top and bottom so that the bubble B and the suspended matter SS can easily pass through. The diameter of the through hole 17 is about several mm to several cm, and here, the through holes 17 having a diameter of about 2 cm are formed with an interval of about 20 cm therebetween. As a material for the floating substance granulation promoting plate 16, other metal materials such as steel and aluminum can be used, and the surface may be subjected to treatment such as painting.

回収容器18は、浮遊物質造粒促進板16の各貫通穴17の下方に対向する位置に設けられたガイドパイプ18aと、このガイドパイプ18aを支持する容器本体18bとからなり、図2に示すように、ガイドパイプ18aの外周面には、4枚の羽根18cが等分に設けられ、この4枚の羽根18cを容器本体18bの内周面に嵌め込むことにより、ガイドパイプ18aが容器本体18bの中間に浮いた状態で支持されている。回収容器18の各部の材料は、ポリプロピレンまたはアクリル樹脂製または鋼やアルミニウム等の金属材料が使用可能であり、表面に塗装などの処理を施してもよい。また、容器本体18b下部の等分4箇所には、ワイヤ支持片18dが形成され、そこに形成された取り付け穴18eに支持ワイヤ18fの一端が差し込まれ、支持ワイヤ18fの他端は、浮遊物質造粒促進板16の各貫通穴17の周辺4箇所に取り付けられたフック18gに係止されて、回収容器18の全体が宙吊り状態になっている。支持ワイヤ18fの長さは、ガイドパイプ18aの先端部と浮遊物質造粒促進板16の下部との間に数mm程度の間隔があくように設定されている。   The recovery container 18 includes a guide pipe 18a provided at a position facing the lower side of each through hole 17 of the suspended solid material granulation promoting plate 16, and a container body 18b that supports the guide pipe 18a, as shown in FIG. As described above, the four blades 18c are equally provided on the outer peripheral surface of the guide pipe 18a. By fitting the four blades 18c into the inner peripheral surface of the container body 18b, the guide pipe 18a is It is supported in a state of floating in the middle of 18b. The material of each part of the collection container 18 can be made of polypropylene or acrylic resin, or a metal material such as steel or aluminum, and the surface may be subjected to treatment such as painting. In addition, wire support pieces 18d are formed at four equal portions at the bottom of the container body 18b, and one end of the support wire 18f is inserted into the attachment hole 18e formed there, and the other end of the support wire 18f The entire collection container 18 is suspended in suspension by being hooked to hooks 18g attached to four locations around each through hole 17 of the granulation promoting plate 16. The length of the support wire 18f is set so that an interval of about several millimeters is provided between the distal end portion of the guide pipe 18a and the lower portion of the suspended material granulation promoting plate 16.

次に、図1および図3を参照して濁水処理槽10の作用について説明する。供給管20から貯水槽12に供給されたトンネル工事による濁水Wは、浮遊物質SSとして支保用の吹き付けコンクリート等のセメント粒子が混じっており、この浮遊物質SSのあるものが、浮遊物質造粒促進板16の貫通穴17を通って沈降する。一方、バブル発生装置14から発生したバブルBは上昇して、あるものは貫通穴17を通って浮遊物質造粒促進板16の上に浮上する。その際、沈降した浮遊物質SSのあるものはバブルBに捕捉されて、貫通穴17を通って浮遊物質造粒促進板16の上に浮遊し、再び貫通穴17を通って沈降する。浮遊物質SSには、水和反応により固化するセメント分が多く存在するため、この沈降、浮上を繰り返すうちに、浮遊物質SSが互いに結合されて造粒化する。そして、造粒化した浮遊物質SSの自重による自然沈降力がバブルBの浮上力を上回ると、凝集浮遊物質Cは濁水Wとともに貫通穴17から回収容器18のガイドパイプ18aを通って容器本体18b内に回収される。この際、ガイドパイプ18aは凝集浮遊物質Cを逃がさずに効率よく回収する役目を果たす。容器本体18b内に流入した濁水Wは、容器本体18bの上部から逸流し、凝集浮遊物質Cのみが容器本体18b内に堆積する。容器本体18b内に堆積された凝集浮遊物質Cは、所定期間経過後、装置を停止して、容器本体18bを浮遊物質造粒促進板16ごと貯水槽12から取り外し、支持ワイヤ18fを外して容器本体18b内部の凝集浮遊物質Cを取り除く。その後、支持ワイヤ18fにより容器本体18bを浮遊物質造粒促進板16に係止させて、浮遊物質造粒促進板16を貯水槽12の支持片11に載せて元の状態に戻し、運転を再開する。   Next, the effect | action of the muddy water processing tank 10 is demonstrated with reference to FIG. 1 and FIG. The muddy water W from the tunnel construction supplied from the supply pipe 20 to the storage tank 12 is mixed with cement particles such as sprayed concrete for support as suspended matter SS, and the suspended matter SS is used to promote granulation of suspended matter. It sinks through the through hole 17 of the plate 16. On the other hand, the bubbles B generated from the bubble generator 14 rise, and some of them rise through the through holes 17 and above the suspended material granulation promoting plate 16. At this time, some of the suspended matter SS that has settled is captured by the bubble B, floats on the suspended matter granulation promoting plate 16 through the through hole 17, and settles again through the through hole 17. Since the suspended matter SS has a large amount of cement that is solidified by the hydration reaction, the suspended matter SS is bonded to each other and granulated while repeating the sedimentation and floating. When the natural sedimentation force due to the dead weight of the granulated suspended matter SS exceeds the lifting force of the bubble B, the aggregated suspended matter C and the muddy water W pass through the guide hole 18a of the recovery container 18 from the through hole 17 and the container body 18b. Collected in. At this time, the guide pipe 18a serves to efficiently collect the aggregated suspended matter C without escaping. The turbid water W that has flowed into the container main body 18b escapes from the upper part of the container main body 18b, and only the aggregated suspended solid C is deposited in the container main body 18b. The aggregated floating substance C deposited in the container body 18b is stopped after a predetermined period of time, the apparatus is stopped, the container body 18b is removed from the water storage tank 12 together with the floating substance granulation promoting plate 16, the support wire 18f is removed, and the container is removed. The aggregated suspended matter C inside the main body 18b is removed. Thereafter, the container body 18b is locked to the suspended material granulation promoting plate 16 by the support wire 18f, and the suspended material granulation promoting plate 16 is placed on the support piece 11 of the water storage tank 12 to return to the original state, and the operation is resumed. To do.

本実施の形態における浮遊物質SSの粒径は0.075mm以下なので、土粒子密度2.65g/cm3、水温10℃とした場合、浮遊物質SSの沈降速度は13.9m/h(約23cm/min)となる。実際の沈降では、相互干渉、乱流や偏流の発生等により沈降速度は減少するので、上記の数値は大体の目安である。また、バブル発生装置14から発生したバブルBの浮上は、バブルBの粒径が0.01mmの場合、その上昇速度は3cm/minになり、粒径1mmのバブルの場合の上昇速度は500〜600cm/minになる。したがって、1つのバルブBに1つの浮遊物質SSが捕捉されて造粒化されると考えると、造粒化された浮遊物質SSがその沈降速度に打ち勝って浮上するには、バブルBの粒径が数百μm程度必要と考えられる。そして最終的に、造粒化した凝集浮遊物質Cの沈降力がバブルBの浮上力を上回ったところで、容器本体18b内に回収される。 Since the particle size of the suspended matter SS in the present embodiment is 0.075 mm or less, when the soil particle density is 2.65 g / cm 3 and the water temperature is 10 ° C., the sedimentation rate of the suspended matter SS is 13.9 m / h (about 23 cm). / Min). In actual sedimentation, the sedimentation speed decreases due to mutual interference, the occurrence of turbulence and drift, etc., so the above figures are approximate. The rising of the bubble B generated from the bubble generator 14 is 3 cm / min when the bubble B has a particle diameter of 0.01 mm, and the rising speed in the case of a bubble with a particle diameter of 1 mm is 500 to 600 cm / min. Accordingly, when one floating substance SS is captured and granulated by one valve B, the particle size of the bubble B is necessary for the granulated floating substance SS to overcome its settling velocity and rise. However, it is considered that about several hundred μm is necessary. Finally, when the settling force of the granulated aggregated floating substance C exceeds the floating force of the bubble B, it is recovered in the container body 18b.

なお、浮遊物質造粒促進板16は、全体的に均一の厚さにすると厚さが厚い場合には重量がかさむので、図3aに示すように、ポリプロピレンまたはアクリル等の樹脂により、貫通穴17の部分を除いた残りの部分が中空になるように一体に成形してもよい。または、上下方向に2分割して、互いに向き合わせて接合するようにしてもよい。肉厚tは数ミリから数センチが好ましく、全体の厚さTは15cm程度、貫通穴17の直径は数ミリから数センチ程度が好ましい。   In addition, since the suspended-material granulation promoting plate 16 is heavy when the thickness is large as a whole, the through-hole 17 is made of a resin such as polypropylene or acrylic as shown in FIG. 3a. The remaining part except for the part may be formed integrally so as to be hollow. Alternatively, it may be divided into two in the vertical direction so as to face each other and join. The wall thickness t is preferably several millimeters to several centimeters, the overall thickness T is preferably about 15 cm, and the diameter of the through hole 17 is preferably about several millimeters to several centimeters.

(実施の形態2)
次に、本発明の実施の形態2について説明する。本実施の形態2は、全体の構成は、図1に示すように貯水槽12とその内部底部に設置されたバブル発生装置14を備えており、実施の形態1と異なるのは、浮遊物質造粒促進板16および回収容器18の構造なので、その点についてのみ図4および図5を用いて説明する。図4において、浮遊物質造粒促進板26には、上下方向に貫通するストレートな差し込み穴27が所定の間隔を置いて複数個形成されている。この差し込み穴27には、ポリプロピレンまたはアクリル製のプラグ(プラグ部材)28が着脱可能に差し込まれている。プラグ28は、図5に示すように、上部の鍔部28aと下部の胴部28bとからなり、軸方向中央部には実施の形態1の貫通穴17と同様な貫通穴28cが形成されている。さらに、鍔部28aの対向する外周2箇所には取っ手28dが形成され、胴部28b外周の等分4箇所には、軸方向に平行に係止溝28eが形成されている。取っ手28dは任意の形状、構造のものでよく、さもなければ鍔部28aを厚くするだけでもよい。このプラグ28の下部には、回収容器29が着脱可能に取り付けられる。回収容器29は、ポリプロピレンまたはアクリル製で、プラグ28の胴部28bと同径またはそれ以下の直径を有する容器本体29aと、この容器本体29aの上端部の等分4箇所から上方に向けて形成された係止片29bとからなる。この係止片29bは、プラグ28の係止溝28eに着脱可能に係合するもので、係止溝28eの部分における内径よりも係止片29bにおける内径が少し小さく設定されて、係止片29bが有する弾性により係止溝28eに弾性的に係止されるようになっている。
(Embodiment 2)
Next, a second embodiment of the present invention will be described. As shown in FIG. 1, the overall configuration of the second embodiment is provided with a water storage tank 12 and a bubble generator 14 installed at the inner bottom thereof. Since it is the structure of the grain promotion board 16 and the collection | recovery container 18, only that point is demonstrated using FIG. 4 and FIG. In FIG. 4, a plurality of straight insertion holes 27 penetrating in the vertical direction are formed in the suspended material granulation promoting plate 26 at predetermined intervals. A plug (plug member) 28 made of polypropylene or acrylic is detachably inserted into the insertion hole 27. As shown in FIG. 5, the plug 28 includes an upper flange portion 28 a and a lower trunk portion 28 b, and a through hole 28 c similar to the through hole 17 of the first embodiment is formed in the central portion in the axial direction. Yes. Furthermore, a handle 28d is formed at two opposing outer peripheral portions of the flange portion 28a, and locking grooves 28e are formed at four equally divided outer peripheral portions of the trunk portion 28b in parallel to the axial direction. The handle 28d may have an arbitrary shape and structure, or the hook portion 28a may be thickened. A collection container 29 is detachably attached to the lower portion of the plug 28. The collection container 29 is made of polypropylene or acrylic, and is formed from a container body 29a having the same diameter as or smaller than the body part 28b of the plug 28, and upward from four equally divided portions at the upper end of the container body 29a. And the latching piece 29b. The locking piece 29b is detachably engaged with the locking groove 28e of the plug 28. The inner diameter of the locking piece 29b is set to be slightly smaller than the inner diameter of the locking groove 28e. Due to the elasticity of 29b, it is elastically locked to the locking groove 28e.

本実施の形態2における浮遊物質造粒促進板および回収部は、以上のように構成されているので、プラグ28を浮遊物質造粒促進板26の差し込み穴27に差し込むことにより、実施の形態1と同様にして、プラグ28の貫通穴28cおよび回収容器29の係止片29bの間を通して、バブル発生装置24からのバブルBおよび濁水W中の浮遊物質SSを浮上、沈降させることができ、その間にバブルBにより浮遊物質SSを造粒化して、回収容器29内に凝集浮遊物質Cを堆積させることができる。そして、所定期間経過後、浮遊物質造粒促進板26の差し込み穴27からプラグ28を取っ手28dを持って回収容器29ごと取り外し、回収容器29内に蓄積した凝集浮遊物質Cを容易に取り除くことができる。   Since the floating substance granulation promoting plate and the recovery unit in the second embodiment are configured as described above, the plug 28 is inserted into the insertion hole 27 of the floating substance granulation promoting plate 26 to thereby implement the first embodiment. In the same manner, the suspended matter SS in the bubble B and the turbid water W from the bubble generating device 24 can be levitated and settled between the through hole 28c of the plug 28 and the locking piece 29b of the recovery container 29, In addition, the suspended solid SS can be granulated by the bubbles B, and the aggregated suspended solid C can be deposited in the recovery container 29. After a predetermined period, the plug 28 is removed from the insertion hole 27 of the suspended material granulation promoting plate 26 with the handle 28d together with the collection container 29, and the aggregated suspended matter C accumulated in the collection container 29 can be easily removed. it can.

なお、本実施の形態2において、プラグ28と回収容器29との連結を、回収容器29に一体に設けた係止片29bにより行っているが、実施の形態1と同様に、ワイヤを用いてその両端をそれぞれプラグ28と回収容器29とに連結してもよい。また、実施の形態1と同様に、回収容器29内にガイドパイプを羽根を介して設けるようにしてもよい。   In the second embodiment, the plug 28 and the recovery container 29 are connected by the locking piece 29b provided integrally with the recovery container 29. However, as in the first embodiment, a wire is used. Both ends thereof may be connected to the plug 28 and the collection container 29, respectively. Further, as in the first embodiment, a guide pipe may be provided in the collection container 29 via a blade.

また、本実施の形態2においても、浮遊物質造粒促進板26は、差し込み穴27の部分を除いた残りの部分が中空になるように成形してもよい。   Also in the second embodiment, the suspended-material granulation promoting plate 26 may be formed so that the remaining part excluding the insertion hole 27 is hollow.

また、上記実施の形態1および2では、回収容器18または29を使用して凝集浮遊物質Cを回収したが、このような回収容器を用いずに、貫通穴17または28cから沈降した凝集浮遊物質Cを貯水槽12の底部に直接堆積させるようにしてもよい。この場合には、貯水槽12底部に堆積した凝集浮遊物質Cを人力により、またはバキューム装置などの機械を使用して除去することになる。   In the first and second embodiments, the aggregated floating substance C is recovered using the recovery container 18 or 29. However, the aggregated floating substance settled from the through hole 17 or 28c without using such a recovery container. C may be deposited directly on the bottom of the water tank 12. In this case, the aggregated suspended matter C deposited on the bottom of the water storage tank 12 is removed manually or using a machine such as a vacuum device.

以上のように、本発明に係る濁水処理槽および濁水処理装置は、浮遊物質としてセメント微粒子を含む濁水からセメント微粒子を容易かつ効率的に捕捉除去することができ、トンネル掘削工事用の他にも、セメントを使用するダム建設工事、構造物基礎工事用等にも適用することができる。   As described above, the turbid water treatment tank and the turbid water treatment apparatus according to the present invention can easily and efficiently capture and remove cement fine particles from muddy water containing cement fine particles as floating substances. It can also be applied to dam construction work using cement, structural foundation work, etc.

本発明の実施の形態1における濁水処理槽の断面図(a)と平面図(b)である。It is sectional drawing (a) and top view (b) of the muddy water processing tank in Embodiment 1 of this invention. 実施の形態1における回収容器の斜視図である。4 is a perspective view of a collection container in Embodiment 1. FIG. 実施の形態1における動作説明図である。FIG. 3 is an operation explanatory diagram according to the first embodiment. 実施の形態1における浮遊物質造粒促進板の別の例を示す部分断面図である。6 is a partial cross-sectional view showing another example of the suspended solids granulation promoting plate in Embodiment 1. FIG. 実施の形態2における浮遊物質造粒促進板、プラグおよび回収容器の断面図である。FIG. 6 is a cross-sectional view of a suspended substance granulation promoting plate, a plug, and a collection container in a second embodiment. 実施の形態2におけるプラグおよび回収容器の分解斜視図である。10 is an exploded perspective view of a plug and a recovery container in Embodiment 2. FIG. 本発明が適用される濁水処理装置の概略構成を説明するブロック図である。It is a block diagram explaining the schematic structure of the muddy water processing apparatus to which this invention is applied.

符号の説明Explanation of symbols

B バブル
C 凝集浮遊物質
SS 浮遊物質
W 濁水
10 濁水処理槽(原水槽)
11 支持片
12 貯水槽
14 バブル発生装置
16 浮遊物質造粒促進板
18 回収容器
18a ガイドパイプ
18b 容器本体
18c 羽根
18d ワイヤ支持片
18e 取り付け穴
18f 支持ワイヤ
18g フック
20 供給管
22 排水ポンプ
24 排水管
26 浮遊物質造粒促進板
27 差し込み穴
28 プラグ(プラグ部材)
28a 鍔部
28b 胴部
28c 貫通穴
28d 取っ手
28e 係止溝
29 回収容器
29a 胴部
29b 係止片
B Bubble C Agglomerated suspended matter SS Suspended matter W Turbid water 10 Turbid water treatment tank (raw water tank)
DESCRIPTION OF SYMBOLS 11 Support piece 12 Water storage tank 14 Bubble generator 16 Floating substance granulation promotion board 18 Collection | recovery container 18a Guide pipe 18b Container main body 18c Blade | wing 18d Wire support piece 18e Mounting hole 18f Support wire 18g Hook 20 Supply pipe 22 Drain pump 24 Drain pipe 26 Floating material granulation promotion plate 27 Insert hole 28 Plug (plug member)
28a collar part 28b trunk part 28c through hole 28d handle 28e locking groove 29 collection container 29a trunk part 29b locking piece

Claims (6)

浮遊物質としてセメント微粒子を含む濁水を貯留する貯水槽と、前記貯水槽内に配置されたバブル発生装置と、前記貯水槽内の前記バブル発生装置の上方に配置されて、前記バブル発生装置から発生したバブルおよび前記浮遊物質を通過させる複数の貫通穴を有する浮遊物質造粒促進板とを備えたことを特徴とする濁水処理槽。   A water storage tank for storing turbid water containing cement fine particles as a suspended substance, a bubble generating device disposed in the water storage tank, and disposed above the bubble generating device in the water storage tank and generated from the bubble generating device A muddy water treatment tank comprising a suspended material granulation promoting plate having a plurality of through holes through which the bubble and the suspended material pass. 前記浮遊物質造粒促進板の各貫通穴の下方に、前記バブルと前記浮遊物質とが結合して造粒化した凝集浮遊物質を蓄積するための回収容器を備えたことを特徴とする請求項1に記載の濁水処理槽。   The recovery container for accumulating the aggregated suspended solids formed by combining the bubbles and the suspended solids below each through hole of the suspended matter granulation promoting plate. The muddy water treatment tank according to 1. 前記回収容器が、前記浮遊物質造粒促進板の各貫通穴の下方に対向する位置に設けられたガイドパイプと、前記ガイドパイプを支持する容器本体とからなることを特徴とする請求項2に記載の濁水処理槽。   The said collection | recovery container consists of a guide pipe provided in the position which opposes the lower part of each through-hole of the said floating substance granulation acceleration | stimulation board, and the container main body which supports the said guide pipe. The muddy water treatment tank of description. 前記浮遊物質造粒促進板および前記回収容器が前記貯水槽に着脱可能に取り付けられていることを特徴とする請求項2または請求項3に記載の濁水処理槽。   The muddy water treatment tank according to claim 2 or 3, wherein the floating substance granulation promotion plate and the recovery container are detachably attached to the water storage tank. 浮遊物質としてセメント微粒子を含む濁水を貯留する貯水槽と、前記貯水槽内に配置されたバブル発生装置と、前記貯水槽内の前記バブル発生装置の上方に配置されて、上下方向に貫通する複数の差し込み穴を有する浮遊物質造粒促進板と、前記浮遊物質造粒促進板の各差し込み穴に着脱可能に差し込まれて、前記バブル発生装置から発生したバブルおよび前記浮遊物質を通過させる貫通穴を有する複数のプラグ部材と、前記プラグ部材と同径以下でその下方に前記プラグ部材との間に空間を設けて連結され、前記バブルと前記浮遊物質とが前記プラグ部材の貫通穴を通る間に結合して造粒化した凝集浮遊物質を蓄積するための回収容器とを備えたことを特徴とする濁水処理槽。   A water storage tank for storing turbid water containing cement fine particles as a suspended substance, a bubble generating device disposed in the water storage tank, and a plurality of penetrating vertically disposed above the bubble generating device in the water storage tank A floating substance granulation promoting plate having insertion holes, and a through hole that is removably inserted into each insertion hole of the floating material granulation promoting plate to allow the bubble generated from the bubble generating device and the floating substance to pass therethrough. A plurality of plug members having a diameter equal to or smaller than that of the plug member, and a space is provided between the plug member and the plug member below the plug member, and the bubble and the floating substance pass through the through hole of the plug member. A turbid water treatment tank comprising a collection container for accumulating aggregated floating substances combined and granulated. 請求項1ないし請求項5のいずれかに記載の濁水処理槽を原水槽として備え、前記原水槽からの濁水を処理して浄化するための複数のプロセスを有する濁水処理装置。   A muddy water treatment apparatus comprising the muddy water treatment tank according to any one of claims 1 to 5 as a raw water tank, and having a plurality of processes for treating and purifying muddy water from the raw water tank.
JP2007009846A 2007-01-19 2007-01-19 Muddy water treatment tank and muddy water treatment equipment Pending JP2008173571A (en)

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Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5136669A (en) * 1974-09-12 1976-03-27 Kogyo Gijutsuin
JPH07195099A (en) * 1993-12-29 1995-08-01 Tanii Kogyo Kk Treating device of waste of ready mixed concrete
JPH10118473A (en) * 1996-08-27 1998-05-12 Nippon Shokubai Co Ltd Gas/liquid dispersion device, gas/liquid contact device and waste water treating device
JPH11309307A (en) * 1998-04-30 1999-11-09 Tomen Kenki Corp Thickener method and thickener apparatus for ready-mixed concrete wastewater
JPH11319866A (en) * 1998-05-21 1999-11-24 Sony Corp Water purification equipment
JP2000254637A (en) * 1999-03-05 2000-09-19 Yoshiya Etsuno Sludge separation device of aeration tank
WO2005123613A1 (en) * 2004-06-15 2005-12-29 Ecodays Co., Ltd. Fluids fluxion method and plant for wastewater treatment

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5136669A (en) * 1974-09-12 1976-03-27 Kogyo Gijutsuin
JPH07195099A (en) * 1993-12-29 1995-08-01 Tanii Kogyo Kk Treating device of waste of ready mixed concrete
JPH10118473A (en) * 1996-08-27 1998-05-12 Nippon Shokubai Co Ltd Gas/liquid dispersion device, gas/liquid contact device and waste water treating device
JPH11309307A (en) * 1998-04-30 1999-11-09 Tomen Kenki Corp Thickener method and thickener apparatus for ready-mixed concrete wastewater
JPH11319866A (en) * 1998-05-21 1999-11-24 Sony Corp Water purification equipment
JP2000254637A (en) * 1999-03-05 2000-09-19 Yoshiya Etsuno Sludge separation device of aeration tank
WO2005123613A1 (en) * 2004-06-15 2005-12-29 Ecodays Co., Ltd. Fluids fluxion method and plant for wastewater treatment

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