JP6386860B2 - Muddy water treatment apparatus and muddy water treatment method - Google Patents

Muddy water treatment apparatus and muddy water treatment method Download PDF

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JP6386860B2
JP6386860B2 JP2014204705A JP2014204705A JP6386860B2 JP 6386860 B2 JP6386860 B2 JP 6386860B2 JP 2014204705 A JP2014204705 A JP 2014204705A JP 2014204705 A JP2014204705 A JP 2014204705A JP 6386860 B2 JP6386860 B2 JP 6386860B2
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健吾 西田
健吾 西田
洋介 志方
洋介 志方
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一般社団法人グリーンディール推進協会
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Description

本発明は、濁水を濃縮するための濁水処理装置および濁水処理方法に関する。   The present invention relates to a muddy water treatment apparatus and a muddy water treatment method for concentrating muddy water.

建設現場等で発生する濁水の処理や、比較的小規模の閉鎖水域の浄化に伴う濁水の処理には、濁水中の懸濁物質(SS成分、例えば、粘土、シルト、セメント成分等)の除去や固化、脱水が避けられない要件である。   For the treatment of turbid water generated at construction sites, etc. and for the treatment of turbid water associated with the purification of relatively small closed water areas, removal of suspended substances (SS components such as clay, silt, cement components, etc.) in muddy water It is an inevitable requirement for solidification and dehydration.

このような濁水の処理において、例えば飲料水精製においては、前処理として凝集剤等の薬品を用いる凝集処理により濁水中の懸濁物質をある程度除いた後、さらに砂ろ過等のろ過処理により、処理水を得ることが行われている。   In such turbid water treatment, for example, in the purification of drinking water, after removing suspended substances in turbid water to some extent by agglomeration treatment using a chemical such as a flocculant as a pretreatment, the treatment is further performed by filtration treatment such as sand filtration. Getting water is done.

凝集処理では、凝集剤撹拌槽、凝集沈降分離水槽、pH調整槽、中和槽等より構成される処理設備を必要とし、連続処理をする場合は、処理中の濁水を貯留する大容量の濁水槽が必要となる。さらに、凝集剤が排出脱水ケーキに混入するため、多くの場合、産業廃棄物としての処分が必要となり、再資源化の観点からも、コスト面でも課題となっている。   In the flocculation treatment, treatment equipment composed of a flocculating agent stirring tank, a flocculation / separation separation water tank, a pH adjustment tank, a neutralization tank, etc. is required. A water tank is required. Furthermore, since the flocculant is mixed into the discharged dehydrated cake, in many cases, disposal as industrial waste is required, which is a problem from the viewpoint of recycling and cost.

前処理に用いられる、凝集剤等の薬品を使用しない濁水処理装置としては、例えば、特許文献1には、ろ過槽内に分離膜を配設した膜モジュールを浸漬し、ポンプを用いて膜モジュールの二次側を吸引することによる吸引圧、あるいは水面のヘッド差による圧力を膜間差圧として膜モジュールによるろ過を行う汚濁水のろ過方法において、コンプレッサを用いて膜モジュールの二次側より一次側へエアーを通気させることにより、膜モジュールの洗浄処理を行う汚濁水のろ過方法が記載されている。   As a turbid water treatment apparatus that does not use chemicals such as a flocculant used for pretreatment, for example, in Patent Document 1, a membrane module in which a separation membrane is arranged in a filtration tank is immersed, and a membrane module is used using a pump. In the filtration method of polluted water that performs filtration through the membrane module using the suction pressure by suctioning the secondary side of the water or the pressure due to the head difference on the water surface as the transmembrane differential pressure, the primary side from the secondary side of the membrane module using a compressor A method for filtering contaminated water is described in which the membrane module is subjected to a cleaning process by aerating air to the side.

しかし、濁水処理装置において、特許文献1のようにポンプとコンプレッサを併用すると設備のコストが増大する。   However, in the turbid water treatment apparatus, when a pump and a compressor are used in combination as in Patent Document 1, the cost of equipment increases.

特開平9−168727号公報JP-A-9-168727

本発明の目的は、簡易な構成で濁水の濃縮を行うことができる濁水処理装置および濁水処理方法を提供することにある。   The objective of this invention is providing the muddy water processing apparatus and muddy water processing method which can concentrate muddy water with a simple structure.

本発明は、懸濁物質を含む濁水を処理するための濁水処理装置であって、濁水をろ過するためのろ過槽と、前記濁水の貯留源と前記ろ過槽の上部とを接続する移送流路と、前記ろ過槽中の濁水に浸漬してろ過処理を行うための少なくとも1つの中空状のろ過材と、吸引側が前記移送流路の途中および前記ろ過材の内部に接続された真空吸引手段と、を備え、前記移送流路の途中と前記真空吸引手段の吸引側とを非連通状態とし、前記濁水の貯留源と前記ろ過槽の上部とを連通状態とし、かつ前記ろ過材の内部と前記真空吸引手段の吸引側とを連通状態とし、その他は前記ろ過槽を密閉した状態で、前記真空吸引手段により真空吸引することによって前記ろ過材を介して前記ろ過槽内に負圧を形成することにより前記濁水を前記ろ過槽内に取り込み、前記ろ過材を前記濁水中に浸漬させた状態で、前記濁水をろ過して前記ろ過材の表面に前記懸濁物質を付着させた後、前記濁水の貯留源と前記ろ過槽の上部とを非連通状態とし、前記ろ過槽の上部と前記真空吸引手段の吸引側とを連通状態とし、前記ろ過材の内部と前記真空吸引手段の吸引側とを非連通状態とし、かつ前記ろ過材の内部を大気側と連通状態とし、その他は前記ろ過槽を密閉した状態で前記真空吸引手段により前記ろ過材の内部に大気を取り込み、前記ろ過材を前記濁水に浸漬させた状態で、その大気を前記ろ過材の外部に排出することにより前記ろ過材の表面に付着した懸濁物質を剥離する濁水処理装置である。 The present invention is a turbid water treatment apparatus for treating turbid water containing a suspended substance, and a transfer channel for connecting a turbid water storage source and an upper part of the filtration tub to filter muddy water. And at least one hollow filter medium for performing a filtration treatment by immersing in turbid water in the filter tank, and a vacuum suction means whose suction side is connected to the middle of the transfer flow path and inside the filter medium , In the middle of the transfer flow path and the suction side of the vacuum suction means is in a non-communication state, the turbid water storage source and the upper portion of the filtration tank is in communication, and the inside of the filter medium and the The suction side of the vacuum suction means is in a communication state, and the others are in a state where the filtration tank is sealed, and vacuum suction is performed by the vacuum suction means to form a negative pressure in the filtration tank through the filter medium. The muddy water is taken into the filtration tank by It is seen, in a state in which the filter medium was immersed in the turbid water, after depositing the suspended matter on the surface of the filter medium by filtering the turbid water, a reservoir source of the turbid water and the upper portion of the filter tank In the non-communication state, the upper portion of the filtration tank and the suction side of the vacuum suction means are in communication state, the inside of the filter medium and the suction side of the vacuum suction means are in non-communication state, and the filter medium The inside is in a communication state with the atmosphere side, and the other is in a state where the filtration tank is sealed, the atmosphere is taken into the filter medium by the vacuum suction means, and the filter medium is immersed in the turbid water. It is a muddy water treatment apparatus which peels the suspended substance adhering to the surface of the said filter medium by discharging | emitting outside the said filter medium.

前記濁水処理装置において、前記ろ過材が内部に位置するように設置され、上端および下端が開口する内筒管を備えることが好ましい。   In the muddy water treatment apparatus, it is preferable that the filter medium is provided so as to be positioned inside, and includes an inner tube having an upper end and a lower end opened.

前記濁水処理装置において、前記剥離の際の前記ろ過材の膨らみを抑制するための縫製、溶着等による貼り合わせ部または膨らみ抑制部材を備えることが好ましい。   In the muddy water treatment apparatus, it is preferable that the muddy water treatment apparatus includes a bonded portion or a swelling suppressing member by sewing, welding or the like for suppressing swelling of the filter medium at the time of peeling.

また、本発明は、懸濁物質を含む濁水を処理するための濁水処理方法であって、濁水をろ過するためのろ過槽中に少なくとも1つの中空状のろ過材を設置して、前記濁水の貯留源と前記ろ過槽の上部とを移送流路で接続し、吸引側が前記移送流路の途中および前記ろ過材の内部に接続された真空吸引手段を用い、前記移送流路の途中と前記真空吸引手段の吸引側とを非連通状態とし、前記濁水の貯留源と前記ろ過槽の上部とを連通状態とし、かつ前記ろ過材の内部と前記真空吸引手段の吸引側とを連通状態とし、その他は前記ろ過槽を密閉した状態で、真空吸引することによって前記ろ過材を介して前記ろ過槽内に負圧を形成することにより前記濁水を前記ろ過槽内に取り込み、前記ろ過材を前記濁水中に浸漬させた状態で、前記濁水をろ過して前記ろ過材の表面に前記懸濁物質を付着させた後、前記濁水の貯留源と前記ろ過槽の上部とを非連通状態とし、前記ろ過槽の上部と前記真空吸引手段の吸引側とを連通状態とし、前記ろ過材の内部と前記真空吸引手段の吸引側とを非連通状態とし、かつ前記ろ過材の内部を大気側と連通状態とし、その他は前記ろ過槽を密閉した状態で前記真空吸引手段により真空吸引することによって前記ろ過材の内部に大気を取り込み、前記ろ過材を前記濁水に浸漬させた状態で、その大気を前記ろ過材の外部に排出することにより前記ろ過材の表面に付着した懸濁物質を剥離する濁水処理方法である。 The present invention is also a turbid water treatment method for treating turbid water containing suspended substances, wherein at least one hollow filter medium is installed in a filtration tank for filtering turbid water, A storage source and the upper part of the filtration tank are connected by a transfer channel, and a suction side is connected to the middle of the transfer channel and the inside of the filter medium. The suction side of the suction means is in a non-communication state, the turbid water storage source and the upper part of the filtration tank are in a communication state, and the inside of the filter medium and the suction side of the vacuum suction means are in a communication state. In a state where the filtration tank is sealed , the muddy water is taken into the filtration tank by forming a negative pressure in the filtration tank through the filter medium by vacuum suction , and the filter medium is taken into the muddy water. The muddy water is filtered while immersed in After depositing the suspended matter on the surface of the filter medium Te, and an upper of said filter tank and the reservoir source of the turbid water to a non-communicating state, a suction side of the upper and the vacuum suction means of the filter tank a communication state, a suction side of the internal and the vacuum suction means of the filtering material and a non-communicating state, and the inside of the filter media to the atmosphere side and the communication with the others the vacuum while sealing the filter tank The air is taken into the filter medium by vacuum suction by a suction means , and the filter medium is immersed in the muddy water, and the air is discharged to the outside of the filter medium on the surface of the filter medium. This is a muddy water treatment method for peeling off adhering suspended solids.

本発明では、真空吸引手段を用いる簡易な構成で濁水の濃縮を行うことができる濁水処理装置を提供する。   The present invention provides a turbid water treatment apparatus capable of concentrating turbid water with a simple configuration using vacuum suction means.

本発明の実施形態に係る濁水処理装置の一例を示す概略構成図であり、真空吸引ろ過工程を示す概略図である。It is a schematic block diagram which shows an example of the muddy water processing apparatus which concerns on embodiment of this invention, and is a schematic diagram which shows a vacuum suction filtration process. 本発明の実施形態に係る濁水処理装置の一例を示す概略構成図であり、水中剥離工程を示す概略図である。It is a schematic block diagram which shows an example of the muddy water processing apparatus which concerns on embodiment of this invention, and is the schematic which shows an underwater peeling process. 本発明の実施形態に係る濁水処理装置の他の例を示す概略構成図である。It is a schematic block diagram which shows the other example of the muddy water processing apparatus which concerns on embodiment of this invention. 本発明の実施形態に係る濁水処理装置の他の例を示す概略構成図である。It is a schematic block diagram which shows the other example of the muddy water processing apparatus which concerns on embodiment of this invention. 本発明の実施形態に係る濁水処理装置の他の例を示す概略構成図である。It is a schematic block diagram which shows the other example of the muddy water processing apparatus which concerns on embodiment of this invention. 本発明の実施形態に係る濁水処理装置におけるろ過材の構成の一例を示す概略図である。It is the schematic which shows an example of a structure of the filter medium in the muddy water processing apparatus which concerns on embodiment of this invention. 本発明の実施形態に係る濁水処理装置を備える濁水処理システムの一例を示す概略構成図である。It is a schematic structure figure showing an example of a muddy water treatment system provided with a muddy water treatment device concerning an embodiment of the present invention.

本発明の実施の形態について以下説明する。本実施形態は本発明を実施する一例であって、本発明は本実施形態に限定されるものではない。   Embodiments of the present invention will be described below. This embodiment is an example for carrying out the present invention, and the present invention is not limited to this embodiment.

<濁水処理>
本発明の実施形態に係る濁水処理装置の一例の概略構成を図1に示し、その構成について説明する。本実施形態に係る濁水処理装置1は、主に、濁水をろ過処理し、濃縮するために用いられる。濁水処理装置1は、濁水をろ過するためのろ過槽10と、ろ過槽10中の濁水に浸漬してろ過処理を行うための少なくとも1つの中空状のろ過材12と、ろ過材12に接続された真空吸引手段としての真空吸引装置14とを備える。
<Muddy water treatment>
A schematic configuration of an example of a muddy water treatment apparatus according to an embodiment of the present invention is shown in FIG. 1, and the configuration will be described. The muddy water treatment apparatus 1 according to the present embodiment is mainly used for filtering and concentrating muddy water. The muddy water treatment apparatus 1 is connected to a filter tank 10 for filtering muddy water, at least one hollow filter medium 12 for performing a filtration process by immersing in muddy water in the filter tank 10, and the filter medium 12. And a vacuum suction device 14 as vacuum suction means.

図1の濁水処理装置1において、移送流路20の一端が濁水の貯留源である被処理濁水槽34中の被処理濁水に浸漬され、他端はろ過槽10の上部の開口部32に接続され、移送流路20の途中には三方バルブ28が設けられている。ろ過材12は中空状になっており、ろ過材12の内部と接続された配管16によりろ過槽10の上部に設けられた開口部30を通して真空吸引装置14の吸引側と接続されている。ろ過槽10は密閉されていてもよい。配管16の途中には三方バルブ24,26が設けられている。三方バルブ28と三方バルブ26とは、配管22により接続されている。ろ過槽10の下部には、バルブ44を介して排出口46が設けられている。図1の例では、濁水処理装置1は1つのろ過材12を有するが、ろ過材12の数は少なくとも1つであればよく、2つ以上であってもよく、これに限定されるものではない。   In the muddy water treatment apparatus 1 of FIG. 1, one end of the transfer channel 20 is immersed in the muddy water to be treated in the muddy water tank 34 to be treated which is a turbid water storage source, and the other end is connected to the opening 32 at the top of the filtration tank 10. A three-way valve 28 is provided in the middle of the transfer channel 20. The filter medium 12 has a hollow shape, and is connected to the suction side of the vacuum suction device 14 through an opening 30 provided in the upper part of the filter tank 10 by a pipe 16 connected to the inside of the filter medium 12. The filtration tank 10 may be sealed. Three-way valves 24 and 26 are provided in the middle of the pipe 16. The three-way valve 28 and the three-way valve 26 are connected by a pipe 22. A discharge port 46 is provided in the lower part of the filtration tank 10 through a valve 44. In the example of FIG. 1, the muddy water treatment apparatus 1 has one filter medium 12, but the number of filter mediums 12 may be at least one and may be two or more, and is not limited thereto. Absent.

次に、濁水処理装置1の動作および濁水処理方法について図1,2を参照して説明する。   Next, the operation of the muddy water treatment apparatus 1 and the muddy water treatment method will be described with reference to FIGS.

図1に示すように、三方バルブ28を被処理濁水槽34とろ過槽10の開口部32との連通状態、三方バルブ24,26をろ過槽10の開口部30と真空吸引装置14との連通状態として、真空吸引装置14を作動させて真空吸引を開始する。真空吸引されることによってろ過材12を介してろ過槽10内に負圧が形成され、被処理濁水槽34から移送流路20を通して懸濁物質(SS成分)を含む濁水等の被処理濁水がろ過槽10に移送され、ろ過材12によって被処理濁水のろ過処理が行われる(真空吸引ろ過工程)。ろ過材12によりろ過処理されたろ過水は、配管16を通して系外へ排出される。一方、ろ過物である懸濁物質等は、ろ過材12の表面に付着される。   As shown in FIG. 1, the three-way valve 28 communicates with the muddy water tank 34 to be treated and the opening 32 of the filtration tank 10, and the three-way valves 24 and 26 communicate with the opening 30 of the filtration tank 10 and the vacuum suction device 14. As a state, the vacuum suction device 14 is operated to start vacuum suction. By vacuum suction, a negative pressure is formed in the filtration tank 10 through the filter medium 12, and muddy water to be treated such as turbid water containing suspended substances (SS component) from the muddy water tank 34 to be treated through the transfer channel 20. The turbid water to be treated is filtered by the filter medium 12 (vacuum suction filtration step). The filtered water filtered by the filter medium 12 is discharged out of the system through the pipe 16. On the other hand, suspended matter or the like that is a filtrate is attached to the surface of the filter medium 12.

ろ過槽10が密閉されている場合、被処理濁水がろ過材12の上端に達すると、ろ過槽10上部の残留空気が排出されないため水位の上昇が止まる。真空吸引が継続しているため、ろ過材12を介して系外に排出されたろ過水量と同等量の被処理濁水がろ過槽10内に連続的に供給され、ろ過槽10内の水位がほぼ一定に保たれる。本構成により、真空吸引により濁水の貯留源である被処理濁水槽34から被処理濁水をろ過槽10に自動供給することができる。また、ろ過槽10中の濁水の水位がほぼ一定に保たれるため、センサやフロート弁等による水位管理を行わなくてもよい。   When the filtration tank 10 is sealed, when the muddy water to be treated reaches the upper end of the filter medium 12, the residual air at the upper part of the filtration tank 10 is not discharged, so that the rise in the water level stops. Since the vacuum suction is continued, the amount of treated muddy water equivalent to the amount of filtered water discharged out of the system through the filter medium 12 is continuously supplied into the filtration tank 10, and the water level in the filtration tank 10 is almost the same. Kept constant. With this configuration, the muddy water to be treated can be automatically supplied to the filtration tank 10 from the muddy water tank 34 to be treated, which is a turbid water storage source, by vacuum suction. Moreover, since the water level of the muddy water in the filtration tank 10 is kept substantially constant, it is not necessary to perform water level management by a sensor, a float valve, or the like.

なお、真空吸引ろ過工程に限定すれば、ポンプ等を用いてろ過槽10に濁水を供給し、真空吸引装置および中空状のろ過材を用いてろ過処理を行えばよく、ろ過槽10は密閉されていなくてもよい。   In addition, if it restrict | limits to a vacuum suction filtration process, a turbid water may be supplied to the filtration tank 10 using a pump etc., and a filtration process may be performed using a vacuum suction device and a hollow filter medium, and the filtration tank 10 is sealed. It does not have to be.

ろ過材12の表面に、汚泥等の懸濁物質が付着すると通水性が低下し、ろ過水の量が減少する。そこで、真空吸引装置14を作動させたまま、図2に示すように、三方バルブ26,28をろ過槽10の開口部32と真空吸引装置14との連通状態として、三方バルブ24を大気側とろ過槽10の開口部30との連通状態とする。大気が三方バルブ24の開口部から吸引されてろ過材12の内部に取り込まれ、ろ過材12の表面より排出されることにより、ろ過材12の表面に付着していた汚泥等の懸濁物質は剥離して落下する(水中剥離工程)。ろ過材12の膨張によるろ過槽10内の水位の上昇は、ろ過槽10内のろ過材12の上部に空間を設けて吸収すればよい。ろ過材12の表面に付着していた汚泥等の懸濁物質が十分に剥離したら、真空吸引装置14を停止すればよい。濃縮された濃縮スラリーは、バルブ44を開状態として、排出口46から排出される(排出工程)。以上の真空吸引ろ過工程、水中剥離工程および排出工程を繰り返すことにより、濁水の濃縮処理が行われる。   When suspended substances such as sludge adhere to the surface of the filter medium 12, the water permeability decreases and the amount of filtered water decreases. Therefore, with the vacuum suction device 14 operating, as shown in FIG. 2, the three-way valves 26 and 28 are in communication with the opening 32 of the filtration tank 10 and the vacuum suction device 14, and the three-way valve 24 is connected to the atmosphere side. A communication state with the opening 30 of the filtration tank 10 is established. Suspended substances such as sludge adhering to the surface of the filter medium 12 are obtained when the air is sucked from the opening of the three-way valve 24 and taken into the filter medium 12 and discharged from the surface of the filter medium 12. Peel and fall (underwater peeling process). The rise in the water level in the filter tank 10 due to the expansion of the filter medium 12 may be absorbed by providing a space above the filter medium 12 in the filter tank 10. When suspended substances such as sludge adhering to the surface of the filter medium 12 are sufficiently separated, the vacuum suction device 14 may be stopped. The concentrated slurry is discharged from the discharge port 46 with the valve 44 opened (discharge process). By repeating the vacuum suction filtration process, the underwater peeling process and the discharging process, the turbid water is concentrated.

本構成により、コンプレッサ等の送気装置を用いなくても、真空吸引装置という簡便な手段で効率的な濃縮処理を実現することができる。これにより、付帯設備の削減と装置の簡素化とにより設備コストのより一層の低減、作業性の向上、省スペース化が可能となる。   With this configuration, an efficient concentration process can be realized by a simple means such as a vacuum suction device without using an air supply device such as a compressor. As a result, it is possible to further reduce the equipment cost, improve workability, and save space by reducing the incidental equipment and simplifying the apparatus.

また、本処理方法では、凝集剤を用いなくてもよいため、凝集剤撹拌槽、pH調整槽、中和槽などの水槽を設ける必要がなく、設備の軽減につながる。凝集剤等の添加物を含まないため、ケーキを産業廃棄物処理する必要がなく、オンサイトで再利用可能となり、コスト低減効果も高い。   Moreover, in this processing method, since it is not necessary to use a flocculant, it is not necessary to provide a water tank such as a flocculant stirring tank, a pH adjustment tank, or a neutralization tank, which leads to a reduction in equipment. Since it does not contain additives such as flocculants, it is not necessary to treat the cake with industrial waste, and it can be reused on-site, resulting in a high cost reduction effect.

被処理濁水槽34は、被処理濁水を貯留し、少なくとも移送流路20の一端を接続または浸漬可能なものであればよく、特に制限はない。図1,2の濁水処理装置1において、被処理濁水槽34中の被処理濁水に移送流路20の一端が浸漬されて真空吸引処理が行われるが、被処理濁水槽34を設けずに、池、河川、湖等の処理対象に移送流路20の一端が直接浸漬されて真空吸引処理が行われてもよい。   The muddy water tank 34 to be treated is not particularly limited as long as it stores muddy water to be treated and can connect or immerse at least one end of the transfer channel 20. In the muddy water treatment apparatus 1 of FIGS. 1 and 2, one end of the transfer channel 20 is immersed in the muddy water to be treated in the muddy water tank 34 to be treated, and vacuum suction processing is performed, but without providing the muddy water tank 34 to be treated, One end of the transfer channel 20 may be directly immersed in a processing target such as a pond, a river, a lake, or the like, and vacuum suction processing may be performed.

移送流路20は、ろ過槽10のどの位置に接続してもよい。   The transfer channel 20 may be connected to any position of the filtration tank 10.

排出口46は、ろ過槽10の下部に設けられればよく、ろ過槽10の下部側面に設けられてもよい。   The discharge port 46 should just be provided in the lower part of the filtration tank 10, and may be provided in the lower side surface of the filtration tank 10. FIG.

三方バルブ24,26,28を用いて真空吸引ろ過工程と水中剥離工程における流路を切り替えているが、二方バルブを用いて流路を切り替えてもよく、特に制限はない。   Although the flow paths in the vacuum suction filtration process and the underwater separation process are switched using the three-way valves 24, 26, and 28, the flow paths may be switched using a two-way valve, and there is no particular limitation.

真空吸引装置14としては、真空吸引できるものであればよく、特に制限はないが、例えば、真空ポンプ、エジェクタ等が挙げられ、高い真空度と高排気量を有する装置が好ましい。   The vacuum suction device 14 is not particularly limited as long as it can perform vacuum suction, and examples thereof include a vacuum pump and an ejector, and a device having a high degree of vacuum and a high displacement is preferable.

ろ過材12への大気の導入は、ろ過材12の上部から導入しても下部から導入してもよいが、ろ過材の表面からほぼ一様の状態で汚泥等を剥離することができる等の点で、下部から導入することが好ましい。   The introduction of air into the filter medium 12 may be introduced from the upper part or the lower part of the filter medium 12, but sludge and the like can be peeled off from the surface of the filter medium in a substantially uniform state. In this respect, it is preferable to introduce from the bottom.

濁水処理に用いられるろ過材12は例えば布材で、水分は通すが、所定の大きさの懸濁物質等は通さないろ過機能を有し、さらに内側に空気等の気体が注入されると内部から外側に気体を排出するように適度な通気性を備えている。ろ過材12の形状および材質は、濁水等の被処理水から懸濁物質を捕捉、分離することができるものであればよく、特に制限はない。ろ過材12の形状および材質は、処理対象となる被処理水の性状、含まれる懸濁物質等の性状等に応じて選択すればよい。ろ過材12の形状は、中空状のものであればよく、特に制限はないが、例えば、円筒形状、楕円筒形状、多角筒形状等の筒型形状や、板形状、球形状、多角形形状等であり、板形状が好ましい。ろ過面積を大きくするためには、できるだけろ過材が膨らまないような構成とし、できるだけ多くのろ過材をろ過槽内に設置するとよい。   The filter medium 12 used for the muddy water treatment is, for example, a cloth material, which has a filtration function that allows moisture to pass through but does not allow a suspended substance or the like of a predetermined size to pass therethrough. Appropriate ventilation is provided so that gas is discharged from the outside. The shape and material of the filter medium 12 are not particularly limited as long as they can capture and separate suspended substances from water to be treated such as turbid water. What is necessary is just to select the shape and material of the filter medium 12 according to the property of the to-be-processed water used as a process target, the property, etc. of the suspended substance contained. The shape of the filter medium 12 is not particularly limited as long as it is hollow. For example, a cylindrical shape such as a cylindrical shape, an elliptical cylindrical shape, or a polygonal cylindrical shape, a plate shape, a spherical shape, or a polygonal shape. The plate shape is preferable. In order to increase the filtration area, it is preferable that the filter medium is configured not to swell as much as possible, and as much filter medium as possible be installed in the filter tank.

例えば、図6に示すような、1つ以上のろ室50を有する板形状のろ過材12を用いることができる。図6に示すろ過材12は、ろ布を縫製処理または溶着等により貼り合わされた貼り合わせ部52によって1つ以上のろ室50が形成された構成となっている。ろ過材12によりろ過処理されたろ過水は、各ろ室50内から下部集水管54を通って排出されるようになっている。各ろ室50にはろ過水が通過するための流路を形成した板状等のパネル材等を挿入してもよい。   For example, a plate-shaped filter medium 12 having one or more filter chambers 50 as shown in FIG. 6 can be used. The filter medium 12 shown in FIG. 6 has a configuration in which one or more filter chambers 50 are formed by a bonding portion 52 in which a filter cloth is bonded by sewing or welding. The filtered water filtered by the filter medium 12 is discharged from the inside of each filter chamber 50 through the lower water collection pipe 54. Each filter chamber 50 may be inserted with a plate-like panel material or the like having a flow path through which filtered water passes.

図6に示すように、ろ過材12の両側面を覆うように、剥離の際のろ過材の膨らみを抑制する膨らみ抑制部材36を設置してもよい。本構成により、水中剥離工程において、ろ過材の膨らみが抑制されるため、図3に示すように、ろ過槽10内に複数のろ過材12を向かい合うように設置する場合、より近接してろ過材12を配置することができ、効率的なろ過を行うことができる。   As shown in FIG. 6, a bulge suppressing member 36 that suppresses the bulge of the filter medium during peeling may be installed so as to cover both side surfaces of the filter medium 12. With this configuration, since the swelling of the filter medium is suppressed in the underwater peeling process, as shown in FIG. 3, when installing a plurality of filter mediums 12 in the filter tank 10 so as to face each other, the filter medium is closer to each other. 12 can be arranged, and efficient filtration can be performed.

膨らみ抑制部材36としては、例えば、網状の剛性部材等が挙げられる。また、図6に示すような縫製処理または溶着等による貼り合わせ部52等により、ろ室50を多設し、ろ過材12の膨らみを抑制する構造としてもよい。   Examples of the swelling suppression member 36 include a net-like rigid member. Moreover, it is good also as a structure which suppresses the swelling of the filter medium 12 by providing many filter chambers 50 by the bonding part 52 etc. by sewing processing or welding as shown in FIG.

図4に示すように、ろ過槽10内に、ろ過材12が内部に位置するように設置され、上端および下端が開口する内筒管38を備えてもよい。本構成により、水中剥離工程において、ろ過材12から排出された空気が内筒管38内を上昇し、内筒管38の内外で比重差が発生し、下部から上方向に向かって水流が発生する。これにより、気水混合流によるろ過材12の表面の洗浄と、ろ過材12の内部からの空気による水中剥離とが行われ、より効率的な水中剥離を行うことができる。   As shown in FIG. 4, an inner cylinder pipe 38 may be provided in the filtration tank 10 so that the filter medium 12 is positioned inside, and the upper end and the lower end are open. With this configuration, in the underwater peeling process, the air exhausted from the filter medium 12 rises in the inner cylinder pipe 38, a specific gravity difference is generated inside and outside the inner cylinder pipe 38, and a water flow is generated upward from the lower part. To do. Thereby, washing | cleaning of the surface of the filter medium 12 by a gas-water mixed flow and underwater peeling by the air from the inside of the filter medium 12 are performed, and more efficient underwater peeling can be performed.

図5に示すように、ろ過槽10内に、複数のろ過材12を、多段および複数列に設置してもよい。図5の例では、ろ過材12を2段および2列に設置しているが、これに限定されない。各ろ過材12には、ろ過材12の両側面を覆うように膨らみ抑制部材36が設置されている。また、全てのろ過材12が内部に位置するように内筒管38が設置されている。上段の各ろ過材12の下部は開口部30a、バルブ40を介して、下段の各ろ過材12の下部は開口部30bを通しバルブ42を介して、配管16により、真空吸引装置14の吸引側と接続されている。   As shown in FIG. 5, a plurality of filter media 12 may be installed in a multistage and a plurality of rows in the filter tank 10. In the example of FIG. 5, the filter media 12 are installed in two stages and two rows, but the present invention is not limited to this. Each filter medium 12 is provided with a swelling suppression member 36 so as to cover both side surfaces of the filter medium 12. Moreover, the inner cylinder pipe 38 is installed so that all the filter media 12 may be located inside. The lower part of each upper filter medium 12 is provided through an opening 30a and a valve 40, and the lower part of each lower filter medium 12 is provided through an opening 30b and through a valve 42 via a pipe 16 and the suction side of the vacuum suction device 14. Connected with.

三方バルブ28を被処理濁水槽34とろ過槽10の開口部32との連通状態、三方バルブ24,26をろ過槽10の開口部30a,30bと真空吸引装置14との連通状態とし、バルブ40,42を開状態として、真空吸引装置14を作動させて真空吸引を開始する。真空吸引されることによって各ろ過材12を介してろ過槽10内に負圧が形成され、被処理濁水槽34から移送流路20を通して懸濁物質(SS成分)を含む濁水等の被処理濁水がろ過槽10に移送され、各ろ過材12によって被処理濁水のろ過処理が行われる(真空吸引ろ過工程)。各ろ過材12によりろ過処理されたろ過水は、配管16を通して系外へ排出される。一方、ろ過物である懸濁物質等は、各ろ過材12の表面に付着される。   The three-way valve 28 is connected to the muddy water tank 34 to be treated and the opening 32 of the filtration tank 10, and the three-way valves 24 and 26 are connected to the openings 30 a and 30 b of the filtration tank 10 and the vacuum suction device 14. , 42 are opened, and the vacuum suction device 14 is operated to start vacuum suction. By being sucked in vacuum, a negative pressure is formed in the filtration tank 10 through each filter medium 12, and muddy water to be treated such as muddy water containing suspended substances (SS component) from the muddy water tank 34 to be treated through the transfer channel 20. Is transferred to the filtration tank 10, and the turbid water to be treated is filtered by each filter medium 12 (vacuum suction filtration process). The filtered water filtered by each filter medium 12 is discharged out of the system through the pipe 16. On the other hand, suspended matter or the like that is a filtrate is attached to the surface of each filter medium 12.

各ろ過材12の表面に、汚泥等の懸濁物質が付着すると通水性が低下し、ろ過水の量が減少する。そこで、真空吸引装置14を作動させたまま、三方バルブ26,28をろ過槽10の開口部32と真空吸引装置14との連通状態として、三方バルブ24を大気側とろ過槽10の開口部30a,30bとの連通状態とすると、大気が三方バルブ24の開口部から吸引されて各ろ過材12の内部に取り込まれる。ろ過材12から排出された空気が内筒管38内を上昇し、内筒管38の内外で比重差が発生し、下部から上方向に向かって水流が発生する。これにより、気水混合流による各ろ過材12の表面の洗浄と、各ろ過材12の内部からの空気による水中剥離とが行われ、より効率的な水中剥離を行うことができる。各ろ過材12の表面に付着していた汚泥等の懸濁物質が十分に剥離したら、バルブを切り替えて真空吸引ろ過工程に入ればよい。   When suspended substances such as sludge adhere to the surface of each filter medium 12, the water permeability decreases and the amount of filtered water decreases. Therefore, with the vacuum suction device 14 being operated, the three-way valves 26 and 28 are brought into communication with the opening 32 of the filtration tank 10 and the vacuum suction device 14, and the three-way valve 24 is connected to the atmosphere side and the opening 30 a of the filtration tank 10. , 30b, the atmosphere is sucked from the opening of the three-way valve 24 and taken into the filter media 12. The air exhausted from the filter medium 12 rises in the inner tube 38, a specific gravity difference is generated inside and outside the inner tube 38, and a water flow is generated upward from the lower part. Thereby, washing | cleaning of the surface of each filter medium 12 by an air-water mixed flow and underwater peeling by the air from the inside of each filter medium 12 are performed, and more efficient underwater peeling can be performed. When the suspended substances such as sludge adhering to the surface of each filter medium 12 are sufficiently separated, the valve may be switched to enter the vacuum suction filtration process.

また、真空吸引ろ過工程の後、別の方法として、真空吸引装置14を作動させたまま、三方バルブ26,28をろ過槽10の開口部32と真空吸引装置14との連通状態として、上段側のバルブ40を閉状態とし、三方バルブ24を大気側とろ過槽10の開口部30a,30bとの連通状態とすると、大気が三方バルブ24の開口部から吸引されて下段の各ろ過材12の内部に取り込まれる。下段の各ろ過材12から排出された空気が内筒管38内を上昇し、内筒管38の内外で比重差が発生し、下部から上方向に向かって水流が発生する。これにより、気水混合流による上段側の各ろ過材12の表面の一次洗浄が行われ、次に、上段側のバルブ40を開状態とすると、上段側の各ろ過材12の内部からの空気による水中剥離が行われる。このように水中剥離を下段から上段へと順次実施することにより、さらに効率的な水中剥離を行うことができる。   In addition, after the vacuum suction filtration step, as another method, the three-way valves 26 and 28 are kept in communication with the opening 32 of the filtration tank 10 and the vacuum suction device 14 while the vacuum suction device 14 is operated. When the three-way valve 24 is in a communication state between the atmosphere side and the openings 30a and 30b of the filtration tank 10, the atmosphere is sucked from the openings of the three-way valve 24 and the lower filter media 12 are in the closed state. Captured inside. The air discharged from the lower filter media 12 rises in the inner cylinder pipe 38, a specific gravity difference is generated inside and outside the inner cylinder pipe 38, and a water flow is generated upward from the lower part. Thereby, primary cleaning of the surface of each upper filter medium 12 by the air-water mixed flow is performed, and then when the upper valve 40 is opened, the air from the inside of each upper filter medium 12 The underwater peeling is performed. In this way, by performing the underwater peeling sequentially from the lower stage to the upper stage, it is possible to perform more efficient underwater peeling.

図7に、本発明の実施形態に係る濁水処理装置1を備える濁水処理システムの一例の概略構成を示す。図7の濁水処理システム3において、被処理濁水槽34からの濁水について、ろ過槽10およびろ過材を備える濁水処理装置1で真空吸引装置14を用いた前ろ過処理が行われる。得られたろ過水は、必要に応じて貯水槽60に貯留された後、ろ過処理装置62に送液され、ろ過されて、処理水が得られる。ろ過処理装置62としては、ろ過処理を行うものであればよく、特に制限はないが、例えば、砂ろ過装置、中空糸等を用いた高度水処理装置等が挙げられる。   In FIG. 7, schematic structure of an example of the muddy water processing system provided with the muddy water processing apparatus 1 which concerns on embodiment of this invention is shown. In the turbid water treatment system 3 in FIG. 7, pre-filtration treatment using the vacuum suction device 14 is performed on the turbid water from the muddy water tank 34 to be treated in the muddy water treatment apparatus 1 including the filtration tank 10 and the filter medium. The obtained filtered water is stored in the water storage tank 60 as necessary, and then sent to the filtration processing device 62 and filtered to obtain treated water. The filtration device 62 is not particularly limited as long as it performs a filtration treatment, and examples thereof include a sand filtration device and an advanced water treatment device using a hollow fiber.

本実施形態に係る濁水処理装置の処理対象となる被処理濁水としては、例えば、土木・建築現場等で発生する濁水、河川・湖沼・池・運河等の底質改善や浚渫に伴う濁水、土壌洗浄後の濁水、粘土・シルト等を含む濁水、セメント成分等の化学物質を含む濁水等が挙げられるが、これらに限定されるものではない。例えば、放流レベルから飲料水生成(高度処理)の前処理まで多様な濁水処理が可能である。   Examples of the muddy water to be treated by the muddy water treatment apparatus according to this embodiment include muddy water generated at civil engineering / construction sites, muddy water, soil due to bottom sediment improvement and dredging of rivers / lakes / ponds / canals, etc. Examples include, but are not limited to, muddy water after washing, muddy water containing clay and silt, muddy water containing chemical substances such as cement components, and the like. For example, various muddy water treatments from the discharge level to the pretreatment of drinking water generation (advanced treatment) are possible.

以下、実施例および比較例を挙げ、本発明をより具体的に詳細に説明するが、本発明は、以下の実施例に限定されるものではない。   Hereinafter, although an example and a comparative example are given and the present invention is explained more concretely in detail, the present invention is not limited to the following examples.

[実施例1]
図3に示すように、上部に2つの開口部30,32が設置された円筒状の樹脂製のろ過槽10(内径230mm、高さ1000mm、容積40L/m)内にろ過材12として中空平板状のろ布(通気度100cm/cm/min、幅90mm×高さ230mm、ろ布面積414cm)2枚(合計ろ布面積828cm)を同じ高さに向かい合うように設置し、移送経路20となる管を、三方バルブ28を介して被処理濁水槽34に浸漬した。配管16により、ろ布を開口部30に接続し、三方バルブ24,26を介して真空吸引装置14の吸引側と接続した。三方バルブ26と三方バルブ28とを配管22により接続した。それぞれの平板状のろ布の両面には、膨らみ抑制部材36として、網状の剛性部材(幅110mm×高さ250mm)を設置した。
[Example 1]
As shown in FIG. 3, a hollow flat plate is used as a filter medium 12 in a cylindrical resin filtration tank 10 (inner diameter 230 mm, height 1000 mm, volume 40 L / m) having two openings 30 and 32 installed at the top. 2 pieces of filter cloth (air permeability 100 cm 3 / cm 2 / min, width 90 mm × height 230 mm, filter cloth area 414 cm 2 ) (total filter cloth area 828 cm 2 ) are installed facing each other and transferred The pipe | tube used as the path | route 20 was immersed in the to-be-processed muddy water tank 34 through the three-way valve | bulb 28. FIG. The filter cloth was connected to the opening 30 by the pipe 16 and connected to the suction side of the vacuum suction device 14 via the three-way valves 24 and 26. The three-way valve 26 and the three-way valve 28 were connected by a pipe 22. On both surfaces of each flat filter cloth, a net-like rigid member (width 110 mm × height 250 mm) was installed as the swelling suppression member 36.

ろ過槽10を密閉し、三方バルブ28を被処理濁水槽34とろ過槽10の開口部32との連通状態、三方バルブ24,26をろ過槽10の開口部30と真空吸引装置14との連通状態として、真空吸引を開始するとろ布を介してろ過槽10内に負圧が形成され、被処理濁水槽34の濁水がろ過槽10内のろ布上端まで上昇した。ろ過水が系外に排出されても常にこの状態が保たれ(水位一定)、ろ過処理を継続した。   The filtration tank 10 is sealed, the three-way valve 28 is in communication with the muddy water tank 34 to be treated and the opening 32 of the filtration tank 10, and the three-way valves 24 and 26 are in communication with the opening 30 of the filtration tank 10 and the vacuum suction device 14. When vacuum suction was started as a state, a negative pressure was formed in the filtration tank 10 through the filter cloth, and the muddy water in the muddy water tank 34 to be treated rose to the upper end of the filter cloth in the filtration tank 10. Even if filtered water was discharged out of the system, this state was always maintained (the water level was constant), and the filtration process was continued.

真空吸引装置14を作動させたまま、図3に示すように、三方バルブ26,28をろ過槽10の開口部32と真空吸引装置14との連通状態として、三方バルブ24を大気側とろ過槽10の開口部30との連通状態とした。ろ過槽10の上部に形成される負圧により、大気が三方バルブ24の開口部から吸引され(吸気量:約400L/min)、ろ過材12を介して大気が排出されることにより、ろ過材12の表面に付着していた汚泥等の懸濁物質が剥離して落下した。   As shown in FIG. 3, with the vacuum suction device 14 being operated, the three-way valves 26 and 28 are in communication with the opening 32 of the filtration tank 10 and the vacuum suction device 14, and the three-way valve 24 is connected to the atmosphere side and the filtration tank. The communication with 10 openings 30 was established. Due to the negative pressure formed in the upper part of the filtration tank 10, the air is sucked from the opening of the three-way valve 24 (intake amount: about 400 L / min), and the air is discharged through the filter medium 12. Suspended substances such as sludge adhering to the surface of 12 peeled off.

このように、コンプレッサ等の送気装置を用いず、真空吸引手段を用いる簡易な構成で濁水の濃縮を行うことができた。また、膨らみ抑制部材により、ろ布の膨らみが抑制された。   Thus, it was possible to concentrate turbid water with a simple configuration using a vacuum suction means without using an air supply device such as a compressor. Moreover, the swelling of the filter cloth was suppressed by the swelling suppressing member.

1 濁水処理装置、3 濁水処理システム、10 ろ過槽、12 ろ過材、14 真空吸引装置、16,22 配管、20 移送流路、24,26,28 三方バルブ、30,30a,30b,32 開口部、34 被処理濁水槽、36 膨らみ抑制部材、38 内筒管、40,42,44 バルブ、46 排出口、50 ろ室、52 貼り合わせ部、54 下部集水管、60 貯水槽、62 ろ過処理装置。   DESCRIPTION OF SYMBOLS 1 Turbid water treatment apparatus, 3 Turbid water treatment system, 10 Filtration tank, 12 Filter material, 14 Vacuum suction apparatus, 16, 22 Piping, 20 Transfer flow path, 24, 26, 28 Three-way valve, 30, 30a, 30b, 32 Opening part , 34 Muddy water tank to be treated, 36 Swelling suppression member, 38 Inner tube, 40, 42, 44 Valve, 46 Discharge port, 50 Filtration chamber, 52 Laminating section, 54 Lower water collection pipe, 60 Water storage tank, 62 Filtration treatment device .

Claims (4)

懸濁物質を含む濁水を処理するための濁水処理装置であって、
濁水をろ過するためのろ過槽と、
前記濁水の貯留源と前記ろ過槽の上部とを接続する移送流路と、
前記ろ過槽中の濁水に浸漬してろ過処理を行うための少なくとも1つの中空状のろ過材と、
吸引側が前記移送流路の途中および前記ろ過材の内部に接続された真空吸引手段と、
を備え、
前記移送流路の途中と前記真空吸引手段の吸引側とを非連通状態とし、前記濁水の貯留源と前記ろ過槽の上部とを連通状態とし、かつ前記ろ過材の内部と前記真空吸引手段の吸引側とを連通状態とし、その他は前記ろ過槽を密閉した状態で、前記真空吸引手段により真空吸引することによって前記ろ過材を介して前記ろ過槽内に負圧を形成することにより前記濁水を前記ろ過槽内に取り込み、前記ろ過材を前記濁水中に浸漬させた状態で、前記濁水をろ過して前記ろ過材の表面に前記懸濁物質を付着させた後、
前記濁水の貯留源と前記ろ過槽の上部とを非連通状態とし、前記ろ過槽の上部と前記真空吸引手段の吸引側とを連通状態とし、前記ろ過材の内部と前記真空吸引手段の吸引側とを非連通状態とし、かつ前記ろ過材の内部を大気側と連通状態とし、その他は前記ろ過槽を密閉した状態で前記真空吸引手段により前記ろ過材の内部に大気を取り込み、前記ろ過材を前記濁水に浸漬させた状態で、その大気を前記ろ過材の外部に排出することにより前記ろ過材の表面に付着した懸濁物質を剥離することを特徴とする濁水処理装置。
A muddy water treatment device for treating muddy water containing suspended matter,
A filtration tank for filtering muddy water;
A transfer flow path connecting the muddy water storage source and the upper part of the filtration tank;
At least one hollow filter medium for performing a filtration treatment by immersing in muddy water in the filtration tank;
A vacuum suction means whose suction side is connected in the middle of the transfer flow path and inside the filter medium;
With
The middle of the transfer flow path and the suction side of the vacuum suction means are in a non-communication state, the turbid water storage source and the upper part of the filtration tank are in a communication state, and the inside of the filter medium and the vacuum suction means The suction side is in a communicating state, and the other is in a state where the filtration tank is sealed, and the turbid water is formed by forming a negative pressure in the filtration tank through the filter medium by vacuum suction by the vacuum suction means. Incorporated into the filtration tank, in a state where the filter medium is immersed in the muddy water, after filtering the muddy water and attaching the suspended matter to the surface of the filter medium,
The turbid water storage source and the upper part of the filtration tank are in a non-communication state, the upper part of the filtration tank and the suction side of the vacuum suction means are in a communication state, and the inside of the filter medium and the suction side of the vacuum suction means to separate the the non-communicated state, and the inside of the filter media to the atmosphere side and the communication with other takes the air inside the filtering material by the vacuum suction means in a closed state of the filter tank, the filter media A muddy water treatment apparatus, wherein the suspended matter attached to the surface of the filter medium is peeled off by discharging the air to the outside of the filter medium in a state of being immersed in the muddy water.
請求項1に記載の濁水処理装置であって、
前記ろ過材が内部に位置するように設置され、上端および下端が開口する内筒管を備えることを特徴とする濁水処理装置。
The muddy water treatment device according to claim 1,
A muddy water treatment apparatus comprising an inner tube having an upper end and a lower end that are installed so that the filter medium is located inside.
請求項1または2に記載の濁水処理装置であって、
前記剥離の際の前記ろ過材の膨らみを抑制するための貼り合わせ部または膨らみ抑制部材を備えることを特徴とする濁水処理装置。
The muddy water treatment apparatus according to claim 1 or 2,
A muddy water treatment apparatus comprising a bonding portion or a swelling suppressing member for suppressing swelling of the filter medium during the peeling.
懸濁物質を含む濁水を処理するための濁水処理方法であって、
濁水をろ過するためのろ過槽中に少なくとも1つの中空状のろ過材を設置して、前記濁水の貯留源と前記ろ過槽の上部とを移送流路で接続し、吸引側が前記移送流路の途中および前記ろ過材の内部に接続された真空吸引手段を用い、前記移送流路の途中と前記真空吸引手段の吸引側とを非連通状態とし、前記濁水の貯留源と前記ろ過槽の上部とを連通状態とし、かつ前記ろ過材の内部と前記真空吸引手段の吸引側とを連通状態とし、その他は前記ろ過槽を密閉した状態で、真空吸引することによって前記ろ過材を介して前記ろ過槽内に負圧を形成することにより前記濁水を前記ろ過槽内に取り込み、前記ろ過材を前記濁水中に浸漬させた状態で、前記濁水をろ過して前記ろ過材の表面に前記懸濁物質を付着させた後、
前記濁水の貯留源と前記ろ過槽の上部とを非連通状態とし、前記ろ過槽の上部と前記真空吸引手段の吸引側とを連通状態とし、前記ろ過材の内部と前記真空吸引手段の吸引側とを非連通状態とし、かつ前記ろ過材の内部を大気側と連通状態とし、その他は前記ろ過槽を密閉した状態で前記真空吸引手段により真空吸引することによって前記ろ過材の内部に大気を取り込み、前記ろ過材を前記濁水に浸漬させた状態で、その大気を前記ろ過材の外部に排出することにより前記ろ過材の表面に付着した懸濁物質を剥離することを特徴とする濁水処理方法。
A muddy water treatment method for treating muddy water containing suspended matter,
At least one hollow filter medium is installed in a filtration tank for filtering turbid water, the storage source of the turbid water and the upper part of the filtration tank are connected by a transfer channel, and the suction side is the transfer channel. Using vacuum suction means connected in the middle and inside the filter medium, the middle of the transfer flow path and the suction side of the vacuum suction means are in a non-communication state, the turbid water storage source and the upper part of the filtration tank, And the inside of the filter medium and the suction side of the vacuum suction means are in a communication state, and the others are in a state where the filter tank is hermetically sealed, and the filter tank is passed through the filter medium by vacuum suction. The turbid water is taken into the filtration tank by forming a negative pressure therein, and the suspended matter is filtered on the surface of the filter medium by filtering the turbid water in a state where the filter medium is immersed in the muddy water. After attaching
The turbid water storage source and the upper part of the filtration tank are in a non-communication state, the upper part of the filtration tank and the suction side of the vacuum suction means are in a communication state, and the inside of the filter medium and the suction side of the vacuum suction means And the inside of the filter medium is in communication with the atmosphere side, and the others are taken in the atmosphere of the filter medium by vacuum suction with the vacuum suction means with the filter tank sealed. A turbid water treatment method characterized in that the suspended material adhering to the surface of the filter medium is peeled off by discharging the air to the outside of the filter medium in a state where the filter medium is immersed in the muddy water.
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