JP3388378B2 - Filtration equipment - Google Patents

Filtration equipment

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Publication number
JP3388378B2
JP3388378B2 JP06302095A JP6302095A JP3388378B2 JP 3388378 B2 JP3388378 B2 JP 3388378B2 JP 06302095 A JP06302095 A JP 06302095A JP 6302095 A JP6302095 A JP 6302095A JP 3388378 B2 JP3388378 B2 JP 3388378B2
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JP
Japan
Prior art keywords
activated carbon
layer
water
sand
filtration
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Expired - Fee Related
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JP06302095A
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Japanese (ja)
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JPH08257312A (en
Inventor
義教 野嶋
有美子 田辺
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Maezawa Industries Inc
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Maezawa Industries Inc
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Priority to JP06302095A priority Critical patent/JP3388378B2/en
Publication of JPH08257312A publication Critical patent/JPH08257312A/en
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Publication of JP3388378B2 publication Critical patent/JP3388378B2/en
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Expired - Fee Related legal-status Critical Current

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  • Filtration Of Liquid (AREA)
  • Water Treatment By Sorption (AREA)

Description

【発明の詳細な説明】 【0001】 【産業上の利用分野】本発明は、浄水施設に設けられて
いる濾過池や濾過槽等の濾過設備に関し、特に、濾材層
の洗浄を効率よく行うための構造に関する。 【0002】 【従来の技術及び発明が解決しようとする課題】図
示すように、浄水施設は、一般に、河川等から沈砂池1
を介して着水井2に取込んだ水に凝集剤Aや酸化剤Bを
注入し、凝集沈殿池3でフロックを分離した後、さら
に、濾過設備4で水中の懸濁物質を除去し、消毒剤Cを
注入して清浄な水とし、これを配水池5から供給するよ
うに構成されている。 【0003】このような浄水施設において、原水の有機
汚濁等が進行している場合には、上記設備に加えて、各
種有機物やアンモニア等を除去するための生物処理設備
や、脱臭,脱色,殺菌及びBODやCODの除去に効果
があるオゾン処理設備、さらに、異臭味等を除去する活
性炭処理設備等の高度浄水処理設備を設けるようにして
いる。 【0004】しかしながら、新設の浄水施設では、原水
の水質に応じて当初から上記のような高度浄水処理設備
を設置することができるが、既設の浄水施設では、スペ
ース的に上記各種の高度処理設備を付加することが困難
である。 【0005】このため、既設の浄水設備においては、凝
集,沈殿,砂濾過という通常の浄水処理では除去できな
い異臭味原因物質,合成洗剤,フェノール類,トリハロ
メタン及びその前駆物質,トリクロロエチレン等の低沸
点有機塩素化合物,農薬等の微量有害物質,水源域での
事故等により一時的に混入する化学物質,その他の有害
物を除去することができる活性炭を前記着水井2等に投
入し、これらの物質を除去するようにしているが、この
とき用いる活性炭としては、200メッシュ程度のいわ
ゆる粉末活性炭が用いられている。 【0006】上記粉末活性炭を用いた処理は、既設の施
設をそのままの状態で使用できるだけでなく、活性炭処
理が短期間の場合には経済的であるなどの利点を有して
いるものの、長期的に使用する場合には不経済になり、
また、活性炭を含む黒色のスラッジが発生するため、そ
の廃棄や処理管理に特別な注意を払う必要があった。 【0007】一方、活性炭として粒径が0.2mm以上
の粒状活性炭を用いる場合は、活性炭の再生処理を行う
ことにより繰返して使用することができるため、長期間
の使用でも経済的であり、スラッジの発生もないため、
処理管理も容易であるという利点がある。 【0008】ところが、上記粒状活性炭を用いる場合
は、通常、活性炭専用の濾過槽を別個に設置する必要が
あるため、前述のように既設の浄水施設には対応するこ
とができなかった。すなわち、活性炭濾過設備を既設の
浄水施設に新たに設置する場合は、例えば、既設の濾過
設備(砂濾過池)の半分を活性炭濾過池として利用する
ことになるので、通常の濾過設備の処理能力が半減して
しまい、浄水施設全体の浄水能力が1/2に落ちてしま
うことになる。これは、他の設備部分に活性炭濾過設備
を設置した場合も略同様であり、浄水設備の処理能力を
大幅に悪化させることになる。さらに、ポンプ等の付帯
設備を新設したり、変更したりする必要が生じることが
あり、コスト的な問題も発生する。 【0009】そこで本発明は、既設の浄水施設に設けら
れている濾過池や濾過槽等の濾過設備をそのままの状態
で使用しながら活性炭処理を行うことができ、しかも、
粒状活性炭を用いて再生使用することが可能で、濾材層
の洗浄も効率よく行うことができる濾過設備を提供する
ことを目的としている。 【0010】 【課題を解決するための手段】上記した目的を達成する
ため、本発明の濾過設備は、濾材層の上方から被処理水
を供給し、濾材層の下方から処理水を導出する濾過池あ
るいは濾過槽等の濾過設備において、前記濾材層を、下
方から砂利層、砂層、粒状活性炭層の順に積層して形成
し、濾材層の上部に、洗浄用水供給源に接続される主管
を設け、該主管から複数の枝管を分岐し、するととも
に、濾材層の上部に設けた主管から複数の枝管を分岐
し、該枝管の先端部を前記砂利層に開口させている。 【0011】そして、前記枝管の中間部に、前記主管か
ら供給される洗浄用水を駆動源として、別に設けた空気
供給管からの空気を吸引するエジェクターを備えるとと
もに、前記枝管の先端開口部に水空気混合物を噴出する
ノズルを備えていることを特徴とするものである。 【0012】特に本発明は、上記濾過設備が既設の砂濾
過池であり、濾材層を構成する砂の一部を抜き取って、
ここに所定の厚さで粒状活性炭を敷設して粒状活性炭層
を形成した濾過設備において、一般の砂濾過池に設けら
れている表面洗浄管を主管としてそのまま使用し、該
管を既設の洗浄用水供給源に接続したまま、濾材層下部
の砂利層に至る枝管の中間部に空気吸引用のエジェクタ
ーを設け、主管から供給される水流を駆動源としてエジ
ェクターで空気を吸引し、この空気を枝管先端部のノズ
ルから空気洗浄用として噴出させるように構成したもの
である。 【0013】 【作 用】上記構成によれば、被処理水は、粒状活性炭
層で活性炭処理されて異臭味物質等が除去された後、通
常の砂濾過により濾過処理が行われる。また、濾材を逆
流洗浄する際に、逆洗水を供給するとともに、枝管の先
端部から水空気混合物を噴出させることにより、通常の
逆洗と空気洗浄とを行うことができる。特に、既設の濾
過池において、砂層の上部を粒状活性炭層に変更する改
造を行った場合は、濾材層の厚さが増して深層濾過の傾
向が強まることから、濾材層の洗浄に空気洗浄を行うこ
とにより、十分な洗浄効果を得ることができる。 【0014】そして、既設の濾過設備を上記構成に改造
した場合は、既設の濾過設備に設けられている表面洗浄
管を上記主管として用いることにより、大きな改造を施
すことなく容易に空気洗浄を行うことができる。 【0015】 【実施例】以下、本発明を、図面に示す実施例に基づい
てさらに詳細に説明する。図1は、本発明を適用した濾
過設備としての砂濾過池の一実施例を示すものであっ
て、既設の砂濾過池を活性炭処理併用方式に改造した実
施例を示すものである。 【0016】この砂濾過池11は、底部に設けた有孔ブ
ロック形の集水装置12の上に、砂利層13,砂層1
4,粒状活性炭層15を積層配置するとともに、底部に
逆洗水導入管を兼ねる処理水流出管16を、上部に被処
理水流入管18及び逆洗水排出用の排水トラフ19をそ
れぞれ設けたもので、粒状活性炭層15内には、空気洗
浄用の複数の枝管20を有する主管21が設けられてい
る。 【0017】上記砂濾過池11は、粒状活性炭層15が
無く、砂層14が図より多い状態で通常の砂濾過池とし
て用いられていた既設のものであって、砂層14の一部
を取り去って粒状活性炭層15を設けたものである。ま
た、上記主管21は、砂層14の表面を洗浄するための
表面洗浄管として使用されていたものであって、以前の
砂層14のやや上方に設けられていたものである。 【0018】すなわち、本実施例に示す砂濾過池11
は、例えば、支持材である砂利層13を200mm、砂
層14を600〜700mmの厚さとして通常の砂濾過
池として用いられていた既設の設備であって、本実施例
では、砂層14の砂を200〜300mm抜いて厚さを
400mmにするとともに、該砂層14の上面に粒状活
性炭層15を、700mmの厚さに敷設したものであ
る。 【0019】そして、上記粒状活性炭層15を設けるた
めの濾材層の改造を実施するのに伴い、表面洗浄管とし
て使用されていた主管21に、先端が前記砂利層13内
に至る複数の枝管20を所定間隔で分岐形成し、該枝管
20の中間部に空気吸引用のエジェクター31を設け、
該エジェクター31により洗浄用の空気を吸引して枝管
先端のノズル32から水空気混合物を噴出させるように
構成したものである。 【0020】上記エジェクター31は、主管21から供
給される洗浄用水を駆動源として、別に設けた空気供給
管33から空気を吸引するものであって、駆動源となる
洗浄用水は、主管21を表面洗浄管として使用していた
ときと同じ供給源から供給される水を利用することがで
きる。すなわち、本実施例は、上述のように、既設の砂
濾過池に粒状活性炭層15を設ける改造を実施するのに
伴い、表面洗浄管として使用されていた主管21に、先
端に砂利層13内に配置されるノズル32を有し、か
つ、中間部にエジェクター31を有する複数の枝管20
を所定間隔で分岐形成するとともに、前記エジェクター
31に空気供給管33を設けたものである。このように
構成することにより、主管21に接続されていた表面洗
浄用の給水設備をそのままの状態で使用することがで
き、新たな動力を用いることなしに、空気洗浄を行うこ
とが可能になる。 【0021】このように、砂利層13内にノズル32を
設けて水空気混合物を噴出させることにより、砂層14
及び粒状活性炭層15からなる濾材層の厚さが以前に比
べて増大しても、逆洗時に処理水排出管16から逆洗水
を導入するとともに、ノズル22から水空気混合物を噴
出することにより、砂層14の砂及び粒状活性炭層15
の粒状活性炭を効率よく逆洗することができる。 【0022】また、上記粒状活性炭層15に用いる活性
炭としては、その粒径が1.2〜1.5mmの範囲の粒
状活性炭を用いることが好ましい。この粒径範囲の粒状
活性炭を用いることにより、粒状活性炭の沈降速度を砂
に比べて僅かに遅いか、あるいは同じ程度にすることが
でき、砂層14及び粒状活性炭層15の逆洗の際に適切
な膨張を得ることが可能となる。しかも、処理能力や通
水抵抗も適切な値とすることが可能であり、濾過速度
を、砂濾過池11として適当な範囲である120〜15
0m/日に保つことができる。例えば、粒状活性炭の径
が小さいと沈降速度が遅くなり、逆洗水の上昇に伴って
活性炭が排水トラフ19部分まで上昇してしまい、排水
トラフ19から逆洗水と共に活性炭が流出してしまう。
さらに、径が小さすぎると、通水抵抗が増加して処理水
量にも影響を与えることになる。一方、粒径が大きいと
活性炭の洗浄時の膨張が小さくなり、洗浄効果が不十分
となる。また、活性炭の単位容量当たりの能力も低下す
る。 【0023】上述のように、砂層14の上面に粒状活性
炭層15を設けることにより、砂濾過池11とは別に活
性炭処理槽を設けることなく、被処理水の活性炭処理を
行うことができる。このとき、粒状活性炭自体も濾材の
一部として作用するので、砂層14の一部を抜いて砂層
自体の厚みが減少した状態でも、砂層14の上面に粒状
活性炭層15が存在するので、砂濾過池11としての濾
過能力はむしろ向上し、活性炭処理と濾過処理とを同時
に行うことができる。 【0024】なお、粒状活性炭層15の厚さは、濾過速
度と空間速度との関係で決定すればよく、排水トラフ1
9の上下位置は、決定した粒状活性炭層15の厚さでの
逆洗による膨張,逆洗速度,濁質の終端速度の関係から
決定すればよい。 【0025】上記実施例に示すように、通常の砂濾過池
11の砂層14の上面に、粒径が1.2〜1.5mmの
粒状活性炭を用いた粒状活性炭層15を所定の厚さで敷
設することにより、濾過処理に加えて活性炭処理も同時
に行うことができ、さらに、空気洗浄を実施可能な構造
にすることにより、十分な洗浄効果も得られる。また、
既設の砂濾過池11においても、砂層14の砂の一部を
粒状活性炭に入替えるとともに、通常設置されている表
面洗浄管を洗浄用空気導入部として利用することによ
り、容易に実施することが可能であり、設備自体を大幅
に変更することなく被処理水の活性炭処理を行うことが
でき、被処理水中の異臭味物質等を除去することができ
る。 【0026】また、上記粒径範囲の粒状活性炭を用いて
所定の期間毎に該活性炭を取出して再生処理を行うこと
により、活性炭自体を長期間にわたって使用することが
できるとともに、スラッジの発生もないため、維持管理
も容易である。 【0027】さらに、既設の設備においても、砂層14
の砂の一部を粒状活性炭に入替え、粒状活性炭層15の
厚さに応じて排水トラフ19の位置を変更するととも
に、表面洗浄管に枝管20を設けて表面洗浄管をブロア
ー等に接続するだけでよく、洗浄ポンプ,流量計等の逆
洗用付帯設備は既設のものをそのまま使用することがで
きるので、活性炭処理を追加することによるコストも僅
かなもので済む。 【0028】したがって、既設の浄水施設に設けられて
いる砂濾過池に大幅な変更を加えることなく、そのまま
の状態で活性炭処理を行うことができ、既設の浄水施設
の改善を図れるが、新設の浄水施設にも同様に適用する
ことができる。 【0029】 【0030】 【0031】 【0032】なお、上記実施例では、本発明の特に好ま
しい態様として、既設の濾過設備を改造する例を挙げて
説明したが、新設のものに同様の構造を採用することも
可能である。 【0033】 【発明の効果】以上説明したように、本発明の濾過設備
は、濾材層の上面に粒状活性炭層を敷設したので、別途
活性炭処理設備を設けることなく活性炭処理を行うこと
ができ、特に、既設の濾過設備を、活性炭処理と濾過処
理とを行う設備として容易に転用することができる。ま
た、空気噴出手段により、濾材層の厚さが増しても十分
な洗浄効果を得ることができる。 【0034】したがって、既設の浄水施設でも容易に活
性炭処理を行うことができ、しかも、粉末活性炭を用い
ずに粒状活性炭を用いているので、連続的に安全な処理
ができ、活性炭の再生処理を行うことにより繰返して使
用することができるため、長期間の処理でも経済的であ
り、スラッジの発生もないため、維持管理も容易であ
る。
Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a filter facility such as a filter pond and a filter tank provided in a water purification facility, and more particularly to a method for efficiently cleaning a filter medium layer. Related to the structure. 2. Description of the Related Art As shown in FIG. 2 , a water purification facility is generally provided with a sand basin 1 from a river or the like.
The flocculant A and the oxidant B are injected into the water taken into the landing well 2 through the, and the floc is separated in the flocculation settling basin 3. It is configured to inject the agent C to make clean water and supply it from the reservoir 5. [0003] In such a water purification facility, when the organic pollution of the raw water is progressing, in addition to the above facilities, a biological treatment facility for removing various organic substances, ammonia, etc., a deodorization, a decolorization, and a sterilization. Ozone treatment equipment that is effective in removing BOD and COD, and advanced water purification treatment equipment such as activated carbon treatment equipment that removes off-flavors and the like are provided. [0004] However, in a newly constructed water purification facility, the above-mentioned advanced water treatment facilities can be installed from the beginning according to the quality of the raw water. Is difficult to add. [0005] For this reason, in existing water purifying equipment, low-boiling organic compounds such as off-flavor-causing substances, synthetic detergents, phenols, trihalomethanes and their precursors, and trichloroethylene which cannot be removed by ordinary water purification treatments such as coagulation, sedimentation and sand filtration. Activated carbon capable of removing trace harmful substances such as chlorine compounds and pesticides, chemical substances temporarily mixed in accidents in water source areas, and other harmful substances is put into the landing well 2 and the like. In this case, so-called powdered activated carbon of about 200 mesh is used as the activated carbon used at this time. [0006] The treatment using the activated carbon powder has the advantages that not only can the existing facility be used as it is, but it is economical when the activated carbon treatment is carried out for a short period of time, but it has a long-term advantage. It becomes uneconomical when used for
In addition, black sludge containing activated carbon is generated, so that special attention must be paid to disposal and treatment management. On the other hand, when granular activated carbon having a particle size of 0.2 mm or more is used as the activated carbon, the activated carbon can be used repeatedly by regenerating the activated carbon. Because there is no occurrence of
There is an advantage that processing management is easy. However, when the above-mentioned granular activated carbon is used, it is usually necessary to separately install a filtration tank dedicated to activated carbon, so that it was not possible to cope with the existing water purification facility as described above. That is, when newly installing activated carbon filtration equipment in an existing water purification facility, for example, half of the existing filtration equipment (sand filtration pond) will be used as the activated carbon filtration pond. And the water purification capacity of the whole water purification facility is reduced by half. This is substantially the same when the activated carbon filtration equipment is installed in another equipment part, and the processing capacity of the water purification equipment is greatly deteriorated. Further, it may be necessary to newly install or change ancillary equipment such as a pump, which may cause a cost problem. Therefore, the present invention can perform the activated carbon treatment while using the filtration facilities such as a filtration pond and a filtration tank provided in an existing water purification facility as they are, and
It is an object of the present invention to provide a filtration facility that can be reused by using granular activated carbon and that can efficiently clean a filter medium layer. [0010] In order to achieve the above-mentioned object, the filtration equipment of the present invention is a filtration equipment for supplying water to be treated from above a filter medium layer and extracting treated water from below the filter medium layer. In a filtration facility such as a pond or a filtration tank, the filter medium layer is formed by laminating a gravel layer, a sand layer, and a granular activated carbon layer in this order from below , and a main pipe connected to a washing water supply source is provided above the filter medium layer. branches a plurality of branch pipes from the main pipe, as well as branches a plurality of branch pipes from the main pipe provided in the upper portion of the filter layer, and the tip of the branches pipe is opened to the gravel layer. [0011] Then, the intermediate portion of the branch pipe, as a drive source a washing water supplied from the main pipe provided with a ejector for sucking air from the air supply pipe which is provided separately from the tip opening of the branch pipe And a nozzle for jetting a water-air mixture. [0012] In particular, the present invention relates to the present invention, wherein the above-mentioned filtering equipment is an existing sand filter, and a part of the sand constituting the filter medium layer is extracted.
In filtration equipment forming the granular activated carbon layer by laying the granular activated carbon where a predetermined thickness, as it uses the surface cleaning tube is provided in the common sand filter as main, the main <br/> tube With the connected to the existing washing water supply source, an ejector for air suction is installed in the middle of the branch pipe to the gravel layer below the filter medium layer, and the ejector sucks air using the water flow supplied from the main pipe as a drive source. This air is ejected from the nozzle at the tip of the branch pipe for air cleaning. According to the above arrangement, the water to be treated is treated with activated carbon in a granular activated carbon layer to remove off-flavor substances and the like, and then subjected to a filtration treatment by ordinary sand filtration. Further, when the backwashing the filter medium, supplies the backwash water by jetting tip or et water air mixture of the lateral pipe, it is possible to perform the air cleaning regular backwashing. In particular, if the existing filter pond is modified to change the upper part of the sand layer to a granular activated carbon layer, the filter medium layer will be thickened and the tendency of deep filtration will increase. By doing so, a sufficient cleaning effect can be obtained. When the existing filtration equipment is modified to the above configuration, the air cleaning can be easily performed without major modification by using the surface cleaning pipe provided in the existing filtration equipment as the main pipe. be able to. DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below in more detail with reference to embodiments shown in the drawings. FIG. 1 shows an embodiment of a sand filtration pond as a filtration facility to which the present invention is applied, and shows an embodiment in which an existing sand filtration pond is modified into a method using a combination of activated carbon treatment. The sand filter 11 is provided with a gravel layer 13 and a sand layer 1 on a perforated block type water collecting device 12 provided at the bottom.
4, a granular activated carbon layer 15 is stacked and arranged, a treated water outflow pipe 16 also serving as a backwash water introduction pipe is provided at the bottom, and a treated water inflow pipe 18 and a drainage trough 19 for backwash water discharge are provided at the top. A main pipe 21 having a plurality of branch pipes 20 for cleaning air is provided in the granular activated carbon layer 15. The sand filtration basin 11 is an existing sand filtration basin that has been used as an ordinary sand filtration basin without the granular activated carbon layer 15 and the sand layer 14 is larger than that shown in the figure. This is provided with a granular activated carbon layer 15. Further, the main pipe 21 is used as a surface cleaning pipe for cleaning the surface of the sand layer 14 and is provided slightly above the previous sand layer 14. That is, the sand filtration pond 11 shown in this embodiment
Is an existing facility used as a normal sand filter with a thickness of the gravel layer 13 as a support material of 200 mm and a thickness of the sand layer 14 of 600 to 700 mm. In the present embodiment, the sand of the sand layer 14 is used. Is removed by 200 to 300 mm to 400 mm in thickness, and a granular activated carbon layer 15 is laid on the upper surface of the sand layer 14 to a thickness of 700 mm. Along with the remodeling of the filter medium layer for providing the granular activated carbon layer 15, a plurality of branch pipes each having a tip extending into the gravel layer 13 are added to the main pipe 21 used as a surface cleaning pipe. 20 branches formed at predetermined intervals, said branch pipe
An ejector 31 for air suction is provided at an intermediate portion of 20,
The cleaning air is sucked by the ejector 31 and the branch pipe is drawn.
So that the water-air mixture is ejected from the tip nozzle 32
It is composed . The ejector 31 is supplied from the main pipe 21.
Separate air supply using the supplied cleaning water as a drive source
It sucks air from the pipe 33 and becomes a driving source
The cleaning water used the main pipe 21 as a surface cleaning pipe.
Water from the same source can be used
Wear. That is, as described above, the present embodiment
To carry out the remodeling to provide a granular activated carbon layer 15 in the filtration pond
Accordingly, the main pipe 21 used as the surface cleaning pipe is
At the end there is a nozzle 32 arranged in the gravel layer 13,
A plurality of branch pipes 20 having an ejector 31 in the middle part
At predetermined intervals, and the ejector
31 is provided with an air supply pipe 33. in this way
By configuring, the surface cleaning connected to the main pipe 21 can be performed.
The water supply system for purification can be used as it is.
Air cleaning without using new power.
And become possible . As described above, the nozzle 32 is provided in the gravel layer 13.
The sand layer 14
And the thickness of the filter medium layer composed of the granular activated carbon layer 15 is
Even if all of them increase, backwash water flows from treated water discharge pipe 16 during backwash.
And a jet of water-air mixture from nozzle 22
The sand and the granular activated carbon layer 15 of the sand layer 14 are discharged.
Can be efficiently backwashed . The activity used for the granular activated carbon layer 15
As charcoal, granules with a particle size in the range of 1.2 to 1.5 mm
Preferably, activated carbon is used. Granularity in this particle size range
By using activated carbon, the settling velocity of granular
Slightly slower or about the same as
Suitable for backwashing of sand layer 14 and granular activated carbon layer 15
It is possible to obtain a proper expansion. Moreover, processing capacity and communication
Water resistance can also be set to an appropriate value, and filtration speed
From 120 to 15 which is a suitable range for the sand filtration pond 11.
0 m / day. For example, if the diameter of the granular activated carbon is small, the sedimentation speed becomes slow, the activated carbon rises to the drainage trough 19 with the rise of the backwash water, and the activated carbon flows out of the drainage trough 19 together with the backwash water.
Further, if the diameter is too small, the flow resistance increases, which affects the amount of treated water. On the other hand, if the particle size is large, the expansion of the activated carbon during cleaning becomes small, and the cleaning effect becomes insufficient. In addition, the capacity per unit capacity of the activated carbon is reduced. As described above, by providing the granular activated carbon layer 15 on the upper surface of the sand layer 14, it is possible to perform the activated carbon treatment of the water to be treated without providing an activated carbon treatment tank separately from the sand filtration pond 11. At this time, the granular activated carbon itself also acts as a part of the filter medium. Therefore, even if the sand layer 14 is partially removed and the thickness of the sand layer itself is reduced, the granular activated carbon layer 15 is present on the upper surface of the sand layer 14. The filtration capacity of the pond 11 is rather improved, and the activated carbon treatment and the filtration treatment can be performed simultaneously. The thickness of the granular activated carbon layer 15 may be determined according to the relationship between the filtration rate and the space velocity.
The upper and lower positions of 9 may be determined from the relationship between the expansion due to backwashing at the determined thickness of the granular activated carbon layer 15, the backwash speed, and the terminal speed of the turbid matter. As shown in the above embodiment, a granular activated carbon layer 15 using a granular activated carbon having a particle size of 1.2 to 1.5 mm is formed on the upper surface of the sand layer 14 of the ordinary sand filtration pond 11 at a predetermined thickness. By laying, the activated carbon treatment can be performed simultaneously in addition to the filtration treatment, and a sufficient cleaning effect can be obtained by adopting a structure capable of performing air cleaning. Also,
Even in the existing sand filter 11, it is possible to easily carry out the process by replacing a part of the sand in the sand layer 14 with granular activated carbon and using a normally installed surface cleaning pipe as a cleaning air introduction unit. Activated carbon treatment of the water to be treated can be performed without greatly changing the equipment itself, and the off-flavor substances and the like in the water to be treated can be removed. Further, by using the granular activated carbon having the above-mentioned particle size range and taking out the activated carbon at predetermined intervals and performing a regeneration treatment, the activated carbon itself can be used for a long period of time and sludge is not generated. Therefore, maintenance is easy. Further, even in the existing facilities, the sand layer 14
Part of the sand is replaced with granular activated carbon, the position of the drainage trough 19 is changed according to the thickness of the granular activated carbon layer 15, and a branch pipe 20 is provided in the surface cleaning pipe to connect the surface cleaning pipe to a blower or the like. It is only necessary to use the existing equipment for backwashing such as a washing pump and a flow meter, so that the cost by adding the activated carbon treatment is small. Therefore, the activated carbon treatment can be carried out without changing the sand filtration pond provided in the existing water purification facility as it is, and the existing water purification facility can be improved. The same can be applied to water purification facilities. [0029] [0030] [0031] [0032] In the above you施例, a particularly preferred embodiment of the present invention has been described by way of example to modify the existing filtration equipment, similar to that of new It is also possible to adopt a structure. As described above, in the filtration equipment of the present invention, the granular activated carbon layer is laid on the upper surface of the filter medium layer, so that the activated carbon treatment can be performed without separately providing activated carbon treatment equipment. In particular, existing filtration equipment can be easily diverted as equipment for performing activated carbon treatment and filtration treatment. Further, even if the thickness of the filter medium layer is increased by the air blowing means, a sufficient cleaning effect can be obtained. Therefore, the activated carbon treatment can be easily performed even in the existing water purification facility, and since the granular activated carbon is used without using the powdered activated carbon, safe treatment can be continuously performed, and the activated carbon can be regenerated. Since it can be used repeatedly by performing, it is economical even for a long-term treatment, and there is no generation of sludge, so that maintenance is easy.

【図面の簡単な説明】 【図1】 本発明の一実施例を示す濾過設備の概略図で
ある。 【図2】 浄水施設の一般的な構成を示す流れ図であ
る。 【符号の説明】 11…砂濾過池、12…集水装置、13…砂利層、14
…砂層、15…粒状活性炭層、16…処理水流出管、1
8…被処理水流入管、19…排水トラフ、20…枝管、
21…主管、31…エジェクター、32…ノズル、33
…空気供給管
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a schematic diagram of a filtration facility showing one embodiment of the present invention. FIG. 2 is a flowchart showing a general configuration of a water purification facility . [Explanation of Signs] 11: sand filter pond, 12: water collecting device, 13: gravel layer, 14
... sand layer, 15 ... granular activated carbon layer, 16 ... treated water outflow pipe, 1
8 ... inflow pipe for treated water, 19 ... drainage trough, 20 ... branch pipe,
21: Main pipe, 31: Ejector, 32: Nozzle, 33
... Air supply pipe

フロントページの続き (58)調査した分野(Int.Cl.7,DB名) B01D 24/02 B01D 24/46 B01D 29/62 C02F 1/28 Continuation of the front page (58) Field surveyed (Int. Cl. 7 , DB name) B01D 24/02 B01D 24/46 B01D 29/62 C02F 1/28

Claims (1)

(57)【特許請求の範囲】 【請求項1】 濾材層の上方から被処理水を供給し、濾
材層の下方から処理水を導出する濾過池あるいは濾過槽
等の濾過設備において、前記濾材層を、下方から砂利
層、砂層、粒状活性炭層の順に積層して形成し、濾材層
の上部に、洗浄用水供給源に接続される主管を設け、該
主管から複数の枝管を分岐し、該枝管の中間部に、前記
主管から供給される洗浄用水を駆動源として、別に設け
た空気供給管からの空気を吸引するエジェクターを備え
るとともに、前記枝管の先端部を前記砂利層に開口さ
、該先端開口部に水空気混合物を噴出するノズルを備
たことを特徴とする濾過設備。
(1) In a filtration facility such as a filter pond or a filter tank for supplying water to be treated from above the filter medium layer and drawing out the treated water from below the filter medium layer, the filter medium layer comprises: Are formed by laminating a gravel layer, a sand layer, and a granular activated carbon layer in this order from below , and a main pipe connected to a cleaning water supply source is provided above the filter medium layer , and a plurality of branch pipes are formed from the main pipe. Branch, in the middle of the branch pipe,
Separately provided with cleaning water supplied from the main pipe as a drive source
Equipped with an ejector that sucks air from the air supply pipe
In addition, a tip end of the branch pipe is opened to the gravel layer, and a nozzle for jetting a water-air mixture is provided at the tip end opening.
Filtration equipment, characterized in that was example.
JP06302095A 1995-03-22 1995-03-22 Filtration equipment Expired - Fee Related JP3388378B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP06302095A JP3388378B2 (en) 1995-03-22 1995-03-22 Filtration equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP06302095A JP3388378B2 (en) 1995-03-22 1995-03-22 Filtration equipment

Publications (2)

Publication Number Publication Date
JPH08257312A JPH08257312A (en) 1996-10-08
JP3388378B2 true JP3388378B2 (en) 2003-03-17

Family

ID=13217230

Family Applications (1)

Application Number Title Priority Date Filing Date
JP06302095A Expired - Fee Related JP3388378B2 (en) 1995-03-22 1995-03-22 Filtration equipment

Country Status (1)

Country Link
JP (1) JP3388378B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001347264A (en) * 2000-06-07 2001-12-18 Shimadzu Corp Water treatment equipment and water treatment method
JP2010158662A (en) * 2008-07-04 2010-07-22 Daikin Ind Ltd Treating method of fluorinated surfactant-containing aqueous solution
CN104399289B (en) * 2014-10-28 2017-06-27 上海市政工程设计研究总院(集团)有限公司 A kind of filter tank air water distributor
CN104984571B (en) * 2015-07-13 2017-10-27 江苏德立环保工程股份有限公司 A kind of high-efficient metallurgical industry waste water purifying device
KR102426331B1 (en) * 2020-03-10 2022-07-29 (주)디아이엔바이로 Porosity filter media for under drain device and Water treatment facility containing the same
CN115403203B (en) * 2022-08-29 2023-09-15 青岛海水淡化有限公司 High-reliability sea water desalting device

Also Published As

Publication number Publication date
JPH08257312A (en) 1996-10-08

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