JPH11123304A - High speed fiber filter for recharge method - Google Patents
High speed fiber filter for recharge methodInfo
- Publication number
- JPH11123304A JPH11123304A JP9290615A JP29061597A JPH11123304A JP H11123304 A JPH11123304 A JP H11123304A JP 9290615 A JP9290615 A JP 9290615A JP 29061597 A JP29061597 A JP 29061597A JP H11123304 A JPH11123304 A JP H11123304A
- Authority
- JP
- Japan
- Prior art keywords
- funnel
- filter
- filter layer
- particles
- cylinder
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Landscapes
- Filtration Of Liquid (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、リチャージ工法に
用いられる高速繊維ろ過装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a high-speed fiber filtration device used in a recharge method.
【0002】[0002]
【従来の技術】地下工事の大規模化は、大量の地下水の
揚水を必要とし、これにともない地下水の揚水による周
辺地盤環境への影響が問題となり、汲み上げた地下水を
元の地下水に還元するリチャージ工法(復水工法)が利
用されるようになってきた。すなわち、図5に示す如
く、リチャージ工法は地下水を揚水するための揚水井1
よりチャンバー2に地下水をポンプPによって吸い上
げ、高速ろ過装置3を介してから復水井4より地下水を
元に戻している。2. Description of the Related Art Large-scale underground construction requires pumping of a large amount of groundwater, and the pumping of groundwater has a problem on the surrounding ground environment. The construction method (condensation method) has come to be used. That is, as shown in FIG. 5, the recharging method uses a pumping well 1 for pumping groundwater.
The groundwater is pumped up into the chamber 2 by the pump P, and the groundwater is returned from the condensing well 4 through the high-speed filtration device 3.
【0003】叙上の高速ろ過装置3は図6に詳示され
る。すなわち、一定直径の筒体3aの中にφ=6〜10
mm、長さ10〜20mmに成形した繊維ろ材3bを0.5
m〜2mの層厚で充填したものである。このものの原水
としてカオリン10ppmを使用した場合の水槽実験の
処理効果の結果を図7に示す。The above-mentioned high-speed filtration device 3 is shown in detail in FIG. That is, φ = 6 to 10 in the cylinder 3a having a constant diameter.
mm, a fiber filter medium 3b formed to a length of 10 to 20 mm
It is filled with a layer thickness of m to 2 m. FIG. 7 shows the results of the treatment effect of the aquarium experiment when 10 ppm of kaolin was used as the raw water.
【0004】ろ層厚の大なる程SS除去率が高まること
が分かる。なを、上記原水カオリン10ppmの粒度分
布については図4に示される通りである。It can be seen that the SS removal rate increases as the thickness of the filter layer increases. Note that the particle size distribution of the raw water kaolin 10 ppm is as shown in FIG.
【0005】[0005]
【発明が解決しようとする課題】しかるに、叙上の現状
モデルの高速ろ過装置3を用いてのリチャージ工法にあ
っては、復水井4周辺の目詰まりによる復水機能の経持
的な低下という難問が生じる。この目詰まりの主な原因
は、揚水中に含まれる微細な懸濁粒子であるが、前記の
図4中には現状モデルのろ過水の粒度分布が示される
が、これによると粒径5μm以上の粒子はある程度除去
できているが、5μm以下の粒子はあまり除去し得てい
ないことが明らかであり、かかる現状タイプの特性によ
って上記の諸難問が生じていることが分かる。However, in the recharging method using the high-speed filtration device 3 of the above-mentioned current model, the condensing function around the condensing well 4 is continuously reduced. A difficult question arises. The main cause of this clogging is fine suspended particles contained in the pumped water. The particle size distribution of the filtered water of the current model is shown in FIG. 4 described above. It is apparent that particles having a particle size of 5 μm or less could not be removed to a certain extent, indicating that the above-mentioned various problems have been caused by the characteristics of the current type.
【0006】本発明は、叙上の事情に鑑みなされたもの
で、その目的とするところは、目詰まりの原因となる微
細懸濁粒子を効果的に除去することのできる高速繊維ろ
過装置を提供することにある。SUMMARY OF THE INVENTION The present invention has been made in view of the above circumstances, and has as its object to provide a high-speed fiber filtration device capable of effectively removing fine suspended particles that cause clogging. Is to do.
【0007】[0007]
【課題を解決するための手段】上記目的を達成するため
に、本発明の高速繊維ろ過装置は、ろ層厚下部が漸次小
径化するように筒体下半をロート状に形成するとしたも
のである。Means for Solving the Problems To achieve the above object, a high-speed fiber filtration device according to the present invention is characterized in that the lower half of the cylindrical body is formed in a funnel shape so that the lower part of the filter layer gradually becomes smaller in diameter. is there.
【0008】[0008]
【作用】本発明のろ過装置にあっては、ろ材は従来のタ
イプと同様のφ=6〜10mm、長さ10〜20mm程度の
圧縮性の繊維ろ材を使用するが、ろ過槽筒体下半がロー
ト状であることにより、その部分のろ過水の流速は速ま
り、ろ材は圧密されて、微細な粒子の捕捉が可能となる
(流速の速まりは除去率の低下をもたらさない。)。こ
こに上下で圧密状態の違ったろ層をつくることができる
ため、粒径の違う懸濁粒子を層別に捕捉できる(上部で
大粒径を下部で小粒径を捕捉)こととなる。In the filtering apparatus of the present invention, a compressible fiber filter medium having a diameter of about 6 to 10 mm and a length of about 10 to 20 mm is used as the filter medium of the conventional type. By having a funnel shape, the flow rate of the filtered water in that part is increased, and the filter medium is compacted, so that fine particles can be captured (an increase in the flow rate does not cause a reduction in the removal rate). Here, since the filter layers having different consolidation states can be formed in the upper and lower portions, suspended particles having different particle sizes can be captured by layer (large particles are captured in the upper portion and small particles are captured in the lower portion).
【0009】このように下半に新たに圧縮性のろ材を圧
密したろ層の小粒径捕捉能を有するフィルターを自動的
に形成し得る結果、不可能であった小粒径の微細な懸濁
粒子を捕捉できるので、復水井周辺の目詰まりを阻止で
きる。[0009] As described above, a filter having a small particle size capturing capability of a filter layer in which a compressible filter medium is newly compacted in the lower half can be automatically formed. Since the suspended particles can be captured, clogging around the condensate well can be prevented.
【0010】[0010]
【発明の実施の形態】本発明の実施の形態を図1に基づ
いて説明する。本発明装置5は、そのろ層5bの下部が
漸次小径化するように筒体5a下半をロート状に形成し
ている。かかるろ層5bの下部に新たに圧密層を形成し
て成る本発明装置5のSS除去率を図2に示す。DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described with reference to FIG. In the device 5 of the present invention, the lower half of the cylindrical body 5a is formed in a funnel shape so that the lower part of the filter layer 5b is gradually reduced in diameter. FIG. 2 shows the SS removal rate of the device 5 of the present invention in which a new consolidation layer is formed below the filter layer 5b.
【0011】前記の図7に示した従来のタイプに比し除
去率は大幅に向上している。さらに、図4の本発明の改
良モデルのろ過水の粒度分布(カオリン10ppm の原水
を用いた水槽実験)をみると、従来タイプでは粒径5μ
m以上の粒子は、ある程度除去できているが、5μm以
下の粒子は、あまり除去できていないのに比し、本発明
のタイプでは、5μm以下の粒子でも測定限界を越えて
除去できていることが分かる。The removal rate is greatly improved as compared with the conventional type shown in FIG. Further, looking at the particle size distribution of the filtered water of the improved model of the present invention shown in FIG.
Particles of m or more could be removed to some extent, but particles of 5 μm or less could not be removed much, but in the type of the present invention, particles of 5 μm or less could be removed beyond the measurement limit. I understand.
【0012】しかして、復水井周辺の目詰まりを確実に
阻止できる。なを、本発明装置にあっては、前記以外の
有利な効果も有してる。すなわち、図3に示す如く、従
来タイプのもの(a)にあっては、ろ材のエアー逆洗々
浄時、一定直径の筒体3aのために、ろ材の局所循環域
6,6を生じ、均一な洗浄を防げるが、本発明の改良タ
イプ(b)にあっては、ロート下端からの吹き上げでろ
材粒子を周壁方向に拡散させる力7が作用して、攪拌が
効果的に行える。Thus, clogging around the condensing well can be reliably prevented. However, the device of the present invention has other advantageous effects other than those described above. That is, as shown in FIG. 3, in the case of the conventional type (a), when the filter medium is backwashed by air, local circulation areas 6 and 6 of the filter medium are generated due to the cylindrical body 3a having a constant diameter. Although uniform washing can be prevented, in the improved type (b) of the present invention, a force 7 for diffusing the filter medium particles in the peripheral wall direction by blowing up from the lower end of the funnel acts, and stirring can be performed effectively.
【0013】このため、攪拌洗浄のために必要とする、
ろ過槽の高さを低くおさえることができる。結局、本発
明にあっては、制限された高さのなかで、有効なろ過層
を厚くでき、微細粒子の捕捉性能があがるという、理想
的な好便さが期し得る。For this reason, it is necessary for stirring cleaning.
The height of the filtration tank can be kept low. As a result, in the present invention, an ideal convenience can be expected in which the effective filtration layer can be thickened within the limited height and the performance of capturing fine particles can be improved.
【0014】[0014]
【発明の効果】以上の如く本発明装置は構成されるの
で、リチャージ工法における復水井周辺の目詰まりを解
消させることができる。As described above, the apparatus of the present invention is constituted, so that clogging around the condensate well in the recharging method can be eliminated.
【図1】本発明装置の全体説明図である。FIG. 1 is an overall explanatory view of the device of the present invention.
【図2】本発明装置の除去率グラフである。FIG. 2 is a graph showing the removal rate of the apparatus of the present invention.
【図3】a,bは従来タイプ,本発明の改良タイプ装置
のエアー逆洗時のろ材粒子の吹き上げ動の説明図であ
る。3 (a) and 3 (b) are explanatory views of a conventional type and an improved type apparatus according to the present invention in which a filter medium particle is blown up during backwashing with air. FIG.
【図4】原水,現状モデルのろ過水,本発明改良モデル
のろ過水の粒度分布グラフである。FIG. 4 is a particle size distribution graph of raw water, filtered water of the current model, and filtered water of the improved model of the present invention.
【図5】リチャージ工法説明図である。FIG. 5 is an explanatory view of a recharge method.
【図6】従来タイプのろ過槽の説明図である。FIG. 6 is an explanatory view of a conventional type filtration tank.
【図7】従来タイプのろ過槽におけるSS除去能力グラ
フである。FIG. 7 is a graph showing the SS removal capability of a conventional type filtration tank.
1 揚水井 2 チャンバー 3 高速ろ過装置 3a 筒体 3b 繊維ろ材 4 復水井 5 装置 5a 筒体 5b ろ層 6 局所循環域 7 拡散させる力 Reference Signs List 1 pumping well 2 chamber 3 high-speed filtration device 3a cylinder 3b fiber filter medium 4 condensing well 5 device 5a cylinder 5b filtration layer 6 local circulation area 7 power to diffuse
Claims (1)
下半をロート状に形成するとしたことを特徴とするリチ
ャージ工法に用いられる高速繊維ろ過装置。1. A high-speed fiber filtration device for use in a recharging method, wherein a lower half of a cylindrical body is formed in a funnel shape so that a lower portion of a filter layer gradually becomes smaller in diameter.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP29061597A JP3637361B2 (en) | 1997-10-23 | 1997-10-23 | High-speed fiber filtration equipment used in the recharge method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP29061597A JP3637361B2 (en) | 1997-10-23 | 1997-10-23 | High-speed fiber filtration equipment used in the recharge method |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH11123304A true JPH11123304A (en) | 1999-05-11 |
JP3637361B2 JP3637361B2 (en) | 2005-04-13 |
Family
ID=17758293
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP29061597A Expired - Lifetime JP3637361B2 (en) | 1997-10-23 | 1997-10-23 | High-speed fiber filtration equipment used in the recharge method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3637361B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007222872A (en) * | 2007-04-26 | 2007-09-06 | Solt Industry Center Of Japan | Filter device |
-
1997
- 1997-10-23 JP JP29061597A patent/JP3637361B2/en not_active Expired - Lifetime
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007222872A (en) * | 2007-04-26 | 2007-09-06 | Solt Industry Center Of Japan | Filter device |
JP4519878B2 (en) * | 2007-04-26 | 2010-08-04 | 財団法人塩事業センター | Filtration device |
Also Published As
Publication number | Publication date |
---|---|
JP3637361B2 (en) | 2005-04-13 |
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