JP3838579B2 - Water purification device - Google Patents

Water purification device Download PDF

Info

Publication number
JP3838579B2
JP3838579B2 JP22258795A JP22258795A JP3838579B2 JP 3838579 B2 JP3838579 B2 JP 3838579B2 JP 22258795 A JP22258795 A JP 22258795A JP 22258795 A JP22258795 A JP 22258795A JP 3838579 B2 JP3838579 B2 JP 3838579B2
Authority
JP
Japan
Prior art keywords
water
water purification
treatment tank
passage
soil layer
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.)
Expired - Lifetime
Application number
JP22258795A
Other languages
Japanese (ja)
Other versions
JPH0947779A (en
Inventor
俊太郎 野口
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Fujita Corp
Original Assignee
Fujita Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Fujita Corp filed Critical Fujita Corp
Priority to JP22258795A priority Critical patent/JP3838579B2/en
Publication of JPH0947779A publication Critical patent/JPH0947779A/en
Application granted granted Critical
Publication of JP3838579B2 publication Critical patent/JP3838579B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Landscapes

  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
  • Cultivation Of Plants (AREA)
  • Treatment Of Biological Wastes In General (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は、生活系排水等の水質浄化の高度処理に用いて好適な水質浄化装置に関する。
【0002】
【従来の技術】
水質浄化を行なうために湿地を用いる水質浄化方法は既に知られている。
このような湿地を用いる水質浄化方法は、従来、排水の流し方から見て大きく次の2種類に分けられる。
▲1▼ 表面流れ方式・・・浄化機能を想定した湿地の表面に処理対象排水を流下させ、湿地末端表面で処理水を集水する方式。
▲2▼ 浸透流れ方式・・・浄化機能を想定した湿地の表面から処理対象排水を流下させ、下部土壌あるいは排水層から処理水を集水する方式。
そして、いづれの方式においても、土壌の物理、化学的作用や土壌中の微生物、植物による吸収などが組み合わさった複雑な機構により水質浄化がなされるといわれている。
【0003】
【発明が解決しようとする課題】
水質浄化機能という観点からみると、土壌および植物の根圏との接触頻度が大きい浸透流れ方式のほうが浄化効率は高いと考えられる。
浸透流れ方式では、短絡流をさけて排水を一様に湿地に流下させるために、表面を湛水させることが求められる。
そして、湛水条件下では酸素供給が、水面からの拡散と植物の茎・根からの輸送に限られ、排水中の負荷が大きい場合、分解に用いる酸素消費量が大きくなり土中は嫌気化する。
しかしながら、脱窒素という観点からみると嫌気状態は望ましいものの、有機物の腐敗や低質土壌の溶出等の問題が生じる。
本発明は前記事情に鑑み案出されたものであって、構造的に嫌気条件と好気条件を無動力で繰り返すことにより、水質浄化効率を高めるようにした水質浄化装置を提供することにある。
【0004】
【課題を解決するための手段】
前記目的を達成するため、本発明の水質浄化装置は、上部が開放された処理槽と、前記処理槽の内部に収容され微生物が繁殖可能で植物が植えられた土壌層と、前記処理槽に排水を供給する排水供給部と、前記土壌層の底部に一端が連通すると共に、中間部が前記処理槽の側壁の上端寄りで側壁の上端よりも低い箇所に位置し、他端が土壌層の底部とほぼ同じ高さかあるいは底部より低位に位置するサイフォン状の通路を設け、前記通路は、前記処理槽内の水位が前記管路の中間部よりも高くなった状態で前記通路内を流れる水量が、前記排水供給部から処理槽に供給される水量よりも多くなるように設定され、前記処理槽の内部の側部には、処理槽の側壁と間隔をあけて処理槽の底部から隔壁が立設され、この隔壁と側壁により処理槽の内部と区画された整流部が設けられ、前記排水供給部による前記処理槽への排水の供給は、前記整流部内の排水が隔壁を越え溢れ出ることで、あるいは、隔壁の上部の流通孔から流出することで行われることを特徴とする。
【0005】
また、本発明は、前記排水供給部と通路の一端が、処理槽内の互い対向する側部箇所に配置されていることを特徴とする。
【0006】
また、本発明は、前記土壌層の底部と処理槽の底部との間には、土壌を支持すると共に水の透過を可能とした透水層が設けられ、前記通路の一端はこの透水層に接続されていることを特徴とする。
また、本発明は、前記通路の中間部が土壌層の上面よりも上位に位置することを特徴とする。
【0007】
また、本発明は、前記水質浄化装置が複数設けられ、排水の流れの上流側に位置するサイフォン状の通路の他端が、排水の流れの下流側に位置する水質浄化装置の排水供給部の一部を構成するように複数の水質浄化装置が直列的に連結されていることを特徴とする。
【0008】
本発明によれば、土壌層において水位の上昇と下降が無動力で繰り返されて行われる。
水位が低い状況では、植物が植えられた土壌層が好気的雰囲気となり、有機物や窒素の酸化反応が促進され、また、水位が高い状況では嫌気的雰囲気となり、脱窒素が促進される。
これらにより水質浄化効率が高められる。
【0009】
【発明の実施の形態】
以下、本発明に係る水質浄化装について説明する。
図1は水質浄化装置の断面正面図を示す。
水質浄化装置2は、処理槽4と、植物6が植えられた土壌層8と、透水層10と、排水供給部12と、サイフォン状の通路14等により構成されている。
前記処理槽4は、例えば、矩形状の底壁402と四つの側壁404から上部が開放された平面視矩形状に形成されている。
また、一つの側壁404寄り箇所には、該側壁404に平行して底壁402から隔壁406が立設され、この隔壁406により、処理槽4の内部が隔壁406の外側の本体部410と、隔壁406の内側の整流部420に区画され、隔壁406の上端406Aは側壁404の上端404Aよりも低く形成されている。
前記整流部420には、排水路16から定常的に排水が供給され、これにより整流部420内の水位が上昇し、隔壁406の上端406Aを越えて本体部410に排水が流入する。あるいは、隔壁406の上部に複数の流通孔が形成され、これら流通孔から本体部410に排水が流入する。
【0010】
前記処理槽4の本体部410の底壁402上には前記透水層10が設けられている。
透水層10は、土壌層8を支持する共に水の通過を可能とした材料、すなわち、水のみを透過する材料で所定の高さ(上下方向の厚さ)で形成され、例えば、合成樹脂製の排水材や、メッシュ材、あるいは、砂利や小石、砕石等で構成することができ、市販品としては、新光ナイロン株式会社の「ヘチマロン」を用いることができる。
透水層10は、処理槽4内の排水を放流する際に、土壌層8内の水を確実に底方へ移動させる上で有利となる。
【0011】
前記土壌層8は前記透水層10の上に設けられ、土壌層8の高さ(上下方向の厚さ)は、例えば、0.5〜1.0m程度に設定され、土壌層8の上面(表面)8Aは隔壁406の上端406Aよりも低位に形成されている。
土壌層8には草花等の植物6が植えられている。
前記土壌層8は微生物が繁殖できるような土が用いられ、空気が流通し易いように、例えば、黒土等をベースとしてパーライト等を混合し空隙率が確保されている。
【0012】
前記サイフォン状の通路14は、一端開口1402が前記透水層10の下部に臨み、他端開口1404が処理槽4の外部に位置するように形成されている。
前記サイフォン状の通路14は、一端開口1402と他端開口1404が低位で、延在方向の中間部1406が高位となるように形成され、詳細には、一端開口1402が処理槽4の底壁402の上面とほぼ同じ高さで、その延在方向の中間部1406が前記隔壁406の上端406Aより僅かに低い高さで、他端開口1404が処理槽4の底壁402の上面とほぼ同じ高さで形成されている。
また、サイフォン状の通路14の断面形状や水位差は、前記処理槽4内の水位が前記通路14の中間部1406よりも高くなった状態で前記通路14内を流れる水量が、隔壁406の上端406Aを越えて本体部410に流入する水量、すなわち、排水路16から排水供給部12に供給される水量よりも多くなるように設定されている。
尚、上記のような構成の処理槽4は、例えば、コンクリートや合成樹脂等で製作可能であり、サイフォン状の通路14は処理槽4の側壁404に、処理槽4の製作時に一体的に製作してもよく、あるいは、管体を用いて製作する等任意である。
また、処理槽4の容量は、排水の土壌層8における平均滞留時間が数日程度になるように設定されている。
【0013】
次に、作用について説明する。
水質浄化装置2では、整流部420に排水路16から定常的に排水が供給され、排水は隔壁406の上端406Aを越えて本体部410に流入する。
そして、排水は土壌層8を通って底壁402上に溜り、本体部410内の排水の水位が土壌層8内において徐々に上昇していく。
やがて、水位が前記通路14の中間部1406よりも高位となった時点で、処理槽4内の排水は通路14から処理槽4の外部に放流され、今度は、処理槽4内の水位が徐々に下降していく。
そして、処理槽4内の水位が通路14の他端開口1404よりも低くなった時点で、あるいは、空気が他端開口1404に入った時点で、通路14による排水の放流が停止される。
通路14による排水の放流が停止されると、本体部410内の排水の水位が徐々に上昇し、前記と同様に、通路14による排水の放流、本体部410内の排水の水位の下降、通路14による排水の放流の停止、本体部410内の排水の水位の上昇が、無動力で繰り返されて行われる。
【0014】
本実施例によれば、土壌のフィルターとしての物理的な作用により、粉塵の捕捉やメタン等の炭化水素ガス等の不純成分の吸着が行なわれることは無論のこと、微生物により不純成分等、汚染物質の分解が行なわれる。
処理槽4内の水位が低い状況では、植物6が植えられた土壌層8に空気が流通して好気的雰囲気となり、好気性微生物が繁殖し、これら好気性微生物の菌体内や植物6により消費されたり、呼吸で使われる等することで有機物や窒素の酸化反応が促進される。
また、処理槽4内の水位が高い状況では、植物6が植えられた土壌層8が嫌気的雰囲気となり、嫌気的微生物が繁殖し、これら嫌気性微生物の菌体内や植物6により消費されたり、呼吸で使われる等することで脱窒素が促進される。
そして、上記の好気、嫌気の異なる雰囲気場を時間的に変化させつつ無動力で繰り返して作り、植物6が植えられた土壌層8の水質浄化効率が格段と高められる。
【0015】
また、実施例では、土壌層8の下方に透水層10を設けたので、排水の放流時、土壌層8内の水を確実に排出でき、好気的雰囲気を作る上で有利となる。
また、本実施例では、通路14の中間部1406が土壌層8の上面8Aよりも高く形成されているので、高水位時、土壌層8の上面8Aは湛水され、排水供給部12と通路14の一端とは処理槽4の対向する箇所に配置されたことと相まって、短絡流が防止され、水質浄化効率がより格段と高められる。
また、排水の土壌層8への供給は、整流部420から静穏に行われるので、水質浄化効率がより格段と高められる。
さらに、流入水量や放流水量、サイフォン状の通路14の水位差等を適宜変更することにより汚染物質の除去効率が大きくなるような制御をすることも可能である。
【0016】
次に、図2を参照して第2実施例について説明する。
図2は第2実施例に係る水質浄化装置200の断面正面図を示す。
第2実施例に係る水質浄化装置200は、一部の側壁404を共通化して第1実施例に係る水質浄化装置2を二つ直列的に連結して構成したものである。
すなわち、排水の流れの上流側に配置された水質浄化装置2のサイフォン状の通路14の他端が、下流側に配置された水質浄化装置2の整流部420の上部に配置され、下流側の整流部420の隔壁406の上端406Aが上流側の処理槽4の底壁402上面よりも低位に設定され、二つの水質浄化装置2により浄化されるようにしたものである。
このように、複数の水質浄化装置2を直列的に連結し、浄化を行う水質浄化装置2を数を増やすことで、より高度な処理を行う上で有利となる。
【0017】
【発明の効果】
以上の説明で明らかように本発明に係る水質浄化装置によれば、何ら動力を用いることなく、植物が植えられた土壌の嫌気的雰囲気と好気的雰囲気との切り換えを繰り返して行うことができ、土壌及び、微生物、植物による水質浄化が効率的になされ、水質浄化効率を格段と高めることが可能となる。
【図面の簡単な説明】
【図1】水質浄化装置の断面正面図である。
【図2】第2実施例に係る水質浄化装置の断面正面図である。
【符号の説明】
2 水質浄化装置
4 処理槽
402 底壁
404 側壁
406 隔壁
410 本体部
420 整流部
6 植物
8 土壌層
10 透水層
12 排水供給部
14 サイフォン状の通路
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a suitable water purification KaSo location using the advanced treatment of water purification, such as household waste water.
[0002]
[Prior art]
A water purification method using a wetland for water purification is already known.
Conventionally, water purification methods using such wetlands can be broadly divided into the following two types as seen from the way of drainage.
(1) Surface flow method: A method that collects treated water at the end of the wetland by allowing the wastewater to be treated to flow down to the surface of the wetland assuming a purification function.
(2) Osmotic flow method: A method that collects treated water from the lower soil or drainage layer by letting the treated wastewater flow down from the surface of the wetland assuming a purification function.
In any of these methods, it is said that water purification is performed by a complicated mechanism in which soil physics, chemical action, microorganisms in soil, absorption by plants, and the like are combined.
[0003]
[Problems to be solved by the invention]
From the viewpoint of the water purification function, it is considered that the osmotic flow method with high contact frequency with soil and plant rhizosphere has higher purification efficiency.
In the osmotic flow method, the surface is required to be submerged in order to avoid the short-circuit flow and allow the drainage to flow down to the wetland uniformly.
Under flooded conditions, oxygen supply is limited to diffusion from the surface of the water and transport from plant stems and roots, and when the load in the drainage is large, the oxygen consumption used for decomposition increases and the soil becomes anaerobic. To do.
However, from the viewpoint of denitrification, anaerobic conditions are desirable, but problems such as organic decay and low-quality soil elution occur.
The present invention was devised in view of the above circumstances, the structurally anaerobic conditions and aerobic conditions by repeating in a non-powered, to provide a water purification KaSo location was to enhance the water purification efficiency is there.
[0004]
[Means for Solving the Problems]
In order to achieve the above object, the water purification apparatus of the present invention includes a treatment tank having an open top, a soil layer in which microorganisms can be propagated and plants are planted, and the treatment tank. One end of the drainage supply unit that supplies drainage and the bottom of the soil layer communicate with each other, the middle part is located near the upper end of the side wall of the treatment tank and lower than the upper end of the side wall, and the other end of the soil layer A siphon-like passage is provided that is approximately the same height as the bottom or lower than the bottom, and the passage is configured to have an amount of water flowing through the passage in a state where the water level in the treatment tank is higher than the middle portion of the pipe. Is set so as to be larger than the amount of water supplied to the treatment tank from the waste water supply unit, and a partition wall is provided on the side part inside the treatment tank from the bottom of the treatment tank at a distance from the side wall of the treatment tank. This partition wall and side wall The drainage supply section supplies the wastewater to the treatment tank when the drainage in the rectification section overflows beyond the partition wall or flows out from the flow hole above the partition wall. It is characterized by being performed .
[0005]
In addition, the present invention is characterized in that the drainage supply section and one end of the passage are arranged at opposite side portions in the treatment tank .
[0006]
Further , according to the present invention, a permeable layer is provided between the bottom of the soil layer and the bottom of the treatment tank so as to support the soil and allow water to pass therethrough, and one end of the passage is connected to the permeable layer. It is characterized by being.
Further, the present invention is characterized in that an intermediate portion of the passage is positioned higher than the upper surface of the soil layer.
[0007]
Further , the present invention provides a plurality of the water purification devices, wherein the other end of the siphon-shaped passage located on the upstream side of the drainage flow is a drainage supply part of the water purification device located on the downstream side of the drainage flow. A plurality of water purification apparatuses are connected in series so as to constitute a part.
[0008]
According to the present invention, the rise and fall of the water level in the soil layer is repeated without power.
In a situation where the water level is low, the soil layer in which the plant is planted becomes an aerobic atmosphere, and an oxidation reaction of organic matter and nitrogen is promoted. In a situation where the water level is high, an anaerobic atmosphere is created and denitrification is promoted.
These improve the water purification efficiency.
[0009]
DETAILED DESCRIPTION OF THE INVENTION
The following describes water purification KaSo location according to the present invention.
FIG. 1 shows a cross-sectional front view of a water purification device.
The water purification device 2 includes a treatment tank 4, a soil layer 8 in which plants 6 are planted, a water permeable layer 10, a drainage supply unit 12, a siphon-shaped passage 14, and the like.
The processing tank 4 is formed, for example, in a rectangular shape in plan view in which an upper portion is opened from a rectangular bottom wall 402 and four side walls 404.
Further, a partition wall 406 is erected from the bottom wall 402 in parallel with the side wall 404 at a location near one side wall 404, and the partition wall 406 allows the inside of the processing tank 4 to be connected to the main body portion 410 outside the partition wall 406, The upper end 406 </ b> A of the partition wall 406 is formed lower than the upper end 404 </ b> A of the side wall 404.
The rectifying unit 420 is constantly supplied with drainage from the drainage channel 16, whereby the water level in the rectifying unit 420 rises, and the drainage flows into the main body 410 beyond the upper end 406 </ b> A of the partition wall 406. Alternatively, a plurality of flow holes are formed in the upper part of the partition wall 406, and the waste water flows into the main body 410 from these flow holes.
[0010]
The water permeable layer 10 is provided on the bottom wall 402 of the main body 410 of the treatment tank 4.
The water permeable layer 10 is a material that supports the soil layer 8 and allows water to pass therethrough, that is, a material that allows only water to pass therethrough, and is formed at a predetermined height (thickness in the vertical direction). Waste water material, mesh material, gravel, pebbles, crushed stone, etc., and “Hetimaron” manufactured by Shinko Nylon Co., Ltd. can be used as a commercial product.
The water permeable layer 10 is advantageous in reliably moving the water in the soil layer 8 to the bottom when discharging the waste water in the treatment tank 4.
[0011]
The soil layer 8 is provided on the water permeable layer 10, and the height (thickness in the vertical direction) of the soil layer 8 is set to about 0.5 to 1.0 m, for example, (Surface) 8 </ b> A is formed lower than the upper end 406 </ b> A of the partition wall 406.
Plants 6 such as flowers are planted in the soil layer 8.
The soil layer 8 is made of soil that allows microorganisms to propagate, and for example, pearlite is mixed based on black soil or the like so as to facilitate air circulation, and the porosity is secured.
[0012]
The siphon-shaped passage 14 is formed such that one end opening 1402 faces the lower part of the water permeable layer 10 and the other end opening 1404 is located outside the treatment tank 4.
The siphon-shaped passage 14 is formed such that the one end opening 1402 and the other end opening 1404 are low and the intermediate portion 1406 in the extending direction is high, and in detail, the one end opening 1402 is the bottom wall of the processing tank 4. The intermediate portion 1406 in the extending direction is substantially the same height as the upper surface of the partition wall 402 and slightly lower than the upper end 406A of the partition wall 406, and the other end opening 1404 is substantially the same as the upper surface of the bottom wall 402 of the processing tank 4. It is formed at a height.
Further, the cross-sectional shape and the water level difference of the siphon-shaped passage 14 are such that the amount of water flowing in the passage 14 in a state where the water level in the treatment tank 4 is higher than the intermediate portion 1406 of the passage 14 is the upper end of the partition wall 406. It is set to be larger than the amount of water flowing into the main body 410 beyond 406A, that is, the amount of water supplied from the drainage channel 16 to the drainage supply unit 12.
Note that the processing tank 4 having the above-described configuration can be manufactured using, for example, concrete or synthetic resin, and the siphon-shaped passage 14 is manufactured integrally with the side wall 404 of the processing tank 4 when the processing tank 4 is manufactured. Alternatively, it may be arbitrarily manufactured by using a tubular body.
Moreover, the capacity | capacitance of the processing tank 4 is set so that the average residence time in the soil layer 8 of a waste_water | drain will be about several days.
[0013]
Next, the operation will be described.
In the water purification device 2, drainage is constantly supplied from the drainage channel 16 to the rectifying unit 420, and the drainage flows into the main body 410 beyond the upper end 406 </ b> A of the partition wall 406.
Then, the wastewater accumulates on the bottom wall 402 through the soil layer 8, and the water level of the wastewater in the main body 410 gradually rises in the soil layer 8.
Eventually, when the water level becomes higher than the intermediate portion 1406 of the passage 14, the waste water in the treatment tank 4 is discharged from the passage 14 to the outside of the treatment tank 4, and this time the water level in the treatment tank 4 gradually increases. To descend.
Then, when the water level in the processing tank 4 becomes lower than the other end opening 1404 of the passage 14 or when the air enters the other end opening 1404, the drainage of the drainage through the passage 14 is stopped.
When the drainage of the drainage through the passage 14 is stopped, the water level of the drainage in the main body 410 gradually rises. Similarly to the above, the drainage of the drainage through the passage 14, the lowering of the water level of the drainage in the main body 410, and the passage The stop of the discharge of the waste water by 14 and the rise of the water level of the waste water in the main body 410 are repeatedly performed without power.
[0014]
According to this embodiment, it is a matter of course that the trapping of dust and the adsorption of impure components such as hydrocarbon gas such as methane are performed by the physical action as a soil filter. Material decomposition takes place.
In a situation where the water level in the treatment tank 4 is low, air flows through the soil layer 8 in which the plant 6 is planted to create an aerobic atmosphere, and aerobic microorganisms propagate. Oxidation reaction of organic matter and nitrogen is promoted by being consumed or used for breathing.
Moreover, in the situation where the water level in the treatment tank 4 is high, the soil layer 8 in which the plant 6 is planted becomes an anaerobic atmosphere, and anaerobic microorganisms are propagated and consumed by the cells of the anaerobic microorganisms or the plant 6. Denitrification is promoted by using it for respiration.
And the atmosphere field where said aerobic and anaerobic are different is made repeatedly without power, changing temporally, and the water purification efficiency of the soil layer 8 in which the plant 6 was planted is raised significantly.
[0015]
In the embodiment, since the water permeable layer 10 is provided below the soil layer 8, the water in the soil layer 8 can be reliably discharged when the drainage is discharged, which is advantageous in creating an aerobic atmosphere.
In the present embodiment, since the intermediate portion 1406 of the passage 14 is formed higher than the upper surface 8A of the soil layer 8, the upper surface 8A of the soil layer 8 is flooded at the time of high water level, and the drainage supply portion 12 and the passage. The short circuit flow is prevented and the water purification efficiency is remarkably enhanced, coupled with the fact that the one end of 14 is disposed at the opposite position of the treatment tank 4.
Moreover, since the supply of the wastewater to the soil layer 8 is performed calmly from the rectifying unit 420, the water purification efficiency is significantly improved.
Furthermore, it is also possible to control to increase the pollutant removal efficiency by appropriately changing the inflow water amount, the discharge water amount, the water level difference of the siphon-like passage 14 and the like.
[0016]
Next, a second embodiment will be described with reference to FIG.
FIG. 2 shows a cross-sectional front view of a water purification device 200 according to the second embodiment.
The water purification apparatus 200 according to the second embodiment is configured by connecting two water purification apparatuses 2 according to the first embodiment in series by sharing a part of the side walls 404.
That is, the other end of the siphon-like passage 14 of the water purification device 2 disposed on the upstream side of the wastewater flow is disposed on the upper side of the rectifying unit 420 of the water purification device 2 disposed on the downstream side, The upper end 406A of the partition wall 406 of the rectifying unit 420 is set lower than the upper surface of the bottom wall 402 of the upstream processing tank 4, and is purified by the two water purification apparatuses 2.
In this way, by connecting a plurality of water purification apparatuses 2 in series and increasing the number of water purification apparatuses 2 that perform purification, it is advantageous in performing more advanced processing.
[0017]
【The invention's effect】
According to the water quality purification KaSo location according to the present invention As is clear from the above description, any without using power, be performed repeatedly switching between anaerobic atmosphere and aerobic atmosphere soil plants were planted In addition, water purification by soil, microorganisms, and plants can be performed efficiently, and the water purification efficiency can be significantly increased.
[Brief description of the drawings]
FIG. 1 is a cross-sectional front view of a water purification device.
FIG. 2 is a cross-sectional front view of a water purification device according to a second embodiment.
[Explanation of symbols]
2 Water purification device 4 Treatment tank 402 Bottom wall 404 Side wall 406 Partition wall 410 Main body 420 Rectification unit 6 Plant 8 Soil layer 10 Water permeable layer 12 Drainage supply unit 14 Siphonic passage

Claims (5)

上部が開放された処理槽と、
前記処理槽の内部に収容され微生物が繁殖可能で植物が植えられた土壌層と、
前記処理槽に排水を供給する排水供給部と、
前記土壌層の底部に一端が連通すると共に、中間部が前記処理槽の側壁の上端寄りで側壁の上端よりも低い箇所に位置し、他端が土壌層の底部とほぼ同じ高さかあるいは底部より低位に位置するサイフォン状の通路を設け、
前記通路は、前記処理槽内の水位が前記管路の中間部よりも高くなった状態で前記通路内を流れる水量が、前記排水供給部から処理槽に供給される水量よりも多くなるように設定され、
前記処理槽の内部の側部には、処理槽の側壁と間隔をあけて処理槽の底部から隔壁が立設され、この隔壁と側壁により処理槽の内部と区画された整流部が設けられ、
前記排水供給部による前記処理槽への排水の供給は、前記整流部内の排水が隔壁を越え溢れ出ることで、あるいは、隔壁の上部の流通孔から流出することで行われる、
ことを特徴とする水質浄化装置。
A treatment tank with an open top;
A soil layer housed in the treatment tank and capable of breeding microorganisms and planted;
A waste water supply unit for supplying waste water to the treatment tank;
One end communicates with the bottom of the soil layer, and the middle portion is located near the upper end of the side wall of the treatment tank and lower than the upper end of the side wall, and the other end is approximately the same height as the bottom of the soil layer or from the bottom. Provide a siphon-like passage located in the lower position,
The passage is configured such that the amount of water flowing in the passage in a state where the water level in the treatment tank is higher than the intermediate portion of the pipe is larger than the amount of water supplied from the drainage supply unit to the treatment tank. Set ,
On the side of the inside of the processing tank, a partition wall is erected from the bottom of the processing tank with a gap from the side wall of the processing tank, and a rectifying section partitioned from the inside of the processing tank by the partition wall and the side wall is provided,
The supply of wastewater to the treatment tank by the wastewater supply unit is performed by overflowing the wastewater in the rectifying unit overflowing the partition wall or by flowing out from the flow hole in the upper part of the partition wall.
A water purification apparatus characterized by that.
前記排水供給部と通路の一端は、処理槽内の互い対向する側部箇所に配置されている請求項記載の水質浄化装置。One end of the drain supply and passage, water purification apparatus according to claim 1, wherein disposed on the side portions of face each other in the processing bath. 前記土壌層の底部と処理槽の底部との間には、土壌を支持すると共に水の透過を可能とした透水層が設けられ、前記通路の一端はこの透水層に接続されている請求項記載の水質浄化装置。Between the bottom of the treatment tank and the bottom of the soil layer, allows transmission of water and the water-permeable layer is provided to support the soil, one end of said passageway claim is connected to the water-permeable layer 1 The water purification apparatus as described. 前記通路の中間部は土壌層の上面よりも上位に位置する請求項記載の水質浄化装置。Middle part water purification device according to claim 1, wherein at an upper level than the upper surface of the soil layer of the passageway. 前記水質浄化装置が複数設けられ、排水の流れの上流側に位置するサイフォン状の通路の他端が、排水の流れの下流側に位置する水質浄化装置の排水供給部の一部を構成するように複数の水質浄化装置が直列的に連結されている請求項記載の水質浄化装置。A plurality of the water purification devices are provided, and the other end of the siphon-shaped passage located on the upstream side of the waste water flow constitutes a part of the waste water supply unit of the water purification device located on the downstream side of the waste water flow water purification device according to claim 1, wherein a plurality of water purification devices are serially connected to.
JP22258795A 1995-08-08 1995-08-08 Water purification device Expired - Lifetime JP3838579B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22258795A JP3838579B2 (en) 1995-08-08 1995-08-08 Water purification device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22258795A JP3838579B2 (en) 1995-08-08 1995-08-08 Water purification device

Publications (2)

Publication Number Publication Date
JPH0947779A JPH0947779A (en) 1997-02-18
JP3838579B2 true JP3838579B2 (en) 2006-10-25

Family

ID=16784812

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22258795A Expired - Lifetime JP3838579B2 (en) 1995-08-08 1995-08-08 Water purification device

Country Status (1)

Country Link
JP (1) JP3838579B2 (en)

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ATE486818T1 (en) * 2004-09-16 2010-11-15 Phytorestore METHOD FOR TREATING POLLUTANTS BY PLANT LEACHING
FR2876047B1 (en) * 2004-09-16 2007-11-16 Phytorestore Soc Par Actions S TREATMENT OF POLLUTANTS BY PHYTOLIXIVIATION
JP2006110495A (en) * 2004-10-15 2006-04-27 Nishihara Environment Technology Inc Hydrogen fermentation apparatus
JP4877546B2 (en) * 2006-09-14 2012-02-15 独立行政法人農業・食品産業技術総合研究機構 Underflow constructed wetland system
JP4587401B2 (en) * 2006-09-29 2010-11-24 有限会社藤島建設 Wastewater filtration system
KR100836788B1 (en) * 2006-12-18 2008-06-10 주식회사 아썸 Equipment using bio-filtration and siphon efflux, and symstem containing the said equipment for treatment of polluted water from non-point source
KR101012749B1 (en) * 2008-05-30 2011-02-10 (주)비포엔지니어링 Open-type Initial Rainwater Treatment Equipment
JP5288559B2 (en) * 2009-09-18 2013-09-11 中国電力株式会社 Nitrification apparatus and biological nitrification denitrification apparatus
CN102863122B (en) * 2012-09-29 2014-01-08 重庆大学 Device and method for domestic sewage treatment
CN103936159B (en) * 2014-03-21 2015-07-08 南大(常熟)研究院有限公司 Constructed wetland sewage treatment device and method for treating sewage

Also Published As

Publication number Publication date
JPH0947779A (en) 1997-02-18

Similar Documents

Publication Publication Date Title
CN207699412U (en) A kind of Drain contamination for river channel mouth sewage-treatment plant
US20090272689A1 (en) Liquid aeration apparatus and wastewater treatment method
CN101538106B (en) Energy-free sewage treatment plant
KR20110048244A (en) Equipment and method for water and stream purification using layered soil system
JP3838579B2 (en) Water purification device
CN111204927A (en) Ecological public toilet sewage treatment circulating system and sewage treatment and recycling method
CN108128986A (en) Integrated multistage AO decentralized sewage treatment devices and method
CN111333271B (en) Sewage treatment system, application thereof and sewage treatment method
CN111170580A (en) Sewage purification treatment system
CN109502917A (en) A kind of residents underground powerless integration compound bio sewage-treatment plant and technique
CN107129116B (en) Floating type comprehensive water treatment equipment and water treatment method using same
CN212713159U (en) Reactor capable of realizing efficient nitrogen and phosphorus removal treatment of sewage with low carbon-nitrogen ratio
KR100266085B1 (en) Sewage treatment apparatus using an artificial swamp
CN211871749U (en) Solar ecological floating island
CN109879536B (en) Rural domestic sewage purification system and purification method
CN104961291B (en) Ecological sewage treatment system of vertical multistage AO
CN114956472B (en) Modularized rural domestic sewage treatment device
CN201358204Y (en) Oil-refining sewage advanced treatment device
CN114906986B (en) Integrated sewage treatment device and method with adjustable process
JP4350358B2 (en) Resource recovery type sewage purification method and apparatus used therefor
CN214244101U (en) Rural sewage treatment system
CN109836016A (en) A kind of Drain contamination for river channel mouth sewage-treatment plant
CN209522733U (en) A kind of residents underground powerless integration compound bio sewage-treatment plant
CN210855710U (en) Ecological sewage treatment system for expressway service area
CN212269787U (en) Exogenous sewage ecological treatment system

Legal Events

Date Code Title Description
A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20040928

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20060524

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20060710

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20060731

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20060731

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090811

Year of fee payment: 3

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100811

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110811

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110811

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120811

Year of fee payment: 6

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120811

Year of fee payment: 6

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130811

Year of fee payment: 7

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

EXPY Cancellation because of completion of term