JPH0121040Y2 - - Google Patents

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Publication number
JPH0121040Y2
JPH0121040Y2 JP1984146723U JP14672384U JPH0121040Y2 JP H0121040 Y2 JPH0121040 Y2 JP H0121040Y2 JP 1984146723 U JP1984146723 U JP 1984146723U JP 14672384 U JP14672384 U JP 14672384U JP H0121040 Y2 JPH0121040 Y2 JP H0121040Y2
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JP
Japan
Prior art keywords
water
layer
treated
filler
filler 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
Application number
JP1984146723U
Other languages
Japanese (ja)
Other versions
JPS6161100U (en
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Filing date
Publication date
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Priority to JP1984146723U priority Critical patent/JPH0121040Y2/ja
Publication of JPS6161100U publication Critical patent/JPS6161100U/ja
Application granted granted Critical
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Expired legal-status Critical Current

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Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

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  • Biological Treatment Of Waste Water (AREA)

Description

【考案の詳細な説明】 〔産業上の利用分野〕 本考案は、浄水装置に係り、より詳細には、池
の水等(以下、廃水・汚水という)を好気的条件
下で微生物を利用して生物学的処理に浄水するよ
うにした廃水・汚水の浄水装置に関する。
[Detailed description of the invention] [Industrial application field] The present invention relates to a water purification device, and more specifically, it uses microorganisms in pond water, etc. (hereinafter referred to as wastewater/sewage) under aerobic conditions. This invention relates to a water purification device for wastewater and sewage that uses biological treatment to purify water.

〔従来の技術〕[Conventional technology]

従来、廃水・汚物の生物学的処理による浄水装
置としては、 フロツク状の生物性増殖体を絶えず循環さ
せ、この生物性増殖体が好気的条件の下で有機
性廃水・汚水と接触するようにして廃水・汚水
の処理を行うようにした活性汚泥法による装
置、 処理槽内に充填材層を配設し、前記充填材の
表面に微生物膜を形成させ、廃水・汚水を前記
微生物膜に接触させるようにして廃水・汚水の
処理を行うようにした生物膜法による装置、 が知られている(岩井重久訳「廃水の生物学的処
理」コロナ社版等参照)。
Traditionally, water purification systems based on the biological treatment of wastewater and sewage have been designed to constantly circulate floc-like biological growth bodies and to bring these biological growth bodies into contact with organic wastewater and sewage under aerobic conditions. A device using the activated sludge method that treats wastewater and sewage by disposing of a filling material layer in the treatment tank, forming a microbial film on the surface of the filling material, and discharging the wastewater and sewage onto the microbial film. Devices using the biofilm method that treat wastewater and sewage by bringing them into contact with each other are known (see ``Biological Treatment of Wastewater,'' translated by Shigehisa Iwai, published by Corona Publishing, etc.).

そして、活性汚泥法には標準活性汚泥法、分散
増殖曝気法、接触安定化法あるいは段階曝気法等
があり、廃水・汚水の処理量その他を考慮して選
択使用されている。しかし、この活性汚泥法の場
合、一般的に活性汚泥が多く必要であり、しかも
この活性汚泥が処理水とともに流出し処理水質を
悪くすることがあり、また、これを解決するには
装置自体を大きくする等の必要性が生じるという
問題点がある。
The activated sludge method includes a standard activated sludge method, a dispersion growth aeration method, a contact stabilization method, a staged aeration method, etc., which are selected and used in consideration of the amount of wastewater/sewage to be treated and other factors. However, in the case of this activated sludge method, a large amount of activated sludge is generally required, and this activated sludge may flow out together with the treated water, worsening the quality of the treated water. There is a problem in that it becomes necessary to increase the size.

また、生物膜法には散水濾床法、回転円板法、
接触酸化法等があり前述活性汚泥法のように設置
条件その他を考慮して選択使用されている。しか
し、この生物膜法の場合、処理当たりの微生物膜
面積が小さいため処理能力がひくく、また前述し
た活性汚泥法の場合と同様に処理水中に微生物膜
が流出し処理水質を悪くするという問題点もあ
る。
Biofilm methods include trickling filter method, rotating disk method,
There are catalytic oxidation methods, etc., and like the activated sludge method mentioned above, they are selected and used in consideration of installation conditions and other factors. However, in the case of this biofilm method, the treatment capacity is low because the microbial film area per treatment is small, and as with the activated sludge method mentioned above, the microbial film leaks into the treated water and deteriorates the quality of the treated water. There is also.

そこで、かかる問題に対処したものとして、第
6図に示すように処理槽1の上部に廃水・汚水流
入部2を、下部に処理水排出部3を配設し、また
処理槽1の内部は上部から順に充填材層8、充填
材と固形粒子との混合充填材層、および支持層5
を形成するとともに、支持層5の下側には処理水
集水装置21および空気吸入口22を設け、前記
充填材として前記固形粒子よりも充分に大きな粒
径のものを使用した構成の浄水装置(特開昭58−
114792号公報参照)や、処理層内部に粒径の細か
い濾過材の前段に粒径の粗い濾過材を配設し、そ
の浄水効率を向上させるようにした浄水装置(特
開昭52−134453号公報参照)が提案されている。
そして、これらの浄水装置によれば、前述したよ
うな問題点が解決できるという利点を有してい
る。
Therefore, as a solution to this problem, as shown in FIG. In order from the top, a filler layer 8, a mixed filler layer of filler and solid particles, and a support layer 5.
, a treated water collection device 21 and an air intake port 22 are provided on the lower side of the support layer 5, and the filler is made of particles having a sufficiently larger particle size than the solid particles. (Unexamined Japanese Patent Publication 1983-
114792), and a water purification device that improves the water purification efficiency by disposing a coarse-grained filter material before a fine-grained filter material inside the treatment layer (Japanese Patent Application Laid-open No. 134453/1983). (see official bulletin) has been proposed.
These water purification devices have the advantage of being able to solve the above-mentioned problems.

しかし、これらの浄水装置は処理槽の上部に設
けられた廃水・汚水流入部より廃水・汚水を充填
材層等を通過させて微生物により浄水し、下部に
設けられた処理水排出部より処理水を排出するよ
うにしたものであるため、浄水処理能力は処理槽
の高さに応じて変わることとなり、浄水処理能力
を向上させるためには処理槽の高さを長くして微
生物生育面積を広くする必要がある。ところが、
微生物生育面積を広くするために処理槽の高さを
長くすると、処理槽自体が大型化するばかりか作
業性の点であまり好ましくないというような問題
点が提起されている。
However, in these water purification devices, wastewater and sewage are passed through a filler layer from the wastewater and sewage inlet located at the top of the treatment tank and purified by microorganisms, and the treated water is discharged from the treated water outlet located at the bottom. Since the treatment tank is designed to discharge water, its water purification capacity varies depending on the height of the treatment tank.In order to improve the water treatment capacity, the height of the treatment tank must be lengthened to increase the area for microbial growth. There is a need to. However,
If the height of the treatment tank is increased in order to increase the area for microbial growth, problems have been raised in that not only does the treatment tank itself become larger, but it is also less favorable in terms of workability.

また、充填材層を横方向に複数個並列設置し
て、被処理水を該充填材層を離隔するための仕切
壁に沿つて被処理水を該充填材層内を循環させる
ようにした浄水装置(特開昭48−35667号公報参
照)も知られている。そして、この構成の場合、
前述した問題が除去できるという利点を有してい
るといえる。
In addition, water purification is provided in which a plurality of filler layers are installed in parallel in the horizontal direction, and the water to be treated is circulated within the filler layer along a partition wall to separate the filler layers. A device (see Japanese Unexamined Patent Publication No. 48-35667) is also known. And for this configuration,
It can be said that this method has the advantage that the above-mentioned problem can be eliminated.

〔考案が解決しようとする問題点〕[Problem that the invention attempts to solve]

しかし、これらの浄水装置の場合、何れも被処
理水を充填材層に送入するに当たつて、該充填材
層を、予め、好気性条件下にして被処理水を送入
するようにしたり、また、被処理水を送入した充
填材層に空気を送り込むようにして、該被処理水
の生物的処理でもつて浄水するようにしているた
め、次ぎのような問題がある。すなわち、 被処理水の爆気状態が、良好でない。
However, in the case of these water purification devices, before sending the water to be treated into the filling material layer, the filling material layer is made to be under aerobic conditions beforehand. In addition, air is sent into the filler layer into which the water to be treated is fed, and the water is purified through biological treatment, which causes the following problems. In other words, the explosive state of the water to be treated is not good.

充填材層を好気性条件下にするための空気送
入設備が複雑構成となる。
The air supply equipment for bringing the filler layer under aerobic conditions is complicated.

また、浄水後の処理水は、単なる清浄水である
ので、該処理水を池等に再循環する場合、別途に
池等の爆気装置が必要になる。
Furthermore, since the treated water after purification is simply clean water, if the treated water is to be recirculated to a pond or the like, a separate detonation device such as a pond is required.

本考案は、上述した点に対処して創案したもの
であつて、その目的とする処は、充填材層へ供給
する被処理水を該充填材層に送入するに際し、空
気が充分に混合された状態の被処理水とし、該充
填材層による生物的浄水効率を高めると共に、そ
の処理槽自体を小型化できるようにした廃水・汚
水の浄水装置を提供することにある。
The present invention was devised in response to the above-mentioned problems, and its purpose is to ensure that air is sufficiently mixed when the water to be treated is fed to the filling material layer. It is an object of the present invention to provide a water purification device for wastewater and sewage in which the water to be treated is in a treated state, the biological water purification efficiency by the filler layer is increased, and the treatment tank itself can be downsized.

(問題点を解決するための手段) そして、上記目的を達成するための手段として
の本考案の浄水装置は、廃水・汚水等の被処理水
を浄水するための浄水装置であつて、被処理水浄
水用処理槽の下位部に複数個の通水孔を穿設した
支持材を配置すると共に、該支持材の上面に複数
の仕切壁を立設して、該仕切壁と処理槽内壁間お
よび隣接する仕切壁間に微生物を生息させた充填
材層をそれぞれ配設し、該充填材層は前段より後
段側に目の細かい充填材を配設した充填材層と
し、また、該充填材層の後段に記充填材層より目
の細かい濾過材層を配設すると共に、該充填材層
と濾過層間または該濾過層の後段に石灰石の砕石
等よりなる被処理水中和層を配設し、上記被処理
水を仕切壁に沿つて該充填材層、濾過層、被処理
水中和層を迂回循環するようにし、さらに該充填
材層の前段部位に被処理水供給用ポンプによつて
被処理水を強制供給する被処理水送入管を配設
し、該被処理水送入管の途中には該被処理水送入
管内を通ずる被処理水の水流により吸引される空
気吸引用配管を配設して、該被処理水送入管内で
吸引空気によつて爆気した被処理水を上記充填材
層に送入できるようにし、また、上記濾過層後
段、または該濾過層の後段に被処理水中和層が配
設されている場合は該被処理水中和層の後段に、
充填材層、濾過層、被処理水中和層を介して浄水
されて得た処理水を排出するための処理水排出管
を設け、該処理水排出管の途中に該処理水の活性
化を図ると共に酸素の供給をするための空気供給
部を設け、また、上記支持材の下方部位に汚泥集
積部を配設した構成よりなる。
(Means for Solving the Problems) The water purification device of the present invention as a means for achieving the above object is a water purification device for purifying water to be treated such as wastewater and sewage. A support member having a plurality of water passage holes is arranged in the lower part of the water purification treatment tank, and a plurality of partition walls are erected on the upper surface of the support member, and a gap between the partition wall and the inner wall of the treatment tank is provided. and a filler layer in which microorganisms live between adjacent partition walls. A filter layer finer than the filler layer is disposed after the layer, and a hydrated layer made of crushed limestone or the like is disposed between the filler layer and the filtration layer or after the filter layer. , the water to be treated is circulated around the filling material layer, the filtration layer, and the water hydration layer to be treated along the partition wall, and further, the water to be treated is supplied to a portion before the filling material layer by a pump for supplying the water to be treated. A to-be-treated water inlet pipe for forcibly supplying treated water is installed, and in the middle of the to-be-treated water inlet pipe there is air suction piping that is sucked in by the water flow of the to-be-treated water passing through the to-be-treated water inlet pipe. is arranged so that the treated water atomized by suction air in the treated water inlet pipe can be sent to the above-mentioned filler layer, and the latter stage of the above-mentioned filtration layer, or the latter stage of the filtration layer. If a water hydration layer to be treated is arranged in the water hydration layer to be treated, then
A treated water discharge pipe is provided for discharging treated water obtained by purification through a filler layer, a filtration layer, and a hydration layer of treated water, and the treated water is activated in the middle of the treated water discharge pipe. In addition, an air supply section for supplying oxygen is provided, and a sludge accumulation section is provided below the support material.

ここで、上記構成において、微生物として、一
般的にバクテリア、酵母、黴類、原生動物、輪虫
類、虫類および昆虫の幼虫のようなものを使用す
る。そして、バクテリアは主として非硝化性の好
気性芽胞形成菌で、その多くは枯草菌である。し
かし、一般的にはこれら多くの種類の集合体より
なるものを用いる。また、充填材層を形成する充
填材すなわち微生物の付着材としては、ウシヒリ
ング、シツシング状充填物、パイプ状、球状ある
いは格子状その他種々の形成で、しかも種々の材
質よりなる充填物を用いることができる。不定形
状、異形状のものでもよい。また、砂、アンスラ
サイト、スラグ、プラスチツク製粒子等でもあつ
てもよい。
Here, in the above configuration, microorganisms such as bacteria, yeast, fungi, protozoa, rotifers, worms, and insect larvae are generally used. Bacteria are mainly non-nitrifying aerobic spore-forming bacteria, most of which are Bacillus subtilis. However, in general, one consisting of aggregations of many of these types is used. In addition, as the filler forming the filler layer, that is, the material to which microorganisms adhere, it is possible to use fillers having various shapes such as oxchilling, shishing, pipe, spherical, or lattice shapes, and made of various materials. can. It may be of irregular shape or irregular shape. It may also be sand, anthracite, slag, plastic particles, etc.

また、仕切壁としては一般的にはプラスチツク
製の板状、凹凸部を有する形状等を用いるが、こ
れに限定されるものでなく他の形状でもよい。ま
た、濾過材層としては前述充填材層を形成する充
填材と同様のものを用いることができる。ただ、
一般的には充填材層より目が細かくなるものを選
択使用する。さらに、被処理水中和層として、石
灰石の砕石等を網袋に入れて形成したものとして
いる。
Further, although the partition wall is generally made of a plastic plate, has a shape having uneven parts, etc., it is not limited thereto, and other shapes may be used. Further, as the filter material layer, the same filler as that forming the filler layer described above can be used. just,
Generally, a material with finer grains than the filler layer is selected and used. Furthermore, the hydrated layer to be treated is formed by placing crushed limestone or the like in a mesh bag.

〔作用〕[Effect]

次ぎに、上記構成に基づく、本考案の浄水装置
について説明する。
Next, a water purification device of the present invention based on the above configuration will be explained.

まず、BOD成分、窒素成分、リン成分その他
の成分を含む有機性成分を有する廃水・汚水を池
等より、処理槽内に被処理水供給用ポンプによつ
て被処理水を強制供給するとともに、該ポンプに
よる被処理水の水流によるエジエクタ作用でもつ
て、空気吸入管により空気を負圧吸引して、該被
処理水中に空気を混入した後、該空気含有被処理
水を処理槽内に送り、該充填材層で循環浄水でき
るようにする。
First, wastewater/sewage containing organic components including BOD components, nitrogen components, phosphorus components, and other components is forcibly fed into the treatment tank from a pond etc. using a pump for supplying treated water. With the ejector action of the water flow of the water to be treated by the pump, air is sucked under negative pressure through the air suction pipe to mix air into the water to be treated, and then the air-containing water to be treated is sent into the treatment tank; The filling material layer enables circulating water to be purified.

そして、該充填材層に送入された被処理水は、
含有する空気でもつて好気性雰囲気下とされた充
填材層で、複層の充填材層の第一層内を仕切壁に
沿つて通過させ、第二、第三…層内を順次循環通
過させるることで、該循環通過過程でBOD成分
等を微生物との接触で食物源として微生物の細胞
内に蓄積、増殖され、除去されたBOD成分等の
一部は合成されて新しい細胞物質となり、残りお
よび充填材層内を仕切壁に沿つて順次循環通過す
るBOD成分等は前記増殖された微生物により酸
化され、また、前記細胞物質は内呼吸作用により
酸化される。
The water to be treated that is sent to the filler layer is
The air contained in the packing material layer is in an aerobic atmosphere, and the first layer of the multi-layered packing material layer is passed along the partition wall, and the second, third, and so on are sequentially circulated through the layers. During the circulation process, BOD components etc. come into contact with microorganisms and are accumulated and multiplied within the cells of microorganisms as a food source. A part of the removed BOD components etc. is synthesized and becomes new cell material, and the remaining The BOD components and the like that circulate through the filler layer along the partition wall are oxidized by the grown microorganisms, and the cellular material is oxidized by internal respiration.

そして、このようにして浄水されて得た処理水
は、濾過材層を通過して処理水内に含まれている
微生物が除去され、また、処理水排出管に配設さ
れている空気供給部により、新たに空気が混入さ
れ、過酸素含有処理水とされた後、再び、池等に
戻し、池等の水を浄水できるように作用する。
The treated water thus purified passes through a layer of filter material to remove microorganisms contained in the treated water, and an air supply section installed in the treated water discharge pipe As a result, air is newly mixed in and the treated water is made into peroxygen-containing treated water, which is then returned to the pond or the like to purify the water in the pond or the like.

以上のように、本考案の浄水装置は、被処理水
の微生物への接触距離を充填材層内を仕切壁に沿
つて蛇行しながら循環通過させるようにして長く
すると共に、被処理水の空気による爆気をエジエ
クタ作用でもつて、充填材層への供給前に行い、
かつ、浄水した後の処理水に空気を供給して池等
に再循環できるようにした点に特徴を有し、この
構成によつて、充填材層による生物的浄水効率を
高めると共に、その処理槽自体を小型化できると
いう格別な作用効果を有する。
As described above, the water purification device of the present invention increases the contact distance of the water to be treated with microorganisms by circulating it through the filler layer in a meandering manner along the partition wall, and also allows the water to be treated to circulate through the layer in a meandering manner along the partition wall. This is done before supplying the explosive gas to the filler layer using an ejector action.
Moreover, it is characterized by supplying air to the treated water after water purification so that it can be recirculated to a pond, etc. With this configuration, the biological water purification efficiency by the filler layer is increased, and the treatment It has the special effect of being able to downsize the tank itself.

〔実施例〕〔Example〕

以下、図面を参照しながら、本考案の実施例に
ついて説明する。
Embodiments of the present invention will be described below with reference to the drawings.

本実施例の浄水装置は、池の水の浄水装置であ
つて、概略すると、処理槽1と被処理水流入部2
および処理水排出部3とよりなる。
The water purification device of this embodiment is a pond water purification device, and roughly speaking, it includes a treatment tank 1 and a water inflow section 2.
and a treated water discharge section 3.

処理槽1は、円筒状の処理槽として形成されて
いて、その内部の下部位には通水穴4を穿つた支
持材5が配設され、この上面に二本の仕切壁6が
立設されていて、対面する仕切壁6間および仕切
壁6と処理槽内壁7間にそれぞれ充填材層8が配
設されている。したがつて、充填材層8は二本の
仕切壁6と処理槽内壁7とにより三つの充填材層
81,82,83として形成されている。そし
て、充填材層83の上部で処理水排出部3の近傍
に濾過材層9が形成されている。ここで、濾過材
層9は、通常、シユロと樹脂とをマツト状に形成
したものを用いるが、その他の材質のものを用い
てもよい。
The treatment tank 1 is formed as a cylindrical treatment tank, and a support member 5 with a water passage hole 4 is provided in the lower part of the interior thereof, and two partition walls 6 are provided on the upper surface of the support member 5. A filler layer 8 is provided between the partition walls 6 facing each other and between the partition wall 6 and the inner wall 7 of the processing tank. Therefore, the filler layer 8 is formed by the two partition walls 6 and the processing tank inner wall 7 as three filler layers 81, 82, and 83. A filtering material layer 9 is formed above the filler layer 83 and near the treated water discharge section 3 . Here, the filtering material layer 9 is usually made of a mat made of silica and resin, but may be made of other materials.

被処理水流入部2は、吸入管10と被処理水供
給用ポンプ11および被処理水供給管12とを有
し、被処理水供給用ポンプ11を介して廃水・汚
水を吸入管10より被処理水供給管12を通じ
て、充填材層8の第一層81に供給できるように
形成されている。また、被処理水供給管12の中
途位置には処理槽1内に酸素を供給して充填材層
8内を好気性条件下にするための空気吸入管13
が配設されている。
The treated water inflow section 2 includes a suction pipe 10, a treated water supply pump 11, and a treated water supply pipe 12, and wastewater/sewage is introduced from the suction pipe 10 via the treated water supply pump 11. It is formed so that it can be supplied to the first layer 81 of the filler layer 8 through the treated water supply pipe 12 . Further, an air suction pipe 13 is provided at a midway position of the water supply pipe 12 to supply oxygen into the treatment tank 1 to make the inside of the filler layer 8 under aerobic conditions.
is installed.

処理水排出部3は、処理水排出管3′と空気供
給部19とを有し、処理水排出管3′の始端側に
は、浄水されて得た処理水を処理槽1外へ排出で
きるように、その処理槽内側口14が濾過材層9
の上部に開口し、他端が処理槽1の外に導出され
ている。
The treated water discharge section 3 has a treated water discharge pipe 3' and an air supply section 19, and a starting end side of the treated water discharge pipe 3' is capable of discharging purified water to the outside of the treatment tank 1. As shown in FIG.
It opens at the top of the tank 1, and the other end is led out of the processing tank 1.

また、処理槽1の底部には、底板15が配設さ
れ、底板15と支持材5との間で汚泥集積部16
が形成され、この汚泥集積部16には集積した汚
泥を処理槽1外へ排出するための汚泥排出部17
が配設されている。
Further, a bottom plate 15 is disposed at the bottom of the treatment tank 1, and a sludge accumulation part 16 is disposed between the bottom plate 15 and the support material 5.
A sludge discharge section 17 is formed in the sludge accumulation section 16 for discharging the accumulated sludge to the outside of the treatment tank 1.
is installed.

ここでは、被処理水流入部2を処理槽1の下部
に、処理水排出部3を処理槽1の上部に配設し廃
水・汚水を充填材層81の下方向より仕切壁6に
沿つて充填材層82方向へ循環通過させるように
構成しているが、被処理水流入部2を処理槽1の
上部に、処理水排出部3を処理槽1の下部(また
は上部)に配設し、廃水・汚水を逆方向に供給す
るようにしてもよい。この場合、濾過材層9およ
び処理水排出部3の処理槽内側口14が充填材層
83の下方に位置するように配設される。
Here, the treated water inflow part 2 is arranged at the lower part of the treatment tank 1, and the treated water discharge part 3 is arranged at the upper part of the treatment tank 1, and wastewater/sewage is discharged from below the filler layer 81 along the partition wall 6. Although the structure is such that the water is circulated in the direction of the filler layer 82, the treated water inlet 2 is arranged at the upper part of the treatment tank 1, and the treated water discharge part 3 is arranged at the lower part (or upper part) of the treatment tank 1. , wastewater/sewage may be supplied in the opposite direction. In this case, the filtration material layer 9 and the treatment tank inner side port 14 of the treated water discharge section 3 are arranged so as to be located below the filler layer 83.

また、充填材層8は、以上のように三つの層に
したものに限るものでなく、例えば、仕切壁6を
一本として充填材層8を二層、仕切壁6を三本以
上として充填材層8を四層以上としてもよい。ま
た、支持材5は処理槽1内部の中央部あるいは上
部に配設するようにしてもよく、さらに仕切壁6
および充填材層8を保持でき、廃水・汚水を通す
通水穴4が穿つてあればどのような構成等であつ
てもよい。二以上配設してもよい。
In addition, the filler layer 8 is not limited to three layers as described above, and for example, one partition wall 6 and two filler layers 8, or three or more partition walls 6. The material layer 8 may have four or more layers. Further, the support material 5 may be arranged at the center or upper part of the processing tank 1, and the partition wall 6
Any configuration may be used as long as it can hold the filler layer 8 and has water passage holes 4 through which wastewater and sewage can pass. Two or more may be provided.

充填材層81,82,83…は充填材で形成さ
れている。そして、これら全ての層内の充填材を
同じものとしてもよいが、通常、第一層81が一
番空隙が大きくなるようにした充填材で形成さ
れ、後段の層ほどその空隙が小さくなるように形
成されている。しかし、他の構成としてもよいこ
とは当然である。そして、これらの層内に微生物
を生息(充填材に微生物膜を形成)させるように
している。また、仕切壁6、処理槽内壁7、支持
材5、濾過材層9も微生物生育体(付着材)とし
てもよい。この場合、処理槽あたりの微生物の量
(微生物膜面積)を多くすることができる。さら
に、前記充填材は例えば網状の袋に入れ(各層全
体あるいは各層を小さく分けてそれぞれを)配設
するようにしてもよい。この場合は、充填材の交
換が簡単に行えるという利点がある。
The filler layers 81, 82, 83, . . . are formed of a filler. The filling material in all of these layers may be the same, but usually the first layer 81 is formed with a filling material that has the largest voids, and the later layers have the smallest voids. is formed. However, it goes without saying that other configurations may also be used. Microorganisms are allowed to live within these layers (a microbial film is formed on the filler). Furthermore, the partition wall 6, the inner wall 7 of the processing tank, the supporting material 5, and the filtering material layer 9 may also be used as microbial growth bodies (adhering materials). In this case, the amount of microorganisms (microbial membrane area) per treatment tank can be increased. Further, the filler may be placed in, for example, a mesh bag (each entire layer or each layer divided into smaller pieces). In this case, there is an advantage that the filling material can be replaced easily.

なお、処理水内にアンモニア成分等が多い場
合、濾過材層9と充填材層83の間、または濾過
材層9の処理水排出部3の処理槽内側口14側に
処理水を中和させるための中和処理槽18を配設
してもよい。この場合は、より浄水力が高まる。
ここで、中和処理層18としては残るのがアンモ
ニア成分の場合は通常保持等のため網袋などに入
れられている石灰石の砕石が用いられる。
In addition, if there is a large amount of ammonia components etc. in the treated water, the treated water is neutralized between the filter material layer 9 and the filler layer 83 or on the treatment tank inner side port 14 of the treated water discharge part 3 of the filter material layer 9. A neutralization treatment tank 18 may be provided for this purpose. In this case, the water purification power is further increased.
Here, if it is the ammonia component that remains as the neutralized layer 18, crushed limestone, which is usually placed in a net bag or the like for retention, is used.

つぎに、以上の構成に基づいてその作用を説明
する。
Next, the operation will be explained based on the above configuration.

まず、被処理水供給用ポンプ11を作動し、
BOD成分、窒素成分、リン成分その他の成分を
含む有機性成分を有する被処理水を池等より被処
理水流入部2の吸入管10および被処理水供給管
12を介して強制流入させると共に、被処理水供
給管12内を流通する被処理水の水流によつて、
空気吸入管13より空気をエジエクタ作用でもつ
て強制吸入して空気を被処理水中に分散混入・爆
気した状態で、処理槽1内に送り込んで、空気含
有被処理水中の空気でもつて、充填材層8を好気
性雰囲気とし、矢印に従い充填材層8の第一層8
1内を仕切壁6に沿つて通過させ、第二、第三…
層82,83…内を、順次、迂回循環通過させ
る。また、処理槽1の下部では矢印に示すように
第二層82の被処理水を第一層81に一部返送さ
せて処理内容を高めている。
First, operate the pump 11 for supplying water to be treated,
Water to be treated having organic components including BOD components, nitrogen components, phosphorus components and other components is forced to flow in from a pond or the like through the suction pipe 10 and the water supply pipe 12 of the water to be treated inlet 2, and Due to the water flow of the treated water flowing through the treated water supply pipe 12,
Air is forcibly sucked in through the air suction pipe 13 using an ejector action, and the air is dispersed and mixed into the water to be treated, and the atomized state is sent into the treatment tank 1. The layer 8 is made into an aerobic atmosphere, and the first layer 8 of the filler layer 8 is moved according to the arrow.
1 along the partition wall 6, the second, third...
The layers 82, 83, . . . are sequentially detoured and circulated. Further, in the lower part of the treatment tank 1, as shown by the arrow, a portion of the water to be treated in the second layer 82 is returned to the first layer 81 to improve the treatment content.

そして、この循環通過する過程のなかでBOD
成分等は、微生物との接触で食物源として微生物
の細胞内に蓄積、増殖され、除去されたBOD成
分等の一部は合成されて新しい細胞物質となり、
充填材層8内を仕切壁6に沿つて蛇行しながら順
次循環通過するBOD成分等は、増殖された微生
物により酸化され、また、細胞物質は内呼吸作用
により酸化される。ここで、充填材層8より流出
した微生物等の汚泥は処理槽1の汚泥集積部16
に溜まり、定期的に汚泥排出部17を作動させて
処理槽1外へ排出する。
In the process of passing through this circulation, BOD
Components, etc. are accumulated and multiplied within the cells of microorganisms as a food source upon contact with microorganisms, and some of the removed BOD components, etc. are synthesized and become new cellular substances.
The BOD components and the like that circulate through the filler layer 8 in a meandering manner along the partition wall 6 are oxidized by the grown microorganisms, and the cellular substances are oxidized by internal respiration. Here, sludge such as microorganisms flowing out from the filler layer 8 is collected in the sludge accumulation section 16 of the treatment tank 1.
The sludge discharger 17 is periodically operated to discharge the sludge to the outside of the treatment tank 1.

そして、上述のようにして浄水された処理水は
濾過材層9を通過して処理水内に含有されている
微生物が除去され、処理水排出部3より再び池等
に戻し、池等の水を浄水する。
The treated water purified as described above passes through the filter material layer 9 to remove microorganisms contained in the treated water, and is returned to the pond etc. from the treated water discharge part 3, and the water in the pond etc. Purify water.

この作動を連続的、間歇的に行い最終的に池等
の水を浄水するように作用する。
This operation is carried out continuously and intermittently, and ultimately works to purify water in ponds, etc.

なお、本考案は、上述した実施例に限定される
ものでなく、本考案の要旨を変更しない範囲内で
変形実施できるものを含む。因みに、第5図に示
すように、被処理水流入部2(送入管12の開口
端)を処理槽1の上・下の両方に配設し、充填材
層8を逆洗する時でも浄水処理が行えるようにし
た構成としてもよい。そして、この場合、処理水
排出部3は濾過材層9の間より処理水の取り出し
ができるように構成され、充填材層8内の目づま
りが軽減でき、層内の微生物の働きをより活発化
させることができるという利点を有する。
It should be noted that the present invention is not limited to the embodiments described above, and includes modifications that can be made without changing the gist of the present invention. Incidentally, as shown in FIG. 5, even when the treated water inflow section 2 (opening end of the feed pipe 12) is arranged both above and below the treatment tank 1 and the filler layer 8 is backwashed. It may also be configured so that water purification treatment can be performed. In this case, the treated water discharge section 3 is configured so that the treated water can be taken out from between the filtration material layers 9, which reduces clogging in the filler layer 8 and makes the microorganisms in the layer more active. It has the advantage of being able to

また、変形例として、第4図に示すように、仕
切壁6を水平に複数(ここでは3個)配設し、充
填材層8を複層形成した構成とすることも可能で
ある。ここで、仕切壁6は処理槽内壁7に互い違
いに設けられていて、廃水・汚水が矢印に従い前
記仕切壁6間に配設された充填材層8内を蛇行し
ながら順に後層の充填材層8内を循環通過できる
ように形成されている。
As a modification, as shown in FIG. 4, it is also possible to have a configuration in which a plurality of partition walls 6 (three in this case) are arranged horizontally and the filler layer 8 is formed in multiple layers. Here, the partition walls 6 are provided alternately on the inner wall 7 of the treatment tank, and wastewater/sewage follows the arrow and snakes through the filler layer 8 disposed between the partition walls 6, sequentially passing through the filler layer in the rear layer. It is formed so that it can circulate through the layer 8.

〔考案の効果〕[Effect of idea]

以上の説明より明らかなように、本考案の浄水
装置によれば、被処理水の微生物への接触距離を
充填材層内を仕切壁に沿つて蛇行しながら循環通
過させるようにして長くすると共に、被処理水の
空気による爆気をエジエクタ作用でもつて、充填
材層への供給前に行い、かつ、浄水した後の処理
水に空気を供給して池等に再循環できるようにし
ているので、被処理水が予め爆気状態にあり、送
り込まれた充填材層による生物的浄水効率を高め
ると共に、その処理槽自体を小型化でき、かつ、
浄水して得た処理水自体にも空気を強制的に含有
させるので、池等の水自体の浄化も容易に行える
という効果を有する。
As is clear from the above explanation, according to the water purification device of the present invention, the contact distance of the water to be treated with microorganisms is lengthened by circulating the water through the filling material layer in a meandering manner along the partition wall. , the atomization of the air in the water to be treated is carried out by ejector action before being supplied to the filler layer, and air is supplied to the treated water after it has been purified so that it can be recirculated to ponds, etc. , the water to be treated is in an explosive state in advance, the biological water purification efficiency is increased by the packed filler layer, and the treatment tank itself can be made smaller;
Since the treated water itself is forced to contain air, it has the effect of easily purifying the water itself in ponds and the like.

【図面の簡単な説明】[Brief explanation of the drawing]

第1〜3図は本考案の実施例を示し、第1図は
その一部を切り欠き充填材を除いた状態での斜視
図、第2図は充填材を配設した状態での縦断面
図、第3図はその平面図、第4図は変形例の断面
図、第5図は本考案の他の実施例を示す断面図、
第6図は従来例の断面図である。 1……処理槽、2……廃水・汚水流入部、3…
…処理水排出部、4……通水穴、5……支持材、
6……仕切壁、7……処理槽内壁、8……充填材
層、9……濾過材層、18……中和処理層。
Figures 1 to 3 show an embodiment of the present invention. Figure 1 is a partially cutaway perspective view with the filler removed, and Figure 2 is a longitudinal cross-section with the filler installed. 3 is a plan view thereof, FIG. 4 is a sectional view of a modified example, and FIG. 5 is a sectional view showing another embodiment of the present invention.
FIG. 6 is a sectional view of a conventional example. 1... treatment tank, 2... wastewater/sewage inflow section, 3...
... Treated water discharge part, 4 ... Water passage hole, 5 ... Support material,
6... Partition wall, 7... Inner wall of treatment tank, 8... Filling material layer, 9... Filtering material layer, 18... Neutralization treatment layer.

Claims (1)

【実用新案登録請求の範囲】 (1) 廃水・汚水等の被処理水を浄水するための浄
水装置であつて、被処理水浄水用処理槽の下位
部に複数個の通水孔を穿設した支持材を配置す
ると共に、該支持材の上面に複数の仕切壁を立
設して、該仕切壁と処理槽内壁間および隣接す
る仕切壁間に微生物を生息させた充填材層をそ
れぞれ配設し、該充填材層は前段より後段側に
目の細かい充填材を配設した充填材層とし、ま
た、該充填材層の後段に記充填材層より目の細
かい濾過材層を配設すると共に、該充填材層と
濾過層間または該濾過層の後段に石灰石の砕石
等よりなる被処理水中和層を配設し、上記被処
理水を仕切壁に沿つて該充填材層、濾過層、被
処理水中和層を迂回循環するようにし、さらに
該充填材層の前段部位に被処理水供給用ポンプ
によつて被処理水を強制供給する被処理水送入
管を配設し、該被処理水送入管の途中には該被
処理水送入管内を通ずる被処理水の水流により
吸引される空気吸引用配管を配設して、該被処
理水送入管内で吸引空気によつて爆気した被処
理水を上記充填材層に送入できるようにし、ま
た、上記濾過層後段、または該濾過層の後段に
被処理水中和層が配設されている場合は該被処
理水中和層の後段に、充填材層、濾過層、被処
理水中和層を介して浄水されて得た処理水を排
出するための処理水排出管を設け、該処理水排
出管の途中に該処理水の活性化を図ると共に酸
素の供給をするための空気供給部を設け、ま
た、上記支持材の下方部位に汚泥集積部を配設
したことを特徴とする浄水装置。 (2) 被処理水中和層を、石灰石の砕石等を網袋に
入れて形成している実用新案登録請求の範囲(1)
に記載の浄水装置。
[Scope of Claim for Utility Model Registration] (1) A water purification device for purifying water to be treated such as wastewater and sewage, which has multiple water passage holes in the lower part of a treatment tank for purifying the water to be treated. At the same time, a plurality of partition walls are erected on the upper surface of the support material, and filler layers in which microorganisms live are placed between the partition walls and the inner wall of the processing tank and between adjacent partition walls. and the filler layer is a filler layer in which a finer filler is disposed on the rear side than the front stage, and a filter material layer finer than the filler layer is disposed in the rear stage of the filler layer. At the same time, a water hydration layer to be treated made of crushed limestone or the like is provided between the filler layer and the filtration layer or after the filtration layer, and the water to be treated is passed through the filler layer and the filtration layer along the partition wall. , the water to be treated is circulated around the hydration layer, and furthermore, a water inlet pipe for forcibly supplying the water to be treated by a pump for supplying the water to be treated is arranged in the front part of the filler layer, An air suction pipe is installed in the middle of the water supply pipe to be sucked in by the water flow of the water to be treated passing through the water supply pipe. The heated and explosive water to be treated can be fed into the filler layer, and if a hydration layer is provided after the filtration layer or after the filtration layer, the water to be treated can be fed to the filling material layer. A treated water discharge pipe for discharging the purified water through the filler layer, filtration layer, and treated water hydration layer is provided after the hydration layer, and the treated water is disposed in the middle of the treated water discharge pipe. A water purification device comprising: an air supply section for activating water and supplying oxygen; and a sludge accumulation section disposed below the support member. (2) Scope of claim for utility model registration (1) where the hydrated layer to be treated is formed by placing crushed limestone, etc. in a mesh bag
The water purification device described in .
JP1984146723U 1984-09-27 1984-09-27 Expired JPH0121040Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1984146723U JPH0121040Y2 (en) 1984-09-27 1984-09-27

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1984146723U JPH0121040Y2 (en) 1984-09-27 1984-09-27

Publications (2)

Publication Number Publication Date
JPS6161100U JPS6161100U (en) 1986-04-24
JPH0121040Y2 true JPH0121040Y2 (en) 1989-06-23

Family

ID=30704959

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1984146723U Expired JPH0121040Y2 (en) 1984-09-27 1984-09-27

Country Status (1)

Country Link
JP (1) JPH0121040Y2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009106919A (en) * 2007-10-29 2009-05-21 Kazuo Miyamoto Filtering apparatus of water in water tank

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5011193B2 (en) * 1971-08-27 1975-04-28
JPS5843160B2 (en) * 1976-05-04 1983-09-24 三郎 岡本 Organic wastewater purification equipment using microorganisms

Also Published As

Publication number Publication date
JPS6161100U (en) 1986-04-24

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