JP3577663B2 - Water purification method and apparatus - Google Patents

Water purification method and apparatus Download PDF

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Publication number
JP3577663B2
JP3577663B2 JP2000340882A JP2000340882A JP3577663B2 JP 3577663 B2 JP3577663 B2 JP 3577663B2 JP 2000340882 A JP2000340882 A JP 2000340882A JP 2000340882 A JP2000340882 A JP 2000340882A JP 3577663 B2 JP3577663 B2 JP 3577663B2
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water
cylinder
inner cylinder
purified
wastewater
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JP2002143887A (en
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高田俊介
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高田 俊介
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Description

【0001】
【発明の属する技術分野】
本発明は,水の浄化方法及びそれに用いられる装置に関するもので、特に細長い閉鎖された水路を利用し、浄化効率を高め、保守を容易にした浄化方法及び装置に関するものである。
【0002】
【従来の技術】
生活排水や魚槽等の水を浄化するための従来の基本的システムは、▲1▼先ず固形物をスクリーン(フィルター)で物理的に排除し、▲2▼次いで、主原因物質である有機物から発生するアンモニアを活性汚泥等の好気性微生物の働きにより亜硝酸へ、更に硝酸塩に変化するまで、酸化分解(硝化)する方法を採るのが一般的である。
【0003】
また、これのみでは水中の硝酸塩が水の酸性度を高め富栄養化の原因となるため、第3のステップとして嫌気性微生物の働きにより、窒素成分を窒素ガスの形で除去(脱窒)し、より高度な浄化を行うことが試みられている。
【0004】
【発明が解決する課題】
しかしながら、好気性微生物を利用した硝化の過程では、微生物の活動を活発ならしめるため相当量の酸素を必要とし、場合によって流動,攪拌等の手段も用いて積極的に酸素を供給するのに対し、嫌気性微生物を利用する脱窒の過程では脱窒槽を密閉したり、一時的に水の流れを滞溜させるなどして酸素を遮断する必要があった。
この硝化,脱窒の過程の相反する条件を、同一の設備内で一連に連続的に行わせることは極めて困難でそれが装置の実用化(小型化)の隘路となっていた。
【0005】
【課題を解決する手段】
本発明は細長く閉鎖された水路の前段部において好気性微生物を繁殖させて硝化作用を行わしめ、好気性微生物によって酸素がほぼ消費された後段に、嫌気性微生物の繁殖を促進する栄養源を配置し、同一水路内で定量の水を継続的に流し続けながら硝化・脱窒作用を連続的に行わせるようにしたものである。
【0006】
また細く長い水路を用いることにより、濾材の特定部分を水が選択的に流れるいわゆるチャネル現象を防ぎ、濾材を有効に利用できると共に、同一水路内に好気性微生物と嫌気性微生物が場所を変えて併存することが可能となり、ほぼ完全な浄化水を得られるとともに装置全体の小型化も実現できる。
【0007】
【発明の実施の形態】
図1は本発明の最も基本的な実施の形態を示す図である。
図1において、被浄化水は左上部の「水槽から」の矢印に示すように被浄化水槽からポンプによって汲み上げられ、左端の筒状の「ろ材容器」に供給される。複数の「ろ材容器」(図示の例では8本)は上下で交互に水流的に連結されており、矢印に示すような経路をたどって右端の「ろ材容器」に到り、そこからもとの水槽に戻されるようになっている。
【0008】
8本の「ろ材容器」は全体として細く長い閉鎖された水路を構成している。
左端のろ材容器は固形物を取り除くための「物理ろ過部」を構成しており、それに続く6本のろ材容器は「好気性バクテリアによる生物ろ過部」となっている。
また、右端の「ろ材容器」は「嫌気性バクテリアによる生物ろ過部」となる。
【0009】
被浄化水は「ポンプ」から左端の「ろ材容器」に供給された状態では有機物と共に好気性微生物の繁殖に十分な酸素を含有しているが、右に進むに従って好気性微生物によって酸素は消費され、含有量が低下し右端の「ろ材容器」に到達した段階で殆ど存在しなくなる。一般に嫌気性微生物が繁殖できるための水中酸素濃度は2mg/l以下と云われているが、この段階において、水中酸素濃度はほぼその数値に達している。
【0010】
この間に被浄化水中の有機物は硝化され、それに伴なって硝酸塩の濃度が増加するがこの硝酸塩成分は右端の「ろ材容器」中の嫌気性微生物によって脱窒され浄水となって水槽に戻されることになる。
【0011】
図2は個々の筒状の「ろ材容器」の内部構造の一例を示す断面図である。
図3は、図2の筒状の「ろ材容器」の中に収納されるろ材を入れる内筒である。
図3に示す内筒1内には、ろ材2(図2)が充填されていて、内筒1の中心軸1aは内筒の上下端部より延出されて設けられている。また、内筒1の上端部には内部にろ材2を充填した後に、水が通過する多数の小孔3aを設けた蓋3が嵌められる。内筒1の底部にも小孔1cが設けられている。
図3に示す内筒1は図2に示す筒体5内に収納される。図2に示す筒体5は側面の上端の対向する位置に蓋6a,6b付きの連通部5a,5bが一対設けられている。また筒体5は側面の下端の対向する位置にも蓋7a,7b付きの連通部5c,5dが一対設けられている。
【0012】
一つの筒体5の上端の連通部5bはその右側に隣接する筒体5(図示せず)の上端の連通部5aに嵌合可能な構造となっていて、これを嵌合することで二つの筒体5、5間には連続した水路が形成される。同様に隣接する二つの筒体5、5の下端同士の連通部5c,5d間でも嵌合により水路が形成できる。これらの間は直接嵌合しない場合でも、ゴムやプラスチックのパイプなどで接続することもできる。
また、筒体5の下端の連通部5dとその右に隣接する筒体5(図示せず)の上端の連通部5aをパイプで連結するという接続方法も可能である。
【0013】
また、筒体5の上下の連通部5a〜5dより外側の側面には蓋付小孔5f,5g,5h,5iを形成しておけば、必要に応じ通気孔或いは排水孔として随時利用できる。
例えば、筒体5の内部に異常なガスの発生が認められた場合、その部位の上部小孔5f,5gの蓋を開ければガスを取り除くことができる。また、沈殿物等があるときは下部小孔5h,5iの蓋を開け流出させることができる。
【0014】
更にこの小孔を利用し、好気性微生物による硝化区域にある筒体5中の水の一部を、嫌気性微生物による脱窒区域の筒体に入る前の段階で取り出し、これを水槽に還流し水質や嫌気性微生物の生育の調整に用いることもできる。
即ち、硝化区域を構成する筒体の総延長が短か過ぎたり、水量が多すぎたり、或いは水量に比しろ材の分量が少な過ぎたりした場合は、嫌気性区域に流入する水の酸素の残存量が過大となり、嫌気性区域での嫌気性微生物の生育に影響を与える場合があるので、水質を監視しながら、水の一部を嫌気性区域に入る前に取り出す必要があるが、その場合のバイパス経路の取出口として用いることができる。
【0015】
筒体5の底部は閉塞しているが、頂部は内筒1を出し入れするための開口状となっており、蓋8を設けることで開閉自在となっている。
このように、ろ材2を収納する筒体を同一規格のカートリッジ化したユニットとしたので、廉価に製造できるだけでなく、適切な個数の筒体5を接続することで、必要な長さの浄化装置を組み立てることができる。
組み立てにあたっては、筒体5の長手方向が鉛直方向に向かうように並列配置して、それぞれの上下の連通部5a〜5dを一つおきに順次接続し、不要の連通部は蓋でふさぐことにより、全体として図1の矢印で示す如き、長いジグザグ状水路を作ることができる。
また、下部連通部5dとその右に隣接する筒体の上部連通部5aをパイプで繋ぎ、それを繰り返すことによっても同様の長いジグザグ状の水路を作ることができる。
なお、筒体5を複数個予め組み合わせたブロックを作り、これを連結して使うこともできる。
【0016】
実際の使用に当たっては、最先端の筒体5の連通部5aに被浄化水を導入する如くし、内筒1には物理的ろ過に適したろ材を封入する。
また最終段の筒体5には、嫌気性微生物の繁殖に適したろ材を封入し、連通部5bより浄化水を排水するようにする。
【0017】
【実施例】
本発明を観賞魚の水槽の浄化装置に適用した場合を例にとると、次の如くなる。
各筒体5の直径は約3cm、長さ約30cmとする。
一般的に60型と呼ばれている巾60cmの角型水槽ではこれを8本連結して用い、その場合有効な筒体総延長は約2m28cmとなる。巾120cmの水槽の場合は更に8本を連結することにより、総延長は約4m56cmとなる。
【0018】
60型水槽に本発明の装置を使用した場合について、市販されているもっとも一般的な浄化装置との比較実験を行った結果を第4図及び第5図に示す。(実験者:東京工業大学助教授、辻正道氏) 実験は、同大水槽に同一条件の水を同量用い、これに健康なエンゼルフィッシュを夫々20匹づつを放して行われた。
比較用の水槽にはエーハイム社製2426型ろ過器を用い、これには同社の推奨するろ材、エーハイサブストラット2.5l及びエーハイメック1.5lを使用した。一方本発明装置には第一段階の物理ろ過用にスポンジフィルターとウールマットを使用し、好気性ろ過区域にパワーハウスM型0.88l及びS型0.88lを使用した。また、終段の嫌気性ろ過区域には有機炭素製剤であるデニボール(商品名)100gを使用した。
【0019】
その結果、第4図に示す如く、ろ過水の硝酸塩濃度は実験開始15〜18日経過後、両装置共に上昇しはじめたが、本発明装置では23〜24日頃から徐々に下がりはじめ、60日以降はほぼ一定に保ったのに対し、比較水槽ではその後もなお上昇し続けた。そして第5図に示す如く、本発明装置ではPHが7.0とほぼ安定したのに対し、比較水槽では急激に下がり続け、42日目には遂にエンゼルフィッシュの生存限界といわれるPH4.5に達し、実験は中止せざるを得なくなった。
【0020】
なお、本発明装置においては引き続き9ヵ月経過後も健全に成長し続けている。即ち、通常の観賞魚飼育程度では全く水替えの必要がないことを意味し、飼育上最大の問題点であった水替えの患わしさを無くしたとも言えるものである。
なお、本発明装置においても当初は比較水槽と同様に硝酸塩が上昇したにも関わらず、やがて低下に転じたことは、最初は水路中に嫌気性微生物が殆ど存在しなかったものが、終段における嫌気性環境の醸成と、有機炭素の作用により、嫌気性微生物の繁殖が促がされ、本来の機能が働きはじめたためと推定される。
【0021】
なお、上記実施例においては、観賞魚水槽の浄化について説明したが、被浄化水が下水,屎尿,河川水等の場合でも同様に適用することができる。被浄化水の水質によっては、嫌気性微生物の繁殖のための栄養源となる有機物の含有量がはじめから少ない場合もあるが、本発明の方法,装置によれば終段のろ材に嫌気性微生物の栄養源となる有機性プラスチック,有機性炭素等を配置することにより、如何なる性質の被浄化水にも対応できる。
【0022】
【本発明の効果】
以上の如く、本発明は細長く閉鎖された水路を用いることにより、終段において嫌気性微生物増殖の好環境を作りだし、嫌気性微生物のもたらす脱窒作用により、ほぼ中性に水を浄化するという作用を連続的に長期間単一の装置で行うことができる方法と装置を提供するものである。
また、筒体を連結し細長い水路をジグザグ状に形成することにより、チャネル現象の発生を最小に抑えると共に、ろ材の交換を容易にし、装置を小型化できるというメリットがある。
【図面の簡単な説明】
【図1】本発明の基本的原理を説明する図
【図2】本発明の水路として使用される筒体の構造を表す図
【図3】筒体内部に挿入される内筒
【図4】本発明装置の実験結果を表すグラフ
【図5】本発明装置の実験結果を表すグラフ
【符号の説明】
1・・・内筒, 1a・・・内筒の中心軸, 1c・・・小孔,
2・・・ろ材, 3・・・内筒の蓋, 3a・・・小孔, 5・・・筒体, 5a〜5d・・・連通部, 5f〜5i・・・小孔,
6a〜6b・・・上部連通部の蓋, 7a〜7b・・・下部連通部の蓋,
8・・・筒体の蓋
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to a method and an apparatus for purifying water, and more particularly to a method and apparatus for purifying water by using a narrow and closed water channel to increase purification efficiency and facilitate maintenance.
[0002]
[Prior art]
Conventional basic systems for purifying water from domestic wastewater and fish tanks are as follows: (1) first physically remove solids with a screen (filter); It is common to employ a method of oxidatively decomposing (nitrifying) the generated ammonia to nitrite and further to nitrate by the action of an aerobic microorganism such as activated sludge.
[0003]
In addition, since nitrate in water alone increases the acidity of water and causes eutrophication, as a third step, nitrogen components are removed (denitrified) in the form of nitrogen gas by the action of anaerobic microorganisms. Attempts have been made to pursue more advanced purification.
[0004]
[Problems to be solved by the invention]
However, in the process of nitrification using aerobic microorganisms, a considerable amount of oxygen is required to increase the activity of the microorganisms. In some cases, oxygen is actively supplied using means such as flow and stirring. In the process of denitrification using anaerobic microorganisms, it was necessary to shut off oxygen by closing the denitrification tank or temporarily stopping the flow of water.
It is extremely difficult to continuously and contradict the conditions of the nitrification and denitrification processes in the same facility, which has been a bottleneck for the practical use (miniaturization) of the apparatus.
[0005]
[Means to solve the problem]
In the present invention, a nutrient for promoting the growth of anaerobic microorganisms is disposed at the latter stage where aerobic microorganisms are propagated and nitrification is performed in the front stage of an elongated closed waterway and oxygen is almost consumed by the aerobic microorganisms. Then, nitrification and denitrification are continuously performed while a fixed amount of water is continuously flown in the same channel.
[0006]
In addition, by using a narrow and long water channel, the so-called channel phenomenon in which water selectively flows through a specific part of the filter medium can be prevented, the filter medium can be used effectively, and aerobic microorganisms and anaerobic microorganisms change places in the same water channel. It is possible to coexist, and almost purified water can be obtained, and at the same time, the size of the entire apparatus can be reduced.
[0007]
BEST MODE FOR CARRYING OUT THE INVENTION
FIG. 1 is a diagram showing the most basic embodiment of the present invention.
In FIG. 1, the water to be purified is pumped up from the water tank to be purified by a pump as shown by an arrow “from a water tank” at the upper left, and is supplied to a cylindrical “filter medium container” at the left end. A plurality of “filter media containers” (eight in the illustrated example) are alternately connected in a vertical manner in a stream of water, and follow a path shown by an arrow to reach the “filter media container” at the right end, and from there, the original. To be returned to the aquarium.
[0008]
The eight "filter medium containers" constitute a narrow and long closed water channel as a whole.
The filter material container at the left end constitutes a “physical filtration unit” for removing solid matter, and the subsequent six filter material containers constitute a “biological filtration unit for aerobic bacteria”.
The "filter medium container" on the right end is a "biological filtration unit for anaerobic bacteria".
[0009]
The water to be purified contains enough oxygen for the propagation of aerobic microorganisms together with organic matter when supplied to the filter medium container at the left end from the pump, but oxygen is consumed by the aerobic microorganisms as it goes to the right. When the content decreases and reaches the "filter medium container" on the right end, it hardly exists. Generally, the oxygen concentration in water for anaerobic microorganisms to propagate is said to be 2 mg / l or less, but at this stage, the oxygen concentration in water almost reaches that value.
[0010]
During this time, the organic matter in the water to be purified is nitrified and the concentration of nitrate increases accordingly.This nitrate component is denitrified by the anaerobic microorganisms in the "filter medium container" on the far right and returned to the water tank as purified water. become.
[0011]
FIG. 2 is a cross-sectional view showing an example of the internal structure of each cylindrical “filter medium container”.
FIG. 3 shows an inner cylinder for storing the filter medium stored in the cylindrical “filter medium container” in FIG. 2.
An inner cylinder 1 shown in FIG. 3 is filled with a filter medium 2 (FIG. 2), and a center shaft 1a of the inner cylinder 1 is provided to extend from upper and lower ends of the inner cylinder. Further, a lid 3 having a large number of small holes 3a through which water passes is fitted into the upper end of the inner cylinder 1 after the filter medium 2 is filled therein. A small hole 1c is also provided at the bottom of the inner cylinder 1.
The inner cylinder 1 shown in FIG. 3 is housed in the cylinder 5 shown in FIG. The cylindrical body 5 shown in FIG. 2 is provided with a pair of communicating portions 5a and 5b with lids 6a and 6b at positions facing the upper end of the side surface. The cylindrical body 5 is also provided with a pair of communicating portions 5c and 5d with lids 7a and 7b at positions facing the lower end of the side surface.
[0012]
The communicating portion 5b at the upper end of one cylindrical body 5 has a structure that can be fitted to the communicating portion 5a at the upper end of the cylindrical body 5 (not shown) adjacent to the right side. A continuous water channel is formed between the two cylinders 5,5. Similarly, a water channel can be formed by fitting between the communicating portions 5c and 5d between the lower ends of two adjacent cylinders 5 and 5. Even when they are not directly fitted, they can be connected by a rubber or plastic pipe.
A connection method is also possible in which a communication portion 5d at the lower end of the cylindrical body 5 and a communication portion 5a at the upper end of the cylindrical body 5 (not shown) adjacent to the right side thereof are connected by a pipe.
[0013]
If small holes with lids 5f, 5g, 5h, 5i are formed on the side surfaces outside the upper and lower communication portions 5a to 5d of the cylindrical body 5, they can be used as vent holes or drain holes as needed.
For example, when an abnormal gas is generated inside the cylindrical body 5, the gas can be removed by opening the lids of the upper small holes 5f and 5g at that portion. Further, when there is a sediment or the like, the lids of the lower small holes 5h and 5i can be opened and discharged.
[0014]
Further, by utilizing the small holes, a part of the water in the cylinder 5 in the nitrification area by the aerobic microorganisms is taken out at a stage before entering the cylinder in the denitrification area by the anaerobic microorganisms, and this is returned to the water tank. It can also be used to regulate water quality and growth of anaerobic microorganisms.
That is, if the total length of the cylinders constituting the nitrification area is too short, the amount of water is too large, or the amount of the filter medium is too small compared to the amount of water, the oxygen of the water flowing into the anaerobic area is reduced. It is necessary to take out some of the water before entering the anaerobic area while monitoring the water quality, since the residual amount may become excessive and affect the growth of anaerobic microorganisms in the anaerobic area. It can be used as an outlet of the bypass path in the case.
[0015]
Although the bottom of the cylinder 5 is closed, the top is an opening for taking the inner cylinder 1 in and out, and the lid 8 is provided so that it can be opened and closed.
As described above, since the cylindrical body storing the filter medium 2 is a unit formed into a cartridge of the same standard, not only can it be manufactured at low cost, but also by connecting an appropriate number of cylindrical bodies 5, a purification device of a required length can be obtained. Can be assembled.
In assembling, the cylinders 5 are arranged in parallel so that the longitudinal direction is directed to the vertical direction, and the upper and lower communication portions 5a to 5d are sequentially connected alternately, and unnecessary communication portions are closed by lids. As a whole, a long zigzag channel can be formed as shown by the arrow in FIG.
A similar long zigzag water channel can also be made by connecting the lower communication portion 5d and the upper communication portion 5a of the cylindrical body adjacent to the right with a pipe and repeating the connection.
In addition, it is also possible to make a block in which a plurality of cylinders 5 are combined in advance, and use these blocks connected.
[0016]
In actual use, the water to be purified is introduced into the communicating portion 5a of the state-of-the-art cylinder 5, and a filter medium suitable for physical filtration is sealed in the inner cylinder 1.
Further, a filter medium suitable for propagation of anaerobic microorganisms is sealed in the final-stage cylinder 5, and purified water is drained from the communication section 5b.
[0017]
【Example】
Taking the case where the present invention is applied to an aquarium fish purifying apparatus as an example, the following is obtained.
Each cylinder 5 has a diameter of about 3 cm and a length of about 30 cm.
In a 60 cm wide square water tank generally called a 60 type, eight of these are connected and used, and in that case, the effective total length of the cylindrical body is about 2 m28 cm. In the case of a water tank with a width of 120 cm, the total length is about 4 m56 cm by connecting eight more.
[0018]
FIG. 4 and FIG. 5 show the results of a comparison experiment with the most common purification device on the market when the device of the present invention was used in a 60-type water tank. (Experimenter: Masamichi Tsuji, Associate Professor, Tokyo Institute of Technology) The experiment was carried out using the same amount of water in the same aquarium and releasing 20 healthy angelfish each.
For the water tank for comparison, a 2426 type filter manufactured by Eheim Co. was used. For this, 2.5 l of Ehi Substrut and 1.5 l of Eheimmech recommended by the company were used. On the other hand, in the apparatus of the present invention, a sponge filter and a wool mat were used for the first stage physical filtration, and 0.88 l of a power house M type and 0.88 l of an S type were used in the aerobic filtration area. In the anaerobic filtration zone at the last stage, 100 g of Deniball (trade name) which is an organic carbon preparation was used.
[0019]
As a result, as shown in FIG. 4, the nitrate concentration of the filtered water started to increase in both devices 15 to 18 days after the start of the experiment, but in the device of the present invention, it gradually started to decrease from around 23 to 24 days, and after 60 days. While it remained almost constant, it still continued to rise in the comparison tank. As shown in FIG. 5, the pH of the apparatus of the present invention was almost stable at 7.0, while the pH of the comparative water tank continued to drop sharply. And the experiment had to be stopped.
[0020]
It should be noted that the device of the present invention continues to grow healthy even after 9 months. In other words, it means that there is no need to change the water at a normal level of ornamental fish breeding, and it can be said that the inconvenience of water changing, which was the biggest problem in breeding, was eliminated.
In addition, in the apparatus of the present invention, although nitrate increased in the same manner as the comparative water tank at first, it eventually turned to decrease, although initially there was almost no anaerobic microorganisms in the waterway, It is presumed that cultivation of anaerobic microorganisms was promoted by the cultivation of anaerobic environment and the action of organic carbon, and the original functions began to work.
[0021]
In the above embodiment, the purification of the ornamental fish tank has been described. However, the present invention can be similarly applied to a case where the water to be purified is sewage, human waste, river water, or the like. Depending on the quality of the water to be purified, the content of organic matter that is a nutrient source for the propagation of anaerobic microorganisms may be low from the beginning. By arranging organic plastic, organic carbon, and the like, which are the nutrient sources of the water, it is possible to cope with the water to be purified of any property.
[0022]
[Effects of the present invention]
As described above, the present invention uses an elongated closed waterway to create a favorable environment for anaerobic microorganism growth at the final stage, and to purify water almost neutrally by the denitrification effect brought by the anaerobic microorganism. And a device capable of continuously performing the same for a long period of time with a single device.
In addition, by forming the elongated water channel in a zigzag shape by connecting the cylindrical bodies, there is an advantage that the occurrence of the channel phenomenon is minimized, the filter medium can be easily replaced, and the apparatus can be downsized.
[Brief description of the drawings]
FIG. 1 is a view for explaining a basic principle of the present invention; FIG. 2 is a view showing a structure of a cylinder used as a water channel of the present invention; FIG. 3 is an inner cylinder inserted into the inside of the cylinder; FIG. FIG. 5 is a graph showing an experimental result of the apparatus of the present invention. FIG. 5 is a graph showing an experimental result of the apparatus of the present invention.
1 ... inner cylinder, 1a ... central axis of inner cylinder, 1c ... small hole,
2 ... filter medium, 3 ... lid of inner cylinder, 3a ... small hole, 5 ... cylindrical body, 5a to 5d ... communication part, 5f to 5i ... small hole,
6a-6b ... lid of upper communication part, 7a-7b ... lid of lower communication part,
8 ... Cylinder lid

Claims (3)

複数個の筒体を、
長手方向が鉛直方向に向かうよう並列配置し、
その上下で交互に水流的に連結し、
細長く閉鎖された水路をジグザグ状に形成し、
被浄化排水の入口側筒体に物理的ろ過材を封入し、
終段の筒体を嫌気性バクテリアによる生物ろ過部とし、
中間部を好気性バクテリアによる生物ろ過部とした水の浄化装置。
Several cylinders,
It is arranged in parallel so that the longitudinal direction goes to the vertical direction,
The upper and lower parts are alternately connected in a stream,
Form an elongated closed water channel in a zigzag shape,
Enclose physical filtration material in the inlet side cylinder of the wastewater to be purified,
The final stage cylinder is used as a biofiltration part by anaerobic bacteria,
Water purification device with the middle part as biological filtration part by aerobic bacteria.
複数個の筒体を、
長手方向が鉛直方向に向かうよう並列配置し、
その上下で交互に水流的に連結し、
細長く閉鎖された水路をジグザグ状に形成し、
前記筒体の中には、蓋及び底部に水が通過する多数の小孔を設けた内筒を収納し、
被浄化排水の入口側に近い筒体の内筒を好気性バクテリアによる生物ろ過部とし、
被浄化排水の出口側に近い部分の筒体の内筒を嫌気性バクテリアによる生物ろ過部とした水の浄化装置。
Several cylinders,
It is arranged in parallel so that the longitudinal direction goes to the vertical direction,
The upper and lower parts are alternately connected in a stream,
Form an elongated closed water channel in a zigzag shape,
In the cylindrical body, an inner cylinder provided with a number of small holes through which water passes on a lid and a bottom portion is housed,
The inner cylinder of the cylinder close to the inlet side of the wastewater to be purified is used as a biological filtration unit for aerobic bacteria,
A water purification device in which the inner cylinder of the portion near the outlet side of the wastewater to be purified has a biological filtration unit for anaerobic bacteria.
複数個の筒体を、
長手方向が鉛直方向に向かうよう並列配置し、
その上下で交互に水流的に連結し、
細長く閉鎖された水路をジグザグ状に形成し、
前記筒体の中には、蓋及び底部に水が通過する多数の小孔を設けた内筒を収納し、
被浄化排水の入口側の筒体の中の内筒に物理的ろ過材を封入し、最終段階の筒体の内筒を嫌気性バクテリアによる生物ろ過部とし、
中間部の筒体の内筒を好気性バクテリアによる生物ろ過部とした水の浄化装置。
Several cylinders,
It is arranged in parallel so that the longitudinal direction goes to the vertical direction,
The upper and lower parts are alternately connected in a stream,
Form an elongated closed water channel in a zigzag shape,
In the cylindrical body, an inner cylinder provided with a number of small holes through which water passes on a lid and a bottom portion is housed,
A physical filtration material is sealed in the inner cylinder in the cylinder on the inlet side of the wastewater to be purified, and the inner cylinder of the final stage cylinder is used as a biofiltration unit using anaerobic bacteria.
A water purifier that uses the inner cylinder of the middle cylinder as a biological filtration unit for aerobic bacteria.
JP2000340882A 2000-11-08 2000-11-08 Water purification method and apparatus Expired - Fee Related JP3577663B2 (en)

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JP6133414B2 (en) * 2013-05-17 2017-05-24 俊介 高田 Water purification apparatus and method
KR101444206B1 (en) * 2014-06-12 2014-10-08 대한민국 Multi -process system for aquaculture waste water with package type bio-filter
JP6024807B2 (en) * 2015-02-16 2016-11-16 栗田工業株式会社 Biological treatment tank, operation method thereof, and organic wastewater treatment method
CN108430216B (en) * 2015-12-22 2022-04-12 国立大学法人东京海洋大学 Denitrification device and aquatic organism feeding system
CN109854193B (en) * 2019-02-23 2023-07-14 中国石油大学(华东) Mud circulation system and method for submarine drilling machine
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