JPH0663593A - Water purifying method and device for closed water area - Google Patents

Water purifying method and device for closed water area

Info

Publication number
JPH0663593A
JPH0663593A JP24722592A JP24722592A JPH0663593A JP H0663593 A JPH0663593 A JP H0663593A JP 24722592 A JP24722592 A JP 24722592A JP 24722592 A JP24722592 A JP 24722592A JP H0663593 A JPH0663593 A JP H0663593A
Authority
JP
Japan
Prior art keywords
water
air
closed
far
mixture
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
Application number
JP24722592A
Other languages
Japanese (ja)
Other versions
JP3216054B2 (en
Inventor
Hachiro Yoshizawa
八郎 吉澤
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.)
Individual
Original Assignee
Individual
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Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to JP24722592A priority Critical patent/JP3216054B2/en
Publication of JPH0663593A publication Critical patent/JPH0663593A/en
Application granted granted Critical
Publication of JP3216054B2 publication Critical patent/JP3216054B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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

Landscapes

  • Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
  • Physical Water Treatments (AREA)
  • Biological Treatment Of Waste Water (AREA)

Abstract

PURPOSE:To maintain an excellent water purifying capacity over a long period of time and to effectively remove green algae, etc., by pressurizing and blowing a air- water mixture formed by mixing fine bubbles with water to a water purifying area and successively passing a far IR radiation area and microorganism water purifying area. CONSTITUTION:Water is sucked through a suction pipe 6 from a net cylinder screen 7 and is discharged from a discharge pipe 8 in the tangent direction within a mixing chamber 15 when the water purifying device is installed on the bottom of a pond a submersible pump 5 is driven and compressed to an air-water mixer 9 via an air supply hose. The fine bubbles are incorporated into the discharge water from the air-water mixer 9 at the time of discharge and the air-water mixture is made into swirling flow in the air-water mixing chamber 15, by which the sand, etc., in the sea water are centrifugally separated. The air-water mixture is then made into rising flow and is successively passed through a far IR septic tank 17 and a microorganism treatment tank 19, by which the air-water mixture is subjected to treatments, such as sterilization treatment and decomposition of org. solids. The air-water mixture is then released upward. The such operations are successively executed, by which the water in the pond is subjected to a circulation treatment.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】この発明は、大型水槽、プール、
池等の水中へ沈設して循環淨水することを目的とした閉
水域の淨水方法及び装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a large aquarium, pool,
The present invention relates to a method and a device for draining water in a closed water area for the purpose of submersing in a water such as a pond and circulating water.

【0002】[0002]

【従来の技術】従来閉水域へ沈設して大量水を淨水する
技術としては、間欠空気揚水装置を使用した循環淨水方
法が知られている(特開平3−52694号)。
2. Description of the Related Art Conventionally, as a technique for immersing a large amount of water by sinking it in a closed water area, a circulation rectifying method using an intermittent air pumping device is known (Japanese Patent Laid-Open No. 3-52694).

【0003】[0003]

【発明により解決すべき課題】前記従来の淨水方法は、
溶存酸素の改善及びこれによる水底側有機物を微生物処
理する点で優れた効果を示し、大量水の改善については
匹敵する技術がない程優れている。然し乍ら比較的少水
量(例えば数トン〜数百トン)を高度に淨水することに
ついては、今後の研究にまつ所が多い。また微生物を利
用した淨水について、ハニカム使用のものが知られてお
り、排水処理においては、それなりの効果を示している
が、大型水槽、池などの淨水としては滿足すべきものが
ない。
DISCLOSURE OF THE INVENTION Problems to be Solved by the Invention
It has an excellent effect in terms of improving dissolved oxygen and microbial treatment of organic matter on the water bottom side, and is excellent in improving a large amount of water so that there is no comparable technology. However, there are many points for future research regarding the high level of cleansing of a relatively small amount of water (for example, several tons to several hundreds of tons). As for the fresh water using microorganisms, the one using a honeycomb is known, and although it shows a certain effect in the wastewater treatment, there is no sufficient fresh water for a large water tank, a pond or the like.

【0004】一方家庭用等の淨水器は各種提案されてい
るが、何れも一度の通過で目的を達成しようとするもの
で、循環淨水とは処理思想を異にしている。
On the other hand, various types of water purifiers for household use have been proposed, but all of them are intended to achieve the purpose by passing them once, and have a different treatment concept from that of circulating fresh water.

【0005】[0005]

【課題を解決する為の手段】然るにこの発明は、淨化水
域に沈設し、吸入水に微細気泡を混入すると共に、遠赤
外線淨化及び微生物処理を行うことにより、淨化水域を
循環淨化することにより前記従来の問題点を解決したの
である。
SUMMARY OF THE INVENTION However, according to the present invention, the deep water is circulated and circulated by performing deep infrared ray sterilization and microbial treatment while depositing fine water bubbles in inhalation water by depositing in the sterilized water area. It solved the conventional problem.

【0006】然してこの発明において用いる資材は、空
気、遠赤放射物質及び微生物であるから、2次公害を発
生するおそれなく、使用動力は水中ポンプ及び空気ポン
プのみであるから、長時間の連続使用に対し、故障を生
じるおそれがきわめて少ないなどの利点がある。前記水
中ポンプに代えて流体ジエツト(水又は空気を加圧噴出
させる)を使用すれば、水中で動く固体は皆無となり、
故障も皆無となる。
However, since the materials used in the present invention are air, far-infrared radiation substances and microorganisms, there is no fear of causing secondary pollution, and the power used is only the submersible pump and the air pump. On the other hand, there is an advantage that the risk of failure is extremely low. By using a fluid jet (pressurizing water or air) instead of the submersible pump, there is no solid moving in water,
There will be no breakdown.

【0007】即ちこの発明は、微細気泡を淨水すべき水
に混合して得た気水混合物を淨水域に加圧して吹き込
み、ついで前記混合物を、遠赤外線放射域を通過させた
後、微生物淨化域を通過させて淨化閉水域の水を循環処
理することを特徴とした閉水域の淨水方法である。また
他の発明は、気水混合物に、旋回力を付与して淨水域へ
吹き込むものであり、遠赤外線放射域は、遠赤外線ボー
ルの層又は遠赤外線多孔質層としたものである。次に物
の発明は、淨化閉水域へ沈設して、循環淨化する装置に
おいて、淨化すべき水の吸入手段、該水中へ微細気泡を
吹き込む手段、遠赤外線淨化手段及び微生物処理手段を
結合することを特徴とした閉水域の淨水装置であり、淨
化すべき水の吸入手段、該水中へ微細気泡を吹き込む手
段。遠赤外線淨化手段及び微生物処理手段を結合した淨
水装置と、水中吊下手段を備えた水中ポンプに噴水手段
を結合させた噴水装置とを組み合せたことを特徴とする
閉水域の淨水装置である。更に他の発明は淨化閉水域へ
沈設して、循環淨化する装置において、架台上へ、水中
ポンプを架設し、水中ポンプの吸入管端へスクリーンを
設けると共に、吐出管へ、気水混合器を設け、吐出管端
を、架台上の淨水槽下部へ接線方向より挿入開口し、前
記淨水槽の下部を、前記気水混合物の吹込み室とし、該
吹込み室の上部へ遠赤外線淨化層を設け、該遠赤外線淨
化層の上部へ微生物処理層を設けたことを特徴とする閉
水域の淨水装置であり、気水混合器は、吐出管の一側
へ、散気盤を設け、散気盤の外側へ加圧空気室を設け、
加圧空気室へ送気ホースを連結したものである。
That is, according to the present invention, a water-air mixture obtained by mixing fine bubbles with water to be brewed is pressurized and blown into the basin of water, and then the mixture is passed through a far infrared radiation region, It is a method of rectifying water in a closed water area, which is characterized by circulating water in the chilled water area after passing through the microbial water area. In another invention, a swirling force is applied to a mixture of air and water to blow it into a fresh water region, and the far infrared radiation region is a layer of far infrared balls or a far infrared porous layer. Next, the invention of the product is to combine the suction means of water to be sterilized, the means for blowing fine bubbles into the water, the far-infrared sterilization means, and the microbial treatment means in a device for circulatory sterilization by sinking into a sterilized closed water area A water discharge device for a closed water region, which is characterized by: a suction means for water to be scavenged; a means for blowing fine bubbles into the water. A freshwater device for a closed water area, characterized by combining a freshwater device combining far-infrared rectifying means and microbial treatment means, and a fountain device combining a fountain means with an underwater pump equipped with an underwater suspension means. is there. Still another invention is an apparatus for submerging into a water-cooled closed area and circulating and circumventing, by installing a submersible pump on a pedestal, providing a screen at the suction pipe end of the submersible pump, and a gas-water mixer to the discharge pipe. Provided, the discharge pipe end is tangentially inserted and opened to the lower part of the water tank on the pedestal, and the lower part of the water tank serves as a blowing chamber for the gas-water mixture, and the far infrared ray conversion layer is formed on the upper part of the blowing chamber. It is a fresh water device in a closed water region, characterized in that a microbial treatment layer is provided on the far infrared ray decontamination layer, wherein the air / water mixer is provided with an air diffuser on one side of the discharge pipe. A pressurized air chamber is provided outside the air board,
An air supply hose is connected to the pressurized air chamber.

【0008】この発明によれば遠赤外線淨化処理によっ
て有害化学物質の分解、水質改善を行うと共に、微生物
処理によって水中に含まれた有機固形物を処理すること
ができる。従つて処理水の水質は急速に改善され、透明
度を著しく改善することができる。
According to the present invention, harmful chemical substances can be decomposed and water quality can be improved by the far infrared ray sterilization treatment, and organic solid matter contained in water can be treated by the microbial treatment. Therefore, the water quality of the treated water is rapidly improved, and the transparency can be significantly improved.

【0009】この発明における吸水容量は、淨化水域の
水量、淨化目的、流入水の水質などによって、適宜定め
る。例えば公園の池のように専ら雨水の流入のみの場合
(生活排水の流入がない)には、1ケ月で全水を通過で
きる容量でよく、生活排水の流入がある場(流入量の割
合にもよるが)には5日〜10日で全水を通過できる容
量とする。具体的には、1時間で10m3 の吸入ポンプ
を使用すれば1日で240m3 であり、10日で240
0m3 となる。
The water absorption capacity in the present invention is appropriately determined according to the amount of water in the water purification area, the purpose of water purification, the quality of the inflow water, and the like. For example, in the case of only rainwater inflow (no domestic effluent inflow), such as in a pond in a park, the capacity that can pass all the water in one month is sufficient, and when the domestic effluent inflow (the ratio of the inflow rate is Depending on the amount of water), the capacity should be such that all water can pass in 5 to 10 days. Specifically, if an inhalation pump of 10 m 3 is used for 1 hour, it will be 240 m 3 in 1 day and 240 in 3 days.
It will be 0 m 3 .

【0010】この発明においては、微細気泡(例えば気
孔径1mm以下の散気盤より加圧放出)を水と混合する為
に、気泡中の酸素の溶解効率が向上するのみならず、洗
滌作用があり、遠赤外線放射物(球又は網目状)を淨化
する作用がある。従って長期に亘りクリーニングの必要
がない。微生物処理層は、ペレツト状、多孔質小球、そ
の他表面積の大きい微生物担体に好気性微生物を着床さ
せたものである。野外の池などにおいては、微生物床の
みを設けて運転すれば、運転中に微生物が自然に着床
し、1週間〜2週間経過後には淨化能力を発揮する。
In the present invention, since fine air bubbles (for example, pressure release from a diffuser having a pore diameter of 1 mm or less) are mixed with water, not only the efficiency of dissolving oxygen in the air bubbles is improved but also a cleaning action is obtained. Yes, it has the effect of shaping far-infrared radiation (sphere or mesh). Therefore, there is no need for cleaning for a long period of time. The microbial treatment layer is formed by implanting aerobic microorganisms on pellet-like, porous small spheres or other microbial carriers having a large surface area. In an outdoor pond or the like, if only a microbial bed is provided and operated, the microorganisms will spontaneously implant during the operation, and after 1 to 2 weeks have passed, the sterilization ability will be exhibited.

【0011】[0011]

【作用】この発明によれば、水と微細気泡との混合物を
加圧流入させ、この混合物を遠赤外線淨化層と、微生物
処理層を通過させるので、有害気体及び有機固形物を処
理し、効率よく淨水できる。
According to the present invention, a mixture of water and fine air bubbles is introduced under pressure, and the mixture is passed through the far infrared ray contaminated layer and the microbial treatment layer, so that harmful gas and organic solid matter are treated and efficiency is improved. I can clean water well.

【0012】[0012]

【実施例1】図4に示す水量100m3 の池に毎時吸入
量0.5m3 の水中ポンプを設置し、毎時送気量0.3
3 のコンプレツサーから1.5Kg/cm2 で送気した。
この場合に送気は、厚さ1cm、面積0.1m2 気孔径1
mmの散気盤を用いた。また遠赤外線放射層は直径5mm〜
10mmの遠赤ボールを厚さ5cm、面積1m2 の層にし
た。次に微生物処理層は、厚さ10cm、面積1m2 で、
5mm〜10mmの多孔性無機質のペレツトを用いて構成し
た。
[Embodiment 1] A submersible pump having an intake volume of 0.5 m 3 per hour was installed in a pond having an amount of water of 100 m 3 shown in FIG.
Air was supplied at 1.5 kg / cm 2 from a m 3 compressor.
In this case, the air supply is 1 cm in thickness and 0.1 m 2 in area and 1 in pore size.
A mm air diffuser was used. The far-infrared radiation layer has a diameter of 5 mm
A 10 mm far-infrared ball was formed into a layer having a thickness of 5 cm and an area of 1 m 2 . Next, the microbial treatment layer has a thickness of 10 cm and an area of 1 m 2 .
It was constructed using a porous inorganic pellet of 5 mm to 10 mm.

【0013】前記実施例によれば、1日12m3 の吸入
量があるので、8〜9日の稼動により全水を処理するこ
とができた。前記により、当初BOD200 ppm、CO
D100 ppm、水深30cm透明であったものが、処理1
0日後にBOD5 ppm、COD2 ppm、水深2m透明
(水底が見える)となり、全水の溶存酸素量がほゞ飽和
状態となつた。
According to the above-mentioned embodiment, since the inhalation amount is 12 m 3 per day, all the water could be treated by the operation for 8 to 9 days. According to the above, initially BOD 200 ppm, CO
D100 ppm, water depth 30 cm, transparent treatment 1
After 0 days, BOD was 5 ppm, COD was 2 ppm, the water depth was 2 m, and the water was transparent (the water bottom was visible), and the dissolved oxygen content of the total water was almost saturated.

【0014】[0014]

【実施例2】池1の水底2へ設置する為に、架台3上
へ、有底の円筒4を設置し、その外側へ水中ポンプ5を
設置する。水中ポンプ5の吸入管6の先端には、網筒ス
クリーン7を連結し、水中ポンプ5の吐出管8の先端
は、前記円筒4へ接線的に挿入開口し、該吐出管8の挿
入部へ気水混合器9を付設する。気水混合器9は、カバ
ー10内が散気盤11と空気室12とに分離され、空気
室12に加圧空気の送気ホース13を連結する。前記散
気盤11は、無数の微細連続気孔(直径1mm以下)を有
する無機質盤で、微細気泡14を、吐出水中に散気す
る。前記円筒4の下部は混合室15となつており、混合
室15の上に、網板16を介し遠赤外線淨化層17が設
けられ、その上に網板18を介して微生物処理層19が
設けてある。前記遠赤外線淨化層17は、大小の遠赤ボ
ール(5mm〜10mm)を充填して形成し、微生物処理層
19は、微細孔ペレツト20を集積して構成してある。
図中21は網筒スクリーンの架台、22は網板、23は
電線コードである。
[Example 2] In order to install on the water bottom 2 of the pond 1, a bottomed cylinder 4 is installed on a pedestal 3, and an underwater pump 5 is installed on the outside thereof. A mesh screen 7 is connected to the tip of the suction pipe 6 of the submersible pump 5, and the tip of the discharge pipe 8 of the submersible pump 5 is tangentially inserted into the cylinder 4 and opened to the insertion portion of the discharge pipe 8. A steam mixer 9 is attached. In the air / water mixer 9, the cover 10 is divided into an air diffuser 11 and an air chamber 12, and an air supply hose 13 for pressurized air is connected to the air chamber 12. The air diffuser plate 11 is an inorganic plate having an infinite number of fine continuous pores (diameter of 1 mm or less), and diffuses the fine air bubbles 14 into the discharge water. The lower part of the cylinder 4 is connected to a mixing chamber 15, and a far infrared ray conversion layer 17 is provided on the mixing chamber 15 via a mesh plate 16 and a microbial treatment layer 19 is provided thereon via a mesh plate 18. There is. The far-infrared ray conversion layer 17 is formed by filling large and small far-infrared balls (5 mm to 10 mm), and the microbial treatment layer 19 is formed by accumulating micropore pellets 20.
In the figure, 21 is a screen cylinder screen mount, 22 is a mesh plate, and 23 is an electric wire cord.

【0015】前記実施例において、水中ポンプ5を始動
すると共に、送気ホース13を介して矢示24のように
加圧空気を供給すると、池1の水底2の水は、網筒スク
リーン7へ矢示25のように吸入され、吸入管6を経て
水中ポンプ5に入り、吐出管8から矢示26のように放
出される。一方送気ホース13から供給された加圧空気
は、空気室12から散気盤11を経て吐出管8内へ放出
され、吐出管8内の水と共に混合室15内へ吹き出され
る。この場合に吐出管8の先端側が、円筒4に対し、接
線方向から、挿入されている為に、気水混合物は矢示2
7、28のように旋回流となって移動する。そこで無機
固形物(例えは砂)などは遠心力を受けて円筒壁側に分
離され、円筒壁に沿って下降する。一方気水混合物は矢
示29のように上昇して遠赤外線淨化層17を通過し、
遠赤外線の淨水、殺菌などの作用を受ける。ついで矢示
30のように微生物処理層19を通過する間に微生物の
処理を受けて有機固形物が分解される(例えば1回の通
過によりほゞ30%の処理可能)。前記微生物処理層1
9を通過した気水混合物は、矢示31のように上昇して
(加圧効果と、微細気泡の浮力により上昇する)水面に
到り、矢示32、32のように放射状に拡散する。この
場合の気水混合物の温度は水深によっても異るが、通常
水底側の水温が低いので、拡散しつつ下降する。このよ
うにして下降した水は再び吸入されるので、結局循環処
理されることになる。
In the above embodiment, when the submersible pump 5 is started and pressurized air is supplied through the air supply hose 13 as indicated by the arrow 24, the water at the bottom 2 of the pond 1 is transferred to the screen cylinder screen 7. It is inhaled as shown by the arrow 25, enters the submersible pump 5 through the suction pipe 6, and is discharged as shown by the arrow 26 from the discharge pipe 8. On the other hand, the pressurized air supplied from the air supply hose 13 is discharged from the air chamber 12 into the discharge pipe 8 through the air diffuser 11 and is blown out into the mixing chamber 15 together with the water in the discharge pipe 8. In this case, since the tip end side of the discharge pipe 8 is inserted into the cylinder 4 from the tangential direction, the mixture of air and water is indicated by the arrow 2.
It moves as a swirling flow like 7, 28. Then, the inorganic solid matter (for example, sand) is subjected to centrifugal force, separated into the cylindrical wall side, and descends along the cylindrical wall. On the other hand, the air-water mixture rises as shown by the arrow 29 and passes through the far infrared ray conversion layer 17,
Receives far-infrared water and sterilization. Then, as shown by the arrow 30, while passing through the microorganism treatment layer 19, the organic solid matter is decomposed by the treatment of microorganisms (for example, about 30% of treatment can be performed by one passage). The microbial treatment layer 1
The air-water mixture passing through 9 rises as indicated by arrow 31 (increases due to the pressurizing effect and the buoyancy of fine bubbles), and diffuses radially as indicated by arrows 32 and 32. Although the temperature of the air-water mixture in this case varies depending on the water depth, since the water temperature on the water bottom side is usually low, the temperature of the air-water mixture drops while diffusing. The water descended in this way is sucked again, so that it is eventually circulated.

【0016】前記における拡散距離は比較的短かい(例
えば半径10m〜20m)ので、前記円筒4と網筒スク
リーンとの間隔を調整し、又は網筒スクリーンの設置位
置を変えたり、複数設置にし、或いは一定時間毎に全装
置を移動し、又は複数の装置を適宜配置するなどの工夫
を要する。この発明の装置を適切に使用する時には、飲
用に適する程の淨化能力を発揮することができる。
Since the diffusion distance in the above is relatively short (for example, a radius of 10 m to 20 m), the interval between the cylinder 4 and the mesh tube screen is adjusted, or the installation position of the mesh tube screen is changed or a plurality of mesh screens are installed. Alternatively, it is necessary to move all the devices at regular intervals or arrange a plurality of devices appropriately. When the device of the present invention is used properly, it can exhibit the potting ability suitable for drinking.

【0017】図4の水面に近接して、浮子33により水
中ポンプ34を浮吊下し、水中ポンプ34にノズル35
を直立設置する。然る時は、水中ポンプ34の始動によ
り、噴水36を所定高さまで噴出させることができる。
前記噴水はエアレーシヨンになると共に、池に噴水の景
観を与える効果がある。
A submersible pump 34 is suspended by a float 33 in the vicinity of the water surface of FIG.
Upright. In that case, by starting the submersible pump 34, the fountain 36 can be ejected to a predetermined height.
The fountain becomes an air race and has an effect of giving a landscape of the fountain to the pond.

【0018】[0018]

【発明の効果】この発明によれば、微細気泡を含む気水
混合物を淨化域に加圧して吹き込み、ついで前記混合物
を遠赤外線放射域と、微生物処理域を順次通過させて処
理するので、有害物及び有機固形物をほゞ完全に処理で
きる効果がある。また浅水域に発生し易い緑藻類(例え
ばアオコ)についても有効に除去し得る効果がある。
EFFECTS OF THE INVENTION According to the present invention, a gas-water mixture containing fine bubbles is pressurized and blown into the conditioned area, and then the mixture is processed by sequentially passing through the far-infrared radiation area and the microbial treatment area. It has the effect that almost all substances and organic solids can be treated. It also has an effect of effectively removing green algae (for example, blue-green algae) that tend to occur in shallow water.

【図面の簡単な説明】[Brief description of drawings]

【図1】この発明の実施例の一部切断した正面図。。FIG. 1 is a partially cutaway front view of an embodiment of the present invention. .

【図2】同じく一部切断した平面図。FIG. 2 is a partially cutaway plan view of the same.

【図3】同じく気水混合器の拡大断面図。FIG. 3 is an enlarged cross-sectional view of the steam mixer.

【図4】同じく設置状態を示す断面図。FIG. 4 is a sectional view showing an installed state of the same.

【符号の説明】[Explanation of symbols]

1 池 2 水底 4 円筒 5 水中ポンプ 6 吸入管 7 網筒スクリーン 8 吐出管 9 気水混合器 10 カバー 11 散気盤 12 空気室 15 混合室 17 遠赤外線淨化層 19 微生物処理層 1 Pond 2 Water bottom 4 Cylinder 5 Submersible pump 6 Suction pipe 7 Net cylinder screen 8 Discharge pipe 9 Air-water mixer 10 Cover 11 Air diffuser 12 Air chamber 15 Mixing chamber 17 Far infrared ray conversion layer 19 Microbial treatment layer

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】 微細気泡を淨水すべき水に混合して得た
気水混合物を淨水域に加圧して吹き込み、ついで前記混
合物を、遠赤外線放射域に通過させた後、微生物淨化域
を通過させて淨化閉水域の水を循環処理することを特徴
とした閉水域の淨水方法
1. A water-air mixture obtained by mixing fine air bubbles with water to be washed is pressurized and blown into a fresh water region, and then the mixture is passed through a far-infrared radiation region, and then a microbial cleansing region. Method for circulating closed water by circulating water through the closed water
【請求項2】 気水混合物に、旋回力を付与して淨水域
へ吹き込むことを特徴とした請求項1記載の閉水域の淨
水方法
2. The method for flushing a closed water area according to claim 1, wherein a swirling force is applied to the air-water mixture and the mixture is blown into the fresh water area.
【請求項3】 遠赤外線放射域は遠赤外線ボールの層又
は遠赤外線多孔質層とした請求項1記載の閉水域の淨水
方法
3. The method for draining water in a closed water area according to claim 1, wherein the far infrared radiation region is a far infrared ball layer or a far infrared porous layer.
【請求項4】 淨化閉水域へ沈設して、循環淨化する装
置において、淨化すべき水の吸入手段、該水中へ微細気
泡を吹き込む手段、遠赤外線淨化手段及び微生物処理手
段を結合したことを特徴とする閉水域の淨水装置。
4. An apparatus for submerging into a closed closed water area and circulating and circulating the water, wherein a means for sucking water to be cooled, a means for blowing fine bubbles into the water, a far infrared ray cleaning means, and a microorganism treatment means are combined. This is a freshwater device in a closed water area.
【請求項5】 淨化すべき水の吸入手段、該水中へ微細
気泡を吹き込む手段、遠赤外線淨化手段及び微生物処理
手段を結合した淨水装置と、水中吊下手段を備えた水中
ポンプと噴水手段を結合させてなる噴水装置とを組み合
せたことを特徴とする閉水域の淨水装置。
5. An underwater pump and a fountain means having an inhalation means for water to be rectified, a means for blowing fine bubbles into the water, a far-infrared rectification means, and a microbial treatment means, and an underwater suspension means. A water discharge device in a closed water area, which is characterized by being combined with a fountain device formed by combining
【請求項6】 淨化閉水域へ沈設して、循環淨化する装
置において、架台上へ、水中ポンプを架設し、水中ポン
プの吸入管端へスクリーンを設けると共に、吐出管へ気
水混合器を設け、吐出管端を、架台上の淨水槽下部へ接
線方向から挿入開口し、前記淨水槽の下部を、前記気水
混合物の吹込み室とし、該吹込み室の上部へ遠赤外線淨
化層を設け、該遠赤外線淨化層の上部へ微生物処理層を
設けたことを特徴とする閉水域の淨水装置。
6. An apparatus for submerging into a closed closed water area and circulating circulation, wherein an underwater pump is installed on a stand, a screen is provided at an end of a suction pipe of the submersible pump, and a steam-water mixer is provided at a discharge pipe. The discharge pipe end is tangentially inserted into the lower part of the fresh water tank on the gantry, and the lower part of the fresh water tank is used as a blowing chamber for the gas-water mixture, and a far-infrared ray conversion layer is provided on the upper part of the blowing chamber. A water purification device in a closed water area, wherein a microbial treatment layer is provided on the far infrared radiation conversion layer.
【請求項7】 気水混合器は、吐出管の一側へ、散気盤
を設け、散気盤の外側へ加圧空気室を設け、加圧空気室
へ送気ホースを連結した請求項6記載の閉水域の淨水装
置。
7. The air / water mixer has an air diffuser provided on one side of the discharge pipe, a pressurized air chamber provided outside the diffuser, and an air supply hose connected to the pressurized air chamber. 6. A fresh water device in a closed water area according to 6.
JP24722592A 1992-08-24 1992-08-24 Method and apparatus for purifying closed water Expired - Fee Related JP3216054B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP24722592A JP3216054B2 (en) 1992-08-24 1992-08-24 Method and apparatus for purifying closed water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP24722592A JP3216054B2 (en) 1992-08-24 1992-08-24 Method and apparatus for purifying closed water

Publications (2)

Publication Number Publication Date
JPH0663593A true JPH0663593A (en) 1994-03-08
JP3216054B2 JP3216054B2 (en) 2001-10-09

Family

ID=17160320

Family Applications (1)

Application Number Title Priority Date Filing Date
JP24722592A Expired - Fee Related JP3216054B2 (en) 1992-08-24 1992-08-24 Method and apparatus for purifying closed water

Country Status (1)

Country Link
JP (1) JP3216054B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010234324A (en) * 2009-03-31 2010-10-21 Kazunori Koishi Filtration method, filtration apparatus and filter bed
CN108579143A (en) * 2018-05-22 2018-09-28 上海市政工程设计研究总院(集团)有限公司 A kind of flat flow hydraulic cyclone setting pot hydraulic cyclone disperser

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010234324A (en) * 2009-03-31 2010-10-21 Kazunori Koishi Filtration method, filtration apparatus and filter bed
CN108579143A (en) * 2018-05-22 2018-09-28 上海市政工程设计研究总院(集团)有限公司 A kind of flat flow hydraulic cyclone setting pot hydraulic cyclone disperser

Also Published As

Publication number Publication date
JP3216054B2 (en) 2001-10-09

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