JPH09234482A - Florting type water quality purifying device and water quality purifying method - Google Patents

Florting type water quality purifying device and water quality purifying method

Info

Publication number
JPH09234482A
JPH09234482A JP4570796A JP4570796A JPH09234482A JP H09234482 A JPH09234482 A JP H09234482A JP 4570796 A JP4570796 A JP 4570796A JP 4570796 A JP4570796 A JP 4570796A JP H09234482 A JPH09234482 A JP H09234482A
Authority
JP
Japan
Prior art keywords
water
cylindrical support
storage container
bacillator
water quality
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.)
Pending
Application number
JP4570796A
Other languages
Japanese (ja)
Inventor
Yuji Hoshino
星野裕治
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.)
BAIOSUTAA KK
Original Assignee
BAIOSUTAA KK
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 BAIOSUTAA KK filed Critical BAIOSUTAA KK
Priority to JP4570796A priority Critical patent/JPH09234482A/en
Publication of JPH09234482A publication Critical patent/JPH09234482A/en
Pending 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

Abstract

PROBLEM TO BE SOLVED: To provide a floating type water quality purifying device realizing effective water quality cleaning, and a water quality cleaning method using this device. SOLUTION: This device is constituted by floating a device main body 50 in water, which is provided with a cylindrical support 2 suspended from a float 1, a storage container 9 housing an aeration device 10, magnetically ionized water generator 17 and an underwater fan 6, and the dissolved oxygen, water temp. and water pollution degree are contrived to be uniformed by performing an effective flow circulation and aeration among the upper layer, the intermediate layer and the lower layer of the water. Also, effective water quality cleaning is performed by microorganism under the constitution consisting of the device main body 50 and a biological reactor provided with an automatic control device by which a biological injection liquid and a biological activating liquid are diffused in accordance with the degree of pH of the water in response to a pH sensor.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、流れのないもしく
は流れの小さい比較的富栄養化の進んだ閉鎖性海域(内
湾等)、池、湖沼等の水中の窒素及びリンを減少させ、
アオコ(淡水藻)や赤潮の原因となる珪藻類、ラン藻類
等の植物性プランクトンの光合成を抑制し、動物性微生
物の活性を促進することにより、COD(化学的酸素要
求量)もしくはBOD(生化学的酸素要求量)を低下さ
せる水質浄化装置及び水質浄化方法に関する。
TECHNICAL FIELD The present invention reduces nitrogen and phosphorus in water of a relatively highly eutrophic closed sea area (inner bay, etc.) where there is little or no flow of water, ponds, lakes, etc.,
By suppressing photosynthesis of phytoplankton such as diatoms and cyanobacteria that cause red tide (freshwater algae) and red tide, and promoting the activity of animal microorganisms, COD (chemical oxygen demand) or BOD (raw oxygen) The present invention relates to a water purification device and a water purification method that reduce the chemical oxygen demand).

【0002】[0002]

【従来の技術】日本では閉鎖性海域に対して1993年
窒素、リンの環境基準と排水基準が施行されたが、これ
は栄養塩である窒素、リンが存在すると空気中の炭酸ガ
スを吸収して光合成を行って赤潮を引き起こす藻類が大
量に増えたり、増殖した藻類が沈澱し分解され嫌気性の
貧酸素水塊の形成による青潮の発生での底生魚貝類のへ
い死が起ることに由来している。
2. Description of the Related Art In Japan, environmental standards for nitrogen and phosphorus and drainage standards were enforced in closed sea areas in 1993. When nitrogen and phosphorus, which are nutrient salts, are present, they absorb carbon dioxide in the air. A large amount of algae that cause red tide by photosynthesis are generated, or the algae that have proliferated are precipitated and decomposed and the anaerobic anoxic water mass is formed, resulting in the death of benthic fish and shellfish due to the generation of blue tide. doing.

【0003】このように、海は広大であるとしても、汚
濁物(農業用肥料、洗剤、有機汚濁物質)が流入し続け
ると海の自浄能力にも限界が生じ、死の海になる危険が
ある。
As described above, even if the sea is vast, if the pollutants (agricultural fertilizers, detergents, organic pollutants) continue to flow in, the self-cleaning ability of the sea will be limited, and there is a danger of becoming a dead sea. is there.

【0004】また一方では、池、湖沼、川のように汚水
が小量の水を汚染した場合には、好気性バクテリア(有
機物質を酸化する)が速い速度で溶存酸素(disso
lved oxygen;略してDO)を吸収する。
On the other hand, when polluted water pollutes a small amount of water, such as ponds, lakes and rivers, aerobic bacteria (which oxidize organic substances) are rapidly dissolved oxygen (disso).
lved oxygen (DO for short) is absorbed.

【0005】この点、水面が非常に広い場合には酸素が
バクテリアによる吸収速度よりも速く溶け込むので溶存
酸素は維持されるのであるが、水面が小さい場合は嫌気
環境となって自浄作用が低下し、魚等の生き物はそこに
住めなくなる。
In this respect, when the water surface is very wide, oxygen dissolves faster than the rate of absorption by bacteria, so dissolved oxygen is maintained, but when the water surface is small, it becomes an anaerobic environment and the self-cleaning action deteriorates. , Creatures such as fish cannot live there.

【0006】このように河川、湖沼及び内湾等の閉鎖性
海域の汚染は容存酸素の量を著しく低下させて生態系を
狂わせ、終局的には酸素がなくても繁殖し硫化水素のよ
うな有毒ガスをつくる嫌気性バクテリア以外に生物がい
ない悪臭を放つ不毛の河川、湖沼、ヘドロの堆積する海
洋となってしまうのである。
As described above, pollution of closed sea areas such as rivers, lakes and marshes significantly reduces the amount of stored oxygen and upsets the ecosystem, and eventually breeds even without oxygen, such as hydrogen sulfide. It becomes barren rivers, lakes and marshes, where odors are present and there is no living thing other than anaerobic bacteria that produce toxic gases, and sludge is deposited.

【0007】したがって、内湾、河川、湖沼等の富栄養
化対策、河川、湖沼の水源保全化対策上、窒素、リンの
除去可能な水質浄化処理装置の開発普及が重要となって
きている。
[0007] Therefore, in order to prevent eutrophication of inner bays, rivers, lakes and marshes, and to conserve the water sources of rivers and lakes, it has become important to develop and popularize water purification treatment devices capable of removing nitrogen and phosphorus.

【0008】上記水源の汚染を改善する処理プロセスと
して、エアレーションがある。このエアレーションは自
然の酸化作用を利用して浮遊懸濁微生物により汚水のC
ODあるいはBODを下げる方法である。
Aeration is a treatment process for improving the pollution of the water source. This aeration utilizes the natural oxidative action to suspend the C
This is a method of lowering OD or BOD.

【0009】上記方法では一般的にエアレーションタン
クの下部から水中に気泡を送り込み酸素を供給するよう
になっている。
In the above method, oxygen is generally supplied by sending bubbles from the lower part of the aeration tank into the water.

【0010】[0010]

【発明が解決しようとする課題】しかしながら、従来の
水質浄化装置ないし水質浄化システムにおいては、装置
の巨大化、高コスト、維持管理の煩雑さ等が無視し得な
い問題点となっている。
However, in the conventional water purification apparatus or water purification system, the enormous size of the apparatus, the high cost, the complexity of maintenance and the like are problems that cannot be ignored.

【0011】また、上記従来の水質浄化装置は本体を地
上(水際)または水底に固定設置する構成であって、機
動性に劣り、管によるエアレーションの際に底泥のヘド
ロを巻き上げてしまうので効果的に広範囲を浄化するこ
とは困難であった。
Further, the above-mentioned conventional water purification apparatus has a structure in which the main body is fixedly installed on the ground (at the water's edge) or at the bottom of the water, which is inferior in maneuverability and causes sludge of the bottom mud to be rolled up during aeration by a pipe. It was difficult to purify a wide area.

【0012】したがって、例えば湖沼の著しい透視度の
悪い場所やアオコの繁殖場所を適宜選択的に一台の水質
浄化装置で順次浄化するということは不可能であった。
Therefore, for example, it was not possible to selectively selectively purify a place in a lake or marshes with a poor transparency or a breeding place for blue-green algae by one water purification device.

【0013】また、従来の水質浄化装置におけるバイオ
注液の投入は水中のCOD値に係わりなくやみくもに常
時投入されていたが、これでは無駄が多く維持コストの
面で問題がある。
Further, the injection of the bio-injection in the conventional water purification apparatus is always blindly performed regardless of the COD value in the water, but this is wasteful and there is a problem in terms of maintenance cost.

【0014】本発明は、上記事情に鑑みてなされたもの
であり、陸地や水底に装置を固定するのではなく、対象
とする内湾、河川、湖沼の水中に浮かべるようにした浮
上型の水質浄化装置であって、移動が容易であり、装置
全体が浮いていて底泥のヘドロの巻き上げを起こさず
に、上層部、中層部、及び下層部の環流によって溶存酸
素の均一化、水温の一定化、栄養分の均一化を図ること
ができ、藻類の発生を防止し、上層、中層の微生物層も
安定する構成の浮上型水質浄化装置及び水質浄化方法に
関するものである。
The present invention has been made in view of the above circumstances, and is a floating type water purification system in which the device is not fixed to the land or the bottom of the water but floated in the water of the target inner bay, river or lake. The equipment is easy to move, and the entire equipment floats without causing sludge sludge to wind up, and the dissolved oxygen is homogenized and the water temperature is kept constant by the circulation of the upper, middle, and lower layers. The present invention relates to a floating-type water purification device and a water purification method, which are capable of homogenizing nutrients, preventing the generation of algae, and stabilizing the upper and middle microbial layers.

【0015】[0015]

【課題を解決するための手段】本発明は、 (1)フロートと、前記フロートに吊支され水深に対応
した1〜6mの長さの筒形支柱と、該筒形支柱内の下方
に配置されて筒形支柱の下端近傍の周壁に開けられた導
入口から周囲の水を筒形支柱内に吸入して筒形支柱上端
の開放口へ押し上げる水中ファンと、前記筒形支柱の下
に固定配置されるとともに側壁面下方に噴出口が複数配
設された収納容器の中に配置されたバッキレータと、前
記バッキレータの収納容器側壁に配設されてバッキレー
タ下端周辺の水を吸い上げて前記筒形支柱内下方に配管
を通して送出する水中ポンプと、該水中ポンプにて吸い
上げられた水が通過するように配管途中に配設された磁
気イオン水発生装置と、前記バッキレータの収納容器の
外側に配設したpHセンサーと、該pHセンサーのpH
検出電気信号を水上または地上に伝達する伝達ライン
と、水上または地上に配設されるとともに前記伝達ライ
ンからのpH検出電気信号を受けて水中のpH度に対応
した量の光合成細菌を含むバイオ注液及び動物性微生物
の活性剤を含むバイオ活性液を注入管を通して前記収納
容器内に送るバイオリアクター及びその自動制御装置
と、からなる構造を特徴とする浮上型水質浄化装置を提
供することにより上記課題を達成するものである。
Means for Solving the Problems (1) The float, a cylindrical strut suspended from the float and having a length of 1 to 6 m corresponding to the water depth, and arranged below the cylindrical strut. The submersible fan that sucks the surrounding water into the cylindrical strut from the inlet port opened on the peripheral wall near the lower end of the cylindrical strut and pushes it up to the opening at the upper end of the cylindrical strut, and is fixed under the cylindrical strut And a tubular support which is disposed in a storage container in which a plurality of ejection ports are disposed below the side wall surface, and which is disposed on the side wall of the storage container of the bakulator and sucks up water around the lower end of the bakulator. A submersible pump for delivering the water through a pipe inward and downward, a magnetic ion water generator arranged in the middle of the pipe so that water sucked up by the submersible pump may pass, and a magnetic ion water generator provided outside the storage container of the bakulator. With pH sensor , PH of the pH sensor
A transmission line for transmitting the detected electric signal to the water or the ground, and a bio-injection system that is arranged on the water or on the ground and that receives the pH detection electric signal from the transmission line and contains an amount of photosynthetic bacteria corresponding to the pH degree in the water. And a bioreactor for feeding a bioactive liquid containing a liquid and an activator of animal microorganisms into the storage container through an injection pipe, and an automatic control device for the bioreactor. It achieves the task.

【0016】(2)また、上記(1)記載の浮上型水質
浄化装置のフロートを水面に浮かべて静止させ、筒形支
柱の長さをバッキレータの収納容器の下端が水底から略
1mの高さに設定し、上記バッキレータが水平360゜
全方位に向かって気泡を発生させる円形バッキレータと
することで、バッキレータの周囲半径10〜30mの範
囲に気泡を噴出させてエアレーションを行うことを特徴
とする水質浄化方法により上記課題を達成するものであ
る。
(2) Further, the float of the floating type water purification apparatus described in (1) above is floated on the water surface and made to stand still, and the length of the cylindrical support is set so that the lower end of the storage container of the bakulator is approximately 1 m above the water bottom. And the aforesaid bakerator is a circular bakerator that generates bubbles in all directions in the horizontal direction of 360 °, so that air bubbles are ejected in the range of a radius of 10 to 30 m around the bakerator to perform aeration. The purification method achieves the above object.

【0017】(3)さらに、上記(2)記載の水質浄化
方法において、中層水が筒形支柱の下端近傍の周壁に開
けられた導入口から吸入されて筒形支柱上端の開放口か
ら上層に環流するとともに、バッキレータ下端周辺の嫌
気性の下層水が水中ポンプにて吸い上げられて磁気イオ
ン水発生装置にて好気水に変換されるとともに前記筒形
支柱内下方に送出されて筒形支柱上端の開放口から上層
に環流することにより、水中の溶存酸素、水温、汚濁度
を均一化することを特徴とする水質浄化方法により上記
課題を達成するものである。
(3) Further, in the water purification method according to the above (2), middle-layer water is sucked from an inlet port opened in the peripheral wall near the lower end of the cylindrical support and is discharged from the open port at the upper end of the cylindrical support to the upper layer. As it circulates, the anaerobic lower layer water around the lower end of the back up is sucked up by the submersible pump, converted into aerobic water by the magnetic ion water generator, and sent out to the inside of the cylindrical strut to the upper end of the cylindrical strut. The above problem is achieved by a water purification method characterized by making the dissolved oxygen in the water, the water temperature, and the degree of pollution uniform by circulating the water from the open port to the upper layer.

【0018】(4)加えて、上記(2)または(3)記
載の水質浄化方法において、水中のpH度が所定値を越
えた場合にのみpHセンサーのpH検出電気信号を受け
て水中のpH度が所定値以下になるまでバイオ注液及び
バイオ活性液を連続的または断続的に注入管を通してバ
ッキレータの収納容器内に送るようにバイオリアクター
を自動制御装置にて制御することを特徴とする水質浄化
方法を提供することにより上記課題を達成するものであ
る。
(4) In addition, in the water purification method according to the above (2) or (3), the pH in water is received by receiving the pH detection electric signal of the pH sensor only when the pH degree in water exceeds a predetermined value. The water quality is characterized by controlling the bioreactor with an automatic controller so that the bioinjection solution and the bioactive solution are continuously or intermittently fed through the injection pipe into the storage container of the bacillator until the temperature falls below a predetermined value. The above object is achieved by providing a purification method.

【0019】尚、上記バイオ注液は好気性細菌ないし嫌
気性細菌を含んだバイオ液を意味し、主として光合成細
菌を含んだものである。
The bio-injection means a bio-solution containing aerobic or anaerobic bacteria, and mainly contains photosynthetic bacteria.

【0020】また、上記水中ファン、バッキレータ、水
中ポンプはモータによって作動する仕組みであるが、当
然ながら本装置には駆動系の電源装置の設備を陸上に有
するものである。
Further, the submersible fan, the bacillator, and the submersible pump are operated by a motor, but of course, this apparatus has a power supply equipment for a drive system on land.

【0021】[0021]

【発明の実施の形態】以下本発明に係わる浮上型水質浄
化装置及び該浮上型水質浄化装置を用いた水質浄化方法
の実施の形態を図面に基づいて詳細に説明する。
BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of a floating-type water purification device and a water-purifying method using the floating-type water purification device according to the present invention will be described below in detail with reference to the drawings.

【0022】図1は本発明に係わる浮上型水質浄化装置
の本体の全体構成を説明するための正面図である。
FIG. 1 is a front view for explaining the overall structure of the main body of the floating-type water purification device according to the present invention.

【0023】図2は上記浮上型水質浄化装置の水中平面
図である。
FIG. 2 is an underwater plan view of the floating type water purification device.

【0024】図3は上記浮上型水質浄化装置のバッキレ
ータ及びその収納容器内外の構成を説明するための縦断
面図である。
FIG. 3 is a vertical cross-sectional view for explaining the structure of the inside and outside of the bacillator of the floating type water purification device and its storage container.

【0025】図4は上記浮上型水質浄化装置によるエア
レーションを説明するための図である。
FIG. 4 is a view for explaining aeration by the floating type water purification device.

【0026】図5は上記浮上型水質浄化装置による中層
水の環流を説明するための図である。
FIG. 5 is a diagram for explaining the circulation of the intermediate layer water by the floating type water purification device.

【0027】図6は上記浮上型水質浄化装置の水中ポン
プと磁気イオン水発生装置による下層水の環流を説明す
るための図である。
FIG. 6 is a view for explaining the circulation of lower layer water by the submersible pump and the magnetic ion water generator of the floating type water purification device.

【0028】図7は上記浮上型水質浄化装置を用いた水
質浄化の全体循環経路を示す図である。
FIG. 7 is a diagram showing an entire circulation path of water purification using the floating type water purification apparatus.

【0029】図8は上記浮上型水質浄化装置のバイオ注
液及びバイオ活性液の投入の構成を説明するための構成
図である。
FIG. 8 is a configuration diagram for explaining the configuration of injection of bio-injection liquid and bio-active liquid in the floating type water purification device.

【0030】図1〜図3において、本発明に係わる浮上
型水質浄化装置の本体50は、フロート1と、前記フロ
ート1に吊支され水深に対応した長さH=1〜6mの筒
形支柱2と、該筒形支柱内の下方に配置されて筒形支柱
の下端近傍の周壁に開けられた導入口4から周囲の水を
筒形支柱内に吸入して筒形支柱上端の開放口5へ押し上
げる水中ファン6と、前記筒形支柱2の下に固定配置さ
れるとともに側壁面下方に噴出口が複数配設された収納
容器9の中に配置されたバッキレータ10と、前記バッ
キレータ10の収納容器9側壁11に配設されてバッキ
レータ下端周辺の水を吸い上げて前記筒形支柱内下方に
配管13を通して送出する水中ポンプ15と、該水中ポ
ンプにて吸い上げられた水が通過するように配管途中に
配設された磁気イオン水発生装置17と、前記バッキレ
ータ10の収納容器9の外側に配設したpHセンサー1
9と、該pHセンサーのpH検出電気信号を地上に伝達
する伝達ライン21と、からなり、図8に示されるよう
に地上に配設されたバイオリアクター30及びその自動
制御装置(バイオリアクターに内臓)が前記伝達ライン
21からのpH検出電気信号を受けて水中のpH度に対
応した量の光合成細菌を含むバイオ注液及び動物性微生
物の活性剤を含むバイオ活性液を注入管23、25を通
して前記浮上型水質浄化装置の本体50の収納容器9内
に送るようになっている。
1 to 3, a main body 50 of a floating-type water purification device according to the present invention comprises a float 1 and a cylindrical column having a length H = 1 to 6 m which is suspended from the float 1 and corresponds to the water depth. 2, and an inlet 5 at the upper end of the cylindrical strut by sucking ambient water into the cylindrical strut through an inlet 4 which is arranged below the cylindrical strut and opened in a peripheral wall near the lower end of the cylindrical strut. Submersible fan 6 that pushes up to, a bacillator 10 that is fixedly arranged under the cylindrical column 2, and is arranged in a storage container 9 in which a plurality of jet outlets are arranged below the side wall surface, and the bacillator 10 is stored. A submersible pump 15 disposed on the side wall 11 of the container 9 for sucking up water around the lower end of the backwater and sending it out through the pipe 13 to the lower part of the inside of the cylindrical support, and a pipe midway through which the water sucked up by the submersible pump passes. Magnetic field A down water generator 17, pH sensor 1 is disposed on the outside of the container 9 of the Bakkireta 10
9 and a transmission line 21 for transmitting the pH detection electric signal of the pH sensor to the ground, and as shown in FIG. 8, the bioreactor 30 installed on the ground and its automatic control device (incorporated in the bioreactor) ) Receives a pH detection electric signal from the transmission line 21, and supplies a bio-injection solution containing photosynthetic bacteria in an amount corresponding to the pH degree in water and a bio-active solution containing an activator of animal microorganisms through injection tubes 23 and 25. It is designed to be sent into the storage container 9 of the main body 50 of the floating-type water purification device.

【0031】尚、符号3はコードカバーであり、符号3
5は水中ポンプやモータ等の電気コード類であり、地上
の電源装置に配線されている。
Reference numeral 3 is a code cover, and reference numeral 3
Reference numeral 5 denotes electric cords such as a submersible pump and a motor, which are wired to a power supply device on the ground.

【0032】次に、上記各部についてさらに個別に詳述
する。
Next, each of the above parts will be described in detail.

【0033】先ず、フロート1は直径60〜100cm
程度のプラスチック製大型球形フロートであって、2〜
6個(通常は4個)を水平状態で対称に組んで中心下方
に以下の筒形支柱2が安定に吊支されるようにする。
First, the float 1 has a diameter of 60 to 100 cm.
It is a large spherical float made of plastic of about 2 to
Six pieces (usually four pieces) are symmetrically assembled in a horizontal state so that the following cylindrical column 2 is stably suspended below the center.

【0034】筒形支柱2は直径約60cm、長さは1〜
6m(対象となる河川、湖沼、入り江等の水深に応じて
変わる)のステンレス製の円筒形であって上端は開放口
5となっており、上端が水面WL下10〜20cmに位
置するように前記フロート1と鎖等の連結具で吊支され
ている。
The cylindrical column 2 has a diameter of about 60 cm and a length of 1 to
6m (depending on the depth of water of the target river, lake, cove, etc.) made of stainless steel, the upper end has an opening 5, and the upper end is located 10 to 20 cm below the water level WL. The float 1 is suspended and supported by a connecting tool such as a chain.

【0035】筒形支柱2の下端は後述のバッキレータ1
0の収納容器9と固着されている。
The lower end of the cylindrical support 2 is a back-up device 1 which will be described later.
It is fixed to the storage container 9 of 0.

【0036】また、筒形支柱2の下端近傍の周壁には周
囲から水を内部に導入する導入口4(開口寸法10cm
×10cm程度)が収納容器の周壁四方に複数(8〜3
6個程度)穿設されている。
In addition, an inlet port 4 (opening size 10 cm) for introducing water from the surroundings is provided in the peripheral wall near the lower end of the cylindrical column 2.
X 10 cm) on each side of the storage container (8-3)
About 6 pieces are drilled.

【0037】且つ、筒形支柱2の下端近傍、つまりバッ
キレータ10を収納している収納容器9の上面には水中
ファン6(モータ7にて比較的低速で駆動)が配設され
ていて、前記導入口4から周囲の中層水、下層水を筒形
支柱2内へ吸い上げて上方へゆっくりと押し上げ、上端
の開放口5から上層(水面下)に噴出拡散されるように
構成されている。
A submersible fan 6 (driven by a motor 7 at a relatively low speed) is provided near the lower end of the cylindrical column 2, that is, on the upper surface of the storage container 9 in which the back-up device 10 is stored. It is configured such that the surrounding middle-layer water and lower-layer water are sucked up from the inlet 4 into the cylindrical column 2 and slowly pushed upward, and are jetted and diffused from the upper opening 5 to the upper layer (below the water surface).

【0038】バッキレータ10は縦横1.6m、高さ1
m程度の箱形ないし円筒形のステンレス製収納容器9に
エアポンプ12とともに収納されたエアレーション(暴
気)装置であって、前記筒形支柱2の外壁に添設した内
径5cm程度の通気管14(筒形支柱2の開放口5より
30cm程度上方へ出ており、装置本体50を浮かべた
状態で上端開口が水面上に出るようにする)から空気を
エアポンプ12にて吸引して円形型バッキレータ10か
ら水平360度に小さな気泡を円形状に噴出させる(収
納容器9の側壁11下側には四方に気泡発生口16が多
数設けられている)。
The back-up device 10 has a height and width of 1.6 m and a height of 1.
An aeration device housed together with an air pump 12 in a box-shaped or cylindrical stainless steel container 9 having a diameter of about 5 m, which is attached to the outer wall of the cylindrical column 2 and has an inner diameter of about 5 cm. The air is drawn out from the opening 5 of the cylindrical support 2 by about 30 cm, and the upper end opening is exposed above the water surface with the apparatus body 50 floating. From the above, small bubbles are ejected in a circular shape at a horizontal angle of 360 degrees (a large number of bubble generating ports 16 are provided in four directions on the lower side of the side wall 11 of the storage container 9).

【0039】また、前記収納容器9の外側には小型の水
中ポンプ15が吸引口を下に向けて4個配設され、下層
の嫌気水を吸い上げて管13(内径20mm)を通して
磁気イオン水発生装置17の中を通り、好気水へと変換
されて筒形支柱2内下方に導入され、前記水中ファン6
にて上方へ押し上げられ、中下層水とともに上層に噴出
して拡散される。
Further, four small submersible pumps 15 are arranged on the outer side of the storage container 9 with their suction ports facing downward, suck up the anaerobic water in the lower layer and generate magnetic ionized water through the pipe 13 (inner diameter 20 mm). After passing through the device 17, it is converted into aerobic water and introduced into the lower part of the cylindrical support 2, and the submersible fan 6
It is pushed up by and is sprayed to the upper layer with the water in the middle and lower layers and diffused.

【0040】上記磁気イオン水発生装置17は1250
0G(ガウス)の残留磁束密度を有し、最大エネルギー
積(B・H)MAX=40MGOeの強力な永久磁石をN
極、S極を交互に配向させて断続的に磁場が形成される
ように組み合わせた中に20mm直径の管(通路)を通
した構造であり、その断続的磁場の中を嫌気水が通過す
ることで水分子はハイドロスピンモーションを起こして
水クラスターが分解しイオン結合が高まることにより、
嫌気水の溶存酸素量(略してDOという)を14%程度
高めて好気水化する磁気処理が為される装置である。
The magnetic ion water generator 17 is 1250.
A strong permanent magnet with a residual magnetic flux density of 0 G (Gauss) and a maximum energy product (B · H) MAX = 40 MGOe is N
It has a structure in which a tube (passage) having a diameter of 20 mm is passed through a combination of poles and S poles that are alternately oriented so that a magnetic field is formed intermittently, and anaerobic water passes through the intermittent magnetic field. As a result, water molecules undergo hydrospin motion, water clusters are decomposed, and ionic bonds are enhanced,
This is a device that is subjected to a magnetic treatment to increase the dissolved oxygen amount of anaerobic water (abbreviated as DO) by about 14% to make it aerobic water.

【0041】バイオ注液は光合成細菌を含む溶液であ
る。この光合成細菌は広義の光合成を行う細菌類をい
い、電子供与体としてH2Oでなく、H2、S2-、S23
2-、有機化合物等が利用され、したがって炭酸還元に伴
うO2発生は起こらない。
Bioinjection is a solution containing photosynthetic bacteria. This photosynthetic bacterium refers to a bacterium that performs photosynthesis in a broad sense, and is not H 2 O as an electron donor, but H 2 , S 2- , S 2 O 3
2- , organic compounds, etc. are used, so that O2 generation due to carbonic acid reduction does not occur.

【0042】本願では光合成細菌として光エネルギーに
依存して嫌気的環境で生育する種類を利用する。即ち、
明るい昼間の時間帯では水底の嫌気層へ向かい、暗い夜
の時間帯には上層へ移動する特性がある。
In the present application, a type of photosynthetic bacterium that grows in an anaerobic environment depending on light energy is used. That is,
It has the property of moving to the anaerobic layer at the bottom of the water during the bright daytime and moving to the upper layer during the dark night.

【0043】バイオ活性液は水中の栄養塩を餌にする動
物性微生物を活性化させる各種アミノ酸を含む87元素
調合剤と微量の重水素からなるバイオ溶液である。
The bioactive liquid is a biosolution consisting of 87 element preparations containing various amino acids that activate animal microorganisms that feed on nutrient salts in water and a trace amount of deuterium.

【0044】pHセンサー19は、水中の酸性度を測り
電気的信号に変換する装置であり、既存の機器を利用す
る。
The pH sensor 19 is a device for measuring the acidity in water and converting it into an electric signal, and uses an existing device.

【0045】該pHセンサー19のpH検出電気信号は
伝達ライン21を通して地上のバイオリアクター30の
自動制御装置(所謂マイクロコンピュータによる電子制
御装置である。)に伝達される。
The pH detection electric signal of the pH sensor 19 is transmitted through a transmission line 21 to an automatic control device (a so-called electronic control device by a microcomputer) of the bioreactor 30 on the ground.

【0046】地上(または水上)に設置されるバイオリ
アクター30は「生物反応装置」とも称され、微生物や
酵素の生体触媒を固定化したリアクター(反応器)を入
れ、生物としての営みを利用してバイオ注液の光合成細
菌及びバイオ活性液を生成する。
The bioreactor 30 installed on the ground (or on the water) is also referred to as a "bioreactor", and a reactor (reactor) in which a biocatalyst of a microorganism or an enzyme is immobilized is put in the bioreactor 30 to utilize its activity as a living organism. To produce photosynthetic bacteria and bioactive liquid in bioinjection.

【0047】上記バイオ注液とバイオ活性液は水の透明
度が悪く汚染度が高くなった場合に相対的に高まるpH
度をpHセンサー19で感知し、所定値を越えた場合に
自動的に収納容器9内のバッキレータ10近傍に注入管
23、25(内径13mm)を通して所定量のバイオ注
液とバイオ活性液が注入される。
The above-mentioned bio-injection solution and bio-active solution have a relatively high pH when the transparency of water is poor and the degree of contamination is high.
The pH sensor 19 senses the degree, and when the value exceeds a predetermined value, a predetermined amount of the bio-injection liquid and the bio-active liquid are automatically injected into the vicinity of the bacillator 10 in the storage container 9 through the injection pipes 23 and 25 (inner diameter 13 mm). To be done.

【0048】次に、上記構成の浮上型水質浄化装置によ
る水質浄化方法について説明する。
Next, a water purification method using the floating type water purification apparatus having the above structure will be described.

【0049】先ず、エアレーションについては、図4に
示されるように浮上型水質浄化装置本体50のフロート
1を水面に浮かべるとともに収納容器9の下にアンカー
34を底Bに沈めて静止させ、筒形支柱2の長さH1を
バッキレータ10の収納容器9の下端が水底から略1m
の高さ(h)に設定し、水上の空気を通気管14を通し
てエアポンプ12で吸い込み、水平360゜全方位に向
かって気泡Kを発生させる円形型バッキレータ10にて
細かな気泡として気泡発生口16から円形状に噴出拡散
させることで、バッキレータ10の周囲半径R1=10
〜30mの範囲でエアレーションが行われる。
First, as for aeration, as shown in FIG. 4, the float 1 of the floating type water purification apparatus main body 50 is floated on the water surface, and the anchor 34 is sunk to the bottom B under the storage container 9 to stand still. The length H1 of the support column 2 is set so that the lower end of the storage container 9 of the back-up device 10 is approximately 1 m
At the height (h) of the water, the air above the water is sucked in by the air pump 12 through the ventilation pipe 14, and bubbles are generated as fine bubbles in the circular type bakulator 10 that generates bubbles K in all directions in the horizontal direction of 360 °. The circular radius R1 = 10
Aeration is performed in the range of up to 30 m.

【0050】これにより溶存酸素は高まり浮遊懸濁微生
物による汚濁物の酸化でCODないしBODは下がる。
As a result, dissolved oxygen is increased and COD or BOD is lowered by the oxidation of the contaminants by the suspended suspended microorganisms.

【0051】次に、中層水、下層水を吸い上げて上層に
環流させる循環流動による浄化効率の改善について説明
する。
Next, the improvement of the purification efficiency by the circulation flow in which the middle layer water and the lower layer water are sucked up and circulated to the upper layer will be described.

【0052】一般に汚染された水源は好気的な上層水と
微好気的な中層水と嫌気的な下層水に分離されていて汚
濁度は均一ではなく、微生物による分解はさほど効率的
に行われているわけではない。また水温も均一ではな
く、溶存酸素は水温が高いと溶解度が下がりその濃度が
低下する。
Generally, the contaminated water source is separated into aerobic upper water, slightly aerobic middle water and anaerobic lower water, and the degree of pollution is not uniform, and decomposition by microorganisms is performed very efficiently. It's not something that has been confused. Also, the water temperature is not uniform, and when the water temperature is high, the solubility of oxygen decreases and its concentration decreases.

【0053】したがって、効果的な水質浄化のためには
水温、溶存酸素(DO)、汚濁度を均一化することが望
ましい。
Therefore, in order to effectively purify the water quality, it is desirable to make the water temperature, dissolved oxygen (DO) and the degree of pollution uniform.

【0054】上記均一化のため、図5に示されるように
中層水(黒矢印)を筒形支柱2の下端近傍の周壁に開け
られた多数の導入口4(開口寸法10cm×10cm)
から水中ファン6で吸入して筒形支柱上端の開放口5か
ら上層に円形状に拡散させて環流するとともに、図6に
示されるようにバッキレータ下端周辺の水底0〜1mの
嫌気性の下層水(黒矢印)を小型の水中ポンプ15にて
水底のヘドロを巻き上げることなく(蓋し、水中ポンプ
15の吸口は水底Bより1m程度上にある。)吸い上げ
て、管13(内径20mm程度)を通して磁気イオン水
発生装置17の中を通し、好気水へと変換して筒形支柱
2内下方に導入し、前記水中ファン6にて中層水ととも
に上方の開放口5へ押し上げ、上層に噴出して円形状に
拡散環流する(拡散の半径R3は約30mである。)。
In order to make the above uniform, as shown in FIG. 5, a large number of inlets 4 (opening size: 10 cm × 10 cm) for opening the middle layer water (black arrow) in the peripheral wall near the lower end of the cylindrical support 2.
From the submersible fan 6 to diffuse circularly to the upper layer from the opening 5 at the upper end of the cylindrical strut to recirculate, and as shown in FIG. (Black arrow) is sucked up by a small submersible pump 15 without rolling up the sludge on the bottom of the water (the lid is closed, and the suction port of the submersible pump 15 is about 1 m above the bottom B of the water.) And the pipe 13 (about 20 mm inside diameter) It passes through the magnetic ion water generator 17, is converted into aerobic water, is introduced into the lower part of the cylindrical column 2, and is pushed up by the submersible fan 6 together with the middle layer water to the upper opening 5 and ejected to the upper layer. And circularly diffuse (the radius R3 of diffusion is about 30 m).

【0055】したがって、水中の溶存酸素、水温、汚濁
度の均一化を図ることができるので、上層水の光合成を
阻止し、藻類の発生を防ぎ、上層、中層の微生物層も安
定化する。また、嫌気的な下層部は微好気的となってヘ
ドロ等の発生する硫化水素、ブタン、アンモニア等は下
層部において微生物にて消化還元される。
Therefore, since the dissolved oxygen in the water, the water temperature, and the degree of pollution can be made uniform, the photosynthesis of the upper layer water is prevented, the generation of algae is prevented, and the upper and middle microbial layers are also stabilized. Further, the anaerobic lower layer becomes slightly aerobic, and hydrogen sulfide, butane, ammonia, etc. generated by sludge and the like are digested and reduced by microorganisms in the lower layer.

【0056】尚、拡散環流範囲は水深5mシュミレーシ
ョンでは半径R3=30mに及ぶことが判った。
It has been found that the diffusion circulation range extends to a radius R3 = 30 m when the water depth is 5 m.

【0057】以上のエアレーション及び各層の循環流動
による浄化効率の改善を図示すると図7のようになる。
The improvement of the purification efficiency by the above aeration and circulating flow of each layer is illustrated in FIG.

【0058】極めて効果的、効率的な各層の循環流動、
エアレーションが同時に行われることが判る。
The circulation flow of each layer is extremely effective and efficient,
It turns out that aeration is performed at the same time.

【0059】次に、バイオ注液及びバイオ活性液の投入
による光合成細菌や微生物の適正量を維持し、COD、
BODを低下させる水質浄化方法について説明する。
Next, by maintaining the proper amount of photosynthetic bacteria and microorganisms by introducing the bio-injection solution and the bio-active solution, COD,
A water purification method for reducing BOD will be described.

【0060】従来は上記バイオ注液やバイオ活性液を水
源に常時投入しており、水質改善の管理はかなり大雑把
なものであった。
Conventionally, the above-mentioned bio-injection solution or bio-active solution is always added to the water source, and the management of water quality improvement has been quite rough.

【0061】この点、きれいになったらバイオ注液等の
投入を停止するようにして時宜に応じたきめ細かい微生
物補充・活性化の管理が望ましいことは言うまでもな
い。
In this respect, needless to say, it is desirable to timely and carefully control the replenishment and activation of microorganisms by stopping the injection of bio-injection or the like when it is clean.

【0062】本願発明は上記管理を水中のpH度とCO
Dの相関に着目し、水中のpH度が所定値(例えばpH
8.0)を越えた場合にのみ図8のようにpHセンサー
19のpH検出電気信号Sを伝達ライン21を介して受
けて水中のpH度が所定値以下(例えばpH7)になる
までバイオ注液及びバイオ活性液を連続的または断続的
に注入管23、24を通してバッキレータの収納容器9
内に送るように地上に設けたバイオリアクター30を自
動制御装置(pHセンサーの電気信号によるマイクロコ
ンピュータ制御で注入量をコントロールする装置)にて
制御する方法である。
In the present invention, the above management is performed by controlling the pH degree in water and CO
Paying attention to the correlation of D, the pH degree in water is a predetermined value (for example, pH
Only when the pH exceeds 8.0), the pH detection electric signal S of the pH sensor 19 is received via the transmission line 21 as shown in FIG. 8 until the pH degree in the water falls below a predetermined value (eg pH 7). Liquid and bioactive liquid are continuously or intermittently passed through injection pipes 23 and 24, and a storage container 9 for a bakulator is provided.
This is a method of controlling the bioreactor 30 provided on the ground so as to be fed into the inside by an automatic control device (a device that controls an injection amount by microcomputer control by an electric signal of a pH sensor).

【0063】収納容器9内に注入されたバイオ注液及び
バイオ活性液はエアレーションの気泡の噴出とともに円
形状に拡散される。
The bio-injection liquid and the bio-active liquid injected into the storage container 9 are diffused into a circular shape with the ejection of air bubbles from the aeration.

【0064】上記注入は常時行われるのではなく、通常
は停止しており、常時または定期的にpH度を測って適
量の前記バイオ注液とバイオ活性液を注入する仕組みと
なっており、不必要な場合にまで注入することがなく、
効果的な光合成細菌の供給及び動物性微生物の活性化が
実現される。
The above injection is not always performed, but is normally stopped, and the pH is measured constantly or regularly to inject an appropriate amount of the bio-injection solution and the bio-active solution. No need to inject until needed
Effective supply of photosynthetic bacteria and activation of animal microorganisms are realized.

【0065】尚、上記注入の量的、時間的制御はバイオ
リアクター30に付設されたマイクロコンピュータによ
る自動制御の注入装置で容易に実現されるが、勿論上記
注入量やバイオ注液、バイオ活性液は対象となる水源の
特性によって種々適正に調整されるべきである。
The quantitative and temporal control of the injection can be easily realized by an injection device automatically controlled by a microcomputer attached to the bioreactor 30, but of course the injection amount, bioinjection, and bioactive solution. Should be properly adjusted according to the characteristics of the water source.

【0066】尚、上記バイオリアクター30及びその自
動制御装置等は地上ではなく水上にフロート1によって
筏のごとく浮かべてもよいが、何れにしても電源装置は
地上に設置する必要があろう。
The bioreactor 30 and its automatic control device may be floated on the water instead of on the ground like a raft by the float 1, but in any case, the power supply device must be installed on the ground.

【0067】以上の構成からなる本願発明の浮上型水質
浄化装置は陸地へ装置本体50を従来のように陸地ない
し水底に固定するのではなく、対象とする流れのない内
湾や湖沼もしくは流れの小さい河川の水中に浮かべるよ
うにした浮上型の水質浄化装置であって、移動が容易で
あり、エアレーションを行うバッキレータ10が水底よ
り上方にあって水平方向に気泡を噴出させる構成なので
底泥のヘドロの巻き上げを起こさず、また好気的上層
水、微好気的中層水、嫌気的下層水の循環が緩やかに行
われるので、水中の溶存酸素の均一化、水温の一定化、
栄養分の均一化を図ることができ、上層での藻類の発生
を防止し、上層、中層の微生物層も安定する構成であ
り、然して効率的・効果的な水源の水質浄化が低コスト
で実現されるることは明らかである。
The floating-type water purification apparatus of the present invention having the above-mentioned configuration does not fix the apparatus main body 50 to the land as in the conventional case, but rather to the target inner bay or lake or small flow where the flow does not occur. It is a floating-type water purification device that floats in the water of a river, is easy to move, and has a structure in which the aeration aquarium 10 is located above the water bottom and ejects bubbles in the horizontal direction. Since the circulation of aerobic upper water, slightly aerobic middle water, and anaerobic lower water does not take place, the dissolved oxygen in water is made uniform, and the water temperature is kept constant.
Nutrients can be made uniform, algae are not generated in the upper layer, and the microbial layers in the upper and middle layers are stable, and efficient and effective water purification of the water source is realized at low cost. It is clear that

【0068】[0068]

【発明の効果】本発明に係わる浮上型水質浄化装置及び
水質浄化方法においては、以下に記載するような効果を
有する。
The floating-type water purification device and the water purification method according to the present invention have the following effects.

【0069】(1)浮上型のため移動が簡単であり、浄
化が必要な場所で効果的に水質浄化が行えるという優れ
た効果を有する。
(1) Since it is a floating type, it is easy to move and has an excellent effect that water quality can be effectively purified at a place where purification is required.

【0070】(2)バイオ注液及びバイオ活性液は必要
な時に必要量のみ投入するので無駄がなく維持コストが
安いという優れた効果を有する。
(2) Since the bio-injection solution and the bio-active solution are added only in a required amount when needed, there is an excellent effect that there is no waste and the maintenance cost is low.

【0071】(3)磁気イオン水発生装置を組み込んで
嫌気性の下層水を水底のヘドロを巻き上げることなく好
気水に変換して循環させるので、溶存酸素の量が上中下
層にわたって均一に増加するという優れた効果を有す
る。
(3) By incorporating a magnetic ion water generator, the anaerobic lower layer water is converted into aerobic water and circulated without rolling up the sludge on the bottom of the water, so that the amount of dissolved oxygen increases uniformly over the upper, middle and lower layers. It has the excellent effect of

【0072】(4)エアレーションと上記下層嫌気水の
好気水化、中下層水の循環、バイオ注液及びバイオ活性
液の注入を組み合わせているので、光合成細菌や動物性
微生物の活性化による窒素、リンの減少、及び溶存酸素
の確保が上中下層にわたって均一に行われるという優れ
た効果を有する。
(4) Since aeration is combined with aerobic aeration of the lower anaerobic water, circulation of the middle and lower layers of water, bioinjection and injection of bioactive liquid, nitrogen by activation of photosynthetic bacteria and animal microorganisms is combined. In addition, it has an excellent effect that phosphorus is reduced and dissolved oxygen is secured uniformly in the upper, middle and lower layers.

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

【図1】本発明に係わる浮上型水質浄化装置の本体の全
体構成を説明するための正面図である。
FIG. 1 is a front view for explaining an overall configuration of a main body of a floating-type water quality purification device according to the present invention.

【図2】上記浮上型水質浄化装置の水中平面図である。FIG. 2 is an underwater plan view of the floating type water purification device.

【図3】上記浮上型水質浄化装置のバッキレータ及びそ
の収納容器内外の構成を説明するための縦断面図であ
る。
FIG. 3 is a vertical cross-sectional view for explaining the configuration of the inside and outside of the bacillator of the floating type water purification device and its storage container.

【図4】上記浮上型水質浄化装置によるエアレーション
を説明するための図である。
FIG. 4 is a diagram for explaining aeration by the floating water purification device.

【図5】上記浮上型水質浄化装置による中層水の環流を
説明するための図である。
FIG. 5 is a diagram for explaining the circulation of middle-layer water by the floating-type water purification device.

【図6】上記浮上型水質浄化装置の水中ポンプと磁気イ
オン水発生装置による下層水の環流を説明するための図
である。
FIG. 6 is a diagram for explaining the circulation of lower layer water by the submersible pump and the magnetic ion water generator of the floating type water purification device.

【図7】上記浮上型水質浄化装置を用いた水質浄化の全
体循環経路を示す図である。
FIG. 7 is a diagram showing an entire circulation path of water purification using the floating type water purification apparatus.

【図8】上記浮上型水質浄化装置のバイオ注液及びバイ
オ活性液の投入の構成を説明するための構成図である。
[Fig. 8] Fig. 8 is a configuration diagram for explaining a configuration of a bio-injection liquid and a bio-active liquid input of the floating type water purification device.

【符号の説明】[Explanation of symbols]

1 フロート 2 筒形支柱 3 コードカバー 4 導入口 5 開放口 6 水中ファン 9 収納容器 10 バッキレータ 11 側壁 12 エアポンプ 13 配管 14 通気管 15 水中ポンプ 16 気泡発生口 17 磁気イオン水発生装置 19 pHセンサー 21 伝達ライン 23、25 注入管 30 バイオリアクター 34 アンカー 50 浮上型水質浄化装置の本体 WL 水面 B 水底 1 Float 2 Cylindrical Strut 3 Cord Cover 4 Inlet 5 Open Port 6 Submersible Fan 9 Storage Container 10 Buckulator 11 Sidewall 12 Air Pump 13 Piping 14 Venting Pipe 15 Submersible Pump 16 Bubble Generation Port 17 Magnetic Ion Water Generator 19 pH Sensor 21 Transmission Line 23, 25 Injection pipe 30 Bioreactor 34 Anchor 50 Main body of floating type water purification device WL Water surface B Water bottom

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 フロートと、前記フロートに吊支され水
深に対応した1〜6mの長さの筒形支柱と、該筒形支柱
内の下方に配置されて筒形支柱の下端近傍の周壁に開け
られた導入口から周囲の水を筒形支柱内に吸入して筒形
支柱上端の開放口へ押し上げる水中ファンと、前記筒形
支柱の下に固定配置されるとともに側壁面下方に噴出口
が複数配設された収納容器の中に配置されたバッキレー
タと、前記バッキレータの収納容器側壁に配設されてバ
ッキレータ下端周辺の水を吸い上げて前記筒形支柱内下
方に配管を通して送出する水中ポンプと、該水中ポンプ
にて吸い上げられた水が通過するように配管途中に配設
された磁気イオン水発生装置と、前記バッキレータの収
納容器の外側に配設したpHセンサーと、該pHセンサ
ーのpH検出電気信号を水上または地上に伝達する伝達
ラインと、水上または地上に配設されるとともに前記伝
達ラインからのpH検出電気信号を受けて水中のpH度
に対応した量の光合成細菌を含むバイオ注液及び動物性
微生物の活性剤を含むバイオ活性液を注入管を通して前
記収納容器内に送るバイオリアクター及びその自動制御
装置と、からなる構造を特徴とする浮上型水質浄化装
置。
1. A float, a cylindrical support hanged from the float and having a length of 1 to 6 m corresponding to the water depth, and a peripheral wall near the lower end of the cylindrical support disposed below the cylindrical support. A submersible fan that sucks ambient water into the cylindrical support from the opened inlet and pushes it up to the open port at the upper end of the cylindrical support, and a jet port that is fixedly arranged under the cylindrical support and located below the side wall surface. A bacillator arranged in a plurality of storage containers arranged, and a submersible pump which is arranged on the storage container side wall of the bakulator and sucks up water around the bottom end of the bacillator and sends it out through a pipe to the lower part of the cylindrical support. A magnetic ion water generator disposed in the middle of the pipe so that water sucked up by the submersible pump can pass through, a pH sensor disposed outside the accommodating container of the bacillator, and a pH detection electricity for the pH sensor. Belief And a bioinjection which is disposed on the water or on the ground and which receives a pH detection electric signal from the transmission line and contains an amount of photosynthetic bacteria corresponding to the pH degree in the water. A floating-type water purification device having a structure comprising a bioreactor for sending a bioactive liquid containing an activator of animal microorganisms into the storage container through an injection pipe and an automatic control device for the bioreactor.
【請求項2】 請求項1記載の浮上型水質浄化装置のフ
ロートを水面に浮かべて静止させ、筒形支柱の長さをバ
ッキレータの収納容器の下端が水底から略1mの高さに
設定し、上記バッキレータが水平360゜全方位に向か
って気泡を発生させる円形バッキレータとすることで、
バッキレータの周囲半径10〜30mの範囲に気泡を噴
出させてエアレーションを行うことを特徴とする水質浄
化方法。
2. The float of the levitation type water purification apparatus according to claim 1 is floated on the water surface and made to stand still, and the length of the cylindrical support is set such that the lower end of the storage container of the bacillator is approximately 1 m above the water bottom. By making the above-mentioned back-up device a circular back-up device that generates bubbles in all 360 ° horizontal directions,
A water purification method characterized by performing aeration by ejecting bubbles in a radius of 10 to 30 m around a bacillator.
【請求項3】 請求項2記載の水質浄化方法において、
中層水が筒形支柱の下端近傍の周壁に開けられた導入口
から吸入されて筒形支柱上端の開放口から上層に環流す
るとともに、バッキレータ下端周辺の嫌気性の下層水が
水中ポンプにて吸い上げられて磁気イオン水発生装置に
て好気水に変換されるとともに前記筒形支柱内下方に送
出されて筒形支柱上端の開放口から上層に環流すること
により、水中の溶存酸素、水温、汚濁度を均一化するこ
とを特徴とする水質浄化方法。
3. The water purification method according to claim 2,
Middle-layer water is sucked in from the inlet opened in the peripheral wall near the lower end of the cylindrical support, and circulates to the upper layer from the opening at the upper end of the cylindrical support. It is then converted into aerobic water by the magnetic ionized water generator, and it is sent to the lower part of the cylindrical column and is circulated to the upper layer from the opening at the upper end of the cylindrical column, thereby dissolving oxygen in the water, water temperature, and pollution. A method for purifying water, which is characterized by equalizing the degree.
【請求項4】 請求項2または請求項3記載の水質浄化
方法において、水中のpH度が所定値を越えた場合にの
みpHセンサーのpH検出電気信号を受けて水中のpH
度が所定値以下になるまでバイオ注液及びバイオ活性液
を連続的または断続的に注入管を通してバッキレータの
収納容器内に送るようにバイオリアクターを自動制御装
置にて制御することを特徴とする水質浄化方法。
4. The water purification method according to claim 2, wherein the pH detection electric signal of the pH sensor is received only when the pH degree in the water exceeds a predetermined value.
The water quality is characterized by controlling the bioreactor with an automatic controller so that the bioinjection solution and the bioactive solution are continuously or intermittently fed through the injection pipe into the storage container of the bacillator until the temperature falls below a predetermined value. Purification method.
JP4570796A 1996-03-04 1996-03-04 Florting type water quality purifying device and water quality purifying method Pending JPH09234482A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4570796A JPH09234482A (en) 1996-03-04 1996-03-04 Florting type water quality purifying device and water quality purifying method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4570796A JPH09234482A (en) 1996-03-04 1996-03-04 Florting type water quality purifying device and water quality purifying method

Publications (1)

Publication Number Publication Date
JPH09234482A true JPH09234482A (en) 1997-09-09

Family

ID=12726838

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4570796A Pending JPH09234482A (en) 1996-03-04 1996-03-04 Florting type water quality purifying device and water quality purifying method

Country Status (1)

Country Link
JP (1) JPH09234482A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007050325A (en) * 2005-08-16 2007-03-01 Bco:Kk Floating aerator
JP2007296496A (en) * 2006-05-02 2007-11-15 Yasushi Iseri Apparatus for cleaning bottom water
JP2010172811A (en) * 2009-01-28 2010-08-12 Yonezaki:Kk Stirring device
CN101913708A (en) * 2010-09-08 2010-12-15 乔世琴 Low-carbon energy-saving method for treating polluted water quality of lake or landscape lake
JP2012176365A (en) * 2011-02-27 2012-09-13 Takatoku:Kk Water clarification method and device combined with sludge curling-up suppressing equipment in lake and pond in lentic state
CN103864204A (en) * 2014-03-21 2014-06-18 北京工业大学 Intermittent biological enhancement device and method for phosphorous removal and recovery

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007050325A (en) * 2005-08-16 2007-03-01 Bco:Kk Floating aerator
JP2007296496A (en) * 2006-05-02 2007-11-15 Yasushi Iseri Apparatus for cleaning bottom water
JP2010172811A (en) * 2009-01-28 2010-08-12 Yonezaki:Kk Stirring device
CN101913708A (en) * 2010-09-08 2010-12-15 乔世琴 Low-carbon energy-saving method for treating polluted water quality of lake or landscape lake
CN101913708B (en) * 2010-09-08 2014-07-16 乔世琴 Low-carbon energy-saving method for treating polluted water quality of lake or landscape lake
JP2012176365A (en) * 2011-02-27 2012-09-13 Takatoku:Kk Water clarification method and device combined with sludge curling-up suppressing equipment in lake and pond in lentic state
CN103864204A (en) * 2014-03-21 2014-06-18 北京工业大学 Intermittent biological enhancement device and method for phosphorous removal and recovery

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