JPH0885000A - Portable aerator - Google Patents

Portable aerator

Info

Publication number
JPH0885000A
JPH0885000A JP25987594A JP25987594A JPH0885000A JP H0885000 A JPH0885000 A JP H0885000A JP 25987594 A JP25987594 A JP 25987594A JP 25987594 A JP25987594 A JP 25987594A JP H0885000 A JPH0885000 A JP H0885000A
Authority
JP
Japan
Prior art keywords
water
dissolved oxygen
portable
aerator
absorption
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
JP25987594A
Other languages
Japanese (ja)
Inventor
Shiyoutarou Mahiko
昇太郎 間彦
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
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 Individual filed Critical Individual
Priority to JP25987594A priority Critical patent/JPH0885000A/en
Publication of JPH0885000A publication Critical patent/JPH0885000A/en
Pending legal-status Critical Current

Links

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)

Abstract

PURPOSE: To provide a method in which such artificial pollution as domestic waste water is dispersedly improved and circulation of an original natural purification function is recovered by constituting a portable aerator, so that absorption of highly dissolved oxygen is obtained and the portable aerator is formed into a portable floating type and easily installed in a place near to the generation source of polluted water in a method for simulating the natural aeration function of a river for polluted water with deficiently dissolved oxygen. CONSTITUTION: An aerator is constituted of a submersible pump 1a and an aspirator 1b, and a meshlike vessel 2a is floated on the water surface by a float 2b. Absorption of dissolved oxygen necessary for purification is caused by injecting water from the upper part of the water surface.

Description

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

【0001】[0001]

【産業上の利用分野】本発明により、溶存酸素の欠乏に
陥り、浄化機能の失った散在する湖沼、人工池等の汚濁
水の浄化がその場所及びより発生源に近い場所で容易に
可能となる。
INDUSTRIAL APPLICABILITY According to the present invention, it is possible to easily purify polluted water such as scattered lakes, artificial ponds, etc., which have lost their purifying function due to lack of dissolved oxygen, at that location and a location closer to the source. Become.

【0002】[0002]

【従来の技術】従来の浄化方法においては、下水処理設
備の活性汚泥による。上記の方法の場合、以下に示す欠
点があつた。 (1)計画、調査、設計、施工、保守に膨大な費用が必
要な為、容易に且つ短期間で設置できない。 (2)微生物による処理であるにもかかわらず高密度集
合型になっており、集められた下水の汚れの度合いと量
の変動に対して四季を通じて安定的に短時間で処理する
事が難しい。
2. Description of the Related Art In conventional purification methods, activated sludge in sewage treatment equipment is used. The above method has the following drawbacks. (1) It cannot be installed easily and in a short period of time because enormous costs are required for planning, investigation, design, construction, and maintenance. (2) Although it is a treatment by microorganisms, it is a high-density aggregate type, and it is difficult to stably treat the sewage collected for a short period of time consistently with variations in the degree and amount of dirt.

【0003】[0003]

【発明が解決しようとする課題】本発明は、上記に鑑
み、分散した発生源に近い場所で、汚れ度合いの低い状
態で、微生物処理に必要な時間をかけて、容易に且つ経
済的に行える方法の提供を目的とする。
In view of the above, the present invention can be carried out easily and economically in a place close to a dispersed source, in a state of a low degree of fouling, in a time required for microbial treatment. The purpose is to provide a method.

【0004】[0004]

【課題を解決するための手段】本発明による課題解決手
段は、図1のごとく、(1)分散する現場に対処可能な
様に、可搬式フロート型とした。(2)水中ポンプ1a
と吸気器1bの併用で、吸入した汚濁水に空気を混入さ
せたものを水面に噴射する事により、高い溶存酸素吸収
が得られるようにした。
As shown in FIG. 1, the means for solving the problems according to the present invention is (1) of a portable float type so as to be able to deal with dispersed sites. (2) Submersible pump 1a
By using the and the air intake device 1b together, a high dissolved oxygen absorption can be obtained by injecting polluted water into which air is mixed into the water surface.

【0005】[0005]

【作用】上記、課題解決手段において、溶存酸素の欠乏
により浄化機能の著しく低下した湖沼、人工池等の浄化
がその場所及び発生源により近い分散場所で容易に可能
になる。
In the above means for solving the problems, it becomes possible to easily purify lakes and marshes, artificial ponds, etc., whose purifying function has been remarkably deteriorated due to lack of dissolved oxygen, at that place and at a dispersing place closer to the source.

【0006】[0006]

【実施例】以下、本発明の構造を図に基づき説明する。
図1は本発明の可搬式の曝気装置の構成図を示す。水中
ポンプ1a吸気器1bからなり、メッシュ状容器2aを
フロート2bで水面に浮かべたものに固定された構造と
なっている。
The structure of the present invention will be described below with reference to the drawings.
FIG. 1 shows a block diagram of a portable aeration apparatus of the present invention. It is composed of a submersible pump 1a and an air intake device 1b, and has a structure in which a mesh container 2a is fixed to a float 2b floating on the water surface.

【0007】図1において、メッシュ状容器2aに水中
ポンプ1aを納めているのは吸入口から漂遊物を吸入し
ない様する為で、又フロート型とするのは水面と噴射口
1cの距離を一定にし溶存効率が水位の影響を受けない
様にする事と水中ポンプ1aの負荷を軽減し損失を小さ
くする配慮でもある。水中ポンプ1aにて吸入した汚濁
水に吸気器1bで大気中の空気を混入させ、噴射口1c
より水面に噴射する。
In FIG. 1, the submersible pump 1a is housed in the mesh container 2a to prevent inhalation of stray matter from the suction port, and the float type is used to keep the distance between the water surface and the jet port 1c constant. It is also a consideration that the dissolution efficiency is not affected by the water level and that the load on the submersible pump 1a is reduced to reduce the loss. Air in the atmosphere is mixed with polluted water sucked by the submersible pump 1a by the air intake device 1b, and the injection port 1c
Spray more water.

【0008】本発明の原理は、自然浄化に必要な溶存酸
素を汚濁水に供給する事である。その方法として川の流
れの曝気機構をシミュレートする事で、大気中の酸素を
平面的に、分散的に、効率良く、経済的に供給できるよ
うになった。それは微生物の働きで最も効率良く浄化す
るには、高密度一括処理ではなく低密度のものを時間に
とらわれず分散処理する必要があるからである。
The principle of the present invention is to supply dissolved water with dissolved oxygen necessary for natural purification. By simulating the aeration mechanism of the river flow as the method, it became possible to supply oxygen in the atmosphere in a planar, dispersive, efficient and economical manner. This is because, in order to purify most efficiently by the action of microorganisms, it is necessary to disperse low-density ones regardless of time, instead of high-density batch treatment.

【0009】使用方法としては、できるだけ汚れの発生
源に近い場所に設置する事がより効果的であり、対象水
質及び水量に合わせて、水面に必要台数を配列する。既
存の下水処理場においても、処理能力をオーバーする場
合には、入口側に設置すれば浄化負荷が軽減されるし、
出口側に設置すれば更に浄化効果が得られる。
As a method of use, it is more effective to install it in a place as close as possible to the source of contamination, and arrange the required number on the water surface according to the target water quality and water quantity. Even in the existing sewage treatment plant, if the treatment capacity is exceeded, installing it on the inlet side will reduce the purification load,
If it is installed on the outlet side, further purification effect can be obtained.

【0010】図2は図1の基本型に微生物生息域を兼ね
備え浄化機能を向上させたものであり、比重1以上の生
息層3aと比重約1の生息層3bと比重1以下の生息層
3cの水質に影響を及ぼさない物質の三層からなる。図
1の曝気装置で生成した溶存酸素吸収した汚濁水の一部
を使用し浄化をおこなうものであり、以下の働きがあ
る。 ・噴射により汚濁水中に生じた微細な気泡を付着し、帯
留時間を長くし酸素溶存を補助する。 ・多種多様の大きさの孔と緩やかな流速という微生物に
適した環境を提供する。 ・比重の異なる物質による立体三層構成の上、比重1以
下及び比重約1の層のものはそれ自体流動性があり、又
比重1以上の層のものも水面に浮いているメッシュ状容
器2a内にあるので相対的に流動性があり目詰まりによ
る機能低下を防止する。
FIG. 2 shows a microbial habitat in addition to the basic type shown in FIG. 1 to improve the purification function. The habitat layer 3a has a specific gravity of 1 or more, the habitat layer 3b having a specific gravity of about 1 and the habitat layer 3c having a specific gravity of 1 or less. It consists of three layers of substances that do not affect the water quality of. Purification is performed by using a part of the polluted water absorbed by the dissolved oxygen generated by the aeration device of FIG. 1, and has the following functions.・ Attach the fine bubbles generated in the polluted water by jetting, prolong the retention time and assist oxygen dissolution.・ Providing an environment suitable for microorganisms with a wide variety of pore sizes and gentle flow rates.・ Mesh-shaped container 2a in which three-dimensional three-layered structure made of substances having different specific gravities, a layer having a specific gravity of 1 or less and a layer having a specific gravity of about 1 itself has fluidity, and a layer having a specific gravity of 1 or more floats on the water surface. Since it is inside, it is relatively fluid and prevents functional deterioration due to clogging.

【0011】上記において、実験結果では、吸気器1b
装着しない場合は、効率的な溶存酸素濃度の上昇は得ら
れなかったので、吸気器1bの効果は確認できた。吸気
器1bとは、配管途中にオリフィスを挿入した場合、そ
の下流側に圧力低下の部分が発生するという現象を利用
し、そこに大気中の空気を吸入させるもの。川の流れの
曝気機構のシミュレーションとは、自然の川の流れで最
も溶存酸素吸収の大きいのは落下部であり、その落下部
の水平単位面積あたりの溶存酸素吸収の機構を解析し、
シミュレートしたという事。それは、水の落下による変
化を次の様に解釈出来る。位置エネルギー+運動エネル
ギーが、流速の増加+溶存酸素濃度の増加に、変化す
る。更に、溶存酸素吸収に大きく寄与するのは、下記に
よるものと考えられている。 ・落下部で、気泡を深部まで運び、それによる接触時
間。 ・落下時に発生する微細気泡の生成量とその水中での漂
遊時間。 ・落下直後の表面水流の乱れによる、水と空気との接触
状態。 結果は、噴射高さ及び噴射圧力及び水中の障害物によっ
て変わるが、吸気器1bを使用した場合、概ね、噴射角
度としては、水平より下側に、30度前後が溶存酸素濃
度の増加に効率良く寄与できた。全エネルギーを、気泡
を深部まで沈ませる事(噴射角度90度)に使用する
と、水の抵抗により深さは確保できず、溶存酸素吸収さ
せる方法としては効率が悪い。又、運動エネルギーを水
平(噴射角度0度)に使用した場合は、落下位置がかわ
るのみで溶存酸素吸収にあまり寄与しない。
In the above, the experimental results show that the intake device 1b
When the device was not attached, an effective increase in the dissolved oxygen concentration could not be obtained, so the effect of the inhaler 1b could be confirmed. The air intake device 1b is a device that takes in air in the atmosphere by utilizing the phenomenon that when an orifice is inserted in the pipe, a pressure drop portion is generated on the downstream side. The simulation of the aeration mechanism of the river flow is that the largest dissolved oxygen absorption in the natural river flow is the falling part, and the mechanism of dissolved oxygen absorption per horizontal unit area of the falling part is analyzed,
That it was simulated. It can interpret the change caused by the fall of water as follows. The potential energy + kinetic energy changes to increase in flow velocity + increase in dissolved oxygen concentration. Further, it is considered that the following is a major contributor to the absorption of dissolved oxygen.・ At the falling part, carry bubbles to the deep part and the contact time by it. -The amount of fine bubbles generated when falling and the stray time in water.・ The state of contact between water and air due to the turbulence of the surface water flow immediately after falling. Although the result varies depending on the injection height and the injection pressure and the obstacles in the water, when the air intake device 1b is used, the injection angle is generally below the horizontal and about 30 degrees is effective for increasing the dissolved oxygen concentration. I was able to contribute well. If all the energy is used to sink the bubbles to a deep portion (injection angle 90 degrees), the depth cannot be secured due to the resistance of water, and the method of absorbing dissolved oxygen is inefficient. Further, when the kinetic energy is used horizontally (injection angle 0 degree), only the falling position is changed and it does not contribute much to the absorption of dissolved oxygen.

【0012】[0012]

【発明の効果】本発明により、溶存酸素欠乏状態の汚濁
水への酸素供給が発生源により近い場所で容易に可能と
なる。結果としてその場所及び下流に水性生物の生息を
促し、それによる更なる自然浄化が行われるので最も効
率的で経済的である。
According to the present invention, it is possible to easily supply oxygen to polluted water in a dissolved oxygen-deficient state at a place closer to the source. As a result, it is the most efficient and economical because it promotes the inhabitation of aquatic organisms in its place and in the downstream and further natural purification is carried out.

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

【図1】本発明である可搬式の曝気装置の基本構成図で
ある。
FIG. 1 is a basic configuration diagram of a portable aeration device according to the present invention.

【図2】本発明に微生物生息域を装備した実施例であ
る。
FIG. 2 is an example in which the present invention is equipped with a microbial habitat.

【符号の説明】[Explanation of symbols]

1a 水中ポンプ 1b 吸気器 1c 噴射口 2a メッシュ状容器 2b フロート 1a Submersible pump 1b Inhaler 1c Injection port 2a Mesh container 2b Float

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 水中ポンプ1aと吸気器1bからなるも
のを水面に浮かべ、それによって生成した空気を混入さ
せた水を水面に噴射し、水に溶存酸素吸収をさせて、小
規模分散で浄化をおこなうことを特徴とする可搬式の曝
気装置。
1. A submersible pump 1a and an air intake device 1b are floated on the water surface, and water mixed with air generated thereby is injected to the water surface to absorb dissolved oxygen in the water and purify by small-scale dispersion. A portable aerator characterized by performing.
JP25987594A 1994-09-16 1994-09-16 Portable aerator Pending JPH0885000A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP25987594A JPH0885000A (en) 1994-09-16 1994-09-16 Portable aerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP25987594A JPH0885000A (en) 1994-09-16 1994-09-16 Portable aerator

Publications (1)

Publication Number Publication Date
JPH0885000A true JPH0885000A (en) 1996-04-02

Family

ID=17340167

Family Applications (1)

Application Number Title Priority Date Filing Date
JP25987594A Pending JPH0885000A (en) 1994-09-16 1994-09-16 Portable aerator

Country Status (1)

Country Link
JP (1) JPH0885000A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH10235397A (en) * 1997-02-26 1998-09-08 Arimitsu Kogyo Kk Aerobic treatment and aerobic treatment apparatus
JP2001300592A (en) * 2000-04-26 2001-10-30 Chisso Corp Night soil treating system
JP2007000846A (en) * 2005-06-27 2007-01-11 Matsushita Electric Works Ltd Fine bubble generating device
WO2016031416A1 (en) * 2014-08-25 2016-03-03 株式会社micro-bub Water purifier
US9847299B2 (en) 2014-09-30 2017-12-19 Murata Manufacturing Co., Ltd. Semiconductor package and mounting structure thereof
CN108249561A (en) * 2018-03-15 2018-07-06 桂林理工大学 A kind of teaching aeration oxygenator

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH10235397A (en) * 1997-02-26 1998-09-08 Arimitsu Kogyo Kk Aerobic treatment and aerobic treatment apparatus
JP2001300592A (en) * 2000-04-26 2001-10-30 Chisso Corp Night soil treating system
JP2007000846A (en) * 2005-06-27 2007-01-11 Matsushita Electric Works Ltd Fine bubble generating device
JP4631561B2 (en) * 2005-06-27 2011-02-16 パナソニック電工株式会社 Microbubble generator
WO2016031416A1 (en) * 2014-08-25 2016-03-03 株式会社micro-bub Water purifier
US9847299B2 (en) 2014-09-30 2017-12-19 Murata Manufacturing Co., Ltd. Semiconductor package and mounting structure thereof
CN108249561A (en) * 2018-03-15 2018-07-06 桂林理工大学 A kind of teaching aeration oxygenator

Similar Documents

Publication Publication Date Title
US3452966A (en) Liquid treatment apparatus and method
JP3197250B2 (en) Purification equipment for lakes, marshes, ponds, etc.
JP3702302B2 (en) Sludge removal equipment
EP0996497A1 (en) Device and process for liquid treatment
JP2010535096A (en) Liquid aeration system
CN209853846U (en) Immobilized microorganism sewage treatment device combining jet aeration
CN103755085B (en) Device and method for removing algal bloom and purifying algae source in branch reservoir bay of channel reservoir
CN201634513U (en) Aeration device for sewage processing system
JPH0885000A (en) Portable aerator
CN205367909U (en) Portable pure oxygen bubbling machine on water
CN101175699B (en) An apparatus for treating small river water
CN107827297B (en) Sewage treatment device is bred to integral type
KR102170073B1 (en) Method and Apparatus for Making Sea Salt
CN109502736B (en) Oxygenation system in river surge biochemical pollution control technology
US7018532B2 (en) Aeration and mixing trough
CN208345862U (en) open water purifying device
CN207418499U (en) A kind of purification of waste water mechanism
WO2006082875A1 (en) System and method for purification of water
CN208327451U (en) A kind of improved protein separator
CN209906427U (en) Device for controlling foam overflow of garbage leachate biochemical treatment facility
CN218969035U (en) Novel oily wastewater treatment system
CN207159033U (en) A kind of efficient integrated sewage disposal device
KR102551132B1 (en) The System for Purifying Wasted Water
CN208308594U (en) A kind of spray painting factory wastewater treatment equipment
JPH10249367A (en) Sewage purifying device