JPH05146796A - Device for purifying closed natural water area - Google Patents
Device for purifying closed natural water areaInfo
- Publication number
- JPH05146796A JPH05146796A JP33591491A JP33591491A JPH05146796A JP H05146796 A JPH05146796 A JP H05146796A JP 33591491 A JP33591491 A JP 33591491A JP 33591491 A JP33591491 A JP 33591491A JP H05146796 A JPH05146796 A JP H05146796A
- Authority
- JP
- Japan
- Prior art keywords
- natural water
- water
- air
- cylindrical body
- aerator
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
- Physical Water Treatments (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、湖沼、貯水池、調整池
あるいはダム等の閉鎖自然水域の浄化装置に関し、特に
閉鎖自然水域水に微細な酸化ガス等の気泡を供給し、か
つ閉鎖自然水域水内に強力な安定した循環流を形成し得
るエアレータを備えた閉鎖自然水域浄化装置に関するも
のである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a purification device for a closed natural water area such as a lake, a reservoir, a regulating pond or a dam, and more particularly to a closed natural water area which supplies fine bubbles of oxidizing gas to the water. The present invention relates to a closed natural water purification device equipped with an aerator capable of forming a strong and stable circulating flow in water.
【0002】[0002]
【従来の技術及び発明が解決しようとする課題】現代に
おける人類の生活様式の高度化に伴い、湖沼等の自然水
域の富栄養化が進行し、自然環境が汚染、劣化してい
る。そこでこうした閉鎖自然水域を浄化すべく種々のエ
アレーション方式が採用されており、湖沼等の水中に設
置された環状や板状のエアレータ細孔から空気を水中に
加圧して噴き出すことによって気泡を細分化して供給す
る方式や回転羽根や放水管などによりせん断力が形成さ
れた水流内に空気を入れてそれを細分化する方式、ある
いは湖沼水等をくみ揚げてその場で上へ噴出する噴水方
式、さらには湖沼水中に没入させて垂設した空気揚水筒
から間欠的に空気を噴出させることによって、湖沼等水
域に対流を発生させる方式等が存在する。2. Description of the Related Art With the advancement of modern human lifestyles, eutrophication of natural waters such as lakes and marshes is contaminated and deteriorated. Therefore, various aeration methods have been adopted to purify such closed natural waters, and air bubbles are subdivided by pressurizing and ejecting air into the water from annular or plate-shaped aerator pores installed in water such as lakes and marshes. Supply method, a method in which air is introduced into a water flow in which a shearing force is formed by a rotating blade or a water discharge pipe to subdivide it, or a fountain method in which lake water or the like is pumped up and ejected upward on the spot, Furthermore, there is a method of generating convection in a water area such as a lake by intermittently ejecting air from an air pumping cylinder that is immersed in the lake water and hung vertically.
【0003】これらの方式のエアレーションでは、基本
的には空気の送量やそれぞれのエアレータの設置個数等
によって必要な調節が行われている。しかし、省エネル
ギー型の高度湖沼水等処理を目的とする高機能閉鎖自然
水域浄化装置の開発のためには、微細な酸化ガス気泡を
多量に発生させ、さらにはその気泡の発生量・供給量と
それを含む循環流の形成を制御する必要がある。In these types of aeration, necessary adjustments are basically made depending on the amount of air fed and the number of aerators installed. However, in order to develop a highly functional closed natural water purification device for the purpose of energy-saving advanced lake water treatment, a large amount of fine oxidizing gas bubbles are generated, and further It is necessary to control the formation of the circulating flow containing it.
【0004】ところが、上記方式のエアレーションに
は、例えば散気管、散気筒にいかに微細な細孔を設けて
も、気泡が細孔から噴出する際の気泡の表面張力によっ
て、結果的にそのほとんどが噴き出しによる散気方式か
回転羽根や突起体とにせん断によって気泡を発生させる
方式であるために、下記のさまざまな欠点があった。例
えば、散気管、散気板、散気筒からの噴き出し方式で
は、そこにいかに微細な細孔を設けても、気泡が細孔か
ら噴出する際の気泡の表面張力によって、結果的に数ミ
リメートル程度の径を有する大きな気泡が発生してしま
い、それよりも小さな気泡を発生させることが不可能で
あるという欠点を有していた。また、その長時間運転に
伴う動力費の増大及び目づまり発生の問題等が存在して
いた。However, in the aeration of the above system, even if fine pores are provided in the diffuser pipe or the diffuser cylinder, for example, most of them eventually result from the surface tension of the bubbles when they are ejected from the pores. There are various drawbacks as described below, because the method is an air diffusion method by jetting or a method of generating bubbles by shearing the rotating blades and the projections. For example, in the method of ejecting air from a diffuser tube, diffuser plate, or cylinder, no matter how fine pores are provided, the surface tension of the bubbles when they eject from the pores results in about several millimeters. However, there is a drawback that large bubbles having a diameter of 10 are generated, and it is impossible to generate bubbles smaller than that. Further, there have been problems such as an increase in power cost and the occurrence of clogging due to the long-time operation.
【0005】そしてまた、上記回転羽根や突起体とのせ
ん断力を利用する方法においては、羽根や突起体との接
触により水棲動物、微小生物等を破壊する問題があっ
た。以上のような欠点や問題点を有した従来の閉鎖自然
水域浄化装置におけるエアレータにおいては、微細気泡
の発生量が少なく、湖沼水等中への酸素溶解量の増大が
期待できなかった。さらには、微細気泡の径と発生量を
容易に制御することと同時に強力かつ安定した循環流の
形成ができないことから、湖沼水等の浄化処理が効率的
に実施できない問題があった。Further, in the method utilizing the shearing force between the rotary blade and the projection, there is a problem that aquatic animals, microscopic organisms and the like are destroyed by the contact with the blade and the projection. In the aerator in the conventional closed natural water purification apparatus having the above-mentioned drawbacks and problems, the amount of fine bubbles generated is small, and it has been impossible to expect an increase in the amount of dissolved oxygen in lake water or the like. Further, since it is not possible to easily control the diameter and the generation amount of the fine bubbles and to form a strong and stable circulation flow, there is a problem that the purification treatment of lake water cannot be efficiently performed.
【0006】[0006]
【課題を解決するための手段及び作用】本発明者らは上
記従来技術の問題点を解決すべく鋭意研究を重ねた結
果、湖沼水等に微細な気泡を容易に供給でき、かつ同水
域に好適な循環流を生成し得るエアレータを備えた閉鎖
自然水域浄化装置を開発した。すなわち本発明は下記の
とおりの閉鎖自然水域浄化装置である。第1の発明は、
内壁に螺旋板を固着してなる円筒体と該円筒体下方開口
部直下に若干の間隔をおいて配置された空気供給口とか
ら構成される旋回式エアレータを、閉鎖自然水域底部に
配設してなることを特徴とする閉鎖自然水域浄化装置で
あり、第2の発明は、円筒体が、その全体又は上方部が
漸縮円筒体であることを特徴とする上記第1発明に記載
の閉鎖自然水域浄化装置であり、第3の発明は、螺旋板
が、多条のものであることを特徴とする第1又は第2発
明に記載の閉鎖自然水域浄化装置である。第4の発明
は、円筒体内の中心軸に旋回板支持支柱を設けたことを
特徴とする第1ないし第3発明のいずれかに記載の排水
処理装置であり、第5の発明は、円筒体下方開口部を縮
小してなることを特徴とする第1ないし第4発明のいず
れかに記載の閉鎖自然水域浄化装置であり、そして第5
の発明は、円筒体内壁に固着される螺旋板が、複数枚で
あり、リード角が0.7〜1.3であることを特徴とす
る第1ないし第5発明のいずれかに記載の閉鎖自然水域
浄化装置である。Means and Actions for Solving the Problems As a result of intensive studies conducted by the present inventors to solve the above-mentioned problems of the prior art, it is possible to easily supply fine air bubbles to lake water or the like, and We have developed a closed natural water purification system equipped with an aerator that can generate a suitable circulating flow. That is, the present invention is a closed natural water purification apparatus as described below. The first invention is
A swirl type aerator composed of a cylindrical body having a spiral plate fixed to the inner wall and an air supply port arranged at a slight distance immediately below the lower opening of the cylindrical body is arranged at the bottom of the closed natural water area. A closed natural water purification apparatus according to a second aspect of the present invention, wherein the whole or upper portion of the cylindrical body is a gradually contracting cylindrical body. A third aspect of the present invention is the closed natural water purification device according to the first or second aspect, characterized in that the spiral plate is a multi-row spiral plate. A fourth invention is the wastewater treatment apparatus according to any one of the first to third inventions, wherein a swivel plate support column is provided on the central axis of the cylindrical body, and the fifth invention is the cylindrical body. The closed natural water purification apparatus according to any one of the first to fourth inventions, characterized in that the lower opening is reduced.
The invention of No. 1 is the closure according to any one of the first to fifth inventions, wherein the spiral plate fixed to the inner wall of the cylindrical body is a plurality of spiral plates, and the lead angle is 0.7 to 1.3. It is a natural water purification device.
【0007】以上の発明においては、第1に、本発明に
係るエアレータによれば、従来の噴き出し方式のエアレ
ータよりもかなり小さい圧力損失となり、流動排水中へ
の気泡発生効率が飛躍的に向上する。第2に、本発明に
係る旋回式のエアレータによれば発生する微細気泡の平
均径を数100ミクロン以下に微細化することができ
る。よって、湖沼水等と酸化ガス気泡との接触面積を従
来方式の10〜100倍程度に、滞留時間を10〜10
0倍に高めることができ、溶解酸素量を飛躍的に増量す
ることができる。In the above invention, firstly, according to the aerator of the present invention, the pressure loss is considerably smaller than that of the conventional jet type aerator, and the efficiency of bubble generation in the flowing drainage is dramatically improved. .. Secondly, according to the swirl type aerator of the present invention, the average diameter of the generated fine bubbles can be reduced to several hundreds of microns or less. Therefore, the contact area between the lake water and the like and the oxidizing gas bubbles is 10 to 100 times that of the conventional method, and the residence time is 10 to 10 times.
It can be increased to 0 times, and the amount of dissolved oxygen can be dramatically increased.
【0008】第3に、漸縮円筒体の採用により、上昇気
液二相流の流速が増強され、閉鎖自然水域内に強力かつ
安定した循環流を形成することができる。しかも、漸縮
円筒体内には格別な突起物が存在しないため、圧力損失
はほとんどない。第4に、高速回転羽根や突起体への衝
突によってエアレーションを行う従来の方式では、微小
生物等が破壊される問題があったけれども、本発明によ
ればそうした問題はほとんど発生しない。第5に、円筒
体下部開口部が縮小されていることから、気体の上昇に
伴うエアリフト効果をさらに向上させ、湖沼等内の循環
流の形成が、その深部におけるへどろ等の沈澱化を防止
して、エアレーションによる浄化処理を行うことができ
る。第6に、下方配置の空気供給管から噴き出された空
気塊は、円筒体中の上昇連行過程で微細化されるのでエ
アレータに目づまりはほとんど発生しない。Thirdly, the adoption of the tapered cylinder increases the flow velocity of the ascending gas-liquid two-phase flow, so that a strong and stable circulating flow can be formed in the closed natural water area. Moreover, since there is no particular protrusion in the tapered cylinder, there is almost no pressure loss. Fourth, although the conventional method of performing aeration by the collision with the high-speed rotating blades or the protrusions has a problem of destroying microscopic organisms, such a problem hardly occurs according to the present invention. Fifth, since the opening in the lower part of the cylindrical body is reduced, the airlift effect due to the rise of gas is further improved, and the formation of a circulating flow in lakes and marshes prevents the sedimentation of medleys etc. Then, the purification process by aeration can be performed. Sixth, since the air mass blown out from the air supply pipe arranged below is atomized in the ascending and entraining process in the cylindrical body, the aerator is hardly clogged.
【0009】[0009]
【 実 施 例 】以下に、本発明の実施例のいくつかを図
面に基づいて説明する。図1は、本発明に係る旋回式エ
アレータを備えた閉鎖自然水域浄化装置を湖沼に適用し
た例の全体構成説明図を示す。図中65は気体移送管、
6は本発明に係る旋回式エアレータ、1は湖沼水等、3
はブロワーあるいはコンプレッサーである。図におい
て、閉鎖自然水域への気体移送管65の端部から、閉鎖
自然水域1水中に浄化用気体が旋回式エアレータ6を介
して供給される。旋回式エアレータ6内では上昇気体
と、これに伴うエアリフト効果による閉鎖自然水域水の
上昇連行過程で気泡の細分化が行なわれ、瞬時に気液更
新が行われる。さらには、気液混合流が螺旋板を内設し
た円筒体内を流通することによって、強力な循環流が水
域に形成される結果、閉鎖自然水域深層部に微細気泡の
運搬が行われ、その一部は旋回式エアレータ下部開口ま
で到達することができる。以上の行程が繰り返し続行さ
れて、湖沼水等1の溶存酸素量が増大され、さらにはそ
の底部にある無酸素塊が拡散されることによって、富栄
養化等により汚染された湖沼水等の閉鎖自然水域の浄
化、再生が図られることとなる。EXAMPLES Some examples of the present invention will be described below with reference to the drawings. FIG. 1 shows an overall configuration explanatory diagram of an example in which a closed natural water purification apparatus including a swirl type aerator according to the present invention is applied to a lake. In the figure, 65 is a gas transfer pipe,
6 is a swivel aerator according to the present invention, 1 is lake water, 3
Is a blower or compressor. In the figure, the purifying gas is supplied into the closed natural water 1 water from the end of the gas transfer pipe 65 to the closed natural water via the swirl aerator 6. In the swirl type aerator 6, bubbles are subdivided in the ascending process of ascending gas and water in the closed natural water region due to the air lift effect accompanied by the ascending gas, and gas-liquid renewal is instantaneously performed. Furthermore, the gas-liquid mixed flow flows through the cylindrical body with the spiral plate inside to form a strong circulation flow in the water area.As a result, fine bubbles are transported to the deep part of the closed natural water area. The part can reach the lower opening of the swivel aerator. By repeating the above process repeatedly, the dissolved oxygen content of lake water etc. 1 is increased, and further the oxygen-free mass at the bottom is diffused to close lake water etc. contaminated by eutrophication etc. Purification and regeneration of natural waters will be achieved.
【0010】上記閉鎖自然水域浄化装置においては、エ
アレータとして図2以下に図示する内部に螺旋板を固着
した円筒体を使用しているため、まず散気管を用いる従
来法のような多大な圧力損失エネルギーを要しなく、そ
して、せん断力を利用して気液を細分化する方式のため
に、散気管の場合のような大直径の気泡が生じるのでは
なく、極めて微小直径の気泡と比較的大直径の気泡の二
種類が発生する。したがって、気泡と湖沼水等との接触
表面積が増大し、気体の水中への溶解効率が非常に向上
し、その結果、高効率で湖沼水等のCODやBODの低
減を図ることができる。In the above-mentioned closed natural water purification apparatus, since the cylindrical body having a spiral plate fixed inside is used as an aerator as shown in FIG. 2 and subsequent figures, first of all, a large pressure loss as in the conventional method using an air diffuser is required. Due to the method that requires less energy and uses the shearing force to subdivide gas-liquid, rather than generating large-diameter bubbles as in the case of diffuser tubes, it is possible to compare bubbles with extremely small diameters. Two types of large diameter bubbles are generated. Therefore, the contact surface area between the bubbles and the lake water or the like increases, and the dissolution efficiency of the gas into the water is greatly improved. As a result, COD and BOD of the lake water and the like can be reduced with high efficiency.
【0011】図2は、本発明の閉鎖自然水域浄化装置を
浄水場混和池に適用した例の全体構成説明平面図であ
る。図2は、浄水場混和池の一部を示すが、まず同池で
は上水を得るために浄化用水路2に入る閉鎖自然水域水
に水路入口2’から活性炭粉等を混入する。しかしこれ
らが水路中で沈降し、活性炭等の必要量を増大させる原
因となっている。これは例えば流速7m/秒で閉鎖自然
水域水が浄化用水路を通過する場合、水路長70mで混
入された活性炭がほぼ全量水路中に沈降するという状況
に代表される。この時本発明に係る旋回式エアレータ6
・・を上向に傾斜して水路2の所々に設置し、これにブ
ロワーあるいはコンプレッサー3より浄化用気体をバル
ブ4・・を介して供給すれば、微細気泡に活性炭粉が付
着し水路下流にまで活性炭粉を運搬することができると
同時に水路隅部底部に活性炭粉が沈澱することも防止で
きる。FIG. 2 is a plan view showing the overall construction of an example in which the closed natural water purification apparatus of the present invention is applied to a water purification plant mixing pond. FIG. 2 shows a part of the water treatment plant mixing pond. In the pond, first, activated carbon powder or the like is mixed into the closed natural body water entering the purification water channel 2 from the water channel inlet 2'to obtain clean water. However, these settle down in the waterways and cause the increase in the required amount of activated carbon and the like. This is represented by a situation in which, for example, when closed natural water at a flow rate of 7 m / sec passes through a purification channel, almost all of the activated carbon mixed with a channel length of 70 m settles in the channel. At this time, the swing type aerator 6 according to the present invention
.. are installed in various places in the waterway 2 with an upward inclination, and if a purifying gas is supplied to this from the blower or the compressor 3 via the valve 4 .. The activated carbon powder can be transported up to and at the same time the activated carbon powder can be prevented from settling at the bottom of the corner of the waterway.
【0012】図3は、本発明実施例の閉鎖自然水域浄化
装置に係る旋回式エアレータの円筒体部の一部切欠斜視
図である。図3において、60は(樹脂製の)円筒体、
61・・は螺旋板、62は螺旋板支持支柱、63は下方
開口部を縮小した気液導入部である。FIG. 3 is a partially cutaway perspective view of the cylindrical body portion of the swirl type aerator according to the closed natural water purification apparatus of the embodiment of the present invention. In FIG. 3, 60 is a (resin) cylindrical body,
61 ... Is a spiral plate, 62 is a spiral plate supporting column, and 63 is a gas-liquid introducing part with a lower opening reduced.
【0013】図4は、本発明実施例の閉鎖自然水域浄化
装置に係る旋回式エアレータの一部切欠取付斜視図であ
り、図5(a)、(b)は平面図及び縦断面図である。
ここで、気体(通常は空気)は気体供給管65より供給
され、空気供給口66より、サポート64に取付られた
旋回式エアレータの円筒体60に供給される。なお、サ
ポート64と気体導入部63及び気体供給管65とは、
強力接着剤等による接着あるいは溶着により固着されて
おり、さらにそれらは、取付用Uバンド68により、エ
アレータ取付架台67に固定されて取付られている。同
図において、気体が気体供給管65内を矢印方向から流
れてくると、空気供給口66において空気塊となって閉
鎖自然水域水中に放出される。この空気塊はその浮力に
より上昇する過程で気液導入部63に導入され、螺旋板
61・・に側って上昇しながら旋回を増す過程で、円筒
体内の旋回閉鎖自然水域水との間に形成されるせん断力
で微細化される。本例では、螺旋板61・・は、90゜
間隔で4枚取着されており、リード角βは1.0であ
る。通常、リード角βは0.7〜1.3程度が望まし
い。次いで、発生した微細気泡を含む気液二相流は、漸
縮円筒体60’内で更にその上昇速度を増し、閉鎖自然
水域内に強力で安定した循環流を連続して形成し、その
深層部まで微細気泡を運搬することとなる。FIG. 4 is a partially cutaway perspective view of a swirl type aerator relating to a closed natural water purification apparatus according to an embodiment of the present invention, and FIGS. 5 (a) and 5 (b) are a plan view and a vertical sectional view. ..
Here, the gas (usually air) is supplied from the gas supply pipe 65, and is supplied from the air supply port 66 to the cylindrical body 60 of the swivel aerator attached to the support 64. The support 64, the gas introduction part 63, and the gas supply pipe 65 are
They are fixed by adhesion or welding with a strong adhesive or the like, and they are fixed and attached to the aerator attachment base 67 by the attachment U band 68. In the figure, when gas flows in the gas supply pipe 65 from the direction of the arrow, it becomes an air mass at the air supply port 66 and is discharged into the closed natural water body water. This air mass is introduced into the gas-liquid introducing portion 63 in the process of rising due to its buoyancy, and in the process of increasing the swirl while rising toward the spiral plate 61, ... It is refined by the shearing force that is formed. In this example, four spiral plates 61 ... Are attached at 90 ° intervals, and the lead angle β is 1.0. Usually, the lead angle β is preferably about 0.7 to 1.3. Then, the gas-liquid two-phase flow containing the generated fine bubbles further increases its rising speed in the gradually contracting cylindrical body 60 ′, continuously forming a strong and stable circulating flow in the closed natural water area, and its deep layer. Fine bubbles will be transported to the part.
【0014】図6は、従来の単管曝気式エアレータによ
る発生気泡と実施例のエアレータによる発生気泡の気泡
径・気泡発生率等の分布図である。この場合の測定条件
は両者共、下記のとおりである。 FIG. 6 is a distribution diagram of bubble diameters, bubble generation rates, etc. of bubbles generated by the conventional single tube aeration type aerator and bubbles generated by the aerator of the embodiment. The measurement conditions in this case are as follows.
【0015】本発明に係るエアレータの閉鎖自然水域内
における設置は、水域内に多数個を配設することが好ま
しく、特に例えば3〜5個を一まとめにしたものを適宜
距離間隔を隔てて、湖沼等の底部中央部と右側とに配設
することにより、湖沼等内に安定した強力な循環流を生
成せしめるようにすることも好ましい。When the aerator according to the present invention is installed in a closed natural water area, it is preferable to dispose a large number of pieces in the water area. Particularly, for example, a group of 3 to 5 pieces is arranged at appropriate distance intervals. It is also preferable to arrange them at the bottom center and the right side of a lake or the like so as to generate a stable and strong circulating flow in the lake or the like.
【0016】[0016]
【発明の効果】以上実施例等で詳述したように、本発明
によれば下記のごとき優れた多くの作用効果が発揮され
る。 (1)本発明に係るエアレータによれば、従来の噴き出
し方式のエアレータよりもかなり小さい圧力損失とな
り、閉鎖自然水域水中での気泡発生効率が飛躍的に向上
する。 (2)従来の噴き出し方式ではセラミックス製等の不規
則多孔質管の細孔の径をミクロン程度に小さくしてもそ
こから発生する気泡の径は平均的に数ミリメートルほど
あったが、本発明に係る旋回式のエアレータによれば発
生する微細気泡の平均径を数100μmから数10μm
に微細化することができる。よって、湖沼水等と酸化ガ
ス等の気泡との接触面積を極端に増大することができ、
その結果湖沼水等中への溶解酸素量を飛躍的に増量する
ことができる。 (3)漸縮円筒体の採用により、上昇気液二相流の旋回
上昇流速が増大され、閉鎖自然水域内に強力かつ安定し
た循環流を形成することができる。この時、漸縮円筒体
内には圧力損失がほとんどない。As described above in detail in the embodiments and the like, according to the present invention, many excellent effects as described below are exhibited. (1) According to the aerator of the present invention, the pressure loss is considerably smaller than that of the conventional jet aerator, and the bubble generation efficiency in the closed natural water body water is dramatically improved. (2) In the conventional ejection method, even if the diameter of the pores of the irregular porous tube made of ceramics or the like is reduced to about micron, the diameter of the bubbles generated therefrom is about several millimeters on average. According to the swirl type aerator of the present invention, the average diameter of the fine bubbles generated is from several 100 μm to several 10 μm.
Can be miniaturized. Therefore, the contact area between the lake water etc. and the bubbles of the oxidizing gas etc. can be extremely increased,
As a result, the amount of dissolved oxygen in lake water or the like can be dramatically increased. (3) By adopting the taper cylinder, the swirl rising velocity of the rising gas-liquid two-phase flow is increased, and a strong and stable circulating flow can be formed in the closed natural water area. At this time, there is almost no pressure loss in the tapered cylinder.
【0017】(4)特に円筒体下部開口部を絞って縮小
したものにあっては、気体の上昇に伴うエアリフト効果
をさらに向上させるために、自然閉鎖水域内水底付近に
沈澱するヘドロ等を巻き上げ、水底付近の腐敗を防止す
ることができる。 (5)高速回転羽根や突起体への衝突によってエアレー
ションを行う従来の方式では、微小生物などが破壊され
る問題があったが、本発明によればそうした問題は全く
発生しない。 (6)本発明に係る旋回式エアレータの空気供給口から
噴き出された空気塊は上昇連行過程で微細化されるので
該エアレータに目づまりはほとんど発生しない。(4) In particular, in the case where the opening at the lower part of the cylindrical body is narrowed and reduced, in order to further improve the airlift effect due to the rise of gas, the sludge and the like that settle near the water bottom in the naturally closed water area are rolled up. , It is possible to prevent decay near the bottom of the water. (5) The conventional method of performing aeration by colliding with a high-speed rotating blade or a protrusion has a problem of destroying microscopic organisms, but according to the present invention, such a problem does not occur at all. (6) Since the air mass ejected from the air supply port of the swirl type aerator according to the present invention is atomized in the ascending and entraining process, there is almost no clogging in the aerator.
【図1】本発明実施例に係る旋回式エアレータを備えた
閉鎖自然水域浄化装置を湖沼に適用した例の全体構成説
明図。FIG. 1 is an overall configuration explanatory diagram of an example in which a closed natural water purification device including a swirl aerator according to an embodiment of the present invention is applied to a lake.
【図2】本発明に係る旋回式エアレータを備えた閉鎖自
然水域浄化装置を浄水場混和池に適用した例の全体構成
説明平面図。FIG. 2 is an overall configuration explanatory plan view of an example in which a closed natural water area purification device including a swirl aerator according to the present invention is applied to a water purification plant mixing basin.
【図3】実施例旋回式エアレータの円筒体部の一部切欠
斜視図。FIG. 3 is a partially cutaway perspective view of a cylindrical body portion of the swivel aerator of the embodiment.
【図4】実施例旋回式エアレータの一部切欠概略取付斜
視図。FIG. 4 is a partially cut-away schematic mounting perspective view of the swivel aerator of the embodiment.
【図5】(a)及び(b)は、実施例旋回式エアレータ
の平面図及び縦断面図。5 (a) and 5 (b) are a plan view and a vertical sectional view of a swivel aerator of an embodiment.
【図6】従来の単管曝気式エアレータと本発明実施例に
係る旋回式エアレータによる発生気泡の気泡径・気泡発
生率の分布図。FIG. 6 is a distribution diagram of bubble diameters and bubble generation rates of bubbles generated by a conventional single tube aeration type aerator and a swirl type aerator according to an embodiment of the present invention.
1:湖沼水等 2:閉鎖自然水域浄化用水路 2’:水路入口 3:ブロワー 4:バルブ 6・・:旋回式エアレータ 60:円筒体 60’:漸縮円筒体 61・・:螺旋板 62:螺旋板支持支柱 63:気液導入部 64:サポート 65:気体供給管 66:空気供給口 67:エアレータ取付架台 68:取付用Uバンド 1: Lake water etc. 2: Closed natural water purification channel 2 ': Channel inlet 3: Blower 4: Valve 6 ...: Swirling aerator 60: Cylindrical body 60': Reduced cylindrical body 61 ... Plate support column 63: Gas-liquid introduction part 64: Support 65: Gas supply pipe 66: Air supply port 67: Aerator mounting stand 68: U band for mounting
Claims (6)
円筒体下方開口部直下に若干の間隔をおいて配置された
気体供給口とから構成される旋回式エアレータを、閉鎖
自然水域底部に配設してなることを特徴とする閉鎖自然
水域浄化装置。1. A swirl type aerator comprising a cylindrical body having a spiral plate fixed to an inner wall thereof and a gas supply port arranged at a slight distance immediately below the lower opening of the cylindrical body to close a natural water area. A closed natural water area purification device characterized by being arranged at the bottom.
筒体であることを特徴とする請求項1記載の閉鎖自然水
域浄化装置。2. The closed natural water purification apparatus according to claim 1, wherein the whole or upper part of the cylindrical body is a gradually contracting cylindrical body.
とする請求項1又は2に記載の閉鎖自然水域浄化装置。3. The closed natural water purification apparatus according to claim 1, wherein the spiral plate has a multi-row structure.
けたことを特徴とする請求項1ないし3のいずれかに記
載の閉鎖自然水域浄化装置。4. The closed natural water purification apparatus according to claim 1, wherein a swivel plate support column is provided on a central axis of the cylindrical body.
特徴とする請求項1ないし4のいずれかに記載の閉鎖自
然水域浄化装置。5. The closed natural water purification apparatus according to claim 1, wherein the lower opening of the cylindrical body is reduced.
枚であり、リード角が0.7〜1.3であることを特徴
とする請求項1ないし5のいずれかに記載の閉鎖自然水
域浄化装置。6. The closure according to claim 1, wherein there are a plurality of spiral plates fixed to the inner wall of the cylindrical body, and the lead angle is 0.7 to 1.3. Natural water purification equipment.
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP33591491A JPH05146796A (en) | 1991-11-27 | 1991-11-27 | Device for purifying closed natural water area |
KR1019920019670A KR930009931A (en) | 1991-11-27 | 1992-10-24 | Closed natural water purifier |
CN92113369A CN1072662A (en) | 1991-11-27 | 1992-11-20 | The refining plant of closed natural water area |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP33591491A JPH05146796A (en) | 1991-11-27 | 1991-11-27 | Device for purifying closed natural water area |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH05146796A true JPH05146796A (en) | 1993-06-15 |
Family
ID=18293781
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP33591491A Pending JPH05146796A (en) | 1991-11-27 | 1991-11-27 | Device for purifying closed natural water area |
Country Status (3)
Country | Link |
---|---|
JP (1) | JPH05146796A (en) |
KR (1) | KR930009931A (en) |
CN (1) | CN1072662A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2011098256A (en) * | 2009-11-04 | 2011-05-19 | Japan Water Agency | Submerged combined aerator |
US8172909B2 (en) | 2005-12-22 | 2012-05-08 | The United States Of America, As Represented By The Secretary Of The Army | Modular prosthetic foot |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20030025596A (en) * | 2001-09-21 | 2003-03-29 | 김대봉 | An underwater interception way make use of an air bubble and equipment |
CN101037276B (en) * | 2007-03-30 | 2010-05-19 | 西安建筑科技大学 | Apparatus for improving aerating reinforced active carbon adsorption water source quality |
CN105566016A (en) * | 2016-02-25 | 2016-05-11 | 中国葛洲坝集团易普力股份有限公司 | Mechanical foaming device for medium-high temperature emulsion explosives |
CN110510819A (en) * | 2019-09-02 | 2019-11-29 | 深圳市前海万绿源环保科技有限公司 | A kind of sewage gas explosion ball treatment process |
-
1991
- 1991-11-27 JP JP33591491A patent/JPH05146796A/en active Pending
-
1992
- 1992-10-24 KR KR1019920019670A patent/KR930009931A/en not_active Application Discontinuation
- 1992-11-20 CN CN92113369A patent/CN1072662A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8172909B2 (en) | 2005-12-22 | 2012-05-08 | The United States Of America, As Represented By The Secretary Of The Army | Modular prosthetic foot |
US8685108B2 (en) | 2005-12-22 | 2014-04-01 | The United States Of America As Represented By The Secretary Of The Army | Modular prosthetic foot |
JP2011098256A (en) * | 2009-11-04 | 2011-05-19 | Japan Water Agency | Submerged combined aerator |
Also Published As
Publication number | Publication date |
---|---|
KR930009931A (en) | 1993-06-21 |
CN1072662A (en) | 1993-06-02 |
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