JPH01500019A - Method and apparatus for introducing gas into a liquid - Google Patents

Method and apparatus for introducing gas into a liquid

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Publication number
JPH01500019A
JPH01500019A JP62503474A JP50347487A JPH01500019A JP H01500019 A JPH01500019 A JP H01500019A JP 62503474 A JP62503474 A JP 62503474A JP 50347487 A JP50347487 A JP 50347487A JP H01500019 A JPH01500019 A JP H01500019A
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liquid
gas
paddle
container
quadrant
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コーネリッセン,ジャン
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ピーケンロート‐ヴィニテックス ベェ.ヴェ.
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D19/00Degasification of liquids
    • B01D19/0042Degasification of liquids modifying the liquid flow
    • B01D19/0052Degasification of liquids modifying the liquid flow in rotating vessels, vessels containing movable parts or in which centrifugal movement is caused
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D19/00Degasification of liquids
    • B01D19/0005Degasification of liquids with one or more auxiliary substances
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20Mixing gases with liquids
    • B01F23/23Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/234Surface aerating
    • B01F23/2342Surface aerating with stirrers near to the liquid surface, e.g. partially immersed, for spraying the liquid in the gas or for sucking gas into the liquid, e.g. using stirrers rotating around a horizontal axis or using centrifugal force
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/02Aerobic processes
    • C02F3/12Activated sludge processes
    • C02F3/14Activated sludge processes using surface aeration
    • C02F3/18Activated sludge processes using surface aeration the aerator having a horizontal axis
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/60Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis
    • 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

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Microbiology (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
  • Mixers Of The Rotary Stirring Type (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるため要約のデータは記録されません。 (57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 液体にガスを導入する方法及び装置 本発明は、主として水平方向に回転する軸を有する回転櫂組立体を備え、液中に 入る容器を用いてガスを液中に導入する方法及びその装置に関し、その櫂は液の 上方に存在するガスから液中にガスを導入するようになっている。[Detailed description of the invention] Method and apparatus for introducing gas into a liquid The present invention comprises a rotary paddle assembly having a shaft that rotates primarily in a horizontal direction, and which is submerged in a liquid. Relating to a method and apparatus for introducing gas into a liquid using a container, the paddle is Gas is introduced into the liquid from the gas present above.

EP−B OOO5553によシこの目的に適合する装置は公知であるが、その 装置ではスポークで回転軸に連結されているスコップが、上方に開口し、そこか ら液体が入るようになっている部分的に円筒をなす容器の内壁に沿って動き、そ の軌道の1部が液体上のガス空間を通る。この軌道の上部で液体がスコップから ガスを通って流れ、それによってガスを吸収し更にガスはスコップで液中にすく h込まれ、軌道の低い部分でガスの泡となって逃げる。この泡は前記スコップの 後方部分に至るので液表面へガスが直接逃げることは阻止される。ガスの液の方 向への移動はむしろ遅い、というのは集められた泡は容易に合体し大きなガスク ッションを形成し、液との接触領域が小さくなるからである。このような装置で はガスのとシ込みは比較的少ない。According to EP-B OOO5553, devices suitable for this purpose are known; In the device, a scoop connected to a rotating shaft with spokes opens upwards, and It moves along the inner wall of a partially cylindrical container that is intended to contain liquid; A part of its trajectory passes through the gas space above the liquid. At the top of this orbit, the liquid comes out of the scoop. The gas flows through the liquid, thereby absorbing the gas, which is then scooped into the liquid. It escapes in the form of gas bubbles in the lower part of its orbit. This foam is removed from the scoop. Since it reaches the rear part, gas is prevented from escaping directly to the liquid surface. Gas liquid side The movement in the direction is rather slow, as the collected bubbles easily coalesce and form large gas This is because the contact area with the liquid becomes smaller. With such a device There is relatively little gas leakage.

本発明は、液体にガスを可成シとシ込むことのできる方法と装置を提供すること を目的にしている。The present invention provides a method and apparatus capable of injecting gas into a liquid. The purpose is

この目的11:達成するために本発明による方法では容器が部分的に液で充たさ れ、櫂は液体が回転するように上方に押し遣られるような速度で駆動され、その 復液が下方にこぼれて水力ジャンプを形成して液のひっくシ返った部分がこのジ ャンプ中に散乱して落下し、これによってガスを液中にとシ込む。To achieve this objective 11, the method according to the invention allows the container to be partially filled with liquid. The paddle is driven at such a speed that the liquid is forced upward in a rotational manner, and its This is the part where the condensate spills downward and forms a hydraulic jump. It scatters and falls during the camp, thereby injecting gas into the liquid.

この水カシヤングによって動くスコツfがガスを液中にとシ込む。ガスの泡の密 度が高い程液中にガスが多く残る。ガスの泡は水力ジャンプによシ液中に残るが 、これが液に対して大きな刺激をもたらす。Scot f, which is moved by this water pump, injects gas into the liquid. dense gas bubbles The higher the temperature, the more gas remains in the liquid. Gas bubbles remain in the liquid due to the hydraulic jump. , which causes great irritation to the liquid.

これによって液とガスとの間に広い境界面をもたらす。This provides a wide interface between liquid and gas.

水を叩いて空気を入れる実験によると、5000mg/l、5以上の散索をとシ 込むことができるが、従来の装置ではそれ以上が可能となる。これによると約2 .5ゆ/ kWhの醒素をとシ込む効率が得られる。According to an experiment by tapping water to introduce air, it was found that 5000 mg/l, 500 mg/l or more, However, conventional equipment allows for much more. According to this, about 2 .. Efficiency of 5 Yu/kWh of energy injection can be obtained.

ガスを液体にとシ込むとともにこの方法は液中の揮発成分を除くのにも使われる が、その場合気をっけなければならないことは、液から逃げるガスが除去される 揮発成分とともに、ガス供給とは別々に排出されるということである。In addition to injecting gas into a liquid, this method is also used to remove volatile components from the liquid. However, in that case, you must be careful that the gas escaping from the liquid is removed. This means that the volatile components are discharged separately from the gas supply.

望むらくは、液へのガスのとり込みは圧力をかけて行うことによシ改善される。Preferably, gas incorporation into the liquid is improved by applying pressure.

本発明はこの方法全実施する装置全提供するものであシ、液体の供給と放出を伴 う容器と、この容器の水平軸に沿って設けられ、液上であって前記容器内のガス からガスを液中にとシ込むようにした曜車とを有し、その特徴とするところは、 曜車の櫂の4が、操作速度で曜車を駆動したとき液体を、櫂が上昇する第1の四 分日中の最も高い点まで液体を押し上げるのに充分なようになっておシ、1万次 の四分円で乱れ落ちる液体の外層は前記quadrant巾を下降する櫂の輪に 入ることはない。The present invention provides a complete apparatus for carrying out this method, which involves supplying and discharging liquids. a container disposed along the horizontal axis of the container, above the liquid and containing the gas in the container; It has a day wheel that allows gas to be injected into the liquid, and its features are as follows: When the four paddles of the day wheel drive the day wheel at the operating speed, the liquid is transferred to the first four paddles as the paddle rises. It is enough to push the liquid up to the highest point in the day, 10,000 times. The outer layer of liquid falling turbulently in the quadrant of I won't go in.

特に、この装置の壁は少なくとも前記第1のquadrantで実質的に曜車の 軸と同軸であシ、櫂の外端部からほんの少しだけ離れたところに位置している。In particular, the wall of the device substantially covers the day wheel in at least said first quadrant. It is coaxial with the shaft and located just a short distance from the outer end of the paddle.

このように液体は櫂によって最も高い点に駆動され最適効果が得られる。最適の 操作としてはガス空間は水を押し上げた後の櫂の輪の内側に残っていることであ り、このことによって櫂の幅が決まる。In this way the liquid is driven by the paddle to the highest point for optimum effect. optimal In operation, the gas space remains inside the paddle ring after pushing up the water. This determines the width of the paddle.

他方において櫂の幅は液体の押し上げの面及び泡導入の面から出来るだけ大きい 方が良い。On the other hand, the width of the paddle is as large as possible in terms of liquid uplift and foam introduction. It's better.

NL−A 6508434で通気装置はそのままで知られる、つまシ、長手軸方 向に配された櫂組立体の回転軸を有する円筒容器からなり、その櫂組立体は液体 をとシ込み、液体は完全に容器を充たし、回転して、前記軸を介してら旋形状の 泡の路をなして導入される泡は、静止した水の中に垂直な泡の路をなす場合に比 較して増加される。この公知の装置は本発明の装置よシ複雑である。すなわち、 その理由はガスを圧力下で中空軸に供給するための付加装置を要するからである 。NL-A 6508434, the venting device is known as it is, the tab, longitudinal axis It consists of a cylindrical container with a rotation axis of a paddle assembly oriented in the The liquid completely fills the container and rotates through the shaft into a spiral shape. Bubbles introduced in a bubble path are compared to vertical bubble paths in still water. Increased compared to This known device is more complex than the device of the invention. That is, The reason is that additional equipment is required to supply gas under pressure to the hollow shaft. .

特に本発明による装置の容器においては、少なくも櫂の動きの第2の四分円では 、泡導入を高める水力ジャンプを出来るだけ小さく保つために、櫂の軌道に接近 して配したバッフル又は壁を備えている。Particularly in the case of the device according to the invention, at least in the second quadrant of the paddle movement. , close to the paddle trajectory to increase foam introduction and keep the hydraulic jump as small as possible. It is equipped with baffles or walls arranged in such a way that the

少なくとも櫂の一部の間には邪魔板又は孔あき板が設けられそれによって引摺ら れるガス泡の寸法を細かにする効果を得ている。A baffle plate or perforated plate is provided between at least a portion of the paddles, thereby preventing the dragging. This has the effect of making the size of the gas bubbles smaller.

更にこの容器の上側が円筒形であって、そこには1つ又はそれ以上のガス供給孔 が明いていて、櫂の第2四分円のときに通じ合うようになっている。Additionally, the upper side of the container is cylindrical and has one or more gas supply holes therein. is clear, and they can communicate in the second quadrant of the paddle.

本発明による装置が揮発性分を液体から除去することも目指すならば、容器には ガス供給口とは別にガス排出口も設けねばならない。If the device according to the invention also aims to remove volatile components from liquids, the container In addition to the gas supply port, a gas discharge port must also be provided.

本発明は図面を参照して以下に更に詳細に説明される。The invention will be explained in more detail below with reference to the drawings.

第1図は休止状態にある本発明の装置の模式断面図、 第2図は活動状態の第1図に相当する断面図、第3図は他の実施例による第2図 に相当する断面図、 第4図は本発明による1装置の側面図である。FIG. 1 is a schematic cross-sectional view of the device of the present invention in a resting state; FIG. 2 is a sectional view corresponding to FIG. 1 in an active state, and FIG. 3 is a second diagram according to another embodiment. A cross-sectional view corresponding to FIG. 4 is a side view of one device according to the invention.

図面に示された装置は、その内部に回転軸3の回シに配された櫂で構成される曜 車を有する円筒容器からなシ、その回転軸3は容器1の長手軸に溢って伸びてい る。実施例において櫂2にはL字形部分があシ図示しないアーム又は円板によっ て軸3に連結されている。第1図に示す休止状態では容器1は部分的に液体4で 充たされておシ、液体の上方にガス空間5が1つ又はそれ以上のガス供給孔と連 通している。若し液体4が通常の圧力下で通気されるものならば、孔6は大気と 連通ずる。The device shown in the drawing has a paddle inside which is arranged on the rotary shaft 3. It is a cylindrical container with a wheel, the rotation axis 3 of which extends over the longitudinal axis of the container 1. Ru. In the embodiment, the paddle 2 has an L-shaped portion and is supported by an arm or disc (not shown). and is connected to the shaft 3. In the resting state shown in FIG. 1, the container 1 is partially filled with liquid 4. When filled, a gas space 5 above the liquid communicates with one or more gas supply holes. I'm passing through. If the liquid 4 is to be vented under normal pressure, the holes 6 are connected to the atmosphere. Communicate.

第2図に示すように軸3が矢印7の方向に回転するならば、液体4は充分な回転 速度で上方の8方向へ追随し押し上げられる。液体の重量によシ液体は押し上げ られた後、下方へ落下するがその際容器1の側壁にまで至る所謂水力ジャンプ9 を形成する。If the shaft 3 rotates in the direction of the arrow 7 as shown in FIG. The speed follows you in eight directions upwards and pushes you up. The weight of the liquid pushes the liquid upwards. After falling, the so-called hydraulic jump 9 reaches the side wall of the container 1. form.

液体はそこでかき回され空間5からのガスと混ぜ合せられ、櫂2は領域9で再び 液体中に入り、矢印10で示すように領域9から液体中にガスの泡を導入する。The liquid is stirred there and mixed with the gas from space 5, and paddle 2 is moved again in region 9. Entering the liquid, gas bubbles are introduced into the liquid from region 9 as indicated by arrow 10.

ガスの泡は液の渦流に伴って再び領域9へ向けて矢印11のように逃げるがその 逃げるガスの泡が領域9で液体を激しく刺激する。The gas bubbles escape again towards area 9 as shown by arrow 11 along with the swirling flow of the liquid, but The escaping gas bubbles violently stimulate the liquid in region 9.

ガスの混合によシ領域9のレベルは第1図に示す静止条件下の液体のレベルとほ ぼ同じである。ガス空間の容積は、上方へ押し上げられた液8と泡の形で液中に とり込まれたガスの量とで可成シ減少する。Due to the mixing of gases, the level in region 9 is approximately the same as the level of the liquid under static conditions as shown in Figure 1. They are almost the same. The volume of the gas space is the liquid 8 pushed upwards and the liquid in the form of bubbles. The amount of gas taken in decreases considerably.

曜車の静止状態でのガス空間5が大きい程、液の押し上げられた部分8及び液4 中に導入されるガスの泡の量が多くなる。しかしながら、ガス空間が増加するこ とは液体の量も減少することになるので、ガスと液体との最適な接触面が得られ る液面レベルがある。ガスの泡を沢山導入することは液量を減らして得られるも のではない。The larger the gas space 5 when the day wheel is at rest, the larger the portion 8 of the liquid pushed up and the larger the liquid 4. The amount of gas bubbles introduced into the tank increases. However, the gas space increases. This means that the amount of liquid is also reduced, so an optimal contact surface between gas and liquid can be obtained. There is a liquid level. Introducing a large number of gas bubbles can be achieved by reducing the amount of liquid. It's not.

櫂2は軸3の方向に、液が充分に押し上げられ充分なガスの泡が導入されるよう な距離だけ伸びている。この幅は、最適な作動のためにはガス空間が櫂2のリン グ内に存在すべきという要求によって限定される。速度が早すぎたり櫂の偏が大 きすぎたシすると、ガス空間が櫂の間にのみあるときに、ガスの泡の導入が減少 する。The paddle 2 is moved in the direction of the axis 3 so that the liquid is sufficiently pushed up and sufficient gas bubbles are introduced. It extends by a distance. This width requires that the gas space be within the paddle 2 ring for optimal operation. limited by the requirement that it be within the group. The speed is too fast or the paddle is too uneven. Setting it too high will reduce the introduction of gas bubbles when the gas space is only between the paddles. do.

液に追随するガスの泡の寸法を小さくするために、第3図に模式的に示したよう に孔明き板12を多数櫂の間に設けることができる。In order to reduce the size of gas bubbles that follow the liquid, as shown schematically in Figure 3, Perforated plates 12 can be provided between the paddles.

ガス泡の寸法を小さくすることによってガスと液体の接憩面を大きくすることが できるが、そうすると領域9もまた逃げるガスのためかき回しか弱くなる。もし ガスの泡が小さすぎると、小さい泡の滞留時間が長くなシすぎる。こういう現象 は装置の使い方によって決まる。By reducing the size of the gas bubble, the interface between gas and liquid can be increased. It can be done, but then the stirring in region 9 will also be weaker due to the escaping gas. if If the gas bubbles are too small, the residence time of the small bubbles is too long. This kind of phenomenon depends on how the device is used.

第3図は断面長方形をなした他の容器の実施例を示す。その側壁13又は対応す る付謔バッフルが櫂2の軌道近くに領域9を形成し、屈曲したバッフル14が液 体を最も高い位置8へ押し上げる。FIG. 3 shows another embodiment of a container having a rectangular cross section. Its side wall 13 or corresponding An attached baffle forms a region 9 near the track of the paddle 2, and a bent baffle 14 Push your body up to the highest position 8.

第4図にみられるように、容器1は通気のために、エア供給を分配するために別 々の複数の供給孔を備えることができる。As can be seen in Figure 4, container 1 is provided separately for ventilation and for distributing the air supply. A plurality of supply holes may be provided.

モータ15は適当な減速手段を用いて軸3を駆動する。Motor 15 drives shaft 3 using suitable speed reduction means.

図示しない連結手段が処理すべき液体を供給し放出するが、その供給と放出は連 続流にしたければ連続的に行われる。液のレベルを維持するために、オーバーフ ローバッフル又は他のレベル制御手段が使われる。Connecting means (not shown) supply and discharge the liquid to be treated, and the supply and discharge are linked. If you want it to be a sequel, it will be done continuously. Overflow to maintain fluid level. Low baffles or other level control means are used.

そのような装置は水への通気例えば水の化学的酸素要求(COD )を減少せし めるための装置に使用できる。酸素をガ、ス空間に空気の代シに入れると酸素量 を4〜5倍に増やすことができる。Such devices can be used to aerate the water, e.g. to reduce the chemical oxygen demand (COD) of the water. It can be used for equipment for recording. When oxygen is introduced into a gas space instead of air, the amount of oxygen increases. can be increased 4 to 5 times.

他方の装置は液体から揮発性成分を除去できるが、この場合は勿論、ガス供給孔 6はさておきそれとは別に設けた放出孔もまた揮発性成分を放出するために必要 となる。The other device can remove volatile components from the liquid, but in this case, of course, the gas supply hole Apart from 6, a separate release hole is also necessary to release volatile components. becomes.

もし液体へのガス導入をもつと増加させるためには、ガス空間5に圧力をかける ことができる。If with the introduction of gas into the liquid, in order to increase the pressure in the gas space 5 be able to.

この装置を使っての実験で、径1mの容器1を使っての水道の水への酸素導入は s oo Orng/l、hで酸素導入効率は2.5 kg/ kWhであった 。これは従来の装置でより可成り改善されている。In an experiment using this device, oxygen was introduced into tap water using container 1 with a diameter of 1 m. The oxygen introduction efficiency was 2.5 kg/kWh at s Orng/l, h . This is a considerable improvement over conventional devices.

ガス導入は更に容器lの長さに直接比例し、構造の面、設けられている空間など によってのみ限定される。複数の容器を1列に又は並列に配することもできる。Gas introduction is also directly proportional to the length of the container l, and depends on the structure, the space provided, etc. limited only by. A plurality of containers can also be arranged in a row or in parallel.

このような装置は低圧の遠心ポンプと考えることができる。上方に押し上げられ た液体の振舞は波頭の崩れに比較でき、その芯部は下方に突進し水力ジャンプの 原因となりかぶさってくる部分がジャンプの中に崩れ込み、ガスを液体の中にと シ込む。Such devices can be thought of as low pressure centrifugal pumps. pushed upwards The behavior of the liquid can be compared to the collapse of a wave crest, with the core rushing downwards and causing a hydraulic jump. The overlying part collapses into the jump, releasing the gas into the liquid. Sink into it.

この装置は例えば大きな水たらいに通気するのに適しておシ、容器1は水に浸け て望みの水位にし、取水口を容器lの1端の軸3の近くに、出口を容器の他端の 周縁部の近くに設けることによって循環流全発生させることができる。This device is suitable for aerating large water basins, for example, and container 1 can be submerged in water. to the desired water level, place the water intake near the shaft 3 at one end of the container L, and the outlet at the other end of the container. By providing it near the periphery, a complete circulation flow can be generated.

通常の圧力下で通気する場合には容器lは大気と自由に連通ずる1つの連続孔6 を備えることができる。When venting under normal pressure, the container l has one continuous hole 6 in free communication with the atmosphere. can be provided.

水力ジャンプ領域9を画定するには2つの曜車2を1つの容器に並べて配列する ことによっても得ることができ、この車は対向して駆動されて隣り合ったジャン プ領域を形成し、互いに横方向を限定する。To define the hydraulic jump area 9, two day wheels 2 are arranged side by side in one container. It can also be obtained by driving the car oppositely to the adjacent jumper. forming dip regions and laterally limiting each other.

バッフル13は省かれるが、各曜車2に対しては屈曲したバッフル14を使うの がよい。The baffle 13 is omitted, but a bent baffle 14 is used for each day wheel 2. Good.

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Claims (10)

【特許請求の範囲】[Claims] 1.主として水平方向に回転する軸を有する櫂組立体を備え、前記櫂が液体上の 空間から液体の中へガスを導入するようになっている液体に浸った容器を用いて 液体の中へガスを導入する方法であって、前記容器(1)が部分的に液で充たさ れ、櫂(2)は液体が回転するように上方(8)に押し上げられ、その後液体の かぶさった部分がジャンプ(9)の中ヘ落下してガスを液体の中ヘ導入するよう な速度で駆動されることを特徴とするガスを液体ヘ導入する方法。1. a paddle assembly having an axis that rotates primarily in a horizontal direction, the paddle being above a liquid; using a container immersed in a liquid adapted to introduce gas into the liquid from a space A method of introducing gas into a liquid, the method comprising: said container (1) being partially filled with liquid; The paddle (2) is pushed upwards (8) as the liquid rotates, and then The covered part falls into the jump (9) and introduces gas into the liquid. A method for introducing a gas into a liquid, characterized in that the gas is driven at a certain speed. 2.液体から揮発性成分を除去するために使用され、液体から逃げるガスがガス 供給口からは別に放出されることを特徴とする請求の範囲第1項記載の方法。2. Used to remove volatile components from a liquid, the gases escaping from the liquid become gas A method according to claim 1, characterized in that the liquid is discharged separately from the supply port. 3.前記ガスが加圧されて供給されることを特徴とする請求の範囲第1項又は第 2項記載の方法。3. Claim 1 or claim 1, wherein the gas is supplied under pressure. The method described in Section 2. 4.液体供給口及び放出口を備えた容器と、前記容器の水平軸に沿って設けられ た櫂車とを有し、液体面上に位置するガス空間からガスを前記液体に導入するよ うになっている請求の範囲第1乃至3項記載の方法を実施する装置であって、櫂 車の櫂(2)の幅が、作動速度で櫂車を駆動するときに、液体(4)を櫂(2) が最高度に向って上方に動いている第1の四半円に押し上げるのに充分ではある が他方次の四分円を降下する液体の層が後者の四分円を下方に動く櫂(2)のリ ングには入り込めないように形成されていることを特徴とする装置。4. a container with a liquid supply inlet and an outlet; and a container provided along a horizontal axis of said container. and a paddle wheel for introducing gas into the liquid from a gas space located above the liquid surface. An apparatus for carrying out the method according to claims 1 to 3, which comprises: The width of the car's paddle (2) allows the liquid (4) to pass through the paddle (2) when driving the paddle car at the operating speed. is sufficient to push it into the first quadrant, which is moving upward towards its highest degree. On the other hand, the liquid layer descending in the next quadrant is caused by the flow of the paddle (2) moving downward in the latter quadrant. A device characterized in that it is formed so that it cannot enter the ring. 5.容器(1)の壁(14)が少なくとも第1の四分円で実質的に櫂車(2,3 )の軸(3)と同軸であることを特徴とする請求の範囲第4項記載の装置。5. The wall (14) of the container (1) is substantially in contact with the paddle wheels (2, 3) in at least the first quadrant. 5. A device according to claim 4, characterized in that it is coaxial with the axis (3) of the device. 6.前記第1四分円に続く櫂の次の四分円の少なくとも端部に容器(1)が櫂の 軌道に対して僅かな距離でパッフル又は壁(13)を備えていることを特徴とす る請求の範囲第4項又は5項記載の装置。6. At least at the end of the next quadrant of the paddle following said first quadrant, the container (1) is placed on the paddle. characterized by having a puffle or wall (13) at a small distance from the orbit. 6. The apparatus according to claim 4 or 5. 7.櫂(2)と軸(3)との間に邪魔板又は孔明き板(12)が設けられている ことを特徴とする請求の範囲第4乃至6項のうちいずれかに記載された装置。7. A baffle plate or perforated plate (12) is provided between the paddle (2) and the shaft (3). An apparatus according to any one of claims 4 to 6, characterized in that: 8.容器の少なくとも上側が円筒形であり、そこには櫂(2)の軌道の前記第2 四分円と連通する1個又はそれ以上のガス供給口を備えたことを特徴とする請求 の範囲第4乃至7項の1つに記載した装置。8. At least the upper side of the container is cylindrical, in which said second part of the track of the paddle (2) Claim characterized by having one or more gas supply ports communicating with the quadrant Apparatus according to one of the ranges 4 to 7. 9.液体から揮発性成分を除去すべく、ガス供給口(6)とは別に設けられたガ ス放出口を備えたことを特徴とする請求の範囲第4項乃至8項のいずれか1つに 記載した装置。9. A separate gas supply port (6) is installed to remove volatile components from the liquid. According to any one of claims 4 to 8, the invention is characterized in that it is equipped with a gas discharge port. Equipment described. 10.対向方向に回転する2つの櫂車を容器1内に並列に備えその水力ジャンプ 領域(9)が隣接するようになっていることを特徴とする請求の範囲第4項乃至 9項のいずれか1つに記載の装置。10. Hydraulic jump with two paddle wheels rotating in opposite directions arranged in parallel inside container 1 Claims 4 to 4, characterized in that the regions (9) are adjacent to each other. 10. Apparatus according to any one of clauses 9.
JP62503474A 1986-06-19 1987-06-18 Method and apparatus for introducing gas into a liquid Pending JPH01500019A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
NL8601602A NL8601602A (en) 1986-06-19 1986-06-19 METHOD AND APPARATUS FOR INPUTING A GAS INTO A LIQUID
NL8601602 1986-06-19

Publications (1)

Publication Number Publication Date
JPH01500019A true JPH01500019A (en) 1989-01-12

Family

ID=19848196

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62503474A Pending JPH01500019A (en) 1986-06-19 1987-06-18 Method and apparatus for introducing gas into a liquid

Country Status (5)

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US (1) US4904420A (en)
EP (1) EP0280689A1 (en)
JP (1) JPH01500019A (en)
NL (1) NL8601602A (en)
WO (1) WO1987007886A1 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5770068A (en) * 1996-02-20 1998-06-23 Ohio University Multi-phase mixing in a hydraulic jump
US6634626B2 (en) 2001-08-10 2003-10-21 Aeromix Systems, Inc. Horizontal surface aerator
US7332078B2 (en) * 2005-07-18 2008-02-19 Dee Thomas Murphy Apparatus for recovering energy from turbulence created within an aerobic biological reactor
WO2007115099A2 (en) * 2006-03-31 2007-10-11 Hills Blair H Apparatus for mixing gasses and liquids

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1167279B (en) * 1956-07-12 1964-04-02 Passavant Werke Ventilation device for wastewater treatment
US3134826A (en) * 1960-10-28 1964-05-26 Michael M Jalma Gas and liquid contact apparatus
US3266786A (en) * 1963-11-22 1966-08-16 Allis Chalmers Mfg Co Two-phase disk contactor
US3348829A (en) * 1963-12-18 1967-10-24 Allis Chalmers Mfg Co Aerator
NL6410463A (en) * 1964-09-09 1966-03-10
US3658305A (en) * 1969-05-08 1972-04-25 Thrive Centers Inc Aeration device
US4101384A (en) * 1974-11-16 1978-07-18 Friedrich Uhde Gmbh Apparatus for the fermentative conversion of a nutrient mixture by means of microorganisms
AU8438482A (en) * 1981-06-02 1982-12-09 Wakelin, R.R.F. Aerate sewage or fluids containing solids
US4468326A (en) * 1982-06-29 1984-08-28 Jorgen Jolner Process in microbiological purification and a device and materials therefor

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WO1987007886A1 (en) 1987-12-30
EP0280689A1 (en) 1988-09-07
NL8601602A (en) 1988-01-18
US4904420A (en) 1990-02-27

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