JP2001321647A - Air permeating agitation device - Google Patents

Air permeating agitation device

Info

Publication number
JP2001321647A
JP2001321647A JP2001034825A JP2001034825A JP2001321647A JP 2001321647 A JP2001321647 A JP 2001321647A JP 2001034825 A JP2001034825 A JP 2001034825A JP 2001034825 A JP2001034825 A JP 2001034825A JP 2001321647 A JP2001321647 A JP 2001321647A
Authority
JP
Japan
Prior art keywords
stirring
gas
boss
aeration
tube boss
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP2001034825A
Other languages
Japanese (ja)
Other versions
JP4596658B2 (en
Inventor
Shigeru Nishioka
茂 西岡
Koichi Kato
好一 加藤
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.)
Satake Chemical Equipment Mfg Ltd
Original Assignee
Satake Chemical Equipment Mfg Ltd
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 Satake Chemical Equipment Mfg Ltd filed Critical Satake Chemical Equipment Mfg Ltd
Priority to JP2001034825A priority Critical patent/JP4596658B2/en
Publication of JP2001321647A publication Critical patent/JP2001321647A/en
Application granted granted Critical
Publication of JP4596658B2 publication Critical patent/JP4596658B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Mixers Of The Rotary Stirring Type (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide an air permeating agitation device which is used for a flue gas desulfurizing apparatus, or the like, is excellent in dispersion of gas to an agitating liquid and high in gas absorbing efficiency and in which the accumulation of air bubbles is not generated on an agitation blade. SOLUTION: The boss part of the agitation blade 2 is formed into a cylindrical tube boss 4, which is fixed on a driving shaft 6 while interposing a supporting plate 5 to form a gap between the boss 4 and the shaft 6. A discharging port 7a of an air permeating tube 7 is formed to have such a structure that the shaft 6 can be inserted and is made open to the inside of the boss 4. An outflow port 4c of the boss 4 is made open to the downstream side of the blade 2 while keeping a sufficient distance.

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】本発明は主として排煙脱硫装
置等において、撹拌翼を備えた撹拌槽に燃焼排気ガス等
のガスを導入して該撹拌槽内にある液体との撹拌を行な
う通気撹拌用撹拌装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention mainly relates to a flue gas desulfurization apparatus and the like, in which a gas such as a combustion exhaust gas is introduced into a stirring tank provided with stirring blades to stir the liquid in the stirring tank. The present invention relates to a stirring device for use.

【0002】[0002]

【従来の技術】排煙脱硫装置として、排気ガス中に含ま
れる二酸化硫黄を液体中の吸収剤に吸収させて、石膏等
として取り除く方式のものがある。
2. Description of the Related Art As a flue gas desulfurization system, there is a system in which sulfur dioxide contained in exhaust gas is absorbed by an absorbent in a liquid and removed as gypsum or the like.

【0003】即ち、撹拌槽内にスラリー等を含んだ液体
を入れ、これに煙道ガス等のガスを導入して撹拌を行な
う通気撹拌方式のもので、この撹拌装置として、図6に
示す如く、液体を貯えた撹拌槽a内に側方から撹拌翼b
を突設し、該撹拌翼の負圧側にガスに連ながる通気管の
排出口cを配置した構造のものが従来一般に用いられて
いた。
That is, a liquid containing slurry or the like is put into a stirring tank, and a gas such as a flue gas is introduced into the stirring tank to stir the liquid. The stirring apparatus is as shown in FIG. , A stirring blade b from the side in a stirring tank a containing liquid.
Conventionally, a structure in which a discharge port c of a ventilation pipe connected to a gas is disposed on the negative pressure side of the stirring blade is provided.

【0004】しかしながらこの構造は、翼背面に図6の
dの如き気泡溜り(キャビティ)が発生して、撹拌槽a
内の液体のフローパターンが変化すると共に該撹拌槽a
内でのガスの分散が劣悪となり、ガス吸収効率が低下す
るという問題があった。
However, in this structure, a bubble reservoir (cavity) as shown in FIG.
The flow pattern of the liquid in the vessel changes and the stirring tank a
There is a problem that the dispersion of the gas in the inside becomes poor and the gas absorption efficiency decreases.

【0005】このため図7に示す如く、撹拌翼bの圧力
側(吐出側)に通気管の排出口cを配置して、翼に絡み
つく気泡溜りを排除するようにした撹拌装置が知られて
いる。
For this reason, as shown in FIG. 7, there is known a stirrer in which a discharge port c of a ventilation pipe is arranged on the pressure side (discharge side) of a stirring blade b so as to eliminate a bubble pool entangled with the blade. I have.

【0006】尚、矢印Xは撹拌翼bの吐出流の方向を示
す。
The arrow X indicates the direction of the discharge flow of the stirring blade b.

【0007】[0007]

【発明が解決しようとする課題】しかしながら前記撹拌
翼bの圧力側にガスの排出口cを配置する方法(図7)
は、液体中へのガス分散が撹拌翼bからの吐出流のみに
よって行なわれるため、良好なガス分散が得られず、且
つ、全体のフローパターンも通気による影響を受けて変
化するので、ガス吸収効率の悪いものとなる問題があっ
た。
However, a method of arranging a gas outlet c on the pressure side of the stirring blade b (FIG. 7).
Since gas dispersion in the liquid is performed only by the discharge flow from the stirring blade b, good gas dispersion cannot be obtained, and the entire flow pattern changes under the influence of the ventilation, so that the gas absorption There was a problem that was inefficient.

【0008】本発明はこれらの問題点を解消し、良好な
ガス分散が得られると共に高いガス吸収効率が得られる
通気撹拌用撹拌装置を提供することを目的とする。
An object of the present invention is to solve these problems and to provide a stirrer for aeration and stirring that can obtain good gas dispersion and high gas absorption efficiency.

【0009】[0009]

【課題を解決するための手段】本発明は上記の目的を達
成すべく、撹拌翼のボス部を円筒状のチューブボスに形
成し、該チューブボスを駆動軸の先端部にその外周面に
おいて間隙を存して固定し、該チューブボスの先端開口
をガスの流出口に形成したことを特徴とする。
According to the present invention, in order to achieve the above object, a boss portion of a stirring blade is formed in a cylindrical tube boss, and the tube boss is provided at a distal end portion of a drive shaft on an outer peripheral surface thereof. The tube boss has a tip opening formed at a gas outlet.

【0010】[0010]

【発明の実施の形態】本発明の通気撹拌用撹拌装置の第
1の実施の形態を図1乃至図3により説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A first embodiment of a stirring apparatus for aeration and stirring according to the present invention will be described with reference to FIGS.

【0011】図1は本第1の実施の形態の撹拌装置1の
縦断面図であり、撹拌翼2の駆動軸6が撹拌槽3の側方
から内方へ向かって突設された通気管7の中心を挿通す
るように形成されている。
FIG. 1 is a longitudinal sectional view of a stirring apparatus 1 according to the first embodiment. A driving pipe 6 of a stirring blade 2 is provided with a ventilation pipe projecting from the side of the stirring tank 3 toward the inside. 7 is formed so as to pass through the center.

【0012】7aは該撹拌槽2の外側に設けられ該通気
管7に連通するガス室、7bは該ガス室7aに連通する
ガス導入管、7cは該ガス室7bにおいて撹拌槽2の側
壁に対向する側面を形成するフランジを示し、該フラン
ジ7cに前記駆動軸6を回動自在に嵌着した。
Reference numeral 7a denotes a gas chamber provided outside the stirring vessel 2 and communicates with the ventilation pipe 7, 7b designates a gas introduction pipe communicating with the gas chamber 7a, and 7c designates a gas chamber 7b provided on the side wall of the stirring vessel 2 in the gas chamber 7b. A flange forming opposing side surfaces is shown, and the drive shaft 6 is rotatably fitted to the flange 7c.

【0013】該撹拌翼2は高吐出型の軸流翼からなって
いる。
The stirring blade 2 is a high discharge type axial flow blade.

【0014】即ち撹拌翼2は、図2及び図3に示す如
く、複数のプロペラ翼2aを円筒状のチューブボス4の
外周に放射状に固定して有すると共に、該チューブボス
4の内周に、半径方向内方へ向かって複数の支持板5を
放射状に突設して有しており、これら支持板5を介して
駆動軸6に撹拌翼2が軸着固定されている。
That is, as shown in FIGS. 2 and 3, the stirring blade 2 has a plurality of propeller blades 2a fixed radially on the outer periphery of a cylindrical tube boss 4, and has an inner periphery of the tube boss 4. A plurality of support plates 5 are provided so as to project radially inward, and the stirring blade 2 is axially fixed to a drive shaft 6 via these support plates 5.

【0015】前記チューブボス4は円筒状の本体の一端
部の直径を根部側程大として末広ノズル状部4aを形成
しており、更に前記チューブボス4の内方に通気管7の
排出口7dを開口させて、該通気管7と前記チューブボ
ス4とが一部、2重円筒管構造4bを形成している。
The tube boss 4 forms a divergent nozzle-like portion 4a by increasing the diameter of one end of the cylindrical body toward the root, and further forms a discharge port 7d of a ventilation pipe 7 inside the tube boss 4. And the ventilation pipe 7 and the tube boss 4 partially form a double cylindrical pipe structure 4b.

【0016】又、前記チューブボス4は、先端部の流出
口4cを、外周部のプロペラ翼2aの後流側の充分離れ
た位置に突出させている。
The tube boss 4 has an outlet 4c at the distal end thereof protruding to a position sufficiently distant on the downstream side of the propeller blades 2a at the outer periphery.

【0017】尚、前記2重円筒管構造4bの部分の長さ
は、撹拌翼2を前後に移動させることによって長さの調
節を行なうことができる。
The length of the double cylindrical tube structure 4b can be adjusted by moving the stirring blade 2 back and forth.

【0018】又、前記支持板5は平板状で、これら支持
板5の間を通過するガスの分散・微細化を行なう整流羽
根として作用するように形成されている。
The support plate 5 has a flat plate shape and is formed so as to act as a rectifying blade for dispersing and miniaturizing the gas passing between the support plates 5.

【0019】前記通気管7は排気ガス等のガスを撹拌槽
3内へ導入するための管路で、通気管7の先端の前記排
出口7dの中心を前記駆動軸6が挿通している。
The vent pipe 7 is a conduit for introducing a gas such as exhaust gas into the stirring tank 3, and the drive shaft 6 passes through the center of the discharge port 7 d at the tip of the vent pipe 7.

【0020】次に本実施の形態の撹拌装置1の作動及び
効果について説明する。
Next, the operation and effect of the stirring device 1 of the present embodiment will be described.

【0021】撹拌装置1を用いて排煙脱硫を行なうとき
は、二酸化硫黄を含むガスを通気管7により撹拌装置1
に供給する。
When flue gas desulfurization is performed using the stirrer 1, a gas containing sulfur dioxide is passed through the stirrer 1 through the ventilation pipe 7.
To supply.

【0022】撹拌槽3内には、例えば水酸化カルシウム
や炭酸カルシウム等を吸収剤としてスラリー状に懸濁し
た液体8が貯えられており、撹拌翼2を回転駆動すると
槽内の液体8は矢印Xの方向の流れを生じて撹拌され
る。
The stirring tank 3 stores a liquid 8 suspended in a slurry state using, for example, calcium hydroxide, calcium carbonate or the like as an absorbent. A flow in the direction of X is created and agitated.

【0023】一方、通気管7からのガスは、図2の矢印
Aに示す如く、排出口7dからチューブボス4の中に放
出され、2重円筒管構造4bのエジェクター効果によっ
てチューブボス4の末広ノズル状部4aから矢印Bの方
向に液体を吸い込んで、これと混合しながら支持板5を
通過する。このとき支持板5は整流羽根として作用し、
液体と混合したガスの分散・微細化が促進される。
On the other hand, the gas from the ventilation pipe 7 is discharged into the tube boss 4 from the discharge port 7d as shown by the arrow A in FIG. 2, and the divergent portion of the tube boss 4 is formed by the ejector effect of the double cylindrical pipe structure 4b. The liquid is sucked from the nozzle portion 4a in the direction of arrow B, and passes through the support plate 5 while mixing with the liquid. At this time, the support plate 5 acts as a rectifying blade,
Dispersion and miniaturization of gas mixed with liquid are promoted.

【0024】このように液体と混合して気泡となったガ
スはチューブボス4の流出口4cから撹拌槽3内の撹拌
翼2の吐出側に送り出され、高吐出型のプロペラ翼2a
によって作られた槽内循環流に乗って良好なフローパタ
ーンが得られるので、気泡の微細化と分散効率の向上が
図れると共に液体内のスラリーや生成した石膏等の固体
の流動性が向上する。即ち、翼の吐出流とガスの吐出エ
ネルギーとの相乗作用により、槽内液体の流動が強化さ
れる。又、チューブボス4の流出口4cをプロペラ翼2
aから充分離れた位置に突出させたので、翼への気泡の
絡み付きが防止される。かくて本撹拌装置1は高いガス
吸収効率が得られる。
The gas mixed with the liquid to form bubbles is sent from the outlet 4c of the tube boss 4 to the discharge side of the stirring blade 2 in the stirring tank 3, and the high discharge type propeller blade 2a
A good flow pattern is obtained by riding on the circulating flow in the tank created by the method, so that the air bubbles can be made finer and the dispersion efficiency can be improved, and the fluidity of the slurry in the liquid and the solid such as the formed gypsum can be improved. That is, the flow of the liquid in the tank is enhanced by the synergistic effect of the discharge flow of the blade and the discharge energy of the gas. The outlet 4c of the tube boss 4 is connected to the propeller blade 2
Since the projection is made at a position sufficiently distant from “a”, entanglement of air bubbles with the wing is prevented. Thus, the present stirring device 1 can obtain high gas absorption efficiency.

【0025】尚、通気管7とチューブボス4とで形成す
る2重円筒管構造4bの部分の長さを調節して、前記エ
ジェクター効果が最良となるように調節を行なうことが
できる。
The length of the double cylindrical pipe structure 4b formed by the ventilation pipe 7 and the tube boss 4 can be adjusted so that the ejector effect is optimized.

【0026】又、本実施の形態では撹拌翼2を軸流翼と
したが、これは斜流翼であってもよい。
In the present embodiment, the stirring blade 2 is an axial flow blade, but this may be an oblique flow blade.

【0027】本発明の通気撹拌用撹拌装置の第2の実施
の形態を図4により説明する。
A second embodiment of the agitating apparatus for aeration and agitation of the present invention will be described with reference to FIG.

【0028】本実施の形態の撹拌装置11もガスの通気
管17内を挿通する駆動軸16の先端部に撹拌翼12が
形成されている。
The stirring device 11 of the present embodiment also has a stirring blade 12 formed at the tip of a drive shaft 16 that passes through a gas ventilation pipe 17.

【0029】即ち撹拌翼12は、複数のプロペラ翼12
aを備えたチューブボス14が、複数の支持板15を介
して駆動軸16の先端部の外周に固定されている。
That is, the stirring blade 12 includes a plurality of propeller blades 12.
The tube boss 14 provided with a is fixed to the outer periphery of the distal end of the drive shaft 16 via a plurality of support plates 15.

【0030】該チューブボス14は円筒状で、前記通気
管17と略同じ直径に形成されており、該チューブボス
14の後端面14aと前記通気管17の先端面17aと
は所定の間隔を存して対向するか又は回動自在に摺接す
るように配置されている。
The tube boss 14 has a cylindrical shape and is formed to have substantially the same diameter as the ventilation pipe 17, and the rear end face 14 a of the tube boss 14 and the front end face 17 a of the ventilation pipe 17 have a predetermined space. Are arranged so as to face each other or to be in sliding contact with each other in a freely rotatable manner.

【0031】前記チューブボス14の先端部には、軸方
向の斜外方へ向かって複数の噴出管14bが突設されて
いる。
At the tip of the tube boss 14, a plurality of ejection pipes 14b are provided to project obliquely outward in the axial direction.

【0032】これら噴出管14bは先細に形成され、そ
の先端部は駆動軸16と平行の軸方向へ向けて先を曲げ
た形状とし、前記プロペラ翼12aの後流側に互いに間
隔を存して開口している。
Each of the jet pipes 14b is formed to have a tapered shape, and the tip of the jet pipe 14b is bent in an axial direction parallel to the drive shaft 16 so as to be spaced from each other on the downstream side of the propeller blade 12a. It is open.

【0033】又、前記通気管17の前端面17aの外周
部と前記チューブボス14の後端面14aの外周部とを
覆う筒状のカバー17bがあって、チューブボス14の
内部に外から液体が侵入するのを防止している。尚、矢
印Xは撹拌翼12の吐出流の方向を示す。
Further, there is a cylindrical cover 17b which covers the outer peripheral portion of the front end face 17a of the ventilation pipe 17 and the outer peripheral portion of the rear end face 14a of the tube boss 14. Liquid from inside is inside the tube boss 14. Prevents intrusion. The arrow X indicates the direction of the discharge flow of the stirring blade 12.

【0034】次に本実施の形態の撹拌装置11の作動及
び効果について説明する。
Next, the operation and effects of the stirring device 11 of the present embodiment will be described.

【0035】ガス導入管17cから送られてきたガスは
通気管17内を通って回転するチューブボス14内に送
られ、複数の噴出管14bから撹拌層13内の液体内へ
噴出される。
The gas sent from the gas introduction pipe 17c is sent into the rotating tube boss 14 through the ventilation pipe 17, and is ejected from a plurality of ejection pipes 14b into the liquid in the stirring layer 13.

【0036】これら噴出管14bは、撹拌翼12を形成
するプロペラ翼12aとは充分な間隔を存して設けられ
ているため、翼への気泡の絡み付きが防止されると共
に、複数の噴出管14bによってガスが撹拌槽13内の
広範囲に渡って放出されるので、槽内液体とガスとの混
合、拡散に好都合となり、ガス吸収効率が向上する。
The jet pipes 14b are provided at a sufficient distance from the propeller blades 12a forming the stirring blades 12, so that air bubbles are not entangled with the impellers, and a plurality of jet pipes 14b are provided. As a result, the gas is discharged over a wide area in the stirring tank 13, so that the mixing and diffusion of the liquid and the gas in the tank are convenient, and the gas absorption efficiency is improved.

【0037】本発明の通気撹拌用撹拌装置の第3の実施
の形態を図5により説明する。
A third embodiment of the agitating device for aeration and agitation of the present invention will be described with reference to FIG.

【0038】本実施の形態の撹拌装置21は、複数のプ
ロペラ翼22aを備えたチューブボス24を、複数の支
持板25を介して駆動軸26の先端部の外周に固定して
撹拌翼22を形成すると共に、該駆動軸26を中空の筒
状に形成して、その内部にガス通路26aを設けた。
In the stirring device 21 of the present embodiment, a tube boss 24 having a plurality of propeller blades 22a is fixed to the outer periphery of the tip end of a drive shaft 26 via a plurality of support plates 25, and the stirring blade 22 is At the same time, the drive shaft 26 was formed in a hollow cylindrical shape, and a gas passage 26a was provided therein.

【0039】又、前記駆動軸26は、その先端の排出口
26bを前記チューブボス24内に開口させた。
The drive shaft 26 has a discharge port 26 b at the end thereof opened into the tube boss 24.

【0040】前記チューブボス24は、後端部24aの
直径を大として漏斗状に形成すると共に、先端部の流出
口24bを前記プロペラ翼22aの取付け位置の後流側
の充分離れた位置に突出させた。
The tube boss 24 is formed in a funnel shape with the diameter of the rear end portion 24a being large, and the outlet port 24b at the front end portion is protruded to a position sufficiently distant on the wake side of the mounting position of the propeller blade 22a. I let it.

【0041】前記駆動軸26には、ガス導入管27bか
らのガスをガス室27a内において駆動軸26内のガス
通路26aに導入するための導入孔26cが設けられて
いる。
The drive shaft 26 is provided with an introduction hole 26c for introducing gas from the gas introduction pipe 27b into the gas passage 26a in the drive shaft 26 in the gas chamber 27a.

【0042】次に本実施の形態の撹拌装置21の作動及
び効果について説明する。
Next, the operation and effects of the stirring device 21 of the present embodiment will be described.

【0043】ガス導入口27bから送られてきたガス
は、導入孔26cより駆動軸26内のガス通路26aに
導入され、排出口26bからチューブボス24内へ放出
される。
The gas sent from the gas inlet 27b is introduced into the gas passage 26a in the drive shaft 26 through the inlet 26c, and is discharged from the outlet 26b into the tube boss 24.

【0044】チューブボス24は、前記排出口26bか
ら放出されるガスによるエジェクター効果により、漏斗
状の後端部24aより液体を吸い込み、これら液体とガ
スの気泡の混合物を先端部の流出口24bより撹拌槽2
3内に放出する。
The tube boss 24 sucks liquid from the funnel-shaped rear end 24a by the ejector effect of the gas discharged from the discharge port 26b, and discharges a mixture of these liquid and gas bubbles from the outlet 24b at the front end. Stirring tank 2
Release into 3.

【0045】前記流出口24bは、前記プロペラ翼22
aから充分離れた位置に開口しているため、翼への気泡
の絡み付きがなく、更に前記プロペラ翼22aによって
作られた槽内循環流に乗って良好なフローパターンが得
られるので、ガス吸収効率の良い通気撹拌用撹拌装置と
することができる。
The outlet 24b is connected to the propeller blade 22
a, the air bubbles are not entangled with the blades, and a good flow pattern can be obtained by riding on the circulation flow in the tank formed by the propeller blades 22a. A good stirring device for aeration and stirring can be obtained.

【0046】尚、前記第1の実施の形態における支持板
5、前記第2の実施の形態における支持板15及び前記
第3の実施の形態における支持板25は、整流羽根とし
て作動するように形成したが、これらは軸流ポンプのバ
ケットとして作動するように形成してもよい。
The support plate 5 in the first embodiment, the support plate 15 in the second embodiment, and the support plate 25 in the third embodiment are formed so as to operate as rectifying blades. However, they may be formed to operate as buckets for axial pumps.

【0047】又、プロペラ翼2a、12a、22aの根
部をチューブボス4、14、24を貫通固定してその根
部端を駆動軸6、16、26の外周面に固定し、前記支
持板5、15、25に形成してもよい。
The roots of the propeller blades 2a, 12a, 22a are fixed through the tube bosses 4, 14, 24, and the ends of the roots are fixed to the outer peripheral surfaces of the drive shafts 6, 16, 26. 15 and 25 may be formed.

【0048】[0048]

【発明の効果】このように本発明によれば、ガスは撹拌
翼の中心部のチューブボスを通って撹拌翼の吐出側に送
り出されるので、翼に絡みつく気泡溜りを生じないと共
にガスの液体中への良好なガス分散が得られ、ガス吸収
効率の高い通気撹拌用撹拌装置が得られる効果を有す
る。
As described above, according to the present invention, the gas is sent out to the discharge side of the stirring blade through the tube boss at the center of the stirring blade, so that no air bubbles are entangled with the blade and the gas in the liquid This has the effect of obtaining a good gas dispersion in the gas and providing a stirrer for aeration and stirring with high gas absorption efficiency.

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

【図1】第1の実施の形態の撹拌装置の縦断面図であ
る。
FIG. 1 is a longitudinal sectional view of a stirring device according to a first embodiment.

【図2】前記撹拌装置の一部縦断面図である。FIG. 2 is a partial vertical sectional view of the stirring device.

【図3】図2におけるIII−III線截断面図である。FIG. 3 is a sectional view taken along line III-III in FIG. 2;

【図4】第2の実施の形態の撹拌装置の縦断面図であ
る。
FIG. 4 is a longitudinal sectional view of a stirring device according to a second embodiment.

【図5】第3の実施の形態の撹拌装置の縦断面図であ
る。
FIG. 5 is a longitudinal sectional view of a stirring device according to a third embodiment.

【図6】従来の通気撹拌用撹拌装置の一例の説明図であ
る。
FIG. 6 is an explanatory view of an example of a conventional stirring device for aeration and stirring.

【図7】従来の通気撹拌用撹拌装置の他の例の説明図で
ある。
FIG. 7 is an explanatory view of another example of a conventional stirring device for aeration and stirring.

【符号の説明】[Explanation of symbols]

1、11、21 撹拌装置 2、12、22 撹拌翼 3、13、23 撹拌槽 4、14、24 チューブボス 4c、24b 流出口 5、15、25 支持板(整流羽根) 6、16、26 駆動軸 7、17 通気管 14b 噴出管 1, 11, 21 Stirring device 2, 12, 22 Stirring blade 3, 13, 23 Stirring tank 4, 14, 24 Tube boss 4c, 24b Outlet 5, 15, 25 Support plate (rectifying blade) 6, 16, 26 Drive Axis 7, 17 Vent pipe 14b Spout pipe

Claims (9)

【特許請求の範囲】[Claims] 【請求項1】 撹拌翼のボス部を円筒状のチューブボス
に形成し、該チューブボスを駆動軸の先端部にその外周
面において間隙を存して固定し、該チューブボスの先端
開口をガスの流出口に形成したことを特徴とする通気撹
拌用撹拌装置。
1. A boss portion of a stirring blade is formed in a cylindrical tube boss, and the tube boss is fixed to a distal end portion of a drive shaft with a gap on an outer peripheral surface thereof. A stirrer for aeration and stirring, which is formed at the outflow port.
【請求項2】 前記駆動軸を内方に挿通したガスの通気
管を設け、該通気管の先端開口を前記チューブボス内に
臨ませたことを特徴とする請求項1に記載の通気撹拌用
撹拌装置。
2. A ventilation stirrer according to claim 1, wherein a gas vent pipe is provided in which the drive shaft is inserted inward, and a distal end opening of the vent pipe faces the tube boss. Stirrer.
【請求項3】 前記通気管と前記チューブボスとが一
部、2重円筒管構造を形成していることを特徴とする請
求項2に記載の通気撹拌用撹拌装置。
3. The agitating apparatus for aeration and agitation according to claim 2, wherein the ventilation pipe and the tube boss partially form a double cylindrical pipe structure.
【請求項4】 前記駆動軸を内方に挿通したガスの通気
管を設け、該通気管の先端面と前記チューブボスの後端
面を対向すると共に、該チューブボスの先端部に複数の
噴出管を連設し、該噴出管は斜外方に延設してその先端
開口を前記撹拌翼により形成される流れ方向に臨ませた
ことを特徴とする請求項1に記載の通気撹拌用撹拌装
置。
4. A gas vent pipe having the drive shaft inserted inward is provided, and a front end face of the gas pipe and a rear end face of the tube boss are opposed to each other, and a plurality of ejection pipes are provided at the front end of the tube boss. The stirrer for ventilation stirring according to claim 1, wherein the jet pipe extends obliquely outward so that its tip opening faces the flow direction formed by the stirring blades. .
【請求項5】 前記駆動軸を中空の筒状に形成してその
内部をガス通路に形成すると共に該ガス通路の先端開口
を前記チューブボス内に臨ませたことを特徴とする請求
項1に記載の通気撹拌用撹拌装置。
5. The apparatus according to claim 1, wherein the drive shaft is formed in a hollow cylindrical shape, the inside of the drive shaft is formed as a gas passage, and a distal end opening of the gas passage faces the inside of the tube boss. The stirring device for aeration stirring according to the above.
【請求項6】 前記チューブボスは、その直径を根部側
程大として、末広ノズル状に形成したことを特徴とする
請求項2又は請求項3又は請求項5に記載の通気撹拌用
撹拌装置。
6. The agitating apparatus for aeration and agitation according to claim 2, wherein the tube boss is formed in a shape of a divergent nozzle with a diameter increasing toward the root.
【請求項7】 前記チューブボスを前記駆動軸に固定す
る支持板をこれら支持板間を通過するガスの分散・微細
化を行なう整流羽根に形成したことを特徴とする請求項
1乃至請求項6のいずれか1に記載の通気撹拌用撹拌装
置。
7. A rectifying vane for dispersing and miniaturizing a gas passing between said support plates, said support plate fixing said tube boss to said drive shaft. The stirrer for aeration stirring according to any one of the above.
【請求項8】 前記2重円筒管構造部分の長さを調節可
能に形成したことを特徴とする請求項3に記載の通気撹
拌用撹拌装置。
8. The agitating device for aeration and agitation according to claim 3, wherein the length of the double cylindrical tube structure is adjustable.
【請求項9】 前記撹拌翼は高吐出型の軸流翼からなる
ことを特徴とする請求項1乃至請求項8のいずれか1に
記載の通気撹拌用撹拌装置。
9. The agitating device for aeration and agitation according to claim 1, wherein the stirring blade is a high discharge type axial flow blade.
JP2001034825A 2000-03-10 2001-02-13 Stirrer for aeration stirring Expired - Fee Related JP4596658B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001034825A JP4596658B2 (en) 2000-03-10 2001-02-13 Stirrer for aeration stirring

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP2000066790 2000-03-10
JP2000-66790 2000-03-10
JP2001034825A JP4596658B2 (en) 2000-03-10 2001-02-13 Stirrer for aeration stirring

Publications (2)

Publication Number Publication Date
JP2001321647A true JP2001321647A (en) 2001-11-20
JP4596658B2 JP4596658B2 (en) 2010-12-08

Family

ID=26587197

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001034825A Expired - Fee Related JP4596658B2 (en) 2000-03-10 2001-02-13 Stirrer for aeration stirring

Country Status (1)

Country Link
JP (1) JP4596658B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101500494B1 (en) * 2013-05-24 2015-03-09 주식회사 포스코 Air chamber for holding pole of stirrer equipped with function of air bubble
JP5918881B1 (en) * 2015-04-24 2016-05-18 光洋サーモシステム株式会社 Stirring fan for heat treatment apparatus and heat treatment apparatus provided with the same
JP2016205377A (en) * 2016-04-07 2016-12-08 光洋サーモシステム株式会社 Stirring fan for heat treatment apparatus, and heat treatment apparatus including the same
CN110663313A (en) * 2019-10-30 2020-01-10 麻阳蓝凤凰农业发展有限公司 Disinfection device before konjaku is planted

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06198151A (en) * 1992-10-16 1994-07-19 Outokumpu Mintec Oy Method and device for dispersing gas in liquid or slurry
JPH07508211A (en) * 1992-06-30 1995-09-14 シユンドス・デフイブラトール・インダストリーズ・アクテイエボラーグ Equipment for mixing processing agents into pulp suspension
JPH09220435A (en) * 1996-02-16 1997-08-26 Ishikawajima Harima Heavy Ind Co Ltd Absorber for exhaust gas desulfurizer
JP2001000851A (en) * 1999-05-27 2001-01-09 Ekato Ruhr & Mischtechnik Gmbh Agitator

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07508211A (en) * 1992-06-30 1995-09-14 シユンドス・デフイブラトール・インダストリーズ・アクテイエボラーグ Equipment for mixing processing agents into pulp suspension
JPH06198151A (en) * 1992-10-16 1994-07-19 Outokumpu Mintec Oy Method and device for dispersing gas in liquid or slurry
JPH09220435A (en) * 1996-02-16 1997-08-26 Ishikawajima Harima Heavy Ind Co Ltd Absorber for exhaust gas desulfurizer
JP2001000851A (en) * 1999-05-27 2001-01-09 Ekato Ruhr & Mischtechnik Gmbh Agitator

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101500494B1 (en) * 2013-05-24 2015-03-09 주식회사 포스코 Air chamber for holding pole of stirrer equipped with function of air bubble
JP5918881B1 (en) * 2015-04-24 2016-05-18 光洋サーモシステム株式会社 Stirring fan for heat treatment apparatus and heat treatment apparatus provided with the same
CN106065864A (en) * 2015-04-24 2016-11-02 光洋热系统股份有限公司 The agitation fan of annealing device and the annealing device with this agitation fan
US10365043B2 (en) 2015-04-24 2019-07-30 Koyo Thermo Systems Co., Ltd. Stirring fan for heat treatment apparatus, and heat treatment apparatus including the same
JP2016205377A (en) * 2016-04-07 2016-12-08 光洋サーモシステム株式会社 Stirring fan for heat treatment apparatus, and heat treatment apparatus including the same
CN110663313A (en) * 2019-10-30 2020-01-10 麻阳蓝凤凰农业发展有限公司 Disinfection device before konjaku is planted

Also Published As

Publication number Publication date
JP4596658B2 (en) 2010-12-08

Similar Documents

Publication Publication Date Title
WO2019037470A1 (en) Microbubble generator
JP2002210326A (en) Wet flue gas desulfurization apparatus and wet desulfurization method
CN207892687U (en) A kind of cartridge type urea mixer
WO2024198137A1 (en) Impeller assembly and pulping apparatus
EP0338967B1 (en) Apparatus for treating slurry by gas-liquid contact method
JP2004024931A (en) Gas-liquid mixing apparatus for generating fine bubble in large quantity
JP2001321647A (en) Air permeating agitation device
JP3340396B2 (en) Gas-liquid mixing device
JP2000271590A (en) Aeration device
JP2008068161A (en) Wet fuel gas desulfurizer
JP3968737B2 (en) Aeration equipment
JP5651829B2 (en) Friction reduction ship and micro bubble generation pump
JP2706322B2 (en) Gas-liquid contact device
JP3447838B2 (en) Underwater stirring aeration equipment
JP2000084382A (en) Air diffusion and stirring device
JP2000107792A (en) Air diffusion-agitation apparatus
JPS59105825A (en) Liquid mixing apparatus
CN208218516U (en) A kind of rotational flow aeration device
JPH10216794A (en) Water area purifying device
JP2000093772A (en) Micro-gas bubble liquid gas mixing and dissolving device
KR950007281Y1 (en) Aerator for water treatment
JPH03229696A (en) Air bubble generator
JPH06285488A (en) Underwater agitation and aeration device
JP3951287B2 (en) Underwater aeration stirrer
JP3414651B2 (en) Underwater mechanical stirring and aeration equipment

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20080205

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20100520

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20100701

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20100806

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20100831

A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20100921

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20131001

Year of fee payment: 3

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

S531 Written request for registration of change of domicile

Free format text: JAPANESE INTERMEDIATE CODE: R313531

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

LAPS Cancellation because of no payment of annual fees