JP2014226633A - Gas-liquid agitation blade - Google Patents

Gas-liquid agitation blade Download PDF

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JP2014226633A
JP2014226633A JP2013109923A JP2013109923A JP2014226633A JP 2014226633 A JP2014226633 A JP 2014226633A JP 2013109923 A JP2013109923 A JP 2013109923A JP 2013109923 A JP2013109923 A JP 2013109923A JP 2014226633 A JP2014226633 A JP 2014226633A
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gas
blade
liquid
wing
stirring blade
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JP6159577B2 (en
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好一 加藤
Koichi Kato
好一 加藤
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Satake Chemical Equipment Mfg Ltd
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Satake Chemical Equipment Mfg Ltd
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Abstract

PROBLEM TO BE SOLVED: To provide a gas-liquid agitation blade capable of acquiring a satisfactory gas absorption performance, i.e., an excellent gas-liquid performance, and capable of being easily applied even to agitation vessels of different depths and sizes.SOLUTION: Blade body parts 2A and 2B which are formed in such a way that a clearance is formed between the confronting faces of a pair of upper and lower blades 2a and 2b and the clearance becomes narrower in the rotational direction of the blades, are attached radially at a plurality of vertical stages to a revolving shaft 3. The blade body parts 2A and 2B of the upper and lower steps are attached at rotational angles different from each other to the revolving shaft 3, and are attached at continuous portions without any axial clearance to the revolving shaft 3.

Description

本発明は、食品工業や化学工業等において、気液の撹拌混合に使用する撹拌翼に関する。   The present invention relates to a stirring blade used for stirring and mixing gas and liquid in the food industry, the chemical industry, and the like.

一般の気液の撹拌混合の方法は、撹拌槽内に液体とガスを供給し、撹拌翼を該撹拌槽内において回転させてガス気泡の粒径を小さくすると共に液体中へ該ガス気泡を分散させ、該液体中の分散ガス気泡の留保分の増加即ちガス吸収効率の増加を図るものである。   A general method of gas-liquid stirring and mixing is to supply liquid and gas into a stirring tank, rotate the stirring blade in the stirring tank to reduce the size of gas bubbles, and disperse the gas bubbles into the liquid. Thus, the retained fraction of dispersed gas bubbles in the liquid is increased, that is, the gas absorption efficiency is increased.

この種の従来の撹拌翼として、図8に示す如く、上下一対の翼bを回転軸cの周りに放射状に配置し、これら一対の翼bの対向面の間に間隙を形成すると共に該間隙を翼bの回転方向Aに向かって狭くなるように形成し、撹拌槽内に液体とガスとを供給しながら、撹拌翼aを回転駆動すると上下一対の翼bの上下間隔が後流側程に大となり、かくて、上下一対の翼b間に高速で流入した流体は翼b内を後流側へ行く程速度が低下すると共に圧力が上昇し、これら上下の翼bの背面に発生しがちな負圧の形成を抑制して気泡だまりの発生を防止し、ガスの吸収性能、即ち気液性能を向上するようにしたものが知られている(特許文献1参照)。   As a conventional stirring blade of this type, as shown in FIG. 8, a pair of upper and lower blades b are arranged radially around a rotation axis c, and a gap is formed between the opposed surfaces of the pair of blades b. When the stirring blade a is rotationally driven while supplying liquid and gas into the stirring tank, the vertical distance between the pair of upper and lower blades b is increased toward the wake side. Thus, the fluid that flows in at a high speed between the pair of upper and lower blades b decreases in speed and increases in pressure as it moves backward in the blade b, and is generated on the back surfaces of these upper and lower blades b. It is known to prevent the formation of bubble accumulation by suppressing the formation of negative pressure, which tends to improve gas absorption performance, that is, gas-liquid performance (see Patent Document 1).

特許第3919262号公報Japanese Patent No. 3919262

この従来の撹拌翼aによれば、気液性能を更に向上させるために、上下一対の翼bを回転軸cの周りに放射状に更に多く配置する必要があるが、回転軸cのボスに対して、翼羽数が増えると物理的に取り付けが不可能になる。即ち、該ボスに、例えば、8枚、12枚の翼を、取り付けたくても、溶接ができず、取りつけることができない。又、多くの翼を設けると前後の翼の干渉により吐出効率が低下して逆に気液性能も低下する問題点があった。   According to this conventional agitating blade a, in order to further improve the gas-liquid performance, it is necessary to dispose more pairs of upper and lower blades b radially around the rotating shaft c. As the number of wings increases, it becomes physically impossible to install. That is, even if 8 or 12 blades are attached to the boss, for example, welding cannot be performed and attachment is not possible. Further, when many blades are provided, there is a problem that the discharge efficiency is lowered due to the interference between the front and rear blades, and the gas-liquid performance is also lowered.

本発明はこのような問題点を解消し、良好な気液性能が得られる気液用撹拌翼を提供することを目的とする。   An object of the present invention is to provide a gas-liquid agitating blade capable of solving such problems and obtaining good gas-liquid performance.

本発明はこの目的を達成すべく、上下一対の翼の対向面の間に間隙を形成すると共に該間隙を翼の回転方向に向かって狭くなるように形成し又は該間隙を翼の回転方向に向かって広くなるように形成した翼体部を、回転軸に放射状に上下複数段に取り付けたことを特徴とする。   In order to achieve this object, the present invention forms a gap between the opposed surfaces of a pair of upper and lower wings and forms the gap so as to narrow toward the rotation direction of the wings. The wing body portion formed so as to become wider toward the top is attached to a rotating shaft in a plurality of upper and lower stages radially.

本発明によれば、良好なガスの吸収性能、即ち、良好な気液性能が得られ、更に、槽の深さや大きさの異なる撹拌槽に対しても容易に適用可能な気液用撹拌翼を提供できる効果を有する。   According to the present invention, good gas absorption performance, that is, good gas-liquid performance is obtained, and furthermore, a gas-liquid stirring blade that can be easily applied to stirring tanks having different tank depths and sizes. The effect that can be provided.

本発明の実施例1の気液用撹拌翼の斜視図である。It is a perspective view of the stirring blade for gas-liquid of Example 1 of this invention. 該撹拌翼の正面図である。It is a front view of this stirring blade. 該撹拌翼の平面図である。It is a top view of this stirring blade. 翼体部の断面図である。It is sectional drawing of a wing body part. 本発明の実施例2の気液用撹拌翼の斜視図である。It is a perspective view of the stirring blade for gas-liquid of Example 2 of this invention. 該撹拌翼の正面図である。It is a front view of this stirring blade. 該撹拌翼の平面図である。It is a top view of this stirring blade. 従来の気液用撹拌翼の斜視図である。It is a perspective view of the conventional gas-liquid stirring blade.

本発明を実施するための形態の実施例を以下に示す。   The example of the form for carrying out the present invention is shown below.

本発明の実施例1を図1乃至図4により説明する。   A first embodiment of the present invention will be described with reference to FIGS.

図1は本発明の実施例1の気液用撹拌翼の斜視図、図2は該撹拌翼の正面図、図3は該撹拌翼の平面図、図4は翼体部の断面図である。   1 is a perspective view of a gas-liquid stirring blade according to a first embodiment of the present invention, FIG. 2 is a front view of the stirring blade, FIG. 3 is a plan view of the stirring blade, and FIG. 4 is a sectional view of a blade body. .

1は本実施例の気液用撹拌翼、2A、2Bは該気液用撹拌翼1の複数の翼体部を示し、これら各翼体部2A、2Bは上側翼2a及び下側翼2bとの上下一対の翼からなり、回転軸3のハブ部3aの周りに90度間隔に放射状に上方段と下方段に固着されている。そして、図4に示す如く各翼体部2A、2Bの上側翼2aと下側翼2bの回転方向の先端部間に間隔dを形成すると共に、これら上側翼2aと下側翼2bの対向面の間隔は、回転方向Aに向かって狭くなるように形成した。   Reference numeral 1 denotes a gas-liquid stirring blade of this embodiment, 2A and 2B denote a plurality of blade bodies of the gas-liquid stirring blade 1, and these blade bodies 2A and 2B are respectively connected to the upper blade 2a and the lower blade 2b. It consists of a pair of upper and lower wings, and is fixed to the upper and lower stages radially around the hub portion 3a of the rotating shaft 3 at intervals of 90 degrees. Then, as shown in FIG. 4, a distance d is formed between the tip portions in the rotational direction of the upper wing 2a and the lower wing 2b of each wing body 2A, 2B, and the distance between the facing surfaces of the upper wing 2a and the lower wing 2b. Was formed so as to become narrower in the rotation direction A.

又、これら上側翼2aと下側翼2bは平板翼で、上下対称に形成されている。   The upper wing 2a and the lower wing 2b are flat wings, and are formed vertically symmetrical.

そして、上方段の各翼体部2Aと下方段の各翼体部2Bは、それぞれ上下の段で回転方向において相互に45度の角度差をもって前記ハブ部3aの周りに固定されており、更に、前記上方段の翼体部2Aと下方段の翼体部2Bは、回転軸3の軸方向において、前記ハブ部3aに間隙を存することなく連続した個所に固定されている。   Each upper wing body portion 2A and each lower wing body portion 2B are fixed around the hub portion 3a with an angular difference of 45 degrees in the rotational direction between the upper and lower tiers. The upper stage wing body part 2A and the lower stage wing body part 2B are fixed to the hub 3a in a continuous position without any gap in the axial direction of the rotary shaft 3.

次に本実施例1の気液用撹拌翼1の作用と効果を説明する。   Next, the operation and effect of the gas-liquid stirring blade 1 of the first embodiment will be described.

撹拌槽(図示せず)内に気液用撹拌翼1を垂設し、該撹拌槽内に液体とガスとを供給しながら、該気液用撹拌翼1を矢印Aの方向に回転駆動する。   A gas-liquid stirring blade 1 is suspended in a stirring tank (not shown), and the gas-liquid stirring blade 1 is rotationally driven in the direction of arrow A while supplying liquid and gas into the stirring tank. .

上方段の翼体部2A及び下方段の翼体部2Bのそれぞれにおいて、上側翼2a及び下側翼2bとからなる上下一対の翼の対向面の間隔が回転方向Aに向かって狭くなるように形成されているので、回転軸3の回転駆動により、前記間隙dから上側翼2aと下側翼2bの間に高速で流入した流体は翼内を後流側へ行く程に速度が低下すると共に圧力が上昇して吐出し、これら上側翼2a又は下側翼2bの背面に発生し勝ちな負圧の形成を抑制し、かくて、ガス気泡の粒径が小さくなると共に、液体中へ該ガス気泡が分散される。   In each of the upper wing body portion 2A and the lower wing body portion 2B, the distance between the opposing surfaces of the pair of upper and lower wings composed of the upper wing 2a and the lower wing 2b is formed so as to narrow toward the rotation direction A. As a result of the rotational drive of the rotary shaft 3, the fluid flowing at a high speed from the gap d between the upper wing 2a and the lower wing 2b decreases in speed and goes to the wake side in the wing, and the pressure is increased. Ascending and discharging, suppressing the formation of negative pressure that tends to occur on the back surface of the upper wing 2a or the lower wing 2b, thus reducing the particle size of the gas bubbles and dispersing the gas bubbles into the liquid Is done.

そして、本実施例1においては、上方段の翼体部2A及び下方段の翼体部2Bが回転角度方向において異なる位置に取り付けられているので、上方段の翼体部2A及び下方段の翼体部2Bがそれぞれ独立の吐出場として液体を吐出し、液体中へのガス気泡を分散させる撹拌作用を行う。又、上方段の翼体部2Aと下方段の翼体部2Bが前記ハブ部3aにおいて連続した上下個所に固定されているので、前述の上方段の翼体部2A及び下方段の翼体部2Bの独立の吐出流が共通の流域における集中的な撹拌作用となる。   In the first embodiment, the upper stage wing body part 2A and the lower stage wing body part 2B are attached at different positions in the rotational angle direction, so the upper stage wing body part 2A and the lower stage wing body part 2B are attached. The body part 2B discharges the liquid as an independent discharge field, and performs a stirring action to disperse the gas bubbles in the liquid. Further, since the upper wing body portion 2A and the lower wing body portion 2B are fixed to the upper and lower portions which are continuous in the hub portion 3a, the upper wing body portion 2A and the lower wing body portion described above. The independent discharge flow of 2B becomes a concentrated stirring action in a common basin.

ところが、前記翼体部が全て同一の平面に設けられていると、それぞれの翼体部の吐出流が相互に影響しあって撹拌作用が低下し、又、上方段の翼体部及び下方段の翼体部が同一の回転角度位置の上下に在ると、これら上下の翼体部からのそれぞれの吐出流が同一の回転角度位置に生じて相互に影響しあって撹拌作用が低下する。更に、上方段の翼体部と下方段の翼体部が前記ハブ部3aにおいて間隔があいて分離した上下個所に固定されていると、前述の如き独立の吐出流の共通の流域における集中的な撹拌作用が得られず、又、回転軸3の回転駆動のための動力が大となり効率上好ましくない。   However, if all of the wing bodies are provided on the same plane, the discharge flow of the wing bodies will affect each other and the stirring action will be reduced, and the upper and lower wing bodies will be lowered. If the wing body portions are above and below the same rotation angle position, the respective discharge flows from the upper and lower wing body portions are generated at the same rotation angle position and affect each other, thereby reducing the stirring action. Further, if the upper and lower wing parts are fixed to the upper and lower parts separated at a distance in the hub part 3a, the above-mentioned independent discharge flow is concentrated in the common basin. In this case, an agitation effect cannot be obtained, and the power for rotationally driving the rotary shaft 3 becomes large, which is not preferable in terms of efficiency.

本発明の実施例2を図5及び図7により説明する。   A second embodiment of the present invention will be described with reference to FIGS.

図5は本発明の実施例2の気液用撹拌翼の斜視図、図6は該撹拌翼の正面図、図7は該撹拌翼の平面図である。   5 is a perspective view of a gas-liquid stirring blade of Example 2 of the present invention, FIG. 6 is a front view of the stirring blade, and FIG. 7 is a plan view of the stirring blade.

本実施例2においては、前記実施例1の気液用撹拌翼1における上方段の翼体部2Aと下方段の翼体部2Bの2段に構成されているのと異なり、気液用撹拌翼1Aが上方段の翼体部2Cと中間段の翼体部2Dと下方段の翼体部2Eの3段に構成されており、上方段の翼体部2Cと中間段の翼体部2Dとはそれぞれ相互に回転方向で30度の角度差をもって前記ハブ部3aの周りに固定されており、又、中間段の翼体部2Dと下方段の翼体部2Eともそれぞれ相互に回転方向で30度の角度差をもって前記ハブ部3aの周りに固定されており、更に、前記上方段の翼体部2Cと中間段の翼体部2Dと下方段の翼体部2Eは、回転軸3の軸方向において、前記ハブ部3aに間隙を存することなく連続した個所に固定されている。   In the second embodiment, unlike the gas-liquid stirring blade 1 of the first embodiment, which is composed of the upper blade body portion 2A and the lower blade body portion 2B, the gas-liquid stirring blade is used. The wing 1A is composed of three stages of an upper wing body part 2C, an intermediate wing body part 2D, and a lower wing body part 2E, and an upper wing body part 2C and an intermediate wing body part 2D. Are fixed around the hub portion 3a with an angular difference of 30 degrees relative to each other in the rotational direction, and the intermediate wing body portion 2D and the lower wing body portion 2E are also mutually in the rotational direction. The upper wing body 2C, the intermediate wing body 2D, and the lower wing body 2E are fixed around the hub 3a with an angle difference of 30 degrees. In the axial direction, the hub portion 3a is fixed to a continuous portion without a gap.

次に本実施例2の気液用撹拌翼1Aの作用と効果を説明する。   Next, the action and effect of the gas-liquid stirring blade 1A of the second embodiment will be described.

撹拌槽(図示せず)内に気液用撹拌翼1Aを垂設し、該撹拌槽内に液体とガスとを供給しながら、該気液用撹拌翼1Aを矢印Aの方向に回転駆動すると、実施例1と同様の作用効果を生ずる。   When the gas-liquid stirring blade 1A is suspended in a stirring tank (not shown) and the liquid and gas are supplied into the stirring tank, the gas-liquid stirring blade 1A is rotationally driven in the direction of arrow A. The same effects as those of the first embodiment are produced.

そして、特に、本実施例2においては、上方段の翼体部2Cと中間段の翼体部2Dと下方段の翼体部2Eの3段の翼体部から構成されているので、上方段の翼体部2Cによる独立の吐出場の吐出流と下方段の翼体部2Eの吐出場の吐出流とが、中間段の翼体部2Dの吐出場の吐出流を中心とする共通の流域における集中的な撹拌作用を生じ、この撹拌作用が更に強力となる。   In particular, in the second embodiment, the upper stage wing body part 2C, the intermediate stage wing body part 2D, and the lower stage wing body part 2E are constituted by three stages of wing body parts. A common flow area in which the discharge flow of the independent discharge field by the blade body part 2C and the discharge flow of the discharge field of the lower-stage blade body part 2E are centered on the discharge flow of the discharge field of the intermediate-stage blade body part 2D This produces a concentrated stirring action at, which becomes even stronger.

上記実施例では、気液用撹拌翼1を2段又は3段の翼体部により構成した例を示したが、撹拌槽の深さに応じて4段以上の翼体部により構成してもよい。   In the above-described embodiment, the gas-liquid stirring blade 1 is configured by the two-stage or three-stage blade body. However, the gas-liquid stirring blade 1 may be configured by four or more blade bodies according to the depth of the stirring tank. Good.

又、上記実施例では、翼体部2A、2B、2C、2D、2Eをハブ部3aに取り付けて固定した例を示したが、これら翼体部2A、2B、2C、2D、2Eを回転軸3に取り付けて固定してもよい。   In the above embodiment, the wing body portions 2A, 2B, 2C, 2D, and 2E are fixed to the hub portion 3a. However, the wing body portions 2A, 2B, 2C, 2D, and 2E are connected to the rotating shaft. 3 may be attached and fixed.

又、上記実施例では、上側翼2aと下側翼2bは平板翼としたが、円弧状の横断面の翼としたり、又は、翼形の横断面の翼としてもよい。   In the above embodiment, the upper wing 2a and the lower wing 2b are flat wings, but may be wings having an arcuate cross section or wings having an airfoil cross section.

又、撹拌する液体やガスの性質によっては、撹拌翼1、1Aを矢印Aとは逆の方向に 回転駆動させて、上側翼2aと下側翼2bの間隙を翼の回転方向に向かって広くなるようにしてもよい。   Also, depending on the properties of the liquid or gas to be stirred, the stirring blades 1 and 1A are driven to rotate in the direction opposite to the arrow A, and the gap between the upper blade 2a and the lower blade 2b becomes wider toward the blade rotation direction. You may do it.

更に又、任意の方向に流れを強化する目的や、中央部におけるせん断作用を強化するために各段の翼体部の翼径をそれぞれ変更してもよい。   Furthermore, the blade diameters of the blade bodies at each stage may be changed in order to enhance the flow in an arbitrary direction or to enhance the shearing action at the center.

本発明の撹拌翼は、食品工業や化学工業等における気液の混合に利用される。   The stirring blade of the present invention is used for gas-liquid mixing in the food industry, the chemical industry, and the like.

1 撹拌翼
1A 撹拌翼
2 翼体部
2A 翼体部
2B 翼体部
2C 翼体部
2D 翼体部
2E 翼体部
2a 上側翼
2b 下側翼
3 回転軸
DESCRIPTION OF SYMBOLS 1 Stirring blade 1A Stirring blade 2 Blade body part 2A Blade body part 2B Blade body part 2C Blade body part 2D Blade body part 2E Blade body part 2a Upper blade 2b Lower blade 3 Rotating shaft

Claims (3)

上下一対の翼の対向面の間に間隙を形成すると共に該間隙を翼の回転方向に向かって狭くなるように形成し又は該間隙を翼の回転方向に向かって広くなるように形成した翼体部を、回転軸に放射状に上下複数段に取り付けた気液用撹拌翼。   A wing body in which a gap is formed between the opposing surfaces of a pair of upper and lower wings, and the gap is formed so as to become narrower in the direction of rotation of the wings, or the gap is formed so as to become wider in the direction of rotation of the wings. A gas-liquid stirring blade in which the parts are attached to the rotating shaft in a plurality of stages on the upper and lower sides. 上下に隣り合う段の前記翼体部は、互いに異なる回転方向の角度で前記回転軸に取り付けられている請求項1に記載の気液用撹拌翼。   2. The gas-liquid stirring blade according to claim 1, wherein the blade body portions of the upper and lower adjacent stages are attached to the rotating shaft at angles of different rotation directions. 上下に隣り合う段の前記翼体部は、前記回転軸に、軸方向に間隙を存せずに連続した個所に取付けられている請求項2に記載の気液用撹拌翼。   The gas-liquid stirring blade according to claim 2, wherein the blade body portions of the upper and lower adjacent stages are attached to the rotating shaft at continuous locations without any gap in the axial direction.
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108014711A (en) * 2017-12-07 2018-05-11 中国恩菲工程技术有限公司 Gas-liquid mechanical couplings agitating device
CN110074046A (en) * 2019-05-13 2019-08-02 韩殿帅 A kind of paddy field oxygen supply bubbled through the water column
WO2024100688A1 (en) * 2022-11-10 2024-05-16 Corob S.P.A. Device for agitating fluid products

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JPS5888126A (en) * 1981-11-16 1983-05-26 Nippon Sheet Glass Co Ltd Stirrer for melted glass
JPS5970499U (en) * 1982-11-05 1984-05-12 味の素株式会社 stirring blade
JPH0596527A (en) * 1990-11-21 1993-04-20 Kajima Corp Apparatus and method for kneading
JPH08507250A (en) * 1993-03-05 1996-08-06 レイモン ベルショットー Device for supplying and diffusing air or other gas into a liquid
JPH1028853A (en) * 1996-07-15 1998-02-03 Satake Kagaku Kikai Kogyo Kk Stirrer for gas-liquid
WO2006101074A1 (en) * 2005-03-22 2006-09-28 Suntory Limited Ventilating/stirring culture tank
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JP2008200565A (en) * 2007-02-16 2008-09-04 Nishihara Environment Technology Inc Biological treatment device
JP2010253372A (en) * 2009-04-23 2010-11-11 Ihi Corp Gas-liquid stirrer
JP2012040556A (en) * 2011-09-27 2012-03-01 Mitsubishi Heavy Ind Ltd Stirring method of fluid and arm rotation type sparger

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108014711A (en) * 2017-12-07 2018-05-11 中国恩菲工程技术有限公司 Gas-liquid mechanical couplings agitating device
CN108014711B (en) * 2017-12-07 2024-02-09 中国恩菲工程技术有限公司 Gas-liquid mechanical coupling stirring device
CN110074046A (en) * 2019-05-13 2019-08-02 韩殿帅 A kind of paddy field oxygen supply bubbled through the water column
WO2024100688A1 (en) * 2022-11-10 2024-05-16 Corob S.P.A. Device for agitating fluid products

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