JP2011251236A - Stirring blade for medium and high viscosity - Google Patents

Stirring blade for medium and high viscosity Download PDF

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JP2011251236A
JP2011251236A JP2010125965A JP2010125965A JP2011251236A JP 2011251236 A JP2011251236 A JP 2011251236A JP 2010125965 A JP2010125965 A JP 2010125965A JP 2010125965 A JP2010125965 A JP 2010125965A JP 2011251236 A JP2011251236 A JP 2011251236A
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stirring blade
tank
blade portion
blade
forced flow
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JP5736127B2 (en
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Shigeru Nishioka
茂 西岡
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 stirring blade which is good in thermal conduction to a liquid in a tank, can sufficiently stir the liquid to thereby achieve uniformization of the liquid temperature, and has a simple structure and exhibits good cleanability.SOLUTION: The stirring blade comprises: a principal stirring blade portion 2 of the inside, formed wider as going downward; a forced flow-generating blade portion 3 of the outside, having an outside part 3a rotating in the vicinity of the inner peripheral surface of the tank 5; and a linking portion 4 to link the principal stirring blade portion 2 and the forced flow-generating blade portion 3, in the lower part. The principal stirring blade portion 2, the forced flow-generating blade portion 3 and the linking portion 4 are formed integrally of a platy body.

Description

本発明は、食品工業、化学工業等において中・高粘度の難流動性液体の伝熱混合に好適な中・高粘度用撹拌翼に関する。   The present invention relates to a medium / high viscosity agitating blade suitable for heat transfer mixing of a medium / high viscosity hardly flowable liquid in the food industry, the chemical industry, and the like.

従来この種の撹拌翼として図4に示す如きアンカー翼aや図5に示す如きヘリカルリボン翼bが知られている。尚、これら図中cは槽、dは回転軸、eは該槽cの外壁に設けられている加熱手段を示す(非特許文献1参照)。   Conventionally, as this kind of stirring blade, an anchor blade a as shown in FIG. 4 and a helical ribbon blade b as shown in FIG. 5 are known. In these figures, c is a tank, d is a rotating shaft, and e is a heating means provided on the outer wall of the tank c (see Non-Patent Document 1).

佐竹化学機械工業株式会社編「撹拌技術」、佐竹化学機械工業株式会社発行、1992年12月18日、P13Edited by Satake Chemical Machinery Co., Ltd. “Agitation Technology”, published by Satake Chemical Machinery Co., Ltd., December 18, 1992, P13

前記アンカー翼aによれば、該アンカー翼aが槽cの内周面の近傍を回転するので、該内周面の近傍で液体が強制的に流動させられ、加熱手段eから槽c内への液体への伝熱が良好に行われるが、該槽c内での液体の撹拌及び上下循環流が不十分で該液体の温度ムラが生ずる問題点があり、又前記ヘリカルリボン翼bによれば、槽c内の液体の撹拌は十分行われるが、部分的な混合不良に伴う熱混合不良部の発生及び構造が複雑で作業後の洗浄が行いにくい問題点があった。   According to the anchor blade a, since the anchor blade a rotates in the vicinity of the inner peripheral surface of the tank c, the liquid is forced to flow in the vicinity of the inner peripheral surface, and the heating means e enters the tank c. However, there is a problem in that the temperature of the liquid is not uniform due to insufficient stirring and up-and-down circulation of the liquid in the tank c. For example, although the liquid in the tank c is sufficiently stirred, there is a problem in that it is difficult to perform cleaning after work due to the complicated generation and structure of a poorly heat-mixed part due to partial mixing failure.

本発明は、これらの問題点を解消し、槽内の液体への伝熱が良好であると共に該液体の撹拌が十分行われて液温の均一化が図れ、構造が簡単で洗浄性が良好な撹拌翼を提供することを目的とする。   The present invention eliminates these problems, heat transfer to the liquid in the tank is good, and the liquid is sufficiently agitated to achieve a uniform liquid temperature, with a simple structure and good cleanability. An object of the present invention is to provide a simple stirring blade.

本発明は上記の目的を達成すべく、下方に向うに従って幅広に形成されている内側の主撹拌翼部と槽の内周面の近傍を回転移動する外側辺を有する外側の強制流動発生翼部とこれら主撹拌翼部と強制流動発生翼部とを下方部において連設する連設部とからなる。   In order to achieve the above-mentioned object, the present invention provides an outer forced flow generating blade portion having an inner main stirring blade portion that is formed wider toward the lower side and an outer side that rotates and moves in the vicinity of the inner peripheral surface of the tank. And the main agitating blade portion and the forced flow generating blade portion are provided in a continuous portion at the lower portion.

本発明によれば、槽内へ液体が中・高粘度の難流動性の液体であっても該液体への伝熱が良好であると共に撹拌が十分行われて該液体が均一の温度になり、更に撹拌翼自体が垂直平面の簡単な構造で洗浄性が良好となる効果を有する。   According to the present invention, even if the liquid into the tank is a non-flowable liquid of medium or high viscosity, heat transfer to the liquid is good and sufficient stirring is performed so that the liquid has a uniform temperature. Further, the stirring blade itself has a simple structure with a vertical plane, and has an effect of improving the cleaning property.

本発明の撹拌翼の実施例1の正面図である。It is a front view of Example 1 of the stirring blade of this invention. 本発明の撹拌翼による撹拌の場合の加熱時間と槽内代表温度の関係を示すグラフである。It is a graph which shows the relationship between the heating time in the case of stirring with the stirring blade of this invention, and the representative temperature in a tank. 従来のアンカー翼による撹拌の場合の加熱時間と槽内代表温度の関係を示すグラフである。It is a graph which shows the relationship between the heating time in the case of stirring by the conventional anchor blade, and the representative temperature in a tank. 従来の撹拌翼でアンカー翼の例の正面図である。It is a front view of the example of an anchor blade with the conventional stirring blade. 従来の撹拌翼でヘリカルリボン翼の例の正面図ある。It is a front view of the example of a helical ribbon blade | wing with the conventional 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.

本発明の撹拌翼の実施例1を図1により説明する。   Embodiment 1 of the stirring blade of the present invention will be described with reference to FIG.

図1は撹拌翼の実施例1の正面図である。   FIG. 1 is a front view of Example 1 of a stirring blade.

1は撹拌翼を示し、該撹拌翼1は、内側の主撹拌翼部2と外側の強制流動発生翼部3とこれら主撹拌翼部2と強制流動発生翼部3とを下方部で連設する連設部4とを板状体により一体に形成されている。   Reference numeral 1 denotes a stirring blade, and the stirring blade 1 includes an inner main stirring blade portion 2, an outer forced flow generation blade portion 3, and the main stirring blade portion 2 and the forced flow generation blade portion 3 arranged in a lower portion. The connecting portion 4 is integrally formed of a plate-like body.

前記主撹拌翼部2は、内側辺2aが垂直で外側辺2bが上端から下方に向うに従って斜外方に傾斜して順次幅広の三角形状に形成され、又前記強制流動発生翼部3は外側辺3aが垂直で下方に向って幅広となる傾斜する内側辺3bを有する鋭い頂角の三角形状に形成され、更に前記連設部と主撹拌翼部2と強制流動発生翼部3の下辺即ち撹拌翼1の下辺1aが後述する槽5の内底面に沿って湾曲状に形成されている。   The main agitating blade portion 2 is formed in the shape of a triangle that is inclined obliquely outwardly as the inner side 2a is vertical and the outer side 2b is directed downward from the upper end, and the forced flow generating blade portion 3 is formed on the outer side. The side 3a is formed in a triangular shape with a sharp apex having a sloping inner side 3b that is vertical and widens downward, and further, the lower side of the connecting part, the main stirring blade part 2, and the forced flow generation blade part 3, The lower side 1a of the stirring blade 1 is formed in a curved shape along the inner bottom surface of the tank 5 described later.

5は槽を示し、該槽5は有底の円形筒状に形成され、且つ底面は下方に突出する湾曲状に形成され、該槽5の中心部に回転軸6が垂下して設けられ、該回転軸6の下端部に1対の前記撹拌翼1をボス7を介して固定し、該撹拌翼1の前記強制流動発生翼部3の外側辺3aを前記槽5の内周面に対して近傍に位置させると共に、前記撹拌翼1の下辺1aを該槽5の内底面に対して近傍に位置させている。   5 indicates a tank, the tank 5 is formed in a bottomed circular cylindrical shape, and the bottom surface is formed in a curved shape protruding downward, and a rotary shaft 6 is provided in a hanging manner at the center of the tank 5; A pair of the stirring blades 1 is fixed to the lower end portion of the rotating shaft 6 via a boss 7, and the outer side 3 a of the forced flow generating blade portion 3 of the stirring blade 1 is set to the inner peripheral surface of the tank 5. And the lower side 1 a of the stirring blade 1 is positioned in the vicinity of the inner bottom surface of the tank 5.

8は該槽5の周面から底面にわたって外方に設けた伝熱ジャケット等からなる加熱手段を示す。   Reference numeral 8 denotes a heating means comprising a heat transfer jacket or the like provided outward from the peripheral surface to the bottom surface of the tank 5.

次に本実施例の撹拌翼1の作用とその効果について説明する。   Next, the operation and effect of the stirring blade 1 of this embodiment will be described.

槽5内に中・高粘度の難流動性の液体を所定の上方のレベルまで満たしてからモータ(図示せず)により回転軸6を回転駆動すると、該回転軸6と共に撹拌翼1が回転する。   When the rotary shaft 6 is driven to rotate by a motor (not shown) after filling the tank 5 with a medium and high viscosity hard-flowing liquid to a predetermined upper level, the stirring blade 1 rotates together with the rotary shaft 6. .

該撹拌翼1の回転において、槽5内の液体の上方部においては、主撹拌翼部2はその幅が狭くしかも回転軸6の近傍に存するのみであるので、該主撹拌翼部2による液体の回転力が小さくて負圧が小であるのに対して、槽5内の液体の下方部においては、主撹拌翼部2の幅が大となって回転軸6から離れた個所でも主撹拌翼部2により液体に回転力が大きく作用して負圧が大となり、かくて液体は、該液体の負圧差により下方に向う強力な流動を生ずると共に回転力が付与され、その後液体は連設部4においても回転力を付与されて槽5内の底面に沿って外方に流動してから該槽5の内周面に沿って上方に流動して循環流Aとなる。   In the rotation of the stirring blade 1, the main stirring blade portion 2 is narrow in the upper portion of the liquid in the tank 5 and only exists in the vicinity of the rotating shaft 6. In the lower part of the liquid in the tank 5, the main agitating blade part 2 is wide and the main agitating part is separated from the rotating shaft 6. The wing part 2 exerts a large rotational force on the liquid to increase the negative pressure. Thus, the liquid generates a strong downward flow due to the negative pressure difference of the liquid and is given a rotational force. Also in the portion 4, a rotational force is applied and flows outward along the bottom surface in the tank 5, and then flows upward along the inner peripheral surface of the tank 5 to become a circulating flow A.

このとき、撹拌翼1の下辺及び強制流動発生翼部3の外側辺3aは槽5の内底面及び内周面の近傍を回転移動するので強制的に強い流動が発生し、かくて加熱手段8から液体への熱の伝達が良好に行われ、前述の循環流Aによって液体が全体にわたって均一に昇温する。   At this time, the lower side 3 a of the stirring blade 1 and the outer side 3 a of the forced flow generating blade portion 3 rotate around the inner bottom surface and the inner peripheral surface of the tank 5, so that a strong flow is generated forcibly, thus heating means 8. Heat is transferred from the liquid to the liquid satisfactorily, and the temperature of the liquid is increased uniformly throughout the entire circulation flow A.

ここで前記撹拌翼1は主撹拌翼部2と強制流動発生翼部3と連設部4とが板状体により一体に形成されているので、該撹拌翼1は構造が簡単で、洗浄が行い易い。   Here, since the stirring blade 1 has a main stirring blade portion 2, a forced flow generation blade portion 3, and a connecting portion 4 integrally formed by a plate-like body, the stirring blade 1 has a simple structure and can be cleaned. Easy to do.

尚、本実施例では、強制流動発生翼部3の内側辺3bが傾斜する例を示したが、該内側辺3bを外側辺3aと同様に垂直に形成してもよい。又、撹拌翼1を2枚以上使用することが好ましい。   In the present embodiment, an example in which the inner side 3b of the forced flow generating blade portion 3 is inclined is shown. However, the inner side 3b may be formed vertically like the outer side 3a. Further, it is preferable to use two or more stirring blades 1.

次に、槽の内周の上部と下部に熱電対を設置し、、槽内で本発明の撹拌翼により撹拌した場合の加熱時間の経過に応じた槽内の温度変化の実験結果を図2に示す一方、従来のアンカー翼により撹拌した場合の加熱時間の経過に応じた槽内の温度変化の実験結果を図3に示す。   Next, FIG. 2 shows the experimental results of the temperature change in the tank as the heating time elapses when thermocouples are installed at the upper and lower parts of the inner periphery of the tank and stirred by the stirring blade of the present invention in the tank. On the other hand, the experimental result of the temperature change in a tank according to progress of the heating time at the time of stirring with the conventional anchor blade is shown in FIG.

これらの実験結果より、アンカー翼の撹拌と比べて本発明の撹拌翼の場合は、加熱時間の早い段階から槽上部温度Tと槽下部温度Tとが一致して、槽内の温度のバラツキが小さく一様となり、熱混合性能に優れていることが実証された。 From these experimental results, in the case of the stirring blade of the present invention as compared with stirring anchor blade, from an early stage of the heating time and the tank upper temperature T a and the tank bottom temperature T b is the same, the temperature in the tank The variation was small and uniform, and it was demonstrated that the thermal mixing performance was excellent.

いずれの場合も撹拌レイノルズ数は約20である。   In either case, the stirring Reynolds number is about 20.

本発明の撹拌翼は、食品工業や化学工業等において、中・高粘度の難流動性の液体であっても撹拌を良好に行いながら均一の昇温や冷却を達成できる。   The stirring blade of the present invention can achieve uniform temperature rise and cooling while stirring well even in the food industry, the chemical industry, etc., even in the case of a medium or high viscosity hard-flowing liquid.

1 撹拌翼
2 主撹拌翼部
2b 外側辺
3 強制流動発生翼部
3a 外側辺
4 連設部
5 槽
DESCRIPTION OF SYMBOLS 1 Stirring blade 2 Main stirring blade part 2b Outer side 3 Forced flow generation blade part 3a Outer side 4 Consecutive part 5 Tank

Claims (4)

下方に向うに従って幅広に形成されている内側の主撹拌翼部と槽の内周面の近傍を回転移動する外側辺を有する外側の強制流動発生翼部とこれら主撹拌翼部と強制流動発生翼部とを下方部において連設する連設部とからなる中・高粘度用撹拌翼。   An inner main agitating blade portion that is formed wider toward the lower side, an outer forced flow generating blade portion having an outer side that rotates in the vicinity of the inner peripheral surface of the tank, and these main agitating blade portion and forced flow generating blade An agitating blade for medium and high viscosity comprising a continuous portion in which the portion is continuously provided at the lower portion. 前記主撹拌翼部と前記強制流動発生翼部と前記連設部とを板状体により一体に形成した請求項1に記載の中・高粘度用撹拌翼。   The medium / high viscosity stirring blade according to claim 1, wherein the main stirring blade portion, the forced flow generation blade portion, and the connecting portion are integrally formed of a plate-like body. 前記主撹拌翼部は、その外側辺が傾斜している三角形状に形成されている請求項1又は請求項2に記載の中・高粘度用撹拌翼。   The medium / high viscosity stirring blade according to claim 1, wherein the main stirring blade portion is formed in a triangular shape whose outer side is inclined. 前記強制流動発生翼部は内側辺を下方に向って内方に傾斜するか垂直に形成した請求項1又は請求項2に記載の中・高粘度用撹拌翼。   3. The medium / high viscosity stirring blade according to claim 1, wherein the forced flow generating blade portion is inclined inward or vertically with an inner side facing downward.
JP2010125965A 2010-06-01 2010-06-01 Tank with stirring blades for medium and high viscosity Active JP5736127B2 (en)

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Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2183496A (en) * 1985-11-30 1987-06-10 Chem Plant Stainless Limited A mixer vessel and a method of mixing
JPH04346826A (en) * 1991-05-24 1992-12-02 Shinko Pantec Co Ltd Agitating device
JPH0518637U (en) * 1991-08-05 1993-03-09 株式会社品川工業所 Heating stirring device
JPH08281089A (en) * 1995-04-09 1996-10-29 Sumitomo Heavy Ind Ltd Vertical type stirring machine
JP2000202268A (en) * 1998-11-11 2000-07-25 Lintec Corp Agitator
JP2001205067A (en) * 2000-01-27 2001-07-31 Shinko Pantec Co Ltd Agitation blade and filtering/drying apparatus
JP2006087979A (en) * 2004-09-21 2006-04-06 Shi Mechanical & Equipment Inc Agitator

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2183496A (en) * 1985-11-30 1987-06-10 Chem Plant Stainless Limited A mixer vessel and a method of mixing
JPH04346826A (en) * 1991-05-24 1992-12-02 Shinko Pantec Co Ltd Agitating device
JPH0518637U (en) * 1991-08-05 1993-03-09 株式会社品川工業所 Heating stirring device
JPH08281089A (en) * 1995-04-09 1996-10-29 Sumitomo Heavy Ind Ltd Vertical type stirring machine
JP2000202268A (en) * 1998-11-11 2000-07-25 Lintec Corp Agitator
JP2001205067A (en) * 2000-01-27 2001-07-31 Shinko Pantec Co Ltd Agitation blade and filtering/drying apparatus
JP2006087979A (en) * 2004-09-21 2006-04-06 Shi Mechanical & Equipment Inc Agitator

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