JPS6346103Y2 - - Google Patents

Info

Publication number
JPS6346103Y2
JPS6346103Y2 JP1983161716U JP16171683U JPS6346103Y2 JP S6346103 Y2 JPS6346103 Y2 JP S6346103Y2 JP 1983161716 U JP1983161716 U JP 1983161716U JP 16171683 U JP16171683 U JP 16171683U JP S6346103 Y2 JPS6346103 Y2 JP S6346103Y2
Authority
JP
Japan
Prior art keywords
blade
tank
liquid
wall
flow
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.)
Expired
Application number
JP1983161716U
Other languages
Japanese (ja)
Other versions
JPS6071336U (en
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 filed Critical
Priority to JP16171683U priority Critical patent/JPS6071336U/en
Publication of JPS6071336U publication Critical patent/JPS6071336U/en
Application granted granted Critical
Publication of JPS6346103Y2 publication Critical patent/JPS6346103Y2/ja
Granted legal-status Critical Current

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  • Mixers Of The Rotary Stirring Type (AREA)

Description

【考案の詳細な説明】 本考案は液状物の循環処理経路中に設けられ低
速撹拌槽の改良にかかるものであり、詳しくは槽
上部から連続的に供給される液状物が槽内におい
て偏液、滞留することなく、槽底中央から順次流
出せしめるように、槽内に低速回転する特定構造
の撹拌翼を設けた低速撹拌槽を提供することを目
的とするものである。
[Detailed description of the invention] This invention relates to the improvement of a low-speed stirring tank installed in the circulation processing path for liquid materials. It is an object of the present invention to provide a low-speed stirring tank in which a stirring blade of a specific structure that rotates at a low speed is installed in the tank so that the liquid flows out from the center of the tank bottom one after another without stagnation.

化学工業、食品工業、薬品工業等において、液
状物に対して混合、分散、化学反応などの各種の
処理を行う場合に、比較的に処理容量の小さな処
理装置を通して大量の被処理液状物を連続的に供
給流過せしめて複数回の処理を繰返すように該流
動経路を閉回路とした循環処理装置があり、この
場合には上記閉回路中に被処理液状物を一時的に
保留しつつ流過せしめる大容量の貯留槽を介在せ
しめている。
In the chemical industry, food industry, pharmaceutical industry, etc., when performing various processes on liquid materials such as mixing, dispersion, and chemical reactions, large amounts of liquid materials are continuously processed through processing equipment with a relatively small processing capacity. There is a circulation treatment device in which the flow path is a closed circuit so that the supply flow is repeatedly passed through and the treatment is repeated multiple times.In this case, the liquid to be treated is temporarily held in the closed circuit and the flow is A large-capacity storage tank is provided to allow for a large amount of water to pass through.

上記の循環処理用の貯留槽は、槽内に供給流過
せしめる大量の被処理液状物が流入口から流出口
に向つて局部的に停滞することなく均一に流動す
ることが必要であり、従来この目的のために槽内
に高速回転撹拌翼を設けることが行われている
が、槽内壁面への液状物の付着、保留液中に生ず
る偏流、槽隅角部に生ずる滞留などの防止が充分
でなく、結果的に循環処理が均一になるまでに、
過度の処理時間と多大の処理動力を要する問題点
があつた。
The above-mentioned storage tank for circulation treatment requires that a large amount of liquid material to be treated be fed into the tank and flow uniformly from the inlet to the outlet without becoming locally stagnant. For this purpose, high-speed rotating stirring blades are installed in the tank, but it is difficult to prevent liquids from adhering to the tank's inner wall, drifting in the retained liquid, and stagnation at the corners of the tank. It is not enough, and as a result, until the circulation process becomes uniform,
There were problems in that excessive processing time and large amounts of processing power were required.

本考案は上記の問題点を解決するものであつ
て、循環処理用の液貯留槽中に、槽内面に生ずる
液付着停滞部分を掻き取る壁面ブレード、底ブレ
ード、保留液中に生ずる偏流を分断分散する水平
ブレードを有する低速撹拌翼を設けることによ
り、槽内液流を均一化することに成功したもので
ある。
The present invention solves the above-mentioned problems, and uses wall blades and bottom blades to scrape off the stagnant portion of liquid adhesion that occurs on the inner surface of the tank in a liquid storage tank for circulation processing. By providing a low-speed stirring blade with a horizontal blade that divides and disperses, we succeeded in making the liquid flow in the tank uniform.

以下、本考案の実施例を図面に従つて説明す
る。第1図は本考案の低速撹拌槽を循環処理経路
中に設けた装置の要部を断面とした説明的側面図
であり図面において1は低速撹拌槽であつて、周
壁2、底3、蓋4よりなる槽体の上部周壁に流入
口5、底中央に流出口6が設けられる。7は蓋4
の中央上部から槽内上部に突出した回転軸であつ
て、適宜の動力源により回転される。8は撹拌翼
であつて、壁面ブレード9、底ブレード10、水
平ブレード11を一体として構成され上部支持部
材12により前記回転軸7端に固着される。
Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is an explanatory side view showing a cross section of the main parts of a device in which a low-speed stirring tank of the present invention is installed in a circulation treatment path. An inlet 5 is provided in the upper peripheral wall of the tank body consisting of 4, and an outlet 6 is provided in the center of the bottom. 7 is lid 4
It is a rotating shaft that protrudes from the upper center of the tank to the upper part of the tank, and is rotated by an appropriate power source. Reference numeral 8 denotes a stirring blade, which is constructed by integrating a wall blade 9, a bottom blade 10, and a horizontal blade 11, and is fixed to the end of the rotating shaft 7 by an upper support member 12.

壁面ブレード9は槽周壁2の内面に近接し上下
方向に延び、底ブレード10は底3内面に近接し
て略回転半径方向に延び、水平ブレード11は槽
1に貯留される被処理液の深さに応じて1または
複数枚設け、その回転方向の面は鉛直面をなし、
略回転半径方向に延びる。底ブレード10、水平
ブレード11は第1図のA−A線における低速撹
拌槽の断面図である第2図に示すように、その内
端縁の位相が回転軸と壁面ブレードとを結ぶ回転
半径に対し回転方向で遅れるように傾斜(通常20
〜40゜)し、且つその端縁が回転中心から適当な
距離を置くように回転半径より短い長さに規制す
るのが好ましい。
The wall blade 9 is close to the inner surface of the tank circumferential wall 2 and extends in the vertical direction, the bottom blade 10 is close to the inner surface of the bottom 3 and extends substantially in the direction of the rotation radius, and the horizontal blade 11 is arranged to extend to the depth of the liquid to be treated stored in the tank 1. one or more sheets are provided depending on the
Extends approximately in the direction of the rotation radius. As shown in FIG. 2, which is a cross-sectional view of the low-speed stirring tank taken along line A-A in FIG. (usually 20
~40°), and the length is preferably restricted to be shorter than the rotation radius so that the end edge is at an appropriate distance from the rotation center.

また、壁面ブレード9、底ブレード10と槽内
面との間隙は成可く小さいことが望ましいが被処
理液の粘度により生ずる付着力の降伏値以上の粘
性応力が回転する撹拌翼と槽内面との間に生ずれ
ば、槽内面に付着した液の剥脱流動を生ずるもの
であり、通常粘度50Pa.s以下の液状物の場合に
は、5mm以下の間隙で、液状物の槽内面への付着
が防止できるものである。
It is desirable that the gaps between the wall blade 9, bottom blade 10 and the inner surface of the tank be as small as possible; If this occurs between the inner surface of the tank and the inner surface of the tank, it will cause the liquid adhering to the inner surface of the tank to peel off and flow. It is possible to prevent adhesion to the surface.

撹拌翼の回転は液状物の混合をするものではな
く、偏流の分断分散と槽内面への付着液の掻き取
りを図るものであるので、高速である必要はな
く、液の粘性特性及び槽の寸法的条件により異る
が通常0.5〜3r.p.m程度の低速回転で充分目的を
達成することができる。
The rotation of the stirring blades does not mix the liquid, but rather divides and disperses the drifting flow and scrapes off the liquid adhering to the inner surface of the tank, so it does not need to be at high speed and depends on the viscosity characteristics of the liquid and the speed of the tank. Although it varies depending on the dimensional conditions, normally a low speed rotation of about 0.5 to 3 rpm is sufficient to achieve the purpose.

上記の条件を具備した低速撹拌槽1は第1図に
示すようにその流入口5に連続流過型処理装置T
の吐出側が接続され、流出口6にポンプPを介し
て連続流過型処理装置Tの供給側が接続されて循
環処理経路が形成され、低速撹拌槽1内に大量の
被処理液状物が流入口5以下の液面になるように
収容されて、ポンプP、回転軸7を回転するとと
もに連続流過型処理装置を稼動せしめて、液状物
の所要の循環処理が行われるのである。
As shown in FIG.
The discharge side of the continuous flow treatment device T is connected to the outflow port 6 via the pump P to form a circulation treatment path, and a large amount of liquid to be treated enters the low-speed stirring tank 1 at the inflow port. The liquid is stored so that the liquid level is 5 or less, and the pump P and rotating shaft 7 are rotated, and the continuous flow type processing device is operated to perform the required circulation treatment of the liquid.

流入口5から供給された液状物は、撹拌翼部材
による撹拌が行われない場合は一点鎖線で示すよ
うな流出口に向う短絡した偏流を生じ、該偏流ゾ
ーンから離れた部分の液状物の流動は僅かとなり
特に周壁2の内面並びに底3の内面に接する液状
物は殆んど流動することなく滞留し、循環処理を
長時間行つても、その系内の被処理液の均一処理
は殆んど不可能に近いものであるが、本考案にお
ける壁面ブレード9、底ブレード10の回転によ
り槽内面に付着停滞する液状物は強制的に剥脱さ
れつつ撹拌され、且つ水平ブレード11の回転に
よる撹拌液流によつて短絡偏流は分断分散されて
全体として略均一な下降液流を生じつつ流出口6
からポンプPに吸引されて連続流過型処理装置に
供給される。
When the liquid supplied from the inlet 5 is not stirred by the stirring blade member, a short-circuited drift toward the outlet as shown by the dashed line occurs, and the flow of the liquid in the part away from the drift zone is caused. In particular, the liquid material in contact with the inner surface of the peripheral wall 2 and the inner surface of the bottom 3 remains almost without flowing, and even if circulation treatment is performed for a long time, the liquid to be treated within the system is hardly uniformly treated. Although this is almost impossible, the rotation of the wall blade 9 and the bottom blade 10 in the present invention forcibly removes the liquid that adheres to the inner surface of the tank and agitates it, and the rotation of the horizontal blade 11 also agitates it. The short-circuit drift is divided and dispersed by the liquid flow, and an approximately uniform descending liquid flow is generated as a whole, while the flow reaches the outlet 6.
The water is sucked into the pump P and supplied to the continuous flow processing device.

前述の回転軸7の下端並びに支持部材12が槽
内の被処理液状物の液面下に位置せしめると、該
回転軸7の低速回転にともない液状物と接触する
部分はその相対速度は極めて小となるために液状
物の付着による部分的滞留を生じ、均一流動の目
的から好ましくない。
When the lower end of the rotating shaft 7 and the support member 12 are positioned below the surface of the liquid to be treated in the tank, the relative speed of the portion that comes into contact with the liquid as the rotating shaft 7 rotates at a low speed is extremely small. This results in partial stagnation due to adhesion of liquid matter, which is undesirable from the viewpoint of uniform flow.

また、水平ブレード11、底ブレード10を前
述のように回転半径方向に対し傾斜せしめておく
と、これらブレードの回転による撹拌作用ととも
に槽直径方向の流動を生ずるので、均一液流を形
成する上で好ましい。
Furthermore, if the horizontal blade 11 and the bottom blade 10 are inclined with respect to the rotational radial direction as described above, the rotation of these blades will produce a stirring action and a flow in the tank diameter direction, which will help in forming a uniform liquid flow. preferable.

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

図面は本考案の実施例を示すものであつて、第
1図は本考案の低速撹拌層を循環処理経路中に設
けた装置の要部を断面とした説明的側面図であ
り、第2図は第1図A−A線における低速撹拌槽
の断面図である。 1……低速撹拌槽、2……周壁、3……底、4
……蓋、5……流入口、6……流出口、7……回
転軸、8……撹拌翼、9……壁面ブレード、10
……底ブレード、11……水平ブレード、12…
…支持部材、T……連続流過型処理装置、P……
ポンプ。
The drawings show an embodiment of the present invention, and FIG. 1 is an explanatory side view showing a main part of the apparatus in which the low-speed stirring layer of the present invention is provided in the circulation treatment path, and FIG. FIG. 1 is a cross-sectional view of the low-speed stirring tank taken along line A-A in FIG. 1...Low speed stirring tank, 2...Surrounding wall, 3...Bottom, 4
... Lid, 5 ... Inlet, 6 ... Outlet, 7 ... Rotating shaft, 8 ... Stirring blade, 9 ... Wall blade, 10
...Bottom blade, 11...Horizontal blade, 12...
...Support member, T...Continuous flow treatment device, P...
pump.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 上部に流入口、底部中央に流出口を設けた縦型
円筒槽の上部中心から槽内上部に突出した回転軸
を垂設し、該回転軸に壁面ブレード、底ブレー
ド、水平ブレードよりなる撹拌翼を固設し、前記
壁面ブレード及び底ブレードは槽内面に対し、5
mm以下の間隙を有せしめてなり、該底ブレードお
よび該水平ブレードの内端縁の位相が回転軸と壁
面ブレードとを結ぶ回転半径に対し回転方向で遅
れるように傾斜し、かつ該回転軸が液面下に位置
しないようにしたことを特徴とする循環処理用低
速撹拌槽。
A vertical cylindrical tank with an inlet at the top and an outlet at the center of the bottom has a rotating shaft protruding from the center of the top to the top of the tank, and a stirring blade consisting of a wall blade, a bottom blade, and a horizontal blade is attached to the rotating shaft. is fixedly installed, and the wall blade and bottom blade are 5.
the inner edge of the bottom blade and the horizontal blade are inclined so that the phases of the inner edges of the bottom blade and the horizontal blade lag in the rotation direction with respect to the rotation radius connecting the rotation axis and the wall blade, and the rotation axis is A low-speed stirring tank for circulation processing that is characterized by not being located below the liquid level.
JP16171683U 1983-10-19 1983-10-19 Low speed stirring tank for circulation treatment Granted JPS6071336U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16171683U JPS6071336U (en) 1983-10-19 1983-10-19 Low speed stirring tank for circulation treatment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16171683U JPS6071336U (en) 1983-10-19 1983-10-19 Low speed stirring tank for circulation treatment

Publications (2)

Publication Number Publication Date
JPS6071336U JPS6071336U (en) 1985-05-20
JPS6346103Y2 true JPS6346103Y2 (en) 1988-12-01

Family

ID=30355322

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16171683U Granted JPS6071336U (en) 1983-10-19 1983-10-19 Low speed stirring tank for circulation treatment

Country Status (1)

Country Link
JP (1) JPS6071336U (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4456221B2 (en) * 2000-03-17 2010-04-28 株式会社井上製作所 Concentric 2-axis mixer
EP2676724A4 (en) * 2011-02-17 2018-01-24 Sintokogio, Ltd. Tank apparatus, circulating-type dispersion system, and dispersion method

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4528235Y1 (en) * 1967-04-12 1970-10-30
JPS54169978U (en) * 1978-05-22 1979-11-30

Also Published As

Publication number Publication date
JPS6071336U (en) 1985-05-20

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