JPH05293349A - Slow and rapid agitating tank - Google Patents

Slow and rapid agitating tank

Info

Publication number
JPH05293349A
JPH05293349A JP4121088A JP12108892A JPH05293349A JP H05293349 A JPH05293349 A JP H05293349A JP 4121088 A JP4121088 A JP 4121088A JP 12108892 A JP12108892 A JP 12108892A JP H05293349 A JPH05293349 A JP H05293349A
Authority
JP
Japan
Prior art keywords
cylinder
rotating shaft
stirring
rotating
fixed
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
JP4121088A
Other languages
Japanese (ja)
Other versions
JP2900296B2 (en
Inventor
Takeshi Okada
猛 岡田
Tomohiko Kusumi
知彦 楠見
Fumiyuki Tatematsu
文之 立松
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.)
MARINE KK
Organo Corp
Original Assignee
MARINE KK
Organo Corp
Japan Organo Co 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 MARINE KK, Organo Corp, Japan Organo Co Ltd filed Critical MARINE KK
Priority to JP4121088A priority Critical patent/JP2900296B2/en
Publication of JPH05293349A publication Critical patent/JPH05293349A/en
Application granted granted Critical
Publication of JP2900296B2 publication Critical patent/JP2900296B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/18Stationary reactors having moving elements inside

Abstract

PURPOSE:To perform slow and rapid agitation in one tank to provide sufficient agitation by coaxially fixing a rotating cylinder of diameters different from each other to a rotating shaft, installing a fixed cylinder between the rotary shaft and the rotating cylinder and projectingly providing agitating blades on the rotating shaft and the rotating cylinder. CONSTITUTION:A rotating shaft 11 is vertically inserted into a tank body 1 and a rotating cylinder 14 with one end open and the other end closed of different diameters from each other is coaxially fixed to the rotating shaft 11. And a fixed cylinder 5 with one end closed and the other end open of diameters different from each other is coaxially fixed to the rotating shaft 11 leaving a space between the rotating shaft 11 and the rotating cylinder 14. Agitating blades are projectingly provided on the rotating shaft 11 and the rotating cylinder 14 and plural agitating chambers 16-18 which are bent in order and coaxially communicate with each other are formed between the rotating shaft 11, the rotating cylinder 14, the fixed cylinder 5 and the tank body 1. An original liquid feed opening 3 and a treated liquid discharge opening 7 are provided on the outermost side and the innermost side of the agitating chambers 16-18 respectively. Thus the whole original liquid is sufficiently agitated and mixed.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、汚泥の凝集処理におい
て、得られるフロックの脱水を容易にするため凝集剤を
添加しつつ急速撹拌ついで緩速撹拌を行う場合等、その
他各種の用途に使用される緩急撹拌槽に関する。
INDUSTRIAL APPLICABILITY The present invention is used for various other purposes, such as in the case of performing flocculation treatment of sludge in which rapid flocculation and then slow flocculation are performed while adding a flocculant to facilitate dehydration of the flocs obtained. The present invention relates to a rapid stirring tank.

【0002】[0002]

【従来の技術】従来、例えば下水処理、産業排水処理等
で発生する汚泥に凝集剤を添加しつつ撹拌してフロック
を生成する緩急撹拌槽として、槽内を、原水供給口を有
する急速撹拌室と、その上位の排出口を有する緩速撹拌
室との連通する上下2室に区画し、槽上面に設置された
1つのモータ及び減速機にそれぞれ接続された内側回転
軸、及び該内側回転軸に回転自在に被嵌され且つ該内側
回転軸より低速回転の中空外側回転軸を上記緩速及び急
速撹拌室内に縦通垂下し、その一方の内側回転軸に上記
急速撹拌室内で回転すべき急速撹拌翼を、他方の外側回
転軸に上記緩速撹拌室内で回転すべき緩速撹拌翼をそれ
ぞれ取付けた構造のものが知られている。
2. Description of the Related Art Conventionally, a rapid agitation chamber having a raw water supply port is used as a rapid agitation tank for adding flocculant to sludge generated in sewage treatment, industrial wastewater treatment, etc. to generate flocs by stirring. And an inner rotary shaft that is divided into two upper and lower chambers that communicate with a slow stirring chamber having an upper discharge port, and that are respectively connected to one motor and a speed reducer installed on the upper surface of the tank, and the inner rotary shaft. A hollow outer rotary shaft, which is rotatably fitted to the inner rotary shaft and rotates at a slower speed than the inner rotary shaft, vertically hangs in the slow and quick stirring chamber, and one of the inner rotary shafts should rotate rapidly in the quick stirring chamber. There is known a structure in which a stirring blade is attached to each of the other outer rotating shafts, and a slow stirring blade to be rotated in the slow stirring chamber is attached.

【0003】[0003]

【発明が解決しようとする課題】しかし、上記従来槽で
は、内側及び外側の二重回転軸、並びに1つのモータか
ら内側回転軸及び外側回転軸へ互に異なる回転を伝達す
るためのさらに別の減速機構が必要であり、しかも槽全
体が急速撹拌室と緩速撹拌室を上下に連続させたタワー
型のものとなるため強固な支持構造が必要となり、それ
らが相まって全体として高価につく欠点があり、さらに
撹拌作用については、急速撹拌室と緩速撹拌室とが上下
直列に連通しているため原水の流れが概して直線的とな
り、それにより撹拌混合が原水全体に十分に及びにくい
難点があった。本発明は、従来の欠点を除くことを課題
とする。
However, in the above-mentioned conventional tank, the inner and outer double rotary shafts, and further another rotary shaft for transmitting different rotations from one motor to the inner rotary shaft and the outer rotary shaft. A deceleration mechanism is required, and since the whole tank is a tower type in which a rapid stirring chamber and a slow stirring chamber are connected vertically, a strong support structure is required, which in combination makes them expensive. Regarding the agitation action, since the rapid agitation chamber and the slow agitation chamber are connected in series in the vertical direction, the flow of the raw water is generally linear, which makes it difficult to agitate and mix the raw water as a whole. It was The present invention aims to eliminate the drawbacks of the prior art.

【0004】[0004]

【課題を解決するための手段】上記課題を解決する手段
として、本発明は、槽本体内に、回転駆動手段に接続さ
れた1本の回転軸を縦通し、上記槽本体内において、一
端を開口し他端を閉成する互に径の異なる1または複数
の回転円筒を、上記回転軸の外側に順次同心的位置関係
で、該回転軸に固定支持させると共に、一端を閉成し他
端を開口する互に径の異なる1または複数の固定円筒
を、上記回転軸と回転円筒の間または内外回転円筒の間
にそれぞれ間隔をあけて差し合わせた状態で、上記槽本
体に固定し、また少くとも上記回転軸及び回転円筒には
撹拌翼をそれぞれ突設し、それにより上記回転軸及び回
転円筒と固定円筒との間に、順次屈曲して同心的に連通
する複数の撹拌室を形成し、上記複数の撹拌室における
最外側の撹拌室に原液供給口を、最内側の撹拌室に処理
液排出口をそれぞれ設けた、緩急撹拌槽を提案する。
As a means for solving the above-mentioned problems, according to the present invention, one rotating shaft connected to a rotation driving means is vertically passed through a tank main body, and one end in the tank main body is inserted. One or a plurality of rotating cylinders having different diameters which are opened and closed at the other end are sequentially fixedly supported on the rotating shaft in a concentric positional relationship outside the rotating shaft, and one end is closed and the other end is closed. Fixed to the tank main body in a state where one or a plurality of fixed cylinders having different diameters, which are open to each other, are fitted with a gap between the rotary shaft and the rotary cylinder or between the inner and outer rotary cylinders, respectively. At least the agitating blades are respectively provided on the rotary shaft and the rotary cylinder so as to form a plurality of agitating chambers that are sequentially bent and concentrically connected to each other between the rotary shaft and the rotary cylinder and the fixed cylinder. , The outermost stirring chamber of the above-mentioned plurality of stirring chambers The supply port, provided the treatment liquid outlet port to each stirring chamber of the innermost proposes a pace stirred tank.

【0005】[0005]

【作用】本発明においては、上記回転軸を回転させる
と、該回転軸と各回転円筒は同一回転数で回転するが、
回転半径の違いにより中心に位置する回転軸の撹拌翼に
よる撹拌は最低緩速撹拌、その外側の回転円筒の撹拌翼
は順次撹拌速度が高くなり、最外側の回転円筒の撹拌翼
による撹拌は最高急速撹拌となる。以下本発明を汚泥の
凝集反応に使用する緩急撹拌槽に実施した例について図
面を参照して説明する。
In the present invention, when the rotary shaft is rotated, the rotary shaft and each rotary cylinder rotate at the same rotational speed.
Due to the difference in the rotation radius, the stirring blade of the rotating shaft located at the center is the slowest stirring, the stirring blade of the outer rotating cylinder has a higher stirring speed, and the stirring blade of the outermost rotating cylinder is the highest stirring. It becomes rapid stirring. Hereinafter, an example in which the present invention is applied to a slow stirring tank used for sludge flocculation reaction will be described with reference to the drawings.

【0006】[0006]

【実施例】図1において、槽本体(1)は、底板(2)
に汚泥供給口(3)を有する上下両端閉成の円筒体で、
その上板(4)から、該槽本体(1)の約2分の1の径
の固定円筒(5)を挿入して、該槽本体(1)と同心位
置に垂下すると共に上端部を適宜上方へ突出した状態
で、該上板(4)に固定してあり、上記固定円筒(5)
は、下端を開口すると共に下半部を下方へ先細りに傾斜
させ、上端は上板(6)により閉成したもので、その上
板(6)近くの側壁に凝集汚泥排出口(7)を開設して
ある。
EXAMPLE In FIG. 1, a tank body (1) is a bottom plate (2).
A cylindrical body with upper and lower ends closed, which has a sludge supply port (3)
From the upper plate (4), a fixed cylinder (5) having a diameter of about ½ of the tank body (1) is inserted, and the cylinder (5) hangs concentrically with the tank body (1) and the upper end portion is appropriately adjusted. The fixed cylinder (5) is fixed to the upper plate (4) in a state of protruding upwards.
Is the one in which the lower end is opened and the lower half is tapered downward, and the upper end is closed by the upper plate (6). The coagulated sludge discharge port (7) is provided on the side wall near the upper plate (6). It has been opened.

【0007】上記固定円筒(5)の上板(6)上には支
持台(8)を固定し、該支持台(8)上にモータ(9)
及び減速機(10)からなる回転駆動手段を設置し、そ
の減速機(10)の出力軸に上端を接続された回転軸
(11)を、上記支持台(8)及び固定円筒上板(6)
の各軸受部(12)、(13)に支承させた状態で、上
記固定円筒(5)内の同心位置に垂下して軸(11)下
端部を固定円筒(5)の開口下端から槽本体(1)内に
若干突出させ、突出端に回転円筒(14)を固定してあ
る。
A support base (8) is fixed on the upper plate (6) of the fixed cylinder (5), and a motor (9) is mounted on the support base (8).
And a rotary drive means composed of a speed reducer (10), and the rotary shaft (11) whose upper end is connected to the output shaft of the speed reducer (10) is connected to the support base (8) and the fixed cylindrical upper plate (6). )
While being supported by the bearings (12) and (13), the lower end of the shaft (11) is hung down to the concentric position in the fixed cylinder (5) from the opening lower end of the fixed cylinder (5) to the tank body. The rotary cylinder (14) is fixed to the projecting end by slightly projecting it into (1).

【0008】上記回転円筒(14)は上記槽本体(1)
の内径と固定円筒(5)の外径のほぼ中間に相当する径
を有する上端開口、下端閉成の円筒体で、その筒部、開
口上端面及び閉成下端面をそれぞれ槽本体(1)と固定
円筒(5)の間に間隔をあけて差し合わせ且つ槽本体
(1)及び固定円筒(5)と同心的に位置させた状態
で、該回転円筒(14)の閉成底板中心部を上記回転軸
(11)の下端にネジ(15)により固定し、このよう
にした回転軸(11)の外周面に撹拌翼(19)…を、
固定円筒(5)の内周面上部及び外周面下端部にじゃま
板(20)…をそれぞれ突設し、また回転円筒(14)
の内外両周面及び底板下面に撹拌翼(21)…を、槽本
体(1)内周面下部にじゃま板(22)…をそれぞれ突
設し、それにより上記回転軸(11)と固定円筒(5)
の間に上記凝集汚泥排出口(7)と直接通じる最内側の
環状撹拌室(16)を、上記固定円筒(5)と回転円筒
(14)の間に上記撹拌室(16)と流通方向を180
度屈曲する環状撹拌室(17)を、上記回転円筒(1
4)と槽本体(1)の間に上記撹拌室(17)と180
度屈曲し且つ上記汚泥供給口(3)と直接通じる最外側
の環状撹拌室(18)をそれぞれ形成する。本例では大
略上記撹拌室(18)、(17)が急速撹拌室に、撹拌
室(16)が緩速撹拌室となる。
The rotating cylinder (14) is the tank body (1).
Is a cylindrical body with an upper end opening and a lower end closed, each of which has a diameter substantially corresponding to the inner diameter of the fixed cylinder (5) and the outer diameter of the fixed cylinder (5). And the fixed cylinder (5) with a gap between them, and with the tank body (1) and the fixed cylinder (5) positioned concentrically, the center of the closed bottom plate of the rotary cylinder (14) is It is fixed to the lower end of the rotary shaft (11) with a screw (15), and the stirring blades (19) are attached to the outer peripheral surface of the rotary shaft (11).
Baffle plates (20) are provided on the upper part of the inner peripheral surface and the lower end part of the outer peripheral surface of the fixed cylinder (5), respectively, and the rotating cylinder (14).
Stirring blades (21) are provided on both the inner and outer peripheral surfaces and the bottom surface of the bottom plate, and a baffle plate (22) is projectingly provided at the lower part of the inner peripheral surface of the tank body (1), whereby the rotary shaft (11) and the fixed cylinder (5)
The innermost annular stirring chamber (16) directly communicating with the coagulated sludge discharge port (7) between the fixed cylinder (5) and the rotating cylinder (14) and the flow direction with the stirring chamber (16). 180
The circular stirring chamber (17) that bends once is attached to the rotating cylinder (1
4) and the tank body (1) between the stirring chamber (17) and 180
The outermost annular stirring chambers (18) which are bent once and communicate directly with the sludge supply port (3) are formed. In this example, the stirring chambers (18) and (17) are roughly the rapid stirring chamber, and the stirring chamber (16) is the slow stirring chamber.

【0009】上記汚泥供給口(3)にはラッパ管(2
3)を介して汚泥供給管(24)が接続され、該供給管
(24)を通じてポンプにより汚泥タンクから汚泥が槽
内に圧送され、また上記凝集汚泥排出口(7)には凝集
汚泥排出管(25)が接続され、該排出管(25)が次
工程の脱水機へ延長している。
A trumpet pipe (2) is provided at the sludge supply port (3).
The sludge supply pipe (24) is connected via 3), the sludge is pumped into the tank from the sludge tank by the pump through the supply pipe (24), and the coagulated sludge discharge pipe is connected to the coagulated sludge discharge port (7). (25) is connected and the discharge pipe (25) extends to the dehydrator of the next step.

【0010】汚泥に添加すべき凝集剤としては、一例と
して上記汚泥供給管(24)に接続された注入管(2
6)から無機系凝集剤を、上記ラッパ管(23)に接続
された注入管(27)からカチオン性高分子凝集剤を、
上記槽本体(1)上部に接続された注入管(28)から
アニオン性高分子凝集剤をそれぞれ注入する。(29)
は管内混合機である。
The coagulant to be added to the sludge is, for example, an injection pipe (2) connected to the sludge supply pipe (24).
6) an inorganic flocculant, and a cationic polymer flocculant from an injection pipe (27) connected to the trumpet pipe (23).
An anionic polymer coagulant is injected from an injection pipe (28) connected to the upper part of the tank body (1). (29)
Is an in-pipe mixer.

【0011】上例の作用は次のようである。汚泥を供給
管(24)、ラッパ管(23)を経て槽本体(1)内に
圧送すると共に各注入管(26)、(27)、(28)
を経て所定の凝集剤を注入し、それと共にモータ(9)
の始動により回転軸(11)及び回転円筒(14)を回
転させると、供給された汚泥は急速撹拌室(18)にお
いて撹拌翼(21)…の回転により急速撹拌されつつ上
昇し、ついで撹拌室(18)の上端において180度方
向転換して撹拌室(17)に流れ、そこで撹拌翼(2
1)…により急速撹拌されつつ降下し、これら急速撹拌
により小粒のフロックに凝集される。ついで凝集汚泥は
撹拌室(17)の下端において180度方向転換して撹
拌室(16)に流れ、そこで撹拌翼(19)…により緩
速撹拌されつつ上昇し、この緩速撹拌により小粒の凝集
汚泥が大粒のポーラスな脱水し易いフロックに凝集さ
れ、そして排出口(7)から排出管(25)を経て次の
脱水機へ送られる。
The operation of the above example is as follows. Sludge is pressure-fed into the tank main body (1) through the supply pipe (24) and the trumpet pipe (23), and at the same time, the respective injection pipes (26), (27), (28).
A predetermined coagulant is injected through the motor and with it a motor (9)
When the rotating shaft (11) and the rotating cylinder (14) are rotated by the start of the, the supplied sludge rises in the rapid stirring chamber (18) while being rapidly stirred by the rotation of the stirring blades (21), and then the stirring chamber. At the upper end of (18), it is turned by 180 degrees and flows into the stirring chamber (17), where the stirring blade (2
1) ... descends while being rapidly stirred, and is agglomerated into small-sized flocs by these rapid stirring. Next, the coagulated sludge is turned 180 degrees at the lower end of the stirring chamber (17) and flows into the stirring chamber (16), where it rises while being slowly stirred by the stirring blades (19), and by this slow stirring, small particles are aggregated. The sludge is agglomerated into large, porous flocs that are easily dehydrated, and is sent from the discharge port (7) to the next dehydrator through the discharge pipe (25).

【0012】図2の他の実施例は、図1における回転円
筒(14)の外側に固定円筒(30a)、その外側に撹
拌翼(32a)…、(32a)…を内外両周面に有する
回転円筒(31a)を順次増設して環状撹拌室(33
a)、(34a)を同心的に付加すると共に、じゃま板
を除き、他の構造は図1と実質的に同一の例である。
In another embodiment of FIG. 2, a fixed cylinder (30a) is provided outside the rotary cylinder (14) shown in FIG. 1, and stirring blades (32a) ... (32a) ... Rotating cylinders (31a) are sequentially added to form an annular stirring chamber (33
A) and (34a) are concentrically added, and the structure other than the baffle plate is substantially the same as that of FIG.

【0013】[0013]

【発明の効果】本発明の緩急撹拌槽によれば、槽内に縦
通する回転軸は回転駆動手段に接続された回転軸1本で
足り、従来のようにさらに別の減速機構を備える必要が
なくなるばかりでなく、各撹拌室が回転軸を中心に同心
的に連続しているので従来槽のような強固な支持構造が
不要となり、それにより槽全体を安価に提供することが
できる利点がえられ、しかも撹拌においては、同心的に
配置された各撹拌室が順次流通方向を180度屈曲転換
して連通しているから、原液全体について十分な撹拌混
合を果すことができるのであって、その使用価値はきわ
めて高いのである。
According to the slow stirring tank of the present invention, only one rotary shaft connected to the rotary driving means is required as the rotary shaft extending longitudinally in the tank, and it is necessary to provide another speed reducing mechanism as in the conventional case. Not only does the stirring chamber disappear, but since each stirring chamber is concentrically continuous around the rotation axis, there is no need for a strong support structure like the conventional tank, which provides the advantage that the entire tank can be provided at low cost. In addition, in stirring, since the respective concentrically arranged stirring chambers are sequentially connected by bending and changing the flow direction by 180 degrees, it is possible to achieve sufficient stirring and mixing for the entire stock solution. Its utility value is extremely high.

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

【図1】縦断面図である。FIG. 1 is a vertical sectional view.

【図2】他の実施例の一部省略縦断面図である。FIG. 2 is a partially omitted vertical sectional view of another embodiment.

【符号の説明】[Explanation of symbols]

1、1a 槽本体 3、3a 汚泥供給口 5、5a、30a 固定円筒 7、7a 凝集汚泥排出口 9 モータ 11、11a 回転軸 14、14a、31a 回転円筒 16、16a、17、17a、18、18a、33a、
34a 撹拌室 19、19a、21、21a、32a 撹拌翼
1, 1a Tank main body 3, 3a Sludge supply port 5, 5a, 30a Fixed cylinder 7, 7a Coagulated sludge discharge port 9 Motor 11, 11a Rotating shaft 14, 14a, 31a Rotating cylinder 16, 16a, 17, 17a, 18, 18a , 33a,
34a Stirring chamber 19, 19a, 21, 21a, 32a Stirring blade

───────────────────────────────────────────────────── フロントページの続き (72)発明者 立松 文之 愛知県名古屋市守山区大字小幡字池下53番 地 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Fumiyuki Tatematsu 53 Ikeshita, Obata, Ohata, Moriyama-ku, Nagoya, Aichi

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 槽本体内に、回転駆動手段に接続された
1本の回転軸を縦通し、 上記槽本体内において、一端を開口し他端を閉成する互
に径の異なる1または複数の回転円筒を、上記回転軸の
外側に順次同心的位置関係で、該回転軸に固定支持させ
ると共に、一端を閉成し他端を開口する互に径の異なる
1または複数の固定円筒を、上記回転軸と回転円筒の間
または内外回転円筒の間にそれぞれ間隔をあけて差し合
わせた状態で、上記槽本体に固定し、また少くとも上記
回転軸及び回転円筒には撹拌翼をそれぞれ突設し、それ
により上記回転軸及び回転円筒と固定円筒との間に、順
次屈曲して同心的に連通する複数の撹拌室を形成し、 上記複数の撹拌室における最外側の撹拌室に原液供給口
を、最内側の撹拌室に処理液排出口をそれぞれ設けた、
緩急撹拌槽。
1. One or a plurality of rotating shafts connected to a rotation driving means are longitudinally passed through the tank body, and one or a plurality of mutually different diameters are opened at one end and closed at the other end in the tank body. The rotating cylinder is sequentially fixed to the outside of the rotating shaft in a concentric positional relationship and fixedly supported on the rotating shaft, and one or a plurality of fixed cylinders having different diameters that are closed at one end and open at the other end, The rotary shaft and the rotary cylinder, or the inner and outer rotary cylinders are fixed to the tank body while being fitted with a gap therebetween, and at least the stirring blades are provided on the rotary shaft and the rotary cylinder, respectively. As a result, between the rotary shaft and the rotary cylinder, and the fixed cylinder, a plurality of stirring chambers that are sequentially bent and communicate with each other concentrically are formed, and a stock solution supply port is provided in the outermost stirring chamber of the plurality of stirring chambers. The process liquid discharge ports are provided in the innermost stirring chambers. ,
A gentle stirring tank.
JP4121088A 1992-04-16 1992-04-16 Slow and fast stirring tank Expired - Fee Related JP2900296B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4121088A JP2900296B2 (en) 1992-04-16 1992-04-16 Slow and fast stirring tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4121088A JP2900296B2 (en) 1992-04-16 1992-04-16 Slow and fast stirring tank

Publications (2)

Publication Number Publication Date
JPH05293349A true JPH05293349A (en) 1993-11-09
JP2900296B2 JP2900296B2 (en) 1999-06-02

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
JP4121088A Expired - Fee Related JP2900296B2 (en) 1992-04-16 1992-04-16 Slow and fast stirring tank

Country Status (1)

Country Link
JP (1) JP2900296B2 (en)

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JP2007237014A (en) * 2006-03-06 2007-09-20 Hitachi Plant Technologies Ltd Stirring device
WO2008032422A1 (en) * 2006-09-12 2008-03-20 Tomoe Engineering Co., Ltd. Flocculator
JP2009534171A (en) * 2006-04-22 2009-09-24 バイエル・テクノロジー・サービシーズ・ゲゼルシャフト・ミット・ベシュレンクテル・ハフツング Reactor
JP2012512017A (en) * 2008-12-17 2012-05-31 マシネンファブリーク グスタフ アイリッヒ ゲーエムベーハー ウント コー. カーゲー Mixer with rotating mixing vessel
JP2013071097A (en) * 2011-09-29 2013-04-22 Yoichi Chiba Crystallizer
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CN106110986A (en) * 2016-07-22 2016-11-16 成都羿博智能设备有限公司 Double-deck free paddle stirrer
CN108057411A (en) * 2018-01-18 2018-05-22 江西金利达钾业有限责任公司 A kind of potassium nitrate reaction kettle
JP2018140389A (en) * 2017-02-24 2018-09-13 オルガノ株式会社 Coagulator
JP2018202328A (en) * 2017-06-05 2018-12-27 オルガノ株式会社 Coagulator
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Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0871306A (en) * 1994-09-02 1996-03-19 Sankei Kk Granulation tank
JP2007237014A (en) * 2006-03-06 2007-09-20 Hitachi Plant Technologies Ltd Stirring device
JP2009534171A (en) * 2006-04-22 2009-09-24 バイエル・テクノロジー・サービシーズ・ゲゼルシャフト・ミット・ベシュレンクテル・ハフツング Reactor
KR100724600B1 (en) * 2006-05-29 2007-06-04 (주)흥원피앤엠 A mixing apparatus
KR100728300B1 (en) * 2006-07-14 2007-06-13 (주)에코데이 Apparatus for egitating chemicals of wastewater treatment
WO2008032422A1 (en) * 2006-09-12 2008-03-20 Tomoe Engineering Co., Ltd. Flocculator
US9694331B2 (en) 2008-12-17 2017-07-04 Maschinenfabrik Gustav Eirich Gmbh & Co. Kg Mixer having rotating mixing container
JP2012512017A (en) * 2008-12-17 2012-05-31 マシネンファブリーク グスタフ アイリッヒ ゲーエムベーハー ウント コー. カーゲー Mixer with rotating mixing vessel
JP2013071097A (en) * 2011-09-29 2013-04-22 Yoichi Chiba Crystallizer
CN106040081A (en) * 2016-07-22 2016-10-26 成都羿博智能设备有限公司 Water supply type stirrer
CN106110986A (en) * 2016-07-22 2016-11-16 成都羿博智能设备有限公司 Double-deck free paddle stirrer
CN106110986B (en) * 2016-07-22 2018-10-09 安徽明光市瑞升机械有限公司 The double-deck free paddle stirrer
JP2018140389A (en) * 2017-02-24 2018-09-13 オルガノ株式会社 Coagulator
US11406919B2 (en) 2017-02-24 2022-08-09 Organo Corporation Flocculation and sedimentation apparatus
JP2018202328A (en) * 2017-06-05 2018-12-27 オルガノ株式会社 Coagulator
CN108057411A (en) * 2018-01-18 2018-05-22 江西金利达钾业有限责任公司 A kind of potassium nitrate reaction kettle

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