JPH0687959B2 - mixer - Google Patents

mixer

Info

Publication number
JPH0687959B2
JPH0687959B2 JP12067790A JP12067790A JPH0687959B2 JP H0687959 B2 JPH0687959 B2 JP H0687959B2 JP 12067790 A JP12067790 A JP 12067790A JP 12067790 A JP12067790 A JP 12067790A JP H0687959 B2 JPH0687959 B2 JP H0687959B2
Authority
JP
Japan
Prior art keywords
communication hole
fluid
mixer
mixing element
mixing
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 - Fee Related
Application number
JP12067790A
Other languages
Japanese (ja)
Other versions
JPH0416222A (en
Inventor
行雄 本望
義衛 繪畑
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.)
GENERAL RESEARCH INSTITUTE OF TECHNICAL DEVELOPMENT CO. LTD.
Original Assignee
GENERAL RESEARCH INSTITUTE OF TECHNICAL DEVELOPMENT 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 GENERAL RESEARCH INSTITUTE OF TECHNICAL DEVELOPMENT CO. LTD. filed Critical GENERAL RESEARCH INSTITUTE OF TECHNICAL DEVELOPMENT CO. LTD.
Priority to JP12067790A priority Critical patent/JPH0687959B2/en
Publication of JPH0416222A publication Critical patent/JPH0416222A/en
Publication of JPH0687959B2 publication Critical patent/JPH0687959B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明はミキサーに係り、特に管体の流路内を流れる数
種類の流体を、その管体内で流しながら混合してなるミ
キサーに関する。
Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a mixer, and more particularly to a mixer obtained by mixing several kinds of fluids flowing in a flow path of a pipe while flowing in the pipe.

〔従来の技術〕[Conventional technology]

一般に、管体の流路内に複数のミキシングエレメントを
収納し、これらミシングエレメントにより、流路内を流
れる数種類の流体を混合してなるミキサーは知られてい
る。
Generally, a mixer is known in which a plurality of mixing elements are housed in the flow path of a tubular body, and several kinds of fluids flowing in the flow path are mixed by these mixing elements.

この種の従来のミキサーは、それぞれ外周部に右捻り、
左捻りいずれかの螺旋状の羽根を有する複数のミキシン
グレメントを有している。これらミキシングエレメント
は、管体の流路内に右捻り、左捻り交互に直列に配置さ
れ、管体の流路内を流れる流体は右捻り、左捻りの反転
力を交互に受けながら、その羽根の間を流れるうちに徐
々に混合されるようになっている。
Conventional mixers of this kind are twisted right around the outside,
It has multiple mix increments with either a left-handed spiral wing. These mixing elements are arranged in series in the flow passage of the pipe in a right-handed twist and a left-handed twist, and the fluid flowing in the flow passage of the pipe body is subjected to the right-handed and left-handed inversion forces alternately, and its blades are rotated. It gradually mixes as it flows through the space.

〔発明が解決しようとする課題〕[Problems to be Solved by the Invention]

しかしながら、従来のミキサーでは、螺旋状の羽根は1
枚または2枚程度であり、構造的にも、外周部に余り多
くの羽根を形成することはできないので、流体の混合効
率はそれ程よくないという問題がある。これを解消する
ために、従来では、管体の流路内に、多数のミキシング
エレメントを直列に配置して流体の混合を繰り返すよう
にしているが、これでは管体の全長が長くなり、ミキサ
ーの大型化につながるという問題がある。
However, in conventional mixers, one spiral blade
The number of blades is about one or two, and structurally, too many blades cannot be formed on the outer peripheral portion, so that there is a problem that the fluid mixing efficiency is not so good. In order to solve this, conventionally, many mixing elements are arranged in series in the flow path of the pipe body to repeat fluid mixing, but this increases the overall length of the pipe body and the mixer. There is a problem that it will lead to the increase in size.

そこで、本発明の目的は、上述した従来の技術が有する
問題点を解消し、管体の全長を長くすることなく、流体
の混合効率を格段に向上させることのできるミキサーを
提供することにある。
Therefore, an object of the present invention is to solve the problems of the above-mentioned conventional techniques and to provide a mixer capable of significantly improving the mixing efficiency of fluids without increasing the overall length of the tubular body. .

〔課題を解決するための手段〕[Means for Solving the Problems]

上記目的を達成するために、請求項1記載の発明は、管
体の流路内にミキシングエレメントを収納し、このミキ
シングエレメントにより、流路内を流れる流体を混合し
てなるミキサーにおいて、ミキシングエレメントは、そ
の外周部に上流側に連通する入口室を、内周部に下流側
に連通する出口室をそれぞれ有し、その周壁部には、軸
方向に間隔をあけて、入口室及び出口室を連通する少な
くとも2列の連通孔を有し、各列の連通孔のうち上流側
の第1連通孔は第1方向旋回力を流体に付与するように
穿孔し、下流側の第2連通孔は第1方向旋回力とほぼ逆
向きの第2方向旋回力を流体に付与するように穿孔して
なることを特徴とするものである。
In order to achieve the above-mentioned object, the invention according to claim 1 is a mixing element in which a mixing element is housed in a channel of a tubular body, and the fluid flowing in the channel is mixed by the mixing element. Has an inlet chamber communicating with the upstream side at its outer peripheral portion and an outlet chamber communicating with the downstream side at its inner peripheral portion, and its peripheral wall portion has an inlet chamber and an outlet chamber at axial intervals. There is at least two rows of communication holes that communicate with each other, and among the communication holes of each row, the first communication hole on the upstream side is perforated so as to impart the first direction turning force to the fluid, and the second communication hole on the downstream side. Is characterized in that it is perforated so as to apply a second direction turning force substantially opposite to the first direction turning force to the fluid.

また、請求項2記載の発明は、ミキシングエレメントの
周壁部には、第1連通孔と第2連通孔との間に位置して
入口室及び出口室を連通する第3連通孔を有し、この第
3連通孔は半径方向噴射力を流体に付与するように穿孔
してなることを特徴とするものである。
The invention according to claim 2 has a third communication hole, which is located between the first communication hole and the second communication hole and which communicates the inlet chamber and the outlet chamber, in the peripheral wall portion of the mixing element, The third communication hole is characterized in that it is formed so as to impart a radial jet force to the fluid.

〔作 用〕[Work]

請求項1記載の発明によれば、上流側の第1連通孔を通
して出口室内に流入する流体は、流路内の流れに直交す
る垂直面内にて第1方向旋回力を受け、先ずこの過程で
充分に撹拌され、次に、下流側の第2連通孔を通った流
体は、第2方向旋回力を受け、この過程で充分に撹拌さ
れるとともに、この流れは、出口室内で上流側の第1方
向旋回力を受けた流れに衝突して、この第1方向旋回力
を打ち消すように作用し、出口室内の流れを層流にす
る。よって上流側からの流体は充分に撹拌、混合され、
層流となって下流側に排出される。
According to the invention described in claim 1, the fluid flowing into the outlet chamber through the first communication hole on the upstream side receives the first direction swirling force in the vertical plane orthogonal to the flow in the flow path, and first, this process The fluid passing through the second communication hole on the downstream side is swirled in the second direction and sufficiently stirred in this process. It collides with the flow that has received the first-direction turning force, and acts so as to cancel this first-direction turning force, so that the flow in the outlet chamber becomes a laminar flow. Therefore, the fluid from the upstream side is sufficiently stirred and mixed,
It becomes a laminar flow and is discharged downstream.

また、請求項2記載の発明によれば、第3連通孔を通っ
た流体は、半径方向に噴出されて、上流側で充分に撹拌
されて流れてくる流体に衝突する。この過程では、流体
の拡散、混合がなされ、これによれば、流体が拡散され
る分だけ上述のものより混合効率に優れる。
According to the second aspect of the invention, the fluid that has passed through the third communication hole is ejected in the radial direction and collides with the fluid that is sufficiently stirred on the upstream side and flows. In this process, the fluids are diffused and mixed, and thus the mixing efficiency is higher than that described above because the fluids are diffused.

〔実施例〕〔Example〕

以下、本発明によるミキサーの一実施例を添付図面を参
照して説明する。
Hereinafter, an embodiment of a mixer according to the present invention will be described with reference to the accompanying drawings.

第1図において、1は管体を示し、この管体1の両端に
は管路接続用にめねじ1a,1aが形成されている。この管
体1の内周には環状座部1bが一体的に形成され、この環
状座部1bに位置決めされて、該管体1の流路1c内には3
個のミキシングエレメント2が順に収納されている。
In FIG. 1, reference numeral 1 denotes a tubular body, and female threads 1a, 1a are formed at both ends of the tubular body 1 for connecting a pipeline. An annular seat portion 1b is integrally formed on the inner circumference of the tubular body 1, and is positioned in the annular seat portion 1b.
The individual mixing elements 2 are stored in order.

このミキシングエレメント2は、第2図からも明らかな
ように、鍔部2aと筒部2bとを一体的に有する部材であ
り、この鍔部2aの外周部は管体1の内周部に嵌め合され
ている。また、ミキシングエレメント2の間には該エレ
メント2の間隔を規制するスリーブ3が介装されてお
り、このスリーブ3の外周部は管体1の内周部に嵌め合
されている。
As is apparent from FIG. 2, this mixing element 2 is a member integrally having a collar portion 2a and a cylindrical portion 2b, and the outer peripheral portion of the collar portion 2a is fitted to the inner peripheral portion of the tubular body 1. Have been combined. Further, a sleeve 3 for regulating the interval between the mixing elements 2 is interposed between the mixing elements 2, and the outer peripheral portion of the sleeve 3 is fitted to the inner peripheral portion of the tubular body 1.

ミキシングエレメント2は、その外周部に、上流側に連
通する入口室を有しており、この例では、管体1の内周
部またはスリーブ3の内周部と、筒部2bの外周部との間
に環状の入口室5が形成されている。また、このミキシ
ングエレメント2は、その内周部に、下流側に連通する
出口室を有しており、この例では、筒部2bの内側に断面
円形の出口室7が穿設されている。
The mixing element 2 has an inlet chamber communicating with the upstream side on the outer peripheral portion thereof, and in this example, the inner peripheral portion of the tubular body 1 or the inner peripheral portion of the sleeve 3 and the outer peripheral portion of the tubular portion 2b. An annular inlet chamber 5 is formed between them. Further, the mixing element 2 has an outlet chamber communicating with the downstream side on the inner peripheral portion thereof, and in this example, an outlet chamber 7 having a circular cross section is bored inside the cylindrical portion 2b.

ミキシングエレメント2の筒部2bの周壁部には、軸方向
に間隔をあけて、入口室5と出口室7とを連通する3列
の連通孔11,12,13が穿設されている。各列の連通孔のう
ち上流側の第1連通孔11は、第3図に示すように、内周
円15のほぼ接線方向に沿って穿孔され、下流側の第2連
通孔13は、第5図に示すように、内周円15のほぼ接線方
向に沿って、しかも第1連通孔11とほぼ逆向きに穿孔さ
れている。また、第1、第2連通孔11,13の中間に位置
する第3連通孔12は、第4図に示すように、内周円15の
ほぼ半径方向に沿って穿孔されている。
Three rows of communication holes 11, 12, 13 for communicating the inlet chamber 5 and the outlet chamber 7 are provided in the peripheral wall portion of the cylindrical portion 2b of the mixing element 2 at intervals in the axial direction. Of the communication holes in each row, the first communication hole 11 on the upstream side is drilled along the tangential direction of the inner circumference circle 15 as shown in FIG. 3, and the second communication hole 13 on the downstream side is As shown in FIG. 5, the inner circumferential circle 15 is bored substantially along the tangential direction and in a direction substantially opposite to the first communication hole 11. Further, as shown in FIG. 4, the third communication hole 12 located in the middle of the first and second communication holes 11 and 13 is bored substantially along the radial direction of the inner circumference circle 15.

次に、本実施例の作用を説明する。Next, the operation of this embodiment will be described.

この種のミキサーは、配管系の途中に接続されるもので
あり、上流側から供給される数種類の流体は3個のミキ
シングエレメント2を通過する間に混合されてそのまゝ
下流側に排出される。
This kind of mixer is connected in the middle of the piping system, and several kinds of fluids supplied from the upstream side are mixed while passing through the three mixing elements 2 and discharged to the downstream side. It

これを詳述すると、供給される流体は入口室5に一時的
に貯留されたのち、3列の連通孔11,12,13を通して出口
室7に排出される。
More specifically, the supplied fluid is temporarily stored in the inlet chamber 5 and then discharged to the outlet chamber 7 through the three rows of communication holes 11, 12, and 13.

上流側の第1連通孔11を通して出口室7に排出される流
体は、流路1c内の流れに直交する垂直面内にて、第3図
に示すように、図中で時計方向に第1方向旋回力を受
け、先ずこの過程で充分に撹拌される。次に、第3連通
孔12を通った流体は、第4図に示すように、内周円15の
半径方向に噴出され、上流側で充分に撹拌されて流れて
くる流体に衝突し、拡散混合される。
The fluid discharged into the outlet chamber 7 through the first communication hole 11 on the upstream side is first in the clockwise direction in the drawing as shown in FIG. 3 in the vertical plane orthogonal to the flow in the flow path 1c. It receives a directional turning force and is first thoroughly agitated in this process. Next, as shown in FIG. 4, the fluid that has passed through the third communication hole 12 is ejected in the radial direction of the inner circumferential circle 15, is sufficiently stirred on the upstream side, collides with the flowing fluid, and diffuses. Mixed.

下流側の第2連通孔13を通った流体は、第5図に示すよ
うに、図中で反時計方向に第2方向旋回力を受け、この
過程で充分に撹拌されるとともに、この流れは、出口室
7内で上流側の第1方向旋回力を受けた流れに衝突し
て、この第1方向旋回力を打ち消すように作用する。
As shown in FIG. 5, the fluid that has passed through the second communication hole 13 on the downstream side receives the second direction turning force in the counterclockwise direction in the figure, is sufficiently agitated in this process, and this flow is In the outlet chamber 7, it collides with the flow that has received the first-direction turning force on the upstream side, and acts so as to cancel the first-direction turning force.

しかして、この実施例によれば、ミキシングエレメント
2に、3方向に向かう3列の連通孔11,12,13が穿設され
ており、これら3列の連通孔を通じて、流体の撹拌、拡
散、混合がなされるので、従来のものと比べて、ミキサ
ーの混合効率は格段に向上する。また、これによれば、
下流側に向かう流れは乱れの少ない流れとなるので、こ
のミキサーの下流には、流れを層流化するための装置な
どが不要になるという利点がある。
Thus, according to this embodiment, the mixing element 2 is provided with three rows of communication holes 11, 12 and 13 extending in three directions. Through these three rows of communication holes, fluid agitation, diffusion, Since the mixing is performed, the mixing efficiency of the mixer is remarkably improved as compared with the conventional one. And according to this,
Since the flow toward the downstream side becomes a flow with little turbulence, there is an advantage that a device for laminarizing the flow is not required downstream of this mixer.

この実施例では、連通孔の数はそれぞれ12個であり、連
通孔の列は3列であるので、1つのミキシングエレメン
ト2の孔の総数は36個となり、36分割で流体が混合され
ることになる。これに対して、従来のものでは、ミキシ
ングエレメントの外周部の螺旋羽根の総数は、せいぜい
多くて2枚であるので、1つのミキシングエレメントで
は、流体は2分割されるだけである。
In this embodiment, the number of communication holes is 12 each, and the number of communication holes is 3, so that the total number of holes of one mixing element 2 is 36, and the fluid is mixed in 36 divisions. become. On the other hand, in the conventional case, the total number of spiral blades on the outer peripheral portion of the mixing element is at most two, so that one mixing element only divides the fluid into two parts.

この比較からも明らかなように、本実施例では、流体を
分割する数が大幅に増大するので、従来のものと比べ
て、流体の混合効率を格段に向上させることができる。
したがって、ミキサーを極めてコンパクトに製造するこ
とができる。
As is clear from this comparison, in the present embodiment, the number of divided fluids is significantly increased, so that the mixing efficiency of fluids can be significantly improved as compared with the conventional one.
Therefore, the mixer can be manufactured extremely compactly.

この実施例では、例えば、連通孔の数をそれぞれn個と
し、連通孔の列をl列とすれば、孔の総数はn×l個と
なり、n×l分割で流体が混合されることになる。すな
わち、このミキサーは、nとlの数を増やすことにより
簡単に混合効率を向上させることができる。
In this embodiment, for example, if the number of communicating holes is n and the row of communicating holes is l, the total number of holes is n × l, and the fluid is mixed in n × l division. Become. That is, this mixer can easily improve the mixing efficiency by increasing the numbers of n and l.

また、ミキシングエレメント2の数を増し、管体1内に
m個のミキシングエレメント2を直列に収納したとすれ
ば、孔の総数はn×l×m個であるが、ミキシングエレ
メント2を通る毎に流体は細かく分割されるので、これ
ら過程では、流体は(n×l)m分割で混合されること
になる。このように、このミキサーは、ミキシングエレ
メント2の数を増大させることにより、飛躍的に混合効
率を向上させることができる。
If the number of mixing elements 2 is increased and m mixing elements 2 are housed in the tube body 1 in series, the total number of holes is n × l × m, but every time the mixing elements 2 pass through. Since the fluid is finely divided, the fluids are mixed in (n × l) m divisions in these processes. In this way, this mixer can dramatically improve the mixing efficiency by increasing the number of mixing elements 2.

以上、一実施例に基づいて本発明を説明したが、本発明
は、これに限定されるものではない。
The present invention has been described above based on the embodiment, but the present invention is not limited to this.

例えば、第3連通孔12は省略してもよい。この第3連通
孔12は、上述したように、流体を、内周円15の半径方向
に噴出させ、上流側から流れてくる流体に衝突させて、
これを拡散混合させるためのものである。しかして、仮
に、第3連通孔12が省略されていても、第1,2の連通孔1
1,13が穿孔されてさえいれば、拡散の過程はなくなる
が、流体を充分に混合することができるし、しかも乱れ
の少ない混合流体を下流に排出することができる。
For example, the third communication hole 12 may be omitted. As described above, the third communication hole 12 causes the fluid to be ejected in the radial direction of the inner circumferential circle 15 and collide with the fluid flowing from the upstream side,
This is for diffusing and mixing this. Therefore, even if the third communication hole 12 is omitted, the first and second communication holes 1
As long as 1 and 13 are perforated, the diffusion process is eliminated, but the fluids can be mixed well and the mixed fluid with little turbulence can be discharged downstream.

〔発明の効果〕〔The invention's effect〕

以上の説明から明らかなように、請求項1記載の発明に
よれば、ミキシングエレメントは、その外周部に上流側
に連通する入口室を、また内周部に下流側に連通する出
口室をそれぞれ有し、その周壁部には、軸方向に間隔を
あけて、入口室と出口室とを連通する少なくとも2列の
連通孔を有し、各列の連通孔のうち上流側の第1連通孔
は第1方向旋回力を流体に付与するように穿孔し、下流
側の第2連通孔は第1方向旋回力とほぼ逆向きの第2方
向旋回力を流体に付与するように穿孔したから、上流側
から供給される流体は第1,2連通孔を通して入口室から
出口室に流入するので、この過程で充分に撹拌、混合さ
れるとともに、第1,2方向旋回力が衝突して互いの旋回
力が打ち消されるので、層流になって下流側に排出され
る。
As is clear from the above description, according to the invention of claim 1, the mixing element has an inlet chamber communicating with an upstream side at an outer peripheral portion thereof and an outlet chamber communicating with a downstream side at an inner peripheral portion thereof. The peripheral wall portion has at least two rows of communication holes, which communicate with the inlet chamber and the outlet chamber, at intervals in the axial direction, and the first communication hole on the upstream side of the communication holes of each row. Is perforated so as to impart a first direction swirl force to the fluid, and the second communication hole on the downstream side is perforated so as to impart a second direction swirl force substantially opposite to the first direction swirl force to the fluid, Since the fluid supplied from the upstream side flows from the inlet chamber to the outlet chamber through the first and second communication holes, it is sufficiently agitated and mixed in this process, and the swirling forces in the first and second directions collide with each other to cause mutual stirring. Since the turning force is canceled out, it becomes a laminar flow and is discharged to the downstream side.

また、請求項2記載の発明によれば、ミキシングエレメ
ントの周壁部には、第1連通孔と第2連通孔との間に位
置して入口室と出口室とを連通する第3連通孔を有し、
この第3連通孔は半径方向の噴出力を流体に付与するよ
うに穿孔したから、この第3連通孔を通して出口室に噴
出される流体は、第1方向旋回力を付与された流れに衝
突して拡散混合されるので、流体は極めて効率よく混合
される。
According to the second aspect of the invention, the peripheral wall portion of the mixing element is provided with a third communication hole which is located between the first communication hole and the second communication hole and which communicates the inlet chamber and the outlet chamber. Have,
Since the third communication hole is bored so as to impart a radial jet output to the fluid, the fluid ejected into the outlet chamber through the third communication hole collides with the flow to which the first direction swirl force is imparted. The fluids are mixed very efficiently because they are diffusively mixed.

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

第1図は本発明によるミキサーの一実施例を示す縦断面
図、第2図はミキシングエレメントの正面図、第3図は
第2図のIII−III断面図、第4図は第2図のIV−IV断面
図、第5図は第2図のV−V断面図である。 1……管体、1c……流路、2……ミキシングエレメン
ト、3……スリーブ、5……入口室、7……出口室、11
……第1連通孔、12……第3連通孔、13……第2連通
孔。
1 is a vertical sectional view showing an embodiment of the mixer according to the present invention, FIG. 2 is a front view of a mixing element, FIG. 3 is a sectional view taken along the line III-III of FIG. 2, and FIG. 4 is a sectional view of FIG. IV-IV sectional view, FIG. 5 is a VV sectional view of FIG. 1 ... Tube, 1c ... Flow path, 2 ... Mixing element, 3 ... Sleeve, 5 ... Inlet chamber, 7 ... Outlet chamber, 11
...... First communication hole, 12 ...... Third communication hole, 13 ...... Second communication hole.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】管体の流路内にミキシングエレメントを収
納し、このミキシングエレメントにより、流路内を流れ
る流体を混合してなるミキサーにおいて、前記ミキシン
グエレメントは、その外周部に上流側に連通する入口室
を、また内周部に下流側に連通する出口室をそれぞれ有
し、その周壁部には、軸方向に間隔をあけて、前記入口
室と前記出口室とを連通する少なくとも2列の連通孔を
有し、各列の連通孔のうち上流側の第1連通孔は第1方
向旋回力を流体に付与するように穿孔し、下流側の第2
連通孔は第1方向旋回力とほぼ逆向きの第2方向旋回力
を流体に付与するように穿孔してなることを特徴とする
ミキサー。
1. In a mixer in which a mixing element is housed in a flow passage of a tubular body, and the fluid flowing in the flow passage is mixed by the mixing element, the mixing element is connected to an outer peripheral portion thereof on an upstream side. At least two rows that communicate with the inlet chamber and the outlet chamber at intervals in the axial direction on the peripheral wall portion. Of the communication holes of each row, the first communication hole on the upstream side is bored so as to impart the first direction swirl force to the fluid, and the second communication hole on the downstream side.
A mixer characterized in that the communication hole is bored so as to impart a second-direction swirl force, which is substantially opposite to the first-direction swirl force, to the fluid.
【請求項2】前記ミキシングエレメントの周壁部には、
第1連通孔と第2連通孔との間に位置して前記入口室と
前記出口室とを連通する第3連通孔を有し、この第3連
通孔は半径方向の噴出力を流体に付与するように穿孔し
てなることを特徴とする請求項1記載のミキサー。
2. The peripheral wall portion of the mixing element includes:
There is a third communication hole that is located between the first communication hole and the second communication hole and that communicates the inlet chamber and the outlet chamber, and the third communication hole imparts a radial jet output to the fluid. The mixer according to claim 1, wherein the mixer is perforated as described above.
JP12067790A 1990-05-10 1990-05-10 mixer Expired - Fee Related JPH0687959B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12067790A JPH0687959B2 (en) 1990-05-10 1990-05-10 mixer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12067790A JPH0687959B2 (en) 1990-05-10 1990-05-10 mixer

Publications (2)

Publication Number Publication Date
JPH0416222A JPH0416222A (en) 1992-01-21
JPH0687959B2 true JPH0687959B2 (en) 1994-11-09

Family

ID=14792213

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12067790A Expired - Fee Related JPH0687959B2 (en) 1990-05-10 1990-05-10 mixer

Country Status (1)

Country Link
JP (1) JPH0687959B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011141024A (en) * 2009-08-06 2011-07-21 Soken Kogyo Kk Cyclone flow generating gasket, cyclone flow generating joint pipe, and cyclone flow pipeline

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0560524U (en) * 1992-01-23 1993-08-10 株式会社荒井製作所 Fluid mixing equipment
JP5604038B2 (en) * 2008-08-25 2014-10-08 株式会社日立製作所 Reaction apparatus and reaction plant
JP2012030207A (en) * 2010-08-03 2012-02-16 Soken Kogyo Kk Fluid mixer, fluid mixing and transporting channel, and fluid mixing method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011141024A (en) * 2009-08-06 2011-07-21 Soken Kogyo Kk Cyclone flow generating gasket, cyclone flow generating joint pipe, and cyclone flow pipeline

Also Published As

Publication number Publication date
JPH0416222A (en) 1992-01-21

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