JPS60227819A - Fluid mixing apparatus - Google Patents

Fluid mixing apparatus

Info

Publication number
JPS60227819A
JPS60227819A JP59083695A JP8369584A JPS60227819A JP S60227819 A JPS60227819 A JP S60227819A JP 59083695 A JP59083695 A JP 59083695A JP 8369584 A JP8369584 A JP 8369584A JP S60227819 A JPS60227819 A JP S60227819A
Authority
JP
Japan
Prior art keywords
conduit
fluid
nozzle
mixing
main fluid
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
JP59083695A
Other languages
Japanese (ja)
Other versions
JPH0139815B2 (en
Inventor
Tadashi Ogura
小倉 忠
Izuru Owaki
大脇 出
Masayuki Yasuda
安田 昌之
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.)
Noritake Co Ltd
Original Assignee
Noritake 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 Noritake Co Ltd filed Critical Noritake Co Ltd
Priority to JP59083695A priority Critical patent/JPS60227819A/en
Publication of JPS60227819A publication Critical patent/JPS60227819A/en
Publication of JPH0139815B2 publication Critical patent/JPH0139815B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40Static mixers
    • B01F25/42Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
    • B01F25/43Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
    • B01F25/431Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor
    • B01F25/4314Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor with helical baffles
    • B01F25/43141Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor with helical baffles composed of consecutive sections of helical formed elements

Landscapes

  • Chemical & Material Sciences (AREA)
  • Dispersion Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)

Abstract

PURPOSE:To mix fluid uniformly and to eliminate the vibration noise by providing a nozzle to a conduit as an inner pipe of double tube structure and injecting the injection fluid into the conduit from the position wherein the tip of the nozzle is projected to the shaft core side other than the inside peripheral wall of the conduit. CONSTITUTION:The kineti energy and the thermal energy incorporated in the steam itself which is dispersed and injected from four sides into the inside of a conduit 10 from nozzles 13a-13d are allowed to collide against main fluid from the radiation directions and the mixing is accelerated with the impact energy of this moment. The mixed fluid of the stream and the main fluid is twisted along the side face of spiral elements 15-20, dispersed uniformly thereby and separated into two at each boundary region of the spiral elements 15-20 and the mixing is accelerated by repeating these division, substitution and superposition. Further, the degree of projection of the above-mentioned nozzles is preferably >=5mm..

Description

【発明の詳細な説明】 (技術分野) 本発明は、主流体を通過させるための導管に注入波体の
注入口を形成した流体混合装置に関し、特に高粘性主流
体に対しスチーム等のガス状流体を混合する流体混合装
置に関する。
DETAILED DESCRIPTION OF THE INVENTION (Technical Field) The present invention relates to a fluid mixing device in which an inlet for an injection wave body is formed in a conduit for passing a main fluid. The present invention relates to a fluid mixing device for mixing fluids.

(技術的背景) 主流体に他の種類の流体を注入して混合する方法として
は1例えばラインミキサーの流入口側にT字管、ノズル
付1字管あるいはマルチ注入口等を有する管等の注入口
部を備えた管を接続し、主流体に他の流体を注入口から
注入して得られる合成流を後続のラインミキサーにより
混合する方法が知られている。
(Technical background) As a method of injecting and mixing other types of fluid into the main flow, there are 1 methods, for example, using a T-shaped pipe, a single-shaped pipe with a nozzle, or a pipe with multiple injection ports on the inlet side of the line mixer. A method is known in which a pipe equipped with an injection port is connected, and another fluid is injected into the main flow through the injection port, and the resultant synthetic stream is mixed by a subsequent line mixer.

このうち、T字管またはノズル付1字管は、注入口から
取入れる例えばスチームの流量が主流体に対して微少で
ある場合に用いられ、スチーム量が増大すると混合がほ
とんど行われず、衝撃音や振動が発生しやすくなって配
管を破損する危険がある。
Among these, a T-tube or a single-tube with a nozzle is used when, for example, the flow rate of steam taken in from the inlet is very small relative to the main flow, and when the amount of steam increases, there is little mixing, resulting in impact noise. There is a risk of damage to the pipes due to vibrations that occur more easily.

そこで、インジェクタを用いて弔−またはマルチノズル
方式を採るとともに、主流体をある程度以上の流速にし
て流れの状態を乱流にし、注入流体との混合を行なうも
のが知られている。しかし、この装置の出口直後では完
全に混合が行なわれていないため、主流体は均一な温度
分布をもった液になっていない。また主流体の量が少な
くなりある程度以下の流速になると、乱流による混合作
用が低下するため注入流体との混合不足が発生し衝撃音
や振動が起きやすくなる。
Therefore, it is known to adopt a nozzle or multi-nozzle system using an injector, and to increase the flow velocity of the main fluid to a certain level or higher to make the flow turbulent and mix it with the injected fluid. However, since complete mixing is not performed immediately after the exit of this device, the main fluid does not have a uniform temperature distribution. Further, when the amount of the main fluid decreases and the flow velocity becomes below a certain level, the mixing effect due to turbulence decreases, resulting in insufficient mixing with the injected fluid, which tends to cause impact sounds and vibrations.

この騒音のレベルはある特定の環境下では許容Sれがた
いものであり、騒音公害として問題となっていた。
This noise level is unacceptable under certain circumstances and has become a problem as noise pollution.

(発明の目的) この発明は、F記問題点を解決するためになされたもの
で、導管にスチームなどの注入流体を噴射し均一に混合
すると共にその際に発生する振動騒音を抑制することを
目的とする。
(Purpose of the Invention) This invention was made to solve the problem described in F, and is aimed at injecting an injection fluid such as steam into a conduit to mix it uniformly and suppressing the vibration noise generated at that time. purpose.

(発明の構成概要および作用) 本発明の流体混合装置の第1の態様は、主流体を流通す
る導管と、該導管の内部にその軸心線方向に配設したス
タティックミキサエレメントと、該導管の外周で二重管
構造を構成し注入流体の注入口を有する外管と、外管の
内部で導管に貫通しかつ導管内周壁から軸心方向に突出
するノズルからなる。
(Structure outline and operation of the invention) A first aspect of the fluid mixing device of the present invention includes a conduit through which a main fluid flows, a static mixer element disposed inside the conduit in the axial direction thereof, and a static mixer element disposed inside the conduit in the axial direction of the conduit. It consists of an outer tube that has a double-tube structure on its outer periphery and has an inlet for injection fluid, and a nozzle that penetrates the conduit inside the outer tube and projects in the axial direction from the inner circumferential wall of the conduit.

導管に供給される注入流体は、4込管内周壁から軸心側
に突出する複数のノズルに案内されて導管内部の主流体
の流速の大きな部分に噴射されるので、均一に分散混合
されると共に噴射部に外部に洩れる騒音は、著しく低減
する。
The injection fluid supplied to the conduit is guided by a plurality of nozzles protruding from the inner circumferential wall of the four-way tube toward the axis and is injected into the portion of the main fluid inside the conduit where the flow velocity is high, so that it is uniformly dispersed and mixed. Noise leaking to the outside from the injection section is significantly reduced.

本発明の第2の態様として第1の態様に付加して、該ノ
ズルに外部信号に基づいて開閉する自動弁を設け、この
自動弁を該装置操作時に適宜開閉するようにしてもよい
。始動時には上流側に備えつけた自動弁から順に開弁し
、逆に停止時には下流側に備え伺けた自動弁から順次閉
弁するように設定すれば、とくに自動弁の停止の際に主
流体がノズルから注入目側に逆流するを防止する。また
主流体の流敬に応じて、或いは騒音、混合効果等を考慮
して、操作処理中に適当数のノズルを開又は閉とするこ
とにより最適の状態で操作できる。
As a second aspect of the present invention, in addition to the first aspect, the nozzle may be provided with an automatic valve that opens and closes based on an external signal, and this automatic valve may be opened and closed as appropriate when the device is operated. If you set the automatic valves installed on the upstream side to open in sequence when starting, and conversely to close the automatic valves installed downstream in sequence when stopped, the main fluid will flow to the nozzle when the automatic valves stop. Prevents backflow from the injection site. In addition, by opening or closing an appropriate number of nozzles during operation processing, depending on the flow rate of the main fluid, or taking noise, mixing effects, etc. into consideration, the operation can be performed in an optimal state.

(実施例) 本発明の実施例を図面にもとづいて説明する。(Example) Embodiments of the present invention will be described based on the drawings.

第1図〜第3図は、第1の実施例をあられし、図中、1
0は主流体を図で左方から右方に向けて流す導管、11
は注入流体としてのスチームを図の上方から取入れる注
入口である。
Figures 1 to 3 show the first embodiment;
0 is a conduit through which the main fluid flows from the left to the right in the figure, 11
is an inlet that takes in steam as the injection fluid from above in the figure.

注入口11の下流側は、導管10の外周を包囲して導管
lOと二重管構造を構成する外管12と連通ずる。この
外管12の内部には、導管IOの外周に第3図のように
放射状に略同心円−ヒで4個のノズル13 (13a−
13d)が略同−軸心方向にその先端を向けて設けられ
、この4個のノズル13a〜13dを1セツトとしてこ
れを導管10の軸線方向に略等間隔で6箇所に配設する
The downstream side of the injection port 11 communicates with an outer tube 12 that surrounds the outer periphery of the conduit 10 and forms a double tube structure with the conduit lO. Inside this outer pipe 12, four nozzles 13 (13a-
13d) are provided with their tips facing substantially in the same axial direction, and these four nozzles 13a to 13d are arranged as one set at six locations at substantially equal intervals in the axial direction of the conduit 10.

(なおノズルの分配は円周方向、軸方向共に、導管の口
径等に応じて分散混合効果、騒音抑1F効果に基づいて
選択される。) 導管10の内部には、導管lOを軸線方向に2分割しな
がら軸線周りに略180°ねじれるスパイラルニレメン
)15〜20が合計6個配設され、これらスパイラルエ
レメント15〜20の境界域は、互いの軸端が直交する
ように連続して設けられる。
(Note that the nozzle distribution is selected in both the circumferential direction and the axial direction based on the dispersive mixing effect and noise suppression effect according to the diameter of the conduit, etc.) A total of six spiral elements 15 to 20 are arranged, which are divided into two and twisted approximately 180 degrees around the axis, and the boundary areas of these spiral elements 15 to 20 are arranged continuously so that their shaft ends are perpendicular to each other. It will be done.

ノズル13a〜13dから導管10の内部に四方から分
散注入されたスチームは、それ自体のもつ運動エネルギ
と熱エネルギを放射方向から主流体に衝突させ、そのと
きの衝撃エネルギで混合を促進する。これらスチームと
主流体の混合流体は、スパイラルエレメント15〜20
の側面に沿ってねじられることにより均一に分散され、
またスパイラルニレメン)15〜20の境界域ごとに2
つに分断されて、これら分割、置換、重ね合せを繰り返
してミキシングを促す。
The steam dispersedly injected into the conduit 10 from all sides from the nozzles 13a to 13d causes its own kinetic energy and thermal energy to collide with the main fluid from the radial direction, and the impact energy at that time promotes mixing. These mixed fluids of steam and main fluid are mixed with spiral elements 15 to 20.
is evenly distributed by being twisted along the sides of the
Also spiral elmmen) 2 for every 15 to 20 boundary areas
These divisions, substitutions, and superimpositions are repeated to promote mixing.

ノズルの突出の程度は少くとも5mm以にが好Iしく、
導管の管径に応じて、その約1/12〜1 、/ 4程
度(より好ましイはl/8〜l /’ 6 ’)とする
ことが好ましい。ノズル口径も約5+om−15mmの
範囲で適宜選択される(但し導管口径に対応してさらに
可変である)、ノズルの角度は導管軸に直交又は斜交し
て配することができ、主流体の流れの向きにや一斜交と
することも混合効果の点から好ましい。
The degree of protrusion of the nozzle is preferably at least 5 mm,
Depending on the diameter of the conduit, it is preferably about 1/12 to 1/4 of that (more preferably 1/8 to 1/'6'). The nozzle diameter is also appropriately selected within the range of about 5+ om - 15 mm (however, it is further variable depending on the conduit diameter).The nozzle angle can be arranged perpendicularly or obliquely to the conduit axis, and the It is also preferable from the viewpoint of the mixing effect that the flow direction is diagonal or diagonal.

第4図は第2の実施例をあられし、第1図の構成と基本
的には同じであるが、さらにノズル(13a−13d)
を開閉する自動弁21(21a〜21e)が設けられる
FIG. 4 shows a second embodiment, which is basically the same as the configuration shown in FIG.
Automatic valves 21 (21a to 21e) that open and close are provided.

この実施例では、導管軸方向に5列に合計20個の自動
弁21が配置される。第5 (A)(B)図のように、
これらの自動弁21a〜21eはエアシリンダ22に供
給される外部信号としてのエア信号により開閉し、始動
時には上流側から自動弁21 a 、 2 l b 、
−21eの順に第5図(B)のように開にし、逆に停止
時には下流側から自動弁21e、21d、・・・21a
の順に第5図(A)のように閉じていく。
In this embodiment, a total of 20 automatic valves 21 are arranged in five rows in the axial direction of the conduit. As shown in Figure 5 (A) and (B),
These automatic valves 21a to 21e are opened and closed by an air signal as an external signal supplied to the air cylinder 22, and at the time of starting, the automatic valves 21a, 2lb,
-21e in order as shown in FIG.
5 (A) in this order.

このようにして、第1.第2の実施例によれば、ノズル
13a〜13dが導管lOの内周壁10aよりも軸心方
向にいくらか突き出しているので、ノズル13a−13
dがら噴出するスチームの噴射音や凝縮音が低減され、
二重管構造であることと相俟って外管12から外部に洩
出する振動騒音をかなり抑制することができる。
In this way, the first. According to the second embodiment, the nozzles 13a-13d protrude somewhat in the axial direction from the inner circumferential wall 10a of the conduit lO, so that the nozzles 13a-13
d The jetting sound of steam and condensation sound are reduced,
Coupled with the double tube structure, the vibration noise leaking outside from the outer tube 12 can be considerably suppressed.

また第2実施例のように、自動弁21を付属せしめた装
置では、始動時や停止時に所定の順序にしたがって自動
弁21を開または閉にするようにしたので、弁開時には
、主流体とスチームが急激に接触したとき発生する衝撃
音(ハンマリング)を防止することができるとともに弁
閉時には、主流体がノズル13を経て注入口11の側へ
逆流するのを確実に防IFできる。
Furthermore, in a device equipped with an automatic valve 21 as in the second embodiment, the automatic valve 21 is opened or closed according to a predetermined order when starting or stopping, so that when the valve is opened, the main fluid It is possible to prevent impact noise (hammering) generated when steam suddenly comes into contact with the steam, and when the valve is closed, it is possible to reliably prevent the main fluid from flowing back to the injection port 11 side through the nozzle 13.

この場合、例えばパルプ原料のような固形分を含んだ液
体のスチーム(注入流体)によりY流体を直接加熱する
ときには、始動時に導管10に主流体を供給すると同時
もしくは供給後上記所定の順序で自動弁21を開状態に
し、また停止時には停市と同時もしくは前記始動時と逆
の順にそれまで開いていた自動弁21を閉状態にするこ
とにより、主流体がノズル21を経て注入口ll側へ逆
流するのを防止する。従って注入口11等の主流体の固
形分によりノズルの目詰まりの発生を防止することがで
きる。
In this case, when the Y fluid is directly heated by steam (injected fluid) of a liquid containing solids such as pulp raw material, the main fluid is supplied to the conduit 10 at the time of startup or automatically in the above-described predetermined order after supply. By opening the valve 21 and closing the automatic valve 21, which had been open until then, at the same time as the stop or in the reverse order from the start, the main fluid passes through the nozzle 21 and flows to the injection port ll side. Prevent backflow. Therefore, it is possible to prevent the nozzle from clogging due to the solid content of the main flow of the injection port 11 and the like.

(比較例) なお、前記従来のインジェクタ方式のもつ欠点を解決す
るために、第6図のように、スタティックミキサーを用
いたインラインミキサーにより、強制的に主流体と注入
流体を混合するようにした流体混合装置も考えられる。
(Comparative example) In order to solve the drawbacks of the conventional injector method, as shown in Figure 6, an in-line mixer using a static mixer was used to forcibly mix the main fluid and the injection fluid. Fluid mixing devices are also conceivable.

図において、lは主流体を図で左方から右方へ流通させ
る導管、2はスチーム管を取入れる注入口である。注入
口2は、導管1の外周に二重管構造になるように設けら
れる外管3と連通し、この外管3は、その内部の導管1
の外周に形成される多数のノズル孔30を通じて導管1
と連通ずる。
In the figure, 1 is a conduit through which the main fluid flows from left to right in the figure, and 2 is an inlet for introducing a steam pipe. The injection port 2 communicates with an outer tube 3 provided on the outer periphery of the conduit 1 so as to have a double tube structure, and this outer tube 3 communicates with the inner conduit 1.
The conduit 1 passes through a number of nozzle holes 30 formed on the outer periphery of the
Communicate with.

導管1の内部には、その軸線方向にねじれ面をもつ複数
のスタティンクミキサエレメント4が、図で左端1aか
ら右端1bまで連続的に配設されている。
Inside the conduit 1, a plurality of static mixer elements 4 having twisted surfaces in the axial direction are continuously arranged from the left end 1a to the right end 1b in the figure.

ところが、このような流体混合装置では、導管1の内部
の主流体がほとんど流れていない所でスチームを注入し
ているため、主流体中心部の混合が不完全であると共に
ノズル孔からの噴射音が外部へ騒音として発生し、問題
の十分な解決にはならない。
However, in such a fluid mixing device, steam is injected into the conduit 1 at a place where the main fluid is hardly flowing, so that mixing in the center of the main fluid is incomplete and the jet noise from the nozzle hole is high. is generated as noise to the outside, and is not a sufficient solution to the problem.

(発明の効果) 本発明によれば、二重管構造の内管としての導管に設け
たノズルであって、その先端が導管内周壁よりも軸心側
に突出した位置から、注入流体を導管内に噴射するよう
にしたので、そのとき発生する噴射音や凝縮音が外部に
洩れるのをかなり抑制することができ、また流速の遅い
主流体に多量のスチームなどの注入流体が高速で接触し
たときであっても、その際に生ずる衝撃音(ハンマリン
グ)を確実に防止することができる。
(Effects of the Invention) According to the present invention, the nozzle is provided in a conduit as an inner tube of a double-pipe structure, and the injected fluid is injected into the conduit from a position where the tip thereof protrudes toward the axis side from the inner circumferential wall of the conduit. Since the jet is injected internally, the leakage of the jetting and condensation noise generated at that time to the outside can be significantly suppressed, and it is also possible to prevent a large amount of injected fluid such as steam from coming into contact with the slow-flowing main fluid at high speed. Even when the impact noise (hammering) occurs at that time, it is possible to reliably prevent the impact sound (hammering) that occurs at that time.

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

第1図は本発明の実施例をあられす構成断面図、第2図
は第1図のX方向矢視図、第3UAは第1図の導管10
部分のA−A線断面図、第4図は他の実施例をあられす
構成半断面図、第5 (A)図と第5 (B)図は第4
図の自動弁の開閉状態を示す構成図、第6図は比較例の
構成断面図である。 10、、、、、、、、、、、、導管。 11、、、、、、、、、、、、注入口。 12、、、、、、、、、、、、外管。 13 (13a−13d)、、、ノズル。 15〜20.、、、、、、スタティックミキサエレメ刈
・。 21 (21a 〜21e)、、、自動弁。 出願人 株式会社ノリタケカンパニーリミテド代理人 
弁理士 加 藤 朝 道 第1図 八 第2図 第3図
FIG. 1 is a cross-sectional view of the configuration of an embodiment of the present invention, FIG. 2 is a view taken in the X direction of FIG. 1, and 3UA is the conduit 10 of FIG. 1.
A sectional view taken along the line A-A of the part, FIG. 4 is a half sectional view showing another embodiment, and FIGS.
FIG. 6 is a configuration diagram showing the opening and closing states of the automatic valve shown in FIG. 6, and FIG. 6 is a configuration sectional view of a comparative example. 10, , , , , , , conduit. 11, , , , , , , injection port. 12, , , , , , , , outer tube. 13 (13a-13d), nozzle. 15-20. ,,,,, Static mixer element cutting. 21 (21a to 21e), automatic valve. Applicant Noritake Co., Ltd. Agent
Patent Attorney Asa Kato Do Figure 1 Figure 8 Figure 2 Figure 3

Claims (1)

【特許請求の範囲】 l)主流体を流通する導管と、該導管の内部にその軸方
向に配設したスタティックミキサニレメン1と、該導管
の外周で二重管構造を構成し注入流体の注入口を有する
外管と、外管の内部で導管に貫通しかつ導管内周壁より
も軸心側に突出するノズルとから成る流体混合装置。 2)主流体を流通する導管と、該導管の内部にその軸方
向に配設したスタティックミキサエレメントと、該導管
の外周で二重管構造を構成し注入波体の注入口を有する
外管と、外管の内部で導管に貫通しかつ導管内周壁より
も軸心側に突出するノズルと、このノズルを外部信号に
基づいて開閉する自動弁を設けた流体混合装置。
[Scope of Claims] l) A conduit through which the main fluid flows, a static mixer element 1 disposed inside the conduit in the axial direction, and a double pipe structure formed on the outer periphery of the conduit, for the injection fluid to flow through the conduit. A fluid mixing device comprising an outer tube having an injection port, and a nozzle that penetrates a conduit inside the outer tube and protrudes toward the axis of the conduit from the inner circumferential wall of the conduit. 2) A conduit through which the main fluid flows, a static mixer element disposed inside the conduit in the axial direction thereof, and an outer tube forming a double pipe structure on the outer periphery of the conduit and having an inlet for the injection wave body. , a fluid mixing device provided with a nozzle that penetrates the conduit inside the outer tube and protrudes toward the axis of the conduit from the inner circumferential wall of the conduit, and an automatic valve that opens and closes this nozzle based on an external signal.
JP59083695A 1984-04-27 1984-04-27 Fluid mixing apparatus Granted JPS60227819A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59083695A JPS60227819A (en) 1984-04-27 1984-04-27 Fluid mixing apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59083695A JPS60227819A (en) 1984-04-27 1984-04-27 Fluid mixing apparatus

Publications (2)

Publication Number Publication Date
JPS60227819A true JPS60227819A (en) 1985-11-13
JPH0139815B2 JPH0139815B2 (en) 1989-08-23

Family

ID=13809627

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59083695A Granted JPS60227819A (en) 1984-04-27 1984-04-27 Fluid mixing apparatus

Country Status (1)

Country Link
JP (1) JPS60227819A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03232557A (en) * 1990-02-07 1991-10-16 Noritake Co Ltd Steam injecting nozzle
JPH0491701U (en) * 1990-12-25 1992-08-10
JP2011167651A (en) * 2010-02-22 2011-09-01 Hymo Corp Treatment method of sewage sludge
CN105019037A (en) * 2015-07-27 2015-11-04 张家港欣阳化纤有限公司 Melt static mixer for spinning
PL423571A1 (en) * 2017-11-24 2019-06-03 Univ Technologiczno Przyrodniczy Im Jana I Jedrzeja Sniadeckich W Bydgoszczy Construction of a mixer for mixing grainy material, with the vibratory round-screw driving system
JP2021509358A (en) * 2018-01-05 2021-03-25 サビック エスケー ネクスレーン カンパニー プライベート リミテッドSabic Sk Nexlene Company Pte. Ltd. Mixing system

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03232557A (en) * 1990-02-07 1991-10-16 Noritake Co Ltd Steam injecting nozzle
JPH0491701U (en) * 1990-12-25 1992-08-10
JP2011167651A (en) * 2010-02-22 2011-09-01 Hymo Corp Treatment method of sewage sludge
CN105019037A (en) * 2015-07-27 2015-11-04 张家港欣阳化纤有限公司 Melt static mixer for spinning
PL423571A1 (en) * 2017-11-24 2019-06-03 Univ Technologiczno Przyrodniczy Im Jana I Jedrzeja Sniadeckich W Bydgoszczy Construction of a mixer for mixing grainy material, with the vibratory round-screw driving system
JP2021509358A (en) * 2018-01-05 2021-03-25 サビック エスケー ネクスレーン カンパニー プライベート リミテッドSabic Sk Nexlene Company Pte. Ltd. Mixing system

Also Published As

Publication number Publication date
JPH0139815B2 (en) 1989-08-23

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