JPS5939173B2 - fluid mixing device - Google Patents

fluid mixing device

Info

Publication number
JPS5939173B2
JPS5939173B2 JP57015257A JP1525782A JPS5939173B2 JP S5939173 B2 JPS5939173 B2 JP S5939173B2 JP 57015257 A JP57015257 A JP 57015257A JP 1525782 A JP1525782 A JP 1525782A JP S5939173 B2 JPS5939173 B2 JP S5939173B2
Authority
JP
Japan
Prior art keywords
small
casing
diameter
mixing device
fluid 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
Application number
JP57015257A
Other languages
Japanese (ja)
Other versions
JPS58133822A (en
Inventor
悟 宮田
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.)
MEIJU SANGYO KK
Original Assignee
MEIJU SANGYO KK
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 MEIJU SANGYO KK filed Critical MEIJU SANGYO KK
Priority to JP57015257A priority Critical patent/JPS5939173B2/en
Publication of JPS58133822A publication Critical patent/JPS58133822A/en
Publication of JPS5939173B2 publication Critical patent/JPS5939173B2/en
Expired 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
    • B01F25/421Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions by moving the components in a convoluted or labyrinthine path
    • B01F25/422Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions by moving the components in a convoluted or labyrinthine path between stacked plates, e.g. grooved or perforated plates

Landscapes

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

Description

【発明の詳細な説明】 本発明は、流体混合装置に関し、更に詳述すれば数種類
の流体の混合が機械動力を用いないで効果的にできる流
体混合装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a fluid mixing device, and more particularly to a fluid mixing device that can effectively mix several types of fluids without using mechanical power.

同じ目的に用いられる装置は既に多数の変形が提案され
、かつ公知になつている。
Numerous variants of devices serving the same purpose have already been proposed and are known.

しかしこれまでの装置は、比較的構造の簡単なものでは
充分な混合効果が得られず、また高い混合効果を有する
ものでは構造が複雑となつて高価となるばかりでなく、
装置全体を大型化しなければならないといった欠点があ
つた。本発明の目的は、これまでの装置の上述した欠点
を持たず、構造的に簡単で、安価に製作することができ
、しかも全体を小型化できて設置スペースをとらず、高
い混合効果を示す流体混合装置を提供することである。
However, with conventional devices, devices with relatively simple structures do not provide sufficient mixing effects, and devices with high mixing effects not only have complicated structures and are expensive;
The drawback was that the entire device had to be made larger. The object of the present invention is to avoid the above-mentioned drawbacks of conventional devices, to be simple in structure, to be manufactured at low cost, to be miniaturized as a whole, to take up little installation space, and to exhibit high mixing effects. An object of the present invention is to provide a fluid mixing device.

以下、本発明の実施例を図面について説明する。Embodiments of the present invention will be described below with reference to the drawings.

図において、1は円筒状のケーシングで、両側の開口部
に夫々外周方向に突出するフランジ2、2を有し、入口
3及び出口4を備えた端板5、6をボルト及びナットに
より着脱可能に取付けている。T(Ta〜7f)はケー
シング1の中空内部に複数配設した流体混合用の導流単
位体である。導流単位体7は第2図及び第3図に示した
ように互いに対向する面に前面開放の多角形状の小室B
a及び8bをハニカム状に多数配列した大小2枚の円板
9、10を一組とし、これを同心的に重合して構成され
る。なお、前記小室Ba、8をは菱形でも良く、要する
に多角形であればよい。前記太径な円板9はケーシング
1の内径に密接する外径を有し、かつ中心に流通孔11
が穿設されている。小径な円板10の外径はケーシング
1の内周面から離間して該内周面との間に流通路12を
形成する。第3図に示したように前記大径な円板9の小
室Baと小径な円板10の小室8bは互いの小室が対向
する他の複数の小室に連通するように位置を違えて配列
されている。
In the figure, 1 is a cylindrical casing, which has flanges 2, 2 protruding toward the outer circumference at openings on both sides, and end plates 5, 6 equipped with an inlet 3 and an outlet 4, which can be attached and detached with bolts and nuts. It is installed on. T (Ta~7f) is a plurality of flow guiding units for mixing fluids arranged inside the hollow of the casing 1. As shown in FIGS. 2 and 3, the flow guiding unit 7 has polygonal small chambers B with open fronts on opposing surfaces.
A set of two large and small disks 9 and 10 in which a large number of disks a and 8b are arranged in a honeycomb shape is formed by concentrically superimposing them. Note that the small chambers Ba and 8 may be rhombic, or in short, may be polygonal. The large-diameter disk 9 has an outer diameter close to the inner diameter of the casing 1, and has a communication hole 11 in the center.
is drilled. The outer diameter of the small-diameter disk 10 is spaced apart from the inner peripheral surface of the casing 1 to form a flow passage 12 therebetween. As shown in FIG. 3, the small chambers Ba of the large-diameter disk 9 and the small chambers 8b of the small-diameter disk 10 are arranged at different positions so that each small chamber communicates with a plurality of other small chambers facing each other. ing.

そして、これら導流単位体7は互いに同径の円板が隣接
するように重ね合わせてケーシング1の中空内部にその
軸線方向と直交する如く並設する。なお、ケーシング1
の入口3及び出口4に流通孔11が対応するように両側
には大径な円板9が配置されるようにする。また、導流
単位体7の大径な円板9と小径な円板10は互いに接合
する小室の前面部分を接着することによつて一体化する
ことが望ましい。以上のように構成された本発明装置は
、異なる2種以上の流体を適宜な圧送手段によつてケー
シング1の入口3からその中空内部に送り込む。
These flow guide units 7 are arranged in parallel in the hollow interior of the casing 1 so that the disks having the same diameter are adjacent to each other and are perpendicular to the axial direction of the casing 1. In addition, casing 1
Large-diameter disks 9 are disposed on both sides so that the flow holes 11 correspond to the inlet 3 and outlet 4 of the main body. Further, it is desirable that the large-diameter disk 9 and the small-diameter disk 10 of the flow guide unit 7 are integrated by bonding the front portions of the small chambers that are joined to each other. The device of the present invention configured as described above feeds two or more different types of fluids into the hollow interior of the casing 1 from the inlet 3 of the casing 1 using appropriate pressure feeding means.

しかして、ケーシング1の中空内部に送り込まれた流体
は第1図に矢印で示したように第1の導流単位体7(7
a)の流通孔11からその内部に達し、小径な円板10
により直進を防たげられて方向を変え、互いに連通する
小室8a,8bを経て中央部から外側に向かつて放射状
に分散、蛇行しながら移動する。そして流体が互いの小
室8a,8bを移動する際に、その小室8a,8bを構
成する複数の側壁に衝突して流れは複雑に反転し、渦流
となる。このように、第1の導流単位体7(7a)を通
過することによつて分散、反転、渦流作用を繰り返えし
ながらケーシング1の内周面に到達した流体は、そのケ
ーシング1の内周面と小径な円板10とによつて形成さ
れた流路12から第2の導流単位体7(7b)の各小室
8a,8bに入り、上述のような分散、反転、渦流作用
を繰り返えしながら中央部に集合され、再び流通孔11
から第3の導流単位体7(7c)の内部に入る。
Therefore, the fluid sent into the hollow interior of the casing 1 flows through the first flow guiding unit 7 (7) as shown by the arrow in FIG.
The small-diameter disk 10 reaches the inside from the communication hole 11 in a).
They are prevented from moving straight, change direction, and move in a radially dispersed and meandering manner from the center toward the outside through the small chambers 8a and 8b that communicate with each other. When the fluid moves through each of the small chambers 8a and 8b, it collides with the plurality of side walls that constitute the small chambers 8a and 8b, causing the flow to reverse in a complicated manner and become a vortex. In this way, the fluid that reaches the inner circumferential surface of the casing 1 while repeating dispersion, reversal, and vortex action by passing through the first flow guiding unit 7 (7a) The small chambers 8a, 8b of the second flow guide unit 7 (7b) enter from the flow path 12 formed by the inner circumferential surface and the small-diameter disk 10, and the dispersion, reversal, and vortex effects as described above are generated. While repeating this process, they are assembled in the center, and the flow holes 11 are opened again.
It enters the inside of the third flow guiding unit 7 (7c).

そして再度各小室8a,8bを経ながら中央部から外側
に向かつて放射状に分散、蛇行を繰り返えしつつ順次導
流単位体の内部を移動し、最終的に出口4から排出され
る。したがつて、本発明装置によれば、導流単位体7(
7a〜7f)の内部に流体を導き、互いに連通状に対向
する各小室8a,8bを移動する過程で分散、反転、渦
流作用を行なわせて混合し、さらに放射状に再分散と集
合を繰り返えし流体の混合をさせるもので、従来の混合
装置のどれよりもはるかに効果的な混合が得られる。
Then, it passes through each of the small chambers 8a and 8b again, radially dispersing outward from the center, repeating meandering and sequentially moving inside the flow guide unit, and is finally discharged from the outlet 4. Therefore, according to the device of the present invention, the flow guiding unit 7 (
7a to 7f), and in the process of moving through the small chambers 8a and 8b facing each other in a communication manner, the fluid is mixed by dispersion, inversion, and vortex action, and then redispersion and aggregation are repeated radially. This mixes the mixing fluids and provides much more effective mixing than any conventional mixing device.

第5図及び第6図に示した他の実施例は、導流単位体7
を構成する大小2枚の円板9,10の中心部を除く夫々
の小室8a,8bの底面中央に、該小室8a,8bの上
面の高さより低くした突起13を設けたものである。
Another embodiment shown in FIGS. 5 and 6 is a flow guiding unit 7
A protrusion 13 is provided at the center of the bottom surface of each of the small chambers 8a, 8b, excluding the central portion of the two large and small disks 9, 10 constituting the disk, which is lower than the height of the top surface of the small chambers 8a, 8b.

これによつて、流体の流れに乱れを積極的に生じさせる
ことができ、層混合効果を高めることができる。また、
前記突起13は流体の小室への流入時の対流現象化にお
ける流体の剪断力を高める。
Thereby, turbulence can be actively caused in the fluid flow, and the layer mixing effect can be enhanced. Also,
The protrusions 13 increase the shearing force of the fluid during convection when the fluid flows into the chamber.

さらに前記突起13を中心部に近づくに従つて順次小さ
くすることにより各小室の容積を均一化し、スムーズな
流体の流れが確保される。以上実施例について説明した
ように、本発明の流体混合装置によれば、流体を導流単
位体の各小室において分散、反転、渦流作用により混合
し、さらに導流単位体の中央から外側へ又は外側から中
央へと放射状に再分散と集合を交互に繰り返えして放射
混合させるものであるから、従来の混合装置に比しては
るかに高い混合効果が得られる。
Further, by making the projections 13 gradually smaller toward the center, the volume of each chamber is made uniform, and smooth fluid flow is ensured. As described above with respect to the embodiments, according to the fluid mixing device of the present invention, fluid is mixed by dispersion, inversion, and vortex action in each small chamber of the flow guide unit, and further from the center of the flow guide unit to the outside or Since it performs radial mixing by alternately repeating redispersion and aggregation radially from the outside to the center, a much higher mixing effect can be obtained compared to conventional mixing devices.

また、本発明によれば混合要素たる導流単位体をケーシ
ングの中空内部にその軸線方向と直交するよう複数並設
したものであるから、装置全体とくに流体の流れ方向を
非常に短かくでき、従つて設置スペースを大きくするこ
とがなく、製作上及び使用上においてきわめて実用的な
流体混合装置を提供することができる。さらに、狭い容
積で長い流動距離を得ることができ、流体の混合をきわ
めて能率よくできる。
Further, according to the present invention, since a plurality of flow guide units serving as mixing elements are arranged in parallel in the hollow interior of the casing so as to be orthogonal to the axial direction of the casing, the entire device, especially the fluid flow direction, can be made very short. Therefore, it is possible to provide a fluid mixing device that is extremely practical in terms of manufacture and use without increasing the installation space. Furthermore, a long flow distance can be obtained in a small volume, making fluid mixing very efficient.

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

図は本発明の実施例を示し、第1図は全体の縦断側面図
、第2図イは導流単位体を構成する大径な円板の斜視図
、第2図叫ま同じく小径な円板の斜視図、第3図は本装
置の要部を拡大して示す縦断正面図、第4図は同じく本
装置の要部を拡大して示す縦断側面図、第5図は他の実
施例の要部を拡大して示す縦断正面図、第6図は同じく
他の実施例の要部を拡大して示す縦断側面図である。 1・・・・・・ケーシング、3・・・・・・入口、4・
・・・・・出口、7・・・・・・導流単位体、8a,8
b・・・・・・小室、9・・・・・・大径な円板、10
・・・・・・小径な円板、11・・・・・・流通孔、1
3・・・・・・突起。
The figures show an embodiment of the present invention, in which Fig. 1 is a longitudinal sectional side view of the whole, Fig. 2 A is a perspective view of a large-diameter disk constituting the flow guiding unit, and Fig. 2 is also a small-diameter circular plate. A perspective view of the plate, FIG. 3 is a longitudinal sectional front view showing an enlarged view of the main parts of this device, FIG. 4 is a longitudinal sectional side view showing an enlarged main part of this device, and FIG. 5 is another embodiment. FIG. 6 is an enlarged longitudinal sectional side view showing the essential parts of another embodiment. 1...Casing, 3...Inlet, 4.
...Outlet, 7...Direction unit, 8a, 8
b... Small chamber, 9... Large diameter disk, 10
・・・・・・Small diameter disc, 11 ・・・Communication hole, 1
3... Protrusion.

Claims (1)

【特許請求の範囲】 1 両端に入口及び出口を備えた円筒状のケーシングと
、互いに対向する面に前面開放の多角形の小室をハニカ
ム状に多数配列した大小2枚の円板を同心的に重合して
なる複数の導流単位体とからなり、前記大径な円板はケ
ーシングの内径に合致する直径を有し、かつ中心に流通
孔を穿設し、前記大径な円板と小径な円板の小室は互い
の小室が対向する他の複数の小室に連通するように位置
を違えて配列されており、これら複数の導流単位体を互
いに同径の円板が隣接するように重ね合わせてケーシン
グ内に設置すると共に、両端には導流単位体の大径な円
板を位置させてその流通孔をケーシングの入口及び出口
に連通させるようにしたことを特徴とする流体混合装置
。 2 大小2枚の円板の中心部を除く夫々の小室の底面中
央に、該小室の上面の高さより低くした突起を設けたこ
とを特徴とする特許請求の範囲第1項記載の流体混合装
置。 3 突起は中心部に近づくに従い順次小さくしたことを
特徴とする特許請求の範囲第2項記載の流体混合装置。
[Claims] 1. A cylindrical casing with an inlet and an outlet at both ends, and two large and small disks concentrically arranged in a honeycomb pattern with a large number of open-front polygonal chambers arranged on opposing surfaces. The large-diameter disk has a diameter that matches the inner diameter of the casing, and a flow hole is bored in the center, and the large-diameter disk and the small-diameter disk have a diameter that matches the inner diameter of the casing. The small chambers of the disc are arranged at different positions so that each small chamber communicates with a plurality of other small chambers facing each other. A fluid mixing device characterized in that the fluid mixing device is installed in a casing in a stacked manner, and a large-diameter disk of a flow guide unit is positioned at both ends so that the flow holes communicate with the inlet and outlet of the casing. . 2. The fluid mixing device according to claim 1, characterized in that a protrusion lower than the height of the top surface of the small chamber is provided at the center of the bottom surface of each of the small chambers, excluding the central portion of the two large and small disks. . 3. The fluid mixing device according to claim 2, wherein the protrusions are gradually made smaller as they get closer to the center.
JP57015257A 1982-02-01 1982-02-01 fluid mixing device Expired JPS5939173B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57015257A JPS5939173B2 (en) 1982-02-01 1982-02-01 fluid mixing device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57015257A JPS5939173B2 (en) 1982-02-01 1982-02-01 fluid mixing device

Related Child Applications (1)

Application Number Title Priority Date Filing Date
JP57123479A Division JPS58133824A (en) 1982-07-15 1982-07-15 Mixing device of fluid

Publications (2)

Publication Number Publication Date
JPS58133822A JPS58133822A (en) 1983-08-09
JPS5939173B2 true JPS5939173B2 (en) 1984-09-21

Family

ID=11883798

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57015257A Expired JPS5939173B2 (en) 1982-02-01 1982-02-01 fluid mixing device

Country Status (1)

Country Link
JP (1) JPS5939173B2 (en)

Cited By (5)

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JP2006281182A (en) * 2005-03-31 2006-10-19 Sunstar Inc W/o/w type emulsion composition
WO2009154188A1 (en) * 2008-06-16 2009-12-23 アイセル株式会社 Mixing element, mixing device, agitation blade, mixing machine, mixing system and reaction device
JP2010023026A (en) * 2008-06-16 2010-02-04 Isel Co Ltd Mixing element, mixing device, mixing method, agitation blade, agitation device, and agitation method
JP2010099574A (en) * 2008-10-22 2010-05-06 Isel Co Ltd Mixing device and mixing system
JP2018535378A (en) * 2017-03-20 2018-11-29 ジーセブン ホールディングスGseven Holdings Liquefaction promoting device by fluid agitation installed on the piping path of heat pump system

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JPH0857279A (en) * 1994-08-24 1996-03-05 Kankyo Kagaku Kogyo Kk Stationary mixer
US5605399A (en) * 1995-10-17 1997-02-25 Komax Systems, Inc. Progressive motionless mixer
JPH1033108A (en) * 1996-07-23 1998-02-10 Kankyo Kagaku Kogyo Kk Bubble-entrained dough for cake, its production and apparatus therefor
US8740450B2 (en) * 2008-01-10 2014-06-03 Mg Grow Up Corp. Static fluid mixer capable of ultrafinely mixing fluids
US9656223B2 (en) 2008-06-16 2017-05-23 Isel Co., Ltd. Mixing unit and device, fluid mixing method and fluid
JP2011121020A (en) * 2009-12-14 2011-06-23 Isel Co Ltd Mixing element, mixing device, mixing method, stirring blade, stirring device, and stirring method
EP2826547B1 (en) * 2012-03-13 2017-08-23 Isel Co., Ltd. Mixing unit, devices using same and fluid mixing method
JP6326172B1 (en) * 2017-07-21 2018-05-16 株式会社エコグローバルユニオン A system for producing water with a high hydrogen content

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006281182A (en) * 2005-03-31 2006-10-19 Sunstar Inc W/o/w type emulsion composition
WO2009154188A1 (en) * 2008-06-16 2009-12-23 アイセル株式会社 Mixing element, mixing device, agitation blade, mixing machine, mixing system and reaction device
JP2010023026A (en) * 2008-06-16 2010-02-04 Isel Co Ltd Mixing element, mixing device, mixing method, agitation blade, agitation device, and agitation method
JP2010099574A (en) * 2008-10-22 2010-05-06 Isel Co Ltd Mixing device and mixing system
JP2018535378A (en) * 2017-03-20 2018-11-29 ジーセブン ホールディングスGseven Holdings Liquefaction promoting device by fluid agitation installed on the piping path of heat pump system

Also Published As

Publication number Publication date
JPS58133822A (en) 1983-08-09

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