JPS5939174B2 - fluid mixing device - Google Patents

fluid mixing device

Info

Publication number
JPS5939174B2
JPS5939174B2 JP57015258A JP1525882A JPS5939174B2 JP S5939174 B2 JPS5939174 B2 JP S5939174B2 JP 57015258 A JP57015258 A JP 57015258A JP 1525882 A JP1525882 A JP 1525882A JP S5939174 B2 JPS5939174 B2 JP S5939174B2
Authority
JP
Japan
Prior art keywords
small
diameter
mixing device
flow guiding
cylindrical
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
JP57015258A
Other languages
Japanese (ja)
Other versions
JPS58133823A (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 JP57015258A priority Critical patent/JPS5939174B2/en
Publication of JPS58133823A publication Critical patent/JPS58133823A/en
Publication of JPS5939174B2 publication Critical patent/JPS5939174B2/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

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きわめて効果的に
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 mix several types of fluids very effectively 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。しかし、これワ までの装置
は、流体が通る筒体内に同形態の複数の混合要素を流れ
方向と同一方向に配置するか、又は直角に配置するかの
いづれかにすぎず、これらを一体的に組合わせて構成し
たものはなかつた。従つて、流動変化が少なくて充分な
混合が得られ□ ず、混合効果はきわめて低いものであ
つた。本発明の目的は、筒体の上流側に流れ方向と同一
方向に流体混合用の筒状導流単位体を配置し、下流側に
は流れ方向と直角に別の流体混合用の円板状導流単位体
を配置して構成し、筒体の上流側9 と下流側とで流体
の流動方向を異ならせるようにして混合効果を著しく高
めるようにした流体混合装置を提供することである。本
発明の他の目的は、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5 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。
Numerous variants of devices serving the same purpose have already been proposed and are known. However, in the devices up to now, a plurality of mixing elements of the same shape are arranged either in the same direction as the flow direction or at right angles within a cylinder through which the fluid passes, and these elements are integrated into one body. There were no combinations of them. Therefore, there was little flow change and sufficient mixing could not be obtained, resulting in extremely low mixing effects. An object of the present invention is to arrange a cylindrical flow guiding unit for fluid mixing in the same direction as the flow direction on the upstream side of the cylinder, and to arrange another disc-shaped flow guide unit for fluid mixing at right angles to the flow direction on the downstream side. It is an object of the present invention to provide a fluid mixing device which is configured by arranging flow guiding units and makes the flow directions of fluid different between the upstream side 9 and the downstream side of a cylinder, thereby significantly enhancing the mixing effect. Another object of the present invention is to provide a fluid mixing device that is structurally simple, can be manufactured at low cost, can be miniaturized as a whole, does not take up much installation space, and exhibits a high mixing effect. .

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は流体が通る円筒体の装置本体で、上流
側に位置する副筒体1aと下流側に位置ク する主筒体
Ibとから構成されている。副筒体1aは比較的小径に
形成され、先端に入口2を有する。主筒本Ibは両側の
開口部に夫々外周方向に突出するフランジ3、3を有し
、端板4、5を配してボルト及びナットにより着脱可能
に取付け5 ている。前記副筒体1aの後端は主筒体I
bの一方の端板4に固定されその中央に穿設した開口6
と連通する。主筒体Ibの他方の端板5には出口7が形
成される。8(8a,8b)は副筒体1a内に配置した
流体混合用の筒状導流単位体である。
In the figure, reference numeral 1 denotes a cylindrical device main body through which fluid passes, and is composed of a sub-cylindrical body 1a located on the upstream side and a main cylinder body Ib located on the downstream side. The sub-cylindrical body 1a is formed to have a relatively small diameter and has an inlet 2 at its tip. The main cylindrical body Ib has flanges 3, 3 protruding toward the outer circumference at openings on both sides, and end plates 4, 5 are disposed thereon and are removably attached 5 with bolts and nuts. The rear end of the sub cylinder 1a is connected to the main cylinder I.
an opening 6 fixed to one end plate 4 of b and bored in the center thereof;
communicate with. An outlet 7 is formed in the other end plate 5 of the main cylinder Ib. Reference numeral 8 (8a, 8b) is a cylindrical flow guide unit for fluid mixing disposed within the sub-cylindrical body 1a.

該筒状導流単位体8(8a,8b)は第2図に示したよ
うに円筒状に形成され、かつ菱形の小室9(9a,9b
)を多数配夕1ルた網目状に形成されている。そしてこ
れら筒状導流単位体8(8a,8b)は同心状に重層し
て流れ方向と同一方向に配置され、その外層の筒状導流
単位体8(8a)の小室9(9a)と内層の筒状導流単
位体8(8b)の小室9(9b)は第3図に示したよう
に互いの小室9(9a),9(9b)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
。また、外層の筒状導流単位体8(8a)の外周面は第
1図に示したように副筒体1aの内周面に密接して塞が
れ、内層の筒状導流単位体8(8b)の内周面は副筒体
1aの中心軸線上に挿通した軸体10によつて塞がれて
いる。従つて幅筒体1aの入口2から入る流体は夫々の
筒状導流単位体8(8a,8bの各小室9(9a,9b
)を経て主筒体1bの内部に流入することになる。なお
、この実施例では前記外層の筒状導流単位体8(8a)
と内層の筒状導流単位体8(8b)は互いの重層面を接
着することによつて一体化し、前記軸体10の一端のね
じ部11を副筒体1aに固設した帯板状の支持部材12
に通してナツト止め13することにより副筒体1a内に
支持させている。
The cylindrical flow guiding unit 8 (8a, 8b) is formed in a cylindrical shape as shown in FIG.
) are arranged in a mesh pattern. These cylindrical flow guide units 8 (8a, 8b) are concentrically stacked and arranged in the same direction as the flow direction, and the small chamber 9 (9a) of the outer layer cylindrical flow guide unit 8 (8a) The small chamber 9 (9b) of the cylindrical flow guiding unit 8 (8b) in the inner layer communicates with a plurality of other small chambers in which the small chambers 9 (9a) and 9 (9b) are opposite each other, as shown in FIG. They are arranged in different positions like this. Further, the outer circumferential surface of the outer layer cylindrical flow guiding unit 8 (8a) is closely closed to the inner circumferential surface of the sub-cylindrical body 1a as shown in FIG. The inner circumferential surface of 8 (8b) is closed by a shaft 10 inserted on the central axis of the sub-cylindrical body 1a. Therefore, the fluid entering from the inlet 2 of the wide cylindrical body 1a flows into each small chamber 9 (9a, 9b) of each cylindrical flow guide unit 8 (8a, 8b).
) and flows into the interior of the main cylindrical body 1b. In addition, in this embodiment, the cylindrical flow guide unit 8 (8a) of the outer layer
and the inner layer cylindrical flow guide unit 8 (8b) are integrated by gluing their overlapping surfaces, and are formed into a strip-like structure with the threaded portion 11 at one end of the shaft 10 fixed to the sub-cylindrical body 1a. support member 12 of
It is supported within the sub-cylindrical body 1a by passing it through and securing it with a nut 13.

14(14a〜14f)は主筒体1b内に配置した流体
混合用の円板状導流単位体である。
Reference numeral 14 (14a to 14f) denotes a disc-shaped flow guiding unit for fluid mixing disposed within the main cylinder 1b.

該円板状導流単位体14は第4図及び第5図に示したよ
うに互いに対向する面に前面開故の六角形状の小室15
(15a,15b)をハニカム状に多数配列した大小2
枚の円板16,17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15(15a,15b)
は例えば菱形でもよく、要するに多角形のものであれば
よい。前記大径な円板16は主筒体1bの内周面に密接
する外径を有し、かつ中心に流通孔18が穿設されてい
る。小径な円板17の外径は主筒体1bの内周面から離
間して該内周面との間に流路19を形成する。また、第
5図に示したように前記大径な円板16の小径15(1
5a)と小径な円板17の小室15(15b)は互いの
小室15(15a,15b)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。そして
、これら円板状導流単位体14(14a〜14f)は互
いに同径の円板が隣接するように重ね合わせて主筒体1
bの中空内部に流れ方向と直角に配置する。なお、主筒
体1bの開口6及び出口7と流通孔18が対応するよう
に両側には大径な円板16を位置させている。また、円
板状導流単位体14(14a〜14f)の大径な円板1
6と小径な円板17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。
As shown in FIGS. 4 and 5, the disk-shaped flow guiding unit 14 has hexagonal small chambers 15 with open front surfaces on opposing surfaces.
(15a, 15b) arranged in a honeycomb shape, large and small 2
A set of disks 16 and 17 is formed by concentrically overlapping them. In addition, the small chamber 15 (15a, 15b)
may be, for example, diamond-shaped; in short, it may be a polygon. The large-diameter disk 16 has an outer diameter that closely contacts the inner circumferential surface of the main cylinder 1b, and has a communication hole 18 bored in its center. The outer diameter of the small-diameter disk 17 is spaced apart from the inner peripheral surface of the main cylinder 1b to form a flow path 19 therebetween. Further, as shown in FIG. 5, the small diameter 15 (1
5a) and the small chambers 15 (15b) of the small diameter disc 17 are arranged at different positions so that each small chamber 15 (15a, 15b) communicates with a plurality of other small chambers facing each other. These disc-shaped flow guide units 14 (14a to 14f) are stacked on top of each other so that discs of the same diameter are adjacent to each other, and the main cylinder body 1
b is placed perpendicular to the flow direction in the hollow interior of the tube. Incidentally, large-diameter disks 16 are positioned on both sides so that the opening 6 and outlet 7 of the main cylinder 1b correspond to the communication holes 18. Moreover, the large-diameter disk 1 of the disk-shaped flow guide unit 14 (14a to 14f)
6 and the small-diameter disk 17 are preferably integrated by gluing the front portions of the small chambers that are joined to each other.

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副筒体1aの入口2か
ら内部に導入する。副筒体」aに導入された流体は第1
図に矢印で示したように互いに連通する筒状導流単位体
8(8a,8b)の各小室9(9a)及び9(9b)を
順次通過しながら軸方向に流動する。そして、各小室9
(9a)及び9(9b)を通過する過程で側壁に衝突し
て流れは複雑に反転し、渦流を生じて盛んに流体の混合
が行われる。このように各小室9(9a)及び9(9b
)を通過することによつて分散、反転、渦流作用を繰り
返えしながら予備混合された流体は端板4の開口6から
主筒体1b内に入る。そして、第1の円板状導流単位体
14(14a)の流通孔18からその内部に達し、小径
な円板17により直進を防そげられて方向を変え、互い
に連通する小室15(15a)及び15(15b)を通
過しながら中央部から外側に向かつて故射状に流動する
。この小室15(15a)及び15(15b)を通過す
る過程で前述の予備混合と同じように分散、反転、渦流
作用により混合が行われる。
The apparatus of the present invention configured as described above introduces two or more different types of fluids into the interior through the inlet 2 of the sub-cylindrical body 1a using appropriate pressure-feeding means. The fluid introduced into the sub cylinder a is
As shown by the arrows in the figure, the fluid flows in the axial direction while successively passing through the small chambers 9 (9a) and 9 (9b) of the cylindrical flow guide unit 8 (8a, 8b) that communicate with each other. And each small room 9
In the process of passing through (9a) and 9 (9b), the flow collides with the side wall and reverses in a complicated manner, creating a vortex and actively mixing the fluids. In this way, each small room 9 (9a) and 9 (9b
), the premixed fluid enters the main cylindrical body 1b from the opening 6 of the end plate 4 while repeating dispersion, reversal, and vortex action. Then, it reaches the inside of the first disc-shaped flow guide unit 14 (14a) through the flow hole 18, is prevented from going straight by the small-diameter disc 17, changes direction, and forms small chambers 15 (15a) that communicate with each other. and 15 (15b) while flowing outward from the center in a radial shape. In the process of passing through the small chambers 15 (15a) and 15 (15b), mixing is performed by dispersion, inversion, and vortex action in the same manner as the premixing described above.

しかして、主筒体1bの内周面に到達した流体はその内
周面と小径な円板17とによつて形成された流路19か
ら第2の円板状導流単位体14(14b)の各小室(1
5a)及び15(15b)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18から第3の円板状導流単位体14(14
c)の内部に入る。
The fluid that has reached the inner circumferential surface of the main cylindrical body 1b passes through the flow path 19 formed by the inner circumferential surface and the small-diameter disk 17 to the second disk-shaped flow guide unit 14 (14b). ) each small room (1
5a) and 15 (15b), the dispersion as described above,
It gathers in the center while repeating reversal and vortex action,
The third disc-shaped flow guide unit 14 (14
c) Go inside.

そして再度各小室15(15a)及び15(15b)を
通過しながら中央部から外側に向かつて故射状に流動し
最終的に出口4から排出される。第7図に示した実施例
は、副筒体1aの胴部側方に別の流体の入口20を設け
、その入口部分に空間部21を形成したものである。
Then, while passing through each of the small chambers 15 (15a) and 15 (15b) again, it flows radially from the center toward the outside, and is finally discharged from the outlet 4. In the embodiment shown in FIG. 7, an inlet 20 for another fluid is provided on the side of the body of the sub-cylindrical body 1a, and a space 21 is formed at the inlet.

この実施例の場合、例えば入口2から水と有機界面活性
剤等の添加材の2液を流入させ、別の入口20から水を
流入させれば、これら3液をきわめて効率よく混合させ
ることができる。また、第8図及び第9図は円板状導流
単位体14の別の実施例を示し、大小2枚の円板16,
17の中心部を除く夫々の小室15(15a)及び15
(15b)の底面に、該小室の上面の高さより低くした
突起22を設けたものである。
In the case of this embodiment, for example, if two liquids, water and an additive such as an organic surfactant, are allowed to flow in from the inlet 2, and water is allowed to flow in from another inlet 20, these three liquids can be mixed extremely efficiently. can. Further, FIGS. 8 and 9 show another embodiment of the disc-shaped flow guiding unit 14, in which two large and small discs 16,
Each small chamber 15 (15a) and 15 except the center of 17
A protrusion 22 is provided on the bottom surface of (15b), which is lower than the height of the top surface of the small chamber.

これによつて、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ことができる。そして、前記
突起22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
発明装置によれば副筒体1a内に流れ方向と同一方向に
複数の筒状導流単位88(8a,8b)を同心状に重層
して配置し、主筒体1b内には流れ方向と直角に複数の
円板状導流単位体14(14a〜14f)を配置し、こ
れら筒状導流単位体8(8a,8b)及び円板状導流単
位体14(14a〜14f)に配列した多数の小室9(
9a,9b)及び15(15a,15b)により流体が
通過する過程において分散、反転、渦流作用を生じさせ
、さらに副筒体1a及び主筒体1bにおける流体の流れ
方向の変化により乱流効果が一層高められるので、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。
Thereby, it is possible to increase the shearing force of the fluid in the convection phenomenon when the fluid flows into the small chamber. By making the protrusions 22 smaller as they approach the center, the volume of each chamber is made uniform, and smooth fluid flow is ensured. As described above in the embodiments, according to the device of the present invention, a plurality of cylindrical flow guide units 88 (8a, 8b) are arranged concentrically and stacked in the same direction as the flow direction in the sub-cylindrical body 1a, A plurality of disc-shaped flow guide units 14 (14a to 14f) are arranged in the main cylinder 1b at right angles to the flow direction, and these cylindrical flow guide units 8 (8a, 8b) and the disc-shaped flow guide units 14 (14a to 14f) are arranged at right angles to the flow direction. A large number of small chambers 9 (
9a, 9b) and 15 (15a, 15b) cause dispersion, reversal, and eddy current effects in the process of fluid passage, and furthermore, changes in the flow direction of the fluid in the sub-cylindrical body 1a and the main cylinder body 1b produce turbulent flow effects. This provides much more effective mixing than any conventional mixing device.

また、本発明装置によれば副筒体1aの内部で予備的に
混合作用を受け、その上主筒体1bの内部で混合作用を
受け、さらには主筒体1bの内部において流体を中央か
ら外側へ又は外側から中央へと故射状に分散と集合を交
互に操り返えして混合させるものであるから、高い混合
効果が得られる。
Further, according to the device of the present invention, the fluid is preliminarily mixed inside the sub cylinder 1a, mixed inside the main cylinder 1b, and furthermore, the fluid is mixed inside the main cylinder 1b from the center. Since the mixture is mixed by alternating dispersion and aggregation in a radial manner outward or from the outside to the center, a high mixing effect can be obtained.

【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図は装置全体の縦断正
面図、第2図は筒状導流単位体の斜視図、第3図は筒状
導流単位体の重層状態を示す部分拡大図、第4図イは円
板状導流単位体を構成する大径な円板の斜視図、第4図
岨ま同じく小径な円板の斜視図、第5図は要部の拡大縦
断側面図、第6図は要部の拡大縦断正面図、第7図は他
の実施例の装置全体の縦断正面図、第8図は第5図の他
の実施例図、第9図は同じく第6図の他の実施例図であ
る。 1a・・・・・・副筒体、1b・・・・・・主筒体、8
(8a,8b)・・・・・・筒状導流単位体、9(9a
,9b)・・・・・・菱形の小室、14(14a〜14
f)・・・・・・円板状導流単位体、15(15a,1
5b)・・・・・・六角形状の小室、16・・・・・・
大径な円板、17・・・・・・小径な円板、18・・・
・・・流通孔、22・・・・・・突起。
The figures show an embodiment of the present invention, in which Fig. 1 is a longitudinal sectional front view of the entire device, Fig. 2 is a perspective view of a cylindrical flow guiding unit, and Fig. 3 is a layered state of the cylindrical flow guiding unit. Partially enlarged view, Figure 4A is a perspective view of a large-diameter disk constituting the disk-shaped flow guide unit, Figure 4A is a perspective view of a similarly small-diameter disk, and Figure 5 is an enlarged view of the main part. 6 is an enlarged vertical sectional front view of the main parts, FIG. 7 is a vertical sectional front view of the entire device of another embodiment, FIG. 8 is a diagram of another embodiment of FIG. 5, and FIG. FIG. 7 is another embodiment diagram similar to FIG. 6; 1a... Sub cylinder body, 1b... Main cylinder body, 8
(8a, 8b)...... Cylindrical flow guide unit, 9 (9a
, 9b)...Rhombic chamber, 14 (14a-14
f)...Disc-shaped flow guiding unit, 15 (15a, 1
5b)... Hexagonal small chamber, 16...
Large diameter disc, 17...Small diameter disc, 18...
...Flow hole, 22...Protrusion.

Claims (1)

【特許請求の範囲】 1 流体が通る比較的小径な副筒体と大径な主筒体とを
備え、副筒体内には円筒状に形成され、かつ菱形の小室
を多数配列して網目状に形成した複数の筒状導流単位体
が同心状に重層して流れ方向と同一方向に配置され、さ
らに前記筒状導流単位体の互いの小室は対向する他の筒
状導溶単位体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、前記主筒体内には大小2枚の円板を
同心的に重合し、かつ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複数の円板状導
流単位体が同径の円板を重ね合わせて流れ方向と直角に
並べて配置され、前記大径な円板は主筒体の内周面に密
接する直径を有し、かつ中心に流通孔が穿設されており
、さらに前記大径な円板の小室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いる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。
[Scope of Claims] 1. Comprising a relatively small-diameter secondary cylinder through which fluid passes and a large-diameter main cylinder, the secondary cylinder is formed into a cylindrical shape and has a mesh-like structure in which a large number of diamond-shaped small chambers are arranged. A plurality of cylindrical flow guiding units formed in the cylindrical flow guiding units are concentrically stacked and arranged in the same direction as the flow direction, and furthermore, each of the small chambers of the cylindrical flow guiding units is formed in the opposite cylindrical flow guiding unit. They are arranged at different positions so as to communicate with a plurality of small chambers, and the main cylinder has two large and small disks concentrically superimposed on each other, and polygonal small chambers with open fronts on opposing surfaces. A plurality of disc-shaped flow guiding units arranged in a honeycomb shape are arranged perpendicularly to the flow direction by overlapping discs of the same diameter, and the large-diameter discs are arranged on the inner circumferential surface of the main cylinder. They have closely spaced diameters and are provided with a communication hole in the center, and the small chambers of the large-diameter disk and the small chambers of the small-diameter disk communicate with a plurality of other small chambers facing each other. A fluid mixing device characterized in that the fluid mixing device is arranged at different positions. 2. The fluid mixing device according to claim 1, wherein a protrusion lower than the top surface of the small chamber is provided on the bottom surface of each small chamber except for the center 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.
JP57015258A 1982-02-01 1982-02-01 fluid mixing device Expired JPS5939174B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57015258A JPS5939174B2 (en) 1982-02-01 1982-02-01 fluid mixing device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57015258A JPS5939174B2 (en) 1982-02-01 1982-02-01 fluid mixing device

Publications (2)

Publication Number Publication Date
JPS58133823A JPS58133823A (en) 1983-08-09
JPS5939174B2 true JPS5939174B2 (en) 1984-09-21

Family

ID=11883824

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57015258A Expired JPS5939174B2 (en) 1982-02-01 1982-02-01 fluid mixing device

Country Status (1)

Country Link
JP (1) JPS5939174B2 (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0472491B1 (en) * 1990-08-23 1995-02-22 Sulzer Chemtech AG Static laminar mixing device, admixing device, as well as the use of the mixing and admixing device
JPH0857279A (en) * 1994-08-24 1996-03-05 Kankyo Kagaku Kogyo Kk Stationary mixer
DE20002920U1 (en) 2000-02-18 2000-04-20 Schroeder & Boos Misch Und Anl Homogenizer
CA2584955C (en) * 2006-05-15 2014-12-02 Sulzer Chemtech Ag A static mixer
US8740450B2 (en) * 2008-01-10 2014-06-03 Mg Grow Up Corp. Static fluid mixer capable of ultrafinely mixing fluids
JP6538952B1 (en) * 2018-12-11 2019-07-03 株式会社西村ケミテック Polishing fluid supply device

Also Published As

Publication number Publication date
JPS58133823A (en) 1983-08-09

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