JPS58150421A - Mixer - Google Patents
MixerInfo
- Publication number
- JPS58150421A JPS58150421A JP57033705A JP3370582A JPS58150421A JP S58150421 A JPS58150421 A JP S58150421A JP 57033705 A JP57033705 A JP 57033705A JP 3370582 A JP3370582 A JP 3370582A JP S58150421 A JPS58150421 A JP S58150421A
- Authority
- JP
- Japan
- Prior art keywords
- space
- filled
- flow passage
- bodies
- forming body
- 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
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/40—Static mixers
- B01F25/42—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
- B01F25/43—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
- B01F25/432—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction with means for dividing the material flow into separate sub-flows and for repositioning and recombining these sub-flows; Cross-mixing, e.g. conducting the outer layer of the material nearer to the axis of the tube or vice-versa
- B01F25/4323—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction with means for dividing the material flow into separate sub-flows and for repositioning and recombining these sub-flows; Cross-mixing, e.g. conducting the outer layer of the material nearer to the axis of the tube or vice-versa using elements provided with a plurality of channels or using a plurality of tubes which can either be placed between common spaces or collectors
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/40—Static mixers
- B01F25/45—Mixers in which the materials to be mixed are pressed together through orifices or interstitial spaces, e.g. between beads
- B01F25/452—Mixers in which the materials to be mixed are pressed together through orifices or interstitial spaces, e.g. between beads characterised by elements provided with orifices or interstitial spaces
- B01F25/4524—Mixers in which the materials to be mixed are pressed together through orifices or interstitial spaces, e.g. between beads characterised by elements provided with orifices or interstitial spaces the components being pressed through foam-like inserts or through a bed of loose bodies, e.g. balls
- B01F25/45241—Mixers in which the materials to be mixed are pressed together through orifices or interstitial spaces, e.g. between beads characterised by elements provided with orifices or interstitial spaces the components being pressed through foam-like inserts or through a bed of loose bodies, e.g. balls through a bed of balls
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/40—Static mixers
- B01F25/45—Mixers in which the materials to be mixed are pressed together through orifices or interstitial spaces, e.g. between beads
- B01F25/452—Mixers in which the materials to be mixed are pressed together through orifices or interstitial spaces, e.g. between beads characterised by elements provided with orifices or interstitial spaces
- B01F25/4524—Mixers in which the materials to be mixed are pressed together through orifices or interstitial spaces, e.g. between beads characterised by elements provided with orifices or interstitial spaces the components being pressed through foam-like inserts or through a bed of loose bodies, e.g. balls
- B01F25/45242—Mixers in which the materials to be mixed are pressed together through orifices or interstitial spaces, e.g. between beads characterised by elements provided with orifices or interstitial spaces the components being pressed through foam-like inserts or through a bed of loose bodies, e.g. balls through a bed of fibres, steel wool or wood chips
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/40—Static mixers
- B01F25/45—Mixers in which the materials to be mixed are pressed together through orifices or interstitial spaces, e.g. between beads
- B01F25/452—Mixers in which the materials to be mixed are pressed together through orifices or interstitial spaces, e.g. between beads characterised by elements provided with orifices or interstitial spaces
- B01F25/4524—Mixers in which the materials to be mixed are pressed together through orifices or interstitial spaces, e.g. between beads characterised by elements provided with orifices or interstitial spaces the components being pressed through foam-like inserts or through a bed of loose bodies, e.g. balls
- B01F25/45243—Mixers in which the materials to be mixed are pressed together through orifices or interstitial spaces, e.g. between beads characterised by elements provided with orifices or interstitial spaces the components being pressed through foam-like inserts or through a bed of loose bodies, e.g. balls through a foam or expanded material body
Landscapes
- Chemical & Material Sciences (AREA)
- Dispersion Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Wood Science & Technology (AREA)
- Nozzles (AREA)
- Processes Of Treating Macromolecular Substances (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は数種の液体乃至Ｒ動体を混合する丸めの！中す
一に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention is a method for mixing several types of liquids or moving bodies. This is about the middle school.
数種の液体乃至流動体、九とえば２液性の塗料や壷着剤
のように主剤と硬化剤とから構成される−のを温合する
場合、一般的には動力を用いて攪拌させることが行なわ
れている。しかしながらこのものにあっては大盤化や機
構の複雑化はさけられず、この丸めに近年無駆１１１ｍ
、いわゆるスタティック塵と揶される！十す−が提供さ
れている。When warming several types of liquids or fluids, such as two-component paints and adhesives, which consist of a main agent and a curing agent, power is generally used to stir them. things are being done. However, it is unavoidable for this type of machine to become larger and the mechanism to become more complicated, and in recent years, this type of car has become 111 m long without a driver.
, is nicknamed static dust! Ten suu are provided.
乙の！中す−としては特公昭５４−２７９８５号公ＩＩ
Ｋ示されているように、送入口と排出口とを夫々設は九
二個の端盤間に、これら各端盤に設は九適蟲長さの数個
の流通溝の・両端を交互に連通する適当長さの数個の貫
通孔を同心状に穿設し丸中間盤を介入し、これを一体的
に結合して両端盤間にジグザク状の流通路を形成し友も
のが知られている。この−のにあっては送入口からジグ
ザク状の流通路内に圧送される数種の液体乃至流動体は
ジグザク状の流通路内を通る際に細分合流を反復して温
合されるわけであシ、構成部品４少なく、を九可一部材
を要しないことから無故障、無振動等の多くの利点を備
えているのであるが、ただこのものくおいてはジグザク
状の流通路が長いほど混合の均一化の点で好ましいもの
の、充分な長さの流通路を設けるとなると、どうして−
径を大きくしなくてはならず、多段に構成することで径
の増大を防ぐとしてもこの場合は構成部品数が増えてし
まうという問題点を有しておシ、ｔえ適蟲長亀の流通溝
及び貫通孔を機械加工で設けるとなると、ジクザタ状流
通路を長くすればするほど加工費も高くなってしまう。Oh no! As a medium, Special Publication No. 54-27985 II
As shown in the figure, the inlet and outlet are each installed between 92 end plates, and each end plate is provided with several flow grooves of 92 mm length alternately at both ends. Several through-holes of suitable length are concentrically drilled to communicate with each other, a round intermediate plate is inserted, and these are integrally connected to form a zigzag-shaped flow path between both end plates. It is being In this case, several types of liquids or fluids are pumped from the inlet into the zigzag-shaped flow path and are heated by repeating subdivision and merging as they pass through the zigzag-shaped flow path. It has many advantages such as no failures and no vibrations because it has fewer legs and 4 components and does not require any flexible parts. Although this is preferable from the point of view of uniform mixing, it is difficult to provide a flow path of sufficient length.
The diameter must be increased, and even if the increase in diameter is prevented by configuring it in multiple stages, there is a problem that the number of component parts will increase in this case. If the flow grooves and through holes are provided by machining, the longer the staggered flow path is, the higher the processing cost will be.
本発明はこのような点に鑑み為され丸ものであシ、その
目的とするとζろは小臘化、特に小径化を図ることがで
きる上に、小径とし九場合にも充分な混合の均一化を行
なうことができ、ま九安価に製作し得る二重サーを提供
するＫＴｏす、他の目的とするとζろは洗浄が容重であ
）、部分的Ｋｌｌ留を生じ九）することがなく、更に混
合の均一化がよ）促進される二中す−を提供するにある
。The present invention was created in view of these points, and has a round shape.The purpose of the present invention is to make the ζ-rotate small in size, especially in diameter, and to achieve sufficient uniformity of mixing even when the diameter is small. For other purposes, it is difficult to clean and does not cause partial Kll retention. Furthermore, it is an object of the present invention to provide a second medium which further promotes uniform mixing.
すなわち本発明は一端に送入口を具備し且つ他端に排出
口を具備する管路内に、多数個の粒状体や針状体あるい
は連続発泡体等の綱状流路形成体を充填して３次元的な
網状流路を形成し九構成として、数種の液体乃至８１１
１体が圧送されて送入口から排出口へと至る関に通過す
る流路が、ラシタムで且つきわめて多岐なものである上
に合流離散が幾度と゛なく繰シ返される３次元的な網状
流路であるために１この綱状流路を通る数種の液体万至
流一体の綱０分化と合流とがいわば際限なく威され。That is, in the present invention, a plurality of granules, needles, continuous foams, or other linear channel-forming bodies are filled in a conduit having an inlet at one end and an outlet at the other end. It forms a three-dimensional network flow path and has nine configurations, allowing several kinds of liquids to 811
The flow path through which one body is pumped from the inlet to the outlet is a lacitum and extremely diverse, and it is a three-dimensional network flow path in which merging and dispersion are repeated many times. Because of this, the differentiation and merging of several types of fluids passing through this rope-like flow path are endless.
、従って混合の均一化が充分になされるようにし圧点に
％黴を有するものであって、以下ｔｇ承ＩＩＩ雄例に轟
いて詳述すれば、第１図において図中−は内径が２０−
＋ＭＩ＆の比較的小径の管であって、その内部は隔壁（
１）によって軸方向に直列的に並ぶ複数個の空間［Ｉ
Ｉｌｌ Ｋ仕切られている。隔４１１（７）は第３８１
！乃至第４図に示すように両端面で開口する小径の貫通
孔ｉｌｌを複数個有する−ので、特に各貫通孔園を円盤
状の隔壁、（７）の軸と平行とするのではなく、一端開
口の位置する部分の径が他端開口の位置する部分の径よ
りも大きく、シかも一端開口を他端開口よシも隔＠ Ｔ
７）の軸のまわシに回転させ九位置に配置して隔壁（７
）の軸と貫通孔（組の軸とが３次元的に交叉しないよう
Ｋしである。？：、の隔壁（７）を数枚、面が交互に逆
になるように１ま九一方の隔壁（１）の中央の軸孔（１
０に一端の小径軸部（Ｉ呻がさし込まれる軸体（９）と
、す：Ｊり状のスペーサ舖とを交互Ｋ１１４壁（１）間
に配置して軸体（１＋のまわシと、スベーＷａＳの内部
とに夫々空間（り （３）を形成しているものであ珈、
そして軸体（！Ｉ）と管−内周面との間の円筒状の空間
（！）Ｋはビーズのような粒体（４）を°充填すゐこと
によ、つて、３次元的な網状流路を形成しである。ζ（
４）を示しているが、ビーズ以外に４たとえば砂粒、金
属球等の粒体な用いても曳く、更には粒状体に代えて針
条乃至棒状体を多数個充填し九シ、あるいは細いセルを
有する合成樹脂の連続発泡体を充填し九）することで３
次元的な網状流路を形成しても良い、しかし、この網状
流路形成体を！中す− ｉｌｌ Ｋ洗浄液を通して行な
う洗浄性の点から鑑みれば、ガうスやセラニックのビー
ズ、っｔ、６球状粒体を用いるのが好ましい、しかして
、この！中す−＋１Ｈｃ一端送入口（６）から流入する
数種の液体乃遷流動体は、１ｌＥ１段の隔壁（７）の貫
通孔（１）を過って空間（！ｌ内に流入する際に貫通孔
（８）の軸の方向から旋回流となっておシ、そして３次
元的な網状流路を通過する間に細分化と合流とが幾度と
な（繰シ返され死後、第２段の隔壁（７）の貫通孔＋８
１を通過してスペーサｌ１１１で囲まれた小さい空間（
３１Ｋ ｍる。この時には混合液がやはり貫通孔（８）
の軸の方向の丸めに求心方向に向かう旋回流として空間
（１）内に各貫通孔＋８１から流入することから、温合
が促進され、次いで再度空間（鵞）内の３次元的な網状
流路を通って排出口（＠）に至る。, therefore, the mixture is sufficiently homogeneous and has % mold at the pressure point, and will be described in detail below in the example of TG Registration III. −
+MI& is a relatively small diameter tube with a partition wall (
1), multiple spaces [I
Ill K is partitioned. Interval 411 (7) is the 381st
! As shown in Fig. 4, it has a plurality of small-diameter through-holes that are open on both end faces. The diameter of the part where the opening is located is larger than the diameter of the part where the opening at the other end is located, and there may be a distance between the opening at one end and the opening at the other end.
Rotate the shaft of 7) and place it in the 9th position and attach the bulkhead (7).
) and the axis of the through hole (set of axes should not intersect three-dimensionally.). The central shaft hole (1) of the partition wall (1)
The shaft (9) into which the small diameter shaft (I) is inserted at one end of the shaft (1) and the J-shaped spacer (1) are arranged alternately between the K114 walls (1). and the inside of Sube WaS, respectively, forming a space (3).
The cylindrical space (!) K between the shaft body (!I) and the inner peripheral surface of the tube is filled with beads-like particles (4), thereby creating a three-dimensional space. This forms a net-like channel. ζ(
4), but in addition to beads, granules such as sand grains and metal balls may also be used, and in place of the granules, many needles or rods may be filled to form 9-cell or thin cells. 9) By filling the open synthetic resin foam with
It is possible to form a dimensional network channel, but this network channel formation body! From the point of view of cleaning performance through medium K cleaning solution, it is preferable to use Gauss or Ceramic beads or 6 spherical particles. Several kinds of liquids and transitional fluids flowing from the inlet port (6) at one end of the center pass through the through hole (1) of the partition wall (7) in the first stage of 1lE and flow into the space (!l). The flow becomes a swirling flow from the direction of the axis of the through hole (8), and as it passes through the three-dimensional network flow path, it subdivides and merges several times (repeatedly, after death, the second stage Through hole in partition wall (7) +8
A small space passing through 1 and surrounded by spacer l111 (
31km. At this time, the mixed liquid still flows through the through hole (8).
Warming is promoted as the swirling flow flows in the centripetal direction into the space (1) from each through hole +81 in the rounding direction of the axis of Go through the road to the outlet (@).
ここで網状流路形成体を充填する空間（りが軸体（９）
を中央に位置させることで円筒状となっているのは、ま
圧空関（３）が管叫の内径よ°）もスペーサ０１によっ
て小径となっているのは、隔壁（１）の支持を軸体ｆｓ
＋やスペーサＩで行なうという点による消極的な作用か
らだけではなく、空間（２）内に流入した混合液が一部
において滞留し九りすることがないようにすることを、
貫通孔（８）の設けた位置や貫通孔（８）の方向ととも
に狙つ九本のであって、混合させる数種の液体乃至流動
体が２液性の塗料や接着剤のように混合されることで硬
化を開始するものが、！中す−（１）内における滞留時
間が長くて内部で硬化しでしまうことがないようにして
いるものである。を九貫通孔閑の方向性については混合
液を旋回させる仁とで混合の均一化をよ）促進すること
に亀なっている。Here, the space (rigashaft (9)
The reason why it has a cylindrical shape by positioning it in the center is because the pressure air barrier (3) has a smaller diameter than the inside diameter of the tube due to the spacer 01. body fs
This is not only due to the negative effect of using + and spacer I, but also to prevent the mixed liquid that has flowed into space (2) from stagnation in a part of the space (2).
The nine holes are aimed at the location of the through hole (8) and the direction of the through hole (8), and several types of liquids or fluids to be mixed are mixed like two-component paint or adhesive. Things that start to harden! The residence time in the medium (1) is long enough to prevent it from curing inside. The nine through-holes are designed to swirl the mixed liquid and promote uniform mixing.
空間Ｃりの長さやその数は第２１１に４示すように適宜
設定すれば良い本のであシ、送入口ｍと排出口（＠）と
の間に網状流路形成体が充填される空間偉）のみを１つ
だけ設は九本のであって４ｈＪＩＩＬ＜、を九貫通孔（
８）の数や位置を考慮するならばこの空間（！）が円筒
状でなくて龜良い、崗、１ｓ２図においては網状流路形
成体を省略している。を九、混合すべき数種の液体乃至
流動体としてｚ液性の塗料や接着剤に関してのみ触れ一
＃−が、その他何らかの添加剤を主剤Ｋｌａ合する場合
、九とえば発泡剤を主剤に混合する場合など他方面に利
用できることはも ゛ちろんである。The length of the space C and the number thereof may be set appropriately as shown in No. 211-4. ) only one through hole (4hJIIL<, nine through holes (
Considering the number and position of 8), it is better that this space (!) is not cylindrical, and the net-like channel forming body is omitted in Figure 1s2. (9) As several liquids or fluids to be mixed, only Z-liquid paints and adhesives are mentioned. (1) When some other additives are combined with the main ingredient (9), for example, a blowing agent may be mixed into the main ingredient. Of course, it can also be used for other purposes, such as when
以上のように本発明にあっては多数個の粒状体や針状体
あるいは連続発泡体等の網状流路形成体を管路内に充填
して３次元的な網状流路を形成し九−のであることから
、この網状流路を通過する関に混合が充分に且つ均一に
なされることはもちろん、網状流路において分岐や合流
する箇所の数を管路の全長や径に比してきわめて多くと
れるも。As described above, in the present invention, a three-dimensional network channel is formed by filling a pipe with a large number of network channel forming bodies such as granules, needles, or open foam. Therefore, it is necessary to ensure sufficient and uniform mixing as it passes through this network channel, and also to ensure that the number of branching and merging points in the network channel is extremely small compared to the total length and diameter of the pipeline. You can get a lot.
のであるとと４に機械加工によらずと龜良りえめに小型
で安価に製作できる本のであり、また充分に均一な混合
を得られるＫもかかわらず小型にできることから、たと
えば２液性の塗料を混合吐出する場合、吐出器として手
持型のスプレーカシを使う時にもこのスプレーカシにミ
＋サーを取付は良り内蔵させ九りして混合液用の配管を
最短とするようなこと本できるものである。4. It is a small and inexpensive product that can be manufactured without using machining, and it can be made small despite being able to obtain a sufficiently uniform mixture. When mixing and dispensing paint, it is a good idea to attach a mixer to the spray dispenser when using a handheld spray dispenser as a dispensing device. It is possible.
第１図は本発明一実施例の断面図、第２図（１）Φ）は
他例の断面図、第３図（ａ） （ｂ） 社同上の隔壁の
断面図及び平（１図、第４図体）（ａ）は他の隔壁の断
面図及び軸体の正面図である。
１１）は！中す−、ｆ！ｌ ［３１は空間、（４）は網
状流路形成体としての粒体、（ｉ）ａ送入口、（１）は
排出口、（））は隔壁、（畠）は貫通孔を示す。
代理人 弁理士 石 １）長 七
第１図 第２図
（０） （ｂ）
第３図
（ａ） （ｂ）
第４図
（０） （ｂ）
手続補正書（方式ン
１ 事件の表示
三重す−
４代理人
郵便番号 ５３０
５ 補正命令の日付
昭和５７年６月１１日
７ 補正の対象
明細書
８ 補正の内容 明細書第９頁第１８行目の「第４図」
の次１１６−Fig. 1 is a cross-sectional view of one embodiment of the present invention, Fig. 2 (1) Φ) is a cross-sectional view of another example, Fig. 3 (a) (b) is a cross-sectional view of the above partition wall, and a plane (Fig. 1, Figure 4) (a) is a sectional view of another partition wall and a front view of the shaft body. 11) Ha! Nakasu-, f! l [31 is a space, (4) is a grain as a network channel forming body, (i) a inlet, (1) is an outlet, ()) is a partition, and (bata) is a through hole. Agent Patent Attorney Ishi 1) Chief 7 Figure 1 Figure 2 (0) (b) Figure 3 (a) (b) Figure 4 (0) (b) Procedural Amendment (Method 1 Case Display Mie) S- 4 Agent postal code 530 5 Date of amendment order June 11, 1980 7 Specification subject to amendment 8 Contents of amendment "Figure 4" on page 9, line 18 of the specification
Next 116-
Claims (1)
る管路内に１多数個の粒状体や針状体あるいは連続発泡
体等の網状流路形成体を充填して３次元的な綱状、流路
を形成して成ることを特徴とす一ズのような球状の粒体
であることを特徴とする特許請求の範囲第１項記載の三
十す−。 （３） 管路内は送入孔と排出孔とに対して夫々小径
の貫通孔を備えた隔壁で仕切られ圧空間を有してこの空
間内に網状流路形成体が充填されていることを特徴とす
る特許請求の範ｉ！Ｉ嬉１項又は第２項１絨の三十す−
。 ｉ４１ 貫通孔はその両端開口位置が管路の軸のまわ
りにずれた位置にあることを特徴とする特許請求の範囲
第３項記載の！キサ−。 （６）空間は送入口と排出口との間に直列的に数個設け
られて、１つお書の空間内に綱状流路形成体が充填され
てお９、各空間を仕切っている噛壷九設けられ九貫通孔
は網状流路形成体の充填され圧空間に開口する一喝開口
位置が、調伏流路ｉ！ｊ成体の充填されておらない空間
に開口する他端開口位置よりも外周１１１に位置してい
ることを特徴とする特許請求の範囲第３項又は１１４墳
記載の！キサ−・ （６）網状流路形成体が充填されている空間は円筒状で
あることを特徴とする特許請求の範囲第５項記載の！キ
サ−。 （７）網状流路形成体が充填されておらない空間は管路
内径よシー小径であることを特徴とする特許請求の範ａ
ＳＳ項記載の！キサ−。[Scope of Claims] 11) One or more network channel forming bodies such as granular bodies, needle-shaped bodies, or open foam bodies are installed in a conduit having an inlet at one end and an outlet at the other end. Thirty glasses according to claim 1, characterized in that they are filled with particles to form a three-dimensional rope shape and a flow path, and are spherical particles like beads. −. (3) The inside of the pipe is partitioned by a partition wall having small-diameter through holes for the inlet hole and the discharge hole, respectively, and has a pressure space, and this space is filled with a mesh channel forming body. Claims i! 1st term or 2nd term 1 carpet of thirty su-
. i41 The opening positions of both ends of the through-hole are shifted from each other around the axis of the conduit, according to claim 3! Kisa. (6) Several spaces are provided in series between the inlet and the outlet, and each space is filled with a rope-shaped channel forming body 9 to partition each space. The opening position of the nine through-holes, which are provided in the chewing pot and open into the pressure space filled with the net-like flow path forming body, is the adjustment flow path i! j Claim 3 or 114, characterized in that it is located on the outer periphery 111 from the other end opening position that opens into a space that is not filled with an adult! (6) The space filled with the network channel forming body is cylindrical, as set forth in claim 5! Kisa. (7) Claim a characterized in that the space that is not filled with the network channel forming body has a diameter smaller than the inner diameter of the pipe.
As stated in the SS section! Kisa.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57033705A JPS606689B2 (en) | 1982-03-03 | 1982-03-03 | mixer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57033705A JPS606689B2 (en) | 1982-03-03 | 1982-03-03 | mixer |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58150421A true JPS58150421A (en) | 1983-09-07 |
| JPS606689B2 JPS606689B2 (en) | 1985-02-20 |
Family
ID=12393830
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP57033705A Expired JPS606689B2 (en) | 1982-03-03 | 1982-03-03 | mixer |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS606689B2 (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5348706A (en) * | 1990-04-26 | 1994-09-20 | Minnesota Mining And Manufacturing Company | Calibration system and method for making |
| US5420038A (en) * | 1990-04-26 | 1995-05-30 | Minnesota Mining And Manufacturing Company | Calibration system and housing |
| US5863129A (en) * | 1998-01-05 | 1999-01-26 | Gary A. Smith | Serial resin mixing devices |
| CN1313214C (en) * | 2005-03-23 | 2007-05-02 | 太原理工大学 | Dual-component automatic spray painting device |
| US7763456B2 (en) | 2006-09-28 | 2010-07-27 | University Of Washington | 3D micro-scale engineered tissue model systems |
| US8247464B2 (en) | 2006-09-28 | 2012-08-21 | University Of Washington | Method of selective foaming for porous polymeric material |
| US8403557B2 (en) * | 2006-09-28 | 2013-03-26 | University Of Washington | Micromixer using integrated three-dimensional porous structure |
| CN103111033A (en) * | 2013-02-26 | 2013-05-22 | 王靖 | Gas-liquid mixing device |
-
1982
- 1982-03-03 JP JP57033705A patent/JPS606689B2/en not_active Expired
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5348706A (en) * | 1990-04-26 | 1994-09-20 | Minnesota Mining And Manufacturing Company | Calibration system and method for making |
| US5420038A (en) * | 1990-04-26 | 1995-05-30 | Minnesota Mining And Manufacturing Company | Calibration system and housing |
| US5863129A (en) * | 1998-01-05 | 1999-01-26 | Gary A. Smith | Serial resin mixing devices |
| CN1313214C (en) * | 2005-03-23 | 2007-05-02 | 太原理工大学 | Dual-component automatic spray painting device |
| US7763456B2 (en) | 2006-09-28 | 2010-07-27 | University Of Washington | 3D micro-scale engineered tissue model systems |
| US8247464B2 (en) | 2006-09-28 | 2012-08-21 | University Of Washington | Method of selective foaming for porous polymeric material |
| US8403557B2 (en) * | 2006-09-28 | 2013-03-26 | University Of Washington | Micromixer using integrated three-dimensional porous structure |
| CN103111033A (en) * | 2013-02-26 | 2013-05-22 | 王靖 | Gas-liquid mixing device |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS606689B2 (en) | 1985-02-20 |
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