JPH0857278A - Method for finely pulverizing substance and apparatus therefor - Google Patents
Method for finely pulverizing substance and apparatus thereforInfo
- Publication number
- JPH0857278A JPH0857278A JP6202246A JP20224694A JPH0857278A JP H0857278 A JPH0857278 A JP H0857278A JP 6202246 A JP6202246 A JP 6202246A JP 20224694 A JP20224694 A JP 20224694A JP H0857278 A JPH0857278 A JP H0857278A
- Authority
- JP
- Japan
- Prior art keywords
- substance
- liquid
- container
- mixture
- inlet
- 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.)
- Pending
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
- B01F25/45—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
Landscapes
- Chemical & Material Sciences (AREA)
- Dispersion Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Crushing And Grinding (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
Description
【０００１】[0001]
【産業上の利用分野】この発明は、薬品、食品、塗料、
化学などの各産業分野で扱う物質の微粒化方法及び装置
に関する。BACKGROUND OF THE INVENTION This invention relates to medicines, foods, paints,
The present invention relates to a method and an apparatus for atomizing substances handled in various industrial fields such as chemistry.
【０００２】２個以上のｎ個の物質が集まり形成されて
いる凝集体を液体中で解砕（破砕）し、液中にｎ個に近
い物質に分け散らし粗大な凝集体が存在しない液体を得
ることを分散と称し、又２種類以上のｍ種類の液体を混
合し、均一化した液体を得ることを乳化と称するが、こ
の発明ではこれらに破砕をも加えて微粒化と総称するこ
とにする。[0002] Aggregates formed by gathering two or more n substances together are crushed (crushed) in a liquid, and dispersed into liquids close to n substances to form a liquid without coarse aggregates. Obtaining is called dispersion, and obtaining a homogenized liquid by mixing two or more kinds of liquids is called emulsification. In the present invention, these are crushed and collectively called atomization. To do.
【０００３】[0003]
【従来の技術】従来、ｎ個の物質の粉体凝集物を液中に
て解砕する、いわゆる、分散処理を行なう場合、ボール
ミルやビーズミルが利用されていた。これらは、ボール
やビーズといった鋼球媒体同士間の運動衝突で起こる磨
砕を利用するものであった。2. Description of the Related Art Conventionally, a ball mill or a bead mill has been used in the case of carrying out a so-called dispersion treatment in which a powder aggregate of n substances is crushed in a liquid. These have utilized the grinding that occurs in the motional collision between steel ball media such as balls and beads.
【０００４】また、ｍ種類の液体を均一化する、いわゆ
る乳化処理を行なう場合、回転式撹拌機や高圧噴射式ホ
モジナイザが利用されていた。前者は槽中で羽根車を回
転するものであり、後者は単一ノズルからの高圧噴射に
よる衝撃を利用するものであった。Further, in the case of carrying out so-called emulsification treatment for homogenizing m kinds of liquids, a rotary stirrer and a high pressure jet homogenizer have been used. The former was to rotate the impeller in the tank, and the latter was to use the impact of high pressure injection from a single nozzle.
【０００５】[0005]
【発明が解決しようとする課題】しかし、これら従来の
ものは、夫々次のような問題点を抱えていた。即ち、ボ
ールミルやビーズミルは、液中分散に用いた場合、媒体
同士の衝突に基づく摩耗が生じ、これらが汚染物として
混入するという問題点があった。又、ｍ種の液体を乳化
する場合、回転式撹拌機においては、撹拌液体中に必然
的に吸気混入を生じ、それに基づく不測の事態や、溜込
み処理での長時間経由という問題点があり、高圧噴射式
ホモジナイザにおいては、単一噴射での衝撃を利用する
故に乳化の効率が低いという問題点があった。However, each of these conventional devices has the following problems. That is, the ball mill and the bead mill have a problem that when they are used for dispersion in a liquid, abrasion occurs due to collision of media with each other, and these are mixed as contaminants. Further, when emulsifying m kinds of liquids, in a rotary stirrer, there is a problem that inhalation is inevitably mixed in the stirring liquid, which causes an unexpected situation and a long time in the accumulation process. The high-pressure injection type homogenizer has a problem that the emulsification efficiency is low because the impact of a single injection is used.
【０００６】この発明は、前述の各問題点を解決すると
共に低コストでかつ高生産性を発揮する物質の微粒化方
法及び装置を提供することを目的としている。It is an object of the present invention to solve the above-mentioned problems and to provide a method and a device for atomizing a substance which is low in cost and exhibits high productivity.
【０００７】[0007]
【課題を解決するための手段】この発明は、前記目的を
達成するため、入口と出口とを有する容器に複数の球状
物を充填し、物質と液体との混合物を前記入口に供給
し、容器内の隣接球状物間の隙間を流し、出口から物質
を微粒化した状態で液体と共に取出すことを特徴とす
る。In order to achieve the above-mentioned object, the present invention fills a container having an inlet and an outlet with a plurality of spherical objects and supplies a mixture of a substance and a liquid to the inlet, It is characterized in that it flows through the gap between the adjacent spherical objects inside and takes out the substance together with the liquid in the atomized state from the outlet.
【０００８】[0008]
【作用】混合物が隣接球状物間の連続した隙間を流れる
際、乱流と流体音響効果で物質が微粒化され、分散及び
乳化を行なう。その際、球状物は運動せず、スタティッ
ク（静的）状態にあるので、汚染物即ちコンタミネーシ
ョンが極小となる。When the mixture flows through the continuous gap between the adjacent spherical substances, the substance is atomized by the turbulent flow and the hydroacoustic effect, and the substance is dispersed and emulsified. At that time, since the spherical object does not move and is in a static state, contaminants or contamination is minimized.
【０００９】[0009]
【実施例】以下、この発明の一実施例を図により説明す
る。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to the drawings.
【００１０】図１は、この発明の一実施例を示す装置概
念図で要部を縦断面で示すものであり、図２は図１のＩ
Ｉ−ＩＩ断面を示すものである。まず構成を説明する
に、図１及び図２において、１は原料、即ち物質と液体
との混合物を受入れる受入れ部である。即ち、分散の場
合は、ｎ個の物質（例、カーボンブラック）が凝集体に
形成されて液体（水）中に存在するもの、即ち、物質と
液体との混合物が原料であり、乳化の場合はｍ種類の流
体（油と水）が互いに分離しているが、混合物とされた
ものがこの場合の原料であり、これら原料をその目的に
応じて受入れるところである。２はポンプで、処理目的
に応じ、数１０〜数１００ｋｇｆ／ｃｍ2の範囲の圧力
で原料を吸いこみ、吐出するコンタミレス形のものであ
る。３は、入口４及び出口５を有し、内部に多数の球状
物６を充填した密閉の円筒形容器であり、前側が穴あき
の抑え部材７により、後側が穴あきの抑え部材８によ
り、内部に球状物６が不動状態即ち動かないように、で
きれば充填率９５％以上で詰めこまれているものであ
る。球状物６は、市販の同一径のボール又はビーズを使
用でき、硬質で耐摩耗性のあるステンレス鋼球であるこ
とが望ましいが、これに限定されるものではない。FIG. 1 is a conceptual view of an apparatus showing an embodiment of the present invention, showing a principal part in a longitudinal section, and FIG.
1 is a cross-sectional view taken along line I-II. First, in order to explain the configuration, in FIGS. 1 and 2, reference numeral 1 is a receiving portion for receiving a raw material, that is, a mixture of a substance and a liquid. That is, in the case of dispersion, n substances (eg, carbon black) are formed into aggregates and exist in the liquid (water), that is, the mixture of the substance and the liquid is the raw material, and in the case of emulsification The m kinds of fluids (oil and water) are separated from each other, but the mixture is the raw material in this case, and these raw materials are accepted according to the purpose. Reference numeral 2 denotes a pump, which is a contamination-less type which sucks and discharges the raw material at a pressure in the range of several tens to several hundreds kgf / cm 2 depending on the purpose of treatment. Reference numeral 3 denotes a closed cylindrical container having an inlet 4 and an outlet 5 and filled with a large number of spherical objects 6 therein. The front side is provided with a perforation suppressing member 7 and the rear side is provided with a perforation suppressing member 8 inside. If possible, the spherical objects 6 are packed at a filling rate of 95% or more so that they do not move. As the spherical substance 6, commercially available balls or beads having the same diameter can be used, and it is preferable that the spherical substance 6 is a hard and wear-resistant stainless steel ball, but is not limited thereto.
【００１１】次に前記実施例の作用を図３をも用いて説
明する。原料を受入れ部１に入れ、ポンプ２を作動する
と、原料は受入れ部１から吸入され、容器３の入口４に
圧送される。入口４内の抑え部材７の穴を通った原料
は、容器３内に入り、隣接した球状物６同士の隙間（球
面と球面の間）を通り図３の矢印のように流れていく。
隙間は沢山の連続した流路を形成しており、断面の縮
小、拡大及び流れの合流、分岐を繰返すことにより、乱
流と流体音響効果を生じ、物質が微粒化されることにな
る。そして、出口５から所定の微粒化した状態での物質
と液体とが取出されるものである。即ち、分散の場合
は、液体（水）中に物質（カーボンブラック）が非凝集
体状に散らばったものとして、又、乳化の場合は、液体
同士（油と水）が均一に懸濁したものとして取出される
ものである。Next, the operation of the above embodiment will be described with reference to FIG. When the raw material is put into the receiving portion 1 and the pump 2 is operated, the raw material is sucked from the receiving portion 1 and sent under pressure to the inlet 4 of the container 3. The raw material having passed through the hole of the restraining member 7 in the inlet 4 enters the container 3 and flows through the gap (between spherical surfaces) between the adjacent spherical objects 6 as shown by the arrow in FIG.
The gap forms a large number of continuous flow paths, and by reducing and enlarging the cross section and repeating flow merging and branching, turbulence and hydroacoustic effects are produced, and the substance is atomized. Then, the substance and the liquid in a predetermined atomized state are taken out from the outlet 5. That is, in the case of dispersion, the substance (carbon black) is dispersed in a non-aggregate form in the liquid (water), and in the case of emulsification, the liquids (oil and water) are uniformly suspended. Is taken out as.
【００１２】尚、物質の破砕についても同様にして取出
しうるものである。The crushing of substances can be taken out in the same manner.
【００１３】前記実施例によれば、ボール及びビーズ
は、様々な材質、材料で作られたものが市販されており
部品として幅広く選択できるので、各種の規格に応じた
プロセッサ（処理装置）を作成することができ、又、装
置そのもののコスト及び消耗品としてのランニングコス
トを安くできる。According to the above-described embodiment, the balls and beads made of various materials and materials are commercially available and can be widely selected as parts, so that a processor (processing device) according to various standards can be prepared. In addition, the cost of the device itself and the running cost as a consumable item can be reduced.
【００１４】又、前記実施例によれば、ボールやビーズ
はスタティック媒体として作用するので、コンタミネー
ションが極小となるものである。Further, according to the above-mentioned embodiment, since the balls and beads act as a static medium, the contamination is minimized.
【００１５】図４はこの発明の第２実施例を示す。この
実施例は球状物６Ａが直径の大きさの種々異なるもので
あり、これら異直径の球状物６Ａを任意、無雑作に容器
３内に充填したもので、他は前実施例と同様である。こ
の実施例は、前実施例と同様の作用をするほか、流路断
面積の変化が大きくかつ複雑となるので、物質の微粒化
の効果がそれだけ大きくなるものである。FIG. 4 shows a second embodiment of the present invention. In this embodiment, the spheres 6A have different diameters, and the spheres 6A having different diameters are arbitrarily and randomly packed in the container 3, and the others are the same as the previous embodiment. . This embodiment has the same effect as the previous embodiment, and since the change in the flow passage cross-sectional area is large and complicated, the effect of atomizing the substance is increased accordingly.
【００１６】図５はこの発明の第３実施例を示す。この
実施例は、球状物６Ｂが上流から下流に向けて容器３内
に直径の大きいものから徐々に小さいものへと順序良く
固定するように充填したものである。FIG. 5 shows a third embodiment of the present invention. In this embodiment, the spherical objects 6B are filled so as to be fixed in order from the one having a larger diameter to the one having a smaller diameter in order from the upstream side to the downstream side.
【００１７】図６はこの発明の第４実施例を示す。この
ものは、前実施例の球状体を大きさの順にパッケージ
（網状袋詰）したものを大きさの順に、６Ｃ，６Ｃ' ，
６Ｃ''，６Ｃ''' 及び６Ｃ''''の５個を容器３内に充填
したものである。FIG. 6 shows a fourth embodiment of the present invention. This is obtained by packaging the spherical bodies of the previous embodiment in the order of size (mesh bagging) in the order of size, 6C, 6C ′,
The container 3 is filled with 5 pieces of 6C ″, 6C ″ ″, and 6C ″ ″.
【００１８】図５及び図６の実施例のものは、この球状
体群を加入又は削除することにより、一連の微粒化の処
理工程を段階的に行うことができるという作用をする。The embodiment shown in FIGS. 5 and 6 has the function of adding or deleting this spherical body group so that a series of processing steps for atomization can be carried out stepwise.
【００１９】図７はこの発明の第５実施例を示す。この
実施例は、容器３を横長で若干斜めになるように作り、
ここに、球状物６を充填した穴あき板ケース６Ｄを収容
したものである。この実施例によれば、入口及び出口の
断面積を大きくでき、そこでの流路抵抗を小さくできる
という作用をする。FIG. 7 shows a fifth embodiment of the present invention. In this embodiment, the container 3 is made horizontally long and slightly inclined,
Here, the perforated plate case 6D filled with the spherical objects 6 is housed. According to this embodiment, the sectional area of the inlet and the outlet can be increased, and the flow path resistance there can be reduced.
【００２０】なお、この発明は、次に示す態様で実施す
ることができる。 (1) ２個以上無限大数に至る範囲内の複数の同直径の球
状物を密着させ、それら球状物同士の間に形成される隙
間を流路として分散及び乳化を行なう装置。 (2) ２個以上無限大数に至る範囲内の複数の夫々異なっ
た直径の球状物を密着させ、それら球状物同士の間に形
成される異なった隙間を流路として分散及び乳化を行な
う装置。 (3) ２個以上無限大数に至る範囲内の複数の同直径の球
状物を密着させて一群に構成したものを１つの集合体と
し、その球状物の異なった集合体同士を密着させ、１工
程の中で集合体ごとに段階的に分散及び乳化を行なう装
置。 (4) ２個以上無限大数に至る範囲内の複数の球状物を密
着させ、これらによって形成される多数の隙間を流路と
し、ここに原料を流すことによって物質の分散及び乳化
を行なう方法。 (5) ２個以上無限大数に至る範囲内の複数の同直径の球
状物を密着させて一群に構成したものを１つの集合体と
し、その球状物の異なった集合体同士を密着させること
により、１工程の中で段階的に分散及び乳化を行なう方
法。 (6) 数十から数百ｋｇｆ／ｃｍ2 範囲での分散及び乳化
を行なう装置としての用途。 (7) 直線流路内でのスタティックミキサに代わる混合エ
レメントとしての用途。 (8) ボール又はビーズの硬質化（耐摩耗の付与）による
粉砕（破砕）としての用途。The present invention can be implemented in the following modes. (1) A device for adhering a plurality of spherical objects having the same diameter within a range of two or more to an infinite number, and dispersing and emulsifying them by using a gap formed between the spherical objects as a flow path. (2) A device for adhering a plurality of spherical objects having different diameters within a range of two or more to an infinite number, and dispersing and emulsifying by using different gaps formed between the spherical objects as channels. . (3) A plurality of spherical objects having the same diameter within the range of at least an infinite number are brought into close contact with each other to form a group, and different spherical objects are brought into close contact with each other, A device that gradually disperses and emulsifies each aggregate in one process. (4) A method of dispersing and emulsifying a substance by bringing a plurality of spherical objects within a range of two or more into an infinite number into close contact with each other and using a large number of gaps formed by these as flow channels . (5) A group of two or more spherical objects of the same diameter within the range of infinity that are in contact with each other is made into one group, and different spherical objects are in close contact with each other. According to the method, stepwise dispersion and emulsification are carried out in one step. (6) Use as a device for dispersing and emulsifying in the range of several tens to several hundreds kgf / cm 2 . (7) Use as a mixing element to replace a static mixer in a straight flow path. (8) Use as crushing (crushing) by hardening the balls or beads (providing abrasion resistance).
【００２１】[0021]
【発明の効果】この発明によれば、低コスト、高生産性
で、かつ、コンタミレスで物質を微粒化できる方法及び
装置を提供する事ができるという効果を奏する。According to the present invention, there is an effect that it is possible to provide a method and an apparatus capable of atomizing a substance with low cost and high productivity and without contamination.
【図１】この発明の一実施例を示す装置概念図で要部を
縦断面で示した図である。1 is a conceptual view of a device showing an embodiment of the present invention, showing a longitudinal section of a main part thereof.
【図２】図１のＩＩ−ＩＩ断面を示す図である。FIG. 2 is a view showing a II-II cross section of FIG.
【図３】この発明の球状物回りの流れの原理作用を示す
図である。FIG. 3 is a diagram showing a principle operation of a flow around a spherical object of the present invention.
【図４】この発明の第２実施例を示す要部縦断面図であ
る。FIG. 4 is a longitudinal sectional view of an essential part showing a second embodiment of the present invention.
【図５】この発明の第３実施例を示す要部縦断面図であ
る。FIG. 5 is a longitudinal sectional view of a main part showing a third embodiment of the present invention.
【図６】この発明の第４実施例を示す要部縦断面図であ
る。FIG. 6 is a longitudinal sectional view of a main part showing a fourth embodiment of the present invention.
【図７】この発明の第５実施例を示す要部縦断面図であ
る。FIG. 7 is a longitudinal sectional view of an essential part showing a fifth embodiment of the present invention.
１ 受入れ部 ２ ポンプ ３ 容器 ４ 入口 ５ 出口 ６ 球状物 ７ 穴あき抑え部材（前側） ８ 穴あき抑え部材（後側） 1 Receiving section 2 Pump 3 Container 4 Inlet 5 Outlet 6 Spherical object 7 Perforation suppression member (front side) 8 Perforation suppression member (rear side)
Claims (4)
物を充填し、物質と液体との混合物を前記入口に供給
し、容器内の隣接球状物間の隙間を流し、出口から物質
を微粒化した状態で液体と共に取出すことを特徴とする
物質の微粒化方法。1. A container having an inlet and an outlet is filled with a plurality of spherical objects, a mixture of a substance and a liquid is supplied to the inlet, a gap between adjacent spherical objects in the container is caused to flow, and a substance is discharged from the outlet. A method for atomizing a substance, characterized in that it is taken out together with a liquid in the atomized state.
部と、この受入れ部の混合物を吸引し加圧するポンプ
と、このポンプにより加圧された混合物を導入する入口
及び混合物を吐出する出口を有し内部に複数の球状物を
充填した容器とを備えた物質の微粒化装置。2. A receiving part for receiving a mixture of a substance and a liquid, a pump for sucking and pressurizing the mixture in the receiving part, an inlet for introducing the mixture pressurized by the pump, and an outlet for discharging the mixture. A device for atomizing a substance, comprising a container having a plurality of spherical objects filled therein.
個までの範囲にあって、同一径又は異なる径に形成され
たものであることを特徴とする請求項１及び２記載の物
質の微粒化方法及び装置。3. The substance according to claim 1 or 2, wherein the spherical particles are formed in the range of two or more to a large number of particles close to infinity and have the same diameter or different diameters. Atomization method and device.
て球状物の径が大きい集合体から径の小さい集合体へと
順に接続されて構成されていることを特徴とする請求項
１及び２記載の物質の微粒化方法及び装置。4. A container for filling spherical objects is configured such that it is connected in order from an upstream to a downstream of an assembly having a large diameter of spherical objects to an assembly having a small diameter. 2. A method and apparatus for atomizing a substance according to 2.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6202246A JPH0857278A (en) | 1994-08-26 | 1994-08-26 | Method for finely pulverizing substance and apparatus therefor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6202246A JPH0857278A (en) | 1994-08-26 | 1994-08-26 | Method for finely pulverizing substance and apparatus therefor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0857278A true JPH0857278A (en) | 1996-03-05 |
Family
ID=16454377
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP6202246A Pending JPH0857278A (en) | 1994-08-26 | 1994-08-26 | Method for finely pulverizing substance and apparatus therefor |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0857278A (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2000116987A (en) * | 1998-10-15 | 2000-04-25 | Sanyo Electric Co Ltd | Detergent dissolving apparatus and washing machine with the same and static dissolver |
| WO2002026368A3 (en) * | 2000-09-26 | 2002-08-08 | Mercatel Groep Bv | Static mixer apparatus and method for manufacturing same |
| EP2002882A1 (en) * | 2007-06-15 | 2008-12-17 | Wageningen University | Process for manufacturing an emulsion |
| JP2009095761A (en) * | 2007-10-17 | 2009-05-07 | Earth Technica:Kk | Vibration mill and operation method of the same |
| CN108686526A (en) * | 2018-07-05 | 2018-10-23 | 马鞍山市思迪包装材料科技有限公司 | A kind of flow-type combination board processing solid-liquid mixing device |
| WO2019001863A1 (en) * | 2017-06-29 | 2019-01-03 | Washtec Holding Gmbh | Foam generator for a vehicle-treatment device |
| JP2019013874A (en) * | 2017-07-05 | 2019-01-31 | 株式会社アクト | Sludge volume reduction method, sludge volume reduction device and waste water purification system |
| CN110194903A (en) * | 2019-04-30 | 2019-09-03 | 清远市绚淳环保新材料有限公司 | Chemical reaction kettle and the processing method for using the chemical reaction kettle |
-
1994
- 1994-08-26 JP JP6202246A patent/JPH0857278A/en active Pending
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2000116987A (en) * | 1998-10-15 | 2000-04-25 | Sanyo Electric Co Ltd | Detergent dissolving apparatus and washing machine with the same and static dissolver |
| WO2002026368A3 (en) * | 2000-09-26 | 2002-08-08 | Mercatel Groep Bv | Static mixer apparatus and method for manufacturing same |
| EP2002882A1 (en) * | 2007-06-15 | 2008-12-17 | Wageningen University | Process for manufacturing an emulsion |
| JP2009095761A (en) * | 2007-10-17 | 2009-05-07 | Earth Technica:Kk | Vibration mill and operation method of the same |
| WO2019001863A1 (en) * | 2017-06-29 | 2019-01-03 | Washtec Holding Gmbh | Foam generator for a vehicle-treatment device |
| CN110769924A (en) * | 2017-06-29 | 2020-02-07 | 瓦什特克控股公司 | Foam generating device for vehicle treatment device |
| JP2019013874A (en) * | 2017-07-05 | 2019-01-31 | 株式会社アクト | Sludge volume reduction method, sludge volume reduction device and waste water purification system |
| CN108686526A (en) * | 2018-07-05 | 2018-10-23 | 马鞍山市思迪包装材料科技有限公司 | A kind of flow-type combination board processing solid-liquid mixing device |
| CN110194903A (en) * | 2019-04-30 | 2019-09-03 | 清远市绚淳环保新材料有限公司 | Chemical reaction kettle and the processing method for using the chemical reaction kettle |
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