JPS58501710A - foam generator - Google Patents

foam generator

Info

Publication number
JPS58501710A
JPS58501710A JP57503429A JP50342982A JPS58501710A JP S58501710 A JPS58501710 A JP S58501710A JP 57503429 A JP57503429 A JP 57503429A JP 50342982 A JP50342982 A JP 50342982A JP S58501710 A JPS58501710 A JP S58501710A
Authority
JP
Japan
Prior art keywords
casing
foam
liquid
air
foam generator
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
Application number
JP57503429A
Other languages
Japanese (ja)
Inventor
パシフイシイ・ジオゼフ・アルバ−ト
Original Assignee
ウエスト ポイント−ペツパ レル,インコ−ポレイテツド
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 ウエスト ポイント−ペツパ レル,インコ−ポレイテツド filed Critical ウエスト ポイント−ペツパ レル,インコ−ポレイテツド
Publication of JPS58501710A publication Critical patent/JPS58501710A/en
Pending legal-status Critical Current

Links

Classifications

    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06BTREATING TEXTILE MATERIALS USING LIQUIDS, GASES OR VAPOURS
    • D06B19/00Treatment of textile materials by liquids, gases or vapours, not provided for in groups D06B1/00 - D06B17/00
    • D06B19/0088Treatment of textile materials by liquids, gases or vapours, not provided for in groups D06B1/00 - D06B17/00 using a short bath ratio liquor
    • D06B19/0094Treatment of textile materials by liquids, gases or vapours, not provided for in groups D06B1/00 - D06B17/00 using a short bath ratio liquor as a foam
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20Mixing gases with liquids
    • B01F23/23Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/235Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids for making foam
    • 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
    • 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
    • B01F25/45Mixers in which the materials to be mixed are pressed together through orifices or interstitial spaces, e.g. between beads
    • B01F25/452Mixers 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
    • B01F25/4524Mixers 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
    • B01F25/45241Mixers 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F33/00Other mixers; Mixing plants; Combinations of mixers
    • B01F33/80Mixing plants; Combinations of mixers
    • B01F33/834Mixing in several steps, e.g. successive steps

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Dispersion Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Nozzles (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるため要約のデータは記録されません。 (57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 泡 発 生 装 置 背景技術 織物工業において水処理工程は、主なエネルだ消費源であると認識されている。[Detailed description of the invention] Foam generation equipment Background technology Water treatment processes in the textile industry are recognized as a major source of energy consumption.

エネルギコストの上昇の出現及び石油、天然ガスの有効利用の関心の高まシにつ れて、例えば、漂白、染色、プリント、仕上げの水処理工程技術についてエネル ギの使用を削減することに多大の考慮が払われている。With the emergence of rising energy costs and growing interest in the effective use of oil and natural gas, For example, water treatment technology for bleaching, dyeing, printing, and finishing can be Considerable consideration has been given to reducing the use of

織物分野においてエネルギ保存研究の結果として発達した技術の1つには、水処 理工程のための泡の利用がある。泡の技術によって織物分野への液体供給総量は 、実質上削減され、それによって、製品の乾燥に必要なエネルギ総量を少なくし ている。エネルギの節減のみならず、泡は、また、生産性向上及び種々の他の利 点をもたらしている。One of the technologies developed as a result of energy conservation research in the textile field is water treatment. There are uses of foam for physical processes. The total amount of liquid supply to the textile field by foam technology is , thereby reducing the total amount of energy required to dry the product. ing. In addition to energy savings, foam also provides increased productivity and various other benefits. It brings points.

泡の技術による最も重要な考察は、例えば、密度、粘度、安定性及び気泡サイズ の一様特性を有する泡を生成することである。泡の物性の多様性が観察者にとっ て容易に判別できる容蘭できない結果を生じるので、そのような一様性は、泡で 染色する際には特に重要である。The most important considerations according to foam technology are e.g. density, viscosity, stability and bubble size. The aim is to produce foam with uniform properties. The diversity of physical properties of bubbles is of great interest to observers. Such uniformity is important for foams, as it would produce results that are not easily discernible. This is especially important when dyeing.

泡発生装置の1つのタイプには、いわゆる「静的泡発生器(static fo amer ) Jと称せられるものがある。このような装置は、空気と液体7石 けん溶液とが互いに、ビード、スクリーンとその信置種類のものの多孔媒体を通 されるとき、小さな気泡分散(すなわち、泡)が発生きれるという原理に基づい て稼動される。One type of foam generator includes the so-called "static foam generator". There is something called J. Such a device uses air and liquid The sapon solution is passed through a porous medium such as beads, screens and the like. Based on the principle that small bubble dispersion (i.e., bubbles) can be generated when It will be operated.

静的泡発生器は、公知である。例えば、1937年8月24日付でウォルター・ ゴスマン(WaltherGosmann )に許可された米国特許第2.09 0.727号に、液体と気体とが多数のガラスのような無腐蝕性物質のボールを 含むチャンバーへ加圧下に送られ、十分混合した液体と気体との混合物を気体の 小さな気泡から成る泡に生成する装置が開示されている。Static foam generators are known. For example, on August 24, 1937, Walter U.S. Patent No. 2.09 granted to Walther Gosmann In No. 0.727, a liquid and a gas pass through a large number of balls of non-corrosive material such as glass. The well-mixed liquid and gas mixture is sent under pressure to the chamber containing the gas. An apparatus is disclosed for producing foam consisting of small air bubbles.

さらに、液体−気体混合物が球状ビードを通過窟れて泡となる特許として開示さ れた装置の例としては、1977年7月26日付でハンス・ウィルセン(Han IIWi1m@en )に許可された米国特許第4,038.037号及び、1 977年11月6日付でハンス・ウルリッヒフォンデルエルツ(Hang−Ul rich von der Eltz )に発行された米国特許第4,061, 001号その他がある。Additionally, a patent has been disclosed in which a liquid-gas mixture passes through a spherical bead and forms bubbles. An example of such a device is the one published by Hans Wilsen on July 26, 1977. IIWi1m@en) and U.S. Pat. On November 6, 977, Hans Ulrich von der Eltz (Hang-Ul) U.S. Patent No. 4,061, issued to Rich von der Eltz There are No. 001 and others.

液体と気体との混合物がスクリーンのようなものを通過する静的泡発生器の公知 の一例として1980年6月10日付でハワードダプルコール、ジ、ニア(Ho ward W、Co1e+Jr )に許可された米国特許第4、207.202 号がある。この特許においては、広げられた金属片が供給さtた液体及び気体を 混合して泡を生じ芒せる多孔性物質として作用している。Known static foam generators in which a mixture of liquid and gas passes through something like a screen As an example, on June 10, 1980, Howard Dapulcole, J.N. U.S. Patent No. 4, 207.202, issued to Ward W. Col. There is a number. In this patent, an expanded piece of metal collects a supplied liquid and gas. It acts as a porous material that mixes and forms bubbles.

多孔性物質の床を採用する静的泡発生器の概念は公知であるが、この発明では、 一様性の水準を改良するような液体と空気との混合を与えている。この改良の認 識は、静的泡発生器を用いて泡を発生させる際に包含1−タ問題を考察すること によって得ることができる。While the concept of static foam generators employing a bed of porous material is known, this invention It provides a mixture of liquid and air that improves the level of uniformity. Acknowledgment of this improvement The knowledge is to consider the inclusion factor problem when generating foam using a static foam generator. can be obtained by

基本的には気泡を発生する、気体と液体(水)との結合は不均一な系である。液 体への界面活性剤の添加は、気泡として液体相中に気体相を安定させるのみに作 用し、気体/液体の比が泡の分散中一定でおるという確信は全くない。それゆえ に、泡の一様性は、気体/液体の混合物が泡発生器を通過する際に適切な流れ動 力(flow dynamitlA)特性を要求することとなる。Basically, the combination of gas and liquid (water), which generates bubbles, is a heterogeneous system. liquid The addition of surfactants to the body only serves to stabilize the gas phase in the liquid phase as air bubbles. There is no certainty that the gas/liquid ratio will remain constant during foam dispersion. therefore Foam uniformity depends on the proper flow motion of the gas/liquid mixture as it passes through the foam generator. This requires flow dynamics characteristics.

この発明は、十分に一様な泡が生成されるように空気及び液体の流れを制御する 装置にこれらが導びかれる構造装置を構成している。This invention controls the flow of air and liquid so that a sufficiently uniform foam is produced. They form a structural device that leads to the device.

発明の概要 この改良された泡発生技術の実施において、空気及び液体が前処理混合され、そ の混合物が静的泡発生器を介して送られて泡を発生する。プリミキサと泡発生器 とは同様な構造でおる。よ#)特に、各々は当該ケーシング内に配置された多数 の回旋状要素をおおう円筒体ケーシングからなる。泡発生器においては、ケーシ ングが、さらに、回旋状要素とケーシングとの間の空間を満たす球形状ビードの 多孔質床を含むという点で泡発生器はシリミキサと異なる。Summary of the invention In implementing this improved foam generation technique, air and liquid are pre-mixed and The mixture is sent through a static foam generator to generate foam. Premixer and foam generator It has a similar structure. In particular, each has a large number placed within the casing. It consists of a cylindrical casing enclosing a convoluted element. In the foam generator, the casing The ring further includes a spherical bead filling the space between the convoluted element and the casing. Foam generators differ from silimixers in that they include a porous bed.

今述べた装置において、グリミキサが連続的に、予期できるように空気と液体と を混合する。静的発生器へのこの混合物の導入においては、回旋状要素と球形状 ビードとの結合した効果には、発達する泡の流れを分割し、また、放射状に混合 して泡の直径にわたる空気−液体の濃度勾配を防ぐようになる。この結果、たと え、泡が高度な液体への空気比(しばしば「ブロー比」と呼ばれる。)を有して いても、すぐれた一様性の泡となる。In the device just described, the grimixer continuously and predictably mixes air and liquid. Mix. In the introduction of this mixture into a static generator, convoluted elements and spherical shapes The combined effect of the bead is to break up the developing foam stream and also to mix it radially. This prevents air-liquid concentration gradients across the diameter of the bubble. As a result, The foam has a high liquid-to-air ratio (often called the "blow ratio"). It produces a foam of excellent uniformity even when mixed.

発明の詳細な説明 添付図面を参照してこの発明の詳細な説明する。Detailed description of the invention The present invention will be described in detail with reference to the accompanying drawings.

ここで、 第1図は、この発明に係る泡発生装置の基本構成を図示する概略図であり、 第2図は、第1図に示されたこの装置の!リミキサ部を斜視する一部断面図でア シ、及び第3図は、第1図で示されたこの装置の静的泡発生器の断面図である。here, FIG. 1 is a schematic diagram illustrating the basic configuration of a foam generating device according to the present invention, FIG. 2 shows the structure of this device shown in FIG. A partial cross-sectional view of the remixer section. 1 and 3 are cross-sectional views of the static foam generator of the apparatus shown in FIG.

添付第1図を参照すれば、加圧下の液体源は、液体(水の混合物と界面活性剤) を!リミキサ12へ送るポンプ10として示されている。加圧エアは前記プリミ キサの上流直前の液体流路に対向する側面に適宜な連絡部によって供給される。Referring to attached Figure 1, the source of liquid under pressure is a liquid (mixture of water and surfactant). of! It is shown as a pump 10 feeding a remixer 12. The pressurized air is The liquid is supplied to the side facing the liquid flow path just before the upstream side of the gasket by a suitable communication part.

空気/液体の!リミキサJ2を通じて流れ、それから、直結した好適なカップラ を介して静的泡発生器14に当流される。泡発生器14内で、この混成物は更に 混合されて適宜な泡塗布器(図示しない)に供給する為に泡の放出を生じる。Air/Liquid! flows through remixer J2 and then directly connected to a suitable coupler. is supplied to the static foam generator 14 via the static foam generator 14. In the foam generator 14, this mixture is further Mixing results in the release of foam for feeding into a suitable foam applicator (not shown).

プリミキサ12の詳細は第2図を参照して理解することができる。プリミキサ1 2は、オハイオ州ディトンのケミニール社の一部門であるケエックス社(the  Kenics Corporation + a division ofC hemineer + Inc、of Dayton + 0hio )により 販売されるケエックスKMOD −60として公知の商業上有用な装置である。Details of premixer 12 can be understood with reference to FIG. Premixer 1 2 is a division of Cheminil Corporation of Diton, Ohio. Kenics Corporation + a division of C by hemineer + Inc, of Dayton + 0hio) It is a commercially useful device known as the KEX KMOD-60.

ゾIJ ミキサ12は、適宜にその両端に山ねじをつけられた円筒状ケーシング 16から成り、その連結部で液体/空気の供給をさせている。ケーシング16内 に回旋状要素18の多数が設けられている。各回旋状要素18は、180度のね じりが添えられた金属の矩形物から成る。回旋状要素18は、ケーシング16の 長手方向の軸に沿って−TjL線上に延長して端と端とをつらねて配置されてい る。回旋状要素18の近接した端は、第2図から理解できるように、互いに90 度の異なる方向に向けられている。The IJ mixer 12 is a cylindrical casing with threaded screws on both ends. 16, and the liquid/air supply is made at the connection part. Inside the casing 16 A large number of convoluted elements 18 are provided. Each convoluted element 18 has a 180 degree angle. It consists of a rectangular piece of metal with a rib attached to it. The convoluted element 18 is formed of the casing 16. It extends along the -TjL line along the longitudinal axis and is arranged end to end. Ru. The adjacent ends of the convoluted element 18 are 90 degrees apart from each other, as can be seen from FIG. oriented in different directions.

前述のこの種のプリミキサは、連続所定流で空気と液体とを混合する。回旋状要 素18は、一様な定常特衣昭58−501710(,3) 流(uniform flow )f生じさぞ、この定常流(uniformf low)は、供給成分から波動または振動を妨げている。Premixers of this type described above mix air and liquid in a continuous, predetermined flow. Convoluted corner Element 18 is a uniform stationary special costume Sho 58-501710 (,3) This steady flow (uniform flow) low) prevents waves or vibrations from the feed components.

この供給成分は、シリミキサの他のタイプでは、特にプIJ ミキサからの混合 流の方向に沿って生じるのに応じて空気/液体の混合の一様性に変化を生じさせ る。This feed component is mixed in other types of silimixers, especially from IJ mixers. causing a change in the uniformity of air/liquid mixing as it occurs along the direction of flow. Ru.

現在のプリミキサ12の付加する特徴としては、グリミキサがプリミキサの他の 種に形成さるノズル効果、すなわち、そらせ板その信置様なものを有さない自由 流れ(free flow )系である。従って空気/液体の流れは、最小の背 圧で太き 範囲にわたって生じる。An additional feature of the current premixer 12 is that the grimixer is a premixer other than the premixer. The nozzle effect formed on the seed, that is, the freedom of not having anything like a deflector It is a free flow system. Air/liquid flow is therefore minimized It occurs over a wide range due to pressure.

静的泡発生器14は、檎造においてはプリミキサー12と同じである。泡発生器 14のケーシング20は、ケーシング16よシ大きな直径である。付は加えるな らば、ケーシング20は、ケーシング20に対向する両端にアダプタ26と28 とが設けられたフランジ24と好適状態で協働するフランジ22を両端に設けて いる。しかしながら、プリミキサ12と泡発生器14との間の最も重要な相違は 、泡発生器14が、回旋状要素32とケーシング20との間の空間を占める球状 ビード30から成る多孔質床をさらに内含することである。好ましくは、これら のビード30は、約1、4 vmの直径である。泡発生器14内にビード30を 保持するために、スクリーン34がケーシング20に対向する両端でフランジ2 2と23との間に設けられている。The static foam generator 14 is the same as the premixer 12 in brewing. foam generator The fourteen casings 20 have a larger diameter than the casing 16. Don't add an attachment casing 20 has adapters 26 and 28 on opposite ends of casing 20. A flange 22 is provided at both ends which preferably cooperates with a flange 24 provided with. There is. However, the most important difference between premixer 12 and foam generator 14 is , the foam generator 14 is spherical and occupies the space between the convoluted element 32 and the casing 20. It further includes a porous bed of beads 30. Preferably these The bead 30 has a diameter of approximately 1.4 vm. Beads 30 are placed inside the foam generator 14. The screen 34 has flanges 2 at opposite ends of the casing 20 in order to retain it. 2 and 23.

ビードJOば、泡発生器14の縦鵬に沿った方向で泡発生器14に供給された空 気/液体の混合から泡を発生する多孔を備えている。回旋状混合要素32は、要 素30の水力中央部周辺で泡を発達させる回転循環を生じ、このようにして放射 状混合を起こす。この混合タイプは、本質的にはケーシング2oの中央部に接合 した物体とケーシング2oの内側壁に近接したその部分との間の空気/液体勾配 を妨げている。開示した泡発生器は、分流の数が2r″に等しく、ここでnは使 用される要素の数であるという公式に従って稼動されるから、これは16分流を 生じさせる。Bead JO refers to the air supplied to the foam generator 14 in the direction along the longitudinal length of the foam generator 14. It has pores that generate bubbles from the gas/liquid mixture. The convoluted mixing element 32 This creates a rotating circulation that develops bubbles around the hydraulic center of the element 30, thus emitting radiation. This causes a mixture of substances. This mixed type is essentially joined to the center of the casing 2o. air/liquid gradient between the object and its part close to the inner wall of the casing 2o is hindering. The disclosed foam generator has a number of divided flows equal to 2r'', where n is used This works according to the formula that the number of elements used is 16. bring about

上述したこの装置を利用すると、一様な所定の再現可能な密度、粘度、安定性及 び気泡サイズの特性が倭られる。Utilizing this device as described above, uniform, predetermined and reproducible density, viscosity, stability and Characteristics of bubble size and bubble size are suppressed.

補正書の翻訳文提出書(特許法第184条の7第1項)13和58年に月1今日 特許庁長官 若 杉 和 夫 殿 1国際出御番号 PCT/US82101472 2発明の名称 3特許出願人 住所 アメリカ合衆国 ジオーノア州 31833ウエストポイントウエスト・ テンプ・ストリート 400国籍 アメリカ合衆国 4代 理 人 住所 東京都港区虎ノ門1丁目26番5号 第17森ビル補正された請求の範囲 1、端と端とをつらねてケーシングの長手方向に延在して配置された多数の回旋 状要素を有する第1の円筒体ケーシングを包み、空気及び液体の混成物を生成す るシリミキサと、 固定され、異々る角度に向けて端と端とをつらねてケーシングの長手方向に延在 して配置されたさらに多数の回旋状要素がその内に配列された第2の円筒体ケー シング及び前記回旋状要素と前記ケーシングとの間の空間を専有する球体状ピー ドの床を含む静的泡発生器と、及び、 前記第2のケーシングの反対端から排出される、空気と液体との均一な分散を生 じさせる前記ビードを介する通路としての泡発生器に前記混成物を供給する前記 第2のケーシングの一端へシリミキサを結合する手段とから成シ、前記分散が泡 の密度、安定性、粘漫及び連続的に均一である気泡サイズ分布の測定可能η物性 特性によシ、特徴づけられる改良した泡発生装置2 前記の空気と液体とが前記 プリミキサ・ケーシングの長手方向に沿って延在する流れの方向で前記ノ″リミ キサ・ケーシングの一端へ供給される請求の範訂第1項に記載する泡発生装置。Submission of Translation of Written Amendment (Article 184-7, Paragraph 1 of the Patent Law) 13 Wa 1 Today, May 1, 2013 Mr. Kazuo Wakasugi, Commissioner of the Patent Office 1 International dispatch number PCT/US82101472 2. Name of the invention 3 Patent applicant Address: 31833 West Point West, Gionoa, United States Temp Street 400 Nationalities United States 4th generation manager Address: 17th Mori Building, 1-26-5 Toranomon, Minato-ku, Tokyo Amended scope of claims 1. A large number of convolutions arranged end to end and extending in the longitudinal direction of the casing. enclosing a first cylindrical casing having shaped elements to produce a mixture of air and liquid; A silimixer, fixed and extending along the length of the casing end-to-end at different angles a second cylindrical case having a further number of convoluted elements arranged therein; a spherical piece occupying a space between the convoluted element and the casing; a static foam generator including a bed of foam, and producing a uniform distribution of air and liquid discharged from the opposite end of said second casing; said admixture to a foam generator as a passage through said bead to means for coupling a silimixer to one end of a second casing, wherein said dispersion is foamed; Measurable physical properties of density, stability, viscosity and continuously uniform bubble size distribution Improved foam generator characterized by characteristics 2 The air and liquid are The said "limit" in the direction of flow extending along the longitudinal direction of the premixer casing. A foam generating device according to claim 1, which is supplied to one end of a kisser casing.

3、各回旋状要素が略180度のねじれを与えられた矩形体から成シ、その近接 した端と端が互いに異なる角度に向けられている請求の範囲第1項ないし第2項 のいずれかに記載の泡発生装置。3. Each convoluted element consists of a rectangular body twisted by approximately 180 degrees, and its proximity Claims 1 and 2, wherein the two ends are oriented at different angles to each other. The foam generator according to any one of the above.

4、前記矩形体の隣接端は、互に90度を成す方向に向けられている請求の範囲 第3項記載の泡発生装置。4. The claim that adjacent ends of the rectangular body are oriented at 90 degrees to each other. The foam generating device according to item 3.

国際調査報告international search report

Claims (1)

【特許請求の範囲】[Claims] 1. 端と端と會つらねてケーシングの長手方向に延在して配置でれた多数の回 旋状要素を有する第1の円筒体ケーシングを包み、空気及び液体の混成物を生成 するプリミキサと、 端と端とをつらねてケーシングの長手方向に延在して配置されたさらに多数の回 旋状要素がその内に配列された第2の円筒体ケーシング及び前記回旋状要素と前 記ケーシングとの間の空間上専有する球体状ビードの床を含む静的泡発生器と、 及び、 前記第2のケーシングの反対端から排出される、空気と液体との均一な分散を生 じさせる前記ビードを介する通路としての泡発生器に前記混成物を供給する前記 第2のケーシングの一端ヘプIJ ミキサを結合する手段とから成る改良した泡 発生装置。 2 前記空気及び液体が前記プリミキサ・ケーシングの長手方向に沿って延在す る流れの方向で前記プリミキサ・ケーシングの一端へ供給される請求の範囲第1 項に記載する泡発生装置。 3、各回旋状要素が略180度のねじれを与えられた矩形体から成り、その近接 した端と端が互いに異なる角度に向けられている請求の範囲第1項ないし第2項 のいずれかに記載の泡発生装置。 4 前記隣接端は、互に略90度を成す方向に向けられている請求の範囲第3項 記載の泡発生装置。1. A large number of turns are arranged end to end and extend in the longitudinal direction of the casing. Wrapping a first cylindrical casing with a spiral element to create a mixture of air and liquid A premixer to A further large number of turns are arranged end to end and extend in the longitudinal direction of the casing. a second cylindrical casing in which a convoluted element is arranged; a static foam generator comprising a bed of spherical beads occupying a space between the casing and the casing; as well as, producing a uniform distribution of air and liquid discharged from the opposite end of said second casing; said admixture to a foam generator as a passage through said bead to An improved foam consisting of a means for coupling the hep IJ mixer at one end of the second casing. Generator. 2 The air and liquid extend along the longitudinal direction of the premixer casing. Claim 1 The foam generating device described in Section. 3. Each convoluted element consists of a rectangular body twisted by approximately 180 degrees, and its adjacent Claims 1 and 2, wherein the two ends are oriented at different angles to each other. The foam generator according to any one of the above. 4. Claim 3, wherein the adjacent ends are oriented at approximately 90 degrees to each other. The foam generator described.
JP57503429A 1981-10-15 1982-10-14 foam generator Pending JPS58501710A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US31177281A 1981-10-15 1981-10-15
US311772FREGB 1981-10-15

Publications (1)

Publication Number Publication Date
JPS58501710A true JPS58501710A (en) 1983-10-13

Family

ID=23208395

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57503429A Pending JPS58501710A (en) 1981-10-15 1982-10-14 foam generator

Country Status (7)

Country Link
EP (1) EP0077652B1 (en)
JP (1) JPS58501710A (en)
BR (1) BR8207931A (en)
DE (1) DE3263150D1 (en)
DK (1) DK276283D0 (en)
IN (1) IN156672B (en)
WO (1) WO1983001395A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2016097306A (en) * 2014-11-18 2016-05-30 フランケ・カフェーマシーネン・アー・ゲーFranke Kaffeemaschinen Ag Device for generating milk foam and method therefor

Families Citing this family (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59230627A (en) * 1983-06-15 1984-12-25 Taisei Corp Mixing method of fluid
IE59155B1 (en) * 1986-08-26 1994-01-12 Pandion Haliaetus Limited Car wash apparatus
US4850705A (en) * 1987-11-18 1989-07-25 Horner Terry A Motionless mixers and baffles
US4840493A (en) * 1987-11-18 1989-06-20 Horner Terry A Motionless mixers and baffles
JPH0660068B2 (en) * 1988-06-10 1994-08-10 株式会社日静プラン Foaming device for foaming concrete
GB2247411A (en) * 1990-06-26 1992-03-04 Ics Texicon Ltd Producing foam
EP0602135B1 (en) * 1991-09-05 1998-10-21 Minnesota Mining And Manufacturing Company Continuous generation and application of foam to moving porous substrate
US5480589A (en) * 1994-09-27 1996-01-02 Nordson Corporation Method and apparatus for producing closed cell foam
GB9620152D0 (en) * 1996-09-27 1996-11-13 Platt Kevin G Improvements in or relating to the manufacture and use of aerated concrete
US7766537B2 (en) * 2005-02-18 2010-08-03 Henry Gembala Lightweight foamed concrete mixer
CN103260734B (en) * 2010-12-23 2016-03-09 赢创有限公司 Be used for preparing equipment and the method for emulsion
CN103501885B (en) * 2011-03-04 2017-06-23 卡尔·波德马耶尔斯基 Liquid foam manufacture method and equipment
DE202011110158U1 (en) * 2011-07-29 2012-12-20 Volker Barth Device for foaming a liquid
WO2015051146A1 (en) 2013-10-02 2015-04-09 Aerocore Technologies Llc Cleaning method for jet engine
US11643946B2 (en) 2013-10-02 2023-05-09 Aerocore Technologies Llc Cleaning method for jet engine
CN105854701A (en) * 2016-05-18 2016-08-17 黑龙江沃德能源工程技术有限公司 Downhole variable-section rotating foam generating device and downhole foam generating method

Family Cites Families (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2090727A (en) * 1934-12-08 1937-08-24 Concordia Elektrizitaets Ag Foam producing device
US3388868A (en) * 1965-10-29 1968-06-18 Nalco Chemical Co Foam producing nozzle
US3643927A (en) * 1970-10-15 1972-02-22 Phillips Petroleum Co Stationary mixture and method for mixing material
US3683446A (en) * 1970-11-13 1972-08-15 Peter Hans Tell Nozzle for alternative blowing or suction
US3711067A (en) * 1971-01-08 1973-01-16 Midland Ross Corp Extruding and mixing equipment
US4068830A (en) * 1974-01-04 1978-01-17 E. I. Du Pont De Nemours And Company Mixing method and system
US4038037A (en) * 1974-09-10 1977-07-26 Wilmsen Hans Apparatus for the manufacture of homogeneous, fine-pored synthetic resin foams
ES448040A1 (en) * 1975-05-24 1977-07-01 Hoechst Ag Device for the application of foam on textile webs
US4133773A (en) * 1977-07-28 1979-01-09 The Dow Chemical Company Apparatus for making foamed cleaning solutions and method of operation
US4207202A (en) * 1978-06-05 1980-06-10 Cole Howard W Jr Apparatus for making small bubble foam

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2016097306A (en) * 2014-11-18 2016-05-30 フランケ・カフェーマシーネン・アー・ゲーFranke Kaffeemaschinen Ag Device for generating milk foam and method therefor

Also Published As

Publication number Publication date
BR8207931A (en) 1983-09-20
IN156672B (en) 1985-10-12
EP0077652A1 (en) 1983-04-27
EP0077652B1 (en) 1985-04-17
DK276283A (en) 1983-06-15
DK276283D0 (en) 1983-06-15
WO1983001395A1 (en) 1983-04-28
DE3263150D1 (en) 1985-05-23

Similar Documents

Publication Publication Date Title
JPS58501710A (en) foam generator
CA2529020C (en) Device and method for generating microbubbles in a liquid using hydrodynamic cavitation
US3526391A (en) Homogenizer
US20080274226A1 (en) Method and System for Generating Foam for the Manufacture of Gypsum Products
JPS58126127A (en) Method and apparatus for manufacturing thermoplastic foamed resin
US3119704A (en) Preparation of aerated cementitious products
CN106747576B (en) A kind of method that normal pressure homogenizing low cost prepares aeroge for building
CN103249476B (en) For the apparatus and method of gas diffusion
GB1290201A (en)
JPH05505141A (en) Media discharge head
US2791404A (en) Apparatus for making cellular products
CN207951317U (en) A kind of dynamic/static fluid mixer of ultrasonic wave forced vibration mixing
JP2006016495A (en) Method for supplying emulsified fuel and apparatus for the same
KR100348031B1 (en) In-line dynamic mixer with folding elements and perforated plates
US4846404A (en) Internal mix spray gun cartridge
US8596855B2 (en) Metering apparatus and method for introducing a powdery medium into a fluid
GB2076672A (en) Making foam
US3233872A (en) Acoustic processing method and means
JPH06190255A (en) Gas and liquid mixing device
US3438612A (en) Pressure differential type mixing device
GB1313103A (en) Process and apparatus for making urea/formaldehyde foams
JPS5665655A (en) Apparatus for generating water droplets containing gas bubbles
SU1183161A1 (en) Mixer of continuous action
JPH04247254A (en) Coating device for reaction-curing paint
JP2019037949A (en) Air bubble-containing liquid manufacturing device and air bubble-containing liquid manufacturing method