EP1827667B1 - Mixing and/or turbulent mixing device - Google Patents
Mixing and/or turbulent mixing device Download PDFInfo
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- EP1827667B1 EP1827667B1 EP05850183A EP05850183A EP1827667B1 EP 1827667 B1 EP1827667 B1 EP 1827667B1 EP 05850183 A EP05850183 A EP 05850183A EP 05850183 A EP05850183 A EP 05850183A EP 1827667 B1 EP1827667 B1 EP 1827667B1
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- flow plate
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- E—FIXED CONSTRUCTIONS
- E03—WATER SUPPLY; SEWERAGE
- E03C—DOMESTIC PLUMBING INSTALLATIONS FOR FRESH WATER OR WASTE WATER; SINKS
- E03C1/00—Domestic plumbing installations for fresh water or waste water; Sinks
- E03C1/02—Plumbing installations for fresh water
- E03C1/08—Jet regulators or jet guides, e.g. anti-splash devices
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- 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
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- 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
- B01F25/4521—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 orifices in elements, e.g. flat plates or cylinders, which obstruct the whole diameter of the tube
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
- B05B1/00—Nozzles, spray heads or other outlets, with or without auxiliary devices such as valves, heating means
- B05B1/34—Nozzles, spray heads or other outlets, with or without auxiliary devices such as valves, heating means designed to influence the nature of flow of the liquid or other fluent material, e.g. to produce swirl
- B05B1/3405—Nozzles, spray heads or other outlets, with or without auxiliary devices such as valves, heating means designed to influence the nature of flow of the liquid or other fluent material, e.g. to produce swirl to produce swirl
- B05B1/341—Nozzles, spray heads or other outlets, with or without auxiliary devices such as valves, heating means designed to influence the nature of flow of the liquid or other fluent material, e.g. to produce swirl to produce swirl before discharging the liquid or other fluent material, e.g. in a swirl chamber upstream the spray outlet
- B05B1/3415—Nozzles, spray heads or other outlets, with or without auxiliary devices such as valves, heating means designed to influence the nature of flow of the liquid or other fluent material, e.g. to produce swirl to produce swirl before discharging the liquid or other fluent material, e.g. in a swirl chamber upstream the spray outlet with swirl imparting inserts upstream of the swirl chamber
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F15—FLUID-PRESSURE ACTUATORS; HYDRAULICS OR PNEUMATICS IN GENERAL
- F15D—FLUID DYNAMICS, i.e. METHODS OR MEANS FOR INFLUENCING THE FLOW OF GASES OR LIQUIDS
- F15D1/00—Influencing flow of fluids
- F15D1/08—Influencing flow of fluids of jets leaving an orifice
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T29/00—Metal working
- Y10T29/49—Method of mechanical manufacture
- Y10T29/49826—Assembling or joining
Definitions
- In the invention is a mixed u / o. Verwirbelungsvorraum (5) for mixing u./o. Swirling liquids u./o. Liquid-solid mixtures u./o. Steaming and / or. Gases according to claim 1.
- the water would thereby become a so-called finely divided state and could possibly be more easily absorbed or utilized by biological organisms such as plants, animals and humans.
- some researchers assume that the water can accumulate in the natural turbulence in the wild in a balanced ratio with air and. Light components and new ones subtle energies through the arising torsional forces in the turbulence and the peculiarity of the dipolar water molecule structures, which react in a special way to water movements.
- These theories are controversial. However, it can be observed that nature in a comprehensive way, in large dimensions and in innumerable variations water u. Air turbulence and a wide range of turbulences of other liquid, vapor and gas mixtures is formed.
- Liquid-solid mixtures u./o. Vapors and / or. Gases emanate from a flow plate, they meet a mixed u./o. Verwirbelungsunter zero, another control element of the mixing u./o. Turbulence.
- Mixed u.lo. Turbulating assistants may be, for example, conical or hyperbolic funnels. If, for example, such funnels are used, liquids such as water form intensive vortices prepared by flow-through plates. A liquid such as water then leaves the funnel in spiraling or swirling form and outside the mixing u./o. Verwirbelungsvortechnisch a spirally flowing or swirling liquid bell.
- the size and vortex intensity (intense right-whirling or intensive left-whirling) of this resulting bell experience has a role for resulting quality improvements generated fluids. So that, for example, a large and intensely swirling water bell can occur at a normal domestic water connection with normal water outflow, the funnel must correspond as well as possible with respective flow plates.
- the mixed u./o. Verwirbelungsvorraum is also suitable for intensive and cost-effective mixing of different substances.
- the substances to be mixed are passed into the individual holes of the flow-through plates, again liquids and / or. Liquid-solid mixtures u./o. Vapors and / or. Gases. You can control the flow rates by choosing the hole sizes and the amount of substance introduced. The exit points from a fürströmplatte can also specify exactly. If you want to mix two substances together, for example, the substance A is passed into a flow hole A and the substance B in a flow hole B. One would then put the exit points of flow hole A and flow hole B close to each other, so that there is a local mixing u. /O. Swirling comes.
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Dispersion Chemistry (AREA)
- Water Supply & Treatment (AREA)
- Health & Medical Sciences (AREA)
- Physics & Mathematics (AREA)
- Fluid Mechanics (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Public Health (AREA)
- Hydrology & Water Resources (AREA)
- Life Sciences & Earth Sciences (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Accessories For Mixers (AREA)
- Physical Water Treatments (AREA)
- Artificial Filaments (AREA)
- Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
- Detergent Compositions (AREA)
- Food-Manufacturing Devices (AREA)
- General Preparation And Processing Of Foods (AREA)
Abstract
Description
Bei der Erfindung handelt es sich um eine Misch- u/o. Verwirbelungsvorrichtung (5) zum Mischen u./o. Verwirbeln von Flüssigkeiten u./o. Flüssigkeits-Feststoff-Gemischen u./o. Dämpfen u./o. Gasen gemäß Anspruch 1.In the invention is a mixed u / o. Verwirbelungsvorrichtung (5) for mixing u./o. Swirling liquids u./o. Liquid-solid mixtures u./o. Steaming and / or. Gases according to
In der Wasserforschung und Wasserfachliteratur setzen sich seit längerem, besonders aufgrund der Studien und Versuche des Wasser- u. Naturforschers Viktor Schauberger, Begriffe wie "lebendiges Wasser", "energiereiches Wasser", "belebtes Wasser" oder "vitales Wasser" immer mehr durch. Gemeint ist damit, dass gutes Wasser neben chemischen und biologischen Qualitäten vor allem auch physikalisch eine gute Qualität aufweisen sollte. Naturbeobachtungen zeigen, dass Wasser und Bewegung sehr häufig untrennbar zusammengehören. Wenn man Wasser in freier Natur beobachtet, bewegt es sich meistens auf die eine oder andere Weise. Selbst in stehenden Gewässern bilden sich ständig Wasserbewegungen aus zwischen verschiedenen Wasserschichten durch sich ändernde Temperaturen und Wasserdichten. Die Wasserverwirbelung ist eine besonders intensive Wasserbewegung. Wasserverwirbelungen und die dabei auftretenden Prozesse werden immer häufiger als eine effiziente Methode der Natur gesehen, die Selbstreinigungskräfte des Wassers anzuregen bzw. freizusetzen und das Wasser in seinem energetischen Zustand zu verbessern. Man redet in diesem Zusammenhang von einer Verbesserung der Energien, Schwingungen und Informationen im Wasser. Es wird angenommen, dass sich die innere Struktur des Wassers verändert, die sog. Clusterstruktur. Darunter versteht man Anhäufungen physikalisch aneinander haftender Wassermoleküle. Wassermoleküle besitzen diese besondere Eigenart, dass sie an einer Stelle leicht positiv und an einer anderen Stelle leicht negativ geladen sind. Hierdurch ziehen sich die Wassermoleküle gegenseitig an. Bei sog. weniger lebendigem Wasser geht man davon aus, dass sich größere Cluster oder "Molekülhaufen" gebildet haben. Bei intensiven Wasserbewegungen wie der Verwirbelung nehmen einige Forscher an, dass sich größere Cluster in immer kleinere Cluster zerteilen bzw. auflösen. Nach diesen Erklärungsansätzen bekäme das Wasser hierdurch einen sog. feinverteilteren Zustand und könnte möglicherweise von biologischen Organismen wie Pflanze, Tier und Mensch leichter aufgenommen bzw. verwertet werden. Weiterhin gehen einige Forscher davon aus, dass sich das Wasser in der natürlichen Verwirbelung in freier Natur in einem ausgewogenen Verhältnis anreichern kann mit Luft- u. Lichtkomponenten und neuen feinstofflichen Energien durch entstehende Torsionskräfte bei der Verwirbelung und die Eigenart der dipolaren Wassermolekülstrukturen, die in besonderer Weise auf Wasserbewegungen reagieren. Diese Theorien werden kontrovers diskutiert. Es lässt sich jedoch beobachten, dass die Natur in umfassender Weise, in großen Dimensionen und in unzähligen Variationen Wasser- u. Luftverwirbelungen sowie ein weites Spektrum von Verwirbelungen anderer Flüssigkeits-, Dampf- und Gasgemische ausbildet. Wie man auch immer einzelne Theorien beurteilen mag, es scheint gute Gründe dafür zu geben, dass die Natur sich so verhält. Es lassen sich durch naturnahe Verwirbelungen z.B. Geschmack und Aussehen von Wasser verbessern. Das Wasser kann auf natürliche Weise mit Sauerstoff angereichert werden. Es lässt sich beobachten, dass kühl verwirbeltes Wasser über längere Zeit kühl bleibt, selbst wenn die das Wasser umgebende Lufttemperatur sehr viel höher ist, ähnlich wie man das aus der Natur z.B. von Bergbachwasser oder Bergseen im Hochsommer kennt. Eine Verlängerung der natürlichen Haltbarkeitsdauer des Wassers scheint durch Verwirbelung ebenso möglich zu sein. Die hier vorgestellte Erfindung kann je nach Anwendung anhand unterschiedlich konstruierter Durchströmplatten mit darauf abgestimmten Misch- u. Verwirbelungsunterstützern jeweils so aufgebaut werden, dass die in der Natur vorkommenden Misch- u./o. Verwirbelungsabläufe u. -prozesse möglichst natumah, aber trotzdem in sehr effizienten Intensitäten und Ausprägungen, nachgeahmt werden können. Hierdurch wird es möglich, Vorgänge, Effekte und Ergebnisse, die in der Natur sehr viel mehr Zeit in Anspruch nehmen, in kürzeren Vorgängen effektiv nachzuahmen.In the water research and water literature sit for a long time, especially due to the studies and experiments of water u. Naturalist Viktor Schauberger, terms such as "living water", "high-energy water", "revitalized water" or "vital water" more and more. What this means is that, in addition to chemical and biological qualities, good water should above all have a good physical quality. Observations from nature show that water and exercise are very often inseparable. When you observe water in the wild, it usually moves in one way or another. Even in stagnant waters, water movements constantly form between different layers of water due to changing temperatures and water densities. The water turbulence is a particularly intense water movement. Water turbulence and the processes involved are increasingly being seen as an efficient method of nature to stimulate or release the self-cleaning power of the water and to improve the water in its energetic state. One speaks in this context of an improvement of the energies, vibrations and information in the water. It is assumed that the internal structure of the water changes, the so-called cluster structure. This refers to accumulations of physically adhering water molecules. Water molecules have this particular peculiarity that they are slightly positive at one point and slightly negatively charged at another. As a result, the water molecules attract each other. With so-called less living water, it is assumed that larger clusters or "molecular clusters" have formed. Intense water movements such as turbulence, some researchers assume that larger clusters split into smaller and smaller clusters or dissolve. According to these explanations, the water would thereby become a so-called finely divided state and could possibly be more easily absorbed or utilized by biological organisms such as plants, animals and humans. Furthermore, some researchers assume that the water can accumulate in the natural turbulence in the wild in a balanced ratio with air and. Light components and new ones subtle energies through the arising torsional forces in the turbulence and the peculiarity of the dipolar water molecule structures, which react in a special way to water movements. These theories are controversial. However, it can be observed that nature in a comprehensive way, in large dimensions and in innumerable variations water u. Air turbulence and a wide range of turbulences of other liquid, vapor and gas mixtures is formed. However one may judge individual theories, there seem to be good reasons why nature behaves this way. It can be improved by natural vortex eg taste and appearance of water. The water can be naturally enriched with oxygen. It can be observed that cool swirled water remains cool for a long time, even if the air temperature surrounding the water is much higher, similar to that known from nature, for example, from mountain stream water or mountain lakes in midsummer. An extension of the natural shelf life of the water seems to be equally possible by turbulence. The invention presented here, depending on the application based on differently designed Durchströmplatten with matching mixing u. Verwirbelungsunterstützern each be constructed so that the occurring in nature Misch- u./o. Verwirbelungsabläufe u. processes as near as possible, but nevertheless can be imitated in very efficient intensities and expressions. This makes it possible to effectively imitate processes, effects and results that take much longer in nature in shorter operations.
Unterschiedliche Misch- u./o. Verwirbelungsvorrichtungen u.- verfahren versuchen bereits, Verwrirbelungsprozesse nutzbar zu machen. Die vorgestellte Erfindung bedient sich mehrerer Funktionsmechanismen gleichzeitig, um auf möglichst wirksame, aber dennoch naturnahe Weise die Flüssigkeits- u./o. Luft- u.lo. Dampf- u./o. Gasqualitäten zu verbessern. Der japanische Wasserforscher Masaru Emoto berichtet in seinen Büchern über Wasser davon, dass Wasser ein äußerst empfindliches und empfindsames Medium ist, das sogar auf menschliche Emotionen und auf Töne in erstaunlicher Weise reagieren kann. Die hier beschriebene Erfindung versucht derartige Phänomene und Beobachtungen zu berücksichtigen. Da die Misch- u./o. Verwirbelungsvorrichtung in intensiven Kontakt mit Dämpfen u./o. Gasen u./o. Flüssigkeits-Feststoff-Gemischen u./o. Flüssigkeiten wie z.B. Wasser kommt, wird angenommen, dass die hier vorgestellte Erfindung selbst auch zu einem Überträger von Schwingungen und Informationen auf das zu mischende u./o. verwirbelnde Medium wird. Die Erfindung wird deshalb durch unterschiedliche Prozesse, Verfahren und Methoden energetisch gereinigt und dazu angeregt, für Dämpfe u./o. Gase u./o. Flüssigkeits-Feststoff-Gemische u./o. Flüssigkeiten wie z.B. Wasser nützliche Energien und Schwingungen möglichst aufzubauen und anzuziehen, um den Flüssigkeiten u./o. Flüssigkeits-Feststoff-Gemischen u./o. Dämpfen u./o. Gasen ein möglichst förderliches und naturnahes Umfeld zu bieten.Different mixing and / or. Swirling devices and methods are already trying to make use of swirling processes. The presented invention makes use of several functional mechanisms at the same time in order to maximize the effectiveness of the liquid u./o. Air and lo. Steam and / or. Improve gas qualities. The Japanese water researcher Masaru Emoto reports in his books on water that water is an extremely sensitive and sensitive medium that can even respond to human emotions and sounds in an amazing way. The invention described herein seeks to take such phenomena and observations into account. Since the mixing u./o. Verwirbelungsvorrichtung in intensive contact with vapors u./o. Gases and / or. Liquid-solid mixtures u./o. Liquids, e.g. Water comes, it is assumed that the invention presented here itself to a transmitter of vibrations and information to be mixed u./o. swirling medium becomes. The invention is therefore energetically purified by different processes, methods and methods and stimulated for vapors u./o. Gases and / or. Liquid-solid mixtures u./o. Liquids, e.g. To build up and attract useful energies and vibrations as much as possible to Liquid-solid mixtures u./o. Steaming and / or. Gases to provide the most beneficial and natural environment.
Dokument
Nachdem Flüssigkeiten u./o. Flüssigkeits-Feststoff-Gemische u./o. Dämpfe u/o. Gase in die Misch- u./o. Verwirbelungsvorrichtung eingeflossen sind, treffen sie auf eine Durchströmplatte, die auf spezielle Weise mit Löchern versehen wurde. Es lassen sich durch den möglichen Einsatz unterschiedlicher Durchströmplatten die Misch- u./o. Verwirbelungsabläufe variieren, um ganz unterschiedliche Effekte und Ergebnisse erzielen zu können. Obwohl die unterschiedlichen Durchströmplatten sich voneinander unterscheiden , weist die Konstruktion der aufgeprägten Löcher u./o. Lochformationen auf diesen Durchströmplatten folgende Merkmale auf:
- Auf einer Durchströmplatte sind alle dort aufgebrachten Löcher u./o. Lochformationen in der gleichen Lochdrehrichtung, im Uhrzeigersinn rechtsdrehend oder gegen den Uhrzeigersinn linksdrehend, angeordnet.
- Die in gleicher Lochdrehrichtung angeordneten Löcher u./o. Lochformationen sind entweder alle in gleichen Winkelgrößen auf einer Durchströmplatte aufgebracht oder die Löcher liegen in bestimmten Anordnungen in unterschiedlichen Winkeln so auf einer Durchströmplatte, dass es zu zusätzlichen lokalen Vermischungen u.lo. Verwirbelungen an diesen Stellen kommt innerhalb der Gesamtvermischung u./o. Gesamtverwirbelung.
- Die Löcher u./o. Lochformationen sind symmetrisch u./o. gleichmäßig auf einer Durchströmplatte verteilt. Dies ist notwendig, damit geordnete u./o. naturnahe u./o. intensive Wirbel erzeugt werden können.
- On a Durchströmplatte are all there applied holes u./o. Hole formations in the same direction of hole rotation, clockwise clockwise or counterclockwise anti-clockwise arranged.
- The arranged in the same direction of rotation holes u./o. Hole formations are either all applied at equal angular sizes on a flow plate, or in certain arrangements the holes lie at different angles on a flow plate such that it causes additional local mixing u.lo. Turbulence at these points comes within the total mix u./o. Gesamtverwirbelung.
- The holes u./o. Hole formations are symmetrical and / or. evenly distributed on a flow plate. This is necessary for orderly u./o. natural and u./o. intense vortices can be generated.
Nachdem Flüssigkeiten u./o. Flüssigkeits-Feststoff-Gemische u./o. Dämpfe u./o. Gase aus einer Durchströmplatte herausströmen, treffen sie auf einen Misch- u./o. Verwirbelungsunterstützer, ein weiteres Steuerungselement der Vermischung u./o. Verwirbelung. Misch- u.lo. Verwirbelungsunterstützer können z.B. konische oder hyperbolische Trichter sein. Verwendet man z.B. derartige Trichter, bilden Flüssigkeiten wie Wasser durch Durchströmplatten vorbereitete intensive Wirbel aus. Eine Flüssigkeit wie Wasser verlässt den Trichter dann in -sich spiralförmig strömend bzw. wirbelnd und formt außerhalb der Misch- u./o. Verwirbelungsvorrichtung eine in sich spiralförmig strömend bzw. wirbelnde Flüssigkeitsglocke. Die Größe und Wirbelintensität (intensiv rechtswirbelnd oder intensiv linkswirbelnd) dieser entstehenden Glocke spielen erfahrungsgemäß eine Rolle für entstehende Qualitätsverbesserungen erzeugter Flüssigkeiten. Damit z.B. eine große und intensiv wirbelnde Wasserglocke an einem gewöhnlichen Haushaltswasseranschluss mit normaler Wasserausflussmenge entstehen kann, muss der Trichter bestmöglich mit jeweiligen Durchströmplatten korrespondieren. Es sind ebenso Misch- u.lo. Verwirbelungsunterstützer einsetzbar, die innerhalb geschlossener Leitungssysteminfrastrukturen funktionsfähig sind. Es sind unterschiedliche Misch- u./o. Verwirbelungsunterstützersysteme u. -verfahren funktionsfähig, je nach verwendeten Durchströmplatten und je nach Flüssigkeiten u./o. Flüssigkeits-Feststoff-Gemischen u./o. Dämpfen u./o. Gasen und je nach gewünschten Effekten und Ergebnissen. Die genaue Konstruktion und Anpassung der jeweiligen Durchströmplatten an spezifische Flüssigkeiten u./o. Flüssigkeits-Feststoff-Gemische u./o. Dämpfe u./o. Gase und an die jeweiligen Misch- u. Verwirbelungsunterstützer erfordert Erfahrung und Kenntnisse der Entstehung der jeweiligen Misch- u.lo. Verwirbelungsabläufe und -strukturen. Dazu sind Analysen und häufig viele Versuche notwendig. Die Vermischungs- u./o. Verwirbelungsabläufe reagieren sehr sensibel auf kleine Veränderungen der unterschiedlichen Einzelfaktoren. Ein entsprechender Gesamteffekt bzw. Gesamtergebnis, z.B. spürbare und deutliche Qualitätsverbesserungen von Flüssigkeiten u./o. Flüssigkeits-Feststoff-Gemischen u./o. Dämpfen u./o. Gasen kann nur bei entsprechender Anpassung der Einzelfaktoren und einem gelungenen Zusammenspiel aller Faktoren (Synergieeffekte) erwartet bzw. erreicht werden. Es sind viele Anwendungen der Erfindung zur Flüssigkeits- u.lo. Flüssigkeits-Feststoff-Gemisch- u.lo. Dampf- u./o. Gasverbesserung möglich und vorstellbar. Die Wasseraufbereitung wurde angesprochen. Eine Verbesserung von Weinen, Bieren und Säften, vor allem auch geschmacklich, scheint naheliegend. Es könnte sich erweisen, dass selbst eine Qualitätsverbesserung von Blut möglich sein könnte durch ein solches Verfahren, denn es wird angenommen, dass auch Blut im Körper vielerlei Verwirbelungen ausbildet. Bei Dämpfen könnte man an eine Anwendung in Saunen denken, wobei man Wasserdämpfe in Saunen ansaugen könnte und sie dann durch die Misch- u./o. Verwirbelungsvorrichtung leiten würde, um sie dann in stark verwirbelnden Bewegungen wieder freizusetzen. Es ist möglich, dass sich hierdurch das Saunaerlebnis und die Saunawirkungen verbessern ließen. Ähnliche Möglichkeiten eröffnen sich für Luft- und andere Gasgemische, z.B. in Verbindung mit Klimaanlagen und anderen Belüftungssystemen.After liquids u./o. Liquid-solid mixtures u./o. Vapors and / or. Gases emanate from a flow plate, they meet a mixed u./o. Verwirbelungsunterstützer, another control element of the mixing u./o. Turbulence. Mixed u.lo. Turbulating assistants may be, for example, conical or hyperbolic funnels. If, for example, such funnels are used, liquids such as water form intensive vortices prepared by flow-through plates. A liquid such as water then leaves the funnel in spiraling or swirling form and outside the mixing u./o. Verwirbelungsvorrichtung a spirally flowing or swirling liquid bell. The size and vortex intensity (intense right-whirling or intensive left-whirling) of this resulting bell experience has a role for resulting quality improvements generated fluids. So that, for example, a large and intensely swirling water bell can occur at a normal domestic water connection with normal water outflow, the funnel must correspond as well as possible with respective flow plates. There are also mixed u.lo. Swirl assistants that are functional within closed-loop management infrastructures. There are different mixed u./o. Swirl Support Systems & Systems -functionally, depending on the used flow plates and depending on liquids u./o. Liquid-solid mixtures u./o. Steaming and / or. Gases and depending on the desired effects and results. The exact construction and adaptation of the respective flow plates to specific fluids u./o. Liquid-solid mixtures u./o. Vapors and / or. Gases and to the respective mixing u. Verwirbelungsunterstützer requires experience and knowledge of the origin of the respective mixing u.lo. Turbulence processes and structures. This requires analyzes and often many tests. The mixing u./o. Turbulence processes are very sensitive to small changes in the various individual factors. A corresponding overall effect or overall result, eg noticeable and significant quality improvements of liquids and / or. Liquid-solid mixtures u./o. Steaming and / or. Gases can only be expected or achieved with a corresponding adjustment of the individual factors and a successful interaction of all factors (synergy effects). There are many applications of the invention for liquid u.lo. Liquid-solid mixture u.lo. Steam and / or. Gas improvement possible and imaginable. The water treatment was addressed. An improvement of wines, beers and juices, especially in terms of taste, seems obvious. It could prove that even a quality improvement of blood could be possible by such a procedure, because it is assumed that also blood in the body forms many vortexes. With vapors one could think of an application in saunas, whereby one could suck in water vapors in saunas and then through the mixing u./o. Swirling device would lead to then release them in highly swirling movements again. It is possible that this could improve the sauna experience and the sauna effects. Similar possibilities open up for air and other gas mixtures, eg in connection with air conditioning systems and other ventilation systems.
Die Misch- u./o. Verwirbelungsvorrichtung ist ebenso geeignet zum intensiven und kosteneffizienten Vermischen unterschiedlicher Substanzen. Hierzu leitet man in die einzelnen Löcher der Durchströmplatten die zu mischenden Substanzen, wiederum Flüssigkeiten u./o. Flüssigkeits-Feststoff-Gemische u./o. Dämpfe u./o. Gase. Man kann durch die Wahl der Lochgrößen und die Menge der eingeleiteten Substanz die Strömungsgeschwindigkeiten steuern. Die Austrittspunkte aus einer Durchströmplatte lassen sich -ebenfalls genau festlegen. Will man zwei Substanzen miteinander vermischen, wird z.B. die Substanz A in ein Durchströmloch A geleitet und die Substanz B in ein Durchströmloch B. Man würde dann die Austrittspunkte von Durchströmloch A und Durchströmloch B nahe aneinander legen, so dass es zu einer lokalen Vermischung u./o. Verwirbelung kommt. Will man nur zwei Substanzen vermischen, wiederholt man das gleiche Prinzip viele Male auf einer Durchströmplatte und erreicht damit viele lokale Vermischungen u./o. Verwirbelungen der beiden Substanzen sowie eine Vermischung u./o. Verwirbelung der vielen einzelnen Lokalvermischungen u./o. Verwirbelungen untereinander und ineinander in einer großen Gesamtvermischung u./o. Gesamtverwirbelung. Man hat dadurch die beiden Substanzen auf Intensive und kosteneffiziente Weise miteinander vermischt u./o, verwirbelt. Ein weiterer Vorteil eines derartigen Vermischungs- u.lo. Verwirbelungsverfahrens ist, dass sich sehr komplexe Vermischungs- u./o. Verwirbelungsabläufe mit zahlreichen Substanzen durchführen lassen, wobei sowohl die Dosierungen als auch die Austrittspunkte einzelner Substanzen genau gesteuert werden können. Will man z.B. zuerst zwei Gase miteinander vermischen u./o. verwirbeln und parallel dazu zwei Flüssigkeiten miteinander vermischen u./o. verwirbeln, um dann das Gasgemisch und das Flüssigkeitsgemisch wiederum miteinander zu vermischen, kann man durch eine effiziente Anordnung der einzuleitenden Substanzen in eine Durchströmplatte und die Festlegung der entsprechenden Austrittspunkte der jeweiligen Substanzen, und durch Festlegung der jeweiligen Mengen und Lochgrößen sowie des geeigneten Vermisch- u./o. Verwirbelungsunterstützers den Vermischungs- u./o. Verwirbelungsablauf genau steuern. In diesem Beispiel würde man die Austrittspunkte der Gase aneinander legen und würde ebenfalls die Austrittspunkte der Flüssigkeiten aneinander legen. Hierdurch käme es dann zunächst zu lokalen Vermischungen u./o. Verwirbelungen der Gase untereinander sowie der Flüssigkeiten untereinander. In der Gesamtvermischung u./o. Gesamtverwirbelung würde sich dann das Gasgemisch mit dem Flüssigkeitsgemisch wiederum vermischen u./o. verwirbeln. Man erreicht in einem Vorgang eine intensive Gesamtvermischung, wofür man bei anderen Vorrichtungen u. Verfahren mehrere Arbeitsschritte, mehr Energieaufwand und mehr Platzaufwand benötigen würde. Es ist auch möglich, die Substanzen gar nicht erst ausströmen zu lassen aus einer Durchströmplatte, sondern die einzelnen Durchströmlöcher schon innerhalb einer Durchströmplatte ineinander übergehen zu lassen, so dass es schon zu lokalen Vermischungen u./o. Verwirbelungen kommt, bevor die Substanzen die Durchströmplatte verlassen. Es bieten sich zahlreiche Variationen an, wie man derartige Abläufe steuern kann. Die genaue Konstruktion einer jeweiligen Anwendung bedarf genauer Planungen, Analysen und Versuche. Es sind zahlreiche Anwendungen dieses Verfahrens möglich, z.B. in technischen und wissenschaftlichen Verfahren, in der Chemie, Biologie, Pharmazeutik, Medizin oder im Getränke- u. Nahrungsmittelbereich.The mixed u./o. Verwirbelungsvorrichtung is also suitable for intensive and cost-effective mixing of different substances. For this purpose, the substances to be mixed are passed into the individual holes of the flow-through plates, again liquids and / or. Liquid-solid mixtures u./o. Vapors and / or. Gases. You can control the flow rates by choosing the hole sizes and the amount of substance introduced. The exit points from a Durchströmplatte can also specify exactly. If you want to mix two substances together, for example, the substance A is passed into a flow hole A and the substance B in a flow hole B. One would then put the exit points of flow hole A and flow hole B close to each other, so that there is a local mixing u. /O. Swirling comes. If you want to mix only two substances, repeating the same principle many times on a Durchströmplatte and thus achieved many local mixing u./o. Turbulence of the two substances and a mixing u./o. Verwirbelung the many individual Lokalvermischungen u./o. Turbulence among each other and into each other in a large total mixture u./o. Gesamtverwirbelung. It has thereby mixed the two substances in an intensive and cost-effective manner u./o, vortexed. Another advantage of such a mixing u.lo. Verwirbelungsverfahrens is that very complex Mixing and / or. Swirling processes can be performed with numerous substances, with both the dosages and the exit points of individual substances can be precisely controlled. For example, if you want to mix two gases with each other u./o. swirl and mix two liquids parallel to each other u./o. vortex, and then mix the gas mixture and the liquid mixture again with each other, one can by an efficient arrangement of the substances to be introduced into a Durchströmplatte and the determination of the corresponding exit points of the respective substances, and by fixing the respective amounts and hole sizes and the appropriate mixing u ./O. Turbulence supporter the mixing u./o. Accurately control the swirling process. In this example, one would put the exit points of the gases together and would also put the exit points of the liquids together. This would then lead first to local mixing u./o. Turbulence of gases among themselves and liquids among themselves. In the total mixture u./o. Gesamtverwirbelung would then mix the gas mixture with the liquid mixture again u./o. swirl. One reaches in one process an intensive total mixing, what you u in other devices. Procedure would require several steps, more energy and more space. It is also possible not to let the substances flow out of a Durchströmplatte, but to let the individual Durchströmlöcher already within a Durchströmplatte into each other, so it is already u./o to local mixing. Turbulence comes before the substances leave the flow plate. There are numerous variations on how to control such processes. The exact construction of a particular application requires accurate planning, analysis and testing. Numerous applications of this method are possible, for example in technical and scientific processes, in chemistry, biology, pharmaceutics, medicine or in the beverage industry. Food industry.
- 11
- Kopfstück SeitenansichtHeadpiece side view
- 22
- Durchströmplatte SeitenansichtDurchströmplatte side view
- 33
- Winkellage eines LochsAngular position of a hole
- 44
- Konischer Trichter SeitenansichtConical funnel side view
- 55
- Zusammengeschraubte Misch- u./o. VerwirbelungsvorrichtungScrewed mixed u./o. The interlacing
- 66
- 12-lochige Durchströmplatte12-hole flow-through plate
- 77
- 24-lochige Durchströmplatte24-hole flow-through plate
- 88th
- 32-lochige Durchströmplatte32-hole flow plate
- 99
- 40-lochige Durchströmplatte40-hole flow plate
- 1010
- 48-lochige Durchströmplatte48-hole flow plate
- 1111
- 60-lochige Durchströmplatte60-hole flow plate
- 1212
- 6-gliederiges Rad als 409-lochige Durchströmplatte6-membered wheel as a 409-hole throughflow plate
- 1313
- 3-gliederige Spirale als 196-lochige Durchströmplatte3-element spiral as a 196-hole flow-through plate
- 1414
- 3-gliederige Formation als 28-lochige Durchströmplatte3-membered formation as a 28-hole flow-through plate
- 1515
- 3-gliederige Formation als 40-lochige Durchströmplatte3-membered formation as a 40-hole flow-through plate
- 1616
- 8-gliederige Formation als 24-lochige Durchströmplatte8-membered formation as a 24-hole flow-through plate
- 1717
- 16-lochige Durchströmplatte16-hole flow-through plate
- 1818
- 8 Dreilochformationen als 24-lochige Durchströmplatte8 three-hole formations as a 24-hole flow-through plate
- 1919
- 8 Vierlochformationen als 32-lochige Durchströmplatte8 four-hole formations as a 32-hole flow-through plate
- 2020
- 8 Fünflochformationen als 40-lochige Durchströmplatte8 five-hole formations as a 40-hole throughflow plate
- 2121
- 12 Dreilochformationen, paarweise angeordnet als 36-lochige Durchströmplatte12 three-hole formations, arranged in pairs as a 36-hole flow-through plate
- 2222
- Querschnitt Durchströmplatte mit speziellen Lochgrößen und LochwinkellagenCross section throughflow plate with special hole sizes and hole angle layers
- 2323
- kleinerer Lochwinkelsmaller hole angle
- 2424
- mittelgroßer Lochwinkelmedium-sized hole angle
- 2525
- größerer Lochwinkellarger hole angle
- 2626
- Querschnitt Durchströmplatte mit speziellen Lochgrößen und LochwinkellagenCross section throughflow plate with special hole sizes and hole angle layers
- 2727
- kleinerer Lochwinkelsmaller hole angle
- 2828
- mittelgroßer-Lochwinkelmedium-sized hole angle
- 2929
- größerer Lochwinkellarger hole angle
- 3030
- Querschnitt Durchströmplatte mit speziellen Lochgrößen und LochwinkellagenCross section throughflow plate with special hole sizes and hole angle layers
- 3131
- kleinerer Lochwinkelsmaller hole angle
- 3232
- größerer Lochwinkellarger hole angle
- 3333
- Querschnitt Durchströmplatte mit speziellen Lochgrößen und LochwinkellagenCross section throughflow plate with special hole sizes and hole angle layers
- 3434
- kleinerer Lochwinkelsmaller hole angle
- 3535
- mittelgroßer Lochwinkelmedium-sized hole angle
- 3636
- größerer Lochwinkellarger hole angle
- 3737
- Querschnitt Durchströmplatte mit speziellen Lochgrößen und LochwinkellagenCross section throughflow plate with special hole sizes and hole angle layers
- 3838
- kleinerer Lochwinkelsmaller hole angle
- 3939
- mittelgroßer Lochwinkelmedium-sized hole angle
- 4040
- größerer Lochwinkellarger hole angle
- 4141
- Querschnitt Durchströmplatte mit speziellen Lochgrößen und LochwinkellagenCross section throughflow plate with special hole sizes and hole angle layers
- 4242
- kleinerer Winkelsmaller angle
- 4343
- größerer Winkellarger angle
Claims (24)
- A mixing and/or swirling device (5) for mixing and/or swirling liquids and/or liquid-solid mixtures and/or vapors and/or gases, comprising a mixing and/or swirling facilitation device and at least one through-flow plate (2), characterized in that the through-flow plate is respectively provided with at least three obliquely arranged, identical hole formations, distributed in a circular, regular positional arrangement, arranged singly or in pairs, respectively consisting of at least two holes, which are adjacent to each other and/or respectively merge into each other inside the through-flow plate, with the distances between the singly arranged hole formations or the hole formations arranged in pairs on the through-flow plate being respectively of the same size.
- The mixing and/or swirling device (5) according to claim 1, characterized in that the mixing and/or swirling facilitation device is conically shaped.
- The mixing and/or swirling device (5) according to claim 1, characterized in that the mixing and/or swirling facilitation device is hyperbolically shaped.
- The mixing and/or swirling device (5) according to claim 1, characterized in that the mixing and/or swirling facilitation device is spherically shaped.
- The mixing and/or swirling device (5) according to claim 1, characterized in that the at least one through-flow plate (6) is provided with six identical hole formations, which are respectively evenly distributed in a circle on the through-flow plate (6), and respectively consist of pairs of holes.
- The mixing and/or swirling device (5) according to claim 1, characterized in that the at least one through-flow plate (7) is provided with twelve identical hole formations, which are respectively evenly distributed in a circle on the through-flow plate (7), and respectively consist of pairs of holes.
- The mixing and/or swirling device (5) according to claim 1, characterized in that the at least one through-flow plate (8) is provided with sixteen identical hole formations, which are respectively evenly distributed in a circle on the through-flow plate (8), and respectively consist of pairs of holes.
- The mixing and/or swirling device (5) according to claim 1, characterized in that the at least one through-flow plate (9) is provided with twenty identical hole formations, which are respectively evenly distributed in a circle on the through-flow plate (9), and respectively consist of pairs of holes.
- The mixing and/or swirling device (5) according to claim 1, characterized in that the at least one through-flow plate (10) is provided with twenty-four identical hole formations, which are respectively evenly distributed in a circle on the through-flow plate (10), and respectively consist of pairs of holes.
- The mixing and/or swirling device (5) according to claim 1, characterized in that the at least one through-flow plate (11) is provided with thirty identical hole formations, which are respectively evenly distributed in a circle on the through-flow plate (11), and respectively consist of pairs of holes.
- The mixing and/or swirling device (5) according to claim 1, characterized in that the at least one through-flow plate (16) is provided with eight identical hole formations, which are respectively evenly distributed in a circle on the through-flow plate (16), and respectively consist of three holes of different sizes.
- The mixing and/or swirling device (5) according to claim 1, characterized in that the at least one through-flow plate (17) is provided with eight identical hole formations, which are respectively evenly distributed in a circle on the through-flow plate (17), and respectively consist of pairs of holes.
- The mixing and/or swirling device (5) according to claim 1, characterized in that the at least one through-flow plate (18) is provided with eight identical hole formations, which are respectively evenly distributed in a circle on the through-flow plate (18), and respectively consist of three holes of the same size.
- The mixing and/or swirling device (5) according to claim 1, characterized in that the at least one through-flow plate (19) is provided with eight identical hole formations, which are respectively evenly distributed in a circle on the through-flow plate (19), and respectively consist of four holes of the same size.
- The mixing and/or swirling device (5) according to claim 1, characterized in that the at least one through-flow plate (20) is provided with eight identical hole formations, which are respectively evenly distributed in a circle on the through-flow plate (20), and respectively consist of five holes of the same size, arranged in a circle.
- The mixing and/or swirling device (5) according to claim 1, characterized in that the at least one through-flow plate (21) is provided with twelve hole formations arranged in pairs, respectively consisting of three holes of different size per hole formation, which are evenly distributed in pairs in a circle on the through-flow plate (21).
- The mixing and/or swirling device (5) according to claim 1, characterized in that the at least one through-flow plate (21) is provided with twelve hole formations arranged in pairs, wherein each hole formation consists of three holes of different sizes, which are evenly distributed in pairs in a circle on the through-flow plate (21), smaller holes with smaller angles (23) inside the through-flow plate (21), (22) opening into medium-sized holes, the medium-sized holes with medium angles (24) in turn also inside the through-flow plate (21), (22) merging into larger holes, and the larger holes having the largest angles (25).
- The mixing and/or swirling device (5) according to claim 1, characterized in that the at least one through-flow plate (16) is provided with eight identical hole formations, wherein the hole formations are evenly distributed in a circle on the through-flow plate (16), and respectively consist of three holes of different sizes, larger holes with smaller angles (27) inside the through-flow plate (16), (26) opening into the medium-sized holes, the medium-sized holes with medium angles (28) in turn also inside the through-flow plate (16), (26) merging into smaller holes, and the smaller holes having the largest angles (29).
- The mixing and/or swirling device (5) according to claim 1, characterized in that the at least one through-flow plate (19) is provided with eight identical hole formations, wherein the hole formations are evenly distributed in a circle on the through-flow plate (19), and respectively consist of four holes of the same size, and holes located closer to the middle of the through-flow plate (19) with smaller angles (31) inside the through-flow plate (19), (30) opening into holes located closer to the edge of the through-flow plate (19), (30) with larger angles (32).
- The mixing and/or swirling device (5) according to claim 1, characterized in that the at least one through-flow plate (2) is provided with hole formations, which respectively consist of holes interconnected inside the through-flow plate (22).
- The mixing and/or swirling device (5) according to claim 17, characterized in that the prolongations of the smaller holes with smaller angles (34), the medium-sized holes with medium angles (35), and the larger holes with larger angles (36) meet outside the through-flow plate (21), (33).
- The mixing and/or swirling device (5) according to claim 18, characterized in that the prolongations the larger holes with smaller angles (38), the medium-sized holes with medium angles (39), and the smaller holes with larger angles (40) meet outside the through-flow plate (16), (37).
- The mixing and/or swirling device (5) according to claim 19, characterized in that the prolongations of the holes located closer to the middle of the through-flow plate (19), (41) with smaller angles (42), and the holes located closer to the edge of the through-flow plate (19), (41) with larger angles (43) meet outside the through-flow plate (19), (41).
- The mixing and/or swirling device (5) according to claim 1, characterized in that the at least one through-flow plate (2) is provided with hole formations, respectively consisting of holes meeting outside the through-flow plate (33).
Priority Applications (1)
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PL05850183T PL1827667T3 (en) | 2004-12-22 | 2005-12-20 | Mixing and/or turbulent mixing device |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
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DE202004019745U DE202004019745U1 (en) | 2004-12-22 | 2004-12-22 | Vortexing device for improving fluids |
PCT/DE2005/002292 WO2006066558A1 (en) | 2004-12-22 | 2005-12-20 | Mixing and/or turbulent mixing device and method |
Publications (2)
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EP1827667A1 EP1827667A1 (en) | 2007-09-05 |
EP1827667B1 true EP1827667B1 (en) | 2010-05-19 |
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EP05850183A Not-in-force EP1827667B1 (en) | 2004-12-22 | 2005-12-20 | Mixing and/or turbulent mixing device |
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US (2) | US20100014378A1 (en) |
EP (1) | EP1827667B1 (en) |
JP (1) | JP4966863B2 (en) |
KR (1) | KR20070099615A (en) |
CN (1) | CN100586545C (en) |
AT (1) | ATE468167T1 (en) |
AU (1) | AU2005318737A1 (en) |
CA (1) | CA2592000A1 (en) |
DE (3) | DE202004019745U1 (en) |
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PL (1) | PL1827667T3 (en) |
RU (1) | RU2403083C2 (en) |
WO (1) | WO2006066558A1 (en) |
Families Citing this family (28)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7611080B2 (en) * | 2006-06-05 | 2009-11-03 | Spraying Systems Co. | Full cone air assisted spray nozzle for continuous metal casting cooling |
US7901641B2 (en) * | 2008-07-22 | 2011-03-08 | Uop Llc | Sprayer for at least one fluid |
US9522348B2 (en) | 2008-07-24 | 2016-12-20 | Food Safety Technology, Llc | Ozonated liquid dispensing unit |
US9174845B2 (en) | 2008-07-24 | 2015-11-03 | Food Safety Technology, Llc | Ozonated liquid dispensing unit |
US20120178895A1 (en) * | 2009-08-26 | 2012-07-12 | Bayer Materialscience Ag | Method and device for the production of a spray application consisting of reactive plastic |
JP5728892B2 (en) * | 2010-11-04 | 2015-06-03 | 日産自動車株式会社 | motor |
WO2013121295A2 (en) * | 2012-02-17 | 2013-08-22 | Wiab Water Innovation Ab | Mixing device |
ES2714503T3 (en) * | 2012-02-21 | 2019-05-28 | Ecolab Usa Inc | Controlled Dissolution Solid Product Dispenser |
WO2014136837A1 (en) * | 2013-03-06 | 2014-09-12 | 帝人株式会社 | Nonaqueous-secondary-battery separator and nonaqueous secondary battery |
KR101507653B1 (en) * | 2013-05-08 | 2015-03-31 | 김소정 | High specific gravity adulteration treating apparatus for water recycling |
KR101587691B1 (en) * | 2013-10-22 | 2016-01-27 | 김소정 | Purifying apparatus for lake |
JP2014221475A (en) * | 2014-06-12 | 2014-11-27 | ヴァトレコ イーペー アーベー | Vortex generator |
EP3218093B1 (en) * | 2014-11-10 | 2018-12-26 | EME Finance Ltd | Device for mixing water and diesel oil, apparatus and process for producing a water/diesel oil micro-emulsion. |
US20160368628A1 (en) | 2015-06-19 | 2016-12-22 | Telebrands Corp. | System, device, and method for filling at least one balloon |
US10259600B2 (en) | 2015-06-19 | 2019-04-16 | Telebrands Corp. | Container sealing device |
US9776744B2 (en) | 2015-06-19 | 2017-10-03 | Telebrands Corp. | Container sealing device |
US9572555B1 (en) * | 2015-09-24 | 2017-02-21 | Ethicon, Inc. | Spray or drip tips having multiple outlet channels |
USD793485S1 (en) | 2015-11-20 | 2017-08-01 | Telebrands Corp. | Device for filling multiple water balloons |
USD793483S1 (en) | 2015-11-20 | 2017-08-01 | Telebrands Corp. | Device for filling multiple water balloons |
USD793484S1 (en) | 2015-11-20 | 2017-08-01 | Telebrands Corp. | Device for filling multiple water balloons |
DE102016208653A1 (en) | 2016-05-19 | 2017-11-23 | Lechler Gmbh | Nozzle for spraying liquids |
FR3059573B1 (en) * | 2016-12-02 | 2019-01-25 | Aptar France Sas | HEAD OF DISTRIBUTION OF FLUID PRODUCT |
IT201600132801A1 (en) | 2016-12-30 | 2018-06-30 | Eme International Ltd | Apparatus and process for producing liquid from biomass, biofuel and biomaterial |
JP6617228B2 (en) * | 2017-09-29 | 2019-12-11 | 株式会社ヤマト | Water agitator |
GB201817692D0 (en) * | 2018-10-30 | 2018-12-19 | Ge Healthcare | Mixing device |
KR102322579B1 (en) * | 2021-02-04 | 2021-11-09 | 태웅엔지니어링 주식회사 | swirl diffuser |
US20220297141A1 (en) * | 2021-03-18 | 2022-09-22 | Spraying Systems Co. | Pulse width modulating spraying system |
CN113090946B (en) * | 2021-04-06 | 2022-04-05 | 西南石油大学 | Clam type pipeline structure for promoting mixing of natural gas and hydrogen in hydrogen-doped natural gas pipeline |
Family Cites Families (22)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
NL6407769A (en) * | 1963-07-10 | 1965-01-11 | ||
US3306587A (en) * | 1964-07-01 | 1967-02-28 | Combustion Eng | Apparatus for mixing fluids |
US3582048A (en) * | 1969-06-12 | 1971-06-01 | Union Oil Co | Inline fluid mixing device |
JPS52148541A (en) * | 1976-06-07 | 1977-12-09 | Toyota Motor Corp | Spray gun for electrostatic powder coating |
JPS53119314A (en) * | 1977-03-24 | 1978-10-18 | Teijin Ltd | Taking off method of tows |
US4471912A (en) * | 1983-03-01 | 1984-09-18 | Hancock Homer H | Waterbubble nozzle |
US4647212A (en) * | 1986-03-11 | 1987-03-03 | Act Laboratories, Inc. | Continuous, static mixing apparatus |
SU1456205A1 (en) * | 1986-09-05 | 1989-02-07 | Центральный Научно-Исследовательский И Проектно-Технологический Институт Механизации И Электрификации Животноводства Южной Зоны Ссср | Mixer |
JPH0466144A (en) * | 1990-07-04 | 1992-03-02 | Toshiba Corp | Nozzle |
US5388906A (en) * | 1991-12-18 | 1995-02-14 | E. I. Du Pont De Nemours And Company | Static mixer for two or more fluids |
US5281132A (en) * | 1992-08-17 | 1994-01-25 | Wymaster Noel A | Compact combustor |
JP3163841B2 (en) * | 1993-04-28 | 2001-05-08 | いすゞ自動車株式会社 | Subchamber engine |
NO177874C (en) * | 1993-07-14 | 1996-10-30 | Sinvent As | Device for mixing the components in a fluid flow, and using the device in a mass flow meter |
JPH0926114A (en) * | 1995-07-12 | 1997-01-28 | Osaka Gas Co Ltd | Main stop type hot water heater |
DE19810753C2 (en) * | 1998-03-12 | 2000-07-13 | Aquatherm Gmbh Kunststoff Extr | Melt mixer for extruders for the production of plastic parts |
US6186179B1 (en) * | 1998-09-18 | 2001-02-13 | Panametrics, Inc. | Disturbance simulating flow plate |
DE19928123A1 (en) * | 1999-06-19 | 2000-12-28 | Karlsruhe Forschzent | Static micromixer has a mixing chamber and a guiding component for guiding fluids to be mixed or dispersed with slit-like channels that widen in the direction of the inlet side |
US6672756B1 (en) * | 2002-02-14 | 2004-01-06 | The United States Of America As Represented By The Secretary Of The Air Force | Fluid mixer |
JP3794687B2 (en) * | 2002-08-23 | 2006-07-05 | 株式会社山武 | Micro emulsifier |
JP4017508B2 (en) * | 2002-11-29 | 2007-12-05 | 株式会社デンソー | Fuel injection device |
DE20219885U1 (en) * | 2002-12-21 | 2004-04-29 | Weisenburger, Günter | Jet for stone and metal surface cleaning device has inserted part in chamber transverse to flow direction of cleaning mixture, which flows through it |
US7048202B2 (en) * | 2004-03-04 | 2006-05-23 | Siemens Vdo Automotive Corporation | Compound-angled orifices in fuel injection metering disc |
-
2004
- 2004-12-22 DE DE202004019745U patent/DE202004019745U1/en not_active Expired - Lifetime
-
2005
- 2005-12-20 WO PCT/DE2005/002292 patent/WO2006066558A1/en active Application Filing
- 2005-12-20 DE DE112005003482T patent/DE112005003482A5/en not_active Withdrawn
- 2005-12-20 JP JP2007547170A patent/JP4966863B2/en not_active Expired - Fee Related
- 2005-12-20 EP EP05850183A patent/EP1827667B1/en not_active Not-in-force
- 2005-12-20 AT AT05850183T patent/ATE468167T1/en active
- 2005-12-20 US US11/722,369 patent/US20100014378A1/en not_active Abandoned
- 2005-12-20 DK DK05850183.4T patent/DK1827667T3/en active
- 2005-12-20 KR KR1020077016339A patent/KR20070099615A/en not_active Application Discontinuation
- 2005-12-20 PL PL05850183T patent/PL1827667T3/en unknown
- 2005-12-20 RU RU2007127622/15A patent/RU2403083C2/en not_active IP Right Cessation
- 2005-12-20 AU AU2005318737A patent/AU2005318737A1/en not_active Abandoned
- 2005-12-20 CN CN200580044205A patent/CN100586545C/en not_active Expired - Fee Related
- 2005-12-20 ES ES05850183T patent/ES2346336T3/en active Active
- 2005-12-20 DE DE502005009612T patent/DE502005009612D1/en active Active
- 2005-12-20 CA CA002592000A patent/CA2592000A1/en not_active Abandoned
-
2012
- 2012-03-24 US US13/429,373 patent/US20130021871A1/en not_active Abandoned
Also Published As
Publication number | Publication date |
---|---|
KR20070099615A (en) | 2007-10-09 |
DE202004019745U1 (en) | 2005-02-24 |
WO2006066558B1 (en) | 2007-06-21 |
US20130021871A1 (en) | 2013-01-24 |
US20100014378A1 (en) | 2010-01-21 |
DE502005009612D1 (en) | 2010-07-01 |
JP2008524530A (en) | 2008-07-10 |
RU2007127622A (en) | 2009-01-27 |
DK1827667T3 (en) | 2010-09-06 |
ATE468167T1 (en) | 2010-06-15 |
WO2006066558A1 (en) | 2006-06-29 |
JP4966863B2 (en) | 2012-07-04 |
PL1827667T3 (en) | 2010-10-29 |
DE112005003482A5 (en) | 2007-11-22 |
CN101087643A (en) | 2007-12-12 |
CA2592000A1 (en) | 2006-06-29 |
RU2403083C2 (en) | 2010-11-10 |
AU2005318737A1 (en) | 2006-06-29 |
CN100586545C (en) | 2010-02-03 |
EP1827667A1 (en) | 2007-09-05 |
ES2346336T3 (en) | 2010-10-14 |
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