DE10310442A1 - Super cavitation assembly promotes molecular integration of fluids by rapid flow reversal within chamber incorporating variable geometry plug - Google Patents

Super cavitation assembly promotes molecular integration of fluids by rapid flow reversal within chamber incorporating variable geometry plug Download PDF

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DE10310442A1
DE10310442A1 DE2003110442 DE10310442A DE10310442A1 DE 10310442 A1 DE10310442 A1 DE 10310442A1 DE 2003110442 DE2003110442 DE 2003110442 DE 10310442 A DE10310442 A DE 10310442A DE 10310442 A1 DE10310442 A1 DE 10310442A1
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flow
difficult
opening
contraption
around
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Rolf Schüler
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SCHUELER, ROLF, 85567 GRAFING, DE
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Rolf Schüler
Schindler, Erhard
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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D19/00—Degasification of liquids
    • B01D19/0073—Degasification of liquids by a method not covered by groups B01D19/0005 - B01D19/0042
    • B01D19/0094—Degasification of liquids by a method not covered by groups B01D19/0005 - B01D19/0042 by using a vortex, cavitation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/40—Mixing liquids with liquids; Emulsifying
    • B01F23/41—Emulsifying
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/50—Mixing liquids with solids
    • 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
    • B01F25/30—Injector mixers
    • B01F25/31—Injector mixers in conduits or tubes through which the main component flows
    • B01F25/312—Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof
    • B01F25/3121—Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof with additional mixing means other than injector mixers, e.g. screens, baffles or rotating elements
    • 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
    • B01F25/30—Injector mixers
    • B01F25/31—Injector mixers in conduits or tubes through which the main component flows
    • B01F25/312—Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof
    • B01F25/3124—Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof characterised by the place of introduction of the main flow
    • B01F25/31241—Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof characterised by the place of introduction of the main flow the main flow being injected in the circumferential area of the venturi, creating an aspiration in the central part of the conduit
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40—Static mixers
    • B01F25/42—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
    • B01F25/43—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
    • B01F25/433—Mixing tubes wherein the shape of the tube influences the mixing, e.g. mixing tubes with varying cross-section or provided with inwardly extending profiles
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40—Static mixers
    • B01F25/42—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
    • B01F25/43—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
    • B01F25/433—Mixing tubes wherein the shape of the tube influences the mixing, e.g. mixing tubes with varying cross-section or provided with inwardly extending profiles
    • B01F25/4335—Mixers with a converging-diverging cross-section
    • 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
    • B01F25/44—Mixers in which the components are pressed through slits
    • B01F25/441—Mixers in which the components are pressed through slits characterised by the configuration of the surfaces forming the slits
    • B01F25/4413—Mixers in which the components are pressed through slits characterised by the configuration of the surfaces forming the slits the slits being formed between opposed conical or cylindrical surfaces
    • 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
    • B01F25/44—Mixers in which the components are pressed through slits
    • B01F25/442—Mixers in which the components are pressed through slits characterised by the relative position of the surfaces during operation
    • B01F25/4422—Mixers in which the components are pressed through slits characterised by the relative position of the surfaces during operation the surfaces being maintained in a fixed but adjustable position, spaced from each other, therefore allowing the slit spacing to be varied
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F31/00—Mixers with shaking, oscillating, or vibrating mechanisms
    • B01F31/80—Mixing by means of high-frequency vibrations above one kHz, e.g. ultrasonic vibrations
    • B01F31/82—Mixing by means of high-frequency vibrations above one kHz, e.g. ultrasonic vibrations the material being forced through a narrow vibrating slit
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F31/00—Mixers with shaking, oscillating, or vibrating mechanisms
    • B01F31/80—Mixing by means of high-frequency vibrations above one kHz, e.g. ultrasonic vibrations
    • B01F31/84—Mixing by means of high-frequency vibrations above one kHz, e.g. ultrasonic vibrations for material continuously moving through a tube, e.g. by deforming the tube

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Dispersion Chemistry (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

A cavitation molecular reactor promotes the integration and disintegration of solid, liquid and/or gaseous substances by rapid flow reversal within an interior chamber. The mixing takes place in a chamber (4) incorporating a moving plug (8) which part blocks the flow and which alters in diameter in response to flow reversal. The plug slides back and forth on a rigid fixed rod. The plug is a truncated cone (9). The cavity sets up a flow pattern with two opposing super-cavitation fields. The change in molecular structure is regulated by the mass flow and pressure of the opposing fluid.

Description

Die Erfindung betrifft eine Vorrichtung zur molekularen Integration und Desintegration von festen, flüssigen und/oder gasförmigen hindurchströmenden und gegenströmenden Komponenten mittels Kavitation. Dabei wird in einem Durchflussreaktor ein hydrodynamisches Kavitationsfeld aufgebaut, das in Abhängigkeit von der Konzentration der beigemengten bzw. gelösten Gase Radikale bzw. Polyoxide erzeugt, die als Katalysatoren sowie als Reaktionspartner sowohl zum Abbau, wie auch zum Aufbau molekularer Verbindungen benutzt werden können.The invention relates to a device for molecular integration and disintegration of solid, liquid and / or gaseous flowing through and countercurrent Components using cavitation. This is done in a flow reactor a hydrodynamic cavitation field is built that is dependent from the concentration of the added or dissolved gases radicals or polyoxides generates both as catalysts and as reactants used for degradation, as well as for building molecular connections can be.

Aus dem Stand der Technik sind kavitative Durchflussreaktoren, bei denen die Kavitationsfelder mittels Ultraschall generiert wird, bekannt. Je nach Anzahl und Anordnung der Ultraschallgeneratoren lassen sich damit auch Superkavitationsfelder aufbauen, das heißt eine Überlagerung von mehreren Kavitationsfeldern, die die Wirkung wesentlich verbessern. Sie werden dazu benutzt, molekulare Verbindungen, z.B. Schadstoffe, zu desintegrieren bzw. neue molekulare Verbindungen zu integrieren. Allen gemeinsam ist jedoch, dass die Erzeugung von Kavitationsfeldern mittels Ultraschall sehr energieaufwendig ist und damit nur bei begrenzten Mengen wirtschaftlich einsetzbar ist.State of the art are cavitative flow reactors, where the cavitation fields are generated using ultrasound, known. Depending on the number and arrangement of the ultrasonic generators supercavitation fields also build up with it, i.e. an overlay of several cavitation fields that significantly improve the effect. They are used to molecular compounds, e.g. pollutants, to disintegrate or integrate new molecular compounds. Common to all, however, is the creation of cavitation fields by means of ultrasound is very energy-intensive and therefore only at limited quantities can be used economically.

Hydrodynamische Kavitationsgeneratoren sind aus dem Stand der Technik bekannt. Auch diese lassen sich durch entsprechende Anordnung der schwer Umströmbahren Körper zu Superkavitationsgeneratoren erweitern, entsprechend DE 10009326 . Hierbei handelt es sich meist um statische Komponenten, die durch Versuche für die jeweiligen Fluide optimiert werden müssen. Eine Regulierungsfunktion wird dann durch Variation des Vordrucks bzw. Verschiebung der turbulenzerzeugenden Elemente erreicht. Diese hydrodynamischen Superkavitationsgeneratoren nach dem Stand der Technik erzielen hervorragende Ergebnisse beim Vermischen von Bestandteilen bzw. Komponenten eines hindurchströmenden Massestromes, mittels eines aufgebauten Superkavitationsfeld.Hydrodynamic cavitation generators are known from the prior art. These can also be expanded accordingly by arranging the bodies which are difficult to flow around to form supercavitation generators DE 10009326 , These are mostly static components that have to be optimized for the respective fluids through tests. A regulating function is then achieved by varying the admission pressure or shifting the turbulence-generating elements. These hydrodynamic supercavitation generators according to the prior art achieve excellent results when mixing components of a mass flow flowing through, by means of an established supercavitation field.

Der Erfindung liegt die Aufgabe zu Grunde, eine Vorrichtung zur molekularen Integration und Desintegration von festen, flüssigen und/oder gasförmigen hindurchströmenden und gegenströmenden Komponenten zu schaffen, die unabhängig von hohen oder niedrigen Vordrucken und unabhängig von Zusammensetzung und Dichteunterschieden der Fluide in der Lage ist, aufgrund ihrer dynamische Regulierungsmöglichkeiten ständig eine hochwirksames Superkavitationsfeld zu gewährleistet.The invention is based on the object Basically, a device for molecular integration and disintegration of solid, liquid and / or gaseous flowing through and counter-flowing components to create that independently of high or low forms and regardless of composition and Differences in density of the fluids are able due to their dynamic regulatory options constantly to ensure a highly effective super cavitation field.

Diese Aufgabe wird beim Molekularreaktor der eingangs beschriebenen Art erfindungsgemäß dadurch gelöst, daß in der Mittelachse der Durchflusskammer Zuführungskanäle eingeführt sind, über die Fluide entgegen der Strömungsrichtung des Massestromes eingebracht werden können, die in Verbindung mit den schwer Umströmbahren Körpern ein hocheffiziente gegenläufige Überlagerung von mindestens zwei Superkavitationsfeldern gewährleisten. Die hierbei freigesetzte energetische Potential schafft die Voraussetzung zum schlagartigen Aufbau neuer oder Abbau bestehender molekularer Verbindungen. Die Steuerung erfolgt dabei durch Variation des Vordruckes des Massestromes und Variation des Druckes des entgegen der Strömungsrichtung zugeführten Fluides.This task is carried out in the molecular reactor initially described type according to the invention solved in that in the Central axis of the flow chamber are introduced via the fluids against the flow direction of the mass flow can be introduced in connection with the difficult flow around bodies a highly efficient opposing overlay guarantee of at least two super cavitation fields. The released here energetic potential creates the prerequisite for sudden Building new or breaking down existing molecular compounds. The Control takes place by varying the upstream pressure of the mass flow and varying the pressure of the fluid supplied against the flow direction.

Claims (16)

Vorrichtung (100) zum Vermischen der Komponenten eines hindurchströmenden und gegenströmenden Massestromes, wobei die Komponenten insbesondere fest, flüssig oder gasförmig sein können, mittels einem hydrodynamischen Superkavitationsfeld, um eine Mischung, insbesondere eine Emulsion oder Suspension, sowie neuartige molekulare Verbindungen und Trennungen (kavitative Integration und Desintegration) zu erzeugen, mit einem Gehäuse (1), das eine Eingangsöffnung/Ausgangsöffnung (2) für die Zufuhr mindestens eines Teils des zu vermischenden Massestromes und eine Ausgangsöffnung/Eingangsöffnung (3) für die Entnahme des Massestromes aufweist. Ebenso ist eine Wechsel der Eingangsöffnung/Ausgangsöffnung (2) und (3) möglich. Dann ist in umgekehrter Weise (3) Eingangsöffnung und (2) Ausgangsöffnung, wobei das Gehäuse (1) eine Durchflusskammer (4) mit einem darin mittels einer Halterung (6) angeordneten schwer Umströmbahren Körper (8) aufweist, und der schwer Umströmbahre Körper (8) mindestens zwei schwer Umströmbahre Teilbereiche (9) besitzt, die für jeweils eine lokale Strömungseinengung sorgen, dadurch gekennzeichnet, dass der Querschnitt der Durchflusskammer (4), der senkrecht zu ihrer Mittelachse genommen wird, wenigstens in einem Teil des Bereichs, der den schwer Umströmbahren Körper (8) umgibt, bei wechselnder Strömungsrichtung des durch die Durchflusskammer (4) durchströmenden Massestromes zuerst größer und dann kleiner wird.Contraption ( 100 ) for mixing the components of a mass flow flowing through and counter-flowing, it being possible for the components to be, in particular, solid, liquid or gaseous, by means of a hydrodynamic supercavitation field, around a mixture, in particular an emulsion or suspension, and novel molecular connections and separations (cavitative integration and disintegration) to generate with a housing ( 1 ) which has an entrance opening / exit opening ( 2 ) for the supply of at least a part of the mass flow to be mixed and an outlet opening / inlet opening ( 3 ) for the removal of the mass flow. Likewise, changing the entrance opening / exit opening ( 2 ) and ( 3 ) possible. Then in reverse ( 3 ) Entrance opening and ( 2 ) Outlet opening, the housing ( 1 ) a flow chamber ( 4 ) with one in it by means of a holder ( 6 ) arranged difficult flow around body ( 8th ), and the body that is difficult to flow around ( 8th ) at least two difficult flow areas ( 9 ), which each ensure local flow restriction, characterized in that the cross section of the flow chamber ( 4 ), which is taken perpendicular to its central axis, at least in a part of the area surrounding the body which is difficult to flow around ( 8th ) surrounds, with changing flow direction through the flow chamber ( 4 ) flowing mass flow first larger and then smaller. Vorrichtung (100) nach Anspruch 1, dadurch gekennzeichnet, das der schwer Umströmbahre Körper (8) entlang der Richtung der Mittelachse der Durchflusskammer (4) verschoben werden kann, und/oder dass der schwer Umströmbahre Körper (8) starr befestigt ist.Contraption ( 100 ) according to claim 1, characterized in that the difficult flow around body ( 8th ) along the direction of the central axis of the flow chamber ( 4 ) can be moved, and / or that the body that is difficult to flow around ( 8th ) is rigidly attached. Vorrichtung (100) nach einem der vorhergehenden Ansprüche , dadurch gekennzeichnet, dass mindestens einer der schwer Umströmbahren Teilbereiche (9) so ausgebildet ist, dass sein Querschnitt, der senkrecht zu der Mittelachse der Durchflusskammer (4) genommen wird, an dem Ende des Teilkörpers, das der Eingangsöffnung/Ausgangsöffnung (2) am nächsten liegt, größer ist als an dem Ende, das der Eingangsöffnung/Ausgangsöffnung (3) am nächsten liegt.Contraption ( 100 ) according to one of the preceding claims, characterized in that at least one of the sub-regions which are difficult to flow around ( 9 ) is designed so that its cross-section, the perpendicular to the central axis of the flow chamber ( 4 ) is taken, at the end of the partial body that the input opening / output opening ( 2 ) closest to the end of the entrance opening / exit opening ( 3 ) is closest. Vorrichtung (100) nach einem der vorhergehenden Ansprüche, dadurch gekennzeichnet, dass mindestens einer der schwer Umströmbahren Teilbereiche (9) als Kegelstumpf ausgebildet ist und durch die wechselseitigen Strömungsrichtung des durch die Durchflusskammer (4) hindurchströmenden Massestromes jede Kegelspitze dem durch die Durchflusskammer (4) hindurchströmenden Massestrom zugewandt oder abgewandt ist.Contraption ( 100 ) according to one of the preceding claims, characterized in that at least one of the sub-regions which are difficult to flow around ( 9 ) is designed as a truncated cone and due to the mutual flow direction of the through the flow chamber ( 4 ) mass flow flowing through each cone tip through the flow chamber ( 4 ) facing or facing away from the flowing mass flow. Vorrichtung (100) nach einem der vorhergehenden Ansprüche, dadurch gekennzeichnet, dass der schwer Umströmbahre Teilbereich (9), der von allen Teilbereichen (9) der Ausgangsöffnung/Eingangsöffnung (2), am nächsten liegt, so ausgestaltet ist, dass sein Querschnitt der senkrecht zu der Mittelachse der Durchflusskammer (4) genommen wird, in wechselseitiger Strömungsrichtung des durch die Durchflusskammer (4) hindurchströmenden Massestromes gesehen erst kleiner und dann wieder größer wird.Contraption ( 100 ) according to one of the preceding claims, characterized in that the sub-area which is difficult to flow around ( 9 ) from all areas ( 9 ) the exit opening / entrance opening ( 2 ), is closest so that its cross section is perpendicular to the central axis of the flow chamber ( 4 ) is taken in the reciprocal flow direction of the through the flow chamber ( 4 ) flowing mass flow seen first smaller and then larger again. Vorrichtung (100) nach einem der vorhergehenden Ansprüche, dadurch gekennzeichnet, dass der schwer Umströmbahre Teilbereich (9), der von allen Teilbereichen (9) der Ausgangsöffnung/Eingangsöffnung (2) am nächsten liegt, einen hohlen Endbereich/Anfangsbereich (5) aufweist, der der Ausgangsöffnung/Eingangsöffnung (2) zugewandt ist, wobei der Querschnitt dieses Hohlraums (5), der senkrecht zu der Mittelachse der Durchflusskammer (4) genommen wird, bei Strömungsrichtung von Ausgangsöffnung/Eingangsöffnung (2) nach Ausgangsöffnung/Eingangsöffnung (3) des durch die Durchflusskammer (4) hindurchströmenden Massestromes kleiner wird, sowie bei Umkehrung der Strömungsrichtung des Massestroms größer wird.Contraption ( 100 ) according to one of the preceding claims, characterized in that the sub-area which is difficult to flow around ( 9 ) from all areas ( 9 ) the exit opening / entrance opening ( 2 ) is closest, a hollow end area / start area ( 5 ) which corresponds to the exit opening / entrance opening ( 2 ) facing, the cross section of this cavity ( 5 ) perpendicular to the central axis of the flow chamber ( 4 ) is taken in the direction of flow from the outlet opening / inlet opening ( 2 ) after exit opening / entrance opening ( 3 ) through the flow chamber ( 4 ) mass flow flowing through becomes smaller, as well as larger when the flow direction of the mass flow is reversed. Vorrichtung (100) nach einem der vorhergehenden Ansprüche, dadurch gekennzeichnet, dass jede Querschnittsfläche des hohlen Endbereichs (5), die dessen Symmetrieachse vollständig enthält, eine Randlinie besitzt, die je nach wechselseitiger Strömungsrichtung des durch die Durchflusskammer (4) hindurchströmenden Massestromes gesehen konvex oder konkav verläuft.Contraption ( 100 ) according to one of the preceding claims, characterized in that each cross-sectional area of the hollow end region ( 5 ), which completely contains its axis of symmetry, has an edge line which, depending on the mutual flow direction of the through the flow chamber ( 4 ) mass flow flowing through seen convex or concave. Vorrichtung (100) nach einem der vorhergehenden Ansprüche, dadurch gekennzeichnet, dass der schwer Umströmbahre Körper (8) so angeordnet ist, dass der Scheitelpunkt der Durchflusskammer (4) mindestens eine Ausbuchtung (7) enthält, die in wechselseitiger Strömungsrichtung des durch die Durchflusskammer (4) hindurchströmenden Massestromes direkt hinter oder vor dem schwer Umströmbahren Körper (8) liegt.Contraption ( 100 ) according to one of the preceding claims, characterized in that the body which is difficult to flow around ( 8th ) is arranged so that the apex of the flow chamber ( 4 ) at least one bulge ( 7 ) contains, which is in the mutual flow direction of the through the flow chamber ( 4 ) mass flows flowing directly behind or in front of the body which is difficult to flow around ( 8th ) lies. Vorrichtung (100) nach einem der vorhergehenden Ansprüche, dadurch gekennzeichnet, dass der schwer Umströmbahre Körper (8) einen hindurchgehenden Hohlraum (10) mit einer Einlassöffnung (11) aufweist, die sich an dein Ende des schwer Umströmbahren Körpers (8) befindet, das der Eingangs/Ausgangs-Öffnung (3) des Gehäuses (1) am nächsten liegt, wobei der durch den schwer Umströmbahren Körper (8) hindurchgehende Hohlraum (10) mindestens eine Auslassöffnung (12) aufweist, die Halterung (6) einen hindurchgehenden Hohlraum (13) mit einer Einlassöffnung/(14) und einer Auslassöffnung (15) aufweist, wobei letztere mit der Einlassöffnung (11) des schwer Umströmbahren Körpers (8) verbunden ist; und die Halterung (6) und der schwer Umströmbahre Körper (8) so miteinander verbunden und in dem Gehäuse (1) angeordnet sind , dass über die Einlassöffnung/(14) der Halterung (6) ein Teil des zu vermischenden Massestroms über die mindestens eine Auslassöffnung (12) des schwer Umströmbahren Körpers (8) in die Durchflusskammer (4) eingeführt werden kann.Contraption ( 100 ) according to one of the preceding claims, characterized in that the body which is difficult to flow around ( 8th ) a cavity passing through ( 10 ) with an inlet opening ( 11 ), which is at your end of the body that is difficult to flow around ( 8th ) that the input / output opening ( 3 ) of the housing ( 1 ) is closest, whereby the body that is difficult to flow around ( 8th ) cavity passing through ( 10 ) at least one outlet opening ( 12 ), the bracket ( 6 ) a cavity passing through ( 13 ) with an inlet opening / ( 14 ) and an outlet opening ( 15 ), the latter with the inlet opening ( 11 ) of the heavily circulating body ( 8th ) connected is; and the bracket ( 6 ) and the heavily flowing body ( 8th ) connected to each other and in the housing ( 1 ) are arranged that via the inlet opening / ( 14 ) the bracket ( 6 ) part of the mass flow to be mixed via the at least one outlet opening ( 12 ) of the heavily circulating body ( 8th ) into the flow chamber ( 4 ) can be introduced. Vorrichtung (100) nach einem der vorhergehenden Ansprüche, dadurch gekennzeichnet, dass der durch den schwer Umströmbahren Körper (8) hindurchgehende Hohlraum (10) so ausgestaltet ist, das er eine Auslassöffnung (12) aufweist, die sich an dem Ende des schwer Umströmbahren Körpers (8) befindet, das der Ausgangsöffnung/Eingangsöffnung (2) des Gehäuses (1) am nächsten liegt.Contraption ( 100 ) according to one of the preceding claims, characterized in that the body which is difficult to flow around ( 8th ) cavity passing through ( 10 ) is designed so that it has an outlet opening ( 12 ) which is located at the end of the body which is difficult to flow around ( 8th ) which is the exit opening / entrance opening ( 2 ) of the housing ( 1 ) is closest. Vorrichtung (100) nach einem der vorhergehenden Ansprüche, dadurch gekennzeichnet, dass der durch den schwer Umströmbahren Körper (8) hindurchgehende Hohlraum (10) so ausgestaltet ist, das er mindestens eine Auslassöffnung (16) aufweist, die sich in einem Oberflächenteilbereich des schwer Umströmbahren Körpers (8) befindet, der Innenwand der Durchflusskammer (4) mindestens teilweise zugewandt ist, und die sich zwischen zwei benachbarten schwer Umströmbahren Teilbereichen (9) befindet.Contraption ( 100 ) according to one of the preceding claims, characterized in that the body which is difficult to flow around ( 8th ) cavity passing through ( 10 ) is designed so that it has at least one outlet opening ( 16 ) which is located in a partial surface area of the body which is difficult to flow around ( 8th ), the inner wall of the flow chamber ( 4 ) faces at least partially, and which is located between two neighboring sub-areas that are difficult to flow around ( 9 ) is located. Vorrichtung (100) nach einem der vorhergehenden Ansprüche, dadurch gekennzeichnet, dass der durch den schwer Umströmbahren Körper (8) hindurchgehende Hohlraum so ausgestaltet ist, das er mindestens eine Auslassöffnung (17) auf weist, die sich in einem Oberflächenteilbereich des schwer Umströmbahren Körpers (8) befindet, der Innenwand der Durchflusskammer (4) mindestens teilweise zugewandt ist, und die sich im Bereich eines schwer Umströmbahren Teilbereiches (9) befindet.Contraption ( 100 ) according to one of the preceding claims, characterized in that the body which is difficult to flow around ( 8th ) passing cavity is designed so that it has at least one outlet opening ( 17 ) has, which is in a partial surface area of the body that is difficult to flow around ( 8th ), the inner wall of the flow chamber ( 4 ) faces at least partially, and which is in the area of a sub-area that is difficult to flow around ( 9 ) is located. Vorrichtung (100) nach einem der vorhergehenden Ansprüche, dadurch gekennzeichnet dass zwischen Eingangsöffnung/Ausgangsöffnung (2) und der Durchflusskammer (4) weitere Zuführungskanäle (18) für die Beimischung von Komponenten zum Massestrom vorhanden sind.Contraption ( 100 ) according to one of the previous ones existing claims, characterized in that between the inlet opening / outlet opening ( 2 ) and the flow chamber ( 4 ) further feed channels ( 18 ) are available for admixing components to the mass flow. Vorrichtung (100) nach einein der vorhergehenden Ansprüche, dadurch gekennzeichnet, dass des weiteren eine Einrichtung bereitgestellt ist, um den schwer Umströmbahren Körper (8) und/oder den Massestrom an mindestes einem Ort in oder durch die Durchflusskammer (4) mit Ultraschall zu beaufschlagen.Contraption ( 100 ) according to one of the preceding claims, characterized in that further a device is provided for the body which is difficult to flow around ( 8th ) and / or the mass flow in at least one place in or through the flow chamber ( 4 ) to be subjected to ultrasound. Vorrichtung (100) zum Vermischen der Komponenten eines hindurchströmenden Massestromes, wobei die Komponenten insbesondere fest, flüssig oder gasförmig sein können, mittels einer gegenläufigen Überlagerung von mindestens zwei hydrodynamischen Superkavitationsfeldern, um eine Mischung, insbesondere eine Emulsion oder Suspension, zu erzeugen,Contraption ( 100 ) for mixing the components of a mass flow flowing through, it being possible for the components to be in particular solid, liquid or gaseous, by means of an opposing superposition of at least two hydrodynamic supercavitation fields in order to produce a mixture, in particular an emulsion or suspension, Einrichtung (100) besteht aus mindestens zwei Vorrichtungen (100) nach einem der Ansprüche 1 bis 13 , wobei die Vorrichtungen (100) so angeordnet und ausgestaltet 10 sind, dass ihre Ausgangsöffnung/Eingangsöffnung (2, 3) als Gesamtheit genutzt werden.Facility ( 100 ) consists of at least two devices ( 100 ) according to one of claims 1 to 13, wherein the devices ( 100 ) are arranged and configured 10 such that their exit opening / entry opening ( 2 . 3 ) can be used as a whole.
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WO2006027002A1 (en) * 2004-09-03 2006-03-16 Crenano Gmbh Multi-chamber supercavitation reactor
WO2007020296A1 (en) 2005-08-19 2007-02-22 Wagner, Manfred Cavitation degasifier
EP1780176A1 (en) 2005-10-25 2007-05-02 Wagner, Manfred Disinfection by cavitation
DE102006007634A1 (en) * 2006-02-18 2007-08-30 Erhard Schindler Device for processing the components of a stream comprises a housing with a pre-chamber which has a cross-section running perpendicular to its central axis in the region surrounding a turbulence-producing element
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DE102007011205A1 (en) * 2007-03-06 2008-09-11 RUHR-UNIVERSITäT BOCHUM High pressure homogenizer producing fine dispersion with narrow size distribution, includes bluff body agitation between constriction and flow stabilization channel
DE202010000075U1 (en) 2010-01-22 2010-04-08 Hafkesbrink, Werner Device for the treatment of flow components by means of turbulent flows
US7762715B2 (en) * 2008-10-27 2010-07-27 Cavitation Technologies, Inc. Cavitation generator
US7833421B2 (en) 2005-10-25 2010-11-16 Elmar Huymann Degermination through cavitation
US8042989B2 (en) * 2009-05-12 2011-10-25 Cavitation Technologies, Inc. Multi-stage cavitation device
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US8603198B2 (en) 2008-06-23 2013-12-10 Cavitation Technologies, Inc. Process for producing biodiesel through lower molecular weight alcohol-targeted cavitation
US8715378B2 (en) 2008-09-05 2014-05-06 Turbulent Energy, Llc Fluid composite, device for producing thereof and system of use
US8746965B2 (en) 2007-09-07 2014-06-10 Turbulent Energy, Llc Method of dynamic mixing of fluids
US8844495B2 (en) 2009-08-21 2014-09-30 Tubulent Energy, LLC Engine with integrated mixing technology
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US9126176B2 (en) 2012-05-11 2015-09-08 Caisson Technology Group LLC Bubble implosion reactor cavitation device, subassembly, and methods for utilizing the same
US9144774B2 (en) 2009-09-22 2015-09-29 Turbulent Energy, Llc Fluid mixer with internal vortex
US9310076B2 (en) 2007-09-07 2016-04-12 Turbulent Energy Llc Emulsion, apparatus, system and method for dynamic preparation
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US9708185B2 (en) 2007-09-07 2017-07-18 Turbulent Energy, Llc Device for producing a gaseous fuel composite and system of production thereof
US9944964B2 (en) 2009-06-15 2018-04-17 Cavitation Technologies, Inc. Processes for increasing bioalcohol yield from biomass
US10065158B2 (en) * 2016-08-19 2018-09-04 Arisdyne Systems, Inc. Device with an inlet suction valve and discharge suction valve for homogenizaing a liquid and method of using the same
US10093953B2 (en) 2013-12-09 2018-10-09 Cavitation Technologies, Inc. Processes for extracting carbohydrates from biomass and converting the carbohydrates into biofuels
WO2022263419A1 (en) * 2021-06-15 2022-12-22 Apw Axenic Prim Water Gmbh Device for treating water
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WO2006027002A1 (en) * 2004-09-03 2006-03-16 Crenano Gmbh Multi-chamber supercavitation reactor
EP1749564A3 (en) * 2005-08-05 2007-09-12 Elmar Huymann Cavitation mixer
DE102005037026B4 (en) * 2005-08-05 2010-12-16 Cavitator Systems Gmbh cavitation mixer
WO2007020296A1 (en) 2005-08-19 2007-02-22 Wagner, Manfred Cavitation degasifier
US7833421B2 (en) 2005-10-25 2010-11-16 Elmar Huymann Degermination through cavitation
EP1780176A1 (en) 2005-10-25 2007-05-02 Wagner, Manfred Disinfection by cavitation
DE102006007634A1 (en) * 2006-02-18 2007-08-30 Erhard Schindler Device for processing the components of a stream comprises a housing with a pre-chamber which has a cross-section running perpendicular to its central axis in the region surrounding a turbulence-producing element
DE102006011881A1 (en) * 2006-03-09 2007-09-13 Vortex-Nanofluid Gmbh Mixing apparatus for nano dispersion, from liquid and at least one liquid/solid additive, has closed housing with inner tube to take dispersion by suction in circular rotary recirculation
DE102007011205A1 (en) * 2007-03-06 2008-09-11 RUHR-UNIVERSITäT BOCHUM High pressure homogenizer producing fine dispersion with narrow size distribution, includes bluff body agitation between constriction and flow stabilization channel
US8746965B2 (en) 2007-09-07 2014-06-10 Turbulent Energy, Llc Method of dynamic mixing of fluids
US9310076B2 (en) 2007-09-07 2016-04-12 Turbulent Energy Llc Emulsion, apparatus, system and method for dynamic preparation
US9708185B2 (en) 2007-09-07 2017-07-18 Turbulent Energy, Llc Device for producing a gaseous fuel composite and system of production thereof
US9399200B2 (en) 2007-09-25 2016-07-26 Turbulent Energy, Llc Foaming of liquids
US8871090B2 (en) 2007-09-25 2014-10-28 Turbulent Energy, Llc Foaming of liquids
US8603198B2 (en) 2008-06-23 2013-12-10 Cavitation Technologies, Inc. Process for producing biodiesel through lower molecular weight alcohol-targeted cavitation
US8715378B2 (en) 2008-09-05 2014-05-06 Turbulent Energy, Llc Fluid composite, device for producing thereof and system of use
US7762715B2 (en) * 2008-10-27 2010-07-27 Cavitation Technologies, Inc. Cavitation generator
US8042989B2 (en) * 2009-05-12 2011-10-25 Cavitation Technologies, Inc. Multi-stage cavitation device
US9944964B2 (en) 2009-06-15 2018-04-17 Cavitation Technologies, Inc. Processes for increasing bioalcohol yield from biomass
US9611496B2 (en) 2009-06-15 2017-04-04 Cavitation Technologies, Inc. Processes for extracting carbohydrates from biomass and converting the carbohydrates into biofuels
US9988651B2 (en) 2009-06-15 2018-06-05 Cavitation Technologies, Inc. Processes for increasing bioalcohol yield from biomass
US8844495B2 (en) 2009-08-21 2014-09-30 Tubulent Energy, LLC Engine with integrated mixing technology
US9556822B2 (en) 2009-08-21 2017-01-31 Turbulent Energy Llc Engine with integrated mixing technology
US9144774B2 (en) 2009-09-22 2015-09-29 Turbulent Energy, Llc Fluid mixer with internal vortex
DE202010000075U1 (en) 2010-01-22 2010-04-08 Hafkesbrink, Werner Device for the treatment of flow components by means of turbulent flows
US8981135B2 (en) 2010-06-22 2015-03-17 Cavitation Technologies, Inc. Process for producing biodiesel through lower molecular weight alcohol-targeted cavitation
US9400107B2 (en) 2010-08-18 2016-07-26 Turbulent Energy, Llc Fluid composite, device for producing thereof and system of use
EP2492335A1 (en) * 2011-02-25 2012-08-29 RWE Power AG Method and device for homogenising a mixture of solid fuel in a liquid
US9126176B2 (en) 2012-05-11 2015-09-08 Caisson Technology Group LLC Bubble implosion reactor cavitation device, subassembly, and methods for utilizing the same
US9682356B2 (en) 2012-05-11 2017-06-20 Kcs678 Llc Bubble implosion reactor cavitation device, subassembly, and methods for utilizing the same
US10093953B2 (en) 2013-12-09 2018-10-09 Cavitation Technologies, Inc. Processes for extracting carbohydrates from biomass and converting the carbohydrates into biofuels
EP3189887A1 (en) 2015-12-29 2017-07-12 AVARUS Suisse Holding AG Cavitation reactor for treating flowable substances
EP3187568A1 (en) 2015-12-29 2017-07-05 AVARUS Suisse Holding AG Installation for the treatment of diesel oil
EP3187257A1 (en) 2015-12-29 2017-07-05 AVARUS Suisse Holding AG Cavitation reactor device for treating flowable substances
EP3187256A1 (en) 2015-12-29 2017-07-05 AVARUS Suisse Holding AG Installation for the treatment of crude oil
EP3187467A1 (en) 2015-12-29 2017-07-05 AVARUS Suisse Holding AG Cavitation reactor for treating flowable substances
EP3187253A1 (en) 2015-12-30 2017-07-05 AVARUS Suisse Holding AG Cavitation reactor for treating a flowable substance
US10065158B2 (en) * 2016-08-19 2018-09-04 Arisdyne Systems, Inc. Device with an inlet suction valve and discharge suction valve for homogenizaing a liquid and method of using the same
WO2022263419A1 (en) * 2021-06-15 2022-12-22 Apw Axenic Prim Water Gmbh Device for treating water
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