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DE3325952A1 - Device for producing high-quality solid/liquid mixtures down to a colloidal system - Google Patents

Device for producing high-quality solid/liquid mixtures down to a colloidal system

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Publication number
DE3325952A1
DE3325952A1 DE19833325952 DE3325952A DE3325952A1 DE 3325952 A1 DE3325952 A1 DE 3325952A1 DE 19833325952 DE19833325952 DE 19833325952 DE 3325952 A DE3325952 A DE 3325952A DE 3325952 A1 DE3325952 A1 DE 3325952A1
Authority
DE
Germany
Prior art keywords
inner container
container
outer container
medium
propeller
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
DE19833325952
Other languages
German (de)
Inventor
Wilfried Dipl Ing Hacheney
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from DE19823241011 external-priority patent/DE3241011A1/en
Application filed by Individual filed Critical Individual
Priority to DE19833325952 priority Critical patent/DE3325952A1/en
Priority to EP19840104960 priority patent/EP0134890B1/en
Priority to DE8484104960T priority patent/DE3483190D1/en
Priority to AT84104960T priority patent/ATE56376T1/en
Priority to DK221984A priority patent/DK221984A/en
Priority to US06/607,353 priority patent/US4580904A/en
Priority to CA000453632A priority patent/CA1263377A/en
Publication of DE3325952A1 publication Critical patent/DE3325952A1/en
Withdrawn legal-status Critical Current

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00—Biological treatment of water, waste water, or sewage
    • C02F3/02—Aerobic processes
    • C02F3/12—Activated sludge processes
    • C02F3/20—Activated sludge processes using diffusers
    • C02F3/205—Moving, e.g. rotary, diffusers; Stationary diffusers with moving, e.g. rotary, distributors
    • C02F3/206—Moving, e.g. rotary, diffusers; Stationary diffusers with moving, e.g. rotary, distributors with helical screw impellers
    • 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
    • B01F23/20—Mixing gases with liquids
    • B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/233—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements
    • B01F23/2334—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements provided with stationary guiding means surrounding at least partially the stirrer
    • B01F23/23341—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements provided with stationary guiding means surrounding at least partially the stirrer with tubes surrounding the stirrer
    • 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
    • B01F23/53—Mixing liquids with solids using driven stirrers
    • 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
    • B01F23/56—Mixing liquids with solids by introducing solids in liquids, e.g. dispersing or dissolving
    • 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
    • B01F25/10—Mixing by creating a vortex flow, e.g. by tangential introduction of flow components
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
    • B01F27/86—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis co-operating with deflectors or baffles fixed to the receptacle
    • B01F27/861—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis co-operating with deflectors or baffles fixed to the receptacle the baffles being of cylindrical shape, e.g. a mixing chamber surrounding the stirrer, the baffle being displaced axially to form an interior mixing chamber
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
    • B01F27/91—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with propellers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/50—Mixing receptacles
    • B01F35/514—Mixing receptacles the mixing receptacle or conduit being transparent or comprising transparent parts
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F2101/00—Mixing characterised by the nature of the mixed materials or by the application field
    • B01F2101/28—Mixing cement, mortar, clay, plaster or concrete ingredients
    • 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
    • B01F23/20—Mixing gases with liquids
    • B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/05—Stirrers
    • B01F27/11—Stirrers characterised by the configuration of the stirrers
    • B01F27/15—Stirrers with tubes for guiding the material
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/05—Stirrers
    • B01F27/11—Stirrers characterised by the configuration of the stirrers
    • B01F27/19—Stirrers with two or more mixing elements mounted in sequence on the same axis
    • B01F27/191—Stirrers with two or more mixing elements mounted in sequence on the same axis with similar elements
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F33/00—Other mixers; Mixing plants; Combinations of mixers
    • B01F33/70—Mixers specially adapted for working at sub- or super-atmospheric pressure, e.g. combined with de-foaming
    • 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00—Technologies for wastewater treatment
    • Y02W10/10—Biological treatment of water, waste water, or sewage

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Dispersion Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Microbiology (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Mixers Of The Rotary Stirring Type (AREA)

Abstract

The device has an inner container 1, through which a medium flows in spiral eddies under the action of gravity, is of rotationally symmetrical shape and has a hyperboloid generatrix in the vertical direction. The inner container 1 is provided with a filling orifice 3 and a discharge orifice 4. It is surrounded by a likewise rotationally symmetrical outer container 5 provided with a hyperboloid generatrix. The medium withdrawn from the bottom discharge orifice of the inner container 1 can be transported back by mechanical means through the space bounded by the inner container and outer container to the filling orifice 3 of the inner container 1, so that the medium once more flows through the inner container. The finished product is withdrawn via a line 13, which can be closed by means of an isolation valve 14. A drivable propeller 8 is provided in the inner container 1 and a drivable propeller 11 is provided in the outer container, by means of which additional acceleration forces are applied to the solid/liquid mixture until a colloid or a coagulate has been obtained as end product (Figure). <IMAGE>

Description

Vorrichtung zum Herstellen hochwertiger Feststoff- Device for the production of high quality solid

Flüssigkeits-Gemische bis zum kolloiden System - Zusatz zu P 32 41 011.5 Die Erfindung bezieht sich auf eine Vorrichtung zum Herstellen hochwertiger Feststoff-Fl üssi gkei ts-Gemi sche bis zum kolloiden System oder bis zur Koagulation mit einem vom Medium unter Schwerkrafteinfluß in Spiralwirbeln durchströmten, rotationssymmetrischen, eine hyperbelförmige Mantellinie in vertikaler Richtung aufweisenden, mit einer oberen Füllöffnung und einer unteren Austragöffnung ausgerüsteten Behälter nach Patent ..... Liquid mixtures up to the colloidal system - addition to P 32 41 011.5 The invention relates to a device for producing high quality Solid-liquid mixtures up to the colloidal system or up to coagulation with a rotationally symmetrical, through which the medium flows under the influence of gravity in spiral vortices having a hyperbolic surface line in the vertical direction, with a upper filling opening and a lower discharge opening after equipped container Patent .....

(Patentanmeldung P 32 41 011.5).(Patent application P 32 41 011.5).

Bei der Vorrichtung nach der Hauptanmeldung wird als Antriebsmedium für die Aufspaltung der Partikel der Mischung im wesentlichen die Schwerkraft des Ausgangsgemisches ausgenutzt und diesem Gemisch beim Durchströmen des Behälters eine intensive Wirbelströmung-aufgegeben.In the device according to the main application, the drive medium is for the splitting of the particles of the mixture essentially the force of gravity of the The starting mixture is used and this mixture is used as it flows through the container an intense vortex-abandoned.

Der Erfindung liegt die Aufgabe zugrunde, den Gegenstand der Hauptanmeldung dahingehend weiterzubilden, daß die Einwirkung auf das Ausgangsgemisch intensiviert wird und der kolloidale Zustand oder eine Koagulation in kurzer Zeit erreicht werden kann.The invention is based on the object of the main application to be further developed in such a way that the effect on the starting mixture is intensified and the colloidal state or coagulation can be achieved in a short time can.

Diese Aufgabe wird nach der Erfindung dadurch gelöst, daß der Behälter als Innenbehälter ausgebildet und von einem ebenfalls rotationssymmetrischen, mit einer hyperbelförmigen Mantellinie versehenen Außenbehälter mit Abstand umschlossen ist und das aus der unteren Austragöffnung des Innenbehälters abgezogene Medium durch den vom Innenbehälter und vom Außenbehälter begrenzten Raum durch mechanische Mittel zur Füllöffnung des Innenbehälters transportierbar ist.This object is achieved according to the invention in that the container designed as an inner container and of a likewise rotationally symmetrical, with a hyperbolic surface line provided outer container enclosed at a distance and the medium withdrawn from the lower discharge opening of the inner container by the space delimited by the inner container and the outer container by mechanical means Means can be transported to the filling opening of the inner container.

Bei einer vorteilhaften Ausführungsform der Erfindung sind im unteren Bereich des Innen- und des Außenbehälters die Geschwindigkeit des Mediums im Innen- und Außenbehälter steuernde Saug-, Pump- oder Propellereinrichtungen vorgesehen.In an advantageous embodiment of the invention are in the lower The area of the inner and outer container, the speed of the medium in the inner and suction, pumping or propeller devices controlling outer containers are provided.

Den aufgrund der Schwerkrafteinwirkung auf das Medium und der gewählen Form des Innenbehälters erzeugte Spiralwirbeln werden durch die genannten mechanischen Einrichtungen im Innenbehälter Saugkräfte überlagert, die die Wirbel geschwindigkeiten erhöhen.The one chosen due to the effect of gravity on the medium and the Spiral vortices generated in the shape of the inner container are produced by the aforementioned mechanical Facilities in the inner container superimposed suction forces that the vortex speeds raise.

Mit dem im unteren Bereich des Innenbehälters und im unteren Bereich des Außenbehälters vorgesehenen mechanischen Mitteln ergibt sich eine Vielzahl von Steuerungsmöglichkeiten des den Innenbehälter und den Raum zwischen dem Innen- und dem Außenbehälter durchströmenden Mediums. Durch die Erhöhung der Geschwindigkeit des im Innenbehälter strömenden Mediums, durch die zusätzliche Verwirbelung dieses Mediums wird ein kolloidiertes Feststoff-Flüssigkeits-Gemisch in außerordentlich kurzer Zeit erzielt.With the one in the lower area of the inner container and in the lower area the outer container provided mechanical means results in a variety of Control options of the inner container and the space between the inner and the the medium flowing through the outer container. By increasing the speed of the medium flowing in the inner container, due to the additional turbulence of this Medium becomes a colloid solid-liquid mixture in extraordinary achieved in a short time.

Das Medium kann auch durch Rückführung zur oberen Füllöffnung des Innenbehälters den Innenbehälter wiederholt durchströmen, bis der angestrebte Endzustand des Mediums erreicht ist.The medium can also be fed back to the upper filling opening of the Inner container flow through the inner container repeatedly until the desired Final state of the medium is reached.

MiVdieser Vorrichtung kann eine Koagulation angestrebt werden. Es kann auch eine Entionisierung des Kolloidats erreicht werden, d.h.Coagulation can be aimed for with this device. It deionization of the colloidate can also be achieved, i.e.

das Kolloidat befindet sich im zwischenaggregatlichen Zustand, was wiederum bedeutet, daß der innere kolloidative Zustand weder in den Bereich des festen, flüssigen, ober gasförmigen oder gar in irgendeinen Bereich der Elektrizität behört. Dieses sozusagen zu Voraussetzung für die Umgestaltung der Ausgangsmaterialien nach dem Durchgang durch die Kolloidphase. Diese Umgestaltungen erfolgen von dem Punkt der Kolloidations aus möglicherweise vielfältig. Je nachdem, ob man den organischen oder anorganischen Bereich betrachte.the colloidate is in the inter-aggregate state, what again means that the internal colloidal state is neither within the range of the solid, liquid, or gaseous or even in any area of electricity heard. This, so to speak, becomes a prerequisite for the redesign of the starting materials after passing through the colloid phase. These redesigns are carried out by the Point of colloidation from possibly diverse. Depending on whether you like the organic or consider an inorganic area.

Im organischen Bereich kommt es zu einer vollkommen veränderten Stoffbildung innerhalb der organischen Stoffbildeprozesse. Im anorganischen Bereich kommt man zu den veränderten mechanischen, physikalischen und chemischen Eigenschaften. Die Veränderungen gehen soweit, dass Gefügebildungen und Kristallisierungen und überhaupt die Grundlagen der Konfigurationen gegenüber dem Ausgangsmaterial geändert werden.In the organic area there is a completely different substance formation within the organic fabric formation processes. In the inorganic area one comes to the changed mechanical, physical and chemical properties. the Changes go so far that microstructures and crystallizations and in general the basics of the configurations can be changed compared to the original material.

Ein Ausführungsbeispiel der erfindungsgemäßen Vorrichtung ist in der Zeichnung schematisch dargestellt und wird im folgenden beschrieben.An embodiment of the device according to the invention is in Drawing shown schematically and is described below.

Die Vorrichtung weist einen Innenbehälter 1 auf, der als rotationssymmetrischer Behälter ausgebildet ist und eine hyperbelförmige Mantellinie 2 besitzt. Dieser Innenbehälter weist eine obere Füllöffnung 3 und eine untere Austragöffnung 4 auf. Der Innenbehälter wird von einem Außenbehälter 5 umschlossen, wobei der Abstand zwischen dem Mantel des Innenbehälters und des Außenbehälters über die gesamte Höhe des Innenbehälters umlaufend gleich ist. Der Aussenbehälter 5 ist somit auch als rotationssymmetrischer Körper ausgebildet, der eine hyperbelförmige Mantellinie aufweist. Der Außenbehälter 5 ist ferner mit einem oberen Umlenkteil 6 versehen, das sich über die Höhe der Einfüllöffnung 3 hinaus erstreckt und im Querschnitt bogenförmig gestaltet ist. Der freie Innenraum 7 des Umlenkteils liegt oberhalb der Einfüllöffnung. Durch die bogenförmige Kontur des Umlenkteils 6 wird das im Ringraum zwischen dem Innenbehälter und dem Außenbehälter hochgeförderte Material so umgelenkt, daß ein Abspritzen von der Innenwand des Außenbehälters vermieden und das Material gleichmäßig in die Füllöffnung 3 des Innenbehälters eingebracht wird.The device has an inner container 1, which is designed as a rotationally symmetrical Container is formed and has a hyperbolic surface line 2. This The inner container has an upper filling opening 3 and a lower discharge opening 4. The inner container is enclosed by an outer container 5, the distance between the jacket of the inner container and the outer container over the entire height of the inner container is the same all round. The outer container 5 is thus also as rotationally symmetrical body formed, which has a hyperbolic surface line having. The outer container 5 is also provided with an upper deflection part 6, the extends beyond the height of the filling opening 3 and is designed arched in cross section. The free interior 7 of the deflection part is above the filling opening. Due to the arched contour of the deflection part 6 that is conveyed up in the annular space between the inner container and the outer container Material deflected in such a way that it is prevented from splashing off the inner wall of the outer container and the material is evenly introduced into the filling opening 3 of the inner container will.

Im unteren Bereich des Innenbehälters 2 ist ein Propeller 8 angeordnet, der auf einer Antriebswelle 9 befestigt ist. Diese Propeller wird mittels eines Motors 10 angetrieben. In dem Ausführungsbeispiel ist auf der Antriebswelle 9 ein weiterer Propeller 11 befestigt, dessen Durchmesser wesentlich größer ist als der des Propellers 8 und dessen Flügel einen anderen Anstellwinkel besitzen als die Flügel des Propellers 8. Durch den Propeller 8 wird das in den Innenbehälter 1 eingegebene Feststoff-Flüssigkeits-Gemisch, das den Behälter in Spiralwirbeln durchströmt,nach unten abgesaugt und durch die Austragsöffnung 4 gedrückt. Das Material wird somit Zentripetal-und entrifugalkräften ausgesetzt.A propeller 8 is arranged in the lower area of the inner container 2, which is attached to a drive shaft 9. This propeller is by means of a Motor 10 driven. In the exemplary embodiment, a is on the drive shaft 9 another propeller 11 attached, the diameter of which is much larger than that of the propeller 8 and its blades have a different angle of attack than that The blades of the propeller 8 are introduced into the inner container 1 by the propeller 8 Solid-liquid mixture flowing through the container in spiral eddies Sucked off at the bottom and pushed through the discharge opening 4. The material will thus Subject to centripetal and entrifugal forces.

Die Propeller können auch gegenläufig arbeiten und separate Antriebe aufweisen.The propellers can also work in opposite directions and have separate drives exhibit.

Das bearbeitete Material kann in der Schlußphase nur unter Einwirkung der Zentripetalkräfte durch einfaches Durchlaufen des Innenbehälters nach der Kolloidation stabilisiert werden. Es kann dann so kolloidiert und dynamisiert austreten.The processed material can only be used in the final phase the centripetal forces by simply passing through the inner container after colloidation be stabilized. It can then emerge colloid and dynamized.

Zu diesem Zweck ist ein vom Boden 12 des Außenbehälters 5 ausgehendes Abzugsrohr 13 vorgesehen, in dem benachbart dem Boden 12 ein Absperrschieber 14 angeordnet ist.For this purpose, an outgoing from the bottom 12 of the outer container 5 is Discharge pipe 13 is provided, in which a gate valve 14 is adjacent to the bottom 12 is arranged.

Alle flüssigen Substanzen können in dieser Vorrichtung behandelt werden. Von großer Bedeutung ist ein derartiger Vorgang beispielsweise für die Durchführung von stoffwechselähnlichen Prozessen zum Zwecke erheblicher Qualitätssteigerungen oder Stoffveränderungen in den Bereichen Wasser, Abwasser, Schlämme, Schadstoffe, Mineralien, Blutwäsche, Dialyse u.dgl.All liquid substances can be treated in this device. Such a process is of great importance, for example for the implementation of metabolism-like processes for the purpose of considerable quality increases or material changes in the areas of water, wastewater, sludge, pollutants, Minerals, blood washing, dialysis and the like.

Im Raum zwischen dem Innenbehälter 1 und dem Außenbehälter 5 können Leitschienen oder Bremsschwellen für das strömende Medium angeordnet sein.In the space between the inner container 1 and the outer container 5 can Guard rails or speed bumps can be arranged for the flowing medium.

Bezugszeichen 1 Innenbehälter 2 Mantellinie 3 Füllöffnung 4 Austragöffnung 5 Außenbehälter 6 Umlenkteil 7 Innenraum 8 Propeller 9 Antriebswelle 10 Motor 11 Propeller 12 Boden 13 Abzugsrohr 14 AbsperrschieberReference number 1 inner container 2 surface line 3 filling opening 4 discharge opening 5 outer container 6 deflector 7 interior 8 propeller 9 drive shaft 10 motor 11 Propeller 12 Bottom 13 Flue pipe 14 Gate valve

Claims (6)

Patentansprüche : Iji Vorrichtung zum Herstellen hochwertiger Feststoff-Flüssi gkeits-Gemische bis zum kolloiden System oder bis zur Koagulation mit einem vom Medium unter Schwerkrafteinfluß in Spezialwirbeln durchströmten, rotationssymmetrischen, eine hyperbelförmige Mantellinie in vertikaler Richtung aufweisenden, mit einer oberen Füllöffnung und einer unteren Austragöffnung ausgerüsteten Behälter nach Patent ..... (Patentanmeldung P 32 41 011.5), d a d u r c h g e k e n n z ei c h n e t , daß der Behälter als Innenbehälter (1) ausgebildet und von einem ebenfalls rotationssymmetrischen, mit einer hyperbelförmigen Mantellinie versehenen Außenbehälter (5) umschlossen ist und daß das aus der unteren Austragöffnung des Innenbehälters abgezogene Medium durch den vom Innenbehälter und vom Außenbehälter begrenzten Raum durch mechanische Mittel zur Füllöffnung (3) des Innenbehälters (1) transportierbar ist. Claims: Iji device for producing high quality solid liquids gkeits mixtures up to the colloidal system or up to coagulation with one of the Medium under the influence of gravity in special vortices flowing through, rotationally symmetrical, having a hyperbolic surface line in the vertical direction, with a upper filling opening and a lower discharge opening after equipped container Patent ..... (patent application P 32 41 011.5), d a d u r c h e k e n n n z ei c h n e t that the container is designed as an inner container (1) and also from one rotationally symmetrical outer container with a hyperbolic surface line (5) is enclosed and that from the lower discharge opening of the inner container withdrawn medium through the space delimited by the inner container and the outer container can be transported by mechanical means to the filling opening (3) of the inner container (1) is. 2. Vorrichtung nach Anspruch 1, dadurch gekennzeichnet, daß der Abstand zwischen dem Mantel des Innenbehälters (1) und des Außenbehälters (5) über die gesamte Höhe des Innenbehälters umlaufend gleich ist und der Außenbehälter (5) ein oberes, über die Höhe der Einfüllöffnung (3) des Innenbehälters (1) hinaus sich erstreckendes Umlenkungsteil (6) aufweist. 2. Apparatus according to claim 1, characterized in that the distance between the jacket of the inner container (1) and the outer container (5) over the whole The height of the inner container is the same all round and the outer container (5) has an upper, extending beyond the height of the filling opening (3) of the inner container (1) Has deflection part (6). 3. Vorrichtung nach Anspruch 1, dadurch gekennzeichnet, daß im unteren Bereich des Innen- und des Außenbehälters die Geschwindigkeit des Mediums im Innen- und Außenbehälter steuernde Saug-, Pump- oder Propellereinrichtungen vorgesehen sind. 3. Apparatus according to claim 1, characterized in that in the lower The area of the inner and outer container, the speed of the medium in the inner and suction, pumping or propeller devices controlling outer containers are provided are. 4. Vorrichtung nach Anspruch 3, dadurch gekennzeichnet, daß sowohl im unteren Bereich des Innenbehälters (1) als auch im unteren Bereich des Außenbehälters (5) je ein antreibbarer Propeller (8, 11) vorgesehen sind, durch die das Medium aus dem Innenbehälter gefördert und durch den Außenbehälter zurück in die Füllöffnung (3) des Innenbehälters (1) transportiert wird.4. Apparatus according to claim 3, characterized in that both in the lower area of the inner container (1) and in the lower area of the outer container (5) each a drivable propeller (8, 11) are provided through which the medium conveyed out of the inner container and through the outer container back into the filling opening (3) of the inner container (1) is transported. 5. Vorrichtung nach Anspruch 4, dadurch gekennzeichnet, daß die Propellerflügel unterschiedliche Anstellwinkel haben und auf einer gemeinsamen vertikalen Antriebswelle (9) angeordnet sind undduenrtere im Außenbehälter vorgesehene Propeller (11) einen größeren Durchmesser aufweist als der Propeller (8) des Innenbehälters (1).5. Apparatus according to claim 4, characterized in that the propeller blades have different angles of attack and on a common vertical drive shaft (9) are arranged undduenrtere propellers (11) provided in the outer container Has a larger diameter than the propeller (8) of the inner container (1). 6. Vorrichtung nach einem der vorhergehenden Ansprüche, dadurch gekennzeichnet, daß im Raum zwischen dem Innenbehälter (1) und dem Außenbehälter (5) Leitschienen oder Bremsschwellen angeordnet sind.6. Device according to one of the preceding claims, characterized in that that in the space between the inner container (1) and the outer container (5) guide rails or speed bumps are arranged.
DE19833325952 1982-11-06 1983-07-19 Device for producing high-quality solid/liquid mixtures down to a colloidal system Withdrawn DE3325952A1 (en)

Priority Applications (7)

Application Number Priority Date Filing Date Title
DE19833325952 DE3325952A1 (en) 1982-11-06 1983-07-19 Device for producing high-quality solid/liquid mixtures down to a colloidal system
EP19840104960 EP0134890B1 (en) 1983-07-19 1984-05-03 Device for the preparation of high quality solid-liquid mixtures up to the colloid system or up to coagulation for the treatment of water or to introduce gases into liquids
DE8484104960T DE3483190D1 (en) 1983-07-19 1984-05-03 DEVICE FOR PRODUCING HIGH-QUALITY SOLID-LIQUID MIXTURES TO THE COLLOID SYSTEM OR TO THE COAGULATION, FOR WATER TREATMENT OR FOR INGATING GASES IN LIQUIDS.
AT84104960T ATE56376T1 (en) 1983-07-19 1984-05-03 DEVICE FOR THE PRODUCTION OF HIGH-QUALITY SOLID-LIQUID MIXTURES UP TO THE COLLOID SYSTEM OR UP TO THE COAGULATION, FOR WATER TREATMENT OR FOR INTRODUCING GASES IN LIQUIDS.
DK221984A DK221984A (en) 1983-07-19 1984-05-04 Apparatus for the preparation of a colloidal system
US06/607,353 US4580904A (en) 1983-07-19 1984-05-04 Device for obtaining high-quality mixtures of solids and liquids extending to the colloidal system or to coagulation intended for treating water or for introducing gases into liquids
CA000453632A CA1263377A (en) 1983-07-19 1984-05-04 Vortex-draft-tube mixer for solids and liquids

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE19823241011 DE3241011A1 (en) 1982-11-06 1982-11-06 Equipment and process for producing high-quality solids/liquid mixtures up to a colloidal system, for water treatment or for introducing gases into liquids
DE19833325952 DE3325952A1 (en) 1982-11-06 1983-07-19 Device for producing high-quality solid/liquid mixtures down to a colloidal system

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DE3325952A1 true DE3325952A1 (en) 1985-01-31

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Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0188737A3 (en) * 1985-01-23 1987-09-16 Röben Kolloid Entwicklung GmbH &amp; Co. KG Apparatus for the preparation of colloids from fluids
DE3827659A1 (en) * 1988-08-16 1990-03-15 Gabor Klaus Dieter Dipl Ing METHOD FOR THE PHYSICAL PROCESSING OF MEDIA - LIQUID TO THIN-WIDTH CONSISTENCY - FOR CHANGING THE BASIC PHYSICAL PROPERTIES AND PROCESSING DEVICE FOR IMPLEMENTING THE PROCESS
DE4220595A1 (en) * 1992-06-24 1994-01-05 Premonex Consulting Ltd Solid-liquid mixing appts. - has a waisted section at inner and outer containers for effective mixture of organic solids
AT407495B (en) * 1999-04-23 2001-03-26 Filz Friedrich Device for treating a liquid
EP2420314A3 (en) * 2007-02-16 2012-09-19 Brunob Ii B.V. Apparatus for and method for mixing small samples of material
WO2012168093A1 (en) 2011-06-10 2012-12-13 Vortex Power Gmbh Whirl device
DE102016013071A1 (en) * 2016-06-28 2017-12-28 Hans-Joachim Boltersdorf Device for treating material with a container

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0188737A3 (en) * 1985-01-23 1987-09-16 Röben Kolloid Entwicklung GmbH &amp; Co. KG Apparatus for the preparation of colloids from fluids
DE3827659A1 (en) * 1988-08-16 1990-03-15 Gabor Klaus Dieter Dipl Ing METHOD FOR THE PHYSICAL PROCESSING OF MEDIA - LIQUID TO THIN-WIDTH CONSISTENCY - FOR CHANGING THE BASIC PHYSICAL PROPERTIES AND PROCESSING DEVICE FOR IMPLEMENTING THE PROCESS
US5292194A (en) * 1988-08-16 1994-03-08 Dieter Gabor Device for preparing liquid to thin pulpy media
DE4220595A1 (en) * 1992-06-24 1994-01-05 Premonex Consulting Ltd Solid-liquid mixing appts. - has a waisted section at inner and outer containers for effective mixture of organic solids
AT407495B (en) * 1999-04-23 2001-03-26 Filz Friedrich Device for treating a liquid
EP2420314A3 (en) * 2007-02-16 2012-09-19 Brunob Ii B.V. Apparatus for and method for mixing small samples of material
WO2012168093A1 (en) 2011-06-10 2012-12-13 Vortex Power Gmbh Whirl device
DE102016013071A1 (en) * 2016-06-28 2017-12-28 Hans-Joachim Boltersdorf Device for treating material with a container

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