DE29903708U1 - Venturi cyclone aerator - Google Patents
Venturi cyclone aeratorInfo
- Publication number
- DE29903708U1 DE29903708U1 DE29903708U DE29903708U DE29903708U1 DE 29903708 U1 DE29903708 U1 DE 29903708U1 DE 29903708 U DE29903708 U DE 29903708U DE 29903708 U DE29903708 U DE 29903708U DE 29903708 U1 DE29903708 U1 DE 29903708U1
- Authority
- DE
- Germany
- Prior art keywords
- venturi
- liquid
- phases
- nozzle
- venturi cyclone
- 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.)
- Expired - Lifetime
Links
- 238000005276 aerator Methods 0.000 title claims 2
- 239000007788 liquid Substances 0.000 claims description 10
- 238000009423 ventilation Methods 0.000 claims description 2
- 238000002347 injection Methods 0.000 claims 1
- 239000007924 injection Substances 0.000 claims 1
- 230000006641 stabilisation Effects 0.000 claims 1
- 238000011105 stabilization Methods 0.000 claims 1
- 230000000694 effects Effects 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000003380 propellant Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C9/00—Combinations with other devices, e.g. fans, expansion chambers, diffusors, water locks
-
- 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
- B01F33/80—Mixing plants; Combinations of mixers
- B01F33/82—Combinations of dissimilar mixers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C5/00—Apparatus in which the axial direction of the vortex is reversed
- B04C5/02—Construction of inlets by which the vortex flow is generated, e.g. tangential admission, the fluid flow being forced to follow a downward path by spirally wound bulkheads, or with slightly downwardly-directed tangential admission
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physics & Mathematics (AREA)
- Fluid Mechanics (AREA)
- Cyclones (AREA)
Description
Kegelschleuder mit Venturi-Einlaufsystem zur intensiven Vermischung zweier Phasen (flüssig-gasförmig)Cone centrifuge with Venturi inlet system for intensive mixing of two phases (liquid-gaseous)
Bekanntlich läßt sich mit Hilfe des Venturi-Effektes bei schnell stromerndem Treibmittel (Flüssigkeit) und entsprechend abgestimmter Düsenöffnung ein Unterdruck erzeugen und z.B. Gas (Luft) ansaugen. Der Flüssigkeitsdruck und die Düsenöffnung bestimmen die dabei mitgerissene Luftmenge. Die Vermischung beider Phasen ist nur unzureichend. It is well known that with the help of the Venturi effect, a low pressure can be generated with a rapidly flowing propellant (liquid) and a correspondingly adjusted nozzle opening, and gas (air) can be sucked in, for example. The liquid pressure and the nozzle opening determine the amount of air entrained . The mixing of the two phases is inadequate.
Bei vielen Applikationen ist es aber wünschenswert, eine möglichst intensive Vermischung von Flüssigkeit und Gas zu bewerkstelligen und diesen Zustand möglichst lange stabil zu halten.However, in many applications it is desirable to achieve the most intensive mixing of liquid and gas possible and to keep this state stable for as long as possible.
Der Erfindung liegt der Lösungsansatz zugrunde, mit einem nachgeschaltetem Rotationskörper
beide Phasen in hohe Rotation zu versetzen. Dabei wird der Partialdruck in der
Drehachse gesenkt. Das Lösungsvermögen von Gas in der Flüssikeit wird erhöht und durch
intensive Verwirbelung relativ lange stabil gehalten.
Dies ist zum Beispiel bei Belüftungsvorgängen von entscheidender Bedeutung.The invention is based on the solution approach of setting both phases into high rotation using a downstream rotating body . This reduces the partial pressure in the axis of rotation. The dissolving capacity of gas in the liquid is increased and kept stable for a relatively long time by intensive turbulence.
This is crucial, for example, in ventilation processes .
Vorteile:Advantages:
* Intensive Vermischung von beiden Phasen* Intensive mixing of both phases
* Bessere Anreicherung* Better enrichment
* Längerer stabiler Zustand* Longer stable state
* Gleichzeitige Separatation spez. schwererer Anteile mit Hilfe der Zentrifugalkraft* Simultaneous separation of heavier particles using centrifugal force
Das System besteht aus zwei Baugruppen:The system consists of two components:
a) Venturi - Einlaufsystema) Venturi inlet system
b) Kegelschleuder (Zyklon)b) Cone centrifuge (cyclone)
Das Einlaufsystem (1) ist konstruktiv so gestaltet, daß das Treibmittel (Flüssigkeit) über
eine Venturidüse (2) bei hoher Strömungsgeschwindigkeit Luft über einen separaten Kanal
(3) ansaugt.The inlet system (1) is designed in such a way that the propellant (liquid) flows
a Venturi nozzle (2) at high flow velocity air via a separate channel
(3) sucks in.
Beide Phasen werden nun einem kegelförmigen Rotationskörper (4) tangential zugeführt und *...·' auf Grund der Kegelgeometrie beschleunigt. Die spez. schwerere Phase (Flüssigkeit) wird i ·* ·Both phases are now fed tangentially to a conical rotating body (4) and accelerated due to the conical geometry. The specifically heavier phase (liquid) is i ·* ·
mit zunehmend schnellerer Drehung an die Kegelwand gedrückt, die leichte Phase (Luft) * · · *pressed against the cone wall with increasingly faster rotation, the light phase (air) * · · *
ist gezwungen die Flüssigkeit zu durchdringen (Mischeffekt) und in die Rotationsachse zu .. t is forced to penetrate the liquid (mixing effect) and into the axis of rotation .. t
wandern. Aufgrund konstruktiver Maßnahmen wird durch hohe Fliehkräfte ein Unterdruck *.!..* in der Drehachse erzeugt. Das Lösungsvermögen von Gas in der Flüssigkeit wird erhöht und bei . .*' · gleichzeitiger intensiven Verwirbelung eine intensive mechanische Vermischung mit ' · · · ·migrate. Due to design measures, a negative pressure *.!..* is generated in the axis of rotation by high centrifugal forces. The dissolving power of gas in the liquid is increased and, with simultaneous intensive turbulence, intensive mechanical mixing with ' · · · ·
ausgezeichneter Stabilität erzeugt.with excellent stability.
Über die Rejektdüse (5) lassen sich schwerere Bestandteile ausschleusen. Damit das System
überhaupt arbeitet, müssen die Eintrittsöffnung bei der Zuführung und die Austrittsöffnung der
Rejektdüse in einem bestimmten,direkten Verhältnis stehen.
Das Gemisch verläßt über das Tauchrohr (6) das SystemHeavier components can be removed via the reject nozzle (5). In order for the system
works at all, the inlet opening at the feed and the outlet opening of the
Reject nozzle in a certain, direct relationship .
The mixture leaves the system via the dip tube (6)
1 Einlaufsystem 2 Venturidüse1 Inlet system 2 Venturi nozzle
3 Ansaugkanal :****"3 Intake channel :****"
4 Rotationskörper ·**:*:4 rotation bodies ·**:*:
5 Rejektöffhung5 Reject opening
6 Gemisch-Ausgang6 Mixture output
Claims (2)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE29903708U DE29903708U1 (en) | 1999-03-02 | 1999-03-02 | Venturi cyclone aerator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE29903708U DE29903708U1 (en) | 1999-03-02 | 1999-03-02 | Venturi cyclone aerator |
Publications (1)
Publication Number | Publication Date |
---|---|
DE29903708U1 true DE29903708U1 (en) | 1999-07-01 |
Family
ID=8070162
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DE29903708U Expired - Lifetime DE29903708U1 (en) | 1999-03-02 | 1999-03-02 | Venturi cyclone aerator |
Country Status (1)
Country | Link |
---|---|
DE (1) | DE29903708U1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20120006357A1 (en) * | 2010-07-12 | 2012-01-12 | Paprima Industries Inc. | Drain apparatus for a dry strainer cleaning head |
-
1999
- 1999-03-02 DE DE29903708U patent/DE29903708U1/en not_active Expired - Lifetime
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20120006357A1 (en) * | 2010-07-12 | 2012-01-12 | Paprima Industries Inc. | Drain apparatus for a dry strainer cleaning head |
US9044782B2 (en) * | 2010-07-12 | 2015-06-02 | Paprima Industries Inc. | Drain apparatus for a dry strainer cleaning head |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
DE68917990T2 (en) | Vortex tube separator. | |
DE2328220C2 (en) | Device for generating a vortex flow | |
US4711720A (en) | Tangentially staged hydrocyclones | |
DE60012558D1 (en) | DEVICE AND METHOD FOR PRODUCING CRYSTALLINE PARTICLES | |
DE1245267B (en) | Centrifugal dust separator with a cyclone and a fine dust secondary separator in the form of a rotary flow vortex | |
EP0400431A2 (en) | Separation unit | |
DE29903708U1 (en) | Venturi cyclone aerator | |
DE679138C (en) | Centrifugal dust separator | |
US3998612A (en) | Annular venturi gas scrubber | |
Mayinger et al. | Operating results and aerosol deposition of a venturi scrubber in self-priming operation | |
DE3715157C2 (en) | ||
DE19916307C2 (en) | Device for the separation of the particle size spectrum of a polydisperse aerosol and its use | |
DE102016004497A1 (en) | Separating device and arrangement for cleaning an intake air of an internal combustion engine | |
DE10217967C1 (en) | Filtering device used for filtering fluids has circulating channel provided around peripheral edge of membrane with its inlet connected to gap and its outlet connected to return channel | |
WO2019186430A2 (en) | A scrubber | |
DE1921785B2 (en) | Dust removal device, especially for underground mining | |
DE1915893C3 (en) | Dedusting device, especially for underground mining | |
DE60210376T2 (en) | Device for dividing a two-phase flow into several partial flows with the same liquid / gas ratio | |
AT254156B (en) | Device for the separation of media of different inertia | |
DD226779A1 (en) | METHOD AND DEVICE FOR DUST SEPARATION FROM A LAMINARY GASSTROM | |
DE830189C (en) | Process for the separation or concentration of the constituents of mixtures of substances or their isotopes by centrifugal force | |
DE2416583A1 (en) | PROCESS FOR SEPARATING SOLID PARTICLES FROM GASES AND DEVICE FOR CARRYING OUT THE PROCESS | |
DE2431876B2 (en) | Method for separating liquids from a gas flow under the action of centrifugal force within a swirl flow and a device for carrying out this method | |
DE102015106663A1 (en) | cyclone | |
AT391426B (en) | Method and device for separating off substances from a flowing medium |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
R207 | Utility model specification |
Effective date: 19990812 |
|
R156 | Lapse of ip right after 3 years |
Effective date: 20021001 |