EP2440315A1 - Stirring device - Google Patents
Stirring deviceInfo
- Publication number
- EP2440315A1 EP2440315A1 EP10734666A EP10734666A EP2440315A1 EP 2440315 A1 EP2440315 A1 EP 2440315A1 EP 10734666 A EP10734666 A EP 10734666A EP 10734666 A EP10734666 A EP 10734666A EP 2440315 A1 EP2440315 A1 EP 2440315A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- stirring
- rotating
- gas
- outlet
- blades
- 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.)
- Granted
Links
- 238000003756 stirring Methods 0.000 title claims abstract description 116
- 239000007788 liquid Substances 0.000 claims description 10
- 230000002706 hydrostatic effect Effects 0.000 claims description 3
- 238000002309 gasification Methods 0.000 abstract description 4
- 210000000056 organ Anatomy 0.000 abstract 7
- 239000012530 fluid Substances 0.000 abstract 1
- 238000013461 design Methods 0.000 description 10
- 230000007704 transition Effects 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 5
- 238000013019 agitation Methods 0.000 description 3
- 238000010276 construction Methods 0.000 description 3
- 230000002349 favourable effect Effects 0.000 description 3
- 239000006185 dispersion Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 230000010355 oscillation Effects 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- 238000012549 training Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
Classifications
-
- 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
-
- 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
- B01F23/2331—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements characterised by the introduction of the gas along the axis of the stirrer or along the stirrer elements
-
- 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
- B01F27/111—Centrifugal stirrers, i.e. stirrers with radial outlets; Stirrers of the turbine type, e.g. with means to guide the flow
-
- 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
- B01F35/71—Feed mechanisms
-
- 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
- B01F35/30—Driving arrangements; Transmissions; Couplings; Brakes
- B01F2035/35—Use of other general mechanical engineering elements in mixing devices
- B01F2035/351—Sealings
-
- 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
- B01F23/2331—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements characterised by the introduction of the gas along the axis of the stirrer or along the stirrer elements
- B01F23/23311—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements characterised by the introduction of the gas along the axis of the stirrer or along the stirrer elements through a hollow stirrer axis
-
- 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
- B01F23/2331—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements characterised by the introduction of the gas along the axis of the stirrer or along the stirrer elements
- B01F23/23316—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements characterised by the introduction of the gas along the axis of the stirrer or along the stirrer elements through a separate hollow guide substantially parallel with the stirrer element
Definitions
- the invention relates to a stirring arrangement with a rotating stirrer for stirring liquids, which has attached to a Rhackorgannabe stirring blades. Furthermore, the stirring arrangement comprises a gassing device, which supplies a gas, such as air, for dispersing by means of the stirring element.
- a gas such as air
- reaction taking place in many chemical reactors or bioreactors which contain a stirring arrangement
- reactions take place in which at least one reaction partner is available as gaseous starting component.
- the agitating device is intended to finely divide the gaseous component thereby providing a large interface between the gaseous component or the liquid in such a way that the gaseous component at least partially or completely dissolves and participates in the reaction taking place in the reactor.
- the task of dispersing gas usually occurs in practice with other primary tasks, such as the mixing of liquid streams of different toughness, with which further reactants are fed, the suspending of solids, the heat transfer to heat exchange elements, the circulation of the liquid to the surface for evaporation of solvents, precipitation and crystallization of solids etc ..
- WO 2008/083673 A2 discloses a stirring arrangement with a stirrer and a gassing device of the type mentioned in the introduction. This gassing device supplies gas below or laterally of the agitator and this gas is dispersed by means of the agitator. In this design of the stirring arrangement, the gas delivery and distribution takes place either laterally and / or below the stirring element in a relatively large distance thereof.
- EP 0 847 709 A1 discloses a stirring element which is used in particular as a gasification stirring element for stirring liquids.
- the liquids a gas, for example air, fed.
- a gas supply via a feed pipe whose mouth is below the stirring axis of the stirrer takes place.
- a plurality of supply pipes may be provided below and / or laterally spaced from the stirring element. The gas is supplied to the outflow of the stirring element of the stirring arrangement via these tubes.
- EP 1 055 450 B1 shows an agitator in which a gas is supplied via co-rotating distributor elements.
- a gas supply can be done via stationary installed feeds, such as pipes below the stirrer or Rohrer side next to the stirrer or an annular gas distributor, a so-called ring shower, which is arranged below the agitator.
- a ring shower has distributed over the circumference a plurality of openings through which the agitator to be supplied gas can escape.
- a gas supply can also take place via co-rotating distributor elements, as is the case with the agitator described in EP 1 055 450 B1.
- the rotating distributor elements for gassing are arranged outside of the actual agitator, so that optimal gassing can no longer take place.
- gassing devices comprise a plurality of individual and separate components, which rigid mounts must be assigned to avoid flow-induced vibrations. If necessary, high-grade material, duplex steels, alloys or titanium must be used for reasons of corrosion. Overall, therefore, the previous gassing facilities are complex, include several items and therefore are complex in terms of construction and costly.
- the invention aims to provide a structurally simple as possible gas supply to the stirring element of a stirring arrangement while achieving a significant cost savings, and also to achieve a targeted gas delivery in any desired fluidically desired location of the stirring element or the stirring blades.
- an optimal dispersion of Gas can be achieved without affecting the fulfillment of a primary task of the stirring arrangement.
- a stirring arrangement with a rotating stirrer for stirring liquids which comprises attached to a Rrockorgannabe stirring blades, and with a gassing device which supplies a gas, such as air, for dispersing mitteis of, stirring member provided;
- the gassing comprises a with the hub of Rchanorangs rotating distributor bushing with an interior for receiving gas, which communicates with co-rotating outlet lines in communicating connection.
- the invention is characterized in that outlet openings of the outlet ducts are arranged in the immediate vicinity of the stirring blades and within the volume swept by the stirring member or in the immediate outflow zones and deliver the gas at respectively desired locations with the respective desired flow direction.
- co-rotating outlet lines are provided with outlet openings arranged in the immediate vicinity of the stirring blades, so that their storage and mounting is simplified. These outlet lines also allow the gas to be discharged in a targeted manner at any location of the stirring element or the stirring blade that is favorable for flow mechanics.
- the gas is passed from the distribution box to the respective desired outlet openings.
- the gassing device preferably comprises a stationary supply line, which is sealed in communicating connection with the inner raum of the rotating distribution socket is.
- a supply of the gaseous component to the stirring element via a single central supply line, whereby one obtains a substantially simplified construction of a stirring arrangement comprising an agitation system and a gassing device.
- the stationary central supply line communicates in a sealed manner with the interior of a central distribution manifold rotating with the hub of the stirring element.
- the rotating distribution box is arranged coaxially and below the Rlickorgannabe. This provides a space-saving arrangement and training of a rotating distributor body.
- the gas supply points which are formed by the outlet openings of the outlet lines, are within the volume swept by the stirring element.
- the outlet lines allow a free choice of the optimum points of gas release in the immediate vicinity of the stirring blades. Both the outflow direction of the supplied gas and the outflow point can be selected in an optimal manner, taking into account the respective design of the stirring element.
- the exhaust ducts exiting the manifold may be separate from the stirrer blades and their orifices may be above the blade height or perimeter.
- the mouth openings or outlets of the outlet lines may be in the area of the agitator blades, and such design forms are also possible in which these port openings lie between the agitator blades.
- the outlet lines can be integrated into the stirring blades of the stirring element.
- transition from the stationary supply line and the distributor tube rotating with the stirring element, with the interior of which the outlet lines are in communicating connection are to be designed such that the amount of loss at the transition from stationary to rotating part is as low as possible and thus a reliable seal at the transition region he follows.
- a hydrostatic closure may be provided at this transition region, or it may be provided a substantial wear-free, axial or radial gap arrangement, which carries out the desired sealing.
- a single central gas supply is provided, which is fixed, and which cooperates with a rotating distribution box whose interior forms a gas receiving space. From this central, co-rotating manifold then the outlet pipes which co-rotate, fed, and these co-rotating outlet with outlet ports in close proximity to the stirring blades and within swept by the stirring or volume in the immediate Ausströmzonen can then optimize the stirring assembly to the respective best Make the supply gas and give this emitted gas stream also a desired flow direction to improve the reaction participation of the gas.
- Figure 1 is a schematic side view of a stirring arrangement with a stirrer and a gassing device according to the invention.
- FIG. 2 shows a schematic side view of a stirring arrangement with a stirring element and a gassing device according to an embodiment variant according to the invention.
- FIG. 1 shows a first embodiment of a stirring arrangement, designated overall by 1.
- This stirring arrangement 1 has a rotating stirring element 2, which is intended for stirring liquids.
- the stirring element 2 comprises a stirring or supply hub 3, to which stirring blades 4 are attached.
- the stirring blades 4 may be of any desired shape and design.
- the stirring arrangement 1 comprises a gassing device, generally designated 5, which supplies a gas, such as air, for dispersing by means of the stirring element 2.
- the gassing device 5 comprises a distributor bushing 6 which rotates with the agitator intake hub 3 of the agitation system 2.
- This distributor bushing 6 encloses an interior which serves for receiving gas.
- the distributor bushing 6 or the interior thereof is in communicating connection with co-rotating outlet lines 7, which discharge the gas at respectively desired locations with a respective desired flow direction.
- the gassing device 5 comprises a stationary supply line 8 which is sealed in communicating connection with the interior of the rotating distribution box 6.
- the co-rotating outlet lines 7 are formed separately to the stirring blades 4.
- a single, central, stationary supply line 8 is provided for a gas to be supplied.
- the distribution box 6 is arranged coaxially and below the Rrockorgannabe 3, which has the interior for gas absorption.
- the stationary supply line 8 and the rotating distribution box 6 communicate with each other in a sealed manner in communication.
- the design is chosen such that the amount of loss at the seal of the transition from stationary supply line 8 and rotating distributor bushing 6 is as small as possible.
- a hydrostatic closure can be provided at this transition region, or the tight connection of fixed supply line 8 and rotating distribution sleeve 6 by means of a wear-free, axial or radial gap arrangement.
- the gas introduced via the fixed feed line 8 into the interior of the rotating distributor bushing 6 is released in a design of the stirring arrangement 1 via the co-rotating outlet lines 7 of the gassing device 5 at a respectively desired, suitable location, the feed points within the volume swept by the stirring element 2 lie.
- the gas can be discharged and discharged at the mouth openings of the co-rotating outlet lines 7 with a respective desired flow direction.
- These mouth openings of the outlet lines 7 may be in the region of the stirring blades 4, or they may also be arranged between them. However, they are always arranged in the immediate vicinity of the stirring blades and within the volume swept by the stirring element.
- These mouth openings of the outlet lines 7 can also be above or below the vertical extent of the stirring blades 4.
- the most favorable locations for the outlet openings of the outlet lines 7 and the most favorable outlet directions can be optimally selected. Due to the compact design of the Gasing device 5 can save in particular assembly costs and / or material costs and reduce. Furthermore, since the outlet lines 7 rotate with one another, the rigid holders for the outlet lines can be omitted without replacement in order to avoid flow-induced oscillations.
- the stirring assembly 1 according to the invention is due to their inventive design relatively inexpensive and associated with much reduced design effort.
- the stirrer 2 of the stirrer assembly 1 according to the invention can therefore finely divided the supplied gas in a very efficient manner, so that optimum reaction conditions of gas and liquid can be realized in a reactor.
- FIG. 2 shows examples of alternatives of the embodiments of the outlet ducts 7 as well as the orientations and the arrangements of the mouth openings thereof. Also, there is an example indicated in which the outlet 7 is integrated into the associated stirring blade 4. All further details of the stirring arrangement 1 'according to FIG. 2 correspond to the details of the stirring arrangement 1 according to FIG. A more detailed explanation is therefore unnecessary.
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
- Accessories For Mixers (AREA)
- Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
Abstract
Description
Claims
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102009024176 | 2009-06-08 | ||
DE102010004206A DE102010004206A1 (en) | 2009-06-08 | 2010-01-08 | Rühranrodnung |
PCT/EP2010/003410 WO2010142406A1 (en) | 2009-06-08 | 2010-06-07 | Stirring device |
Publications (2)
Publication Number | Publication Date |
---|---|
EP2440315A1 true EP2440315A1 (en) | 2012-04-18 |
EP2440315B1 EP2440315B1 (en) | 2014-03-05 |
Family
ID=43049432
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP10734666.0A Active EP2440315B1 (en) | 2009-06-08 | 2010-06-07 | Stirring device |
Country Status (12)
Country | Link |
---|---|
US (1) | US8894047B2 (en) |
EP (1) | EP2440315B1 (en) |
JP (1) | JP2012529363A (en) |
KR (1) | KR20120012977A (en) |
AU (1) | AU2010257782B2 (en) |
BR (1) | BRPI1010845A2 (en) |
CA (1) | CA2764466C (en) |
CL (1) | CL2011003088A1 (en) |
DE (1) | DE102010004206A1 (en) |
ES (1) | ES2458923T3 (en) |
RU (1) | RU2542258C2 (en) |
WO (1) | WO2010142406A1 (en) |
Family Cites Families (43)
Publication number | Priority date | Publication date | Assignee | Title |
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US1073878A (en) * | 1912-01-20 | 1913-09-23 | Walter E Trent | Agitating and mixing apparatus. |
US1180170A (en) * | 1914-06-13 | 1916-04-18 | William James Rolfe | Rotary lawn-sprinkler. |
US1214113A (en) * | 1916-03-08 | 1917-01-30 | James A Anderson | Tank for treating garbage. |
NL20637C (en) * | 1925-12-26 | |||
US2288063A (en) * | 1940-10-28 | 1942-06-30 | Jr George W Ashlock | Drink mixing device |
US2559518A (en) * | 1948-03-26 | 1951-07-03 | Standard Oil Dev Co | Recirculating tank mixing system |
US2652228A (en) * | 1950-01-11 | 1953-09-15 | Carrier Corp | Bearing construction |
US2592904A (en) * | 1950-04-10 | 1952-04-15 | Chiksan Co | Hydraulic agitator |
US2983452A (en) * | 1958-06-12 | 1961-05-09 | Virgual T Lindbloom | Rotary sprayer |
DE1083771B (en) * | 1958-08-08 | 1960-06-23 | Hefefabrik Weingarten G M B H | Device for intensive aeration and gassing of liquids |
US3227547A (en) * | 1961-11-24 | 1966-01-04 | Union Carbide Corp | Degassing molten metals |
JPS52108370A (en) * | 1976-03-10 | 1977-09-10 | Tatsuya Arai | Apparatus of gassliquid contact reaction without gas compresser |
FR2402472A1 (en) * | 1977-09-13 | 1979-04-06 | Alsthom Atlantique | APPARATUS FOR HOLDING SOLID PRODUCTS IN SUSPENSION AND METHOD OF USE |
US4184775A (en) * | 1977-10-05 | 1980-01-22 | Nobuo Akizawa | Apparatus for washing cereals |
NL7803906A (en) | 1978-04-12 | 1979-10-16 | Noordvos Schroeven Bv | METHOD, DEVICE AND PROPELLER FOR DISTRIBUTING A GAS, POWDER OR LIQUID MATERIAL IN A LIQUID. |
JPS5541802A (en) * | 1978-09-18 | 1980-03-24 | Hitachi Ltd | Rotary atomizer |
JPS5541836A (en) * | 1978-09-20 | 1980-03-24 | Hitachi Ltd | Liquid gas contact equipment having agitator blade |
CH645280A5 (en) | 1979-06-01 | 1984-09-28 | Chemap Ag | DEVICE FOR GASING A LIQUID. |
US4688945A (en) * | 1985-10-02 | 1987-08-25 | Stranco, Inc. | Mixing apparatus |
FI885526A (en) * | 1988-11-29 | 1990-05-30 | Outokumpu Oy | REAKTOR FOER BEHANDLING AV ORGANISKT AVFALL. |
JP2706322B2 (en) * | 1989-07-17 | 1998-01-28 | 三菱重工業株式会社 | Gas-liquid contact device |
US5061080A (en) * | 1990-11-21 | 1991-10-29 | Roberts Filter Manufacturing Company | Rotary agitator |
DE9201820U1 (en) | 1992-02-13 | 1992-04-09 | Kirschenmann, Guenter, Dipl.-Ing., 7507 Pfinztal | Gassing agitator |
FI94317C (en) | 1992-10-16 | 1995-08-25 | Outokumpu Mintec Oy | Methods and apparatus for dispersing gas in liquid |
US5342429A (en) * | 1993-05-05 | 1994-08-30 | Aluminum Company Of America | Purification of molten aluminum using upper and lower impellers |
US5427456A (en) * | 1994-04-12 | 1995-06-27 | Synektron Corporation | Fluid bearing with asymmetrical groove pattern |
US5616304A (en) * | 1995-04-21 | 1997-04-01 | Innovative Biosystems, Inc. | Slurry reactor |
US5620250A (en) * | 1996-03-05 | 1997-04-15 | Pro-Quip, Inc. | Jet mixer having a self-centering liquid bearing hub arrangement |
RU2107618C1 (en) * | 1996-04-22 | 1998-03-27 | Мордовский государственный университет им.Н.П.Огарева | Mixer |
DE29621503U1 (en) | 1996-12-11 | 1997-03-06 | Kordeuter, Franz, 88213 Ravensburg | Fan-like parasol |
DE29621683U1 (en) * | 1996-12-13 | 1997-02-13 | Ekato Ruehr Mischtechnik | Stirrer |
US6346412B1 (en) * | 1997-09-03 | 2002-02-12 | Newbio, Inc. | Microbial remediation reactor and process |
DE29909312U1 (en) | 1999-05-27 | 1999-08-12 | Ekato Rühr- und Mischtechnik GmbH, 79650 Schopfheim | Agitator |
TW393572B (en) * | 1999-11-30 | 2000-06-11 | Taidoc Technology Co Ltd | Fast clinical thermometer and its forecast method |
JP2002102668A (en) * | 2000-10-02 | 2002-04-09 | Kankyo Soken Kk | Apparatus for treating unused organic substance |
JP2004176640A (en) * | 2002-11-27 | 2004-06-24 | Kumamoto Technology & Industry Foundation | Fluid sucking and mixing device |
DE20307199U1 (en) | 2003-05-08 | 2003-07-10 | Ekato Rühr- und Mischtechnik GmbH, 79650 Schopfheim | stirrer |
DE102005017327B4 (en) | 2005-04-14 | 2007-08-30 | EKATO Rühr- und Mischtechnik GmbH | processing plant |
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DE102007001711A1 (en) | 2007-01-11 | 2008-07-17 | EKATO Rühr- und Mischtechnik GmbH | Stirring arrangement with a stirrer and a gassing device |
CN101190403B (en) * | 2007-04-27 | 2010-09-15 | 方民 | High-efficiency fluid mixed stirring leaf blade unit |
KR101157719B1 (en) * | 2007-05-22 | 2012-06-20 | 가부시끼가이샤 도시바 | Device and method for producing micro gas bubbles |
-
2010
- 2010-01-08 DE DE102010004206A patent/DE102010004206A1/en not_active Ceased
- 2010-06-07 ES ES10734666.0T patent/ES2458923T3/en active Active
- 2010-06-07 BR BRPI1010845A patent/BRPI1010845A2/en not_active IP Right Cessation
- 2010-06-07 EP EP10734666.0A patent/EP2440315B1/en active Active
- 2010-06-07 RU RU2011153766/05A patent/RU2542258C2/en active
- 2010-06-07 CA CA2764466A patent/CA2764466C/en active Active
- 2010-06-07 US US13/375,377 patent/US8894047B2/en active Active
- 2010-06-07 AU AU2010257782A patent/AU2010257782B2/en active Active
- 2010-06-07 KR KR1020117028491A patent/KR20120012977A/en not_active Application Discontinuation
- 2010-06-07 WO PCT/EP2010/003410 patent/WO2010142406A1/en active Application Filing
- 2010-06-07 JP JP2012514378A patent/JP2012529363A/en active Pending
-
2011
- 2011-12-06 CL CL2011003088A patent/CL2011003088A1/en unknown
Non-Patent Citations (1)
Title |
---|
See references of WO2010142406A1 * |
Also Published As
Publication number | Publication date |
---|---|
AU2010257782A1 (en) | 2011-12-15 |
ES2458923T3 (en) | 2014-05-07 |
RU2011153766A (en) | 2013-07-20 |
JP2012529363A (en) | 2012-11-22 |
US20120069694A1 (en) | 2012-03-22 |
DE102010004206A1 (en) | 2010-12-09 |
RU2542258C2 (en) | 2015-02-20 |
CL2011003088A1 (en) | 2012-05-18 |
AU2010257782B2 (en) | 2014-01-09 |
CA2764466A1 (en) | 2010-12-16 |
KR20120012977A (en) | 2012-02-13 |
US8894047B2 (en) | 2014-11-25 |
BRPI1010845A2 (en) | 2016-04-05 |
EP2440315B1 (en) | 2014-03-05 |
CA2764466C (en) | 2014-03-11 |
WO2010142406A1 (en) | 2010-12-16 |
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