SE542677C2 - Mixing apparatus comprising a rotor and a stator - Google Patents
Mixing apparatus comprising a rotor and a statorInfo
- Publication number
- SE542677C2 SE542677C2 SE1850579A SE1850579A SE542677C2 SE 542677 C2 SE542677 C2 SE 542677C2 SE 1850579 A SE1850579 A SE 1850579A SE 1850579 A SE1850579 A SE 1850579A SE 542677 C2 SE542677 C2 SE 542677C2
- Authority
- SE
- Sweden
- Prior art keywords
- rotor
- mixing
- stator
- mixing chamber
- fluids
- Prior art date
Links
Classifications
-
- 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
- B01F27/27—Mixers with stator-rotor systems, e.g. with intermeshing teeth or cylinders or having orifices
- B01F27/272—Mixers with stator-rotor systems, e.g. with intermeshing teeth or cylinders or having orifices with means for moving the materials to be mixed axially between the surfaces of the rotor and the stator, e.g. the stator rotor system formed by conical or cylindrical surfaces
- B01F27/2722—Mixers with stator-rotor systems, e.g. with intermeshing teeth or cylinders or having orifices with means for moving the materials to be mixed axially between the surfaces of the rotor and the stator, e.g. the stator rotor system formed by conical or cylindrical surfaces provided with ribs, ridges or grooves on one surface
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C7/00—Digesters
- D21C7/06—Feeding devices
-
- 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
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/05—Stirrers
- B01F27/11—Stirrers characterised by the configuration of the stirrers
- B01F27/112—Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades
- B01F27/1125—Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades with vanes or blades extending parallel or oblique to the stirrer axis
- B01F27/11252—Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades with vanes or blades extending parallel or oblique to the stirrer axis paddle wheels
-
- 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
- B01F27/192—Stirrers with two or more mixing elements mounted in sequence on the same axis with dissimilar 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
- B01F27/27—Mixers with stator-rotor systems, e.g. with intermeshing teeth or cylinders or having orifices
-
- 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
- B01F27/27—Mixers with stator-rotor systems, e.g. with intermeshing teeth or cylinders or having orifices
- B01F27/271—Mixers with stator-rotor systems, e.g. with intermeshing teeth or cylinders or having orifices with means for moving the materials to be mixed radially between the surfaces of the rotor and the stator
- B01F27/2712—Mixers with stator-rotor systems, e.g. with intermeshing teeth or cylinders or having orifices with means for moving the materials to be mixed radially between the surfaces of the rotor and the stator provided with ribs, ridges or grooves on one surface
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21B—FIBROUS RAW MATERIALS OR THEIR MECHANICAL TREATMENT
- D21B1/00—Fibrous raw materials or their mechanical treatment
- D21B1/04—Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres
- D21B1/12—Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres by wet methods, by the use of steam
- D21B1/30—Defibrating by other means
- D21B1/34—Kneading or mixing; Pulpers
- D21B1/342—Mixing apparatus
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C9/00—After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
- D21C9/10—Bleaching ; Apparatus therefor
-
- 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
- B01F2101/47—Mixing of ingredients for making paper pulp, e.g. wood fibres or wood pulp
Abstract
According to the present invention, there is provided a mixing apparatus (10) for mixing fluids. The apparatus comprises a housing (12) having a mixing chamber (14). At least one inlet opening (18) communicates with the mixing chamber (14), wherein the inlet opening (18) enabling fluids to be fed into the mixing chamber (14). At least one outlet (22) is provided in the housing (12) and communicates with the mixing chamber (14). A rotor (24) is arranged in the mixing chamber (14) and is adapted to be connected to a drive shaft (28) to rotate with the drive shaft. The rotor (24) includes mixing elements (32) arranged around the rotor (24) and along its extension, wherein the rotor (24) includes a discharge end (34) arranged with discharging elements (36) for discharging the fluids radially. A stator (38) is arranged in the mixing chamber (14) and includes a number of stator openings (40) allowing mixed fluids discharged by the discharging elements (36) of the rotor (24) to flow radially through the stator openings (40) from the mixing chamber (14) and further toward the at least one outlet (22), wherein a tangential movement of the discharged fluids is prevented.
Description
ln many industrial applications, such as within different chemical industrieswhere various chemicals have to be mixed with different suspensions of rawmaterial or into combinations of raw material, it is of high importance tohomogenize media having different properties such as different densities to obtainhomogenous suspensions. Such industries include paint manufacturing and pulpand papermanufacturing.
Within the pulp and paper industry, throughout the fiberline, i.e. thedifferent process steps involved when converting wood chips or other fibrous rawmaterial into pulp, there are several positions where mixing apparatuses are usedto mix different kind of media into the pulp suspension. The treatment mediaadded to the fiber suspension may for example be for heating, delignification orbleaching purposes. Often the treatment media are in gaseous or liquid state.
When mixing treatment media into a fiber suspension, it is of highimportance for the mixing result that an even or homogenous distribution isachieved.
Cylindrical mixers are provided in a wide range of configurations. Forexample, the rotor of the mixer may have a center axis aligned with or arrangedperpendicularly to the general flow direction of the media. Also, the outlet and inletof the mixer may both be positioned axially with respect to the center axis of therotor, or one of the inlet or outlet may be positioned perpendicularly to the centeraxis of the rotor. ln many cylindrical mixer configurations, particularly wherein theoutlet is arranged perpendicularly to the inlet and a center axis of the outlet isperpendicular to a center axis of the rotor, or in a tangential direction in relation tothe rotor, there is a remaining rotation of the media flowing out from the mixer, e.g. the pulp suspension. 2 This remaining rotation of the pulp suspension may cause a separation ofmedia or fluids when the mixed media have different densities due to thecentrifugal force, which is an undesired phenomenon particularly frequent whengaseous media are mixed with media with higher density such as pulp.
Thus, there is a need for improved mixing apparatuses for mixing media orfluids with different density properties and, in particular, for mixing apparatuses formixing treatment media into a fiber suspension, e.g. lignocellulosic pulp suspension.
SUMMARY OF THE INVENTION An object of the present invention is to provide an improved mixingapparatus for mixing media or fluids with different density properties.
Another object of the present invention, is to provide an improved mixingapparatus for mixing treatment media into a fiber suspension, e.g. lignocellulosicpulp suspension These and other objects are achieved by the present invention by meansof a mixing apparatus for mixing media or fluids according to the claims.
According to an aspect of the present invention, there is provided a mixingapparatus for mixing fluids, for example, a gaseous medium into a pulpsuspension. The mixing apparatus comprises a housing having a mixing chamber,at least one inlet opening communicating with the mixing chamber. The inletopening enables fluids to be fed into the mixing chamber. A drive shaft isconnectable to a drive device for rotation of the drive shaft in operation and a rotoris arranged in the mixing chamber and is adapted to be connected to the driveshaft to rotate with the drive shaft. At least one outlet is provided in the housingand is communicating with the mixing chamber. The at least one outlet iscommunicating with an outlet duct for enabling a discharge of mixed fluids. Therotor has a rotor axis extending through the mixing chamber and being concentricwith the drive shaft, wherein the rotor includes mixing elements arranged aroundthe rotor and along its extension. The rotor includes a discharge end arranged withdischarging elements for discharging the fluids radially. A stator is arranged in themixing chamber including stator openings allowing mixed fluids discharged by thedischarging elements of the rotor to flow radially through the stator openings fromthe mixing chamber and further toward the at least one outlet, whereby a 3 tangential movement of the discharged fluids is prevented. The stater is encircied in a radial direction bv a diseharae space deiimited hv an interior waii of thehousing the discharde end ef the rotor and the stator. The discharee spaceeernsnunieates tfvith the eutiet duct via the at ieast ene outšet wherein duringeeeratšon. fštsšds are fefced to fiow titroudti ttie stator epenšnds and in a serni~cireuiar ttow in the discharge space tetvards the at ieast one outiet and otitiet duct.
The present invention is based on the insight that by, during discharge ofthe fluids, Stopping or preventing the remaining rotation of the fluids, e.g. the pulpsuspension, and thus the tangential movement of the fluids by means of the stator,the separation of fluids with different density properties caused by the centrifugalforce can be minimized. This effect is also improved by the uniform radialdischarge of fluids from the mixing zone within the mixing chamber.
According to an embodiment of the present invention, a center axis of theoutlet duct is perpendicularly, e.g. radially, displaced in a direction towards the atleast one outlet in relation to a center axis the rotor. ln embodiments of the present invention, an interior volume of the outletduct increases in proportion to a volume of the discharged fluid in a flow direction.
According to embodiments of the invention, the stator is shaped as tubularelement. ln embodiments of the invention, the stator openings is arranged radiallyadjacent to and outside the discharging elements of the rotor in a flow direction.
According to embodiments of the invention, the stator openings aredistributed along the stators entire circumference to provide a symmetric dischargeflow of fluid. ln embodiments of the invention, the mixing elements of the rotor areprotrusions with a curved or angled trailing surface in a direction of rotation of therotor.
According to embodiments of the invention, the mixing elements of saidrotor are distributed along substantially entire longitudinal extension of the rotor. ln embodiments of the present invention, the discharging elements of the rotor are protrusions curved or angled in a flow direction. 4 samma-inie-ates--with--the-eastiet-daset--vi-a--the--a-t--ieast--eneat:i:Eetï--xivifiereiifg--during ei:feelar-flow-in"the-däsena-arge--spase--tewarfds-the--at-least--ene-eutiet»arteš--eutle-t--duetfFurther advantageous embodiments of the device according to the presentinvention and further advantages of the present invention emerge from the de- tailed description of embodiments.
BRIEF DESCRIPTION OF THE DRAWINGSThe present invention will now be described, for exemplary purposes, in moredetail by way of embodiments and with reference to the enc|osed drawings, inwhich: Fig. 1 i||ustrates a schematical axial cross-section of a first preferredembodiment of the present invention; Fig. 2 i||ustrates a schematical partly cross-sectional view of a firstpreferred embodiment of the present invention; Fig. 3 i||ustrates a schematical view of the mixing apparatus and the out|etopening in a direction perpendicu|ar to a center axis of the rotor and shaft; Fig. 4 i||ustrates a schematical cross-section view of the mixing apparatusin a direction along the extension of the center axis of the rotor and shaft; Fig. 5 i||ustrates schematically the outside of the housing of the mixingapparatus according to the present invention.
DETAILED DESCRIPTION OF PREFERRED EMBODIMENTS ln the drawings, similar or corresponding elements are denoted by thesame reference numbers. Generally, in the drawings, arrows indicate the directionof the flow of fluid in the mixing apparatus, into and out of the mixing apparatus.
For the purpose of this disclosure, the term longitudinal refers to thedirection along which a body, part or element has its greatest extension. Further,when the term longitudinal is used in connection with the axes of shafts or similar,the longitudinal axis corresponds to the rotational axis of the shaft or similar.
With reference first to Fig. 1, the mixing apparatus 10 comprises a housing12, wherein the interior thereof is called a homogenization chamber or mixingchamber 14 with an inlet duct 16 having an inlet 18 into the mixing chamber 14.Further, the mixing apparatus 10 comprises an out|et duct 20 having an out|et 22 from the mixing Chamber 14 and a rotor 24 arranged axially with the direction offlow from the inlet opening 18 and transverse to the direction of flow to the outlet22.
The housing 12 is, in this embodiment of the present invention, preferabiyof a cylindrical, she|| or helix shaped design, as shown in Fig. 5. The housing 12 isfurther provided with an end part or end cap 26. The end cap 26 includes asubstantially central opening for a shaft 28 of the rotor 24 with necessary sealing,and possibly bearings for the shaft 28.
The substantially cylindrical wall of the housing 12 is, as explained above,provided with inlet and outlet 18, 22. Preferably, the shape of the inlet opening 18such that a center axis and an axis of symmetry that is concentric with the centeraxis RR of the rotor 24 and the shaft 28.
The outlet 22 is in some embodiments of the present invention shaped asa rectangle as shown in Fig. 3. Fig. 3 illustrates the mixing apparatus 10 and theoutlet 22 schematically in a direction perpendicular to a center axis RR of the rotor24 and shaft 28.
The outlet duct 20 is, according to preferred embodiments of the presentinvention, shaped such that a center axis Rou of the outlet duct 20 is radiallydisplaced in a direction towards the outlet 22 in relation to the center axis RR of therotor 24 and such that an interior volume of the outlet duct 20 increases inproportion to a volume of the discharged fluid.
Hence, the rotor 24 is mounted to the shaft 28 in the mixing chamber 14and rotates with the drive shaft 28. The shaft 28 is driven by a motor, for example,an electrical motor. The rotor 24 has a number of mixing elements 32 arrangedaround the rotor and along its longitudinal extension.
Further, the rotor 24 includes a discharge end 34 arranged with dischargingelements 36 for discharging the fluids in a direction substantially radially, inrelation to the center axis RR of the rotor 24 towards to outlet 22 and outlet duct20.
The purpose of the mixing elements 32 is to cause turbulence in the fluidsor media and thereby to obtain a homogenization or mixing of the fluids or mediaand to avoid a separation of, for example, gas from a medium. However, as theskilled person realizes, the shape and design of the mixing elements 32 as well as their number and exact location on the rotor and in relation to the inner wall of the 6 housing, to the inlet opening, depend on the medium or media to be treated, theconsistency of the medium or media, gas content of media, volume flow throughthe mixing chamber, amount of gas added to medium or media to mention a fewinfluencing parameters. ln addition to cause turbulence, the mixing elementscauses a flow of media through the mixing chamber towards the end part of therotor, where for example, the flow velocity of the medium or media can beregulated by means of the inter alia the rotational speed of the rotor.
The mixing elements 32 can, according to certain embodiments, bedistributed along the longitudinal extension of the rotor 24 in a gradually dislocatedmanner such that each line of mixing elements 32 are arranged with an inclinationin relation to the center axis RR of the rotor 24. Further, in certain embodiments,the mixing elements 32 are protrusions with a curved or angled trailing surface in adirection of rotation of the rotor 24 and the discharging elements 36 areprotrusions curved or angled in a flow direction.
A stator 38 is arranged at the end of the mixing chamber 14 adjacent to theoutlet 22. The stator 38 comprises a number of stator openings 40 arrangedradially adjacent to and outside the discharging elements 36 of the rotor 24 in aflow direction (indicated with arrows).
Preferably, the stator 38 is shaped as tubular element provided inside thehousing, for example as an insert lining or attached to the housing by means of forinstance bolts or screws. An important purpose of the stator 38 and the statoropenings 40 is, in essence, to function as an end of the mixing zone within themixing chamber 14 and to stop or prevent a tangential movement of thedischarged fluids when entering into and flowing through the stator openings 40.
A common problem in prior art mixing devices is a separation of gas frommedium during the outflow or discharge caused by remaining rotation in the mediasince the centrifugal force acts differently on gases compared to liquids or pulpsuspensions, for example. This is a pronounced problem when gas is mixed withpulp suspension.
Turning now to Fig. 4 which illustrates a schematical cross-section view ofthe mixing apparatus in a direction along the extension of the center axis RR of therotor 24 and shaft 28, i.e. the center axis RR of the rotor 24 points out from thefigure. As shown in Fig. 4, the stator 38 is encircled in a radial direction by a 7 discharge space 42 communicating with the mixing Chamber 14 via the statoropenings 40 and the outlet duct 20 via the outlet 22.The discharge space 42 is delimited by an interior wall 44 of the housing12, the discharge end 34 of the rotor 24 and the stator 38. ln Fig. 4, the flow ofmedia is indicated with arrows B, C, and D. Arrow B illustrates the flow of media inthe mixing chamber 14, where the rotation of the rotor 24 causes turbulence androtation of media and thereby homogenization and mixing of the media, forexample, gaseous medium and pulp suspension. Arrows C illustrate discharge ofmedia through the stator openings 40 and arrows D illustrate the semi-circular flowof media following the interior wall 44 of the housing 12 towards the outlet 22 andthen further to the outlet duct 20. As can be seen in Fig. 4, the volume of and thewidth (seen as a distance between the stator 38 and the interior wall 44 of thehousing 12) of the discharge space 42 increases in a flow direction.The invention shall not be considered limited to the embodiments illus- trated, but can be modified and altered in many ways by one skilled in the art,without departing from the scope of the appended claims.
Claims (1)
1. A mixing apparatus (10) for mixing fluids comprising: a housing (12) having a mixing Chamber (14), at least one inletopening (18) communicating with the mixing chamber (14), said inletopening (18) enabling fluids to be fed into the mixing chamber (14), a drive shaft (28) connectable to a drive device for rotation of the driveshaft (28) in operation, at least one outlet (22) provided in the housing (12) andcommunicating with the mixing chamber (14), said at least one outlet (22)communicating with an outlet duct (20) for enabling a discharge of mixedfluids; a rotor (24) arranged in said mixing chamber (14) adapted to beconnected to the drive shaft (28) to rotate with said drive shaft (28), saidrotor (24) having a center axis (RR) extending through the mixing chamber(14) and being concentric with said drive shaft (28), said rotor (24)including mixing elements (32) arranged around said rotor (24) and alongits extension, wherein said rotor (24) includes a discharge end (34)arranged with discharging elements (36) for discharging the fluids radially;and a stator (38) arranged in said mixing chamber (14) including statoropenings (40) allowing mixed fluids discharged by the dischargingelements (36) of the rotor (24) to flow radially through said stator openings(40) from the mixing chamber (14) and further toward the at least oneoutlet (22), whereby a tangential movement of the discharged fluids isprevented, characterized in that the stator (38) is encircled in a radial directionby a discharge space (42), said discharge space (42) being delimited byan interior wall (44) of said housing (12), said discharge end (34) of therotor (24) and said stator (38), said discharge space (42) communicatingwith the outlet duct (20) via the at least one outlet (22), wherein duringoperation fluids are forced to flow through the stator openings (40) and ina semi-circular flow in the discharge space (42) towards the at least oneoutlet (22) and outlet duct (20). _ The mixing apparatus according to claim 1, wherein a center axis (Rou) of the outlet duct in said housing (12) is perpendicularly displaced in adirection towards the at least one outlet (22) in relation to a center axis (RR)of said rotor (24). _ The mixing apparatus according to claim 2, wherein an interior volume of said outlet duct (20) increases in proportion to a volume of the dischargedfluid in a flow direction. _ The mixing apparatus according to any one preceding claims, wherein said stator (38) is shaped as tubular element. _ The mixing apparatus according to any one preceding claims, wherein the stator openings (40) are arranged radially adjacent to and outside saiddischarging elements (36) of said rotor (24) in a flow direction. _ The mixing apparatus according to any one of preceding claims, wherein said stator openings (40) are distributed along the stators (38) entirecircumference to provide a symmetric discharge flow of fluid. _ The mixing apparatus according to any one of preceding claims, wherein said mixing elements (32) of said rotor (24) are protrusions with a curved orangled trailing surface in a direction of rotation of the rotor (24). _ The mixing apparatus according to any one of preceding claims, wherein said mixing elements (32) of said rotor (24) are distributed alongsubstantially entire longitudinal extension of the rotor (24). _ The mixing apparatus according to any of the preceding claims, wherein said discharging elements (36) of said rotor (24) are protrusions curved orangled in a flow direction.
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SE1850579A SE542677C2 (en) | 2018-05-18 | 2018-05-18 | Mixing apparatus comprising a rotor and a stator |
PCT/SE2019/050326 WO2019221652A1 (en) | 2018-05-18 | 2019-04-09 | Mixing apparatus comprising a rotor and a stator |
CN201980032532.4A CN112118903A (en) | 2018-05-18 | 2019-04-09 | Mixing device comprising a rotor and a stator |
EP19804201.2A EP3793717A4 (en) | 2018-05-18 | 2019-04-09 | Mixing apparatus comprising a rotor and a stator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SE1850579A SE542677C2 (en) | 2018-05-18 | 2018-05-18 | Mixing apparatus comprising a rotor and a stator |
Publications (2)
Publication Number | Publication Date |
---|---|
SE1850579A1 SE1850579A1 (en) | 2019-11-19 |
SE542677C2 true SE542677C2 (en) | 2020-06-23 |
Family
ID=68540856
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SE1850579A SE542677C2 (en) | 2018-05-18 | 2018-05-18 | Mixing apparatus comprising a rotor and a stator |
Country Status (4)
Country | Link |
---|---|
EP (1) | EP3793717A4 (en) |
CN (1) | CN112118903A (en) |
SE (1) | SE542677C2 (en) |
WO (1) | WO2019221652A1 (en) |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
SU1331547A1 (en) | 1985-10-31 | 1987-08-23 | Ленинградское Специальное Конструкторское Бюро Всесоюзного Научно-Производственного Объединения Целлюлозно-Бумажной Промышленности | Apparatus for mixing fibrous suspension with reagents |
US5863120A (en) * | 1997-01-31 | 1999-01-26 | Beloit Technologies, Inc. | Medium consistency liquid mixture |
US6309788B1 (en) * | 1998-11-06 | 2001-10-30 | Canon Kabushiki Kaisha | Process for producing toner |
AUPQ503900A0 (en) * | 2000-01-11 | 2000-02-03 | Commonwealth Scientific And Industrial Research Organisation | Apparatus for mixing |
GB0326233D0 (en) * | 2003-11-11 | 2003-12-17 | Power Technologies Invest Ltd | System and method for pulverising and extracting mositure |
CN101850230B (en) * | 2009-03-31 | 2012-07-04 | 中国石油化工股份有限公司 | Fluid continuous reactor and application thereof |
CN103534016B (en) * | 2011-02-28 | 2016-04-20 | 苏舍米克斯帕克有限公司 | Dynamic mixer and uses thereof |
CN106582358B (en) * | 2015-10-19 | 2019-05-28 | 上海弗鲁克科技发展有限公司 | Mixing and dispersing device |
US11419451B2 (en) * | 2016-08-08 | 2022-08-23 | Plant Tap, LLC | Apparatus and method for producing beverages from dry ingredients |
-
2018
- 2018-05-18 SE SE1850579A patent/SE542677C2/en unknown
-
2019
- 2019-04-09 EP EP19804201.2A patent/EP3793717A4/en active Pending
- 2019-04-09 WO PCT/SE2019/050326 patent/WO2019221652A1/en active Application Filing
- 2019-04-09 CN CN201980032532.4A patent/CN112118903A/en active Pending
Also Published As
Publication number | Publication date |
---|---|
WO2019221652A1 (en) | 2019-11-21 |
EP3793717A4 (en) | 2022-03-02 |
SE1850579A1 (en) | 2019-11-19 |
CN112118903A (en) | 2020-12-22 |
EP3793717A1 (en) | 2021-03-24 |
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