EP0048312A1 - Method and apparatus for continuously mixing a liquid and powder - Google Patents
Method and apparatus for continuously mixing a liquid and powder Download PDFInfo
- Publication number
- EP0048312A1 EP0048312A1 EP80850136A EP80850136A EP0048312A1 EP 0048312 A1 EP0048312 A1 EP 0048312A1 EP 80850136 A EP80850136 A EP 80850136A EP 80850136 A EP80850136 A EP 80850136A EP 0048312 A1 EP0048312 A1 EP 0048312A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- wheel
- powder
- liquid
- gap
- cavity
- 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- Withdrawn
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
- B05B3/00—Spraying or sprinkling apparatus with moving outlet elements or moving deflecting elements
- B05B3/02—Spraying or sprinkling apparatus with moving outlet elements or moving deflecting elements with rotating elements
- B05B3/08—Spraying or sprinkling apparatus with moving outlet elements or moving deflecting elements with rotating elements in association with stationary outlet or deflecting elements
- B05B3/082—Spraying or sprinkling apparatus with moving outlet elements or moving deflecting elements with rotating elements in association with stationary outlet or deflecting elements the spraying being effected by centrifugal forces
- B05B3/085—Spraying or sprinkling apparatus with moving outlet elements or moving deflecting elements with rotating elements in association with stationary outlet or deflecting elements the spraying being effected by centrifugal forces in association with sectorial deflectors
-
- 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
- B01F25/60—Pump mixers, i.e. mixing within a pump
- B01F25/64—Pump mixers, i.e. mixing within a pump of the centrifugal-pump type, i.e. turbo-mixers
- B01F25/642—Pump mixers, i.e. mixing within a pump of the centrifugal-pump type, i.e. turbo-mixers consisting of a stator-rotor system with intermeshing teeth or cages
-
- 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
- B01F25/70—Spray-mixers, e.g. for mixing intersecting sheets of material
- B01F25/74—Spray-mixers, e.g. for mixing intersecting sheets of material with rotating parts, e.g. discs
- B01F25/743—Spray-mixers, e.g. for mixing intersecting sheets of material with rotating parts, e.g. discs the material being fed on both sides of a part rotating about a vertical axis
Definitions
- the present invention relates to a method and apparatus for continuously mixing liquid and powder to a substantially homogenous mixture.
- the apparatus comprises a mixture having a mixer housing and individual lines for supplying liquid and powder respectively to said apparatus.
- the object of the present invention is to avoid the aforementioned problems when preparing mixtures of liquid and powder.
- the method according to the present invention is mainly characterized in that the liquid and the powder are charged respectively, by separate lines, to a cavity arranged in a rotatable wheel and to powder spaces also arranged in said wheel, so as to be thrown by centrifugal force outwardly towards the periphery of said wheel, whereat the liquid is urged from said cavity, via a gap in said wheel, towards the upper side of said wheel and forms a mist curtain at the exit cf said gap, at which location the powder grains or particles thrown from said cavity by said centrifugal force are captured in said mist curtain and mixed therewith.
- the apparatus according to The invention is characterized in that the mixer housing includes a wheel arranged for rotation about a shaft in the mixer housing, whereat the line through which the liquid passes discharges into a cavity in the wheel, while The line through which the powder passes discharges into spaces in the upper part of said wheel, and the cavity communicates with said upper side of said wheel via a circumferentially extending gap having a configuration substantially corresponding to the configuration of the outer surface of a truncated cone, with the apex of said cone directed downwardly.
- One advantage afforded by means of the invention is that the amount of powder and the amount of liquid fed to The apparatus can be held constant during the whole of the mixing operation, which is extremely important, for example, when preparing mixtures within the medical industry.
- the ratio of powder to liquid can be set to any desired value for each particular mixture.
- the apparatus according to the invention operates continuously, as opposed to known apparatus where one "lump of dough" is mixed at a time, for example, in a so-called "batching".
- Figure 1 is a vertical sectional view of an apparatus according to the invention.
- Figure 2 is a sectional view taken on the line II-II of Figure 1.
- Figure 3 is a part of the vertical sectional view of Figure 1 shown in larger scale. Similar elements in the various views of the drawing have been identified by the same references.
- the apparatus illustrated in the drawing comprises a mixer housing 1 having a lid or cover 2.
- a wheel arrangement comprising an upper wheel 3 and a lower wheel 4 which is rotatably mounted on a shaft 5 by means of bearings 6.
- Located beneath the upper and the lower wheels 3 and 4 respectively is a cavity 7 which communicates with the upper side of the upper wheel 3 via a circumferentially extending gap defined by the outer surfaces 8 and 9 respectively of frusto-conical elements, with the apexes of said elements directed downwardly.
- Milled on the upper surface of the upper wheel 3 are blades 10, while blades 11 are milled on the lower surface of said upper wheel 3.
- the lower wheel 4 has a circumferentially extending edge 14 located adjacent the mouth of the gap 9.
- the lower wheel 4 is provided around its periphery with blades 15 for throwing out the powder and liquid mixture via a diffusor 16 and an outlet 17.
- the outlet may optionally be supplemented with a nozzle 18 which is used when the finished mixture is more flowable.
- the lid or cover 2 has a compartment 19 located above the centre of the wheel arrangement for receiving the powder phase, for further transport of said powder phase to the spaces 13.
- the lid is also provided on the undersurface thereof with pins 2C which lie adjacent the edge 14.
- the powder phase is fed to said compartment or space 19 with the aid of a transporter 21, for example a feed screw.
- the liquid phase is passed to the cavity 7 through a pipe 22.
- the wheels 3,4 of the wheel arrangement located within the housing 1,2 rotate about the shaft 5 at a speed which may lie between 1000 and 5000 rpm.
- the wet phase, or the liquid is passed to the mixer via the pipe 22, to the cavity 7.
- the liquid is thrown outwardly through the gap 8 and further through the gap 9.
- the liquid thus obtains the form of a skin which extends constantly outwardly while becoming thinner and thinner.
- the liquid skin leaves the gap 9 it strikes the edge 14 and is broken up into microscopic droplets so as to form a curtain.
- powder is supplied by the conveyor 21 to the compartment 19 and further to the spaces 13.
- the powder is thrown from the spaces 13, with the aid of centrifugal force and the blades 10, outwardly towards the periphery of the upper wheel 3, at the same time as said powder is whipped up and impinges on the curtain of liquid at the edge 14.
- the two phases, liquid and powder, are now thrown outwardly together and collide with pins 20, where the instantaneous mixture of powder and liquid takes place.
- the finished mixture is caught immediately by the blades 15 and is thrown outwardly via the diffusor 16 to the outlet 17. Granulates and stiff mixtures leave the mixer at the outlet 17, while the readily flowable mixture is taken out via the nozzle 18.
Abstract
A method and apparatus for continuously mixing a liquid and a powder to form a substantially homogenous mixture. The liquid and powder are fed, via separate lines (22,21) to a cavity (7) in a rotating wheel (3,4) and to powder-accommodating spaces (13) respectively in said rotating wheel (3,4) and are thrown therefrom by centrifugal force outwardly towards the periphery of the wheel. The liquid is pressed from the cavity (7) via a gap (8,9) arranged in the wheel in a direction towards the upper side of said wheel and forms a mist curtain as it exits from the gap. The mist curtain captures the powder particles thrown by centrifugal force from the powder-accommodating spaces (13) and is mixed with said particles.
Description
- The present invention relates to a method and apparatus for continuously mixing liquid and powder to a substantially homogenous mixture. The apparatus comprises a mixture having a mixer housing and individual lines for supplying liquid and powder respectively to said apparatus.
- In known methods of mixing a liquid with a powder, the liquid and powder are often kneaded together. Such methods, however, often result in the formation of lumps and agglomerates which is highly undesirable. it is often necessary to wet-grind the mixture in order to obtain the desired structure. When producing readily flowable mixtures, a further problem arises, namely that the internal friction in the mixture is so low that it is often impossible to avoid the formation of agglomerates, meaning that the lumps thus formed must be filtered off at a later stage.
- The object of the present invention is to avoid the aforementioned problems when preparing mixtures of liquid and powder. Accordingly, the method according to the present invention is mainly characterized in that the liquid and the powder are charged respectively, by separate lines, to a cavity arranged in a rotatable wheel and to powder spaces also arranged in said wheel, so as to be thrown by centrifugal force outwardly towards the periphery of said wheel, whereat the liquid is urged from said cavity, via a gap in said wheel, towards the upper side of said wheel and forms a mist curtain at the exit cf said gap, at which location the powder grains or particles thrown from said cavity by said centrifugal force are captured in said mist curtain and mixed therewith. The apparatus according to The invention is characterized in that the mixer housing includes a wheel arranged for rotation about a shaft in the mixer housing, whereat the line through which the liquid passes discharges into a cavity in the wheel, while The line through which the powder passes discharges into spaces in the upper part of said wheel, and the cavity communicates with said upper side of said wheel via a circumferentially extending gap having a configuration substantially corresponding to the configuration of the outer surface of a truncated cone, with the apex of said cone directed downwardly.
- One advantage afforded by means of the invention is that the amount of powder and the amount of liquid fed to The apparatus can be held constant during the whole of the mixing operation, which is extremely important, for example, when preparing mixtures within the medical industry. The ratio of powder to liquid can be set to any desired value for each particular mixture. Moreover, the apparatus according to the invention operates continuously, as opposed to known apparatus where one "lump of dough" is mixed at a time, for example, in a so-called "batching".
- The invention will now be described in more detail with reference to the accompanying drawing, which illustrates schematically an embodiment of an apparatus according to the invention
- Thus, Figure 1 is a vertical sectional view of an apparatus according to the invention. Figure 2 is a sectional view taken on the line II-II of Figure 1. Figure 3 is a part of the vertical sectional view of Figure 1 shown in larger scale. Similar elements in the various views of the drawing have been identified by the same references.
- The apparatus illustrated in the drawing comprises a
mixer housing 1 having a lid orcover 2. Arranged within thehousing 1 is a wheel arrangement comprising anupper wheel 3 and alower wheel 4 which is rotatably mounted on ashaft 5 by means of bearings 6. Located beneath the upper and thelower wheels cavity 7 which communicates with the upper side of theupper wheel 3 via a circumferentially extending gap defined by theouter surfaces upper wheel 3 areblades 10, whileblades 11 are milled on the lower surface of saidupper wheel 3. Arranged between theblades 10 arespaces 13 which are intended to receive the powder to be mixed with said liquid, while thecavity 7, which is divided into compartments by means of theblades 11, is intended to receive the liquid to be mixed with said powder. Thelower wheel 4 has a circumferentially extendingedge 14 located adjacent the mouth of thegap 9. Thelower wheel 4 is provided around its periphery withblades 15 for throwing out the powder and liquid mixture via adiffusor 16 and anoutlet 17. The outlet may optionally be supplemented with anozzle 18 which is used when the finished mixture is more flowable. The lid orcover 2 has acompartment 19 located above the centre of the wheel arrangement for receiving the powder phase, for further transport of said powder phase to thespaces 13. The lid is also provided on the undersurface thereof with pins 2C which lie adjacent theedge 14. The powder phase is fed to said compartment orspace 19 with the aid of atransporter 21, for example a feed screw. The liquid phase is passed to thecavity 7 through apipe 22. - When the apparatus is in operation, the
wheels housing shaft 5 at a speed which may lie between 1000 and 5000 rpm. The wet phase, or the liquid, is passed to the mixer via thepipe 22, to thecavity 7. As a result of the centrifugal force, and with the aid of theblades 11, the liquid is thrown outwardly through thegap 8 and further through thegap 9. The liquid thus obtains the form of a skin which extends constantly outwardly while becoming thinner and thinner. When the liquid skin leaves thegap 9 it strikes theedge 14 and is broken up into microscopic droplets so as to form a curtain. At the same time as liquid is supplied through thepipe 22, powder is supplied by theconveyor 21 to thecompartment 19 and further to thespaces 13. The powder is thrown from thespaces 13, with the aid of centrifugal force and theblades 10, outwardly towards the periphery of theupper wheel 3, at the same time as said powder is whipped up and impinges on the curtain of liquid at theedge 14. The two phases, liquid and powder, are now thrown outwardly together and collide withpins 20, where the instantaneous mixture of powder and liquid takes place. The finished mixture is caught immediately by theblades 15 and is thrown outwardly via thediffusor 16 to theoutlet 17. Granulates and stiff mixtures leave the mixer at theoutlet 17, while the readily flowable mixture is taken out via thenozzle 18. - The invention is not restricted to the described embodiment, but can be modified within the scope of the accompanying claims. Particular note should be taken to the expressions "cavity" and "powder spaces", since "a cavity" can in principle be said to comprise "a plurality of cavities" while "powder spaces" can be well said to be "a powder space".
Claims (5)
1. A method of continuously mixing liquid and powder together to form a substantially homogenous mixture, characterized by feeding the liquid and the powder via separate lines to a cavity in a rotatable mixing wheel and to powder-accommodating spaces arranged in said wheel, so as to be thrown out towards the periphery of the wheel by centrifugal force, whereat the liquid is pressed from said cavity via a gap in said wheel in a direction towards the upper side of said wheel and, as it exits from the wheel, is thrown out towards a peripherally extending edge on the peripheral side of the gap to form a mist curtain, which captures the powder particles thrown out by the centrifugal force, whereat the mixture of liquid and powder particles are then thrown outwardly towards the periphery of the wheel and are caught by mixer pins in the housing of the mixer wheel, to form a homogenous mixture which is fed towards the outlet of the mixer housing.
2. An apparatus for carrying out the method according to claim 1, comprising a mixer and a mixer housing (1, 2) and having separate lines (21,22) for supplying liquid and powder, characterized in that the mixer housing comprises a wheel arrangement (3,4) arranged for rotation on a shaft (5) in the mixer housing (1,2), whereat the liquid line (22) discharges into a cavity (7) in the wheel while the powder line discharges into powder-accommodating spaces (13) in the upper part of the wheel, and the cavity (7) communicates with the upper side of said wheel via a circumferentially extending gap (8,9) which opens out adjacent a circumferentially extending edge (14) located on the peripheral side of the gap, whereat the shape of the gap corresponds substantially to the shape of the outer surface of a truncated cone with the apex of said cone facing downwardly, and whereat the mixer housing (1,2) includes mixer pins (20) arranged to capture liquid from the mist curtain and the powder thrown out by centrifugal force from the powder spaces, to provide said mixture.
3. An apparatus according to claim 2, characterized in that the powder spaces (13) in the upper part of the wheel arrangement are separated from one another by means of blades (10) which are directed outwardly from the centre of the wheel.
4. An apparatus according to claim 2 or claim 3, characterized in that the cavity (7), which is located around the centre of the wheel arrangement, is divided into different compartments by means of blades (11) directed outwardly from the centre of said wheel.
5. An apparatus according to any one of claims 2-4, characterized in that the conical gap has a lower (8) and an upper (9) conical part, of which conical parts the apex angle of the lower part is more obtuse than the apex angle of the upper part.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP80850136A EP0048312A1 (en) | 1980-09-19 | 1980-09-19 | Method and apparatus for continuously mixing a liquid and powder |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP80850136A EP0048312A1 (en) | 1980-09-19 | 1980-09-19 | Method and apparatus for continuously mixing a liquid and powder |
Publications (1)
Publication Number | Publication Date |
---|---|
EP0048312A1 true EP0048312A1 (en) | 1982-03-31 |
Family
ID=8187484
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP80850136A Withdrawn EP0048312A1 (en) | 1980-09-19 | 1980-09-19 | Method and apparatus for continuously mixing a liquid and powder |
Country Status (1)
Country | Link |
---|---|
EP (1) | EP0048312A1 (en) |
Cited By (20)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0145823A1 (en) * | 1982-09-29 | 1985-06-26 | Dowell Schlumberger Corporation | Apparatus for mixing solids and fluids |
EP0201767A2 (en) * | 1985-05-17 | 1986-11-20 | YTRON Dr. Karg GmbH | Cyclone mixing device for the continuous mixing of powders with liquids |
US4633566A (en) * | 1985-04-04 | 1987-01-06 | General Electric Company | Apparatus and method for constructing and disassembling a truss structure |
FR2620044A1 (en) * | 1987-09-08 | 1989-03-10 | Pillon Francis | METHOD AND APPARATUS FOR SPREADING OR MIXING PULVERULENTS BY DEPOSITING PARTICLES SUSPENDED IN AIR |
US4832051A (en) * | 1985-04-29 | 1989-05-23 | Symbion, Inc. | Multiple-electrode intracochlear device |
US4838781A (en) * | 1988-09-12 | 1989-06-13 | Fischer Erwin C | Containerized fuel fireplace insert |
US4930930A (en) * | 1988-12-21 | 1990-06-05 | General Electric Company | Truss beam attachment apparatus |
DE4330632C1 (en) * | 1993-09-10 | 1995-02-09 | Santrade Ltd | Device for coating solid particles |
DE4330633C1 (en) * | 1993-09-10 | 1995-04-13 | Santrade Ltd | Device for covering small solid bodies |
US5505875A (en) * | 1991-09-03 | 1996-04-09 | Degussa Aktiengesellschaft | Storage-stable encapsulated sodium percarbonate and process for its production |
DE19833307A1 (en) * | 1998-07-24 | 2000-01-27 | Bran & Luebbe | Mixer used for mixing powder into a liquid stream in the food industry has a mixing rotor with a rinsing nozzle opening covered by an impingement plate or ring for uniform distribution of a rinsing stream |
WO2000037164A1 (en) * | 1998-12-21 | 2000-06-29 | Global Powder Ab | Device and method for continuous mixing |
CN106457178A (en) * | 2014-02-27 | 2017-02-22 | 施蓝姆伯格技术公司 | Mixing apparatus with stator and method |
JP2018522727A (en) * | 2015-08-13 | 2018-08-16 | ネッツシュ−ファインマールテヒニック ゲーエムベーハー | Apparatus and method for dispersing at least one substance in a fluid |
US10137420B2 (en) | 2014-02-27 | 2018-11-27 | Schlumberger Technology Corporation | Mixing apparatus with stator and method |
US10625933B2 (en) | 2013-08-09 | 2020-04-21 | Schlumberger Technology Corporation | System and method for delivery of oilfield materials |
US10633174B2 (en) | 2013-08-08 | 2020-04-28 | Schlumberger Technology Corporation | Mobile oilfield materialtransfer unit |
US10895114B2 (en) | 2012-08-13 | 2021-01-19 | Schlumberger Technology Corporation | System and method for delivery of oilfield materials |
US11453146B2 (en) | 2014-02-27 | 2022-09-27 | Schlumberger Technology Corporation | Hydration systems and methods |
US11819810B2 (en) | 2014-02-27 | 2023-11-21 | Schlumberger Technology Corporation | Mixing apparatus with flush line and method |
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DE838593C (en) * | 1949-05-04 | 1952-05-12 | Eugen Bellmann | Mixing method and device |
FR1165939A (en) * | 1955-11-30 | 1958-10-30 | Equip Ind Et Laitiers Soc D | Comminution machine |
DE1068670B (en) * | 1959-11-12 | Schriesheim bei Heidelberg Hermann Mehne | Device for mixing powdery or granular. Good with thick liquids | |
DE1275511B (en) * | 1963-05-11 | 1968-08-22 | Kurashiki Rayon Co | Device for the continuous mixing of liquids |
GB1239319A (en) * | 1968-09-05 | 1971-07-14 | ||
DE2216986B2 (en) * | 1971-04-16 | 1974-01-24 | Paul Montreuil Sous Bois Rayneri (Frankreich) | |
US3820759A (en) * | 1972-06-05 | 1974-06-28 | Hege Avanced Syst Corp | Centrifugal mixing apparatus and method |
CH559576A5 (en) * | 1973-12-04 | 1975-03-14 | Mueller Hans Maennedorf | |
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US3986705A (en) * | 1973-10-30 | 1976-10-19 | Nautamix Patent A.G. | Method and device for continuously mixing and/or granulating substances |
US3998433A (en) * | 1974-05-10 | 1976-12-21 | Funken Co., Ltd. | Continuous mixing machine for moistening powdered material |
GB2000039A (en) * | 1977-06-23 | 1979-01-04 | Naito M | Apparatus for generating finely divided particulate bubbles in a liquid |
JPS5481559A (en) * | 1977-12-09 | 1979-06-29 | Asahi Chem Ind Co Ltd | Method of continuous mixing of liquid and powder |
US4175873A (en) * | 1976-09-10 | 1979-11-27 | Funken Co., Ltd. | Process and apparatus for mechanically mixing two immiscible liquids and one or more other substances |
-
1980
- 1980-09-19 EP EP80850136A patent/EP0048312A1/en not_active Withdrawn
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CH559576A5 (en) * | 1973-12-04 | 1975-03-14 | Mueller Hans Maennedorf | |
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JPS5481559A (en) * | 1977-12-09 | 1979-06-29 | Asahi Chem Ind Co Ltd | Method of continuous mixing of liquid and powder |
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Title |
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Cited By (27)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0145823A1 (en) * | 1982-09-29 | 1985-06-26 | Dowell Schlumberger Corporation | Apparatus for mixing solids and fluids |
US4633566A (en) * | 1985-04-04 | 1987-01-06 | General Electric Company | Apparatus and method for constructing and disassembling a truss structure |
US4832051A (en) * | 1985-04-29 | 1989-05-23 | Symbion, Inc. | Multiple-electrode intracochlear device |
EP0201767A2 (en) * | 1985-05-17 | 1986-11-20 | YTRON Dr. Karg GmbH | Cyclone mixing device for the continuous mixing of powders with liquids |
EP0201767A3 (en) * | 1985-05-17 | 1987-12-23 | Ytron Dr. Karg Gmbh | Cyclone mixing device for the continuous mixing of powders with liquids |
FR2620044A1 (en) * | 1987-09-08 | 1989-03-10 | Pillon Francis | METHOD AND APPARATUS FOR SPREADING OR MIXING PULVERULENTS BY DEPOSITING PARTICLES SUSPENDED IN AIR |
US4838781A (en) * | 1988-09-12 | 1989-06-13 | Fischer Erwin C | Containerized fuel fireplace insert |
US4930930A (en) * | 1988-12-21 | 1990-06-05 | General Electric Company | Truss beam attachment apparatus |
US5505875A (en) * | 1991-09-03 | 1996-04-09 | Degussa Aktiengesellschaft | Storage-stable encapsulated sodium percarbonate and process for its production |
WO1995007135A1 (en) * | 1993-09-10 | 1995-03-16 | Santrade Ltd. | Device for coating solid particles |
DE4330633C1 (en) * | 1993-09-10 | 1995-04-13 | Santrade Ltd | Device for covering small solid bodies |
AU665914B2 (en) * | 1993-09-10 | 1996-01-18 | Santrade Limited | Device for coating solid particles |
DE4330632C1 (en) * | 1993-09-10 | 1995-02-09 | Santrade Ltd | Device for coating solid particles |
US5593500A (en) * | 1993-09-10 | 1997-01-14 | Santrade Ltd. | Device for coating solid particles |
DE19833307A1 (en) * | 1998-07-24 | 2000-01-27 | Bran & Luebbe | Mixer used for mixing powder into a liquid stream in the food industry has a mixing rotor with a rinsing nozzle opening covered by an impingement plate or ring for uniform distribution of a rinsing stream |
WO2000037164A1 (en) * | 1998-12-21 | 2000-06-29 | Global Powder Ab | Device and method for continuous mixing |
US7036976B1 (en) | 1998-12-21 | 2006-05-02 | Global Power Ab | Device and method for continuous mixing of at least two components |
US10895114B2 (en) | 2012-08-13 | 2021-01-19 | Schlumberger Technology Corporation | System and method for delivery of oilfield materials |
US10633174B2 (en) | 2013-08-08 | 2020-04-28 | Schlumberger Technology Corporation | Mobile oilfield materialtransfer unit |
US10625933B2 (en) | 2013-08-09 | 2020-04-21 | Schlumberger Technology Corporation | System and method for delivery of oilfield materials |
US10137420B2 (en) | 2014-02-27 | 2018-11-27 | Schlumberger Technology Corporation | Mixing apparatus with stator and method |
EP3110539A4 (en) * | 2014-02-27 | 2017-11-08 | Services Pétroliers Schlumberger | Mixing apparatus with stator and method |
CN106457178B (en) * | 2014-02-27 | 2020-11-06 | 施蓝姆伯格技术公司 | Mixing apparatus and method with stator |
CN106457178A (en) * | 2014-02-27 | 2017-02-22 | 施蓝姆伯格技术公司 | Mixing apparatus with stator and method |
US11453146B2 (en) | 2014-02-27 | 2022-09-27 | Schlumberger Technology Corporation | Hydration systems and methods |
US11819810B2 (en) | 2014-02-27 | 2023-11-21 | Schlumberger Technology Corporation | Mixing apparatus with flush line and method |
JP2018522727A (en) * | 2015-08-13 | 2018-08-16 | ネッツシュ−ファインマールテヒニック ゲーエムベーハー | Apparatus and method for dispersing at least one substance in a fluid |
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