EP2230004A1 - Kaskadenartige Beschichtungsvorrichtung für pulverförmiges Material sowie darauf bezogenes Verfahren - Google Patents

Kaskadenartige Beschichtungsvorrichtung für pulverförmiges Material sowie darauf bezogenes Verfahren Download PDF

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Publication number
EP2230004A1
EP2230004A1 EP09155601A EP09155601A EP2230004A1 EP 2230004 A1 EP2230004 A1 EP 2230004A1 EP 09155601 A EP09155601 A EP 09155601A EP 09155601 A EP09155601 A EP 09155601A EP 2230004 A1 EP2230004 A1 EP 2230004A1
Authority
EP
European Patent Office
Prior art keywords
liquid additive
powdery material
delivery
nozzles
flow rate
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP09155601A
Other languages
German (de)
English (en)
French (fr)
Inventor
Heinz Meier
Christian BÜRGE
Beat Schnider
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sika Technology AG
Original Assignee
Sika Technology AG
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Sika Technology AG filed Critical Sika Technology AG
Priority to EP09155601A priority Critical patent/EP2230004A1/de
Priority to CN2010800123961A priority patent/CN102355941A/zh
Priority to MX2011009827A priority patent/MX2011009827A/es
Priority to EP10709839A priority patent/EP2408545A1/de
Priority to BRPI1009463A priority patent/BRPI1009463A2/pt
Priority to PCT/EP2010/053584 priority patent/WO2010106154A1/de
Publication of EP2230004A1 publication Critical patent/EP2230004A1/de
Priority to US13/236,244 priority patent/US20120058265A1/en
Withdrawn legal-status Critical Current

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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B28—WORKING CEMENT, CLAY, OR STONE
    • B28C—PREPARING CLAY; PRODUCING MIXTURES CONTAINING CLAY OR CEMENTITIOUS MATERIAL, e.g. PLASTER
    • B28C7/00—Controlling the operation of apparatus for producing mixtures of clay or cement with other substances; Supplying or proportioning the ingredients for mixing clay or cement with other substances; Discharging the mixture
    • B28C7/04—Supplying or proportioning the ingredients
    • B28C7/0404—Proportioning
    • B28C7/0413—Proportioning two or more flows in predetermined ratio
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/50—Mixing liquids with solids
    • B01F23/54—Mixing liquids with solids wetting solids
    • 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
    • B01F25/20—Jet mixers, i.e. mixers using high-speed fluid streams
    • B01F25/21—Jet mixers, i.e. mixers using high-speed fluid streams with submerged injectors, e.g. nozzles, for injecting high-pressure jets into a large volume or into mixing chambers
    • B01F25/212—Jet mixers, i.e. mixers using high-speed fluid streams with submerged injectors, e.g. nozzles, for injecting high-pressure jets into a large volume or into mixing chambers the injectors being movable, e.g. rotating
    • 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
    • B01F25/40—Static mixers
    • B01F25/42—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
    • B01F25/43—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
    • B01F25/431—Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor
    • B01F25/43195—Wires or coils
    • B01F25/431951—Spirally-shaped baffle
    • 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
    • B01F25/72—Spray-mixers, e.g. for mixing intersecting sheets of material with nozzles
    • 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
    • B01F27/114—Helically shaped stirrers, i.e. stirrers comprising a helically shaped band or helically shaped band sections
    • 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
    • B01F27/115—Stirrers characterised by the configuration of the stirrers comprising discs or disc-like elements essentially perpendicular to the stirrer shaft axis
    • 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
    • B01F35/20—Measuring; Control or regulation
    • B01F35/21—Measuring
    • B01F35/211—Measuring of the operational parameters
    • B01F35/2111—Flow rate
    • 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
    • B01F35/20—Measuring; Control or regulation
    • B01F35/21—Measuring
    • B01F35/211—Measuring of the operational parameters
    • B01F35/2113—Pressure
    • 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
    • B01F35/20—Measuring; Control or regulation
    • B01F35/22—Control or regulation
    • B01F35/2201—Control or regulation characterised by the type of control technique used
    • B01F35/2209—Controlling the mixing process as a whole, i.e. involving a complete monitoring and controlling of the mixing process during the whole mixing cycle
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B28—WORKING CEMENT, CLAY, OR STONE
    • B28C—PREPARING CLAY; PRODUCING MIXTURES CONTAINING CLAY OR CEMENTITIOUS MATERIAL, e.g. PLASTER
    • B28C5/00—Apparatus or methods for producing mixtures of cement with other substances, e.g. slurries, mortars, porous or fibrous compositions
    • B28C5/02—Apparatus or methods for producing mixtures of cement with other substances, e.g. slurries, mortars, porous or fibrous compositions without using driven mechanical means effecting the mixing
    • B28C5/06—Apparatus or methods for producing mixtures of cement with other substances, e.g. slurries, mortars, porous or fibrous compositions without using driven mechanical means effecting the mixing the mixing being effected by the action of a fluid
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B28—WORKING CEMENT, CLAY, OR STONE
    • B28C—PREPARING CLAY; PRODUCING MIXTURES CONTAINING CLAY OR CEMENTITIOUS MATERIAL, e.g. PLASTER
    • B28C5/00—Apparatus or methods for producing mixtures of cement with other substances, e.g. slurries, mortars, porous or fibrous compositions
    • B28C5/38—Apparatus or methods for producing mixtures of cement with other substances, e.g. slurries, mortars, porous or fibrous compositions wherein the mixing is effected both by the action of a fluid and by directly-acting driven mechanical means, e.g. stirring means ; Producing cellular concrete
    • B28C5/381—Producing cellular concrete
    • B28C5/386—Plants; Systems; Methods
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F2215/00—Auxiliary or complementary information in relation with mixing
    • B01F2215/04—Technical information in relation with mixing
    • B01F2215/0413—Numerical information
    • B01F2215/0418—Geometrical information
    • B01F2215/0427—Numerical distance values, e.g. separation, position
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F2215/00—Auxiliary or complementary information in relation with mixing
    • B01F2215/04—Technical information in relation with mixing
    • B01F2215/0413—Numerical information
    • B01F2215/0436—Operational information
    • B01F2215/044—Numerical composition values of components or mixtures, e.g. percentage of components
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F2215/00—Auxiliary or complementary information in relation with mixing
    • B01F2215/04—Technical information in relation with mixing
    • B01F2215/0413—Numerical information
    • B01F2215/0436—Operational information
    • B01F2215/0468—Numerical pressure values
    • 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
    • B01F25/40—Static mixers
    • B01F25/42—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
    • B01F25/43—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
    • B01F25/431—Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor
    • B01F25/43197—Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor characterised by the mounting of the baffles or obstructions
    • B01F25/431971—Mounted on the wall

Definitions

  • the invention relates to a device for treating, in particular coating, of pulverulent material with at least one liquid additive.
  • the device comprises a conveying device, which contains at least one conveying line, through which the powdered material is conveyed, and at least one introduction device for introducing the liquid additive into the at least one conveying line according to the preamble of the first claim.
  • the invention relates to a method for treating powdered material with at least one liquid additive and to a use of a device for treating pulverulent material with at least one liquid additive according to the preambles of the further independent claims.
  • the material cement is usually obtained from cement clinker.
  • the cement clinker the precursor of the cement rotary kiln, ground to cement powder, then mixed with gypsum, which acts as a setting regulator, resulting in the mixing process, the final product cement.
  • the recovered cement is stored in silos after production.
  • the material cement is mixed with aggregates, chemical additives and water.
  • the addition of the additives should improve the properties of the concrete in chemical and / or physical terms.
  • the additives can influence the flow properties, the viscosity, the compression behavior and the setting behavior of the concrete.
  • liquid additive during further processing, in particular during the promotion, is difficult, since the powdery materials required for the production of the concrete, in particular their dust, can react with the liquid additive and affect the promotion of the powdery material by contamination of the conveyor. This can occur especially when a too large amount of additive is added locally or the additive contaminates the conveyor, which can lead to clogging and failure of the promotion of the powdery material.
  • the reaction of the powdery materials, in particular their dust, with the liquid additive can further affect the contamination of the introduction device, the introduction of the liquid additive.
  • the pulverulent materials required for the production of the concrete typically have high dust concentrations and / or high temperatures, which is particularly conducive to the formation of the above-mentioned soiling.
  • a reliable and controllable introduction of the liquid additives and a homogeneous distribution of the liquid additive on the powdery material are important for the quality of the final product and the trouble-free flow of the treatment process.
  • Object of the present invention is therefore to ensure a controlled, reliable and constant treatment of the powdery material with liquid additive in a device of the type mentioned.
  • the core of the invention is thus that the introduction device 6 of the device 1 comprises a supply line 7 and at least two nozzles 8, about which the liquid additive 3 in the delivery line 5 and the powdery material 2 can be inserted, wherein the outlet openings 9 of the at least two Nozzles 8, at a distance of 0.5 - 10 m, in particular 1 - 5 m, are attached to the conveying line 5.
  • the advantages of the invention can be seen, inter alia, in the fact that the arrangement of the outlet openings 9 of the at least two nozzles 8 at a distance of 0.5 - 10 m, a local supersaturation with liquid additive 3 in the conveying line 5 can be prevented. Among other things, thereby the flow rate of the liquid additive can be distributed to a plurality of nozzles 8 and by the distance of the outlet openings 9 from each other, the addition of liquid additive can be distributed over a larger area in the delivery line.
  • the device 1 has means 10 for determining the flow rate FI FZ of the liquid additive 3 and means 11 for determining the delivery pressure P FZ of the liquid admixture 3 and optionally means 12 for determining the flow rate FI PM of the powdery material 2 .
  • An increase in the delivery pressure P FZ can indicate, for example, a blockage in the introduction device 6 or an increase in the flow rate FI FZ , due to an increase in the flow rate FI PM of the powdery material 2.
  • another nozzle 8 can be switched on (cascade), whereupon the delivery pressure P FZ thanks to the larger outlet area falls back into the normal value range P FZ opt and the spray pattern remains in a safe area.
  • the conveying of liquid additive within a normal value range P FZ opt is advantageous in that the nozzle, in particular when dealing with flat-jet nozzles, has a pressure range or flow range in which an optimum spray pattern is ensured.
  • the device 1 comprises at least one mixing device 14, which mixes the mixture of powdered material 2 and liquid additive 3. This is particularly beneficial to the homogeneous distribution of the liquid additive to the powdery material.
  • the mixing device 14 actively moves the powdery material 2 in the conveying direction of the powdery material 2, in particular blockages of the conveying line 5 can be prevented or respectively dissolved.
  • At least one of the nozzles 8 is movable, in particular rotatable relative to the axis of the outlet direction of the liquid additive 3.
  • the spray pattern of the flow rate FI FZ and / or the delivery pressure P FZ , in particular the delivery pressure P FZ , of the liquid additive 3 are adjusted.
  • the at least one nozzle 8 can also be movably arranged in and out of the delivery line 5. This is among other things the prevention of contamination of the nozzle 8 conducive, since thereby the nozzles, in particular the outlet opening 9, are protected from the dust 17 of the powdery material 2. Furthermore, nozzles outside of the delivery line 5 can thereby be cleaned by a cleaning device 18, which improves the structural design of the cleaning environment. Furthermore, unused nozzles outside the delivery line can be protected from the dust 17. Both variants increase the flexibility of the device 1 over the amount and viscosity of the liquid additive 3.
  • FIG. 1 the schematic structure of a device 1 for treating, in particular coating, of powdered material 2 with at least one liquid additive 3 is shown.
  • the device 1 comprises at least one conveying device 4, which has at least one conveying line 5 contains, through which the powdery material 2 is conveyed, and at least one introduction device 6 for introducing the liquid additive 3 in the at least one delivery line comprising the powdery material 2.
  • the introduction device 6 comprises a supply line 7 and at least two nozzles 8, about which the liquid additive 3 in the conveying line 5 and the powdery material 2 can be inserted, wherein the outlet openings 9 of the at least two nozzles 8, at a distance of 0.5 - 10 m, in particular 1 - 5 m, are attached to the conveying line 5.
  • the device comprises at least three nozzles 8.
  • the device can ensure the treatment of powdered material 2 with at least one liquid additive 3 in a wider range of flow rate FI FZ .
  • pastedered material is meant in this document a material which is obtained by breaking up a dry solid, for example by crushing, grinding, crushing or milling in mills, or by spray-drying.
  • the pulverulent materials 2 typically have a particle size of essentially 1 to 200 ⁇ m, preferably 3 to 30 ⁇ m and / or a Blaine fineness of 2000 to 8000 cm 2 / g, preferably 3000 to 6000 cm 2 / g .
  • powdery material 2 are non-hydraulic, hydraulic and latent hydraulic powder material of all kinds, preferably such, which is needed for the construction industry in large quantities.
  • all materials which are used for the production of concrete, mortar or gypsum, in particular cement particles are suitable in principle as powdery materials 2. It can also substances or additives, such as for example, silica, fly ash, light aggregate, slag, fiber materials, for example, organic such as polypropylene fibers, etc. or inorganic such as basalt, glass, etc. may be used.
  • the powdery material 2 preferably comprises at least one binder which is preferably selected from the group consisting of cement, mortar, gypsum, silica, fly ash, slag and blast furnace slag or a mixture thereof.
  • the powdery material 2 is cement.
  • liquid admixture 3 are typically suitable substances which can be atomized and / or dropletized and / or vaporized and have a viscosity of 1-500 mPa * s.
  • the at least one liquid additive 3 is typically selected from the group consisting of dispersant, condenser, flow agent, retarder, accelerator, stabilizer, shrinkage reducer, air entraining agent and corrosion inhibitor or a mixture thereof.
  • a high-performance concrete condenser preferably the product ViscoCrete® from Sika, as the liquid additive.
  • This high-performance concrete condenser reduces the water content of cement and improves the workability of the concrete.
  • the conveying device 4 which contains at least one conveying line 5, through which the powdery material 2 is conveyed, is typically a conveying device in the construction industry.
  • Such a conveyor device 4 is used, for example, for transporting the production of the powdery material 2 to an intermediate storage, such as an intermediate silo, to a mobile means of transport, such as a truck or railway wagon, or a repository.
  • the transport of the powdery material 2 in a conveyor line 5 is usually by means of bucket elevators, conveyor belts, pneumatic or in so-called Heilier, also called "air slides".
  • Such air conveyor troughs are commercially available, for example, from Mahr GmbH, Germany.
  • Air conveyor troughs typically consist of rectangular steel tubes with a width of 10-100 cm and a height of 10-100 cm, while the powdery material 2 has a filling level of typically 1 ⁇ 4 -3 ⁇ 4 of the area intended for the powdered material during conveyance.
  • the movement of the powdery material 2 in an air conveyor trough is based on the fluidization of the powdered material by air, as well as the inclination of the trough of 5 to 10 °, which together with the kinetic energy, which brings the powdered material in entering the air conveyor trough, a movement allows the powdery material.
  • the fluidization is done by flowing with air from below through the located on a perforated substrate powdery material, whereby the particles of the powdery material remain within the resulting fluidized bed in a continuous up and down movement and so to speak remain in limbo.
  • the separation of Fluidisierluft and the powdery material is carried out by a release fabric made of plastic or glass fibers, wherein the fluidizing air can pass through the tissue, the powdered material 2 to be delivered but not.
  • dust is understood in the present document, the undesirable disperse distributions of solids, in particular of powdery material 2, in gases caused by mechanical processes or by fluidization, in particular by the transport in the delivery line 5, wherein the solid material in the Ambient air within the conveying line 5 is dispersed
  • the delivery line 5 is an air conveyor trough.
  • the powdery material 2 is transported through the conveying line 5 at a constant speed of about 0.5-10 m / s.
  • the introduction device 6 for introducing the liquid admixture 3 into the at least one delivery line 5 comprises a supply line 7 and at least two nozzles 8. Via at least one nozzle, the liquid admixture 3 can be introduced into the delivery line 5 and to the powdery material 2.
  • the liquid additive 3 can, for example, be atomized (aerosol) and / or dripped (drops) and / or vaporized (steam). Due to the different consistency, the coating thickness of the powdery material can be adjusted with the liquid additive.
  • the liquid additive 3 is typically conducted to the at least two nozzles 8 at a pressure of 1-15 bar, preferably 3-7 bar.
  • the pressure of the supply line is greater than or equal to, in particular greater than the nominal pressure of the nozzles.
  • the introduction device 6 to a pump for conveying the liquid additive 3, and at least one valve 19 in front of at least one nozzle 8.
  • the supply line 7 consists of a main supply line 71 and Sub-leads 72, which connect the main lead 71 with the nozzles 8.
  • Suitable nozzles 8 allow, inter alia, the spraying of liquid additive 3 at pressures of 1 to 30 bar, preferably 3 to 7 bar.
  • these are flat jet nozzles, mist nozzles or two-component nozzles, in particular flat-jet nozzles.
  • Fog nozzles are advantageous in that they can atomize pressurized liquids into very fine droplets with a large specific surface area.
  • Two-substance nozzles are characterized by a very fine atomization by the mixing of liquids with air or gas. Further, they can produce various spray patterns, such as flat jet, hollow cone or full cone spray patterns.
  • Flat jet nozzles are characterized by a uniform distribution of liquid and pressure. Furthermore, they allow a great variability in the choice of the spray angle. Particularly suitable nozzles have a spray angle of 30 ° - 120 °. Depending on the design of the outlet opening 9 of the nozzle, an elliptical or rectangular impact surface 16 is possible.
  • Flat jet nozzles are inexpensive and allow by a defined and easily adjustable impact surface 16 targeted treatment of the powdery material 2 with the liquid additive 3. This is to the effect of advantage that thereby the contact of the liquid additive 3 with the delivery line 5, in particular the walls and, if it is an air conveyor trough, the separating fabric, can be avoided. This reduces the risk of blocking the delivery of the powdery material 2 in that either the fluidization of the powdery material 2 is restricted or the powdery material settles on the walls and clumps.
  • the at least two nozzles 8 have a nozzle bore of 0.1 - 1 mm.
  • the nozzles 8 are typically arranged on the conveying line 5, that the liquid additive 3 as uniform as possible with a possible large part of the powdery material 2 can be brought into contact.
  • the nozzles are arranged on the powder material 2 opposite wall of the delivery line. It is also advantageous if the nozzles, in particular the outlet opening 9, in the conveying line 5 have the largest possible distance to the powdery material 2. On the one hand, this allows a greater flexibility in the treatment with the liquid additive 3, on the other hand, the nozzles are less exposed to the dust 17 of the powdery material 2, whereby the possibility of contamination of the nozzles is reduced.
  • the distance between the outlet opening 9 of the nozzle 8 and the powdery material 2 is typically dependent on the filling level of the powdery material 2, the shape of the cross section of the conveying line and the spraying angle of the nozzle.
  • the outlet opening 9 does not necessarily have to be circular disk-shaped, but may have other cross-sectional geometries; in particular, it may, for. B. be formed as an elongated slot whose length is a multiple of its height.
  • the exit direction of the liquid additive 3 when leaving the nozzle does not necessarily have to be identical to the direction of the nozzle axis.
  • the spray pattern of the flow rate FI FZ and / or the delivery pressure P FZ of the liquid admixture 3 can be adjusted by rotation of the nozzle to the axis of the discharge direction, in particular if it is a nozzle with a spray pattern with an elliptical or rectangular impact surface 16.
  • FIG. 2 is a plan view of the powdery material 2, which is transported in the conveying line 5 and shows possible positions of impact surfaces 16.
  • the spraying of the outer region 20 can be prevented by the larger impact surface 162 by rotation of the nozzle to the axis of the exit direction.
  • This can cause pollution the outer region 20, for example, the delivery line 5, in particular the walls and, if it is an air conveyor trough, the release fabric, be avoided.
  • the addition of the liquid additive 3 can be distributed over a larger area in the delivery line.
  • the rotatability of the at least one nozzle to the axis of the outlet direction of the liquid additive 3 by a control system 13 is adjustable.
  • At least one of the at least two nozzles promotes the liquid additive 3 in the delivery line 5 and the powdery material 2. It is particularly advantageous if the device 1 has at least two nozzles in normal operation, which promote the liquid additive 3 in the delivery line 5 and a nozzle which does not deliver a liquid additive. As a result, the device 1 can react accordingly both upon reaching a defined upper delivery pressure P FZ compared to normal or optimal operation and also with a drop in the delivery pressure P FZ and ensure the promotion in the normal value range P FZ opt .
  • the at least one nozzle 8 can also be movably arranged in and out of the delivery line 5. This is among other things the prevention of contamination of the nozzle 8 conducive, since thereby the nozzles, in particular the outlet opening 9, are protected from the dust 17 of the powdery material 2. Furthermore, nozzles outside of the delivery line 5 can thereby be cleaned by a cleaning device 18, which improves the cleaning environment. Furthermore, unused nozzles outside the delivery line can be protected from the dust 17.
  • the movement of the at least one nozzle into the delivery line 5 in or out by a control system 13 is adjustable.
  • nozzles 8 allow a higher flexibility of the device 1 with respect to the flow rate FI FZ and the delivery pressure P FZ , thereby, for example, liquid additives can be used over a wider viscosity range.
  • nozzles can both mobility, in the delivery line 5 in and out and rotatable to the axis of the exit direction of the liquid additive 3, have.
  • the device 1 has at least one cleaning device 18 for cleaning the introduction device 6.
  • the cleaning device 18 may comprise a means for cleaning the introduction device 6, which is selected from the group consisting of sieve, solvent, compressed air, mechanical tool and ultrasound. Further, the cleaning device 18 parts or the entire introduction device 6 as needed and / or time permanently or at regular intervals clean and it may be advantageous if the cleaning device 18 is regulated by a control system 13.
  • the cleaning device 18 may be further arranged inside or outside the delivery line 5. It may of course be used on a combination of the mentioned means and be advantageous.
  • the device 1 comprises at least one mixing device 14, which mixes the mixture of powdered material 2 and liquid additive 3.
  • mixing device 14 are typically devices that can mix the powdery material 2 and the liquid additive 3 to a fully or partially mixed common flow stream.
  • the mixing device 14 is arranged, at least partially, in the delivery line 5.
  • the mixing device 14 can be a static mixing device in which mixing succeeds by repeated division of the material flow 21, and a dynamic mixing device in which the material flow is multiply divided or even swirled by means of a moving element.
  • material flow in the present document means powdery material 2 in the delivery line 5 and additionally, if present, liquid additive 3 in connection with pulverulent material,
  • devices are suitable, which have molded parts, which the material flow 21 in the Conveying line 5 can be mixed by multiple parts, distracting and merging.
  • the moldings pflugscharähnliche mixing tools whose size, arrangement, peripheral speed and geometric shape are sized and matched to each other that they are able to mix the material flow 21 optimally.
  • molded parts in a spiral shape or helices are advantageous, which can cause a rotation reversal and flow division in the material flow and thereby ensure a good and continuous mixing.
  • Static mixers are advantageous in that they require little maintenance, typically slow down the flow of material, and require no external power.
  • screw mixers are suitable as dynamic mixing devices.
  • the shaping of the screw conveyor for example a simple, interrupted or opposite screw conveyor, gives the material flow 21 a swirling, three-dimensional movement.
  • the bringing together of the powdery material and the liquid additive by pushing movements along the delivery line 5 and in the material flow 21 itself.
  • a wobble member 141 is suitable, as in Figure 3a and 3b is shown.
  • the tumble element 141 may be partially or completely located in the material flow 21.
  • the flow direction of the material flow 21 is shown by a straight arrow.
  • the wobble member includes one or more disc-like mold members 142 which are coupled to the wobble member axis 143 so as to wobble vertically with respect to the wobble member axis upon rotation of the wobble member axis.
  • the at least one disc-like shaped part is fixedly arranged on the wobble axis 143 in such a way that the disc-like shaped part is inclined relative to the vertical axis 144 of the wobble element axis 2 ° -20 ° is.
  • a possible inclination 145 of the disc-shaped molding with respect to the vertical axis 144 of the wobble element axis 143 is in FIG. 3b shown.
  • the disk-like moldings are typically circular metal plates.
  • the tumble element axis is typically arranged substantially horizontally to the flow direction of the powdery material 2 in the delivery line 5. The tumbling motion of the disk-shaped moldings to the direction of flow of the powdery material 2 is to ensure a good and continuous mixing.
  • the rotation of the disk-like shaped parts about the wobble element axis is advantageously so fast that powdery material 2 experiences an acceleration in the direction of the conveying direction of the powdery material in contact with the disk-like shaped part.
  • the advantage of the dynamic mixing devices is that, in addition to the mixing process, they also actively move the powdery material 2 in the conveying direction of the powdered material. This can be used to prevent and / or eliminate clogging, in particular by clumping powdery material in the delivery line.
  • the mixing device 14 is in particular a mixing device which actively moves the powdery material 2 in the conveying direction of the powdery material 2.
  • the mixing device 14 is a tumbling element.
  • the mixing device 14 may further be a mechanical or a pneumatic mixing device.
  • pneumatic mixing devices are preferably mixing devices, which comprises at least one mixing nozzle 15 through which a gas, in particular air, can be blown into the mixture of powdered material 2 and liquid additive 3.
  • the gas jet generated by the mixing nozzle 15 generates the necessary mixing movements in the material flow 21.
  • the device 1 has means 10 for determining the flow rate FI FZ of the liquid admixture 3, for example a flow meter, and means 11 for determining the delivery pressure P FZ of the liquid admixture 3, for example a manometer.
  • the device 1 has means 12 for determining the flow rate FI PM of the pulverulent material 2, for example a flow meter for pulverulent media.
  • the determination of the flow rate FI PM of the powdery material 2 can be carried out empirically or technically.
  • the device 1 may further comprise at least one control system 13, which has as a measured variable the flow rate FI FZ of the liquid additive 3 and / or the delivery pressure P FZ of the liquid additive and / or the flow rate FI PM of the powdery material 2.
  • control system 13 as a measured variable to the delivery pressure P FZ of the liquid additive.
  • control system 13 can switch on or off at least one nozzle 8 as a controlled variable and / or can connect or disconnect at least one cleaning device as a controlled variable.
  • the mass ratio of added liquid additive 3 to powdery material 2 is typically 1:10 - 1: 1000, in particular from 1: 100 - 1: 500.
  • control system 13 has means 10 for determining the flow rate FI FZ of the liquid admixture 3, for example a flow meter, and means 11 for determining the delivery pressure P FZ of the liquid admixture 3, for example a manometer.
  • control system 13 has means 12 for determining the flow rate FI PM of the pulverulent material 2, for example a flow meter for pulverulent media.
  • Deviations of the delivery rate of the liquid admixture 3, for example due to contamination, can be compensated by changing the delivery pressure P FZ , in particular in conjunction with corresponding rotation of the nozzles to the axis of the discharge direction of the liquid additive, and / or by switching on or off of nozzles 8.
  • the control system 13 can in particular have the use of the cleaning devices 18 and / or the use of the mixing devices 14 as a controlled variable. It is particularly advantageous if the control system 13 has as control variables the mentioned devices and a rotation of the nozzles to the axis of the discharge direction of the liquid additive and a connection or disconnection of nozzles.
  • FIG. 4 schematically an example of a device 1 is shown.
  • Powdery material 2 is conveyed through the conveying line 5 of the conveying device 4, and liquid additive 3 is sprayed via the introduction device 6 into the conveying line 5 via nozzles 8.
  • the apparatus further comprises a means 12 for determining the flow rate FI PM of the powdery material 2.
  • mixing devices 14 are located in the delivery line 5, which are located at least partially in the material flow 21 of the powdery material.
  • the mixers are tumble elements as previously described.
  • the introduction device 6 comprises a feed line 7 consisting of a main feed line 71 and secondary feed lines 72 and four nozzles 8, of which the outlet openings 9 of three nozzles are arranged in the feed line 5 and deliver liquid additive and a nozzle no liquid additive promotes and is located outside the conveyor line 5 for protection from the dust 17.
  • the four nozzles are nozzles which can be moved into and out of the delivery line 5 and are rotatable with respect to the axis of the discharge direction of the liquid additive 3. Both mobilities are controlled variables of a control system 13.
  • the device further comprises means 10 for determining the flow rate FI FZ of the liquid additive 3 and the delivery pressure P FZ 11 of the liquid additive.
  • the secondary lines 72 further include a 1-way valve 22, in particular a 1-way valves with two switching positions that can be electrically actuated on.
  • the control system 13 can thereby turn on or off the promotion of individual nozzles.
  • the invention comprises a method for treating, in particular coating, powdery material 2 with at least one liquid additive 3, wherein the liquid additive 3 is brought into contact with the powdery material 2 via a previously described device 1.
  • the step comprises determining the flow rate FI PM of the powdery material 2, determining the flow rate FI FZ of the liquid additive 3 and determining the delivery pressure P FZ of the liquid additive 3.
  • the invention comprises the use of a device 1, as described above, for treating, in particular coating, powdery material 2 with at least one liquid additive 3.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Dispersion Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Structural Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Fluid Mechanics (AREA)
  • Nozzles (AREA)
EP09155601A 2009-03-19 2009-03-19 Kaskadenartige Beschichtungsvorrichtung für pulverförmiges Material sowie darauf bezogenes Verfahren Withdrawn EP2230004A1 (de)

Priority Applications (7)

Application Number Priority Date Filing Date Title
EP09155601A EP2230004A1 (de) 2009-03-19 2009-03-19 Kaskadenartige Beschichtungsvorrichtung für pulverförmiges Material sowie darauf bezogenes Verfahren
CN2010800123961A CN102355941A (zh) 2009-03-19 2010-03-19 用于粉末状材料的级联型涂覆装置以及与其相关的方法
MX2011009827A MX2011009827A (es) 2009-03-19 2010-03-19 Dispositivo de revestimiento tipo cascada para material pulverulento y metodo asociado.
EP10709839A EP2408545A1 (de) 2009-03-19 2010-03-19 Kaskadenartige beschichtungsvorrichtung für pulverförmiges material sowie darauf bezogenes verfahren
BRPI1009463A BRPI1009463A2 (pt) 2009-03-19 2010-03-19 dispositivo de revestimento do tipo cascata para material pulverizado, bem como processo associado
PCT/EP2010/053584 WO2010106154A1 (de) 2009-03-19 2010-03-19 Kaskadenartige beschichtungsvorrichtung für pulverförmiges material sowie darauf bezogenes verfahren
US13/236,244 US20120058265A1 (en) 2009-03-19 2011-09-19 Cascade-type coating device for powdery material and associated method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP09155601A EP2230004A1 (de) 2009-03-19 2009-03-19 Kaskadenartige Beschichtungsvorrichtung für pulverförmiges Material sowie darauf bezogenes Verfahren

Publications (1)

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EP2230004A1 true EP2230004A1 (de) 2010-09-22

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EP09155601A Withdrawn EP2230004A1 (de) 2009-03-19 2009-03-19 Kaskadenartige Beschichtungsvorrichtung für pulverförmiges Material sowie darauf bezogenes Verfahren
EP10709839A Withdrawn EP2408545A1 (de) 2009-03-19 2010-03-19 Kaskadenartige beschichtungsvorrichtung für pulverförmiges material sowie darauf bezogenes verfahren

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US (1) US20120058265A1 (zh)
EP (2) EP2230004A1 (zh)
CN (1) CN102355941A (zh)
BR (1) BRPI1009463A2 (zh)
MX (1) MX2011009827A (zh)
WO (1) WO2010106154A1 (zh)

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CN103537391A (zh) * 2013-09-29 2014-01-29 广州有色金属研究院 一种可调式双通道送粉装置

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CN110921356A (zh) * 2019-11-28 2020-03-27 福建南方路面机械有限公司 一种称重给料装置及物料处理系统
CN114451559B (zh) * 2022-01-10 2024-06-21 北京金康普食品科技有限公司 粉状脂溶性微量营养素预混料的制备系统、方法及食品

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GB521867A (en) * 1938-11-29 1940-06-03 Nat Stone & Granite Paving Com Improvements in or relating to the mixing concrete
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CN103537391B (zh) * 2013-09-29 2015-12-23 广州有色金属研究院 一种可调式双通道送粉装置

Also Published As

Publication number Publication date
WO2010106154A1 (de) 2010-09-23
US20120058265A1 (en) 2012-03-08
MX2011009827A (es) 2011-10-19
EP2408545A1 (de) 2012-01-25
CN102355941A (zh) 2012-02-15
BRPI1009463A2 (pt) 2016-03-01

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