EP1712271B1 - Dispositif pour homogénéiser et/ou disperser des matériaux fluides - Google Patents
Dispositif pour homogénéiser et/ou disperser des matériaux fluides Download PDFInfo
- Publication number
- EP1712271B1 EP1712271B1 EP06006605A EP06006605A EP1712271B1 EP 1712271 B1 EP1712271 B1 EP 1712271B1 EP 06006605 A EP06006605 A EP 06006605A EP 06006605 A EP06006605 A EP 06006605A EP 1712271 B1 EP1712271 B1 EP 1712271B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- dispersing device
- homogenising
- homogenizing
- container
- dispersing
- 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.)
- Not-in-force
Links
- 239000000463 material Substances 0.000 title claims abstract description 19
- 230000009969 flowable effect Effects 0.000 title claims description 11
- 238000012384 transportation and delivery Methods 0.000 claims description 23
- 239000007788 liquid Substances 0.000 claims description 12
- 239000000654 additive Substances 0.000 claims description 11
- 238000000034 method Methods 0.000 claims description 9
- 239000011345 viscous material Substances 0.000 abstract description 2
- 239000000126 substance Substances 0.000 description 18
- 239000004744 fabric Substances 0.000 description 15
- 238000004140 cleaning Methods 0.000 description 5
- 230000001419 dependent effect Effects 0.000 description 4
- 235000011837 pasties Nutrition 0.000 description 4
- 238000005086 pumping Methods 0.000 description 4
- 239000000499 gel Substances 0.000 description 3
- 239000006185 dispersion Substances 0.000 description 2
- 239000011346 highly viscous material Substances 0.000 description 2
- 238000000265 homogenisation Methods 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 238000004886 process control Methods 0.000 description 2
- 238000011144 upstream manufacturing Methods 0.000 description 2
- 230000000996 additive effect Effects 0.000 description 1
- 239000002537 cosmetic Substances 0.000 description 1
- 239000006071 cream Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 238000003780 insertion Methods 0.000 description 1
- 230000037431 insertion Effects 0.000 description 1
- 238000007726 management method Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 235000010746 mayonnaise Nutrition 0.000 description 1
- 239000002674 ointment Substances 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 238000013386 optimize process Methods 0.000 description 1
- 210000000056 organ Anatomy 0.000 description 1
- 239000006072 paste Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Images
Classifications
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- 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
- B01F23/40—Mixing liquids with liquids; Emulsifying
- B01F23/47—Mixing liquids with liquids; Emulsifying involving high-viscosity liquids, e.g. asphalt
-
- 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
- B01F23/56—Mixing liquids with solids by introducing solids in liquids, e.g. dispersing or dissolving
-
- 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
- B01F25/50—Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle
- B01F25/52—Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle with a rotary stirrer in the recirculation tube
-
- 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
- B01F25/50—Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle
- B01F25/53—Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle in which the mixture is discharged from and reintroduced into a receptacle through a recirculation tube, into which an additional component is introduced
-
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F33/00—Other mixers; Mixing plants; Combinations of mixers
- B01F33/80—Mixing plants; Combinations of mixers
- B01F33/82—Combinations of dissimilar mixers
- B01F33/821—Combinations of dissimilar mixers with consecutive receptacles
-
- 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
-
- 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
- B01F35/221—Control or regulation of operational parameters, e.g. level of material in the mixer, temperature or pressure
- B01F35/2214—Speed during the operation
- B01F35/22141—Speed of feeding of at least one component to be mixed
-
- 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
- B01F35/221—Control or regulation of operational parameters, e.g. level of material in the mixer, temperature or pressure
- B01F35/2214—Speed during the operation
- B01F35/22142—Speed of the mixing device during the operation
- B01F35/221422—Speed of rotation of the mixing axis, stirrer or receptacle during the operation
-
- 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
- B01F27/1122—Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades anchor-shaped
Definitions
- the invention relates to a device for homogenizing and / or dispersing flowable substances (original substance), in particular in liquid or pasty form.
- homogenizing and / or dispersing devices which are also referred to as homogenizers, are used in particular for the production of viscous or highly viscous products, ointments, pastes, gels, creams, doughs, mayonnaises or the like in the pharmaceutical, cosmetic, chemical and food industries used.
- the homogenizing and dispersing device of such a device which is also referred to as a homogenizer, includes for example EP 0 801 974 B1 a coaxial rotor / stator arrangement. This arrangement can be designed in several stages, so that the material template (product master) can go through the homogenizing and / or dispersing device several times with different intensity turbulence.
- Such a homogenizer is often placed on or in the bottom of a container, such as a mixing container, which is filled with a stock (product master) to a desired stock level. Wings may be provided to enhance the pumping action of the product master to the homogenizer.
- the product stream leaving the homogenizing and / or dispersing device can be returned to the container for an internal circulation operation, for example to the vicinity of the container bottom.
- the product stream from the homogenizing and / or dispersing device can be supplied to the container by, for example, an external circulation the upper region of which is preferably returned above the level of the fabric master.
- the homogenizing and / or dispersing device is associated with a pumping device, a common drive for the pumping device and the homogenizing and / or dispersing device is usually present, so that the delivery rate of the pumping device and the delivery rate of the homogenizing and / or dispersing device are immediate are mutually dependent on the shared drive. Furthermore, it has been shown that, for example, in the case of the addition of additives such as liquids, powdered substances or the like by suction, the substances sucked in the region of the homogenizing and / or dispersing device can be conveyed back in the direction of the container for the fabric template. Depending on the process conditions, even sucked powder, for example, can blow back into the container.
- An apparatus for homogenizing and / or dispersing flowable, in particular liquid or pasty substances (fabric master) according to the preamble of claim 1 is made EP 0 801 974 B1 known.
- the invention aims, while overcoming the difficulties described above, to provide a device for homogenizing and / or dispersing flowable substances of the generic type, which has universal controllability and controllability of the product streams before and after the homogenizing and / or dispersing device, in particular for avoidance cavitation phenomena also allowed during the cleaning process. Also, a return of sucked additives to the container with the fabric template should be reliably avoided.
- a variable optimized process control for homogenizing and dispersing especially taking into account shear-sensitive products, such as gels, mascara, etc., should be achieved, in particular, a viscosity-dependent process management should be implemented in an individual form.
- an apparatus for homogenizing and / or dispersing flowable, in particular liquid or pasty substances comprises a container for a fabric master and a motorized homogenizer and / or disperser (homogenizer).
- the fabric feed is conveyed from a container outlet by means of a feed pump to the homogenizing and / or dispersing device, which optionally associated with entry devices for additives in liquid or powdery form. If appropriate, the homogenizing and / or dispersing device can permit a discharge back into the container for the fabric template on the outlet side.
- such a device for homogenizing and / or dispersing is characterized in that the feed pump is driven separately to the homogenizing and / or dispersing, a sensor, preferably a pressure sensor, between the pump outlet and the inlet side of the homogenizing and / or Dispergier nails is arranged, which controls the separate drive of the feed pump variable in accordance with the flow characteristics of the stock and / or corresponding process parameters such that the product flow promotion to the homogenizing and / or dispersing always under pre-pressure.
- a sensor preferably a pressure sensor
- the conveying process by the feed pump and the product processing operation in the homogenizing and / or dispersing independently and universally controllable and controllable, so that these two units for optimization variable to the process conditions for realizing a viscosity-dependent process control, in particular also considering shear-sensitive Tune and control products.
- the conveying process by means of the feed pump and the homogenization and / or dispersion in homogenizing and / or dispersing independently influenced so that the feed pump, for example, taking into account the product type, such as viscous or highly viscous substances, can be controlled so that it is always possible to ensure that the product quantity or amount of substance conveyed by the feed pump in the direction of the homogenizing and / or dispersing device is always greater than the conveying capacity of the homogenizing and / or dispersing device. Thanks to the universal controllability and controllability can thus shorter Artsverweil initiatives realize and the product stream may optionally be exposed to lower shear effects, so that you can ensure a gentle treatment of the fabric template.
- the throughputs of the device for homogenizing and / or dispersing can be optimized and increased.
- cavitation phenomena can be reliably avoided since the product stream is conveyed to the homogenizing and / or dispersing device always under admission pressure.
- a cleaning cycle it is therefore possible to avoid cavitation phenomena and the resulting noise phenomena, since the high delivery rate can be adjusted in a corresponding manner independently of the product flow rate through the homogenizing and / or dispersing device.
- a sensor preferably a pressure sensor, is arranged between the pump outlet and the inlet side of the homogenizing and / or dispersing device, which is used for controlling the feed pump, in particular for controlling the speed of the feed pump.
- an openable and closable product discharge is arranged in the material flow direction upstream of the inlet side of the homogenizing and / or dispersing device.
- shear-sensitive products such as gels, mascara, etc.
- the feed pump is formed by a centrifugal pump, which can be optimized only for the intended conveying purpose in terms of the viscosity characteristics of the processed fabric templates in a corresponding manner.
- a centrifugal pump can also be used to promote viscous and especially highly viscous substances.
- a centrifugal pump as a preferred embodiment of a feed pump allows design due to a substantially shear-free or at least low-shear treatment of the fabric templates to be processed.
- the feed pump preferably has a tangential outlet which is connected to the inlet side of the homogenizing and / or dispersing device. This allows a largely lossless promotion of the material template in this feed pump in the direction of the homogenizing and / or dispersing done.
- the design of the device is such that the return of the product stream from the outlet side of the homogenizing and / or dispersing to the vicinity of the container outlet at the container bottom and / or to the upper region of the container, preferably above the fabric template cover, can take place.
- the return of the product stream from the outlet side of the homogenizing and / or dispersing to the vicinity of the container outlet at the container bottom and / or to the upper region of the container, preferably above the fabric template cover can take place.
- an internal or external return promotion or circulation can be realized in the inventive device without major design effort.
- containers for the fabric template are arranged axially and / or radially conveying stirrer in order to achieve a uniform mixing of the fabric already in the container.
- axially and / or radially imparting stirring element even an exclusive return delivery internally to the vicinity of the container outlet may be sufficient, so that a more process-consuming external recycling can be dispensed with.
- the drive for the homogenizing and / or dispersing device and the drive for the feed pump is controlled by means of a frequency converter. This makes it possible to realize a very sensitive control and regulation of the respective drive motors.
- the device for homogenizing and / or dispersing flowable substances is designed such that the delivery rate of the feed pump and the delivery rate of the homogenizing and / or dispersing device are variable independently of each other.
- a universal change and influencing of the respective delivery rates of the feed pump and the homogenizing and / or dispersing device is achieved even taking into account the product viscosity and / or the energy density.
- the entry means of the additives are activated in liquid or powder form when the sensor designed in particular as a pressure sensor detects negative pressure conditions.
- the sensor designed in particular as a pressure sensor detects negative pressure conditions.
- a sensitive addition control with respect to the amounts of additive can be achieved, and in particular, it is also effectively avoided that added additives via the entry devices directly into the container, since a so-called. Knockback can be effectively suppressed.
- the device according to the invention is designed such that the residence time in the shear zone of the homogenizing and / or dispersing device can be adjusted or varied by the delivery rate (rotational speed) of the feed pump for energy density adjustment.
- the delivery rate rotational speed
- product warmings can be limited when passing through the homogenizing and / or dispersing device, because the product residence time in the homogenizing and / or dispersing device can be adjusted and changed, for example as a function of the viscosity of the product stream.
- the feed pump and the homogenizing and / or dispersing device form a compact structural unit.
- This provides a compact and space-saving design for the device and its units with the further advantage of a maintenance-friendly design.
- FIG. 1 is a device for homogenizing and / or dispersing flowable, in particular liquid or pasty substances, which is also referred to as a material template, provided overall with the reference numeral 1.
- This device 1 comprises a container 2 for the fabric template, which in FIG. 1 only partially shown.
- the container 2 also only schematically indicated with 3 stirrer is arranged, which is preferably designed axially and / or radially promotional.
- the container 2 has a container outlet 4 which communicates with a feed pump 5.
- the feed pump 5 is connected to a homogenizing and / or dispersing device 6, which is shown schematically in the drawing and is referred to there as a dispersing device.
- This homogenizing and / or dispersing device 6 is driven by a motor 7, while the feed pump 5 is also driven by an independent further motor 8.
- the feed pump 5 and the homogenizing and / or dispersing device 6 are driven by separate drives.
- FIG. 1 With an arrow is in FIG. 1 the substance flow direction entered.
- an insertion device 9 for additives arranged between the outlet of the feed pump 5 and the inlet of the homogenizer and / or Dispersing device 6 .
- this entry device 9 can be used for adding liquid or powdery substances which are added to the product stream, which leaves the feed pump 5, before the product stream enters the homogenizing and / or dispersing device 6.
- a product discharge 10 can be provided, via which an emptying can take place.
- a further product discharge 11 is connected to the outlet of the homogenizing and / or dispersing device 6 and also permits emptying via corresponding valve controls.
- FIG. 1 an external circulation and / or an internal circulation of the product stream leaving the homogenizing and / or dispersing device 6 are removed.
- An external circulation line 12 leads from the outlet side of the homogenizing and / or dispersing device 6 back to the interior of the container 2, wherein an introduction into the container 2 preferably takes place above the level of the material template in the container 2.
- an internal circulation line 13 is connected on the outlet side to the homogenizing and / or dispersing device 6, which preferably returns the product stream to the vicinity of the container outlet 4 in the radial direction.
- a sensor 14 is further arranged between the feed pump 5 and the homogenizing and / or dispersing device 6, which is preferably a pressure sensor. Alternatively, it may be a volume flow dependent operating sensor or the like if necessary.
- this sensor 14 detects the pressure of the product flow in the material flow direction in front of the inlet side of the homogenizing and / or dispersing device 6. If this sensor 14 detects, for example, negative pressure conditions, the entry device 9 can be activated for pulverulent or liquid substances without the There is a risk that the introduced via the entry device 9 additives strike back into the interior of the container 2.
- the sensor 14 also serves to control the independent drive motors 7 and 8 for the feed pump 5 and the homogenizing and / or dispersing device 6. With the help of this sensor 14, these motors 7 and 8 are also controlled so that they are controlled to each other the flow properties of the material template and the product flow, the product flow promotion to the homogenizing and / or dispersing device 6 always takes place under pre-pressure. As a result, cavitation phenomena can be effectively avoided.
- Registered pump 5 is designed as a centrifugal pump, which may have, for example, a tangential outlet which communicates with the inlet side of the homogenizing and / or dispersing device 6 in communicating connection.
- a centrifugal pump as a feed pump 5 allows a low-shear promotion of the product flow from the container outlet 4. Therefore, such a centrifugal pump is particularly advantageous for shear-sensitive substances.
- the in FIG. 1 shown device is operated with internal circulation, it may be advantageous if the product flow does not pass through the homogenizing and / or dispersing device 6 several times, but that a product discharge via the product discharge 10 in FIG. 1 is made. In this case, then the feed pump 5 is driven in the form that it allows a product discharge.
- Essential in the device 1 according to the invention for homogenizing and / or dispersing flowable substances is the fact that the feed pump 5 and the homogenizing and / or dispersing device 6 are driven by separate drive motors 7 and 8, so that these two organs are independently operable , With the help of the sensor 14 but it is ensured that in particular the feed pump 5 is always operated so that the product flow to the inlet side of the homogenizing and / or dispersing device 6 is always conveyed under a certain variable form.
- the device 1 of the invention allows for homogenizing and / or dispersing flowable substances a universally controllable product flow line within the system optionally in conjunction with an external and / or an internal circulation.
- the feed pump 5 and the homogenizing and / or dispersing 6 form a compact unit, so that you get a space-saving design of the device 1 total, which is designed to be easy to maintain.
- the sensor 14 operatively cooperate with the motors 7 and 8 associated frequency converters such that not only the individual drive parameters of feed pump 5 and homogenizing and / or dispersing 6 are variable and independently controllable, but that under ensures all variable operating conditions that the feed pump 5 provides a pressurized product stream at the inlet side of the homogenizing and / or dispersing device 6. Also, a mutual vote of the delivery rate of the feed pump 5 and the residence time in the shear zone of the homogenizing and / or dispersing device 6 is possible, so that you can make an energy density adjustment to optimize the process control.
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Civil Engineering (AREA)
- Structural Engineering (AREA)
- Dispersion Chemistry (AREA)
- Treatment Of Fiber Materials (AREA)
- Confectionery (AREA)
Claims (12)
- Dispositif d'homogénéisation et/ou de dispersion de matières coulantes, en particulier liquides ou pâteuses (présentation des matières), dispositif qui comprend un récipient (2) pour présenter la matière et un dispositif d'homogénéisation et/ou de dispersion entraîné par moteur (6), la matière présentée étant transportée d'une sortie de récipient (4) au moyen d'une pompe d'alimentation (5) au dispositif d'homogénéisation et/ou de dispersion (6), auquel sont associés des dispositifs de chargement (9) d'additifs de forme liquide ou poudreuse, le dispositif d'homogénéisation et/ou de dispersion (6) permettant, côté sortie, un refoulement vers le récipient (2),
caractérisé en ce que la pompe d'alimentation (5) est entraînée séparément du dispositif d'homogénéisation et/ou de dispersion (6), en ce qu'un capteur de pression (14) est disposé entre la sortie de la pompe et le côté entrée du dispositif d'homogénéisation et/ou de dispersion, capteur qui commande l'entraînement séparé (8) de la pompe d'alimentation (5) de manière variable conformément aux aptitudes à l'écoulement de la matière présentée et/ou conformément à des paramètres de processus correspondants de telle sorte que le transport du courant de matière vers le dispositif d'homogénéisation et/ou de dispersion (6) a toujours lieu sous pression d'admission. - Dispositif suivant la revendication 1,
caractérisé en ce qu'une dérivation de matière (10) pouvant être ouverte et fermée, dans la direction du courant de matière est disposée en amont, côté entrée du dispositif d'homogénéisation et/ou de dispersion (6). - Dispositif suivant la revendication 1 ou 2,
caractérisé en ce que la pompe d'alimentation (5) est une pompe centrifuge. - Dispositif suivant une des revendications 1 à 3,
caractérisé en ce que la pompe d'alimentation (5) présente une sortie tangentielle, qui est reliée au côté entrée du dispositif d'homogénéisation et/ou de dispersion (6). - Dispositif suivant une des revendications 1 à 4,
caractérisé en ce que le refoulement du courant de matière a lieu depuis le côté sortie du dispositif d'homogénéisation et/ou dispersion (6) vers une zone proche de la sortie du récipient (4) et/ou vers la zone supérieure du récipient (2), de préférence, au-dessus du niveau de matière présentée. - Dispositif suivant une des revendications 1 à 4,
caractérisé en ce qu'un organe d'agitation (3) à débit axial et/ou radial est disposé dans le récipient (6). - Dispositif suivant une des revendications 1 à 6,
caractérisé en ce que l'entraînement (7) pour le dispositif d'homogénéisation et/ou de dispersion (6) et l'entraînement (8) pour la pompe d'alimentation (5) sont commandés au moyen de convertisseurs de fréquence. - Dispositif suivant une des revendications précédentes,
caractérisé en ce que le rendement de la pompe d'alimentation (5) et le rendement du dispositif d'homogénéisation et/ou de dispersion (6) peuvent être variés indépendamment l'un de l'autre. - Dispositif suivant une des revendications 1 à 8,
caractérisé en ce que les directions de chargement (9) des additifs de forme liquide ou poudreuse sont activées, lorsque le capteur (14), qui est en particulier conçu comme capteur de pression, capte des conditions de vide. - Dispositif suivant une des revendications 1 à 9,
caractérisé en ce que le temps de séjour dans la zone de cisaillement du dispositif d'homogénéisation et/ou de dispersion (6) est réglé ou varié par le rendement (nombre de tours) de la pompe d'alimentation (5), afin d'accorder les densités de flux d'énergie. - Dispositif suivant une des revendications précédentes,
caractérisé en ce que la pompe d'alimentation (5) et le dispositif d'homogénéisation et/ou de dispersion (6) forment une unité modulaire compacte, laquelle est, en particulier, fixée sur le récipient (2) au moyen d'une collerette. - Dispositif suivant une des revendications précédentes,
caractérisé en ce qu'un dispositif de commande est prévu, qui règle automatiquement la pompe d'alimentation (5) sur des conditions de pression d'alimentation, de préférence en fonction du nombre de tours du dispositif d'homogénéisation et/ou de dispersion (6).
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102005017075A DE102005017075A1 (de) | 2005-04-13 | 2005-04-13 | Vorrichtung zum Homogenisieren und/oder Dispergieren fliessfähiger Stoffe |
Publications (3)
Publication Number | Publication Date |
---|---|
EP1712271A2 EP1712271A2 (fr) | 2006-10-18 |
EP1712271A3 EP1712271A3 (fr) | 2007-10-24 |
EP1712271B1 true EP1712271B1 (fr) | 2008-11-19 |
Family
ID=36676585
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP06006605A Not-in-force EP1712271B1 (fr) | 2005-04-13 | 2006-03-29 | Dispositif pour homogénéiser et/ou disperser des matériaux fluides |
Country Status (4)
Country | Link |
---|---|
US (1) | US20060233042A1 (fr) |
EP (1) | EP1712271B1 (fr) |
AT (1) | ATE414565T1 (fr) |
DE (2) | DE102005017075A1 (fr) |
Families Citing this family (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE602006011824D1 (de) * | 2005-07-07 | 2010-03-11 | Rohm & Haas | Verfahren zur Herstellung von Schlämmen |
US20070189112A1 (en) * | 2006-02-16 | 2007-08-16 | Sandra Knape | Procedure and device for homogenizing |
DE202006008820U1 (de) | 2006-06-03 | 2006-08-17 | Frymakoruma Ag | Homogenisator-Vorrichtung mit horizotal gelagerten Zahnkränzen |
DE202007004912U1 (de) * | 2007-04-03 | 2007-07-26 | Blum, Holger | Vorrichtung zur Behandlung von Ballastwasser mit wässriger Acroleinlösung |
DE102008011253A1 (de) * | 2008-02-27 | 2009-09-10 | SÜDDEKOR GmbH | System und Verfahren |
DE102008045820A1 (de) | 2008-09-05 | 2010-04-08 | Axel Wittek | Übergangselemente zum Überleiten einer Dispersion bei der Behandlung in einer Rotor-Stator-Dispergiermaschine |
JP2011036862A (ja) * | 2010-08-05 | 2011-02-24 | Sintokogio Ltd | 循環式分散システム及び循環式分散方法 |
CN105026026A (zh) * | 2013-03-01 | 2015-11-04 | 利乐拉瓦尔集团及财务有限公司 | 液体处理混合器及方法 |
CN103933883B (zh) * | 2014-04-03 | 2016-05-18 | 符向东 | 压滤精煤均质化系统及方法 |
EP3838389A1 (fr) * | 2019-12-16 | 2021-06-23 | Sika Technology Ag | Dispositif d'incorporation des matières pulvérulentes, en particulier des matières pulvérulentes explosives de poussière, dans un liquide, en particulier facilement inflammable |
CN111229086A (zh) * | 2020-03-01 | 2020-06-05 | 天伟化工有限公司 | 聚氯乙烯糊树脂生产中聚合乳化剂的配置系统及其控制方法 |
Family Cites Families (25)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2148608A (en) * | 1936-11-20 | 1939-02-28 | Stubner Emile C De | Dispersion apparatus |
GB702811A (en) * | 1951-04-02 | 1954-01-20 | Giovanola Freres Sa | Apparatus for the cavitation treatment of liquids |
US3285331A (en) * | 1964-05-21 | 1966-11-15 | Bratland Arthur | Combined mixing and homogenising apparatus |
US4096586A (en) * | 1976-03-04 | 1978-06-20 | Societe D'assistance Technique Pour Produits Nestle S.A. | Solubilization of casein |
US4664528A (en) * | 1985-10-18 | 1987-05-12 | Betz Laboratories, Inc. | Apparatus for mixing water and emulsion polymer |
US4823987A (en) * | 1986-04-28 | 1989-04-25 | Ryco Graphic Manufacturing, Inc. | Liquid mixing system and method |
US5114239A (en) * | 1989-09-21 | 1992-05-19 | Halliburton Company | Mixing apparatus and method |
US5087864A (en) * | 1989-10-30 | 1992-02-11 | Abel Manufacturing Co., Inc. | Apparatus for selectively controlling a plurality of electric motors |
US5240380A (en) * | 1991-05-21 | 1993-08-31 | Sundstrand Corporation | Variable speed control for centrifugal pumps |
DE4135648C1 (en) * | 1991-10-29 | 1993-05-13 | Erich Netzsch Gmbh & Co Holding Kg, 8672 Selb, De | Mixing powdered solid into liq. phase e.g. for paint mfr. |
US5590960A (en) * | 1993-11-04 | 1997-01-07 | E. I. Du Pont De Nemours And Company | One tank paint makeup process using a recirculation loop with liquid injection |
US5571281A (en) * | 1996-02-09 | 1996-11-05 | Allen; Thomas E. | Automatic cement mixing and density simulator and control system and equipment for oil well cementing |
US6048391A (en) * | 1996-09-27 | 2000-04-11 | Serco Holland | Means for and methods of preparing a glue for corrugated board |
CA2220972C (fr) * | 1996-11-29 | 1999-03-09 | Canadian Fracmaster Ltd. | Homogeneisateur/technologie de melange a vitesse de cisaillement elevee pour l'hydratation a la volee des liquides de fracturation et le melange a la volee des laitiers de ciment |
DE19738085C1 (de) * | 1997-09-01 | 1998-12-03 | Basf Ag | Verfahren zur Herstellung von Feststoffen durch Fällung |
DE20002920U1 (de) * | 2000-02-18 | 2000-04-20 | Schröder & Boos Misch- und Anlagentechnik GmbH & Co. KG, 27578 Bremerhaven | Homogenisator |
JP4156191B2 (ja) * | 2000-11-22 | 2008-09-24 | 株式会社小松製作所 | エマルジョン製造装置 |
US6663349B1 (en) * | 2001-03-02 | 2003-12-16 | Reliance Electric Technologies, Llc | System and method for controlling pump cavitation and blockage |
US6655922B1 (en) * | 2001-08-10 | 2003-12-02 | Rockwell Automation Technologies, Inc. | System and method for detecting and diagnosing pump cavitation |
DE10255514A1 (de) * | 2002-11-27 | 2004-06-09 | Endress + Hauser Gmbh + Co. Kg | Druckregelverfahren zur Vermeidung von Kavitationen in einer verfahrenstechnischen Anlage |
DE10320739B3 (de) * | 2003-05-09 | 2004-10-21 | Ika - Werke Gmbh & Co. Kg | Vorrichtung zum Dispergieren und/oder Homogenisieren |
US7144148B2 (en) * | 2004-06-18 | 2006-12-05 | General Electric Company | Continuous manufacture of high internal phase ratio emulsions using relatively low-shear and low-temperature processing steps |
US20070025178A1 (en) * | 2005-07-27 | 2007-02-01 | Xerox Corporation | Pigment dispersions and preparation method thereof |
US20070189112A1 (en) * | 2006-02-16 | 2007-08-16 | Sandra Knape | Procedure and device for homogenizing |
US7448795B2 (en) * | 2006-10-23 | 2008-11-11 | Wenger Manufacturing, Inc. | Preconditioner having mixer shafts independently driven with variable frequency drives |
-
2005
- 2005-04-13 DE DE102005017075A patent/DE102005017075A1/de not_active Withdrawn
-
2006
- 2006-03-29 EP EP06006605A patent/EP1712271B1/fr not_active Not-in-force
- 2006-03-29 DE DE502006002095T patent/DE502006002095D1/de active Active
- 2006-03-29 AT AT06006605T patent/ATE414565T1/de not_active IP Right Cessation
- 2006-04-13 US US11/279,679 patent/US20060233042A1/en not_active Abandoned
Also Published As
Publication number | Publication date |
---|---|
DE102005017075A1 (de) | 2006-10-19 |
EP1712271A3 (fr) | 2007-10-24 |
US20060233042A1 (en) | 2006-10-19 |
ATE414565T1 (de) | 2008-12-15 |
DE502006002095D1 (de) | 2009-01-02 |
EP1712271A2 (fr) | 2006-10-18 |
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