EP2536487B1 - Dispositif de melange de maniere discontinue des composants additifs pour produits melanges - Google Patents

Dispositif de melange de maniere discontinue des composants additifs pour produits melanges Download PDF

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Publication number
EP2536487B1
EP2536487B1 EP10797996.5A EP10797996A EP2536487B1 EP 2536487 B1 EP2536487 B1 EP 2536487B1 EP 10797996 A EP10797996 A EP 10797996A EP 2536487 B1 EP2536487 B1 EP 2536487B1
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EP
European Patent Office
Prior art keywords
mixing
component
individual components
metering
tank
Prior art date
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Application number
EP10797996.5A
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German (de)
English (en)
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EP2536487A1 (fr
Inventor
Klaus Ehrlinger
Tobias Cherdron
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KHS GmbH
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KHS GmbH
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Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20—Mixing gases with liquids
    • B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/236—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids specially adapted for aerating or carbonating beverages
    • B01F23/2363—Mixing systems, i.e. flow charts or diagrams; Arrangements, e.g. comprising controlling means
    • 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
    • B01F23/49—Mixing systems, i.e. flow charts or diagrams
    • 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
    • B01F33/84—Mixing plants with mixing receptacles receiving material dispensed from several component receptacles, e.g. paint tins
    • 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
    • B01F33/84—Mixing plants with mixing receptacles receiving material dispensed from several component receptacles, e.g. paint tins
    • B01F33/846—Mixing plants with mixing receptacles receiving material dispensed from several component receptacles, e.g. paint tins using stored recipes for determining the composition of the mixture to be produced, i.e. for determining the amounts of the basic components to be dispensed from the component 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
    • B01F35/71—Feed mechanisms
    • B01F35/717—Feed mechanisms characterised by the means for feeding the components to the mixer
    • B01F35/7173—Feed mechanisms characterised by the means for feeding the components to the mixer using gravity, e.g. from a hopper
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/71—Feed mechanisms
    • B01F35/717—Feed mechanisms characterised by the means for feeding the components to the mixer
    • B01F35/7176—Feed mechanisms characterised by the means for feeding the components to the mixer using pumps
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/71—Feed mechanisms
    • B01F35/717—Feed mechanisms characterised by the means for feeding the components to the mixer
    • B01F35/718—Feed mechanisms characterised by the means for feeding the components to the mixer using vacuum, under pressure in a closed receptacle or circuit system
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/71—Feed mechanisms
    • B01F35/717—Feed mechanisms characterised by the means for feeding the components to the mixer
    • B01F35/71805—Feed mechanisms characterised by the means for feeding the components to the mixer using valves, gates, orifices or openings
    • 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
    • B01F35/80—Forming a predetermined ratio of the substances to be mixed
    • B01F35/88—Forming a predetermined ratio of the substances to be mixed by feeding the materials batchwise
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F2101/00—Mixing characterised by the nature of the mixed materials or by the application field
    • B01F2101/305—Treatment of water, waste water or sewage
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20—Mixing gases with liquids
    • B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/237—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids characterised by the physical or chemical properties of gases or vapours introduced in the liquid media
    • B01F23/2376—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids characterised by the physical or chemical properties of gases or vapours introduced in the liquid media characterised by the gas being introduced
    • B01F23/23762—Carbon dioxide
    • B01F23/237621—Carbon dioxide in beverages

Definitions

  • the invention relates to a device according to the preamble of claim 1.
  • a base component e.g., water
  • at least one of e.g. flavoring and / or coloring and / or preserving additive component which in turn is prepared by mixing several individual components
  • methods and mixing plants are known, which are also referred to as a mixer and u.a. a plant component, e.g. a tank for degassing the base component (water), one or more metered additions and / or mixing lines for metered mixing of the at least one additional component, a device for carbonizing the consisting of the main component and the at least one additional component mixed product and a device for buffering the mixed product.
  • the additional component which is also referred to as syrup in the case of beverages, is usually premixed in a separate pre-mixing chamber (also syrup) from the individual components and then mixed in the mixing device with the degassed main component (water) or diluted with this main component to the final concentration ,
  • Such a device has been exemplified by the DE 2 220 224 B1 known.
  • This document provides that components are conveyed to or after the mixing by the effect of negative and / or pressure from one tank to the next. This approach is expensive because of the high cost of generating negative pressure.
  • a disadvantage of this method is a significant design effort, since for each component a separate Dosierstrang u.a. with flow vessel, with level measurement, with inlet control, with pump, with flow meter, with flow control valve etc. required.
  • Another disadvantage is that by the metered addition of the individual components continuously or constantly working pumps undesired heating of the individual components, especially those of individual components, which are present as small components only with a small mass or proportion in the final product. This warming can lead to significant product damage.
  • a further disadvantage of known methods for in-line metering is that a frequently assured, ie redundant, measurement of the metered individual components, ie in particular control and / or verification of the measured values of metering devices used for metering (bulk metering), is often desired. and / or volumetric flow meter) and / or scales as well as inline control measurement methods for detecting erroneous measurements or dosages are not possible or very complicated.
  • the object of the invention is to provide a device with which the investment cost of an entire system for producing mixed products, especially mixed drinks is substantially reduced. To solve this problem, a device according to the patent claim 1 is formed.
  • a general feature of the invention is that the device for mixing or producing the respective additional component from its individual components is an integral part of the mixing device or the mixer, in which the admixing of this additional component to the basic or main component (eg water) , Alone through this training results in a significant reduction in the investment volume of an entire system by eliminating a separate premix or syrup room and the local facilities.
  • the basic or main component eg water
  • the additional component e.g. when mixed products in the form of drinks, it is, for example, a flavoring and / or coloring and / or preserving component.
  • a special feature of the invention further consists in that only one single batch tank is provided for blending the additional component from the individual components into which all individual components required for the respective formulation are metered during each metering cycle and preferably introduced at least partially one after the other.
  • the individual components or the additional component composed thereof are discharged into the buffer tank via a fluid connection, in free fall, so that intensive mixing of the individual components takes place already in the fluid connection.
  • "batchwise blending of the additional components” is thus to be understood as meaning that at least all the individual components forming the respective additional component are metered into each metering cycle the batch tank are introduced and that this batch tank is then emptied into the mixing and buffer tank.
  • the in the Fig. 1 generally designated 1 (mixer) is used to produce mixed products in the form of drinks by mixing a liquid base component GK, namely usually water, with an additional component ZK (blended syrup), which as flavoring and / or coloring and / or preserving Component in turn is produced by mixing several individual components K1 - K5, as well as for carbonizing and buffering the respective mixed product.
  • GK liquid base component
  • ZK biended syrup
  • the mixing device 1 can be functionally subdivided into a plurality of device or plant sections 1.1 - 1.4, of which the section 1.1 for the treatment of the basic component GK or of the water by degassing and the Plant section 1.2 for the metered admixing of one or more additional components ZK to the basic component GK and the system section 1.3 for providing the additional component ZK by mixing this component from the individual components K1 - K5 according to the respective prescribed recipe.
  • the section 1.4 is used for carbonization and intermediate storage of the mixed product.
  • the plant section 1.1 essentially comprises a tank 2 to which the water is supplied in the required amount during operation of the mixing device 1, in such a way that the tank 2 is partially filled with the basic component GK, so that in the tank 2, a lower liquid space 2.1 and lying above a gas space 2.2 are formed.
  • the gas space 2.2 is for the degassing of the basic component GK via a line 3 with a vacuum source (vacuum pump) in combination.
  • the tank 2 Via a basic component GK and then the mixing product leading line 4, the tank 2 is connected to a buffer tank 5, which communicates via a product line 6 with a filling machine, not shown, for filling the mixed product or beverage in bottles or in other containers.
  • a connecting valve 7 via which a concentrated aqueous sugar solution (eg 70% sugar solution) can be introduced into the basic component GK for sweetening the mixed product, as well as a another connection valve 8 is provided, via which the additional component ZK is introduced into the basic component GK.
  • a concentrated aqueous sugar solution eg 70% sugar solution
  • the line 4 in a line section in front of the buffer tank 5 a Karbonmaschinesumble, which is indicated in the figure with the arrow 9 and in the inter alia, a flow meter 10 and following this, a flow control valve 11 in the line 4 is provided are.
  • a CO 2 line 12 which with a CO2 gas pressurized, not shown, CO2 source is connected and in which a flow meter for measuring the line 12 flowing through the amount of CO2 gas and a metering valve CO2 14 are provided.
  • Control electronics not shown controls, taking into account the measurement signals of the flow meter 10 and 13, for example, the metering valve CO2 14 in the form that after in-line carbonation or after the Karbonmaschinesumble 9, the mixed product has the required or predetermined CO2 content.
  • a line 15 is provided which communicates with a source for providing the sugar concentrate and in which a flow meter 16, a metering valve sugar / large component 17, the connection valve 7 and a lock - or drain valve 18 are provided, with which the other end of the line 15 can be opened and closed to a sequence 18.1 and which is of course during the admixture of the sugar to the basic component GK in the closed state, but for example, for rinsing or cleaning the Line 15 is opened.
  • the liquid sugar can also be metered in section 1.3, for example, as a single component K5.
  • the system section 1.3 in which the metered mixing of the additional component ZK from the individual components K1 - K4 takes place, comprises, inter alia, two metering lines 19 and 20, of which the metering line 19 has a plurality of separate connections for the individual components K1 - K4 each formed by a separate valve 21 ,
  • the individual components K1 - K4 are, for example, small components which are contained in the additional component ZK possibly with a small mass or proportion and of which, for example, the individual component K1 may also be water, preferably degassed water from the tank 2.
  • the metering line 20 has a port formed by the valve 22 for supplying the single component K5, which is a large component, i. a component which is contained in the additional component ZK with the largest mass or proportion.
  • the metering 19 and 20 flow meters 23 and 24 (mass and / or volumetric flow meter) are provided. Furthermore, in the metering 20 in the flow direction in front of the local flow meter 24, for example, a metering and delivery pump 25 is provided.
  • the two metering lines 19 and 20 are connected in the flow direction of the components K1 - K5 to the flow meter 23 and 24 via valves 26 to a main line 27, which in turn a lower inlet and outlet of a collection or batch tank 28 with a below this container arranged mixing and buffer tank 29 for the additional component ZK connects.
  • a check valve 30 is further provided, between the connection of the lines 20 and 27 and the mixing and buffer tank 29th
  • the additional component ZK leading line 31 is connected in the starting from the mixing and buffer memory 29, a metering or circulation pump 32, a flow meter 33 (mass and / or volume flow meter), a metering valve Concentrates 34, the connecting valve 8 and a locking or drain valve 35 are arranged, with which the mixing and buffer memory 29 remote end of the line 31 can be closed or opened to a sequence 35.1 out.
  • the delivery rate of the dosing or circulating pump 32 is adjusted so that the volume flow generated by this pump is greater than the maximum amount of additive component ZK to be admixed to the basic component GK.
  • the unnecessary subset of the additional component ZK is returned to the mixing and buffer tank 29.
  • the mixing of the Additional component ZK to the basic component GK takes place when the connection valve 8 is opened by activating the metering valve concentrates 34 from the control electronics as a function of the signals from the flow meter 33 and a further flow meter provided in the line 4, for example the flowmeter 10.
  • the peculiarity of the mixing device 1 consists in the system components serving for blending the additional component ZK and the special control of the blending process.
  • the latter takes place in such a way that in the respective metering cycle the individual components K1-K5 are metered one after the other or introduced into the batch tank 28 as a function of the measuring signals of the flow meters 23 and 24 in the batch tank 28 corresponding to the respective recipe, namely at least for one of the components K1 - K4 for gentle treatment by suction with negative pressure.
  • the batch tank 28 is connected via a vacuum regulating valve 37 having a vacuum line 36 to the gas space 2.2 of the tank 2, u.a. with the advantage that an additional vacuum source is not required and in particular aroma losses or losses of individual components are avoided, since these are washed out again in the tank 2 and thus ultimately fed into the mixed product.
  • one of the individual components K1 - K4 is water, so that by briefly opening the associated valve 21 of this component a separating "water plug" through the lines 19 and 27 can be funded in the batch tank 28.
  • the metered introduction of the component K5 in the batch tank 28 is carried out with the pump 25 and possibly supported by negative pressure. Basically, however, it is possible to dispense with the pump 25 and also introduce the individual component K5 dosed into the batch tank 28 by suction.
  • the use of a separate metering line 20 for the larger individual component K5 has the advantage that u.a.
  • the metering of the smaller individual components K1 - K4 can be done with higher accuracy, Furthermore, there is the possibility that the dosage of the individual component K5 performed in parallel with the metering of the individual components K1 - K4 by the use of the metering line 20 can be.
  • the contents of this container is emptied by blocking the valves 26 and opening the valve 30 into the mixing and buffer tank 29.
  • the arrangement is such that after the opening of the valve 30, the contents of the batch tank 28, the trunk line 27 in free fall or flow, can flow through and this is already a mixing of the individual components.
  • the trunk line 27 is designed for this purpose with a correspondingly large cross-section.
  • the batch tank 28 is brought to ambient pressure by opening a venting valve 38. It is also possible to pressurize the batch tank 28 for accelerated evacuation.
  • the batch tank 28 with means which enable a redundancy measurement and / or redundant checking of the metering of the individual components and, in particular, also of the smaller individual components K1-K4.
  • a further flow meter and / or a level measurement 39 is provided at the inlet / outlet of the batch tank 28 and / or the batch tank 28 is equipped with a weighing device, with then also introduced into the batch tank 28 amounts of the individual components K1 - K5 can be determined for a redundancy measurement.
  • a level measurement of Flosstechniksspiegels in batch tank 28 is possible.
  • individual sectors of the bakery tank 28 may be formed with different diameters, as shown in the figure.
  • the redundancy measurement can be used in all cycles for all Single components K1 - K5 are performed. To save time, but this can also be done at intervals, for example, per batch or cycle only for the first introduced individual component, the temporal order of introducing the individual components in the batch tank 28 is arbitrarily or rotationally changing selected.
  • the batch tank 28 has a reduced volume, so that very short cycle times, for example cycle times of less than five minutes, can be achieved for the respective metering cycle consisting of the metering phase and the emptying of the batch tank 28 into the mixing and buffer tank 29.
  • the interior of the mixing and buffer tank 29 is preferably designed, for example, divided by dividing sheets, that it has a ridge-first-in / first-out characteristic and in this tank by the return of the partial flow via the line 31.1 the mixing of the individual components is further increased, so that with suitable products for complete mixing of the additional component ZK mechanically moving mixing and / or stirring elements are not required.
  • connection valves 7 and 8 are preferably designed as cross valves, with the in the Fig. 2 schematically illustrated training, in the open state (position b of Fig. 2 ) the connection between the line 16 and 31 and the line 4 consists. In the closed state of the respective connection valve 7 or 8 (position a of Fig. 2 Not only is this connection blocked, but it is also possible, for example, during a working cycle of the mixing device 1, in which the connection is not needed, the line 16 and 31 to flush after opening the drain valve 18 and 35 respectively.
  • the additional component ZK for the next product batch can already be prepared in the batch tank 28 during the emptying of the mixing and buffer tank 29 according to the new formulation and then after the complete Emptying or emptying the mixing and buffer tank 29 are drained into this.
  • mixing products of the basic component GK and of at least one individual component K1-K5 can be prepared in the respectively required formulation, all individual components K1-K5 being available at the corresponding connections of the metering lines 19 and 20 by controlled opening of the valves 21 and 22, however, only those individual components K1 - K5 are introduced into the batch tank 28, which are actually required for the current formulation.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Accessories For Mixers (AREA)

Claims (10)

  1. Dispositif servant à mélanger par lots des composants additifs (ZK) composés de composants individuels (K1 - Kn) pour des produits mélangés contenant lesdits composants additifs (ZK) ainsi que servant à tamponner le composant additif (ZK) respectif, sachant que ledit dispositif fait partie intégrante d'un mélangeur servant à obtenir les produits mélangés en mélangeant au moins un composant additif (ZK) et au moins un composant de base (GK) et qu'il présente un seul réservoir à lots (28), qui est relié aux raccordements fournissant les composants individuels (K1 - Kn) afin d'introduire de manière dosée les composants individuels (K1 - K5) par l'intermédiaire de soupapes de commande et/ou de dosage (21, 22, 26) et à un réservoir de mélange et de tamponnage (29) destiné au composant additif (ZK) respectif mélangé afin de tamponner le composant additif (ZK) mélangé, caractérisé en ce que le réservoir de mélange et de tamponnage (29) est disposé sur un niveau en dessous du réservoir à lots (28), et en ce que le dispositif est réalisé de telle manière que les composants individuels (K1 - K5) provenant du réservoir à lots (28) peuvent être évacués, en chute libre, dans le réservoir de mélange et de tamponnage (29) par l'intermédiaire d'un raccord pour liquide de manière à donner lieu, déjà dans le raccord pour liquide, à un mélange des composants individuels.
  2. Dispositif selon la revendication 1, caractérisé en ce que le dispositif est réalisé en vue d'un refoulement des composants individuels (K1 - Kn) dans le réservoir à lots (28) par le vide ou par une dépression et/ou en vue d'un refoulement assisté par le vide des composants individuels (K1 -Kn) dans le réservoir à lots (28).
  3. Dispositif selon la revendication 1 ou 2, caractérisé en ce que le dispositif est réalisé en vue d'une introduction décalée dans le temps d'au moins une partie des composants individuels (K1 -Kn) respectivement requis au cours d'un cycle de dosage, et en ce qu'à cet effet, de manière préférée, les raccordements, présentant respectivement une soupape (21), d'au moins deux composants individuels (K1 - K4) sont prévus au niveau d'une conduite de dosage (19) commune servant à introduire de manière dosée et de manière décalée dans le temps lesdits composants individuels (K1 - K4) dans le réservoir à lots (28).
  4. Dispositif selon l'une quelconque des revendications précédentes, caractérisé en ce qu'une conduite de dosage (20) autonome est attribuée à au moins un composant individuel (K5), de préférence à au moins un composant individuel (K5), qui forme, dans le composant additif (ZK) mélangé, la fraction la plus importante en comparaison avec les autres composants individuels.
  5. Dispositif selon l'une quelconque des revendications précédentes, caractérisé par un circuit englobant un système de stockage de mélange et de tamponnage (29) et présentant une pompe de dosage ou de recirculation (32), destinée au composant additif (ZK), sachant que la pompe de dosage ou de recirculation (32) est de manière préférée une pompe du type servant à refouler le composant additif (ZK) au niveau d'une ligne de mélange ou d'un poste de mélange (8) afin de mélanger le composant additif au composant de base ou principal (GK).
  6. Dispositif selon l'une quelconque des revendications précédentes, caractérisé en ce qu'une entrée et une sortie du réservoir à lots (28) sont reliées, par l'intermédiaire d'un raccord pour liquide (27, 30) commandé, au réservoir de mélange et de tamponnage (29), et en ce que l'acheminement dosé des composants individuels (K1 - K5) dans le réservoir à lots (28) au cours du cycle de dosage respectif ainsi que l'évacuation des composants individuels (K1 - K5) hors du réservoir à lots (28) se font à l'issue du cycle de dosage respectif par l'intermédiaire du raccord pour liquide (27, 30) commandé.
  7. Dispositif selon l'une quelconque des revendications précédentes, caractérisé par des moyens (23, 24) servant à détecter et/ou à mesurer la quantité respectivement introduite au cours d'un cycle de dosage dans le réservoir à lots (28), de chaque composant individuel (K1 - K5), sachant qu'en cas d'utilisation au moins d'une conduite de dosage (19, 20), lesdits moyens sont obtenus par un système de mesure disposé dans la conduite de dosage (19, 20), par exemple se présentant sous la forme d'un débitmètre (23, 24).
  8. Dispositif selon l'une quelconque des revendications précédentes, caractérisé en ce que le réservoir à lots (28) comprenant un système de mesure autonome servant à détecter et/ou à mesurer la quantité d'au moins un composant individuel introduit, au cours du cycle de dosage respectif, dans le réservoir à lots (28).
  9. Dispositif selon l'une quelconque des revendications précédentes, caractérisé en ce que la dépression en vue du refoulement des composants individuels (K1 - K5) dans le réservoir à lots (28) est prélevée d'un élément fonctionnel (2), servant au dégazage du composant de base ou principal (GK), du mélangeur (1), et en ce qu'à cet effet l'espace intérieur du réservoir à lots (28) est en liaison, de manière préférée par l'intermédiaire d'un raccord (36, 37) commandé, avec un espace intérieur (2.2) du composant d'installation (2) servant au dégazage.
  10. Dispositif selon l'une quelconque des revendications précédentes, caractérisé en ce que le réservoir de mélange et de tamponnage (29) est en liaison, par l'intermédiaire d'une soupape de raccordement (8) réalisée de préférence sous la forme d'une soupape croisée, avec le poste de mélange ou la ligne de mélange aux fins du mélange avec le composant principal ou de base (GK).
EP10797996.5A 2010-02-16 2010-12-07 Dispositif de melange de maniere discontinue des composants additifs pour produits melanges Active EP2536487B1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102010008165A DE102010008165A1 (de) 2010-02-16 2010-02-16 Vorrichtung zum Ausmischen der, einer Grund- oder Hauptkomponente beizumischenden Zusatzkomponenten eines Mischproduktes
PCT/EP2010/007408 WO2011101011A1 (fr) 2010-02-16 2010-12-07 Dispositif de mélange du composant additif à incorporer à un composant de base ou principal d'un produit mélangé

Publications (2)

Publication Number Publication Date
EP2536487A1 EP2536487A1 (fr) 2012-12-26
EP2536487B1 true EP2536487B1 (fr) 2015-08-12

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EP10797996.5A Active EP2536487B1 (fr) 2010-02-16 2010-12-07 Dispositif de melange de maniere discontinue des composants additifs pour produits melanges

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US (1) US9364801B2 (fr)
EP (1) EP2536487B1 (fr)
DE (1) DE102010008165A1 (fr)
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CN117920015A (zh) * 2024-03-20 2024-04-26 上海复迪源码生物技术有限公司 用于制备纳米制剂的制备系统及控制方法

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DE102010008165A1 (de) 2011-08-18
US20120236682A1 (en) 2012-09-20
WO2011101011A1 (fr) 2011-08-25
EP2536487A1 (fr) 2012-12-26
US9364801B2 (en) 2016-06-14

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