EP2504084A2 - Procédé et dispositif de fabrication d'un produit mixte, notamment d'une boisson mixte - Google Patents

Procédé et dispositif de fabrication d'un produit mixte, notamment d'une boisson mixte

Info

Publication number
EP2504084A2
EP2504084A2 EP10754688A EP10754688A EP2504084A2 EP 2504084 A2 EP2504084 A2 EP 2504084A2 EP 10754688 A EP10754688 A EP 10754688A EP 10754688 A EP10754688 A EP 10754688A EP 2504084 A2 EP2504084 A2 EP 2504084A2
Authority
EP
European Patent Office
Prior art keywords
base component
mixing chamber
component
mixed product
mixed
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.)
Granted
Application number
EP10754688A
Other languages
German (de)
English (en)
Other versions
EP2504084B1 (fr
Inventor
Klaus Ehrlinger
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.)
KHS GmbH
Original Assignee
KHS GmbH
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 KHS GmbH filed Critical KHS GmbH
Priority to SI201031530T priority Critical patent/SI2504084T1/sl
Priority to PL10754688T priority patent/PL2504084T3/pl
Publication of EP2504084A2 publication Critical patent/EP2504084A2/fr
Application granted granted Critical
Publication of EP2504084B1 publication Critical patent/EP2504084B1/fr
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

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
    • B01F23/232—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles
    • B01F23/2321—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles by moving liquid and gas in counter current
    • 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
    • B01F23/234—Surface aerating
    • 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
    • B01F23/234—Surface aerating
    • B01F23/2341—Surface aerating by cascading, spraying or projecting a liquid into a gaseous atmosphere
    • B01F23/23412—Surface aerating by cascading, spraying or projecting a liquid into a gaseous atmosphere using liquid falling from orifices in a gaseous atmosphere, the orifices being exits from perforations, tubes or chimneys
    • 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
    • B01F23/2362—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids specially adapted for aerating or carbonating beverages for aerating or carbonating within receptacles or tanks, e.g. distribution machines
    • 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
    • B01F23/70—Pre-treatment of the materials to be mixed
    • 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
    • B01F23/70—Pre-treatment of the materials to be mixed
    • B01F23/703—Degassing or de-aerating materials; Replacing one gas within the materials by another gas
    • 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
    • B01F35/2202—Controlling the mixing process by feed-back, i.e. a measured parameter of the mixture is measured, compared with the set-value and the feed values are corrected
    • 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
    • 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
    • B01F35/2212—Level of the material in the mixer
    • 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 method according to claim 1 and to a device according to claim 5 or 7, respectively for the production of icing products, e.g. consist as mixed drinks of at least one liquid base or base component and at least one of the base component dosed admixed additional component, which latter is a liquid additive component and / or a gaseous additive component in the form of a CO2 gas.
  • icing products e.g. consist as mixed drinks of at least one liquid base or base component and at least one of the base component dosed admixed additional component, which latter is a liquid additive component and / or a gaseous additive component in the form of a CO2 gas.
  • Processes and devices for producing mixed products in the form of mixed drinks and in particular also of carbonated or carbonated mixed drinks are known.
  • liquid base or base component e.g. of beverage water
  • degas e.g., water
  • at least one preferably flavor-forming additive component e.g., syrup
  • the mixed beverage is a carbonated beverage
  • carbonation and buffering of the mixed beverage with CO 2 gas also take place until it is filled into containers or bottles.
  • the preparation of such mixed products takes place in multi-component mixing plants, which are often referred to as a mixer.
  • the degassing of the at least one base component can be carried out in different ways, for example by a single or multi-stage vacuum degassing and / or by a single or multi-stage pressure degassing.
  • vacuum degassing the partial pressure gradient, which is necessary for the release of foreign gases dissolved in the at least one base component, is achieved by vacuum or pressure reduction.
  • pressure degassing the delivery of the Foreign gases from the respective base component obtained by diffusion into an oxygen and / or nitrogen-free carrier gas, eg C02 gas.
  • the mixing of the base component with the at least one additive component (e.g., syrup) to the finished or mixed product has heretofore been governed by a ratio control, i. by controlling the volume flows of the base component and the additional component to one setpoint in each case. Both setpoints are set in relation to the preselected or desired recipe.
  • a ratio control i. by controlling the volume flows of the base component and the additional component to one setpoint in each case. Both setpoints are set in relation to the preselected or desired recipe.
  • the carbonization or metering of the CO 2 gas also takes place in known processes and mixing plants via a ratio metering or via spray carbonization.
  • the mixed product is sprayed into a container pressurized with CO 2 gas.
  • the gas pressure is according to the u.a. set by the dosing rate and the temperature-dependent saturation pressure.
  • the CO 2 gas dissolves in the mixed product until a balance is achieved between the pressure of the CO 2 gas atmosphere and the CO 2 gas partial pressure or saturation pressure of the carbonated mixed beverage.
  • the carbonated mixed product or mixed beverage produced with the mixing plant is usually filled into containers or bottles with the aid of a filler.
  • the latter like the mixing plant, is part of a complete filling line. Due to disturbances in the environment and / or in the system and / or due to disruptions of the packaging material (eg bottle breakage, etc.), stops or reduced performance often occur.
  • known systems for uncoupling or buffering between mixing plant and filler require a buffer tank or tank which in known mixing plants has a relatively large volume, for example a volume up to 1000 liters got to.
  • Such buffer tanks are usually operated with a highly fluctuating level, so that the mixed product must be superimposed in the buffer tank with a C02 gas cushion, the pressure of which is higher than the CO 2 saturation pressure in the mixed product.
  • the level changes, it is necessary to add or remove the CO2 gas in the respective buffer tank, which leads to a high consumption of CO 2 gas.
  • the object of the invention is to provide a method for producing mixed products from at least one base component and at least one additional component, which can be carried out while maintaining a high dosing accuracy with a reduced control effort and / or mechanical complexity.
  • a method according to claim 1 is formed.
  • An apparatus for producing mixed products by mixing at least one base component with an additional component is the subject matter of claims 5 or 7.
  • the at least one base or base component is a liquid component.
  • the at least one additional component is a liquid and / or gaseous component, in the latter case CO 2 gas.
  • the metered admixing of the at least one preferably liquid additional component to the at least one liquid base component in the mixing chamber takes place in such a manner that the addition or metering of the at least one additional component is controlled or regulated as a function of the amount of the mixed product which is taken (quantity) from the mixing chamber.
  • means are preferably provided for level-controlled or volume-controlled tracking or refilling of the at least one base component to the mixing space, in such a way that the at least one base component and the at least one additional component are replaced or replenished by the at least one base component formed total volume in the mixing chamber is constant.
  • the metered addition of the at least one additional component in the mixing chamber can be carried out continuously or intermittently or batchwise.
  • the mixing chamber also forms the buffer memory, from which the mixed product is fed to the following in the overall systems filler. Since continuous operation is not required for mixing, the mixing space and thus also the reduced volume buffer or buffer tank formed by this mixing space can be carried out, for example with a volume of only 100 liters at a nominal capacity of the apparatus or mixing plant of 30 m 3 / h. Alone by the reduced volume of serving as a buffer tank mixing space results in a significant reduction in the size of the mixing plant according to the invention or apparatus for producing mixed products.
  • a common functional container for example, the functions of degassing and the subsequent carbonizing the at least one base component.
  • the functional container or a functional space formed in this then preferably also serves as a mixing chamber and preferably as a combined mixing chamber and buffer tank.
  • the height-level or volume-controlled tracking of the at least one base component into the mixing chamber is effected in the simplest case by virtue of the mixing space having at least one mixing chamber inlet for the at least one base component a filling height-determining element, for example in the form of an overflow, and means are to select the mixing chamber inlet. constantly during the operation of the mixing plant or device with the at least one base component to flow.
  • the mixing apparatus or apparatus is used to produce a carbonated, i.e. carbonated or co2 gasified liquid mixed product, preferably mixed beverage by mixing a liquid main or base component, for example water, with at least one liquid additive component, for example with a flavoring additive component, e.g. Syrup.
  • a liquid main or base component for example water
  • a flavoring additive component e.g. Syrup.
  • the single functional container 2 which usually has a mixing plant, namely the degassing or liberation of the base component (eg water) of unwanted, dissolved in this base component foreign gas constituents, the metered addition of CO 2 gas to the base component, for example, with an amount corresponding to the CO 2 saturation pressure of the mixed product, the metered feeding of the at least one additional component as well as the function of the buffer memory.
  • the base component eg water
  • the base component eg water
  • the partition wall 4 is provided in the illustrated embodiment with a central passage 5 which connects the subspaces 2.2 and 2.3 with each other and in the illustrated embodiment in the manner of one in the subspace 2.3 sufficient and immersion immersion tube is executed.
  • the passage 5 is enclosed by an annular overflow weir 6, so that at the bottom of the functional space 2.2, i. on the partition wall 4 two subspaces are formed, namely an outer annular subspace 2.2.1 between the inner surface of the wall of the functional container 2 and the overflow weir 6 and an inner subspace 2.2.2, via the passage 5 with the functional space 2.3 in Connection stands.
  • a plurality of nozzles 7 are arranged at a distance both from the separating wall 3 delimiting this functional space at the bottom and at a distance from the upper side of the functional tank 2, and via a line 8 with control valve 9 to a source (not shown) for providing the liquid base component are connected.
  • the nozzles 7 are arranged and designed such that when the control valve 9 is open, the base component exits from the nozzles 7 exiting in a vertical upward direction and then falling back onto the partition wall 3, which in the illustrated embodiment lies at the edge region 3.1, ie in the Near the wall of the functional container 2 as a perforated plate or floor with a Variety of openings and in its central region 3.2 is formed as a closed wall or as a closed bottom.
  • a line 10 which is provided in the interior of the functional space 2.2 with at least one nozzle 11, which at a distance above the overflow weir 6 and above the subspace 2.2.2 and at a distance below the formed as a baffle section 3.2 the partition 3 is located.
  • the nozzle 11 is formed and arranged so that the nozzle jet issuing from this nozzle is directed vertically upwards, i. directed to the baffle serving section 3.2.
  • the line 10 is connected via a control valve 12 to a source, not shown, which provides the CO2 gas under pressure.
  • the control valve 12 is controlled so that the gas pressure within the functional container 2 and in particular also within the functional spaces 2.1 and 2.2 corresponds to the CO2 concentration in the produced mixed product, namely u.a. also taking into account further parameters, e.g. the temperature of the mixed product, dosage or recipe of the mixed product, etc.
  • control valve 12 is u.a. taking into account measurement signals which provide pressure sensors 12.1 provided on the functional spaces 2.1 and 2.2 and / or provided temperature sensors 12.2, controlled so that the CO 2 pressure in the functional tank 2 is set so high that the desired CO 2 content in the mixed product is achieved It should be remembered that adding the CO2-free syrup will reduce the CO2 content in the finished product.
  • the output or the pressure side of a pump 13 is connected in the flow direction of the CO2 gas to the control valve 12, which is connected to its input via a line 14 to the subspace 2.2.1.
  • the additional component serving as a mixing chamber and at the same time as a buffer memory functional space 2.3 is connected to a line 15, in which inter alia, controlled by a suitable meter, for example by a flow meter 16 metering valve 17 and a pump to lead the additional component are provided under pressure.
  • the flow meter 16 is, for example, a magneto-inductive flow meter (MID).
  • MID magneto-inductive flow meter
  • a density measurement is preferably integrated into the flowmeter 16, so that a dosage is possible which is, inter alia, independent of temperature and / or pressure or at least largely temperature and / or pressure independent.
  • the meter may, however, also be, for example, a mass flow meter (MDM), by which, although not directly the volume flow can be measured, but by which the mass flow, the density and the temperature can be determined.
  • MDM mass flow meter
  • vent tank 19 vent lantern
  • the input of the pump 18 is connected via a vent tank 19 (vent lantern) to a source, not shown, for providing the additional component.
  • the vent tank 19 is vented via a vent valve assembly 20, so that this container is then completely filled with the additional component and thus in particular a buffering of the additional component in the vent tank 9 by a pressurized inert gas buffer, such as C02 gas buffer is not necessary, which contributes significantly to the reduction of the inert gas or CO 2 gas consumption.
  • a pressurized inert gas buffer such as C02 gas buffer
  • a product line 21 with pump 22 and flow meter 23 is connected, via the (product line) the device 1 with a filling machine, not shown, for filling bottles or other containers associated with the mixed product.
  • a return line 24 is connected to the product line 21 so that the pump 22 can be operated, for example, at a constant delivery rate, irrespective of the actual quantity of the mixed product conveyed to the filling machine and detected by the flow meter 23 .
  • the flow meter 23 is, for example, a magneto-inductive flow meter (MID) and is of course also designed that with him phases with stop / go operation and / or with a performance of the filler are detected error-free.
  • MID magneto-inductive flow meter
  • the operation of the device 1 can be described as follows:
  • the functional space 2.1 takes place, as already stated, the degassing and at the same time at least partially carbonizing the base component with. For example, 80-90% of the CO 2 concentration of the mixed product.
  • the functional space 2.1 is also subjected to the required CO 2 gas pressure for this, controlled by the control valve 12.
  • the base component is sprayed upward in the direction of the ceiling or in the direction of the upper boundary of the functional space 2 and then rains back onto the bottom of the functional space 2.1 formed by the partition wall 3.
  • a pressure degassing of the base component takes place by diffusion and at the same time also the carbonization of the base component. This is in equilibrium with the CO 2 gas pressure in the functional space 2.1 (CO 2 pressure equal to the saturation pressure).
  • the height of the functional space is used twice, resulting in an extension of the residence time of the sprayed base component in the functional space 2.1 and also to an increase in the Exchange surface between the base component and the C02 gas in the functional space 2.1 leads.
  • the foreign gas content in the base component is still about 10% or less after the treatment.
  • the degassed and carbonized base component builds up on the partition wall 3 and then passes through the openings partition wall section 3.1 in the func- tion room 2.2, in the local subspace 2.2 arranged below the partition wall section 3.1.
  • at least one control valve 9 controlling filling level sensor 9.1 is provided, for example, from a Min / max probe is formed and controls the liquid level in the subspace 2.2.1 such that the level of this liquid level is constantly well below the upper edge of the overflow weir 6.
  • the base component from the subspace 2.2.1 is constantly conveyed via the line 10 to the arranged above the subspace 2.2 nozzle 1 1, ie the subspace 2.2 .2 and thus the inlet to the functional space 2.3 are constantly overflowed with the base component.
  • the base component in the line 0 is mixed with the C02 gas supplied via the control valve 12, in such a way that the from the at least one nozzle 1 1 upward in the functional space 2.2 and serving as a baffle partition wall section 3.2 deployed Base component has a far above the C02 saturation CO 2 components, for example, a CO 2 concentration of 210% of the CO 2 saturation concentration.
  • the greater part of the CO 2 gas which has passed into the functional space 2.1 via the dividing wall section 3.1 is used in the manner described above for degassing and simultaneous carbonization of the base components discharged from the nozzles 7.
  • This C02 gas is discharged via a valve arrangement provided on the upper side of the functional container 2 or the functional space 2.1 - which is also referred to in practice as Fremdgasabschnüffelung 25, and indeed for discharging the removed from the base component defective gases.
  • the functional space 2.3 is always completely filled with the mixed product, in such a way that the liquid from the subspace 2.3 is present through the passage 5 in the subspace 2.2.2 up to the upper edge of the overflow weir 6.
  • the additional component is supplied via the metering valve 17 controlled by the flow meter 16 continuously or intermittently or batchwise, depending on the amount of the mixed product taken from the functional space 2.3 and the filler via the product line 21, i. as a function of the measuring signal of the flow meter 23 and as a function of the required dosage of the additional component in the mixed product.
  • the dosage of the additional component is thus ultimately in response to the amount of mixed product taken from the device 1 via the product line 21.
  • serving as a mixing chamber and buffer memory function space 2.3 is constantly filled with the base component, and in fact that at least the greater part of emerging from the at least one nozzle 1 1 basic component reaches the top of the subspace 2.2.2. If the liquid level in the subspace 2.2.2 has dropped below the level of the upper edge of the overflow weir 6 and thus refilling of the subspace 2.3 with the base component is necessary, the base component which has reached the subspace 2.2.2 passes via the passage 5 into the subspace 2.3.
  • the base component discharged from the nozzle 1 1 flows back over the edge of the overflow weir 6 into the subspace 2.1 .1.
  • a direct mixing of the basic component recorded in subspace 2.2.1 with the component in subspace 2.2.2 or with the mixed product in subspace 2.3 is avoided by the partition wall 4 with the overflow weir 6.
  • the pump 13 has a delivery rate V13, which is greater than the delivery rate V22 of the pump 22. Regardless of the operating condition of the Pump 22, the flow rate V 3 of the pump 13 in any case greater than the maximum flow rate V22 of the pump 22.
  • V13 the delivery rate of the subspace 2.2.2 and the overflow weir 6
  • the subspace 2.3 is constantly a constant Has filling level and the base component removed with the finished mix on the product line 21 is constantly replaced immediately.
  • Advantages of the device 1 according to the invention include u.a. in their compact design, in the particularly simple control of the dosage of at least one additional component and in particular in a reduced consumption of CO 2 gas.
  • the entire mixing plant is summarized, for example, in a single functional container.
  • the functional space 2.3 forms both the mixing tank and the buffer tank.
  • the inventive type of control or regulation of the metering is within the apparatus 1 for the correct functioning of the mixing plant - in contrast to the prior art - a continuous volume flow not required lent, so that in contrast to known mixing plants, a large-volume buffer tank to ensure a continuous Operation of the mixing plant is not required even in a stop / go operation of the filling machine.
  • a rated power of the device 1 of 30 m 3 / h is a volume of only 100 I for the serving as a buffer memory space 2.3 is fully sufficient, which contributes to a significant reduction in the construction volume of the device 1, in particular also taking into account It is a fact that known systems require buffer storages with a much larger volume.
  • a further advantage of the invention consists in the fact that, as a result of the described design and control of the device 1, the mixing vessel and buffer reservoir
  • At least one additional component in this functional space e.g. Fade dosages, for example due to a faulty concentration of the additional component, etc. compensate.
  • the degassing and carbonization of the base component in more than one stage, for example, in the form that in the common functional container 2 a plurality of the functional space 2.1 corresponding functional spaces are provided, namely in terms of their function cascade successively such, i0 that the degassed in a first functional space and at least partially carbonated base component is further degassed in a further functional space and nachkarbonIFF etc.
  • at least the degassing possibly also the degassing and Vorkarbonmaschine make the base component in an additional system.
  • the mixing plant or device according to the invention can also be designed for admixing two or more than two, even different additional components to at least one base component, but all versions are preferred in common that the dosage of at least one additional liquid component to at least one ßasiskomponente in dependence from the withdrawn amount of the mixed product.
  • Another essential advantage of the method according to the invention is that it is no longer necessary to prepare the mixed product according to its manufacture. with a CO2 gas cushion, the pressure of which is higher than the CO 2 saturation pressure in the mixed product. This is due to the now made possible, continuously producing the mixed product even with fluctuating amount per unit time, whereby a buffering in a buffer tank is unnecessary. By this procedure according to the invention, the consumption of CO 2 gas is considerably reduced.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Accessories For Mixers (AREA)
  • Non-Alcoholic Beverages (AREA)
  • Apparatus For Making Beverages (AREA)

Abstract

L'invention concerne un procédé de fabrication d'un produit liquide mixte à partir d'au moins un composant liquide de base et d'au moins un composant liquide additif mélangé au composant de base sous forme dosée. Le dosage du ou des composants liquides additifs dans le composant de base est réalisé en fonction de la quantité de produit mixte prélevé dans la chambre de mélange (2.3).
EP10754688.9A 2009-11-24 2010-09-07 Procede pour la production d'un melange, notamment d'une boisson Active EP2504084B1 (fr)

Priority Applications (2)

Application Number Priority Date Filing Date Title
SI201031530T SI2504084T1 (sl) 2009-11-24 2010-09-07 Postopek za izdelavo mešanega izdelka zlasti pijače
PL10754688T PL2504084T3 (pl) 2009-11-24 2010-09-07 Sposób wytwarzania produktu mieszanego, zwłaszcza napoju mieszanego

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102009054313A DE102009054313A1 (de) 2009-11-24 2009-11-24 Verfahren sowie Vorrichtung zum Herstellen eines Mischproduktes, insbesondere Mischgetränkes
PCT/EP2010/005477 WO2011063867A2 (fr) 2009-11-24 2010-09-07 Procédé et dispositif de fabrication d'un produit mixte, notamment d'une boisson mixte

Publications (2)

Publication Number Publication Date
EP2504084A2 true EP2504084A2 (fr) 2012-10-03
EP2504084B1 EP2504084B1 (fr) 2017-08-23

Family

ID=43216220

Family Applications (1)

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EP10754688.9A Active EP2504084B1 (fr) 2009-11-24 2010-09-07 Procede pour la production d'un melange, notamment d'une boisson

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US (1) US8968812B2 (fr)
EP (1) EP2504084B1 (fr)
DE (1) DE102009054313A1 (fr)
PL (1) PL2504084T3 (fr)
SI (1) SI2504084T1 (fr)
WO (1) WO2011063867A2 (fr)

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Publication number Priority date Publication date Assignee Title
DK2537793T3 (en) 2011-06-22 2017-09-11 Skånemejerier Ab New method of filling and apparatus therefor

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Publication number Publication date
DE102009054313A1 (de) 2011-05-26
EP2504084B1 (fr) 2017-08-23
WO2011063867A3 (fr) 2011-07-21
SI2504084T1 (sl) 2017-10-30
PL2504084T3 (pl) 2018-02-28
WO2011063867A2 (fr) 2011-06-03
US20120174796A1 (en) 2012-07-12
US8968812B2 (en) 2015-03-03

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