EP2623190A1 - Dispositif de carbonatation pour le vin et des boissons contenant du vin - Google Patents

Dispositif de carbonatation pour le vin et des boissons contenant du vin Download PDF

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Publication number
EP2623190A1
EP2623190A1 EP13153406.7A EP13153406A EP2623190A1 EP 2623190 A1 EP2623190 A1 EP 2623190A1 EP 13153406 A EP13153406 A EP 13153406A EP 2623190 A1 EP2623190 A1 EP 2623190A1
Authority
EP
European Patent Office
Prior art keywords
beverage
pressure vessel
wine
carbon dioxide
pressure
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP13153406.7A
Other languages
German (de)
English (en)
Inventor
Swen Wunderlich
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.)
Apollo Produkt- und Vertriebs-GmbH
Original Assignee
Apollo Produkt- und Vertriebs-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 Apollo Produkt- und Vertriebs-GmbH filed Critical Apollo Produkt- und Vertriebs-GmbH
Publication of EP2623190A1 publication Critical patent/EP2623190A1/fr
Withdrawn legal-status Critical Current

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Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B67—OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
    • B67D—DISPENSING, DELIVERING OR TRANSFERRING LIQUIDS, NOT OTHERWISE PROVIDED FOR
    • B67D1/00—Apparatus or devices for dispensing beverages on draught
    • B67D1/0015—Apparatus or devices for dispensing beverages on draught the beverage being prepared by mixing at least two liquid components
    • B67D1/0016—Apparatus or devices for dispensing beverages on draught the beverage being prepared by mixing at least two liquid components the beverage being stored in an intermediate container before dispensing, i.e. pre-mix dispensers
    • 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
    • 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
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40—Static mixers
    • B01F25/42—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
    • B01F25/43—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
    • B01F25/431—Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor
    • B01F25/4314—Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor with helical baffles
    • B01F25/43141—Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor with helical baffles composed of consecutive sections of helical formed elements
    • 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
    • B67—OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
    • B67D—DISPENSING, DELIVERING OR TRANSFERRING LIQUIDS, NOT OTHERWISE PROVIDED FOR
    • B67D1/00—Apparatus or devices for dispensing beverages on draught
    • B67D1/0042—Details of specific parts of the dispensers
    • B67D1/0057—Carbonators
    • B67D1/006—Conventional carbonators
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B67—OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
    • B67D—DISPENSING, DELIVERING OR TRANSFERRING LIQUIDS, NOT OTHERWISE PROVIDED FOR
    • B67D1/00—Apparatus or devices for dispensing beverages on draught
    • B67D1/0042—Details of specific parts of the dispensers
    • B67D1/0057—Carbonators
    • B67D1/0061—Carbonators with cooling means
    • B67D1/0066—Carbonators with cooling means outside the carbonator
    • B67D1/0067—Cooling coil
    • 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
    • B01F35/90—Heating or cooling systems
    • B01F2035/98—Cooling

Definitions

  • the present invention relates to a carbonator for wine and wine-based beverages with a pressure vessel, a wine source, which is connected via a beverage supply line with a beverage inlet opening of the pressure vessel or connectable, a conveyor which promotes the beverage from the wine source in the pressure vessel, a carbon dioxide source, which via a gas supply line with a gas inlet opening of the pressure vessel is connected or connectable, and a dispensing device which is connected via a beverage discharge line with a beverage outlet opening of the pressure vessel or connectable. Furthermore, the invention relates to a dispensing system for tapping wine and wine-containing beverages in glasses and decanters, and a method for the enrichment of wine or wine-containing beverages with carbon dioxide.
  • a Karbonisiervortechnisch of the aforementioned type is for example from the DE 10 2010 012 175 A1 known.
  • This carbonator has a pressure vessel for enriching a beverage with carbon dioxide.
  • the pressure vessel is connected to a beverage source via a beverage supply line connected to a beverage inlet opening of the pressure vessel.
  • a positive displacement pump is connected, which promotes the beverage from the beverage source into the pressure vessel.
  • the pressure vessel is connected via a connected to a gas inlet opening of the pressure vessel gas supply line with a carbon dioxide source.
  • the pressure vessel via a beverage outlet to a beverage discharge line connected.
  • a flow cooler is provided at the beverage discharge line.
  • a conventional dispensing device is connected.
  • the present invention provides a Karbonisiervoriques of the aforementioned type, wherein the carbon dioxide source is adapted to press carbon dioxide with a gas pressure of about 1.5 to 2.4 bar in the pressure vessel, wherein the conveyor is formed, the drink with a raised compared to the carbon dioxide, in particular increased by about 1 bar fluid pressure in the pressure vessel, and that a static mixer disposed in the beverage discharge line and is designed such that a liquid pressure of the carbonated beverage as it flows through the mixer between an input of the mixer and an output of the mixer as it flows through the mixer by at least 0.5 bar decreases.
  • the total length of the beverage discharge line can be designed relatively short, as this ensures a pressure drop of at least 0.5 bar.
  • the liquid is pressed into the beverage discharge line with the pressure prevailing in the pressure vessel filling pressure. If the dispensing device is opened and accordingly the beverage flows through the beverage discharge line, this pressure builds up on the frictional losses in the beverage discharge line, but due to the brevity of the line, this pressure reduction is minimal and hardly measurable.
  • the mixer is designed so that the fluid pressure is reduced by at least 0.5 bar. The corresponding pressure reduction is measurable at the outlet of the beverage discharge line, ie at the dispensing device.
  • the temperature of the wine remains almost constant due to the short beverage discharge line, so that an increase in the saturation pressure of the wine is prevented.
  • the wine does not lead to a CO 2 -binding in the beverage discharge line and the wine is zapfbar bubble-free with a manageable dispensing pressure.
  • the wine is mixed with the carbon dioxide not only in the pressure vessel but also in the mixer, so that at the outlet of the mixer a mixing quality of about 99.5% can be achieved.
  • the wine or wine-containing beverages are carbonated with a relatively low gas pressure of about 1.5 to 2.4 bar.
  • the drink must be conveyed according to pre-cooled in the pressure vessel, so that the saturation pressure of the beverage is below the gas pressure.
  • the carbon dioxide may be forced into the pressure vessel at a pressure of about 1.8 bar when the wine is delivered to the pressure vessel at a carbonizing temperature of about 6 ° C and a liquid pressure of about 2.8 bar. About 5 g of carbon dioxide are dissolved in the wine per liter. This roughly corresponds to the amount of carbon dioxide in a prosecco.
  • the carbonator according to the invention allows a possible foam-free cones of carbonated wines and wine-based beverages in glasses and decanters.
  • the mixer is designed such that the fluid pressure between the inlet of the mixer and the outlet of the mixer decreases by 0.5 to 1.0 bar, preferably 0.63 bar.
  • the saturation pressure of wine or wine-based beverages depends, inter alia, on the ingredients, the pH, the sugar content and the temperature of the wine, it has been shown in tests that particularly good tapping results were achieved with static mixers which reduce the liquid pressure by 0 , Deg. 5 to 1.0 bar. Particularly good results were achieved with a static mixer in which the liquid pressure between the input and the output of the mixer drops by 0.63 bar.
  • the mixer 25 to 35 mixing elements Preferably, the mixing elements of the mixer are in contact with each other and / or are arranged such that they together form an opposing spiral.
  • the static Mixers were particularly good Zapfdies achieved, in which the wine and the wine-containing drinks can be tapped as possible without foaming.
  • the length of the beverage discharge line is between 20 and 50 cm.
  • an injection nozzle is provided at the beverage inlet opening of the pressure vessel and designed such that the beverage is injected into the pressure vessel.
  • the beverage can absorb the carbon dioxide almost completely and in proportion to its solubility.
  • the conveyor may comprise a pump which conveys the beverage from the wine source into the pressure vessel.
  • a pump which conveys the beverage from the wine source into the pressure vessel.
  • the wine source includes a bag-in-box container.
  • Bag-in-box containers are particularly easy to handle.
  • a flow cooler for cooling the beverage is provided on the beverage supply line.
  • the flow cooler is designed such that the beverage is cooled to a carbonization temperature of 4 ° to 10 ° Celsius, preferably 6 ° Celsius.
  • the flow cooler cools the drink in particular the carbonating temperature before it is pumped into the pressure vessel.
  • the saturation pressure of the beverage is reduced before the carbonization, so that the liquid pressure necessary for the carbonation of the beverage can be comparatively low at about 1.5 to 2.4 bar.
  • the carbon dioxide source is configured such that the carbon dioxide is forced into the pressure vessel at a gas pressure of 2 bar. Particularly good tapping results were achieved.
  • a pressure reducer and / or a shut-off valve are arranged or is.
  • the gas pressure of the carbon dioxide flowing into the pressure vessel can be controlled or monitored in a simple manner.
  • the carbon dioxide source comprises a gas container.
  • This gas container may be, for example, a carbon dioxide bottle.
  • a cooling device for cooling the beverage located in the pressure vessel is provided in particular to a carbonization temperature of 4 ° to 10 ° Celsius, preferably 6 ° Celsius. Due to the constant cooling of the beverage, an increase of the saturation pressure and concomitant CO 2 unbinding is prevented.
  • a level control unit which regulates the level of the pressure vessel.
  • the level control can easily consist of two electrodes. For example, an electrode arranged in the lower region of the pressure vessel may drop the fill level below the lower level level and a second arranged in the upper region of the pressure vessel electrode register reaching a maximum level of the pressure vessel.
  • a bypass line bypassing the pressure vessel which connects the beverage supply line to the beverage discharge line.
  • This bypass line allows the wine to be tapped directly without first enriching the wine with carbon dioxide.
  • the bypass line can be connected on the input side, for example, with the wine source or with the beverage supply line behind a possible pump or a flow cooler.
  • the bypass line can be connected in front of or behind the static mixer to the beverage discharge line.
  • a beverage additive device with a beverage additive source is provided, which is connected or connectable to the beverage discharge line via a beverage additive supply line.
  • the beverage additive device allows an admixture of other beverage additives to the drink, so that it can be changed in taste and appearance.
  • the beverage additive line has an opening valve.
  • the beverage additive source comprises a bag-in-box container.
  • the bag-in-box container is particularly easy to handle.
  • a metering pump can be provided which conveys the beverage additive from the beverage additive source into the beverage discharge line.
  • the amount of added beverage additive can be easily promoted and dosed.
  • the carbonator has a display over which a user of the carbonator can select the beverage to be dispensed.
  • the display allows the user to choose whether to tap a carbonated or noncarbonated beverage and whether to add a beverage additive to the beverage.
  • the display may be connected to a control unit which controls the valves of the carbonator to open and close the valves according to the selection.
  • the delivery unit and / or the metering pump can be controlled via the control unit.
  • a coupling of the control unit with the level control unit is possible.
  • other settings such as the temperature of the drink, the CO 2 content of the drink, etc. can be controlled via the control unit.
  • a device of the present invention relates to a dispensing system for tapping wine and wine-containing drinks in jars and carafes, in which a carbonator of the type described above is provided. It is advantageous that the Karbonisiervoriques of the type described above with conventional dispensing systems, for example, in restaurants is operable by the dispensing device of the Karbonisiervoriques is connected to a tap of the dispensing system, or can be operated as part of a mobile dispensing system.
  • the present invention relates to a process for the enrichment of wine or wine-based beverages with carbon dioxide in a carbonator the type described above or in a dispensing system of the type described, in which the carbon dioxide is pressed from a carbon dioxide source in a pressure vessel with a gas pressure of about 1.5 to 2.4 bar, in particular 2 bar, the drink from a wine source in the pressure vessel with a liquid pressure increased by about 1 bar compared to the carbon dioxide and a carbonizing temperature of 4 ° to 10 ° Celsius, preferably 6 ° Celsius, a liquid pressure of the carbonated beverage in a pressure vessel downstream static mixer by at least 0.5 bar, in particular between 0.5 and 1.0 bar, preferably 0.63 bar is reduced, and the carbonated beverage is tapped at a dispensing device in glasses and carafes.
  • the beverage is injected into the pressure vessel.
  • the beverage can absorb the carbon dioxide almost completely and in proportion to its solubility.
  • the carbon dioxide and the beverage are pressed or promoted in a defined mixing ratio until reaching an upper level of the pressure vessel at a lower level of the pressure vessel.
  • FIG. 1 a carbonator according to a first embodiment of the present invention is shown.
  • the carbonator is used to fortify wine or wine-based beverages with carbon dioxide.
  • the carbonator has a pressure vessel 1, which is almost completely enclosed by a cooling device 2.
  • a beverage supply port 3 is formed with an injection nozzle 4.
  • a beverage supply line 5 is connected, via which the pressure vessel 1 is connected to a wine source 6, which has a bag-in-box container.
  • a conveyor 7 is connected to a pump which conveys the beverage from the wine source 6 via the beverage supply line 5 into the pressure vessel 1.
  • a flow cooler 8 is provided on the beverage supply line 5, which cools the drink before being injected into the pressure vessel 1 to an adjustable Karbonmaschinesemperatur.
  • the beverage supply line 5 has a controllable beverage supply opening valve 9, which is arranged between the pump 7 and the flow cooler 8.
  • a gas inlet opening 10 is formed, to which a gas supply line 11 is connected.
  • the pressure vessel 1 is connected to a carbon dioxide source 12, which has a cylinder filled with carbon dioxide gas.
  • a controllable pressure reducer 13 and a controllable shut-off valve 14 are arranged.
  • a beverage outlet opening 15 is provided, to which a beverage discharge line 16 is connected.
  • a static mixer 17 is arranged, which has thirty mixing elements 18.
  • the mixing elements 18 are in contact with each other and are arranged to collectively form an opposing spiral.
  • a tap 19 is connected for tapping the carbonated beverage in glasses and carafes.
  • the pressure vessel 1 has a level control unit 34 with two electrodes 20, 21 for level measurement held on sensors, a lower electrode 20 being arranged in the lower third of the pressure vessel 1 and an upper electrode 21 being arranged in the upper area of the pressure vessel 1.
  • the pump 7 a drink from the bag-in-box container 6 in the pressure vessel 1.
  • the drink in the pressure vessel 1 Before the drink in the pressure vessel 1 with a Injected pressure of about 3 bar, it passes through the through-flow cooler 8, where the beverage is cooled down to a carbonation temperature of about 6 ° Celsius.
  • the saturation pressure of the beverage By cooling the wine to a carbonating temperature of about 6 °, the saturation pressure of the beverage is about 1.8 bar, the saturation pressure not only on the temperature of the beverage but also among the ingredients, the pH and the sugar content of the beverage is dependent.
  • the carbon dioxide is forced by the pressure prevailing in the gas cylinder 12 filling pressure via the gas supply line 11 into the pressure vessel 1, wherein the gas pressure is reduced by the intermediate pressure reducer 13 to 2 bar.
  • the wine By injecting the beverage into the pressure vessel 1, the wine is finely dusted, whereby the carbon dioxide is almost completely dissolved in the wine. So enriched are about 5g of carbon dioxide dissolved in the wine per liter.
  • the beverage and the carbon dioxide are introduced into the pressure vessel 1 until the upper electrode 21 registers the reaching of the maximum level of the pressure vessel 1. Upon reaching the maximum level, the pump 7 is turned off.
  • the carbonated in the pressure vessel 1 beverage is constantly cooled by the surrounding the pressure vessel 1 cooling device 2 at 6 ° C, in order to avoid a CO 2 unbound.
  • the carbonated beverage is forced through the beverage discharge line 16 due to the carbonizing pressure of about 2 bar prevailing in the pressure vessel 1.
  • the carbonated beverage flows through the static mixer 17, wherein the fluid pressure between an inlet 22 and an outlet 23 of the mixer 17 decreases by about 0.63 bar.
  • the beverage and carbon dioxide in mixer 17 continue to move mixed, so that sets a mixing quality of about 99.5% at the output 23 of the mixer 17.
  • FIG. 3 a carbonator according to a second embodiment of the present invention is shown.
  • the structure of this carbonator corresponds to the carbonator according to the first embodiment.
  • bypass line 24 surrounding the pressure vessel 1 which connects the beverage supply line 5 directly to the beverage discharge line 16.
  • the bypass line 24 is connected on the input side between the flow cooler 8 and the pressure vessel 1 to the beverage supply line 5, which now has a controllable beverage supply opening valve 33, and has a bypass opening valve 25.
  • the bypass line 24 is connected between the static mixer 17 and the tap 19 to the beverage discharge line 16 and has a further controllable bypass opening valve 32.
  • the carbonator has a beverage additive device 26, which is connected via a beverage additive line 27 between the static mixer 17 and the tap 19 to the beverage discharge line 16.
  • a beverage additive source 28 is connected to a bag-in-box container.
  • a metering pump 29 which conveys the beverage additive into the beverage discharge line 16, and a controllable beverage additive opening valve 30 are connected.
  • a controllable beverage discharge opening valve 31 is arranged in the beverage discharge line 16 between the mixer 17 and the dispensing device 19.
  • wine may be carbonated and tapped almost without foam.
  • the user can select between carbonated and non-carbonated wine via an unillustrated control unit which can be optionally provided with a beverage additive.
  • the pump 7 conveys the wine through the bypass line 24 into the dispensing device 19, the valves 25 and 32 being opened and the valves 33, 31 and 30 being closed.
  • the wine is conveyed to the tap of the carbonated wine in the pressure vessel 1, there carbonated and conveyed through the beverage discharge line 16 into the dispensing device 19, wherein the valves 33 and 31 are opened and the valves 25, 19 and 30 are closed.
  • the valve 30 is opened accordingly and the metering pump 29 is turned on.
  • both the carbonated and the non-carbonated beverage can be changed in terms of taste and color by the metered addition of the beverage additive.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Dispersion Chemistry (AREA)
  • Devices For Dispensing Beverages (AREA)
EP13153406.7A 2012-02-01 2013-01-31 Dispositif de carbonatation pour le vin et des boissons contenant du vin Withdrawn EP2623190A1 (fr)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE102012100844A DE102012100844A1 (de) 2012-02-01 2012-02-01 Karbonisiervorrichtung für Wein und weinhaltige Getränke

Publications (1)

Publication Number Publication Date
EP2623190A1 true EP2623190A1 (fr) 2013-08-07

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EP13153406.7A Withdrawn EP2623190A1 (fr) 2012-02-01 2013-01-31 Dispositif de carbonatation pour le vin et des boissons contenant du vin

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EP (1) EP2623190A1 (fr)
DE (1) DE102012100844A1 (fr)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2017096505A1 (fr) * 2015-12-07 2017-06-15 Cornelius, Inc. Post-mélangeur de boisson pour mélanger un fluide de base avec un ou plusieurs fluides supplémentaires
CN109700315A (zh) * 2019-01-22 2019-05-03 康富（天津）有限公司 饮料机和使用其制备混气饮料的方法
LU500315B1 (en) * 2021-06-22 2022-12-22 Rotarex Solutions S A Carbonator with insulating housing

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
LU92380B1 (en) 2014-02-19 2015-08-20 Luxembourg Patent Co Sa In-line carbonation of water-base beverages
EP3519349A4 (fr) * 2016-09-30 2020-09-09 The Coca-Cola Company Systèmes de distribution de boisson
CN110840291B (zh) * 2019-11-27 2021-09-28 山东省葡萄研究院 一种醒酒机
US12005408B1 (en) 2023-04-14 2024-06-11 Sharkninja Operating Llc Mixing funnel

Citations (9)

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Publication number Priority date Publication date Assignee Title
US3991219A (en) * 1974-12-26 1976-11-09 Dagma Deutsche Automaten Und Getrankemaschinen G.M.B.H. & Co. Method for mixing a carbonated beverage
GB2157963A (en) * 1984-04-25 1985-11-06 Int Distillers & Vintners Limi Apparatus for dissolving gases in liquids
DE19742301A1 (de) * 1997-05-06 1998-11-12 Hans Asal Vorrichtung zur Herstellung Gas-angereicherten Wassers
US5842600A (en) * 1996-07-11 1998-12-01 Standex International Corporation Tankless beverage water carbonation process and apparatus
DE19849628A1 (de) * 1998-10-28 2000-05-04 Margret Spiegel Verfahren und Anordnung zum Einbringen von Gas in eine Flüssigkeit
USRE37499E1 (en) * 1990-10-16 2002-01-08 Sanyo Electric Co., Ltd Apparatus for manufacturing carbonated water
WO2007141339A1 (fr) * 2006-06-09 2007-12-13 Balda Solutions Deutschland Gmbh Procédé et dispositif pour enrichir un courant de liquide avec un gaz
EP1880618A1 (fr) * 2005-05-13 2008-01-23 Wataru Murota Procede et appareil pour produire une boisson aqueuse reductrice contenant de l'oxygene
DE102010012175A1 (de) 2010-03-19 2011-09-22 Carbotek Holding Gmbh Schankanlage und Imprägniervorrichtung

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Publication number Priority date Publication date Assignee Title
DE19947822A1 (de) * 1999-10-05 2001-04-12 Linde Gas Ag Verfahren und Vorrichtung zur Abgabe von carbonisiertem Trinkwasser über einen Wasserhahn

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3991219A (en) * 1974-12-26 1976-11-09 Dagma Deutsche Automaten Und Getrankemaschinen G.M.B.H. & Co. Method for mixing a carbonated beverage
GB2157963A (en) * 1984-04-25 1985-11-06 Int Distillers & Vintners Limi Apparatus for dissolving gases in liquids
USRE37499E1 (en) * 1990-10-16 2002-01-08 Sanyo Electric Co., Ltd Apparatus for manufacturing carbonated water
US5842600A (en) * 1996-07-11 1998-12-01 Standex International Corporation Tankless beverage water carbonation process and apparatus
DE19742301A1 (de) * 1997-05-06 1998-11-12 Hans Asal Vorrichtung zur Herstellung Gas-angereicherten Wassers
DE19849628A1 (de) * 1998-10-28 2000-05-04 Margret Spiegel Verfahren und Anordnung zum Einbringen von Gas in eine Flüssigkeit
EP1880618A1 (fr) * 2005-05-13 2008-01-23 Wataru Murota Procede et appareil pour produire une boisson aqueuse reductrice contenant de l'oxygene
WO2007141339A1 (fr) * 2006-06-09 2007-12-13 Balda Solutions Deutschland Gmbh Procédé et dispositif pour enrichir un courant de liquide avec un gaz
DE102010012175A1 (de) 2010-03-19 2011-09-22 Carbotek Holding Gmbh Schankanlage und Imprägniervorrichtung

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2017096505A1 (fr) * 2015-12-07 2017-06-15 Cornelius, Inc. Post-mélangeur de boisson pour mélanger un fluide de base avec un ou plusieurs fluides supplémentaires
CN109700315A (zh) * 2019-01-22 2019-05-03 康富（天津）有限公司 饮料机和使用其制备混气饮料的方法
CN109700315B (zh) * 2019-01-22 2023-11-10 康富（天津）有限公司 饮料机和使用其制备混气饮料的方法
LU500315B1 (en) * 2021-06-22 2022-12-22 Rotarex Solutions S A Carbonator with insulating housing
WO2022268847A1 (fr) * 2021-06-22 2022-12-29 Rotarex Solutions S.A. Carbonateur doté d'un boîtier isolant

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Publication number Publication date
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