Classifications

• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
  • F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
  • F04B49/00—Control, e.g. of pump delivery, or pump pressure of, or safety measures for, machines, pumps, or pumping installations, not otherwise provided for, or of interest apart from, groups F04B1/00 - F04B47/00
  • F04B49/22—Control, e.g. of pump delivery, or pump pressure of, or safety measures for, machines, pumps, or pumping installations, not otherwise provided for, or of interest apart from, groups F04B1/00 - F04B47/00 by means of valves
• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
  • F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
  • F04B53/00—Component parts, details or accessories not provided for in, or of interest apart from, groups F04B1/00 - F04B23/00 or F04B39/00 - F04B47/00
  • F04B53/06—Venting
• • A—HUMAN NECESSITIES
  • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
  • A23B—PRESERVATION OF FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES; CHEMICAL RIPENING OF FRUIT OR VEGETABLES
  • A23B2/00—Preservation of foods or foodstuffs, in general
  • A23B2/003—Control or safety devices for sterilisation or pasteurisation systems
• • A—HUMAN NECESSITIES
  • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
  • A23B—PRESERVATION OF FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES; CHEMICAL RIPENING OF FRUIT OR VEGETABLES
  • A23B2/00—Preservation of foods or foodstuffs, in general
  • A23B2/70—Preservation of foods or foodstuffs, in general by treatment with chemicals
  • A23B2/725—Preservation of foods or foodstuffs, in general by treatment with chemicals in the form of liquids or solids
  • A23B2/792—Apparatus for preserving using liquids
• • C—CHEMISTRY; METALLURGY
  • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
  • C12H—PASTEURISATION, STERILISATION, PRESERVATION, PURIFICATION, CLARIFICATION OR AGEING OF ALCOHOLIC BEVERAGES; METHODS FOR ALTERING THE ALCOHOL CONTENT OF FERMENTED SOLUTIONS OR ALCOHOLIC BEVERAGES
  • C12H1/00—Pasteurisation, sterilisation, preservation, purification, clarification, or ageing of alcoholic beverages
  • C12H1/12—Pasteurisation, sterilisation, preservation, purification, clarification, or ageing of alcoholic beverages without precipitation
  • C12H1/14—Pasteurisation, sterilisation, preservation, purification, clarification, or ageing of alcoholic beverages without precipitation with non-precipitating compounds, e.g. sulfiting; Sequestration, e.g. with chelate-producing compounds
• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
  • F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
  • F04B49/00—Control, e.g. of pump delivery, or pump pressure of, or safety measures for, machines, pumps, or pumping installations, not otherwise provided for, or of interest apart from, groups F04B1/00 - F04B47/00
  • F04B49/06—Control using electricity
• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
  • F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
  • F04B53/00—Component parts, details or accessories not provided for in, or of interest apart from, groups F04B1/00 - F04B23/00 or F04B39/00 - F04B47/00
  • F04B53/10—Valves; Arrangement of valves
  • F04B53/108—Valves characterised by the material
  • F04B53/1082—Valves characterised by the material magnetic
• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
  • F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
  • F04B2205/00—Fluid parameters
  • F04B2205/09—Flow through the pump

Definitions

• the invention relates to a method and a device for preserving beverages and the use of the device for this purpose.
• Preservatives such as dialkyl dicarbonates, sulfur dioxide, natamycin, benzoates or sorbates are used in the beverage industry for the cold sterilization of non-alcoholic carbonated or still fruit juice beverages, fruit juices, wines, non-alcoholic wines, ciders, ice teas and other beverages.
• Dialkyl dicarbonates such as dimethyl dicarbonate or diethyl dicarbonate in particular, are a special cold disinfectant and have a number of advantages. The outstanding advantage lies in the fact that taste and color are not affected, in contrast to diligent bottling.
• the advantage consists in particular in the absence of any impairment of taste and the disappearance of the effect. Due to the decomposition of the dialkyl dicarbonates into harmless components, no preservative or preservative is consumed by the actual consumer.
• dialkyl dicarbonates Compared to cold aseptic filling, the significantly lower investment costs in plant engineering are known to be an advantage when using dialkyl dicarbonates. According to the state of the art, only on-line membrane dosing pumps are used to add dialkyl dicarbonates. This is necessary because the volume of beverages to be treated is not certain from the outset. An advantage of diaphragm pumps is that their pump chamber is completely closed.
• the devices with diaphragm pumps usually consist of a magnetically or electrically driven diaphragm pump, storage vessels, a device attached to the beverage line for atomizing the dialkyl dicarbonate, a flow meter attached to the beverage line, and an electronic controller. Dosing pumps of this type are usually permanently installed in the beverage line.
• the dosing pumps should be suitable for several different performance parameters, especially for small and very small quantities. In addition, these dosing pumps should have a high degree of accuracy during dosing, a high atomization pressure and a wide control range.
• Dialkyl dicarbonates are thus metered proportionally into the beverage tube in the amount required.
• Examples of these pumps are the VelcorinDT devices from Lanxess.
• WO1998042983A1 discloses a metering pump for the metered delivery of liquids.
• the dosing pumps used for such a device and method must meet un ferent performance parameters. On the one hand, they should be suitable for supplying small or very small quantities. In addition, these dosing pumps should have a high level of accuracy, but at the same time also provide a high atomization pressure and also have a wide control range, especially for a wide variety of applications.
• a device according to the invention for preserving beverages has a measuring device which is suitable and intended for determining a flow rate of a liquid flowing through a beverage line and a pump device which conveys a preservative, in particular dialkyl dicarbonate, into the beverage line and the pump device being dependent can be controlled by a flow rate determined by the measuring device.
• the device has a venting or degassing device for venting the pump device and this venting device has a valve device.
• the invention described here serves in particular to take precautions in order to implement the metering process as gas-free as possible and in particular to safely remove gas bubbles from the pump device.
• the device preferably has a conveying line which opens into the beverage line and the pump device preferably conveys the preservative through this conveying line.
• the term "ventilation” is used for simplification, even if the medium to be discharged is a gas other than air. It is preferably at the gases are gases selected from a group of gases including CO 2 , methanol, methyl carbonate and dimethyl carbonate.
• the device has a nozzle device and in particular a nozzle head, which injects the preservative into the beverage line and/or atomizes the preservative in the beverage line and/or in the beverage.
• This nozzle device or this nozzle head preferably protrudes at least in sections into the beverage line.
• the nozzle device or the nozzle head is preferably part of the conveying line and in particular forms one end of this conveying line.
• the pump device is therefore preferably used for spraying the preservative into the beverage line and/or into the beverage.
• the pump device is therefore preferably a pump device which is suitable and intended for conveying a medium, such as the preservative here, under pressure and/or a pump device which is suitable and intended for atomizing the To effect preservatives means in the beverage line.
• the valve device is preferably a controlled valve device.
• a (particularly active) valve device is understood, which can be actively actuated by a control process and which, in particular, does not open due to excess pressure or a flow movement, such as a check valve.
• the invention thus describes a device and a method for pump venting and in particular for pump head venting and in particular for fully automatic pump head venting.
• the pump device is a metering pump and in particular a diaphragm pump or a diaphragm dosing pump.
• Diaphragm pumps have proven to be suitable pumping devices to meet the criteria described above.
• this pump device has a delivery rate that is greater than 0.01 l/h and preferably greater than 0.02 l/h.
• the pump device preferably has a delivery rate that is less than 60 l/h, preferably less than 50 l/h, preferably less than 40 l/h, preferably less than 30 l/h and preferably less than 20 l/h .
• the pump device can preferably be regulated in a power range in which the ratio between the lowest delivery rate and the highest delivery rate is less than 0.1, preferably less than 0.01. In this way, a wide variety of requirements when bottling beverages can be met with a single type of pump.
• the pump device preferably conveys the preservative to a nozzle device under pressure, and preferably under a pressure of between 5 bar and 100 bar, preferably between 15 bar and 50 bar.
• the beverage is preferably conveyed through the beverage line with a flow rate of 40l/h - 80000l/h.
• valve device described above is particularly preferably used to vent a pump head of the pump device and/or a predetermined area of the pump device in which outgassing media can collect and/or which pushes the medium to be dosed in the direction of the beverage line.
• the pump head is sometimes also referred to as a dosing head or delivery unit. This is in particular the area through which the pumped medium flows (sucked in and/or pumped).
• the pump head is preferably delimited by a suction valve, a pressure valve and a delivery element (such as a diaphragm of a piston or the like). This means that the pump head could also be referred to as a "metering device”.
• the valve device is a solenoid valve. Solenoid valves or magnetically controlled valves have the advantage that they can be switched very quickly and also with very high cycle speeds.
• the device has a control device for controlling the valve device and in particular the valve device designed as a solenoid valve.
• this control device is suitable for the cyclic activation of the solenoid valve.
• the control device is particularly preferably suitable and intended to control the valve device in response to or taking into account a (delivery) movement of the pump device and in particular a pump stroke.
• the solenoid valve can be activated cyclically with every nth pump stroke (where n is preferably a natural number).
• the valve device can be controlled taking into account a position of an element of the pump device, for example taking into account the position of a pump piston, a diaphragm of a diaphragm pump or a position of a valve of the pump device (in particular if the pump device is a diaphragm pump).
• a detection device is preferably provided, which detects this position or position.
• control device is suitable and intended to also control the valve device as a function of different operating modes of the device. It is thus possible, for example, for the valve device to be opened cyclically in a dosing operation in order to reliably discharge gas bubbles that are produced in this dosing operation. The detailed procedures are described below.
• This cyclical opening of the valve device is preferably adapted to the pump cycle of the pump device.
• the device has a monitoring device for monitoring the venting process. In this way, it can always be monitored during operation whether and to what extent ventilation is taking place is made or may be necessary.
• the control of the valve can be adapted to this monitoring.
• the valve device can also be actuated manually and/or by user intervention.
• manual actuation of the valve device is also possible.
• emergency actuation or emergency venting is possible. It is thus possible for a user to actuate the valve device directly.
• the user it would also be possible for the user to actuate the valve device by means of a control device.
• the valve means is a single screw valve, e.g. H. a valve that can be screwed into a specific area of the pump device.
• the valve device is preferably a two-way valve.
• venting valve at different positions, for example between the pump head and the nozzle device.
• installation at the highest point in the pump head is advantageous, particularly in the case of a structure with a directly attached nozzle.
• the valve device has a seat seal and in particular a soft seat seal.
• the valve device is particularly preferably designed with little dead space.
• This configuration has the (design) advantage that the internal volume of the valve (that is, the part that comes into contact with the medium) is designed to be as small as possible. In this way it is achieved that the efficiency of the pump device and the dosing accuracy are not influenced too greatly.
• the valve device is in an area of the pump device and in particular in a product space of the pump device arranged, and/or the valve device is arranged (in relation to the medium to be conveyed) in an upper and in particular a highest area of the pump device and/or the product space.
• the highest area is understood to mean an area which is arranged at the highest point in a vertical direction or towards the center of the earth in comparison to other areas.
• the valve device is preferably arranged in such a way that a gaseous medium can collect in one area of the valve device.
• venting of the pump device is possible in a particularly favorable manner.
• gas bubbles can be discharged or discharged from the pump device in a particularly favorable manner.
• valve device (and in particular an outlet of the valve device) is followed by a line for conducting ventilation gases and/or a liquid (and in particular the liquid to be conveyed).
• a line for conducting ventilation gases and/or a liquid and in particular the liquid to be conveyed.
• the line serves to feed these media at least partially and in particular the liquid media back into a circuit and/or to return them to the pump device.
• the discharged gas and/or liquid can be fed into a vessel via this line.
• the device has a measuring vessel and/or a measuring device for detecting a level of a liquid and/or gaseous medium, and the line described above preferably opens into this measuring vessel.
• the measuring vessel can be a measuring burette, for example, ie a vessel which has a measuring scale.
• a measuring vessel is understood to mean a device which has a volume for accommodating a liquid medium and which also enables this volume to be determined.
• a measuring vessel can also allow liquid to pass through.
• the device has a receiving space for at least temporarily receiving a liquid medium discharged from the pump device via the valve device. This receiving space is preferably in flow connection with the line described above, which connects to the direction Ventilein. This receiving space is preferably formed by the measuring vessel described above.
• the discharged quantity of gas or liquid is preferably conveyed via a line into a calibration vessel or measuring vessel on the suction side.
• This measuring vessel is preferably designed in such a way that a gas phase can escape and a liquid phase is or can be fed back to the process and/or the pump device.
• the device and in particular the measuring vessel therefore preferably has a separating device in order to be able to separate gaseous and liquid components of the medium escaping via the vent valve.
• This separating device can also be formed by the shape of the measuring vessel itself.
• the measuring vessel preferably has a filling level measuring device. Particularly preferably, this measuring vessel has a floating device, in particular for measuring the fill level. However, other sensors would also be possible, which are suitable and intended for determining a filling level within a measuring vessel.
• the device has an evaluation device for evaluating and/or determining the filling level (of the measuring vessel).
• an image recording device such as a camera can be used, which monitors the filling level inside the measuring vessel.
• This filling level measuring device can also output data which can be used to control the pump device and/or the valve device.
• the device has a sensor device which detects at least one parameter which is characteristic of the substance or the media conveyed out of the valve device.
• a flow measuring device can be installed in the line connected to the valve device be provided in order to determine the flow rate of the gaseous and/or liquid medium flowing in the line.
• a measuring device which outputs a parameter that is characteristic of whether the emerging medium is a gaseous or a liquid medium.
• a temperature sensor can preferably be used here, for example (as a measuring device or sensor device).
• This temperature sensor (in particular electronically controlled) is preferably kept at a suitable temperature. As soon as liquid medium is conveyed out of the valve device and it hits the temperature sensor, the temperature of the sensor changes, since the temperature of the liquid is preferably somewhat lower than that of the sensor. The temperature sensor can thus generate a signal for the controller to detect the medium that has flowed back.
• this sensor device Based on the measured values of this sensor device, it can be determined whether gas is escaping from the pump or whether liquid is already escaping.
• a sensor device is therefore particularly preferably provided and in particular a sensor device is installed in the named line, which monitors the venting function. For example, as long as a gas flows past the sensor device, the venting process is to be continued. If liquid flows past the sensor device, the venting has been successfully completed.
• the measuring vessel has an inlet for a liquid and/or an outlet for a liquid, with this outlet being flow-connected to the pump device.
• the measuring vessel preferably also has a discharge device for discharging a gaseous medium.
• This discharge device can have a filter device for filtering the medium to be discharged.
• the suction-side measuring vessel or the suction-side measuring burette preferably has a float, with the aid of which the level in the vessel is monitored and, in particular in normal operation, a calculation of the actual metered quantity of the pump is made possible.
• the level in the measuring vessel drops because the pump draws in liquid but discharges gas via the solenoid valve. If the venting process is successfully completed in this pump venting operating procedure, the amount of liquid sucked in by the pump equalizes the amount that is fed to the measuring vessel via the valve and the line or return line. In this state, the level in the measuring vessel remains stable.
• the device has at least one temperature measuring device for detecting a temperature of at least one element of the pump device.
• the corresponding element is preferably the pump head and/or a piston and/or a membrane section of the pump device or generally a movable element of the pump device which is in direct contact with the medium to be pumped. Elevated temperatures (however, temperatures below 45°C) intensify the decomposition processes of the dimethyl dicarbonate and thus the formation of the gas phase.
• control device mentioned above also controls the valve device, taking this measured temperature into account.
• the control device can shorten the intervals of the cyclic venting strokes and/or the intervals of the valve openings.
• the present invention is also directed to a method for preserving beverages, a flow rate of a liquid flowing through a beverage line being determined by means of a measuring device, and a preservative and in particular dialkyl dicarbonates being conveyed into the beverage line by means of a pump device, with a conveying line being fed into the beverage line opens and the pump device promotes the preservatives through this beverage line and wherein the Pump device is controlled in dependence on a flow rate determined by the measuring device.
• the pump device is vented at least at times by means of a venting device, this venting taking place by means of a controlled valve device. It is therefore also proposed in terms of the method that controlled venting of the pump device takes place at least in some operating states.
• the pump device can be operated in different operating states.
• the valve device is controlled cyclically in a working operation and/or the valve device is controlled in a working operation, taking into account a pumping operation of the pump device.
• valve device which is in particular a solenoid valve
• This opening of the valve device preferably takes place before the subsequent dosing stroke and preferably in a predetermined time space before this dosing stroke.
• This predetermined period of time is preferably less than 0.5 s, preferably less than 0.3 seconds, preferably less than 0.2 s, preferably less than 0.1 seconds, preferably less than 0.08 s, preferably less than 0 .06 s, preferably less than 0.05 s, preferably less than 0.04 s, preferably less than 0.03 s, preferably less than 0.02 s.
• This period of time is preferably greater than 1/100 s, preferably greater than 2/100 s and preferably greater than 3/100 s.
• valve actuation is possible when there is no pressure or when the internal pressure of the pump is low.
• the dosing accuracy of the pump device is influenced only slightly and, on the other hand, only a small amount of force is required for the magnetic valve or for its actuation.
• ventilation can also be carried out during production breaks in an operating mode in which production takes place, but no pump operation, which preservatives into the beverage line.
• the valve device can be opened cyclically in order to safely eject any gas bubbles that form and/or to dose the next pump stroke with the required accuracy.
• the device can preferably be operated in a warming or heating operating mode and/or is operated in this operating mode at least temporarily. This is in particular a waiting position before the arrival of another batch of the beverage to be bottled.
• cyclic automatic pump strokes are preferably triggered when a valve is open. In this process, the readiness to pump is preferably maintained despite the formation of gas bubbles in the pump head, these gas bubbles being discharged cyclically in this process.
• the intervals of the cyclic venting strokes are preferably changed here and, in particular, shortened.
• the system control preferably enables a venting operating mode that can be selected manually or generally by user intervention and in which the pump device is operated with an open valve at a (advantageously fixed) time interval. In this operating mode, an intensive venting or degassing process takes place.
• a gaseous and/or liquid medium discharged via the valve device is conducted into a vessel and in particular a measuring vessel.
• a medium discharged via the valve device is analyzed in order to determine whether it is a gaseous or a liquid medium.
• a temperature of at least one element of the pump device is determined at least temporarily.
• FIG. 1 shows a schematic representation of a device according to the invention
• FIG. 1 shows a device 1 for preserving beverages according to the internal prior art of the applicant.
• the reference number 10 refers to a beverage line, via which a liquid to be filled into containers, and in particular a beverage, is fed to a filling machine 20 .
• the reference number 2 designates a flow measuring device which determines or measures a flow of the beverage through the beverage line 20 .
• This flow measuring device 3 outputs a control signal S to a control device 14 .
• This control device 14 controls the pump device 4, taking this control signal S into account.
• the pump device 4 pumps a preservative from a reservoir 8 and conveys it via a nozzle head 6 into the beverage line 10, more precisely here in a curved area 10a of the beverage line 10.
• Reference number 5 designates a conveying line and the nozzle head is preferably also a component this delivery line 5.
• FIG. 2 shows a more detailed illustration to illustrate the invention.
• the pump device 4 is also shown here, which is a diaphragm pump, in particular a metering pump.
• a valve device 22 is provided on a (preferably) upper region of this pump device, which valve device forms part of the venting device, which is denoted in its entirety by 2 .
• this valve device 22 is preferably a solenoid valve.
• This solenoid valve can be controlled by a control device 30 (shown only schematically) in order to open and close.
• a vent line 24 connects to this solenoid valve device 22 .
• Reference number 3 designates a measuring device which determines whether a gaseous or liquid medium is flowing or flowing in this ventilation line 24 . In this way it can be determined whether the venting is successful or whether there is still air or gas in general in the pump device 4 .
• the line 24 preferably opens into a measuring vessel 28.
• This has a float device 34 and a scale with which the filling level of the liquid in the measuring device 3 or the measuring vessel 28 can be checked.
• the reference number 32 designates an optionally present sensor device, which detects the fill level of the liquid in the measuring container.
• the data from this measuring device 32 are also preferably used to control the valve device 22 and/or to control the pump device 4 .
• the reference number 16 designates an optionally present temperature measuring device, which measures a temperature of at least one element of the pump device 4 and in particular a temperature in the region of the pump head. Degassing behavior within the liquid to be metered can also change depending on this temperature. Data from this temperature detection device 16 is therefore preferably also used to control the valve device 22 and/or the pump device 4 .
• data for controlling the valve device 22 which relate to the operation of the pump device 4 itself are preferably also used.
• data can be used that characterize the position of a pump element such as a pump piston or the like. This data is also preferably used in order to control the valve device 22 . It is thus possible, for example, for the valve device 22 to always be actuated at a specific period of time, for example, as mentioned above, shortly before another pump stroke is due.
• Dialkyl dicarbonates are preferably used as preservatives.
• Dimethyl dicarbonate is very particularly preferably used, and dimethyl dicarbonate with a purity of >99.8% is even more preferably used as a preservative.
• dimethyl dicarbonate is used, which has been stabilized by suitable methods.
• EP 2 016041 B1 describes the use of at least one protic acid from the series of inorganic acids and organic carboxylic acids and derivatives thereof, the organic carboxylic acids being saturated and mono- or polyunsaturated aliphatic monocarboxylic acids and saturated and mono- or polyunsaturated aliphatic di- and polycarboxylic acids and their derivatives are hydroxamic acids, hydroxycarboxylic acids, aldehyde and keto acids, reactions to stabilize dialkyl dicarbonates against chemical and thermal degradation, the protonic acid or mixtures thereof in an amount of 0.01 to 100,000 ppm based on dialkyl dicarbonates or mixtures thereof is used.
• dimethyl dicarbonate is used in a mixture with phosphorus compounds, such as preferably phosphates, even more preferably with trimethyl phosphate or phosphoric acid.
• phosphorus compounds such as preferably phosphates, even more preferably with trimethyl phosphate or phosphoric acid.
• the phosphorus compound is preferably used in an amount of between 0.01 ppm and 1000 ppm, based on the total amount of the mixture of dimethyl dicarbonate and phosphorus compounds.

Landscapes

• Engineering & Computer Science (AREA)
• General Engineering & Computer Science (AREA)
• Mechanical Engineering (AREA)
• Life Sciences & Earth Sciences (AREA)
• Chemical & Material Sciences (AREA)
• Wood Science & Technology (AREA)
• Zoology (AREA)
• Food Science & Technology (AREA)
• Polymers & Plastics (AREA)
• Organic Chemistry (AREA)
• Biochemistry (AREA)
• Bioinformatics & Cheminformatics (AREA)
• General Health & Medical Sciences (AREA)
• Genetics & Genomics (AREA)
• Health & Medical Sciences (AREA)
• Devices For Dispensing Beverages (AREA)
• Food Preservation Except Freezing, Refrigeration, And Drying (AREA)
• Apparatus For Disinfection Or Sterilisation (AREA)
• Control Of Positive-Displacement Pumps (AREA)
• Vacuum Packaging (AREA)
• Details Of Reciprocating Pumps (AREA)
• Distillation Of Fermentation Liquor, Processing Of Alcohols, Vinegar And Beer (AREA)
• Non-Alcoholic Beverages (AREA)

Priority Applications (9)

Applications Claiming Priority (2)

Publications (1)

Family

ID=76137946

Family Applications (1)

Country Status (21)

Families Citing this family (3)

Citations (9)

Family Cites Families (7)

• 2021
  • 2021-05-26 LT LTEP21175892.5T patent/LT4095224T/lt unknown
  • 2021-05-26 SI SI202130218T patent/SI4095224T1/sl unknown
  • 2021-05-26 HU HUE21175892A patent/HUE068885T2/hu unknown
  • 2021-05-26 EP EP21175892.5A patent/EP4095224B1/de active Active
  • 2021-05-26 PT PT211758925T patent/PT4095224T/pt unknown
  • 2021-05-26 HR HRP20241338TT patent/HRP20241338T1/hr unknown
  • 2021-05-26 ES ES21175892T patent/ES2990987T3/es active Active
  • 2021-05-26 DK DK21175892.5T patent/DK4095224T3/da active
  • 2021-05-26 RS RS20241237A patent/RS66112B1/sr unknown
  • 2021-05-26 PL PL21175892.5T patent/PL4095224T3/pl unknown
• 2022
  • 2022-05-24 BR BR112023024440A patent/BR112023024440A2/pt unknown
  • 2022-05-24 MX MX2023014080A patent/MX2023014080A/es unknown
  • 2022-05-24 US US18/562,872 patent/US12460629B2/en active Active
  • 2022-05-24 AU AU2022283562A patent/AU2022283562A1/en active Pending
  • 2022-05-24 JP JP2023572770A patent/JP2024520004A/ja active Pending
  • 2022-05-24 CN CN202280037834.2A patent/CN117377748A/zh active Pending
  • 2022-05-24 CA CA3217292A patent/CA3217292A1/en active Pending
  • 2022-05-24 WO PCT/EP2022/064128 patent/WO2022248514A1/de not_active Ceased
• 2023
  • 2023-11-15 CL CL2023003398A patent/CL2023003398A1/es unknown
  • 2023-11-21 CO CONC2023/0015731A patent/CO2023015731A2/es unknown
  • 2023-11-24 ZA ZA2023/10874A patent/ZA202310874B/en unknown

Patent Citations (10)

Also Published As

Similar Documents

Legal Events