METHOD AND DEVICE FOR DISPENSING A BEVERAGE ENRICHED WITH A GAS FROM A GAS PRESSURE VESSEL

Abstract

In a method for dispensing a beverage in which a gas from a gas pressure vessel in which the gas is stored under pressure is mixed with the beverage, it is provided that the beverage is transported out of the storage container (2) by a pump (3) and that the pressure of the gas is lowered to less than 0.5 bar, more preferably less than 100 mbar, above ambient pressure and is fed to the aspirated beverage on the suction side of the pump (3).

Claims

1. A method for dispensing a beverage, the method comprising: mixing a gas from a gas pressure vessel in which the gas is stored under pressure with the beverage, delivering the beverage from a storage vessel (2) by a pump (3), and reducing a pressure of the gas is reduced to less than 0.5 above the ambient pressure, and feeding the gas at a suction side of the pump (3), to the beverage drawn in by the pump.

2. The method as claimed in claim 1, wherein the beverage is a cold-brew coffee.

3. The method as claimed in claim 1, further comprising adding at least one of water or ice to the beverage.

4. The method as claimed in claim 1, wherein the gas is nitrogen.

5. The method as claimed in claim 1, wherein the beverage is stored in a storage vessel (2) as a beverage concentrate, and the storage vessel (2) is cooled and the beverage is dispensed as a cold beverage.

6. The method as claimed in claim 1, wherein the pump (3) comprises a geared pump.

7. The method as claimed in claim 1, further comprising delivering the beverage enriched with gas to a beverage outlet (7) by a counterpressure element (6) arranged downstream from the pump (3).

8. The method as claimed in claim 7, wherein the counterpressure element (8) comprises a restrictor or a static mixer.

9. The method as claimed in claim 1, further comprising arranging a gas metering valve (13) by which a volume of the gas fed to the beverage is metered in a feed line (12) for the gas fed to the sucked-in beverage.

10. A beverage dispensing device for dispensing a beverage enriched with a gas at a beverage outlet (7), the device comprising: a high-pressure connection (19) for connecting a gas pressure vessel in which the gas under pressure is stored, a pump (3) for delivering the beverage to the beverage outlet (7) via a suction line (4) from the storage vessel (2), and a pressure relief device (17) connected on an input side to the high-pressure connection (19) that is configured to reduce the pressure of the gas to a pressure less than 0.5 bar above ambient pressure, and which is connected on an output side to a gas feed line (12, 12′) which opens into the suction line (4) in order to feed in the gas at a reduced pressure to the sucked-in beverage at a suction side of the pump (3).

11. The beverage dispensing device as claimed in claim 10, further comprising a counterpressure element (6), by which the beverage enriched with gas adapted to be is delivered to the beverage outlet (7), arranged downstream from the pump (3) in a delivery direction.

12. The beverage dispensing device as claimed in claim 11, wherein the counterpressure element (6) comprises a restrictor or a static mixer.

13. The beverage dispensing device as claimed in claim 10, wherein the pump comprises a geared pump.

14. The beverage dispensing device as claimed in claim 10, further comprising a gas metering valve (13) arranged in the gas feed line (12) that is configured for metering a volume of the gas fed to the beverage.

15. The beverage dispensing device as claimed in claim 14, wherein the gas metering valve is a timed shut-off valve.

16. The method of claim 3, wherein the beverage is stored in a storage vessel (2) as a beverage concentrate, and the water is added to the beverage concentrate upstream or downstream from the pump.

17. The method of claim 8, wherein the static mixer is a spiral mixer.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0022] Further advantages and properties of the invention emerge from the following description of an exemplary embodiment with the aid of the drawings, in which:

[0023] FIG. 1 shows a water flow diagram of a device for dispensing a coffee beverage enriched with gas, and

[0024] FIG. 2 shows a partially cutaway isometric illustration of a counterpressure element, in the form of a spiral mixer, used in the exemplary embodiment.

DETAILED DESCRIPTION

[0025] The device illustrated in FIG. 1 in the form of a water flow diagram comprises a storage vessel 2 with a cold-brew coffee beverage, an electric pump 3 which is connected to the storage vessel 2 on the suction side via a suction line 4, and a counterpressure element 6, in the form of a spiral mixer, attached to the discharge side of the pump 3. The outlet line 5′ leads from the spiral mixer 6 to a beverage outlet 7 at which the cold-brew coffee beverage enriched with gas is dispensed into a drinking vessel 8 positioned below it. The beverage outlet can here be integrated into the outlet head of a fully automatic coffee machine such that the coffee beverage enriched or frothed with gas can be dispensed as a further beverage option by the fully automatic coffee machine.

[0026] A flow meter 9, by which the amount of beverage can be metered, and a shut-off valve 10 which is opened at the beginning of the beverage preparation and is closed once the beverage preparation is complete in order to prevent fluid still situated in the line 4 from flowing back, are situated in the suction line 4. A gas feed line 12 opens into the suction line 4. A gas metering valve 13, a fixed orifice plate 14, and a non-return valve 15 are situated in the gas feed line 12. In the exemplary embodiment, the gas metering valve 13 is configured as a timed air valve, i.e. as a switching valve which intermittently opens and closes in quick succession. The frequency at which the air valve operates can here lie within the range of 10 and 30 Hz. The non-return valve 15 serves only to restrict or prevent liquid from penetrating the air feed line.

[0027] The pump 3, the counterpressure element 6, the flow meter 9 and the gas metering valve 13 are combined to form a pump module or a pump assembly 1. This furthermore comprises the shut-off valve 10 in the feed line 4 and also the non-return valve 15 and the orifice plate 14 in the gas feed line 12.

[0028] The pump module 1 and the storage vessel 2 are arranged in a refrigerator 16. The storage vessel 2 is here designed as a disposable vessel with a pouch situated in a cardboard box (bag in box, BiB, packaging). A pressure relief device 17 and a shut-off valve 18 are connected outside the refrigerator 16 to the gas feed line 12′ leading to the pump module 1. A gas pressure vessel (not shown here), for example a conventional gas canister at approximately 200 bar gas pressure, can be connected on the input side via the pressure relief device 17. The pressure relief device 17 is configured or set in the exemplary embodiment such that it reduces the pressurized gas at the input to an output pressure of just 50 mbar at which the gas is fed into the feed line 4 at the output side of the pump. At the pressure relief device (or pressure-reducing valve), the output pressure is fed as a control input and ensures, by a pressure transducer, that a pressure valve blocks flow when the predetermined target output pressure is exceeded and opens when the pressure falls below it. The output pressure thus cannot rise above this pre-set value. A piston or a diaphragm can here serve as a pressure transducer.

[0029] Lastly, a flushing connection 20, which opens into the gas feed line 12 upstream from the non-return valve 15 via a shut-off valve 21 and a flushing line 22, is shown in the exemplary embodiment. After a product has been prepared, a flushing process with cold or warm water can be performed via this flushing line 22. For this purpose, the valve 10 is closed at the product input, the valve 21 is opened at the flushing water inflow 20, and the pump 3 is set in operation. A collecting vessel is placed below the beverage outlet 7 in order to collect the flushing water. The flushing process serves in particular to flush the non-return valve 15 so that it cannot clog up and jam. A further flushing valve 21′ connected in parallel in the exemplary embodiment to the valve 21 is provided optionally to connect a further pump module (not shown here), which is optionally housed in the refrigerator 16, to the flushing connection 20.

[0030] In order to dispense a frothed cold-brew coffee beverage, the valve 10 is opened at the product input 4′ and the pump 3 is set in operation. A ready-made beverage stored in the storage vessel 2 is sucked in therefrom and delivered to the beverage outlet 7 via the spiral mixer 6.

[0031] At the same time, the shut-off valve 18 at the gas inlet is opened and nitrogen from the gas pressure vessel connected to the gas connection 19 flows via the gas metering valve 13 by which the amount of gas fed in can be metered, the orifice plate 14, and the non-return valve 15 to the gas feed line 12 which opens into the suction line 4. The pump 3 thus sucks in gas from the gas connection 19 in addition to ready-to-drink beverage from the storage vessel 2. By virtue of the spiral mixer 6, a high pressure is generated at the pump output or in the pump 3. This results in mixing of the air/beverage mixture in the pump and in this way generates a creamy and frothy fluid, enriched with gas, which is dispensed at the beverage outlet 7.

[0032] A spiral mixer 6, employed as a counterpressure element in FIG. 1, is illustrated in FIG. 2. A spiral mixer is a so-called static mixer in which a plurality of spirals 62, 63, offset relative to one another in each case by 90° and arranged one behind the other, are arranged in a tubular housing 61. The successive spirals moreover each have an opposite direction of rotation. Each spiral splits the stream of flowing liquid into two partial streams. These are in turn split into partial streams at each transition to the respective following spiral and in each case merged with partial streams from the preceding spiral. In this way, the stream of liquid is mixed. The spiral mixer moreover represents a largely laminar flow resistance without there being any need here for the flow cross-section to be reduced. The housing 61 of the mixer 6 is shown in FIG. 2 in a partially cut-away view so that the spiral sections 62, 63, each offset by 90° and situated inside, can be seen.