EP1067088A1 - Draught breverage refrigerator - Google Patents

Draught breverage refrigerator Download PDF

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Publication number
EP1067088A1
EP1067088A1 EP00305488A EP00305488A EP1067088A1 EP 1067088 A1 EP1067088 A1 EP 1067088A1 EP 00305488 A EP00305488 A EP 00305488A EP 00305488 A EP00305488 A EP 00305488A EP 1067088 A1 EP1067088 A1 EP 1067088A1
Authority
EP
European Patent Office
Prior art keywords
beverage
carbon dioxide
heat exchanger
heat exchange
liquid
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Withdrawn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
EP00305488A
Other languages
German (de)
French (fr)
Inventor
Michael Ernest Garrett
Evelyn Arthur Shervington
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.)
BOC Group Ltd
Original Assignee
BOC Group Ltd
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 BOC Group Ltd filed Critical BOC Group Ltd
Publication of EP1067088A1 publication Critical patent/EP1067088A1/en
Withdrawn legal-status Critical Current

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25DREFRIGERATORS; COLD ROOMS; ICE-BOXES; COOLING OR FREEZING APPARATUS NOT OTHERWISE PROVIDED FOR
    • F25D31/00Other cooling or freezing apparatus
    • F25D31/002Liquid coolers, e.g. beverage cooler
    • F25D31/003Liquid coolers, e.g. beverage cooler with immersed cooling element
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B67OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
    • B67DDISPENSING, DELIVERING OR TRANSFERRING LIQUIDS, NOT OTHERWISE PROVIDED FOR
    • B67D1/00Apparatus or devices for dispensing beverages on draught
    • B67D1/08Details
    • B67D1/0857Cooling arrangements
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25DREFRIGERATORS; COLD ROOMS; ICE-BOXES; COOLING OR FREEZING APPARATUS NOT OTHERWISE PROVIDED FOR
    • F25D3/00Devices using other cold materials; Devices using cold-storage bodies
    • F25D3/10Devices using other cold materials; Devices using cold-storage bodies using liquefied gases, e.g. liquid air

Definitions

  • draught beverage denotes a beverage which is supplied from a large container, such as a barrel, or keg, via pipework to be discharged from a tap into a glass or other drinking vessel.
  • a large container such as a barrel, or keg
  • a compressed gas typically nitrogen or carbon dioxide
  • the expanded carbon dioxide may be allowed to pass through a liquid heat exchange medium within the heat exchanger before being vented to atmosphere. This both improves heat exchange between the carbon dioxide and the liquid medium and also promotes circulation of the medium.
  • the heat exchanger comprises at least two adjacent passages arranged for the flows of beverage and carbon dioxide therethrough.
  • a heat exchange medium is preferably provided to facilitate heat exchange therebetween.
  • Heat exchange occurs in such an arrangement between the passage, or coil, containing carbon dioxide and the liquid heat exchange medium and between the bubbles of carbon dioxide and the medium, and between the heat exchange medium and the passage containing the beverage, this latter exchange being assisted by the circulation of the medium.
  • the expansion of the carbon dioxide takes place surrounded by the liquid medium, so as to maximise the cooling of the medium.
  • the heat exchanger may comprise means adapted to sense the temperature of the beverage and/or of the heat exchange medium, means being provided to actuate the flow of carbon dioxide whenever the sensed temperature(s) rises above predetermined level(s).
  • This arrangement means that carbon dioxide is only used when cooling is actually required, and therefore carbon dioxide is conserved.
  • the heat exchanger is preferably connected in circuit with the pipework adjacent the tap and upstream thereof, so that substantially only that beverage to be dispensed is cooled.
  • the carbon dioxide is supplied from a source of liquid carbon dioxide, an orifice or control valve being provided and adapted to allow the liquid carbon dioxide to expand in a controlled manner, the valve being located within the heat exchanger, thereby to produce a reduction in its temperature according to the Joule-Kelvin effect.
  • the liquid carbon also moves from the liquid to the gas phase, so as to maximise its refrigerating effect in the heat exchanger.
  • Beverage is pumped from a source 2 by a pumping means 4 (which might be a conventional pump, or a source of a pumping gas such as nitrogen, as is known in the art) through pipework 6 (which might be of considerably length, as is the case where draught containers are located in a cellar a significant distance away from the point of dispensing of the beverage) to a tap 8, from which the beverage is discharged into a glass or other drinking vessel.
  • a pumping means 4 which might be a conventional pump, or a source of a pumping gas such as nitrogen, as is known in the art
  • pipework 6 which might be of considerably length, as is the case where draught containers are located in a cellar a significant distance away from the point of dispensing of the beverage
  • the pipework within the heat exchanger is in the form of a coil 12, which is in heat exchange relationship with another coil 14 by virtue of their mutual immersion in a heat exchange medium (L), such as water, contained in the heat exchanger 10.
  • the coils 12,14 are arranged so that they respectively pass countercurrent flows of beverage and carbon dioxide gas.
  • the carbon dioxide flows from a source of liquid carbon dioxide 16, through a control valve 18, into the coil 14 and hence out of the heat exchanger 10 to be vented to atmosphere (A).
  • the carbon dioxide can be allowed to exit the coil within the heat exchanger so as to bubble up through the heat exchange medium (L), thus both improving heat exchange therebetween and also promoting circulation of the medium and enhancing heat exchange between the coil 12 and the medium (L).
  • the carbon dioxide then vents to atmosphere through a vent at the top of the heat exchanger.
  • a temperature sensor 20 is provided to sense the temperature within the heat exchanger 10, and is operatively linked to a controller 22 which is effective to actuate the flow of carbon dioxide via an on/off valve 24 whenever the sensed temperature falls below a predetermined level. In this way carbon dioxide is conserved, so as not to overcool beverage in the coil 12 when the tap 8 is not open and beverage is static in the pipework 6. Means (not shown) may also be provided to sense the temperature of the beverage in the pipework immediately upstream of the tap 8 or in the coil 12, and effective to retain beverage in the coil 12 until it is at the predetermined, optimum temperature.
  • the system described above has several advantages over conventional draught beverage refrigeration devices. Since no mechanical refrigeration is required, there is no requirement for any external energy supply; beverage can be pumped through the system using a compressed gas such as nitrogen, and cooled by the carbon dioxide above. Cooling is only required for the actual beverage dispensed, and not for the entire barrel or keg, thus minimising the refrigeration required, and the beverage is dispensed at the optimum desired temperature.
  • the apparatus is simple to operate and maintain, and relatively inexpensive. For example, 25 kg of liquid carbon dioxide would yield over 4 MJ of "refrigeration", which would be adequate to chill about 100 litres of a typical beverage.
  • the cylinder 16 could be positioned within the heat exchanger 10 (not shown) so that the temperature reduction arising as carbon dioxide flows from the cylinder and hence the pressure therein is reduced can be used further to cool the liquid medium (L), so maximising the cooling effect.
  • the coil 14 is configured so as to minimise the possibility that it might become blocked in use by "plugs" of solid carbon dioxide; this might be achieved by the configuration of the coil 14, as is known in the art, or by using a known sintered block heat exchanger.
  • the valve 24 should preferably also be linked closely to the control valve 18 so as to ensure that the apparatus runs smoothly, and to avoid sudden carbon dioxide flow pulses, which would tend to create such "plugs".

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Devices That Are Associated With Refrigeration Equipment (AREA)
  • Devices For Dispensing Beverages (AREA)

Abstract

Refrigeration apparatus for use in the dispensing of draught beverages comprising a heat exchanger (12) through which flows beverage (6) to be dispensed, beverage flowing through the heat exchanger being in heat exchange relationship with a flow of a fluid cooled below ambient temperature following its controlled expansion, characterised in that the fluid comprises carbon dioxide (16) and in that the expanded carbon dioxide is vented to atmosphere.

Description

  • This invention relates to an apparatus for use in the dispensing of draught beverages. For the avoidance of doubt, the term "draught beverage" denotes a beverage which is supplied from a large container, such as a barrel, or keg, via pipework to be discharged from a tap into a glass or other drinking vessel. Typically, such draught beverage containers are located in a cellar some distance away from the dispensing tap, the beverage being pumped to the tap by means of a compressed gas, typically nitrogen or carbon dioxide.
  • Many types of draught beverage, particularly beers, lagers and the like, are cooled prior to being dispensed by means of small refrigeration units, because consumers usually prefer cool drinks. Conventional refrigeration units use chlorofluorocarbons and/or hydrofluorocarbons as a circulating refrigerant, however these substances are increasingly environmentally objectionable. Also, these refrigeration units require an external power supply for their operation. Thus, conventional refrigeration units are polluting and energy inefficient.
  • In accordance with the present invention, refrigeration apparatus for use in the dispensing of draught apparatus comprises a heat exchanger through which flows beverage to be dispensed, beverage flowing through the heat exchanger being in heat exchange relationship with a flow of a fluid cooled below ambient temperature following its controlled expansion, characterised in that the fluid comprises carbon dioxide and in that the expanded carbon dioxide is vented to atmosphere.
  • With such an arrangement, mechanical refrigeration is not required, hence there is no need for an external power supply. Accordingly, cool drinks can be supplied even where electrical power is unreliable or unavailable, such as in less developed countries or at outdoor events. Moreover, carbon dioxide is relatively unpolluting and, provided there is adequate ventilation, safe in use - it is also familiar to those who work in bars and public houses, where it is in widespread use for pumping and/or carbonating draught beverages.
  • The expanded carbon dioxide may be allowed to pass through a liquid heat exchange medium within the heat exchanger before being vented to atmosphere. This both improves heat exchange between the carbon dioxide and the liquid medium and also promotes circulation of the medium.
  • Advantageously, the heat exchanger comprises at least two adjacent passages arranged for the flows of beverage and carbon dioxide therethrough. A heat exchange medium is preferably provided to facilitate heat exchange therebetween. Heat exchange occurs in such an arrangement between the passage, or coil, containing carbon dioxide and the liquid heat exchange medium and between the bubbles of carbon dioxide and the medium, and between the heat exchange medium and the passage containing the beverage, this latter exchange being assisted by the circulation of the medium. Preferably, the expansion of the carbon dioxide takes place surrounded by the liquid medium, so as to maximise the cooling of the medium.
  • Advantageously, the heat exchanger may comprise means adapted to sense the temperature of the beverage and/or of the heat exchange medium, means being provided to actuate the flow of carbon dioxide whenever the sensed temperature(s) rises above predetermined level(s). This arrangement means that carbon dioxide is only used when cooling is actually required, and therefore carbon dioxide is conserved.
  • Where the beverage is dispensed through a tap connected to a source of the beverage by pipework, the heat exchanger is preferably connected in circuit with the pipework adjacent the tap and upstream thereof, so that substantially only that beverage to be dispensed is cooled.
  • Preferably, the carbon dioxide is supplied from a source of liquid carbon dioxide, an orifice or control valve being provided and adapted to allow the liquid carbon dioxide to expand in a controlled manner, the valve being located within the heat exchanger, thereby to produce a reduction in its temperature according to the Joule-Kelvin effect. Ideally, the liquid carbon also moves from the liquid to the gas phase, so as to maximise its refrigerating effect in the heat exchanger.
  • The invention will now be described by way of example and with reference to the accompanying drawing, which is a schematic diagram of an apparatus in accordance with the invention for refrigerating a draught beverage during the dispensing thereof.
  • Beverage is pumped from a source 2 by a pumping means 4 (which might be a conventional pump, or a source of a pumping gas such as nitrogen, as is known in the art) through pipework 6 (which might be of considerably length, as is the case where draught containers are located in a cellar a significant distance away from the point of dispensing of the beverage) to a tap 8, from which the beverage is discharged into a glass or other drinking vessel.
  • Immediately upstream of the tap 8 the beverage pipework 6 passes through a thermally-insulated heat exchanger 10. The pipework within the heat exchanger is in the form of a coil 12, which is in heat exchange relationship with another coil 14 by virtue of their mutual immersion in a heat exchange medium (L), such as water, contained in the heat exchanger 10. The coils 12,14 are arranged so that they respectively pass countercurrent flows of beverage and carbon dioxide gas. The carbon dioxide flows from a source of liquid carbon dioxide 16, through a control valve 18, into the coil 14 and hence out of the heat exchanger 10 to be vented to atmosphere (A). Alternatively, the carbon dioxide can be allowed to exit the coil within the heat exchanger so as to bubble up through the heat exchange medium (L), thus both improving heat exchange therebetween and also promoting circulation of the medium and enhancing heat exchange between the coil 12 and the medium (L). The carbon dioxide then vents to atmosphere through a vent at the top of the heat exchanger.
  • The reduction in temperature of the carbon dioxide arising from its expansion (and, preferably, its conversion from the liquid to the gaseous state) as it flows through the control valve 18 and the coil 14, cools the liquid medium (L) and, by conduction and convection, the beverage passing through coil 12.
  • A temperature sensor 20 is provided to sense the temperature within the heat exchanger 10, and is operatively linked to a controller 22 which is effective to actuate the flow of carbon dioxide via an on/off valve 24 whenever the sensed temperature falls below a predetermined level. In this way carbon dioxide is conserved, so as not to overcool beverage in the coil 12 when the tap 8 is not open and beverage is static in the pipework 6. Means (not shown) may also be provided to sense the temperature of the beverage in the pipework immediately upstream of the tap 8 or in the coil 12, and effective to retain beverage in the coil 12 until it is at the predetermined, optimum temperature.
  • It will be appreciated that the system described above has several advantages over conventional draught beverage refrigeration devices. Since no mechanical refrigeration is required, there is no requirement for any external energy supply; beverage can be pumped through the system using a compressed gas such as nitrogen, and cooled by the carbon dioxide above. Cooling is only required for the actual beverage dispensed, and not for the entire barrel or keg, thus minimising the refrigeration required, and the beverage is dispensed at the optimum desired temperature. The apparatus is simple to operate and maintain, and relatively inexpensive. For example, 25 kg of liquid carbon dioxide would yield over 4 MJ of "refrigeration", which would be adequate to chill about 100 litres of a typical beverage.
  • A number of alternative arrangements will occur to those skilled in the art. For example, the cylinder 16 could be positioned within the heat exchanger 10 (not shown) so that the temperature reduction arising as carbon dioxide flows from the cylinder and hence the pressure therein is reduced can be used further to cool the liquid medium (L), so maximising the cooling effect. Also, it is clearly desirable that the coil 14 is configured so as to minimise the possibility that it might become blocked in use by "plugs" of solid carbon dioxide; this might be achieved by the configuration of the coil 14, as is known in the art, or by using a known sintered block heat exchanger. The valve 24 should preferably also be linked closely to the control valve 18 so as to ensure that the apparatus runs smoothly, and to avoid sudden carbon dioxide flow pulses, which would tend to create such "plugs".

Claims (7)

  1. Refrigeration apparatus for use in the dispensing of draught beverages comprising a heat exchanger through which flows beverage to be dispensed, beverage flowing through the heat exchanger being in heat exchange relationship with a flow of a fluid cooled below ambient temperature following its controlled expansion, characterised in that the fluid comprises carbon dioxide and in that the expanded carbon dioxide is vented to atmosphere.
  2. Apparatus according to Claim 1 in which the heat exchanger comprises at least two adjacent passages arranged for the flows of beverage and carbon dioxide therethrough.
  3. Apparatus according to Claim 2 in which the heat exchanger includes a liquid heat exchange medium.
  4. Apparatus according to Claim 2 or Claim 3 in which the heat exchanger comprises means adapted to sense the temperature of the beverage and/or of the heat exchange medium, means being provided to actuate the flow of carbon dioxide whenever the sensed temperature(s) rise(s) above predetermined level(s).
  5. Apparatus according to any preceding claim in which the beverage is dispensed through a tap connected by pipework to a source of beverage, in which the heat exchanger is connected to the pipework adjacent the tap and upstream thereof in relation to the flow of beverage.
  6. Apparatus according to any preceding claim comprising a source of liquid carbon dioxide and a valve adapted to allow liquid carbon dioxide to expand in a controlled manner, the valve being located within the heat exchanger.
  7. Apparatus according to any preceding claim in which the expanded carbon dioxide is allowed to pass through a liquid heat exchange medium within the heat exchanger before being vented to atmosphere.
EP00305488A 1999-07-02 2000-06-29 Draught breverage refrigerator Withdrawn EP1067088A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB9915567 1999-07-02
GBGB9915567.3A GB9915567D0 (en) 1999-07-02 1999-07-02 Draught beverage refrigerator

Publications (1)

Publication Number Publication Date
EP1067088A1 true EP1067088A1 (en) 2001-01-10

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EP00305488A Withdrawn EP1067088A1 (en) 1999-07-02 2000-06-29 Draught breverage refrigerator

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EP (1) EP1067088A1 (en)
CA (1) CA2312620A1 (en)
GB (1) GB9915567D0 (en)
ZA (1) ZA200003248B (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2439555A (en) * 2006-06-29 2008-01-02 Gerald Lincoln Paczensky Draught beverage cooler
EP2031328A1 (en) * 2007-08-31 2009-03-04 Vin Service S.r.l. An equipment for refrigerating beverages
US9671148B2 (en) 2013-08-16 2017-06-06 Rroro's Innovations, Llc Apparatus and method for cooling a containerized fluid

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5140822A (en) * 1991-02-08 1992-08-25 The Coca-Cola Company Method and apparatus for chilling and carbonating a liquid using liquid carbon dioxide
WO1994012425A1 (en) * 1992-11-20 1994-06-09 Ab Konstruktions-Bakelit Method and apparatus for carbonating and chilling a liquid
WO1995009124A1 (en) * 1993-09-28 1995-04-06 Post-Mix Equipment Ab Method and device for cooling and carbonating a liquid
GB2307975A (en) * 1995-12-09 1997-06-11 Booth Dispensers Drink cooling
FR2762076A1 (en) * 1997-04-14 1998-10-16 Georges Maury Refrigerating capsule for inclusion in drinks can

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5140822A (en) * 1991-02-08 1992-08-25 The Coca-Cola Company Method and apparatus for chilling and carbonating a liquid using liquid carbon dioxide
WO1994012425A1 (en) * 1992-11-20 1994-06-09 Ab Konstruktions-Bakelit Method and apparatus for carbonating and chilling a liquid
WO1995009124A1 (en) * 1993-09-28 1995-04-06 Post-Mix Equipment Ab Method and device for cooling and carbonating a liquid
GB2307975A (en) * 1995-12-09 1997-06-11 Booth Dispensers Drink cooling
FR2762076A1 (en) * 1997-04-14 1998-10-16 Georges Maury Refrigerating capsule for inclusion in drinks can

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2439555A (en) * 2006-06-29 2008-01-02 Gerald Lincoln Paczensky Draught beverage cooler
GB2439555B (en) * 2006-06-29 2011-10-26 Gerald Lincoln Paczensky Draught beverage cooler
EP2031328A1 (en) * 2007-08-31 2009-03-04 Vin Service S.r.l. An equipment for refrigerating beverages
US9671148B2 (en) 2013-08-16 2017-06-06 Rroro's Innovations, Llc Apparatus and method for cooling a containerized fluid

Also Published As

Publication number Publication date
CA2312620A1 (en) 2001-01-02
ZA200003248B (en) 2001-01-17
GB9915567D0 (en) 1999-09-01

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