Beverage dispense system

Information

  • Patent Grant
  • 6609391
  • Patent Number
    6,609,391
  • Date Filed
    Friday, August 9, 2002
    21 years ago
  • Date Issued
    Tuesday, August 26, 2003
    20 years ago
Abstract
In one aspect the present invention provides a chilled beverage dispense system including a beverage recirculation loop and a glycol recirculation loop, a first chiller to cool the beverage and a second chiller to cool the glycol, a heat exchanger through which the cooled beverage and the cooled glycol are passed to further cool the beverage and a dispense valve located in the beverage recirculation loop downstream of the heat exchanger. The glycol recirculation loop including a bypass valve upstream of the heat exchanger, whereby in a standby, non-dispense mode the glycol bypasses the heat exchanger and when a beverage dispense is required, the glycol is diverted through the heat exchanger.
Description




BACKGROUND




This invention relates to a beverage dispense system in which a chilled beverage is presented to the consumer. It is particularly applicable to beverages such as beer or lager.




Conventional beer/lager cooling systems typically have a bulk beverage supply located at a separate location (called a cellar room) from the bar counter and the beverage is chilled in the cellar by being passed through an ice bank cooler to a temperature just below its ultimate dispense temperature. The chilled beverage is then pumped from the cellar room to the bar within an insulated python.




If one wishes to dispense the beverage at very cold temperatures e.g. below 0° C., such a system has problems. In particular, one has to chill the beverage in the cellar room to an even lower temperature. Whilst one can utilize glycol mixtures in the ice bank cooler instead of water to obtain lower beverage temperatures, the lower the required beverage temperature the greater the risk that it will freeze solid in the cooler or the python during periods when the beverage is not being dispensed. It will then be impossible to operate the dispense system when the next drink is required to be dispensed.




It is an object of the invention to provide a system which is capable of successfully dispensing a chilled beverage from a bulk supply to a temperature close to the freezing point of the beverage.




SUMMARY OF THE INVENTION




Accordingly in one aspect the invention provides a chilled beverage dispense system including a beverage recirculation loop and a glycol recirculation loop, a first chiller to cool the beverage and a second chiller to cool the glycol, a heat exchanger through which the cooled beverage and the cooled glycol are passed to further cool the beverage and a dispense valve located in the beverage recirculation loop downstream of the heat exchanger, the glycol recirculation loop including a bypass valve upstream of the heat exchanger, whereby in a standby, non-dispense mode the glycol bypasses the heat exchanger and when a beverage dispense is required, the glycol is diverted through the heat exchanger.




In another aspect the invention provides a method of dispensing a cooled beverage in which the beverage is passed in a recirculation loop through a first chiller to cool it and then through a heat exchanger and then via a dispense head to return to the first chiller, a glycol coolant is passed in a recirculation loop through a second chiller to a bypass valve to avoid passing through the heat exchanger when beverage is not being dispensed and then back to the second chiller, the bypass valve being actuated when a dispense is required whereby the glycol coolant passes through the heat exchanger to further cool the beverage before it is dispensed.




It will be appreciated, therefore, that the beverage can be maintained in its first cooled condition, e.g. from 0.5° to 1.5° C., typically 1° C., in the standby mode by means of recirculation through its first chiller but that when dispense is required it is further cooled by heat exchange within the heat exchanger with the colder glycol that is now diverted from its bypass mode to flow through the heat exchanger. The glycol may be maintained at, e.g. from −8.5° to −9.5° C., typically −9° C., to give a second cooling to the beverage which may then be dispensed at e.g. from −4° to −5° C., typically −4.5° C. It will be appreciated that these ranges will vary depending on the beverage to be dispensed.




The heat exchanger may be of any convenient plate, tube or other construction.




During standby mode, glycol remaining in the heat exchanger will, of course, warm up from its chilled temperature but will be maintained at about the temperature of the recirculating beverage.




If the heat exchanger is located close to the dispense valve so that the amount of beverage at any point in time from the heat exchanger to the dispense valve is small relative to the amount to be dispensed, it may be possible to arrange a control system that commences dispense at the same time as operating the bypass valve to divert the glycol through the heat exchanger. However, it is preferred that a control system be used that, on a dispense being actuated, first operates the bypass valve to further cool the beverage and then, after a delay, opens the dispense valve. The delay may be a predetermined time or may be determined by a temperature sensor for the beverage positioned between the heat exchanger and the dispense valve. In this latter embodiment, the dispense valve will only open once the temperature sensor indicates to the control system that the required dispense temperature has been reached.




The glycol coolant used may be pure glycol but will usually be a water/glycol mixture, e.g. of proportions from 25:75 to 50:50, depending on the degree of cooling required.




In a preferred embodiment a water recirculation loop is included in the system in order to provide a spray of chilled water onto a glass or other receptacle into which the beverage is to be dispensed. The water may conveniently be chilled in the same first chiller used for the beverage recirculation loop. This first chiller may be a single ice bank cooler of conventional design with a portion of the beverage recirculation loop and of the water recirculation loop immersed in water/ice within the cooler.




A water dispense valve is provided in the water recirculation loop and controlled quantities of chilled water at from, e.g. 0.5° to 1.5° C., may be sprayed onto the beverage receptacle in response to signals from the beverage dispense control system. The receptacle may be sprayed before, during and/or after beverage is dispensed into it.




The invention provides a system in which cooler than usual beverage can be dispensed safely and without risk of freezing. A conventional ice bank cooler can be used for the initial cooling (first chiller) and to maintain the cooled effect between dispenses and the heat exchanger is used to provide the extra cooling when required for a dispense. Between dispenses the heat exchanger is bypassed by the recirculating glycol coolant and the system “idles” with the beverage at the temperature achieved by the first chiller.




The dispense valve can be permanently chilled in the beverage recirculation loop and so does not harmfully affect dispense temperature after standing unused.











DESCRIPTION OF THE DRAWINGS




A better understanding of the structure, function, operation, and advantages of the present invention can be had by reference to the Detailed Description that is set out below and that refers to the following drawing figures, wherein:





FIG. 1

is a schematic illustration of a beverage dispense system of the present invention:





FIG. 2

is a similar illustration to

FIG. 1

of a modified system of the present invention; and





FIG. 3

is a diagrammatic representation of possible sequences in time.











DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS




In

FIG. 1

a first chiller


10


, which is an ice bank cooler, contains portions of recirculation loops for water and for a beverage.




The water flows from a source (not shown), e.g. the mains, via an optional boost pump


11


and a pressure regulator


12


into an outer water loop


13


in chiller


10


which continues into an inner water loop


14


. Loop


14


includes a recirculation pump


15


. Cooled water from inner loop


14


is pumped from chiller


10


around a recirculation loop


16


. A solenoid valve


17


, adjacent a rotatable turntable


18


underneath a beverage dispense head


19


, is connected to loop


16


but is closed in the idle, non-dispense mode. A water line


20


leads from the solenoid valve to a spray head


21


through which cooled water may be sprayed onto a glass


22


underneath the dispense head


19


when solenoid valve


17


is opened. In the idle mode, the water returns to chiller


10


via an optional non-return valve


23


and continues to circulate around its inner loop


14


and its recirculation loop


16


. The water in outer loop


13


in chiller


10


is standing water while valve


17


is closed. When valve


17


is opened to commence spraying of the glass water pressure from its source, boosted if required by pump


11


, introduces fresh water via loop


13


into loops


14


and


16


.




An optional bleed line


24


is connected into recirculation loop


16


.




Beverage flows from a source (not shown) via metering turbine


24


into an outer beverage loop


25


which passes through chiller


10


and out again where it joins an inner loop


26


. Loop


26


passes through a recirculating pump


27


and then back into the chiller. If desired a flow turbine may be included in this loop


26


, e.g. between pump


27


and the junction of loops


25


and


26


.




The cooled beverage leaves chiller


10


in a recirculation loop


28


and passes through a heat exchanger


29


. On leaving heat exchanger


29


where in dispense mode it is further cooled by a glycol line to be described below, the beverage passes through a temperature sensor


30


, e.g. a thermistor housing, and from there through dispense head


19


and via a non-return valve


31


to the chiller


10


. Between non-return valve


31


and chiller


10


the beverage passes through a restrictor tube or compensator valve


33


to control the speed of beverage recirculation to prevent, e.g. decarbonation. The recirculation speed may be kept, for example, to about 1½ liters per minute, which is a typical dispense rate. Restrictor


33


may be dispensed with if the above-mentioned optional flow turbine is used in conjunction with pump


27


to control the flow speed. If the system remains in idle mode without dispense for some time, predetermined, the speed of beverage circulation may be reduced. It may then be speeded up again for dispense and for a period after dispense to maintain the desired temperature. The beverage continues to be recirculated around its loop


28


and inner loop


26


in the idle mode. The beverage in outer loop


25


is standing beverage during the idle mode but when the dispense head


19


is operated to dispense into glass


22


, fresh beverage flows into loops


25


and


26


from the source.




A bleed line


32


is connected into recirculation loop


28


.




The water and beverage recirculation lines may be contained within a conventional python and may conveniently be contained in a single python for a substantial portion of their lengths. This single python line is indicated generally by arrows AA.




The glycol coolant is cooled in chiller


40


and is circulated around a recirculation loop


41


by pump


42


. The glycol flow is indicated by block headed arrows plus line headed arrows. From chiller


40


the glycol travels to bypass valve


43


adjacent heat exchanger


29


. In the idle, nondispense state the glycol bypasses the heat exchanger and returns to chiller


40


for recirculation. The recirculation lines of loop


41


may also be contained within a conventional python, indicated generally by arrows BB. When the bypass valve


43


is opened the glycol flow is diverted through the heat exchanger where it causes further cooling of the beverage passing through in its loop


28


.




Glycol chiller


40


has an overflow reservoir


44


whose purpose will be described in more detail below. Reservoir


44


contains a heating element


45


and a thermostat


46


. Glycol from reservoir


44


can be pumped by pump


47


and non-return valve


48


into the heat exchanger


29


from where it leaves in the glycol recirculation loop


41


to return to chiller


40


.




One possible routine for operation of the dispense system is now described.




In the idle, non-dispense situation the beer and water are recirculating through their recirculation loops at about, say, 1° C. The glycol is recirculating in its loop, missing out the heat exchanger


29


, at about, say, −9° C.




A glass


22


is placed on turntable


18


and the control unit (not shown) is pressed to select a ½ pint or 1 pint dispense of the beverage.




This actuates the bypass valve


43


which diverts glycol in its recirculation loop to pass through the heat exchanger to further cool the beverage. Solenoid


17


is also actuated and cold water is sprayed via head


21


onto the glass


22


. The turntable


18


motor mechanism (not shown) is also started so that glass


22


rotates on the turntable.




Thermistor


30


is sensing the beer temperature as it leaves the heat exchanger


29


and, when it signals that the desired dispense temperature has been reached the dispense valve in dispense head


19


is opened to allow the cooled beverage to be dispensed into the glass. The metering turbine


24


is actuated by the flow of beer in from the source to replace dispensed beer and the water spray and turntable rotation are maintained as dispense continues.




If desired, during dispense an ultrasonic shock can be given to the beverage in the glass on the turntable at a predetermined point of the dispense as indicated by the metering of turbine


24


. This can improve the appearance and presentation of the beverage in the glass e.g. by assisting in the generation of a foamed head on the beverage. Means to provide such a shock are not shown here but are known in the art. The water solenoid


17


closes at another predetermined point of the metered dispense. The glycol bypass valve


43


is switched to stop further cooling, again at a predetermined point of the metered dispense, usually towards the end of the metered dispense. As bypass valve


43


is so switched, the glycol pump


47


is actuated to provide a timed flow, e.g. of from 4 to 5 seconds, at about 0.5 liters/minute, of glycol warmed by heater


45


to about, say, 8° C. through the heat exchanger


29


. This is just a sufficient amount of heat glycol to flush colder glycol from the heat exchanger and thereby prevents the risk of beverage freezing in the heat exchanger when the dispense has finished. (It will be appreciated that the bypass arrangement prevents the heat exchanger from getting too cold during periods of no dispense which would also have the risk of beverage freezing.).




A second ultrasonic shock may be administered to the beverage in the glass just before or at the end of the dispense to nucleate the beverage for final appearance.




When metering turbine


24


indicates that the required amount of beverage has been dispensed, the control system closes the dispense valve at the dispense head. The turntable may be timed to continue to rotate for a preset but adjustable time after dispense is finished. The water solenoid valve


17


can be re-opened after a preset but adjustable time to provide a further spray onto the exterior of the glass for a short time, e.g. 2 or 3 seconds, to clear condensation on the glass as the ice crystal nucleation occurs in the beverage. This water spray and the turntable rotation then conveniently stop to bring the dispense cycle to an end. The system then reverts to its stable, idle mode.




When the glycol from reservoir


44


is returned to chiller


40


, this excess volume of glycol in the chiller overflows through overflow pipe


48


into reservoir


44


to maintain the normal level of glycol in the chiller.




The above routine is illustrated diagrammatically in FIG.


3


. It will be appreciated that the routine may be varied in a number of respects, particularly in respect of the timings, e.g. of the glass spraying stages, the ultrasonic shocks and the turntable over run at the end of the dispense.




In

FIG. 2

is shown a modification of the system of FIG.


1


. Like parts have been given the same reference numerals and will not all be described again in detail here.




The beverage and water chiller and recirculation loops are the same as in FIG.


1


and the pumping, monitoring and metering means are also the same as are the heat exchanger and dispense head/turntable arrangements.




The glycol recirculation loop, chiller and reservoir arrangements are also the same but the heated glycol line from the reservoir to the heat exchanger takes a different route. In the

FIG. 2

arrangement, instead of the warmed glycol from reservoir


44


being pumped directly to heat exchanger


29


it is now pumped to the heat exchanger via a glycol line


50


which passes through chiller


10


before reaching the heat exchanger. This is to bring the glycol to the same temperature as the recirculating beverage before it passes into the heat exchanger. As indicated a portion of glycol line


50


may be accommodated in the python AA for the water and beverage recirculation loops. Otherwise, the operation of the glycol line to the thermostat is the same as described above with reference to FIG.


1


.




It will be appreciated that many further modifications are possible within the scope of the present invention. For example, chillers


10


and


40


may conveniently be positioned in a single housing.




In the unlikely event of the system freezing at some point, this may be detected by an optional turbine, e.g. the optional flow turbine referred to in conjunction with pump


27


above. This turbine by indicating no flow when flow is expected can signal to the control to shut down the system for investigation.



Claims
  • 1. A method of dispensing a liquid from a dispense head, comprising the steps of:circulating a liquid through a liquid circulation line the liquid circulation line passing through a first heat exchanger, the first heat exchanger remote form the dispense head and cooled by a mechanical refrigeration system for cooling the liquid to a first temperature and the liquid cooling line then passing to and through a second heat exchanger and then from the second heat exchanger to a dispense head adjacent thereto, circulating a cooling fluid through a cooling fluid line the cooling fluid line passing through a third heat exchanger, the third heat exchanger remote form the dispense head and cooled by a mechanical refrigeration system for cooling the cooling fluid to a second temperature below the first temperature and the cooling fluid line passing through a bypass valve, operating the bypass valve to initiate a flow of the cooling fluid through the second heat exchanger to cool the liquid flowing there through, operating the dispense head to dispense the liquid there from.
  • 2. The method as defined in claim 1, and further including the step of: operating the bypass valve to terminate the flow of cooling fluid through the second heat exchanger to prevent freezing of any of the liquid flowing there through.
  • 3. The method as defined in claim 1, and further including the step of:warming the second heat exchanger after the liquid has been dispensed from the dispense head to prevent freezing of any of the liquid flowing there through.
  • 4. The method as defined in claim 1, and further including the steps of:sensing the temperature of the liquid adjacent the dispense head prior to dispensing the liquid there from and then dispensing the liquid there from when a predetermined dispense temperature thereof is reached.
  • 5. The method as defined in claim 1, and further including the steps of:sensing the flow of the liquid through the liquid circulation line and operating the bypass valve to stop flow of the cooling fluid through the second heat exchanger and/or initiating warming of the second heat exchanger if flow of the liquid is sensed to have stopped.
  • 6. A liquid dispenser, comprising:a liquid circulation line extending through a first heat exchanger, the first heat exchanger remote form the dispense head and cooled by a mechanical refrigeration system for cooling the liquid flowing there through to a first temperature, and the liquid circulation line extending through a second heat exchanger adjacent the dispense head and from the second heat exchanger to the liquid dispense head, a cooling fluid circulating line extending through a third heat exchanger, the third heat exchanger remote form the dispense head and cooled by a mechanical refrigeration system for cooling the cooling fluid flowing there through to a second temperature below the first temperature, and the cooling fluid circulation line extending through a bypass valve, the bypass valve operable by a control to either direct the flow of cooling fluid to permit circulation thereof through the second heat exchanger for heat exchange cooling of the liquid passing there through or to bypass the second heat exchanger and be circulated back to the third heat exchanger, and the control also for operating the dispense head to dispense the liquid from the dispense head while cooling fluid is flowing through the second heat exchanger.
  • 7. The fluid dispenser as defined in claim 6, and further including a temperature sensor adjacent the dispense head and connected to the control and the control first operating the bypass valve to cool the liquid passing through the second heat exchanger and subsequently dispensing the liquid from the dispense head when a predetermined dispense temperature of the liquid is sensed.
  • 8. A dispensing system for dispensing a beverage from a dispensing head, the beverage dispensing system, comprising:a beverage circulation line extending through a water bath type heat exchanger cooled by a mechanical refrigeration system and located at a position remote from the dispense head, the beverage flowing from a source thereof through a beverage line, the beverage line having a portion thereof immersed in the water bath heat exchanger for heat exchange cooling thereof to a first temperature and flowing there from to a second heat exchanger adjacent the dispense head and extending from the second heat exchanger to the beverage dispense head, a cooling fluid circulating line extending through a third heat exchanger, the third heat exchanger remote form the dispense head and cooled by a mechanical refrigeration system for cooling the cooling fluid flowing there through to a second temperature below the first temperature, and the cooling fluid circulation line extending through a bypass valve, the bypass valve operable by a control to either direct the flow of cooling fluid to permit circulation thereof through the second heat exchanger for heat exchange cooling of the beverage passing there through or to bypass the second heat exchanger and be circulated back to the third heat exchanger, and the control also for operating the dispense head and the bypass valve to dispense the beverage from the dispense head while cooling fluid is flowing through the second heat exchanger.
  • 9. The dispensing system as defined in claim 8, and further including a temperature sensor adjacent the dispense head and connected to the control and the control first operating the bypass valve to cool the beverage passing through the second heat exchanger and subsequently dispensing the beverage from the dispense head when a predetermined dispense temperature of the beverage is sensed.
  • 10. The dispensing system as defined in claim 8, and further including a beverage flow meter for sensing the volume and flow of the beverage as it is dispensed from the dispensing head.
  • 11. The dispensing system as defined in claim 8, and the control, during a dispense of the beverage from the dispense head, operating the bypass valve to stop flow of the cooling fluid through the second heat exchanger if a predetermined low temperature is sensed by the temperature sensor.
  • 12. The dispensing system as defined in claim 8, and further including a second cooling fluid line emanating from the third heat exchanger and the third heat exchanger including a heater for separately warming a portion of the cooling fluid flowing through the second cooling fluid line and the second cooling fluid line for providing the warmed cooling fluid under pressure to the second heat exchanger and the control for operating the pump to flush any colder cooling fluid there from to insure against freezing of the beverage.
  • 13. The dispensing system as defined in claim 8, and further including a pressurized water line emanating from the water bath heat exchanger for cooling the water and the line for delivering the cooled water to a separate dispense point adjacent the dispense head, and a turntable positioned below the dispense head for receiving a beverage receptacle thereon and operable by the control when beverage is dispensed from the dispense head into the beverage receptacle to rotate the beverage receptacle and the water line including a valve operable by the control to spray the cooled water onto the exterior surface of the beverage receptacle as the beverage receptacle is rotated by the turntable.
  • 14. The dispensing system as defined in claim 13, and including a device for administering an ultra-sonic shock to the beverage in the beverage receptacle for initiating ice particle formation in the beverage.
  • 15. The dispensing system as defined in claim 12, and the second cooling fluid line first passing through the water bath heat exchanger to warm the cooling fluid to the first predetermined temperature.
  • 16. The dispensing system as defined in claim 8, and the cooling fluid including glycol.
  • 17. The dispensing system as defined in claim 8, and the beverage including a percentage by volume of alcohol.
Parent Case Info

The present application is a continuation of application Ser. No. 09/838,925 filed Apr. 20, 2001, now U.S. Pat. No. 6,431,403.

US Referenced Citations (9)
Number Name Date Kind
3958428 Kelso May 1976 A
4676400 Lamont et al. Jun 1987 A
4679408 Nelson Jul 1987 A
5694787 Cleleand et al. Dec 1997 A
5743108 Cleland Apr 1998 A
5873259 Spillman Feb 1999 A
5996842 Riley et al. Dec 1999 A
6341500 Paxman Jan 2002 B1
6431403 Davis Aug 2002 B1
Continuations (1)
Number Date Country
Parent 09/838925 Apr 2001 US
Child 10/216486 US