EP2295369A1 - Ice bank cooler - Google Patents
Ice bank cooler Download PDFInfo
- Publication number
- EP2295369A1 EP2295369A1 EP10194049A EP10194049A EP2295369A1 EP 2295369 A1 EP2295369 A1 EP 2295369A1 EP 10194049 A EP10194049 A EP 10194049A EP 10194049 A EP10194049 A EP 10194049A EP 2295369 A1 EP2295369 A1 EP 2295369A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- coolant
- temperature
- dispense
- cooler
- concentrate
- 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.)
- Granted
Links
- 239000002826 coolant Substances 0.000 claims abstract description 112
- 235000013361 beverage Nutrition 0.000 claims abstract description 55
- 230000004044 response Effects 0.000 claims abstract description 22
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 91
- 238000001816 cooling Methods 0.000 claims description 86
- 238000000034 method Methods 0.000 claims description 14
- 238000013019 agitation Methods 0.000 claims description 3
- 238000012544 monitoring process Methods 0.000 claims description 3
- 235000008504 concentrate Nutrition 0.000 description 97
- 239000012141 concentrate Substances 0.000 description 97
- 239000003085 diluting agent Substances 0.000 description 55
- 239000000203 mixture Substances 0.000 description 35
- 230000008901 benefit Effects 0.000 description 9
- 239000006188 syrup Substances 0.000 description 9
- 235000020357 syrup Nutrition 0.000 description 9
- 239000012809 cooling fluid Substances 0.000 description 8
- 238000005265 energy consumption Methods 0.000 description 7
- 239000012530 fluid Substances 0.000 description 7
- 238000013461 design Methods 0.000 description 6
- 239000007789 gas Substances 0.000 description 6
- 238000009413 insulation Methods 0.000 description 6
- 238000009434 installation Methods 0.000 description 5
- 230000004048 modification Effects 0.000 description 5
- 238000012986 modification Methods 0.000 description 5
- 235000014214 soft drink Nutrition 0.000 description 5
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 4
- 235000014171 carbonated beverage Nutrition 0.000 description 4
- 230000001419 dependent effect Effects 0.000 description 3
- 238000001125 extrusion Methods 0.000 description 3
- 239000000796 flavoring agent Substances 0.000 description 3
- 235000019634 flavors Nutrition 0.000 description 3
- 238000012546 transfer Methods 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 235000016795 Cola Nutrition 0.000 description 2
- 241001634499 Cola Species 0.000 description 2
- 235000011824 Cola pachycarpa Nutrition 0.000 description 2
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 2
- 235000013334 alcoholic beverage Nutrition 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 239000004615 ingredient Substances 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
- 238000005086 pumping Methods 0.000 description 2
- 241001482175 Pythonidae Species 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 230000002528 anti-freeze Effects 0.000 description 1
- 235000013405 beer Nutrition 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 235000019987 cider Nutrition 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 235000015203 fruit juice Nutrition 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 1
- 239000012774 insulation material Substances 0.000 description 1
- 235000015095 lager Nutrition 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B67—OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
- B67D—DISPENSING, DELIVERING OR TRANSFERRING LIQUIDS, NOT OTHERWISE PROVIDED FOR
- B67D1/00—Apparatus or devices for dispensing beverages on draught
- B67D1/0015—Apparatus or devices for dispensing beverages on draught the beverage being prepared by mixing at least two liquid components
- B67D1/0021—Apparatus or devices for dispensing beverages on draught the beverage being prepared by mixing at least two liquid components the components being mixed at the time of dispensing, i.e. post-mix dispensers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B67—OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
- B67D—DISPENSING, DELIVERING OR TRANSFERRING LIQUIDS, NOT OTHERWISE PROVIDED FOR
- B67D1/00—Apparatus or devices for dispensing beverages on draught
- B67D1/08—Details
- B67D1/0857—Cooling arrangements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B67—OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
- B67D—DISPENSING, DELIVERING OR TRANSFERRING LIQUIDS, NOT OTHERWISE PROVIDED FOR
- B67D1/00—Apparatus or devices for dispensing beverages on draught
- B67D1/08—Details
- B67D1/0857—Cooling arrangements
- B67D1/0858—Cooling arrangements using compression systems
- B67D1/0861—Cooling arrangements using compression systems the evaporator acting through an intermediate heat transfer means
- B67D1/0864—Cooling arrangements using compression systems the evaporator acting through an intermediate heat transfer means in the form of a cooling bath
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B67—OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
- B67D—DISPENSING, DELIVERING OR TRANSFERRING LIQUIDS, NOT OTHERWISE PROVIDED FOR
- B67D1/00—Apparatus or devices for dispensing beverages on draught
- B67D1/08—Details
- B67D1/0857—Cooling arrangements
- B67D1/0858—Cooling arrangements using compression systems
- B67D1/0861—Cooling arrangements using compression systems the evaporator acting through an intermediate heat transfer means
- B67D1/0865—Cooling arrangements using compression systems the evaporator acting through an intermediate heat transfer means by circulating a cooling fluid along beverage supply lines, e.g. pythons
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B67—OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
- B67D—DISPENSING, DELIVERING OR TRANSFERRING LIQUIDS, NOT OTHERWISE PROVIDED FOR
- B67D1/00—Apparatus or devices for dispensing beverages on draught
- B67D1/08—Details
- B67D1/0857—Cooling arrangements
- B67D1/0858—Cooling arrangements using compression systems
- B67D1/0861—Cooling arrangements using compression systems the evaporator acting through an intermediate heat transfer means
- B67D1/0865—Cooling arrangements using compression systems the evaporator acting through an intermediate heat transfer means by circulating a cooling fluid along beverage supply lines, e.g. pythons
- B67D1/0867—Cooling arrangements using compression systems the evaporator acting through an intermediate heat transfer means by circulating a cooling fluid along beverage supply lines, e.g. pythons the cooling fluid being a liquid
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B67—OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
- B67D—DISPENSING, DELIVERING OR TRANSFERRING LIQUIDS, NOT OTHERWISE PROVIDED FOR
- B67D1/00—Apparatus or devices for dispensing beverages on draught
- B67D1/08—Details
- B67D1/0878—Safety, warning or controlling devices
- B67D1/0882—Devices for controlling the dispensing conditions
- B67D1/0884—Means for controlling the parameters of the state of the liquid to be dispensed, e.g. temperature, pressure
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25D—REFRIGERATORS; COLD ROOMS; ICE-BOXES; COOLING OR FREEZING APPARATUS NOT OTHERWISE PROVIDED FOR
- F25D17/00—Arrangements for circulating cooling fluids; Arrangements for circulating gas, e.g. air, within refrigerated spaces
- F25D17/02—Arrangements for circulating cooling fluids; Arrangements for circulating gas, e.g. air, within refrigerated spaces for circulating liquids, e.g. brine
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B67—OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
- B67D—DISPENSING, DELIVERING OR TRANSFERRING LIQUIDS, NOT OTHERWISE PROVIDED FOR
- B67D2210/00—Indexing scheme relating to aspects and details of apparatus or devices for dispensing beverages on draught or for controlling flow of liquids under gravity from storage containers for dispensing purposes
- B67D2210/00028—Constructional details
- B67D2210/0012—Constructional details related to concentrate handling
- B67D2210/00125—Treating or conditioning the concentrate, e.g. by heating, freezing
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25D—REFRIGERATORS; COLD ROOMS; ICE-BOXES; COOLING OR FREEZING APPARATUS NOT OTHERWISE PROVIDED FOR
- F25D31/00—Other cooling or freezing apparatus
- F25D31/002—Liquid coolers, e.g. beverage cooler
- F25D31/003—Liquid coolers, e.g. beverage cooler with immersed cooling element
Abstract
Description
- This invention relates to beverage dispense and has particular, but not exclusive, application to the field of soft drinks which are typically dispensed chilled. More especially, the invention concerns the dispense of post-mix beverages such as colas and flavoured sodas in which a concentrate such as a syrup or flavour is mixed with a diluent, typically still or carbonated water, at the point of dispense.
- The concentrate and diluent are typically mixed in the correct proportions in a post-mix dispense valve for dispense of the beverage at a dispense outlet of a counter top fitting such as a dispense tower. The tower may have multiple outlets for the dispense of the same or different beverages.
- Usually the beverage ingredients are delivered to the tower in separate supply lines from remote sources of the ingredients. Typically, the diluent supply lines pass through a cooler for dispense of chilled beverages. The cooler is often positioned well away from the serving area and the diluent lines are contained in an insulated sheath known as a python to prevent the diluent warming up between the cooler and the tower. The concentrate lines are also contained in the python and may be passed through the cooler.
- Chilled post-mix soft drinks such as colas and flavoured sodas are typically dispensed by mixing a diluent with a concentrate in a ratio of approximately 5:1. Dispense of a drink having a temperature of about 4 to 5°C can be achieved if the diluent temperature is about 2°C and the concentrate temperature is about 14°C. Accurate control of the diluent temperature in particular is desirable to maintain the required temperature and this can be a problem during periods of high cooling demand when several drinks are dispensed one after another.
- For this reason, many dispense systems are designed to meet these requirements which in practice may only occur for a limited period of time each day. As a result, for a large part of each day when the cooling demand is low, the system is operating under conditions that are not required to meet the cooling demand. This is inefficient, is wasteful of energy and adds to operating costs. As energy costs rise and the environmental effects of inefficient use of energy increase, there is a need for the design of beverage dispense systems that are more efficient and make better use of available energy.
- The present invention seeks to provide a system for dispensing beverages, particularly soft drinks and more especially post-mix soft drinks.
- It is a preferred object of the invention to provide such a system that can provide one or more benefits and advantages from reduced energy consumption, simplified installation, less syrup waste and easier sanitisation.
- According to a first aspect of the invention, there is provided a beverage dispense system as defined in claim 1.
- Preferably, the cooling module is located within the dispense unit.
- Preferably, a pump is provided for pumping coolant around the re-circulation line and a motor for the pump is operable to control pump speed in response to the coolant temperature in the coolant re-circulation line.
- Preferably, the chamber includes an inlet and an outlet connected to the coolant re-circulation line and a flow guide for directing flow of water through the chamber between the inlet and the outlet to optimise heat exchange with concentrate in the concentrate line.
- In one embodiment, the coolant is a diluent such as water and the dispense unit includes a post-mix dispense valve connected to the concentrate line and to the coolant re-circulation line.
- Preferably, the coolant re-circulation line is connected to a source of still water and includes a carbonator for carbonating the water supplied to the post-mix valve.
- Preferably, the cooler comprises a bath of coolant, the carbonator being located within the bath and the water re-circulation line includes a cooling coil within the bath for return flow to the carbonator.
- In another embodiment, the dispense unit includes a post-mix dispense valve connected to the concentrate line and to a further re-circulation line extending between the cooler and the dispense unit within the python for circulating a diluent such as water.
- Preferably, both re-circulation lines are connected to a common water supply and the diluent re-circulation line includes a carbonator for carbonating the water supplied to the post-mix valve.
- Preferably, the cooler comprises a bath of coolant, the carbonator being located within the bath and the diluent re-circulation line includes a cooling coil within the bath for return flow to the carbonator.
- In one arrangement, the diluent re-circulation line passes through the cooling module.
- In another arrangement, the diluent re-circulation line by-passes the cooling module.
- Preferably, a pump is provided for pumping diluent around the diluent re-circulation line and a motor for the pump is operable to control pump speed in response to the diluent temperature in the diluent re-circulation line.
- Preferably, the cooler includes an evaporator coil within the bath, and an agitator for circulating coolant in the bath, wherein a clearance gap is provided between the evaporator coil and a wall of the bath to permit coolant to circulate on both sides of the evaporator coil.
- Preferably, a motor for the agitator is operable to control agitator speed in response to coolant temperature in the bath.
- According to a second aspect of the invention, there is provided a method of dispensing a post-mix beverage as defined in claim 16.
- In one embodiment, the coolant is a diluent such as water and both the coolant re-circulation line and concentrate line are connected to a post-mix dispense valve of the beverage dispenser.
- In another embodiment, a further re-circulation line is provided that extends between the cooler and the beverage dispenser within the python for circulating a diluent such as water and both the further re-circulation line and concentrate line are connected to a post-mix dispense valve of the beverage dispenser. In this embodiment, the coolant re-circulation line may be connected to the post-mix dispense valve wherein one of the coolant and diluent re-circulation lines circulates still water and the other circulates carbonated water.
- According to a third aspect of the invention, there is provided a beverage dispense system employing a cooling circuit in which a cooling fluid is circulated, a temperature sensor for monitoring the temperature of the cooling fluid and a pump for circulating the cooling fluid in the circuit wherein the pump speed is controlled in response to the temperature of the cooling fluid.
- By controlling the pump speed in response to the temperature of the cooling fluid, the circulation of the cooling fluid can be higher during periods of high cooling demand than during periods of low cooling demand thereby reducing power consumption during periods of low cooling demand.
- The cooling circuit may provide cooling for one or more product lines. In a system for dispensing post-mix beverages, the product lines may contain a concentrate such as a syrup or flavour for mixing with a diluent such as still or carbonated water to produce a desired beverage. In this arrangement, the cooling circuit may form part of the dispense circuit and contain diluent for mixing with concentrate that has been cooled by the diluent prior to dispense. Alternatively, the cooling circuit may be separate from the dispense circuit and contain a coolant for cooling both the concentrate and diluent.
- According to a fourth aspect of the invention, there is provided a method of controlling circulation of fluid in a cooling circuit for a beverage dispense system in response to the temperature of the fluid whereby the circulation of cooling fluid is increased in response to an increase in cooling demand.
- The cooling fluid may be a diluent such as still or carbonated water for a post-mix beverage in which the diluent is mixed with a concentrate such as a syrup or flavour that has been cooled by the diluent prior to dispense.
- According to a fifth aspect of the invention, there is provided a beverage dispense system for a post-mix beverage comprising a post-mix dispense valve connected to sources of a diluent and a concentrate, wherein a supply line for the concentrate passes through a cooling chamber adjacent to the dispense valve.
- By cooling the concentrate adjacent to the dispense valve, the source of concentrate can be located close to the dispense valve reducing the length of the concentrate line making replacement of the concentrate source easier, reducing concentrate waste and facilitating cleaning of the concentrate line.
- According to a sixth aspect of the invention, there is provided a method of dispensing a post-mix beverage comprising providing a post-mix dispense valve, connecting the dispense valve to sources of a diluent and a concentrate, and cooling the concentrate by passage through a cooling chamber positioned adjacent to the dispense valve.
- The diluent may be passed through the cooling chamber to cool the concentrate and the circulation of diluent may be controlled in response to the cooling demand.
- According to a seventh aspect of the invention, there is provided an ice bank cooler comprising a bath containing a coolant, an evaporator coil in the bath for cooling the coolant and forming a thermal reserve of frozen coolant on the evaporator coil, and an agitator for agitating coolant in the bath wherein a motor driving the agitator is operable in response to the coolant temperature in the bath.
- By controlling the agitator motor in response to coolant temperature in the bath, the circulation of the coolant in the bath can be increased by employing a higher motor speed during periods of high cooling demand than during periods of low cooling demand thereby reducing power consumption during periods of low cooling demand.
- According to an eighth aspect of the invention, there is provided a method of controlling agitation of coolant in an ice bank cooler for a beverage dispense system in response to the temperature of the coolant in the cooler whereby the coolant circulation is increased in response to an increase in cooling demand.
- According to a ninth aspect of the invention, there is provided an ice bank cooler comprising a bath containing a coolant, an evaporator coil in the bath for cooling the coolant and forming a thermal reserve of frozen coolant on the evaporator coil, and an agitator for agitating coolant in the bath wherein the coil is arranged so that coolant circulated in the cooler by the agitator passes over frozen coolant on both sides of the coil.
- By arranging the coil so that circulation of coolant in the cooler occurs over both sides of the coil, the available surface area of the frozen coolant and thus the cooling capacity of the thermal reserve provided by the frozen coolant during periods of high cooling demand is increased.
- According to a tenth aspect of the invention, there is provided a method of controlling temperature of coolant in an ice bank cooler for a beverage dispense system by arranging an evaporator coil in the cooler so that coolant circulated in the cooler passes over frozen coolant on both sides of the coil.
- According to an eleventh aspect of the invention, there is provided a python for a beverage dispense system, the python comprising a core having a plurality of fluid lines formed integrally by extrusion and a cover of thermal insulation around the core.
- By extruding the core, any number of fluid lines can be provided according to the system requirements and the core can be cut to the required length of the python and covered with thermal insulation.
- According to a twelfth aspect of the invention, there is provided a method of forming a python for a beverage dispense system comprising extruding a core having a plurality of fluid lines and covering the core with thermal insulation material.
- According to a thirteenth aspect of the invention, there is provided a beverage dispense system for a post-mix beverage comprising a diluent source, a concentrate source, a post-mix dispense valve, a diluent line for supply of diluent from the diluent source to the post-mix dispense valve, a concentrate line for supply of concentrate from the concentrate source to the post-mix dispense valve, a cooler located distally from the post-mix dispense valve, and a heat exchange unit located proximally to the post-mix dispense valve, wherein the diluent line comprises a re-circulation loop for circulating diluent between the cooler and the post-mix dispense valve, and the concentrate is cooled in the heat exchange unit by heat exchange with diluent in the re-circulation loop.
- Other features, benefits and advantages of the invention in each of its aspects will be understood from the description hereinafter of an exemplary embodiment given by way of example only, with reference to the accompanying drawings in which:-
-
Figure 1 is a schematic lay-out of a beverage dispense system embodying the invention; -
Figure 2 is a view, to an enlarged scale, showing details of the syrup cooling in the dispense tower of the system shown inFigure 1 ; -
Figure 3 is a view, to an enlarged scale, showing a modification of the soda re-circulation circuit of the system ofFigure 1 ; -
Figure 4 is a view, to an enlarged scale, showing details of the cooler for the soda-re-circulation circuit ofFigure 3 ; and -
Figures 5 and 6 show details of the python shown inFigure 1 . - Referring first to
Figure 1 of the drawings, a post-mix beverage dispense system is shown comprising a manifold valve block 1 provided with a plurality of post-mix dispense valves generally designated by the reference number 3. In this embodiment, the manifold valve block 1 has sixdispense valves - The dispense valves 3 are connected by individual supply lines generally designated by the reference number 5 to separate supplies of a concentrate generally designated by the reference number 7. In this embodiment, there are six
supply lines 5a,5b,5c,5d,5e,5f and six supplies ofconcentrate 7a,7b,7c,7d,7e,7f - one for each dispensevalve - The manifold valve block 1 is also connected to a diluent re-circulation line or loop generally designated by reference number 9 for supplying diluent to each of the dispense
valves valve - The dispense valves 3 are configured to mix carbonated water and concentrate in the relative proportions required for the beverage to be dispensed. The relative proportions may vary for different beverages and the valves are configured individually on initial set-up according to the beverage to be dispensed. Such configuration may be carried out manually or automatically. For example, the dispense valves 3 may be controlled by a programmable controller such as a microprocessor that allows the relative proportions of diluent and concentrate to be set on an individual basis at any time by a service engineer. The controller may also control other functions of the dispense system via a suitable user interface for operating the dispense valves 3 according to customer selection of a desired beverage. Alternatively, the dispense valves 3 may be manually operable.
- The diluent re-circulation loop 9 includes a
carbonator tank 11 and acirculation pump 13 driven by anelectric motor 14. Thecarbonator tank 11 is provided at a location remote from the manifold valve block 1, for example in a storage area such as a cellar or cold room, and in this embodiment, is immersed in a bath of chilled water provided by an ice bank cooler 15. Chilled carbonated water is pumped around the re-circulation loop 9 from thecarbonator tank 11 to the manifold valve block 1 and back to thecarbonator tank 11. The carbonated water returning to thecarbonator tank 11 passes through a coolingcoil 17 immersed in the chilled water bath of cooler 15 to cool the carbonated water prior to re-entering thecarbonator tank 11. - Between the cooler 15 and the manifold valve block 1, the re-circulation loop 9 is contained in an insulated sheath 19 (commonly referred to as a "python") and the temperature of the carbonated water returning to the
carbonator tank 11 is monitored by atemperature sensor 20 provided before the coolingcoil 17 for a purpose described later herein. - The
carbonator tank 11 has an inlet connected to a source of still water such as mains water via asupply line 25 for adding still water to thecarbonator tank 11 to replace carbonated water that has been dispensed when the water level in thecarbonator tank 11 falls to a pre-determined minimum. The upper and lower water levels in thecarbonator tank 11 are controlled by level sensors (not shown) that also control operation of apump 27 in thewater supply line 25 to boost the water pressure for addition to thecarbonator tank 11 where it is simultaneously carbonated by injecting a supply of carbonating gas into the water stream as it is added to thecarbonator tank 11. - The pressure of carbonating gas in the headspace above the water level in the
carbonator tank 11 is maintained at a level sufficient to prevent the carbonating gas coming out of solution so that the desired carbonation level of the carbonated water circulating in the carbonated water re-circulation loop 9 is maintained. Typically, the carbonating gas is carbon dioxide but other gases such as nitrogen may be employed and the term "carbonating" gas is to be construed accordingly. - The
water supply line 25 passes through a coolingcoil 29 immersed in the chilled water bath of the cooler 15 upstream of a T-junction 31 for supply of chilled water to either the carbonatingtank 11 or to a coolant re-circulation line orloop 21 according to demand. Cooling the still water before it is added to thecarbonator tank 11 assists the carbonation process to achieve the desired carbonation level in the carbonated water for dispense of carbonated beverages from the dispense valves 3. - The
coolant re-circulation loop 21 passes from the cooler 15 to a cooling module 32 adjacent to the manifold valve block 1 for cooling concentrate supplied to the manifold valve block 1 in thesupply lines 5a,5b,5c,5d,5e,5f. The cooling module 32 has achamber 33 with an inlet connected to there-circulation loop 21 to receive chilled water from the cooler 15 and an outlet connected to there-circulation loop 21 to return the water back to the cooler 15. The return flow of water passes through a coolingcoil 35 immersed within the chilled water bath of cooler 15. The water is circulated around thecoolant loop 21 by apump 23. Between the cooler 15 and thecoolant chamber 33, thecoolant re-circulation loop 21 is contained in theinsulated sheath 19 and the temperature of the water returning to the cooler 15 is monitored by atemperature sensor 39 provided before the coolingcoil 35 for a purpose described later herein. - The manifold valve block 1 and
coolant chamber 33 are contained in a beverage dispenser, for example in a dispense tower (not shown), provided at a location remote from the cooler 15 such as a bar or similar serving area where the tower may be located on a counter top for connection to the various supply lines 5 for the concentrates 7, and there-circulation loops 9 and 21 for carbonated water and coolant. The re-circulation loop 9 may supply carbonated water to more than one tower 1 in the same or different serving areas. Alternatively or additionally, thecarbonator tank 11 may supply carbonated water to separate re-circulation loops 9 for supply to more than one tower. Similarly, there-circulation loop 21 may supply coolant to more than one tower 1 in the same or different serving areas. Alternatively or additionally,separate re-circulation loops 21 may be provided for supply of coolant to more than one tower. All combinations and configurations are possible according to the number and position of the towers. - Referring now to
Figure 2 , the arrangement for cooling the concentrate supplied to the tower 1 is shown in more detail. Most post-mix beverages contain approximately 85% of diluent and 15% of concentrate. In many existing dispense systems the concentrate is cooled by passing the supply lines to the dispense tower in the python. This increases the cooling demand in the python resulting in an energy consumption to cool the soda in the soda re-circulation loop 9 that is higher than actually required to achieve and maintain the required concentrate temperature. For example, at a dispense rate of 4 drinks per minute, the energy to cool the concentrate (syrup) is 10 kcal. A 20 metre python containing six concentrate supply lines contains 10 litres of concentrate and the energy consumption is 10W/m or 1750 KWh per year. - To reduce the energy consumption for cooling the concentrate, the present invention removes the concentrate lines from the python and cools the concentrate in the dispense tower. More specifically, the concentrate is cooled within the tower immediately prior to dispense and the supply lines 5 passing through the
coolant chamber 33 contain a significantly lower volume of concentrate that is subjected to cooling compared to existing systems in which the concentrate supply lines are contained in thepython 19. - As shown, the
concentrate supply lines 5a,5b,5c,5d,5e,5f pass through thecoolant chamber 33 within the tower to the manifold valve block 1. Thechamber 33 is insulated to prevent heat exchange between the coolant in thechamber 33 and the warmer surroundings in the serving area. The carbonated water re-circulation loop 9 by-passes thecoolant chamber 33 and is connected to the manifold valve block 1 within the tower 1. - The
coolant re-circulation loop 21 is connected to thechamber 33 for circulating chilled still water through thechamber 33 to cool the concentrate delivered in supply lines 5a,b,5c,5d,5e,5f to the dispensevalves chamber 33 is provided with aninternal flow guide 37 that directs the flow of coolant through thechamber 33 to optimise heat exchange with theconcentrate supply lines 5a,5b,5c,5d,5e,5f passing through thechamber 33. - In this embodiment, the
flow guide 37 comprises a partition wall that divides thechamber 33 into aninlet chamber 33a and an outlet chamber 33b. Coolant from there-circulation loop 21 enters theinlet chamber 33a at the lower end of thecoolant chamber 33. The coolant is confined by theflow guide 37 to flow upwards to the upper end of thecoolant chamber 33 where it flows across the partition wall into the outlet chamber 33b. The coolant is confined by theflow guide 37 to flow downwards to the lower end of thecoolant chamber 33 where it exits the coolant chamber and returns to there-circulation loop 21. - In this embodiment, three of the concentrate supply lines pass through the
inlet chamber 33a and the other three concentrate supply lines pass through the outlet chamber 33b. It will be understood, however that other arrangements of the concentrate supply lines 5 may be employed as desired. For example, while the lines are shown extending linearly through thecoolant chamber 33, this is not essential and other configurations of the concentrate lines within thecoolant chamber 33 may be employed such as coils to increase the surface area available for heat transfer to achieve the desired cooling of the concentrate. Furthermore, it will be understood that other configurations ofcoolant chamber 33 may be employed to direct the flow of coolant over the concentrate supply lines 5 to achieve the desired cooling of the concentrate. - As will be appreciated, the above arrangement reduces the length of the
concentrate supply lines 5a,5b,5c,5d,5e,5f which reduces syrup wastage and makes sanitisation of the lines easier. Also, the concentrate sources can be sited close to the dispense tower, for example on a shelf under the counter top in the serving area, which simplifies replacement of the concentrate sources. - Typically, the concentrate and diluent are mixed in a ratio approximately of 1:5 and a temperature of approximately 4 to 5°C in the dispensed beverage can be achieved with a concentrate temperature of around 14°C where the diluent temperature is about 2°C. Passage of the concentrate supply lines 5 through the cooling
chamber 33 is generally sufficient to achieve the necessary cooling of the concentrate without passing the concentrate lines 5 through thepython 19 or the cooler 15. - The syrup cooling requirement in the cooling
chamber 33 is dependent on a number of factors including the ambient temperature and beverage dispense while heat gain in the carbonated water circuit is dependent on a number of factors including the ambient temperature, the python (length, insulation, number of tubes etc) and beverage dispense. - Existing beverage dispense systems are typically designed to meet the higher cooling demand that arises during periods when beverages are being dispensed (dispense mode) than in periods when no beverages are being dispensed (stand-by mode). Many dispense systems, however, are only operable in the dispense mode for about 20% of the day (less than 4 hours) and for the remaining 80% of the day (more than 20 hours) the system is in the stand-by mode. As a result, designing the system to meet the cooling demand in the dispense mode leads to a significant waste of energy in the stand-by mode.
- To reduce this heat gain, the present invention provides
temperature sensors carbonator tank 11 and of still water in thecoolant re-circulation loop 21 from the coolingchamber 33 to the cooler 15. The temperatures detected by thesensors electric motors sensor - More specifically, the system is designed so that, in periods of low cooling demand when the temperatures of the carbonated water and still water in the
re-circulation loops 9,21 are below the pre-set temperatures such as in the stand-by mode or in periods of low dispense, the re-circulation pumps 13,23 are switched to the low speed to reduce energy consumption and, in periods of high cooling demand, if the temperatures of the carbonated water or still water in there-circulation loops 9,21 rise above the pre-set temperatures, such as in the dispense mode or at higher ambient temperatures, the associatedre-circulation pump - It will be understood that the
pumps sensors - In a modification (not shown), the
coolant re-circulation loop 21 is also connected to the manifold valve block 1 which can be designed so that each dispense valve can selectively dispense a mixture of concentrate and either carbonated water from re-circulation loop 9 or still water fromre-circulation loop 21 or a mixture of both carbonated water and still water. In this way, carbonated drinks, or still drinks or drinks with a variable carbonation level can be dispensed. Alternatively, the manifold valve block 1 may be designed so that one or more dispense valves can dispense the carbonated water and the or each of the remaining dispense valves can dispense the still water. In another modification (not shown), one or more dispense valves may be configured to dispense diluent only, for example to dispense still or carbonated water without any concentrate. Other arrangements that can be employed will be apparent to those skilled in the art. - Referring now to
Figure 3 , a modification of the above-described system is shown in which like reference numerals are used to indicate corresponding parts. - In this modification, the still water re-circulation line or
loop 21 inFigure 1 is omitted and thecoolant chamber 33 is connected to the diluent re-circulation line or loop 9. In this way, the chilled carbonated water supplied to the manifold valve block 1 also passes through thecoolant chamber 33 to cool the syrup supplied to the manifold valve block 1 in the concentrate supply lines (not shown inFigure 3 for clarity). In this way, one re-circulation loop can be used both to supply diluent to the manifold valve block and to cool the concentrate. The operation of this modified system is similar to that ofFigure 1 and will be understood from the description already provided. With this arrangement, the system only dispenses carbonated drinks. It will be understood, that the system ofFigure 1 could be adapted so as to dispense only still drinks by omitting the carbonated water re-circulation loop 9 inFigure 1 and connecting thestill water loop 21 to the manifold valve block 1. - Referring now to
Figure 4 , the arrangement of the ice bank cooler 15 is shown in more detail. Known ice bank coolers typically comprise a bath containing water that is cooled by placing an evaporator of a refrigeration circuit in the bath so that ice forms on the evaporator during periods of low cooling demand to provide a thermal reserve for periods of high cooling demand during which the ice melts to provide additional cooling. A sub-zero ice bank may be produced by the use of an additive that suppresses the freezing point of water. For example an aqueous mixture of water with glycol, a salt, antifreeze or other suitable material added to the water in the bath. - Usually, the evaporator is situated close to the side wall of the bath and the water in the bath is circulated by an agitator driven by an electric motor to wash across the surface of the ice bank on the inwardly facing side of the evaporator to melt the ice during periods of high demand. Washing across one side of the ice bank reduces the available surface area for cooling during periods of high demand which reduces efficiency.
- Also many systems employ an agitator and motor combination that is designed to circulate the water to meet the cooling requirement during periods of high cooling demand. As previously mentioned, this is wasteful of energy as the high cooling demand mainly arises during the dispense mode which is only in operation for about 20% of the day with the remainder being the stand-by mode when the cooling demand is much lower.
- To improve cooling efficiency, the present invention provides the ice bank cooler 15 with an
evaporator coil 41 spaced away from the side wall of the bath so that water circulated by theagitator 43 washes across both sides of thecoil 41 as shown by the arrows thereby doubling the available surface area of theice bank 44 that forms on thecoil 41 for the additional cooling required during periods of high demand. - To obtain the benefit of the larger available surface area of the
ice bank 44, the circulation of the water within the bath requires improved performance of theagitator 43. As a result, more power is required to operate theagitator 43 during periods of high demand and the present invention employs atemperature sensor 45 to monitor the temperature of the water in the bath and control operation of amotor 47 driving theagitator 43 in response to the water temperature. - In this embodiment, the
motor 47 is a twin-speed motor that is switched from low speed, for example 1500 rpm, to high speed, for example 3000 rpm, when the temperature of the water detected by thesensor 45 rises above a pre-set temperature, for example 1°C. It will be understood, however, that other motor speeds may be employed to take account of factors such as the cooling requirement, the capacity of the cooler and other design parameters of the system. - In this way, in periods of low cooling demand when the temperature of the water in the water bath is below the pre-set temperature such as in the stand-by mode or in periods of low dispense, the
motor 47 is switched to the low speed to reduce energy consumption and, in periods of high cooling demand when the temperature of the water in the water bath circuit rises above the pre-set temperature such as in the dispense mode, themotor 45 is switched to the high speed to operate theagitator 43 to meet the increased cooling demand. In this way, operation of the agitator and motor combination is more energy efficient leading to cost savings. - It will be understood that the
agitator 43 may be driven with a twin-speed motor for selection of high or low agitation speeds as described or a variable speed motor may be employed such that the agitator speed can be adjusted to provide high and low speeds and any intermediate speeds as desired. Where a variable agitator speed is permitted, this may be controlled by a suitably programmed microprocessor or other control system responsive to the temperature detected by thetemperature sensor 45. - Referring now to
Figures 5 and 6 , there is shown an alternative python design according to the present invention. In the traditional python design, the diluent lines, concentrate lines and coolant lines are bundled together within an insulated sheath. The diameter of the python is dependent on the number and size of individual lines that are wrapped within the sheath. The diameter of the python increases with increased number of lines with the result that construction, handling and installation of the python becomes more difficult and the available surface area of the python for heat transfer from ambient increases. - The present invention simplifies the python construction by removing the concentrate lines through the provision of cooling for the concentrate in the dispense tower and forming
lines single extrusion 53 that can be cut to the required length, formed into an annular configuration as shown by the arrows, surrounded withinsulation 55 and provided with quick-fit connectors (not shown) at both ends for attaching the diluent andcoolant lines - In this way, pythons having any desired length can be made from a common extrusion and provided with the appropriate fluid connections at each end for connection to matching connectors on the cooler 15 and dispense tower 1 when the python is installed. This is easier than bundling several separate fluid lines together within an insulation sheath. Also, the overall diameter of the python can be reduced thereby reducing the weight of the python making handling and installation easier and reducing the surface area for heat exchange with the environment. Alternatively or additionally, the python can have insulation of increased thickness to reduce heat exchange with the environment without increasing the overall diameter of the python compared to existing python designs.
- As will be appreciated, the above-described system has a number of advantages and benefits. For example lower energy consumption by reducing the heat gain and controlling the speed of the motors driving the re-circulation pumps and agitator in response to the temperature of the water in the re-circulation loops and water bath respectively. Also easier sanitisation of the concentrate lines and less wastage of concentrate in the concentrate lines can be achieved by removing the concentrate lines from the python and providing shorter concentrate lines from the concentrate sources to the dispense tower. This also allows easier replacement of the concentrate sources by enabling the concentrate sources to be placed below the dispense tower within the serving area. Also reduced installation time may be possible by the use of a customised python that can be connected to the diluent and coolant lines by multi-port block connectors during installation.
- It will be understood that the invention is not limited to the embodiments above-described which are intended to illustrate the various benefits and advantages of the invention. Moreover, it will be understood that any of the features of the embodiments above-described may be employed separately or in combination with any other feature in a beverage dispense system.
- Furthermore, while the invention has been described with particular reference to the dispense of soft drinks, it will be understood that the invention is not limited to such application and the invention could be employed for the dispense of alcoholic drinks such as cocktails while features of the invention could be employed in systems for the dispense of alcoholic drinks. For example, the ice bank cooler could be used to cool beer, lager, cider and the like for dispense.
- We also disclose a beverage dispense system for a post-mix beverage comprising a beverage dispense unit at a first location, a cooler at a second location remote from the dispense unit, a python extending from or near the cooler to or near the dispense unit, a concentrate source at the first location, a concentrate line extending between the concentrate source and the dispense unit without passing through the python, a cooling module at the first location, a coolant re-circulation line extending between the cooler and the cooling module within the python, wherein the cooling module comprises a chamber through which the concentrate line passes and the chamber is connected to the coolant re-circulation line for passing coolant through the chamber to transfer heat from the concentrate to the coolant for cooling the concentrate.
- We also disclose a method of dispensing a post-mix beverage comprising providing a post-mix beverage dispenser at a first location, providing a cooler at a second location remote from the beverage dispenser, providing a concentrate source at the first location, connecting a concentrate line from the concentrate source to the beverage dispenser without passing through the python, providing a cooling module at the first location, providing a coolant re-circulation line extending between the cooler and the cooling module within a python, connecting the coolant re-circulation line to a chamber of the cooling module, and passing the concentrate line through the chamber for cooling the concentrate by heat exchange with the coolant in the chamber.
Claims (15)
- An ice bank cooler comprising a bath containing a coolant, an evaporator coil in the bath for cooling the coolant, and an agitator for agitating coolant in the bath wherein a motor driving the agitator is operable in response to the coolant temperature in the bath.
- A cooler according to claim 1 wherein, the motor is a twin-speed motor switched between an upper speed when the temperature of the coolant is above a pre-determined temperature and a lower speed when the temperature of the coolant is below the pre-determined temperature.
- A cooler according to claim 1 wherein, the motor is a variable speed motor and the motor speed is adjustable in response to the temperature of the coolant in the bath.
- A cooler according to any preceding claim including a temperature sensor for monitoring the temperature of coolant in the bath.
- A cooler according to any preceding claim wherein the coolant forms a thermal reserve of frozen coolant on the evaporator coil.
- A cooler according to any preceding claim wherein the evaporator coil is arranged so that coolant circulated in the cooler by the agitator passes over both sides of the evaporator coil.
- A cooler according to any preceding claim wherein the coolant is water.
- A method of controlling agitation of coolant in an ice bank cooler for a beverage dispense system in response to the temperature of coolant in the cooler whereby coolant circulation is increased in response to coolant temperature.
- A method according to claim 8 comprising providing an agitator for agitating the coolant and controlling operation of the agitator in response to the temperature of the coolant.
- A method according to claim 9 comprising providing a motor to drive the agitator and controlling the motor speed in response to the temperature of the coolant.
- A method according to any of claims 8 to 10 comprising providing a temperature sensor for monitoring the temperature of coolant and increasing coolant circulation when the coolant temperature exceeds a pre-determined temperature.
- A method according to any of claims 8 to 11 comprising providing an evaporator coil for cooling the coolant and forming a thermal reserve of frozen coolant on the evaporator coil.
- A method according to claim 12 further comprising circulating the coolant to pass over both sides of the evaporator coil.
- An ice bank cooler comprising a bath containing a coolant, an evaporator coil in the bath for cooling the coolant, and a motor for driving an agitator or a pump wherein the motor is operable in response to the coolant temperature.
- An ice bank cooler according to claim 14 wherein the motor is a twin-speed motor or a variable speed motor.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB0613596A GB2440329B (en) | 2006-07-08 | 2006-07-08 | Beverage dispense |
EP07252746.8A EP1876137B1 (en) | 2006-07-08 | 2007-07-09 | Beverage dispense |
Related Parent Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP07252746.8 Division | 2007-07-09 | ||
EP07252746.8A Division EP1876137B1 (en) | 2006-07-08 | 2007-07-09 | Beverage dispense |
Publications (2)
Publication Number | Publication Date |
---|---|
EP2295369A1 true EP2295369A1 (en) | 2011-03-16 |
EP2295369B1 EP2295369B1 (en) | 2016-04-13 |
Family
ID=36926692
Family Applications (3)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP10194049.2A Active EP2295369B1 (en) | 2006-07-08 | 2007-07-09 | Ice bank cooler |
EP10194051.8A Not-in-force EP2295370B1 (en) | 2006-07-08 | 2007-07-09 | Beverage dispense system |
EP07252746.8A Active EP1876137B1 (en) | 2006-07-08 | 2007-07-09 | Beverage dispense |
Family Applications After (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP10194051.8A Not-in-force EP2295370B1 (en) | 2006-07-08 | 2007-07-09 | Beverage dispense system |
EP07252746.8A Active EP1876137B1 (en) | 2006-07-08 | 2007-07-09 | Beverage dispense |
Country Status (5)
Country | Link |
---|---|
EP (3) | EP2295369B1 (en) |
DK (1) | DK1876137T3 (en) |
ES (1) | ES2424148T3 (en) |
GB (3) | GB2448621B (en) |
PL (1) | PL1876137T3 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US10793413B2 (en) | 2015-05-05 | 2020-10-06 | Cornelius Beverage Technologies Limited | Coolant recirculation apparatus for a beverage dispense system |
Families Citing this family (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2452919B (en) * | 2007-09-18 | 2013-02-13 | Scottish & Newcastle Plc | Systems and methods for dispensing beverage |
JP2011509222A (en) * | 2008-01-08 | 2011-03-24 | アイエムアイ コーネリアス (ユーケイ) リミテッド | After-mix beverage dispenser with cooler |
GB0918840D0 (en) * | 2009-10-28 | 2009-12-09 | Diageo Great Britain Ltd | Slush machine |
GB2558112B (en) * | 2012-06-01 | 2019-06-26 | Cornelius Beverage Tech Limited | Method of controlling condensation on a beverage dispense head |
EP3019438B1 (en) * | 2013-07-12 | 2017-05-17 | Britvic Soft Drinks Limited | Chilled beverage dispense system with carbonator, and method |
CA2955689A1 (en) * | 2014-07-23 | 2016-01-28 | Manitowoc Foodservice Companies, Llc | Recirculating method and system for beverage dispenser |
US11034569B2 (en) | 2018-02-14 | 2021-06-15 | Taphandles Llc | Cooled beverage dispensing systems and associated devices |
WO2020172225A1 (en) * | 2019-02-21 | 2020-08-27 | The Coca-Cola Company | Beverage dispensing system with remote micro-ingredient storage systems |
US11339045B2 (en) | 2020-10-20 | 2022-05-24 | Elkay Manufacturing Company | Flavor and additive delivery systems and methods for beverage dispensers |
Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1209544A (en) | 1968-07-15 | 1970-10-21 | Gaskell & Chambers Non Drip Me | Improvements in or relating to beverage coolers |
US4545505A (en) * | 1982-07-14 | 1985-10-08 | Reed Industries, Inc. | Electronic control circuits for electrically conductive liquids/solids |
EP0315439A2 (en) | 1987-11-02 | 1989-05-10 | The Coca-Cola Company | Ice bank control system for beverage dispenser |
GB2213246A (en) | 1987-12-03 | 1989-08-09 | Imi Cornelius | Beverage cooler |
GB2291698A (en) | 1994-07-22 | 1996-01-31 | Imi Cornelius | Beverage cooling systems |
GB2317680A (en) | 1996-09-20 | 1998-04-01 | Daniel Joseph Ryan | An ice bank cooler system |
WO2002084188A1 (en) * | 2001-04-12 | 2002-10-24 | Hartek Beverage Handling Gmbh | Beverage cooling device |
US20030071060A1 (en) * | 2001-09-20 | 2003-04-17 | Paul Haskayne | Beverage dispenser |
US20030094005A1 (en) | 1993-09-22 | 2003-05-22 | Bethuy Timothy W. | Electronically controlled beverage dispenser |
Family Cites Families (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3011681A (en) | 1959-02-18 | 1961-12-05 | Wallace R Kromer | Method of and apparatus for cooling, storing, mixing and dispensing beverages |
GB2004356B (en) * | 1977-09-13 | 1983-10-12 | Marston Paxman Ltd | Temperature-conditioning apparatus |
GB1575855A (en) * | 1978-03-28 | 1980-10-01 | British Syphon Ind Ltd | Beverage dispense systems |
US4365486A (en) * | 1981-06-29 | 1982-12-28 | Fuji Electric Co., Ltd. | Water-cooled heat-accumulating type drink cooling system |
GB8324882D0 (en) | 1983-09-16 | 1983-10-19 | Schweppes Ltd | Beverage dispensing systems |
US4676400A (en) | 1985-06-27 | 1987-06-30 | Lamont Charles E | Liquid dispensing system |
US4913183A (en) * | 1988-04-12 | 1990-04-03 | Schneider Metal Manufacturing Co. | Thermo plastic carbonated water manifold and method of making same |
GB8903409D0 (en) * | 1989-02-15 | 1989-04-05 | Imi Cornelius Uk Ltd | Beverage cooling system |
US5279446A (en) * | 1991-01-11 | 1994-01-18 | The Cornelius Company | Beverage cooling system |
US5228312A (en) * | 1991-06-17 | 1993-07-20 | Wilshire Partners | Method and apparatus for dispensing cold beverages |
US5433348A (en) * | 1993-01-14 | 1995-07-18 | Lancer Corporation | Modular dispensing tower |
US5673820A (en) * | 1995-09-13 | 1997-10-07 | Abc Dispensing Technologies, Inc. | Juice dispenser |
GB2327748A (en) | 1997-07-25 | 1999-02-03 | Scottish & Newcastle Plc | Cooling apparatus |
GB2346679A (en) * | 1999-02-03 | 2000-08-16 | David Sharp | Controlled cooling of beverages |
GB2356390B (en) * | 1999-10-26 | 2004-07-21 | Imi Cornelius Inc | Juice dispenser with removable cooled cabinet |
GB2397369B (en) * | 2001-10-19 | 2005-11-16 | Manitowoc Foodservice Co Inc | Beverage dispenser with integral ice maker |
GB0315803D0 (en) | 2003-07-05 | 2003-08-13 | Imi Cornelius Uk Ltd | Beverage dispense system |
-
2006
- 2006-07-08 GB GB0809292A patent/GB2448621B/en not_active Expired - Fee Related
- 2006-07-08 GB GB0804872A patent/GB2446312B/en not_active Expired - Fee Related
- 2006-07-08 GB GB0613596A patent/GB2440329B/en not_active Expired - Fee Related
-
2007
- 2007-07-09 EP EP10194049.2A patent/EP2295369B1/en active Active
- 2007-07-09 EP EP10194051.8A patent/EP2295370B1/en not_active Not-in-force
- 2007-07-09 EP EP07252746.8A patent/EP1876137B1/en active Active
- 2007-07-09 PL PL07252746T patent/PL1876137T3/en unknown
- 2007-07-09 DK DK07252746.8T patent/DK1876137T3/en active
- 2007-07-09 ES ES07252746T patent/ES2424148T3/en active Active
Patent Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1209544A (en) | 1968-07-15 | 1970-10-21 | Gaskell & Chambers Non Drip Me | Improvements in or relating to beverage coolers |
US4545505A (en) * | 1982-07-14 | 1985-10-08 | Reed Industries, Inc. | Electronic control circuits for electrically conductive liquids/solids |
EP0315439A2 (en) | 1987-11-02 | 1989-05-10 | The Coca-Cola Company | Ice bank control system for beverage dispenser |
GB2213246A (en) | 1987-12-03 | 1989-08-09 | Imi Cornelius | Beverage cooler |
US20030094005A1 (en) | 1993-09-22 | 2003-05-22 | Bethuy Timothy W. | Electronically controlled beverage dispenser |
GB2291698A (en) | 1994-07-22 | 1996-01-31 | Imi Cornelius | Beverage cooling systems |
GB2317680A (en) | 1996-09-20 | 1998-04-01 | Daniel Joseph Ryan | An ice bank cooler system |
WO2002084188A1 (en) * | 2001-04-12 | 2002-10-24 | Hartek Beverage Handling Gmbh | Beverage cooling device |
US20030071060A1 (en) * | 2001-09-20 | 2003-04-17 | Paul Haskayne | Beverage dispenser |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US10793413B2 (en) | 2015-05-05 | 2020-10-06 | Cornelius Beverage Technologies Limited | Coolant recirculation apparatus for a beverage dispense system |
Also Published As
Publication number | Publication date |
---|---|
ES2424148T3 (en) | 2013-09-27 |
GB2448621B (en) | 2010-04-28 |
EP2295370B1 (en) | 2016-04-13 |
EP1876137B1 (en) | 2013-05-22 |
GB0804872D0 (en) | 2008-04-16 |
GB2448621A (en) | 2008-10-22 |
EP1876137A1 (en) | 2008-01-09 |
EP2295369B1 (en) | 2016-04-13 |
GB0809292D0 (en) | 2008-07-02 |
PL1876137T3 (en) | 2013-10-31 |
GB0613596D0 (en) | 2006-08-16 |
GB2446312B (en) | 2009-02-11 |
EP2295370A1 (en) | 2011-03-16 |
GB2446312A (en) | 2008-08-06 |
GB2440329A (en) | 2008-01-30 |
DK1876137T3 (en) | 2013-07-29 |
GB2440329B (en) | 2009-11-04 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
AU2008346270B2 (en) | Post-mix beverage dispenser with cooler | |
EP1876137B1 (en) | Beverage dispense | |
EP1627849B1 (en) | Beverage dispense system | |
US7757498B2 (en) | Cold carbonation and cold syrup system for beverage dispenser with remote tower | |
US20080120988A1 (en) | Cold carbonation system for beverage dispenser with remote tower | |
US8011190B2 (en) | Product cooling | |
EP3521239B1 (en) | A coolant recirculation apparatus for a beverage dispense system | |
WO2014110434A1 (en) | Front room beverage dispense apparatus | |
WO2011051000A1 (en) | Beverage coolers | |
GB2558112B (en) | Method of controlling condensation on a beverage dispense head | |
GB2160502A (en) | Drink supply system for postmixed drinks | |
GB2502631A (en) | Beverage dispense system which creates condensation or ice on a dispense head | |
WO2011116000A1 (en) | Apparatus and method for recirculating stillwater and/or semi-carbonated water | |
GB2446792A (en) | Beverage dispense system | |
AU2005301036A1 (en) | Inline booster with spraying means for beverage dispensing system | |
GB2460231A (en) | Dispensing frozen beverages | |
GB2441215A (en) | Beverage dispense | |
IE86196B1 (en) | Beverage coolers | |
GB2440202A (en) | Multi-Compressor Cooling Apparatus with Current Start-up Control and Used for Cooling Beverages | |
IES85866Y1 (en) | Beverage coolers | |
GB2498757A (en) | Automatically priming soda recirculation pumps used in the dispense of post-mix carbonated beverages |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
AC | Divisional application: reference to earlier application |
Ref document number: 1876137 Country of ref document: EP Kind code of ref document: P |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IS IT LI LT LU LV MC MT NL PL PT RO SE SI SK TR |
|
AX | Request for extension of the european patent |
Extension state: AL BA HR MK RS |
|
TPAC | Observations filed by third parties |
Free format text: ORIGINAL CODE: EPIDOSNTIPA |
|
17P | Request for examination filed |
Effective date: 20110916 |
|
17Q | First examination report despatched |
Effective date: 20140205 |
|
GRAP | Despatch of communication of intention to grant a patent |
Free format text: ORIGINAL CODE: EPIDOSNIGR1 |
|
RIC1 | Information provided on ipc code assigned before grant |
Ipc: F25D 31/00 20060101ALI20151001BHEP Ipc: B67D 1/08 20060101ALI20151001BHEP Ipc: F25D 17/02 20060101ALI20151001BHEP Ipc: B67D 1/00 20060101AFI20151001BHEP |
|
INTG | Intention to grant announced |
Effective date: 20151105 |
|
GRAS | Grant fee paid |
Free format text: ORIGINAL CODE: EPIDOSNIGR3 |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
RAP1 | Party data changed (applicant data changed or rights of an application transferred) |
Owner name: CORNELIUS BEVERAGE TECHNOLOGIES LIMITED |
|
RAP1 | Party data changed (applicant data changed or rights of an application transferred) |
Owner name: CORNELIUS BEVERAGE TECHNOLOGIES LIMITED |
|
AC | Divisional application: reference to earlier application |
Ref document number: 1876137 Country of ref document: EP Kind code of ref document: P |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IS IT LI LT LU LV MC MT NL PL PT RO SE SI SK TR |
|
REG | Reference to a national code |
Ref country code: GB Ref legal event code: FG4D |
|
REG | Reference to a national code |
Ref country code: AT Ref legal event code: REF Ref document number: 789917 Country of ref document: AT Kind code of ref document: T Effective date: 20160415 Ref country code: CH Ref legal event code: EP Ref country code: CH Ref legal event code: NV Representative=s name: BOVARD AG, CH |
|
REG | Reference to a national code |
Ref country code: IE Ref legal event code: FG4D |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R096 Ref document number: 602007045897 Country of ref document: DE |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: PLFP Year of fee payment: 10 |
|
REG | Reference to a national code |
Ref country code: LT Ref legal event code: MG4D |
|
REG | Reference to a national code |
Ref country code: AT Ref legal event code: MK05 Ref document number: 789917 Country of ref document: AT Kind code of ref document: T Effective date: 20160413 |
|
REG | Reference to a national code |
Ref country code: NL Ref legal event code: MP Effective date: 20160413 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: FI Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20160413 Ref country code: NL Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20160413 Ref country code: PL Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20160413 Ref country code: LT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20160413 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: PT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20160816 Ref country code: LV Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20160413 Ref country code: GR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20160714 Ref country code: AT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20160413 Ref country code: ES Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20160413 Ref country code: SE Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20160413 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: BE Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20160413 |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R097 Ref document number: 602007045897 Country of ref document: DE |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: RO Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20160413 Ref country code: CZ Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20160413 Ref country code: EE Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20160413 Ref country code: SK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20160413 Ref country code: DK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20160413 |
|
PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
26N | No opposition filed |
Effective date: 20170116 |
|
GBPC | Gb: european patent ceased through non-payment of renewal fee |
Effective date: 20160713 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: MC Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20160413 |
|
REG | Reference to a national code |
Ref country code: IE Ref legal event code: MM4A |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SI Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20160413 Ref country code: GB Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20160713 |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: PLFP Year of fee payment: 11 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20160709 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LU Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20160709 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: HU Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT; INVALID AB INITIO Effective date: 20070709 Ref country code: CY Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20160413 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: MT Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20160731 Ref country code: IS Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20160413 Ref country code: TR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20160413 |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: PLFP Year of fee payment: 12 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: BG Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20160413 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: FR Payment date: 20230616 Year of fee payment: 17 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: IT Payment date: 20230711 Year of fee payment: 17 Ref country code: CH Payment date: 20230801 Year of fee payment: 17 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: DE Payment date: 20230614 Year of fee payment: 17 |