APPARATUS FOR AND METHODS OF RAPIDLY CHILLING A BEVERAGE
20170176096 ยท 2017-06-22
Inventors
Cpc classification
F25D31/007
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F25B21/02
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F25B2321/0212
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F25D2700/16
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F25D27/005
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F25D31/006
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F25B2321/023
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F25D2400/361
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F25B2321/0252
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F25D31/008
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F25B21/04
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F25D2700/06
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
International classification
F25D31/00
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F25B21/02
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
Abstract
Apparatus for and method of rapidly chilling a beverage in which a vessel having high thermal mass relative to the amount of beverage to be introduced into the vessel is cooled through contact with a cooling module to a temperature low enough that a volume of beverage introduced into the vessel is rapidly cooled.
Claims
1. Apparatus for chilling a fluid, the apparatus comprising: a base; a cover connected to the base, the cover comprising at least one cooling station; and a cooling unit connected to the base and positioned to be in thermal communication with the cooling station; the cooling station being adapted to receive a heat conductive bottom portion of a vessel such that the bottom portion is in thermal communication with the cooling unit when the bottom portion is received by the cooling station, the cooling unit being adapted to cool the vessel when empty and when the bottom portion is received by the cooling station to a temperature below 5 C. in less than about four minutes, the cooling station including at least one vapor chamber.
2. Apparatus as claimed in claim 1 wherein the cooling unit comprises a thermoelectric element having a T in the range of about 80 C. to about 90 C. when a hot side temperature of the thermoelectric element is in a range of about 25 C. to about 35 C.
3. Apparatus as claimed in claim 1 wherein the cooling unit comprises a thermoelectric element having a heat transport capacity of more than 50 watts.
4. Apparatus as claimed in claim 1 wherein the at least one cooling station comprises a cooling element with an exposed top surface essentially flush with a top surface of the cover.
5. An apparatus for altering a temperature of a vessel, the apparatus comprising: at least one preparation surface; and a heat transferring unit positioned beneath the preparation surface to be in thermal communication with the preparation surface, the heat transferring unit comprising a first thermally conductive layer, a second thermally conductive layer and a thermoelectric element arranged between and in thermal communication with the first and second thermally conductive layers, the preparation surface being adapted to receive a thermally conductive bottom portion of a vessel such that said bottom portion is in thermal communication with the heat transferring unit when the bottom portion is placed on the preparation surface and the apparatus further comprising a vessel presence sensor configured to detect the presence of a vessel on the preparation surface.
6. An apparatus according to claim 5, wherein said vessel presence sensor includes an inductive sensor.
7. An apparatus according to claim 6 wherein said vessel presence sensor includes a reference sensor for measuring a background signal and wherein said vessel presence sensor detects the presence of a vessel by subtracting the backroad signal from a signal from the inductive sensor.
8. An apparatus according to claim 5, wherein the apparatus further comprises a temperature sensor.
9. An apparatus according to claim 7, wherein the temperature sensor is configured to detect the temperature of the preparation surface.
10. An apparatus according to claim 7, wherein the temperature sensor is configured to detect the temperature of a vessel placed on the preparation surface.
11. An apparatus according to claim 7 wherein the apparatus further comprises a control system configured to control the function of the thermoelectric element in dependence of at least one of said vessel presence sensor and said temperature sensor.
12. An apparatus according to claim 7 wherein the apparatus further comprises a physical condition sensor configured to detect a presence of an object other than a vessel on or in the immediate vicinity of the preparation surface and wherein the control system is configured to shut down the thermoelectric element if the physical condition sensor indicates the presence of an object other than a vessel.
13. An apparatus according to claim 11 further including a system status sensor for generating a status sensor signal indicating whether an overall temperature of the apparatus falls outside of a predetermined range and the control system is configured to receive the status sensor signal and to cause the apparatus to shut down when the status sensor signal indicates the overall temperature of the apparatus falls outside of the predetermined range.
14. An apparatus according to claim 5 wherein the apparatus is adapted to decrease a temperature of a vessel.
15. An apparatus according to claim 14 wherein the apparatus is adapted to reverse a polarity of the thermoelectric element so that the thermoelectric element heats rather than cools when an amount of ice accumulates on or around a vessel which would trap the vessel.
16. An apparatus comprising: at least one preparation surface; a heat transferring unit positioned beneath the preparation surface to be in thermal communication with the preparation surface, the heat transferring unit comprising a first thermally conductive layer, a second thermally conductive layer and a thermoelectric element arranged between and in thermal communication with the first and second thermally conductive layers; a vessel placed on the preparation surface, the vessel having a thermally conductive bottom portion and the vessel being placed such that said bottom portion is in thermal communication with the heat transferring unit when the bottom portion is placed on the preparation surface; and a vessel presence sensor configured to detect the presence of the vessel on the preparation surface.
17. A system according to claim 16, wherein the vessel is made of a material having a specific heat capacity in the range of about 0.2 J/g C. to about 4 J/g C.
18. A system according to claim 16, wherein the vessel is at least partially coated with a surface treatment to protect the vessel from corrosion.
19. A system according to claim 18 wherein the surface treatment is a beverage container coating.
20. A system according to claim 18 wherein the surface treatment comprises a varnish.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
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DETAILED DESCRIPTION
[0033] Various embodiments are now described with reference to the drawings, wherein like reference numerals are used to refer to like elements throughout. In the following description, for purposes of explanation, numerous specific details are set forth in order to promote a thorough understanding of one or more embodiments. It may be evident in some or all instances, however, that any embodiment described below can be practiced without adopting the specific design details described below. In other instances, well-known structures and devices are shown in block diagram form in order to facilitate description of one or more embodiments.
[0034] With initial reference to
[0035] The cover 30 includes at least one cooling station 90. In the embodiment of
[0036] Also as shown in
[0037] Preferably the cover 30 is made of an insulating material and provided with an easy-to-clean and aesthetically pleasing surface treatment. An insulating material could prevent a user from injuring themselves from the extreme cold and also to make the unit more convenient to handle. The cover 30 is preferably dimensioned so that the overall beverage chilling system 10 can have a relatively compact footprint. For example, the beverage chilling system 10 can be about 10 cm tall, about 50 cm wide, and about 30 cm deep, but other dimensions and aspect ratios are possible.
[0038]
[0039] In a present preferred embodiment, the cooling element 120 is preferably a thermoelectric element such as a Peltier element. Because of the thermal loads imposed by relatively rapid chilling the vessel 50, which typically exceed those imposed by conventional applications, it is presently preferred to use a two-stage Peltier element. One measure of the refrigerating capacity of a thermoelectric element is AT, which is a measure of the temperature differential the thermoelectric element can maintain between its hot side and its cold side at a given temperature for the hot side. In a presently preferred embodiment, it is preferred to use a thermoelectric element having a T in the range of about 80 C. to about 90 C. when the hot side temperature of the thermoelectric element is in the range of about 25 C. to about 35 C. A thermoelectric element meeting these criteria is a Model FPK2-19808NC element from Qinhuangdao Fulianjing Electronic Co Ltd., but it will be readily apparent to one of ordinary skill in the art that other devices can be used as cooling elements 120.
[0040] Another figure of merit for a preferred implementation of the cooling element 120 is its efficiency and how much heat it can transport. A presently preferred cooling rate more than about 20 Watts, and more preferably more than about 35 Watts, and most preferably more than 50 Watts.
[0041] The Model FPK2-19808NC mentioned above is rated to be able to transport approximately 50 Watts per element at 12 V and 6 Amps. The cooling efficiency of such an element is 50 Watts/(12 V*6 Amps)=0.7. Choosing an element with lower heat transportation capabilities would result in a longer cooling time. Choosing an element with lower efficiency would increase the power consumption of the system.
[0042] When the vessel 50 is placed in the receptacle aperture 40 (see
[0043] The cooling elements 120 are preferably supplied with a power through a power cord 140. The power cord 140 is connected to an external power supply 150. It is preferred to position the power supply 150 away from the other components of the beverage chilling system 10 so that heat generated by the power supply 150 does not contribute to the heat load imposed upon the cooling elements 120. However, it may also be possible to place the power supply 150 inside the cover 30. Also shown in
[0044] The embodiment of
[0045]
[0046] The embodiment of
[0047] A preferred embodiment of a pedestal-shaped first thermally conductive plate 110 for use with the embodiment of
[0048]
[0049] The PCB 600 of
[0050]
[0051]
[0052] At or near the receptacle aperture 40 there is preferably provided a sensor package 230. In this context, near means sufficiently proximate that the sensors in the sensor package 230 can detect conditions in the receptacle after 40 as well as in a vessel 50 placed in receptacle aperture 40. The sensor package 230 is preferably supplied with a temperature sensor 240 (see
[0053] The sensor package 230 is also preferably supplied with a physical condition sensor 250 (see
[0054] The beverage chilling system 10 may also include a system status sensor 260 (see
[0055]
[0056] As mentioned, it is preferable to include a ventilation system to remove waste heat generated by the cooling elements 120. As described, this ventilation system may include a radiator assembly 180 and a fan assembly 200 forcing air past the radiator assembly 180 and outside of the cover 30. For this purpose the cover 30 may be provided with a series of vents 550 as shown in
[0057] As mentioned, in high humidity environments it is possible that condensation can occur within the aperture 40 as well as on a vessel 50 placed within the aperture 40. It is preferable that liquid water produced by this condensation not be permitted to collect at a position where it could freeze and obstruct the aperture 40 or cause damage to internal components. Therefore, in such circumstances, it is preferable to provide a means for the water produced by condensation to drain away from the base of the aperture 40 and be collected elsewhere.
[0058] Also as mentioned, the receptacle aperture 40 may be provided with a temperature sensor. It is also possible to provide the vessel 50 with a temperature sensor which may be a small sensor/display combination. The vessel-mounted sensor could also include thermochromic paint or one or more pieces of thermochromic plastic that change color depending on their temperature.
[0059] The various sensors described above make up part of an overall control system 280 that also includes the CPU 270. One possible arrangement for such a control system is shown in
[0060] The I/O interface 290 may also be connected to one or more communications interfaces 310. The communications interface 310 may be any device for communicating data to or from the CPU 270 and an outside device. For example, the communications interface 310 may be a USB interface, or an Ethernet interface. The communications interface 310 may additionally or alternately include a wireless interface such a WiFi, Bluetooth, or an NFC interface.
[0061] The I/O interface 290 may also be connected to a reader 365. The reader 365 can be configured in a known manner to read material relevant to a particular vessel 50 or to a particular beverage. This material could be a barcode on the side of the vessel 50 or a barcode located elsewhere. The material could also be an RFID tag located within the vessel 50 as described more fully below. It will also be appreciated that the ranger 365 need not be integral with the beverage chilling system 10 and could instead be one of the external devices serving as external device 360.
[0062] The I/O interface 290 may also be connected to one or more indicators, displays, or user interfaces. For example, the I/O interface 290 may be connected to LEDs that serve as status indicators 60. The LEDs can change color from, for example, red to blue when the vessel 50 has reached an operational temperature or when the combination of the beverage and the vessel 50 reaches the desired serving temperature.
[0063] The I/O interface 290 may also be connected to the user interface 70. The user interface 70 may be a knob for adjusting temperature, or it may be more complex, including, for example, a touchscreen and an array of indicators. Several possible arrangements for the user interface 70 are shown in
[0064] The user interface 270 can also be implemented as software operating on a computer or as an application on a smart phone or tablet or other wireless communication device. To implement this, the communications interface 310 could be configured to interface with an external device 360 such as a wireless enabled device such as a computer, tablet, or cell phone. The user could use an application on the mobile device to control operation of the beverage chilling system 10. In a commercial establishment the external device 360 could be the establishment's vending system and the communications interface 310 could be configured to exchange data wirelessly with the establishment's vending system so as to create a record every time the beverage chilling system 10 is used. This could help reduce loss due to pilferage or excessive comping of patrons. If the external device 360 is a wireless enabled device such as a computer, tablet, or cell phone, an application could be installed on the external device 360 and the user interface for the application could, for example, be a visual representation of a display with controls such as anyone or combination of the arrangements shown in
[0065] The control system 280 can also include various control units such as a cooling element power control unit 370 for each of the cooling elements 120. The cooling element power control unit 370 preferably uses pulse width modulated control of the cooling elements in which a duty cycle of pulses is used to control the average power supplied to the cooling elements.
[0066] If the beverage chilling system 10 has a pre-chill unit, then the control system 280 can also include a pre-chill power control 380 which would be electrically connected to a pre-chill cooling element 390. The control system can also include a fan power control 400 electrically connected to a fan motor 410 to control operation of the fan assembly 200. The fan speed can be controlled automatically to be greater when a vessel is present (as detected for example by the sensors 650) so that the cooling load on the cooling elements is increased and causing them to generate more waste heat.
[0067] There may also be provision for reversing the polarity of the cooling elements so that they heat rather than cool. This could be useful if an excess amount of ice accumulates at the receptacle 40 which may interfere with operation or even cause the vessel 50 to become trapped in or on the receptacle 40.
[0068] The vessel 50 may be made of any one of several materials. The material is preferably selected so that the thermal capacity of the material and the mass of material used ensure sufficient thermal mass to cool the beverage introduced into the vessel 50 sufficiently quickly. Suitable materials include aluminum, copper, gold, or silver, or their alloys, or steel. Alternatively, one part of the vessel 50 may be made from one material and another part may be made from another material. This permits the use of an insulating material on the parts of the vessel 50 likely to come into contact with a user's fingers or lips. Aluminum in the vessels 50 may be anodized. The external surface of the vessel may be supplied with a surface effect such as an etched frost effect. It is preferred for aesthetic reasons that the vessel 50 maintains a coating of frost even after it has reached a thermal equilibrium with the beverage inside. To achieve this, it is preferred to have an operational temperature below 10 C. Coatings can be used to achieve or enhance this effect. It may be even desirable to include a system for misting or sprinkling water onto the outside of the vessel 50 when it is in the receptacle aperture 40 so as to promote an aesthetically pleasing frost effect on the exterior surface of the vessel 50.
[0069] One consideration in the design of a suitable vessel 50 is that when the vessel 50 is used in a commercial establishment it is likely to be washed in a commercial dishwasher in which it may be exposed to a combination of high temperature and corrosive cleaning agents. It is therefore preferred to coat at least the metallic portions of the inside and the outside of the vessel 50 with a surface treatment that can protect the metal from corrosion. It has been found that beverage container coatings can be used for this purpose. For example, for the outside of the vessel 50 a varnish made by The Valspar Corporation provides adequate protection. The specific presently preferred varnish (Product Code 6275000030, Product Name E500B030) includes diethylene glycol butyl ether with a solvent and dimethyl succinate, but one of ordinary skill in the art will understand that other varnishes or other coating material may be used. For the interior the Valspar 93AA Beverage lining, Product ID 13S93AA may be used. Again, one of ordinary skill in the art will understand that other coatings used to line beverage containers or coatings used for other applications may be used. Other coatings for the outside or inside of the vessel 50 may be used so long as they substantially arrest or sufficiently retard corrosion and do not create any toxicity issues for users who will be drinking from the vessel 50. As another example, powder coatings may be used.
[0070] The vessel 50 may have any one of several configurations. For example, the vessel 50 could be provided with one or more elements that protrude into the interior volume of the vessel 50 and increase the interior surface area of the vessel 50 to promote heat flow from the beverage to the vessel 50. This is shown in
[0071] For some applications, the vessel 50 will dimensioned to provide an interior volume sufficient to hold a shot of beverage. For example, in the embodiment of
[0072] In the embodiment of
[0073] The above embodiment is made of multiple materials. The vessel 50 may also be machined from a solid piece of material, in which case protrusion 320 could be formed during the machining process and so could be integral with the rest of the vessel 50.
[0074]
[0075] As mentioned above, the cooling station 90 need not be configured as an aperture and can instead have a different configuration, for example, one that is flush with or even protruding above the top surface of cover 30. This is shown in
[0076] Also, the case of a beverage being chilled in a metallic can, the bottom of the vessel 50 which would receive the can could be shaped to conform to the dome shape commonly found on the bottom of such cans. In such an embodiment, the vessel 50 would be placed in the receptacle aperture 40 and the can would be placed in the vessel 50 after the vessel 50 had reached the predetermined operational temperature. Also, the system could be configured so that the vessel 50 is not removable from the receptacle aperture 40 in normal use.
[0077] As mentioned, the beverage chilling system 10 may include a vessel pre-chill station which maintains the vessel 50 at a temperature below ambient temperature so that the vessels 50 may be chilled to their operational temperature more quickly.
[0078] One advantage of using a thermoelectric device is that by reversing polarity the cooling element 120 can be made to heat rather than chill a vessel 50 placed in receptacle aperture 40. The vessel 50 may be preheated to rapidly heat beverages. Also, reversing polarity may be used to evaporate liquid in the receptacle aperture 40.
[0079] In an example of use, the beverage chilling system 10 is placed on a bar counter. If an external power supply 150 for the cooling elements 120 is used, it is preferably placed away from the console, for example, below a bar counter, so that the external power supply 150 is not exposed to spillage and the cooling element 120 is not exposed to heat generated by the external power supply 150.
[0080] The individual operating the beverage chilling system 10 would place one of the vessels 50 into one of the receptacle apertures 40. At this part of the serving cycle, the vessel 50 will be at an ambient temperature or a prechill temperature (see
[0081] With further reference to
[0082] The time during which step S20 is being performed constitutes a first phase (Phase I or vessel chilling phase) of the overall beverage serving cycle (see
[0083] Anytime after the vessel 50 reaches an operational temperature the user may add the desired beverage, e.g., spirits, into the vessel 50 in step S30. Once this is done, heat flows from the beverage to the vessel 50 as the temperature of the beverage decreases and the temperature of the vessel 50 increases until the beverage and the vessel 50 are nearly in thermal equilibrium in step S40. Here, it should be understood that a thermal equilibrium means that the vessel 50 and the liquid within it have reached nearly the same temperature. The system will not be in thermal equilibrium in the sense that the cooling module 100 continues to cool the vessel 50 and a fluid within vessel 50 as long as the vessel 50 remains in the receptacle aperture 40. Primary cooling of the beverage, however, is caused by transferring heat from the beverage to the vessel 50. Additional cooling that may result by direct action of the cooling element 120 during the liquid chilling phase of the serving cycle is secondary.
[0084] The time during which step S40 is being performed constitutes a second phase (Phase II or liquid chilling phase) of the overall beverage serving cycle (see
[0085] Thus, the thermal mass of the vessel 50 and the refrigerating capabilities of the cooling element 120 are selected to be such that the temperature of the vessel 50 and beverage at thermal equilibrium reach a desired serving temperature in an acceptably short period of time. The serving temperature can be a predetermined value which may be selectively programmable according to the beverage using a user interface 70 provided for that purpose. Alternatively the equilibrium temperature may be determined when the rate of change of the temperature of the vessel falls below a predetermined threshold. Once the serving temperature has been achieved, the vessel 50 with the beverage inside it may be removed from cooling station 90 and served or consumed. This corresponds to step S50. The user may then put another vessel 50 in the receptacle aperture 40.
[0086] As an example, ambient or room temperature in a commercial bar will typically be in the range of about 20 C. to about 30 C. Using four minutes as an example of a duration for a serving cycle implies that each cooling station may be used to chill about 15 servings an hour. As mentioned, a serving cycle is made up of two distinct periods: (1) Phase I, the amount of time it takes a vessel 50 placed in the receptacle aperture 40 to reach a predetermined operational temperature (the vessel chilling period) and (2) Phase II, the amount of time it takes the combination of the vessel 50 and a beverage added to the vessel 50 to reach a serving temperature (the beverage chilling period). There may also be an idling period between Phase I and Phase II during which the vessel 50 remains at the operational temperature before a beverage is added to the vessel 50 but for the purposes of this discussion it is assumed that the user will want to add a beverage to the vessel 50 as soon as the vessel 50 is at its operational temperature.) It is also assumed that in most instances the user will remove the vessel/beverage combination from the receptacle aperture 40 soon after it reaches its serving temperature.
[0087] Assuming that serving the beverage and handling payment takes about 2 minutes, a 4 minute serving cycle implies it would be desirable for the beverage chilling system 10 to be able to cool the vessel 50 to its operational temperature (Phase I) in about 2 to 3 minutes. Assuming the desired temperature for the vessel 50 before the beverage is introduced is in the range of about 5 C. to about 35 C., as an example, it may be desired to reduce the temperature of the vessel 50 from about 25 C. to about 20 C. in about 2-3 minutes. It is also desired to cool the beverage once it has been added to the vessel 50 (Phase II) in an amount of time less than the amount of time required to cool the vessel 50 when it is empty (Phase I). In other words, the serving cycle is divided between Phase I and Phase II, and more time for one of these phases leaves less time for the other. It is preferred to make Phase II as short as possible. While this in the abstract appears to leave more time for Phase I there are countervailing considerations. Shortening Phase II implies using a lower operational temperature, a vessel 50 having higher thermal mass, or both. Using a lower operational temperature and/or vessel 50 having higher thermal mass, however, increases the duration of Phase I. Thus, at some point, efforts to shorten Phase II will actually increase the duration of the serving cycle because any decrease in the duration of Phase II will be more than offset by a greater increase in the duration of Phase I. In other words shortening Phase I implies a lower operational temperature which implies lengthening Phase I. If the constraints on the length of the serving cycle constitute a time budget oft minutes, e.g. 4 minutes, then it is preferred to expend more of that time budget on Phase Ito make Phase II as short as possible. There is however, a natural limit as further shortening of Phase II incurs a time penalty of an even greater lengthening of Phase I. In a presently preferred embodiment, it is preferred to select the operational temperature and vessel thermal mass such that the serving cycle is about four minutes, Phase I is about 3 minutes, and Phase II is about minute. Thus the duration ratio of Phase Ito Phase II is preferably about 7:1.
[0088] Aluminum is presently the preferred material for the vessel 50 because of its high heat conductivity and because it has a specific heat capacity that permits the use of a vessel 50 of acceptable mass. The wall thickness and overall form and mass of the vessel 50 is determined empirically or based on thermal calculation optimization. For instance, if the vessel has thin walls, it will get cold faster, but it may then not have a sufficient thermal capacity and the temperature at thermal equilibrium with an added beverage will be higher, compared to a vessel with thicker walls.
[0089] Some of the considerations and trade-offs involved in the design of the beverage chilling system 10 are summarized in the following table:
TABLE-US-00001 Advantage Drawback Better Peltier Lower cooling time None efficiency Lower power consumption Higher cooling Lower cooling time Higher power capacity consumption Higher heat Lower cooling time Larger footprint dissipation rate More noise
[0090] As suggested, the design considerations for the vessel 50 and the overall system can be understood in terms of thermal mass, or, equivalently, thermal capacitance or heat capacity. These terms refer to the ability of a body to store thermal energy. Thermal capacitance is typically referred to by the symbol Cth and measured in units of J/ C. or J/K per unit mass. A related quantity is specific heat capacity, measured in terms of J/g C. For a preferred material for the vessel, aluminum, the specific heat capacity is 0.902 J/g C. and the specific heat capacity of 100 grams of aluminum is therefore 90.2 Joules/ C. For an alcoholic beverage that is 50% alcohol (100 proof), the specific heat capacity may be approximated as the average of the specific heat capacity of ethyl alcohol, 2.46 J/g C., and water, 4.184 J/g C., or about 3.32 J/g C. If a serving size is approximately 4 cl (about 40 grams) and one wishes to reduce the temperature of the serving from say 20 C. to about 0 C. then this means that the vessel must be able to extract about 4000 Joules from the beverage. Thus it is desired to make the vessel have as much mass as practical in view of the fact that it is generally not desirable to make the vessel so heavy that it is difficult for a user to manipulate it.
[0091] As mentioned, thermal mass together with operational temperature determine the rate at which cooling of the vessel 50 occurs during Phase I as well as the rate of cooling of the beverage added to the vessel 50 occurs during Phase II. Because the rate of cooling is a function of the initial temperature differential, it is desirable as a practical matter that the vessel 50 initially be as cold as possible. The temperature of the vessel 50 before a beverage is introduced will obviously in turn depend on the temperature of the cooling element. It is therefore desirable to use a relatively cold cooling element, preferably, one that can achieve temperatures of 50 C.
[0092] To show the effects of vessel mass and initial vessel temperature on the duration of Phase II, tests were conducted using vessels made of aluminum and having four different masses as follows:
TABLE-US-00002 Vessel 1 2 3 4 Mass [g] 11.5 35.5 45.5 76.5
[0093] The vessel was chilled to an initial operational temperature as indicated in the data below. Two centiliters of water at an ambient temperature of about 27 C. as shown were then added to the vessel. The temperature of the vessel and of the water were then measured separately several intervals. The results are shown below:
TABLE-US-00003 Vessel 1 Time [s] 0 1 3 7 17 27 35 Vessel temperature [ C.] 9.5 3.7 3.7 10.1 12 9.7 11 Liquid temperature [ C.] 26.5 25.5 23 18.6 14.7 12.1 11 Vessel 2 Time [s] 0 1 3 9 13 19 22 Vessel temperature [ C.] 19.8 8.5 0.1 3.5 4.2 5.8 4.1 Liquid temperature [ C.] 26.8 24.2 20.3 15.6 13.1 11.1 8.5 Vessel 3 Time [s] 0 3 8 14 18 22 27 Vessel temperature [ C.] 22.4 6.3 0.1 0.3 0.2 0 0.1 Liquid temperature [ C.] 26.8 22.5 14 10.3 8.1 6.6 6.1 Vessel 4 Time [s] 0 2 7 12 16 26 43 Vessel temperature [ C.] 14.3 14.3 15 15.7 0.7 0.6 1.7 Liquid temperature [ C.] 27 24.8 18.2 12 9 7.6 5.1
[0094] As can be seen, the lightest vessel, vessel 1, when cooled down to an initial temperature of 9.5 C. takes about 35 seconds to cool the water within it to an equilibrium temperature of 11 C. Vessel 2, which was more massive than vessel 1 and cooled to a lower initial temperature, was able to cool the water within it to 8.5 C. in about 22 seconds. Vessel 3, which was more massive than vessel 2 and cooled to an even lower initial temperature, was able to cool the water within it to 6.1 C. in about 27 seconds. Vessel 4, which is more massive than vessel 3 but cooled to a higher initial temperature, was able to cool the water within it to 7.6 C. in about 26 seconds. This data thus in general demonstrates the dependence of (1) the time it takes to achieve a given final temperature on (2) the mass of the vessel and its initial temperature.
[0095] These results are depicted in
[0096] To show the effects of vessel mass and initial vessel temperature on the duration of Phase I, tests were conducted using vessels made of aluminum and having four different masses as follows:
TABLE-US-00004 Vessel 1 2 3 4 Mass [g] 10 35 45 82
[0097] The vessel was initially at room temperature. The temperature of the vessel was then measured separately several intervals. The results are shown below:
TABLE-US-00005 Time [s] 0 10 30 60 90 120 200 400 Vessel 1 Vessel temperature 23.43 18.06 4.96 7.28 12.6 15.75 19.38 20.48 [ C.] Vessel 2 Vessel temperature 23.24 14.24 2.91 5.19 9.65 12.99 16.62 20.54 [ C.] Vessel 3 Vessel temperature 24.62 16.25 5.81 2.98 8.61 12.89 19.03 24.81 [ C.] Vessel 4 Vessel temperature 25.35 23.62 18.73 12.45 8.01 3.81 3.23 12.56 [ C.]
[0098] As can be seen, it takes the lightest vessel, vessel 1, about 400 seconds to cool to about 20.5 C. but it can be cooled to about 12.6 C. in about 90 seconds. Vessel 2, which was more massive than vessel 1 could also be cooled to about 20.5 C. in about 400 seconds, but took 120 seconds to reach about 12.99 C. The other data are as shown. This data thus in general demonstrates the dependence of (1) the time it takes to achieve a given final temperature on (2) the mass of the vessel and the temperature one is trying to reach.
[0099] These results are depicted in
[0100] The above description includes examples of one or more embodiments. It is, of course, not possible to describe every conceivable combination of components or methodologies for purposes of describing the aforementioned embodiments, but one of ordinary skill in the art may recognize that many further combinations and permutations of various embodiments are possible. Accordingly, the described embodiments are intended to embrace all such alterations, modifications and variations that fall within the spirit and scope of the appended claims. Furthermore, to the extent that the term includes is used in either the detailed description or the claims, such term is intended to be inclusive in a manner similar to the term comprising as comprising is construed when employed as a transitional word in a claim. Furthermore, although elements of the described aspects and/or embodiments may be described or claimed in the singular, the plural is contemplated unless limitation to the singular is explicitly stated. Additionally, all or a portion of any aspect and/or embodiment may be utilized with all or a portion of any other aspect and/or embodiment, unless stated otherwise.