The invention generally relates to post-mix beverage dispensing systems, and more particularly relates to a compact and portable post-mix beverage dispensing system suitable for use on airplanes, railcars, or other applications where space and/or facilities are limited.
Post-mix beverage dispensing systems provide a convenient and efficient means for dispensing carbonated beverages to consumers. Such systems produce carbonated water, and mix flavored syrups with the carbonated water in desired ratios at a dispensing head or bar gun. Where such systems can be used, post-mixed beverages are highly cost-effective compared to more expensive pre-packaged carbonated beverages such as canned or bottled soft drinks.
Presently, commercial airlines typically serve prepackaged beverages to their passengers. Prepackaged beverages such as canned beverages are stored at room temperature in a portable cart that is sufficiently narrow to pass down the aisles of most commercial aircraft. As passengers request carbonated beverages, flight attendants remove the selected canned beverages from the portable cart, and pour the beverages over ice in a glass or cup. This process is time-consuming, and can be difficult or impossible under turbulent flight conditions. On short flights, at least some passengers often are unable to obtain a beverage due to the time required to dispense canned beverages to previously served passengers. In addition, the cost per serving of canned beverages is considerably higher than the cost per serving cost post-mixed carbonated beverages. Serving pre-packaged beverages also generates considerable waste such as empty beverage cans that must be handled, temporarily stored, and discarded. In addition, pre-packaged carbonated beverages have a limited shelf life.
The challenges associated with producing compact and portable post-mix beverage dispensing systems are numerous. Such systems must operate without external sources of water and electric power. In addition, such systems must be sufficiently compact to permit their use in limited spaces such as the narrow confines of airplanes. Because such systems necessarily include stored high pressure carbon dioxide gas, the systems also must comply with stringent government safety regulations governing the packaging and transportation of high pressure gas containers. Furthermore, the makers of the most popular carbonated beverages (e.g. Coke ® and Pepsi ®, require their products to be consistently dispensed according to exacting product standards. One such requirement is that the dispensed beverages have a commercially acceptable level of carbonation of about 3 percent to about 4 percent.
Others have attempted to produce compact and portable post-mix beverage dispensing systems with limited success. For example, U.S. Pat. Nos. 5,411,179 and 5,553,749 to Oyler et al. describe self-contained beverage dispensing systems that use a single low-pressure motorless carbonator to carbonate flat water to produce soda for use in post-mixing and dispensing carbonated beverages. Unfortunately, such low-pressure motorless carbonators produce soda having only about 2.5 percent carbonation, which is well below a commercially acceptable level of carbonation and/or product standards dictated by makers of Coke ® and Pepsi®. Others have tried to address this problem by developing portable beverage dispensers that include a single high-pressure motorless carbonator. The term “high pressure motorless carbonator” as used herein refers to a motorless carbonator that operates at an internal pressure of at least about 100 psi. For example, U.S. Pat. No. 6,021,922, U.S. Pat No. 6,234,349, and U.S. Pat. No. 6,253,960 to Bilskie et al. describe self-contained high-pressure beverage dispensing systems that include a single motorless carbonator that operates at a gas pressure of between 90-110 psi. Unfortunately, these systems also do not provide a highly portable and compact beverage dispensing system that produces soda that consistently meets commercially acceptable levels of carbonation and complies with applicable federal safety regulations for use on commercial aircraft.
Accordingly, there is a need for an effective, compact, and highly portable beverage dispensing system that operates without external sources of water and electric power. In addition, there is a need for such a system that is sufficiently compact to permit its use in limited spaces such as the narrow aisles of airplanes and passenger railcars. Such a system also must comply with applicable government safety regulations, and must consistently supply a commercially acceptable level of carbonation.
A portable beverage dispensing system includes a supply of flat water and a supply of pressurized gaseous carbon dioxide. A first motorless carbonator is configured to receive a portion of the flat water and a portion of the carbon dioxide and to cause a portion of the carbon dioxide to dissolve in the flat water to produce partially carbonated soda. A second motorless carbonator is configured to receive a portion of the partially carbonated soda and a portion of the carbon dioxide and to cause a portion of the carbon dioxide to dissolve in the partially carbonated soda and to produce fully carbonated soda. The system also includes a dispenser for selectively dispensing the fully carbonated soda.
A portable beverage dispensing module includes a housing and a cylinder in the housing containing pressurized carbon dioxide. A first motorless carbonator is located in the housing, and is configured to receive flat water from a flat water supply and to receive a portion of the carbon dioxide. The first carbonator causes a portion of the carbon dioxide to dissolve in the flat water to produce partially carbonated soda. A second motorless carbonator is also located in the housing. The second carbonator is configured to receive the partially carbonated soda and a portion of the carbon dioxide, to cause a portion of the carbon dioxide to dissolve in the partially carbonated soda, and to produce fully carbonated soda. At least one pneumatic pump powered by the pressurized carbon dioxide is configured to pump flat water from the flat water supply to the first carbonator. The module further includes a dispenser for selectively dispensing the fully carbonated soda.
A high pressure gas cylinder for a portable beverage dispensing system includes a neck having a throat. A piercable membrane seals the throat of the cylinder. The term “high pressure gas cylinder” as used herein refers to cylinder that is capable of safely storing compressed gas at a pressure of at least about 1800 psi.
A two-stage motorless carbonator includes a first carbonation chamber having a flat water inlet, a first carbon dioxide inlet, and a first soda outlet. A second carbonation chamber includes a soda inlet, a second carbon dioxide inlet, and a second soda outlet. A conduit connects the first soda outlet of the first carbonation chamber to the soda inlet of the second carbonation chamber. Partially carbonated soda from the first carbonation chamber is passed to the second carbonation chamber through the conduit and is further carbonated in the second carbonation chamber.
A schematic view of an embodiment of a compact and portable beverage dispensing system 10 according to the invention is shown in
The system provides two sequential stages of carbonation. Flat water is first carbonated to between about 2.4 percent and about 3.6 percent by the first carbonator 60, and is then passed to the second carbonator 70 where the soda from the first carbonator 60 is further carbonated up to about 3.6 percent to about 4.2 percent. Thus, the system is capable of supplying soda with a carbonation level (by weight percent) that meets or exceeds commercial standards for post-mixed beverages.
The system further includes a plurality of gas regulators 210, 220, 230; a pair of pneumatic water booster pumps 80, 100; a plurality of carbonated beverage flavorant supply pumps 140; a plurality of non-carbonated beverage supply pumps 160; a plurality of gas conduits 300, 310, 320, 330, 340, 350, 360; a plurality of flat water conduits 400, 410, 420, 430, 440; a plurality of soda conduits 500, 510, 520; and a plurality of flavorant conduits 600, 610. Flat water, soda, flavorants for carbonated beverages, and non-carbonated beverages are supplied to a bar gun 120 for dispensing in a manner known in the art.
Compressed carbon dioxide (CO2) gas is supplied to the system 10 from a CO2 cylinder 30 through a CO2 supply valve 35. In a preferred embodiment, the cylinder 30 is a disposable high-pressure cylinder 30 capable of supplying compressed CO2 at a pressure up to at least about 1800 psi The supply valve permits and controls entry of CO2 into the system 10 from the cylinder. A primary regulator 200 regulates the pressure of the CO2 entering the system 10 from the cylinder 30 to about 120 psi. Detailed descriptions of embodiments of the cylinder 30 and supply valve 35 are discussed below
CO2 from the cylinder 30 passes through three distinct conduit networks within the system 10. CO2 is delivered through gas conduit 300 at a pressure of about 120 psi to a first regulator 230 and a second regulator 220. The first gas regulator 230 supplies CO2 at about 83 psi to the second water booster pump 100 via gas conduit 310. The second gas regulator 220 supplies CO2 to the first carbonator 60 and the second carbonator 70 at about 100 psi through gas conduit 320. The second gas regulator 220 also supplies gas at about 100 psi to the third regulator 210 through gas conduit 330. The third gas regulator 210 regulates the supply of gas to the first water booster pump 80 via gas conduit 360, the non-carbonated beverage pumps 160 via gas conduits 350, and the carbonated beverage flavorant pumps 140 via gas conduits 340 at about 56 psi. The regulators preferably are adjustable in-line high pressure gas regulators such as those available from Ashby Industries.
The water booster pumps 80, 100 are pneumatic pumps powered by pressurized CO2 gas. The water booster pumps 80, 100 pump flat water (uncarbonated) within the system 10 without electricity. The first and second water booster pumps 80, 100 may be FloJet® G Series pumps such as FloJet® Model G58 pumps, which are available from FloJet Corp. of Irvine, CA. Other suitable pneumatic pumps may also be used in system 10. The first water booster pump 80 draws flat water from the flat water supply 20 through water conduit 400 and pumps the flat water to and through the cold plate 50. The flat water supply 20 may be a disposable bag. The cold plate 50 is chilled to about 32 degrees Fahrenheit by ice residing in the ice tray 40. A drain 110 may be provided for draining melted ice from the ice tray 40 to a drain receptacle or bag 112. The flat water is chilled in the cold plate 50 to about 33 degrees Fahrenheit. A portion of the chilled water passes through conduit 420 and to a water pressure regulator 90. Preferably, a water pressure regulator 90 is provided to regulate the pressure of the chilled flat water passed to the second water booster pump 100 through water conduit 430 to about 30 psig(?). The second water booster pump 100 pumps the chilled flat water to the first carbonator 60 at about 100 psi. Another portion of the chilled flat water exiting the cold plate 40 is diverted to the beverage dispensing gun 120 via water conduit 425.
Chilled flat water is subjected to a first stage of carbonation in the first carbonator 60. The solubility of gaseous CO2 in water is maximized when the water temperature is minimized and the pressure of the CO2 gas to which the cold water is exposed is maximized. Because the flat water is introduced into the first carbonator 60 at a temperature of about 33 degrees Fahrenheit and the CO2 gas is introduced into the first carbonator at a high pressure (about 100 psi), the carbonation of the flat water in the first carbonator is highly effective. In a preferred embodiment, the first carbonator 60 is capable of carbonating chilled flat water to between about 2.4 percent and about 3.6 percent. The pressure of the CO2 gas that is introduced into the first carbonator 60 is limited by the pressure of the supplied flat water. If the gas pressure exceeds the water supply pressure, the flow of water into the carbonator 60 will be inhibited by the excessive gas pressure.
The partially carbonated soda produced by the first carbonator 60 passes to the second carbonator through soda conduit 500 at a pressure of about 100 psi. The second carbonator 70 further carbonates the partially carbonated soda to between about 3.6 percent and about 4.2 percent. Details of embodiments of the first and second carbonators 60, 70 are discussed below. The fully carbonated soda produced by the second carbonator 70 is delivered to the cold plate 50 through soda conduit 510. The fully carbonated soda is chilled to about 33 degrees Fahrenheit by the cold plate 50, and is passed to a soda dispensing gun 120 through conduit 520 for post-mixing with carbonated beverage flavorants in a manner known in the art.
The system 10 includes one or more carbonated beverage flavorant supplies 130. The carbonated beverage flavorant supplies 130 may be disposable bags containing flavored syrups for soft drinks. The flavored syrup is drawn from each bag 130 through a syrup conduit 600 by a dedicated pneumatic pump 140. The pneumatic pumps 140 may be FloJet® N5000 pumps, which are available from FloJet Corp. of Irvine, California, though other suitable pneumatic pumps may also be used. The pumps 140 pump the syrups to a beverage dispensing gun 120 through syrup conduits 610.
The system 10 may also include supplies 150 of noncarbonated beverages or noncarbonated beverage concentrates or flavorants. For example, the supplies 150 may be disposable bags containing juices, juice concentrates, or fruit-flavored flavorants. When a supply 150 includes a concentrate or flavorant, the concentrate or flavorant is post-mixed with flat water at the dispensing gun 120. Each juice, juice concentrate, or other flavorant is drawn from its bag 150 by a dedicated pump 150 through a conduit 700, and is delivered to the dispensing gun 120 through a conduit 610.
The beverage dispensing gun 120 is of a type known in the art. For example, the beverage dispensing gun 120 may be an 8, 10, or 12-button Wunder-Bar™ bar gun produced by Automatic Bar Controls, Inc. of Vacaville, California. Other suitable beverage dispensers or bar guns may also be used.
As shown in
As shown in
The partially carbonated soda then passes from the first carbonator 60 through outlet 64 and soda conduit 500, and enters the second carbonator 70 through inlet 76 at about 100 psi. Carbon dioxide enters the carbonator from gas conduit 320 at about 100 psi through gas inlet 72, and is caused to partially dissolve in the partially carbonated soda until carbonation reaches between about 3.6 and 4.2 percent. In one embodiment, the second carbonator 70 is capable of producing about 1.5 fluid ounces of fully carbonated soda per second. The fully carbonated water exits the second carbonator 70 through soda outlet 74, and is passed to the cold plate of system 10 through soda conduit 510. When supplied with partially carbonated soda having about 2.4-3.6 percent carbonation, the second carbonator is capable of producing fully carbonated soda carbonated to about 3.6-4.2 percent. The second stage of carbonation ensures that the fully carbonated soda meets acceptable commercial carbonation standards. Though the first and second carbonators 60, 70 are shown as separate components connected together by a bracket 79, persons of ordinary skill in the art will recognize that a single component having first and second carbonation chambers may also be used.
In operation, as carbonated soda is drawn from the carbonator 60 through outlet 64, the weight of the float 65 causes the float 65 and needle 67 to fall to a closed position and to prevent pressurized gas from completely backfilling the inner chamber 63 of the carbonator 60. Flat water then enters the evacuated portion of chamber through water inlet 66. As the flat water backfills the inner chamber 63 and reaches a level in the enclosure 61 that is sufficient to cause the float 65 and needle 67 to rise in the chamber 63, carbon dioxide is permitted to enter the chamber 63 through tube 69. Once an equilibrium is reached in the chamber 63, water and gas both are prevented from entering the chamber 63. At the high pressure (about 100 psi) and low temperature (about 33 degrees F.) within the chamber 63, the carbon dioxide gas is caused to at least partially dissolve in the flat water to form soda. In the two-stage carbonator shown in
Although only a few exemplary embodiments of this invention have been described in detail above, those of ordinary skill in the art will readily appreciate that many modifications are possible in the exemplary embodiments without materially departing from the novel teachings and advantages of this invention. Accordingly, all such modifications are intended to be included within the scope of the appended claims. In the claims, where a means-plus-function clause is recited, the clause is intended to cover the structures described herein as performing the recited function and not only structural equivalents, but also equivalent structures. Thus, although a nail and screw may not be structural equivalents in that a nail employs a cylindrical surface to secure wooden parts together, whereas a screw employs a helical surface, in the environment of fastening wooden parts, a nail and screw may be equivalent structures.
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