INLINE GAS/LIQUID INFUSION SYSTEM WITH ADJUSTABLE ABSORPTION OUTPUT AND SELF-TUNING CAPABILITY

Abstract

An inline gas/liquid infusion system featuring an electronic control logic and subsystem having a signal processor configured to: receive signaling containing information about a liquid pressure of an incoming liquid provided from a pump to an inline gas liquid absorption device and about a gas pressure of an incoming gas provided to the inline gas liquid absorption device; and determine corresponding signaling containing information to control the liquid pressure of the incoming liquid provided from the pump to the inline gas liquid absorption device in order to provide real time adjustable set point output levels of gas absorption in the inline gas liquid absorption device, based upon the signaling received.

Claims

1. An inline gas/liquid infusion system comprising: an electronic control logic subsystem having a signal processor configured to: receive signaling containing information about a liquid pressure of an incoming liquid provided from a pump to an inline gas liquid absorption device and about a gas pressure of an incoming gas provided to the inline gas liquid absorption device; and determine corresponding signaling containing information to control the liquid pressure of the incoming liquid provided from the pump to the inline gas liquid absorption device in order to provide real time adjustable set point output levels of gas absorption in the inline gas liquid absorption device, based upon the signaling received.

2. An inline gas/liquid infusion system according to claim 1, wherein the signal processor is configured to provide the corresponding signaling as output signals to the pump to adjust the liquid pressure of the incoming liquid provided from the pump to the inline gas liquid absorption device, including by varying characteristics of a voltage signal output to the pump.

3. An inline gas/liquid infusion system according to claim 1, wherein the signaling contains information about the liquid pressure sensed and the gas pressure sensed; and the signal processor is configured to determine the real time adjustable set point output levels of the gas absorption by monitoring the signaling received and adjusting the liquid pressure of the incoming liquid provided from the pump to the inline gas liquid absorption device based upon a differential pressure between the liquid pressure sensed and the gas pressure sensed.

4. An inline gas/liquid infusion system according to claim 1, wherein the inline gas/liquid infusion system comprises the pump configured to: receive the corresponding signaling provided as output signaling from the signal processor, and also receive the incoming liquid; and pump the incoming liquid, based upon the output signaling received, including where the pump is a motor driven pump.

5. An inline gas/liquid infusion system according to claim 1, wherein the inline gas/liquid infusion system comprises the inline gas liquid absorption device configured to: receive the liquid pressure of the incoming liquid provided from the pump, and the gas pressure of the incoming gas provided from a pressurized gas tank, and provide a gas infused liquid, including providing the gas infused liquid to a dispenser system or valve.

6. An inline gas/liquid infusion system according to claim 1, wherein the signaling includes liquid pressure input signals received from a liquid pressure sensing device configured to sense the liquid pressure of the incoming liquid provided from the pump, and provide the liquid pressure input signals containing information about the liquid pressure of the incoming liquid provided from the pump.

7. An inline gas/liquid infusion system according to claim 6, wherein the inline gas/liquid infusion system comprises the liquid pressure sensing device.

8. An inline gas/liquid infusion system according to claim 1, wherein the signaling includes gas pressure input signals received from a gas pressure sensing device configured to sense the gas pressure of the incoming gas provided from a pressurized gas tank to the inline gas liquid absorption device, and provide gas pressure input signals containing information about the gas pressure of the incoming gas provided from the pressurized gas tank to the inline gas liquid absorption device.

9. An inline gas/liquid infusion system according to claim 8, wherein the inline gas/liquid infusion system comprises the gas pressure sensing device.

10. An inline gas/liquid infusion system according to claim 8, wherein the pressurized gas tank is configured to provide CO.sub.2 or nitrogen.

11. An inline gas/liquid infusion system according to claim 1, wherein the inline gas liquid absorption device includes, or takes the form of, a mixing valve, a carbonator, a nitrogenator or an infuser.

12. An inline gas/liquid infusion system according to claim 1, wherein the pump includes, or takes the form of, a diaphragm, gear, lobe, flexible impeller, vane or centrifugal pump.

13. An inline gas/liquid infusion system according to claim 1, wherein the corresponding signaling controls the pump so as to provide adjusted flow and pressure conditions of the incoming liquid provided to the inline gas liquid absorption device.

14. An inline gas/liquid infusion system according to claim 1, wherein the signaling includes at least one feedback signal that contains the information about the liquid pressure of the incoming liquid provided from the pump to the inline gas liquid absorption device.

15. A method comprising: receiving, with a signal processor, signaling containing information about a liquid pressure of an incoming liquid provided from a pump to an inline gas liquid absorption device and about a gas pressure of an incoming gas provided to the inline gas liquid absorption device; and determining, with the signal processor, corresponding signaling containing information to control the liquid pressure of the incoming liquid provided from the pump to the inline gas liquid absorption device in order to provide real time adjustable set point output levels of gas absorption in the inline gas liquid absorption device, based upon the signaling received.

16. A method according to claim 15, wherein the method further comprises providing, with the signal processor, the corresponding signaling as output signals to the pump to adjust the liquid pressure of the incoming liquid provided from the pump to the inline gas liquid absorption device, including by varying characteristics of a voltage signal output to the pump.

17. A method according to claim 15, wherein the signaling contains information about the liquid pressure sensed and the gas pressure sensed; and the method further comprises determining, with the signal processor, the real time adjustable set point output levels of the gas absorption by monitoring the signaling received and adjusting the liquid pressure of the incoming liquid provided from the pump to the inline gas liquid absorption device based upon a differential pressure between the liquid pressure sensed and the gas pressure sensed.

18. A method according to claim 15, wherein the method further comprises arranging in the inline gas/liquid infusion system the pump configured to: receive the corresponding signaling provided as output signaling from the signal processor, and also receive the incoming liquid; and pump the incoming liquid, based upon the output signaling received, including where the pump is a motor driven pump

19. A method according to claim 15, wherein the method further comprises arranging the inline gas/liquid infusion system with the inline gas liquid absorption device configured to: receive the liquid pressure of the incoming liquid provided from the pump, and the gas pressure of the incoming gas provided from a pressurized gas tank, and provide a gas infused liquid, including providing the gas infused liquid to a dispenser system or valve.

20. A method according to claim 15, wherein the method further comprises receiving as at least part of the signaling liquid pressure input signals from a liquid pressure sensing device configured to sense the liquid pressure of the incoming liquid provided from the pump, and provide the liquid pressure input signals containing information about the liquid pressure of the incoming liquid provided from the pump

21. A method according to claim 15, wherein the method further comprises receiving as at least part of the signaling gas pressure input signals from a gas pressure sensing device configured to sense the gas pressure of the incoming gas provided from a pressurized gas tank to the inline gas liquid absorption device, and provide gas pressure input signals containing information about the gas pressure of the incoming gas provided from the pressurized gas tank to the inline gas liquid absorption device.

22. A method according to claim 21, wherein the method further comprises configuring the gas tank to provide CO.sub.2 or nitrogen.

23. A method according to claim 15, wherein the method further comprises configuring the inline gas/liquid infusion system with an electronic control logic subsystem that includes the signal processor.

24. A method according to claim 15, wherein the method further comprises configuring the inline gas liquid absorption device with a mixing valve, a carbonator, a nitrogenator or an infuser.

25. A method according to claim 15, wherein the method further comprises configuring the pump with a diaphragm, gear, lobe, flexible impeller, vane or centrifugal pump.

26. A method according to claim 15, wherein the method further comprises controlling with the corresponding signaling the pump so as to provide adjusted flow and pressure conditions of the incoming liquid provided to the inline gas liquid absorption device.

27. A method according to claim 15, wherein the method further comprises including in the signaling at least one feedback signal that contains the information about the liquid pressure of the incoming liquid provided from the pump to the inline gas liquid absorption device.

Description

BRIEF DESCRIPTION OF THE DRAWING

[0050] The drawing includes FIGS. 1-6, which are not necessarily drawn to scale, which are briefly described as follows:

[0051] FIG. 1 shows a standard beverage carbonator that is known in the art.

[0052] FIG. 2 shows a standard beverage carbonator operation diagram that is known in the art.

[0053] FIG. 3 shows an inline gas liquid infusion system with an adjustable absorption level, according to some embodiments of the present invention.

[0054] FIG. 4 shows an example of an application having the inline gas liquid infusion system shown in FIG. 3 with an adjustable output, self-tuning application, and also having a single dispenser valve, e.g., for dispensing a nitrogen and/or CO2 infused coffee, tea, latte, or other drinks, according to some embodiments of the present invention.

[0055] FIG. 5 shows an example of an application having the inline gas liquid infusion system shown in FIG. 3 with an adjustable output, self-tuning application, and also having a single or multiple dispenser valve, e.g., for dispensing a water carbonation to/for beverages like soda, according to some embodiments of the present invention.

[0056] FIG. 6 shows an electronic control logic subsystem having a signal processor, according to some embodiments of the present invention.

[0057] Not every element or arrow in every Figure is labeled with a lead line and reference numeral/label, so as to reduce clutter in the drawing.

DETAILED DESCRIPTION OF BEST MODE OF THE INVENTION

[0058] The following is a specific description of the operation of the present invention, mentioning all of the components and functions thereof:

FIG. 3

[0059] In summary, the present invention provides an Adjustable Inline Gas Infusion System, generally indicated as 10, that operates by infusing gas into a liquid or beverage to a desired amount or end products dispense gasification characteristic level as illustrated in FIG. 3. Examples of descriptive gasification levels include: fizzy, foamy, gassy, bubbly, etc.

[0060] The adjustable Inline Gas Infusion system 10 consists of the following system elements:

[0061] 1) Motor Driven Pump 1,

[0062] 2) Liquid Pressure Sensing Device 2,

[0063] 3) Gas Pressure Sensing Device 3,

[0064] 4) Electronic Control Subsystem 4, and

[0065] 5) Inline Liquid/Gas Absorption Device 5.

[0066] In FIG. 3, the electronic control logic subsystem 4 is also known herein as a controller), and the inline gas liquid absorption device 5 is also known herein as a carbjet. FIG. 3 also shows pressure input signals provided from the liquid pressure sensing device 2 and the a gas pressure sensing device 3 to the electronic control logic subsystem 4, and output signals provided from the electronic control logic subsystem 4 to the motor driven pump 1. In addition, FIG. 3 shows that the electronic control logic subsystem 4 receives input signals, and that the output signals from the electronic control logic subsystem 4 are also provided as an output to control external devices, valves, etc. FIG. 3 shows that the motor driven pump 1 receives incoming liquid pressure, e.g., from a commercial water supply, tank or pressurized vessel; that the gas pressure sensing device 3 receives and senses gas input pressure regulated (e.g., 0-100 PSI) from a tank, which may typically take the form of CO2 or nitrogen; and that the carbjet 5 receives pumped incoming liquid from the motor driven pump 1 and pressurized gas from the tank (see FIGS. 4-5), and provides a gas infused liquid to a dispensing system or valve, e.g., like that shown in relation to FIGS. 4-5.

[0067] The incoming liquid stream pressure and flow that is provided to the inline gas infusion system 10 varies by application as is illustrated in FIG. 3. For typical beverage soft drink carbonation applications, the water is provided from the restaurant or store's commercial building water system, e.g., as shown in FIG. 5. For Beer, Coffee, Teas and other beverages, the incoming liquid may be provided from a Keg or other pressurized vessel, a bag in box, non-pressurized cask, bucket, or any other liquid containing vessel, e.g., as shown in FIGS. 4 and 5. Based on these applications, the incoming liquid pressure received by the motor driven pump 1 may be variable or fixed and range from 0-100 psi and up to 3 gallons per minute (GPM). The device can be tuned for a variety of incoming liquid pressure and flow conditions, e.g. beyond those described herein. The input signals provided to the electronic control logic subsystem 4 may contain information about the one or more incoming liquid pressure and flow conditions for programming and tuning the electronic control logic subsystem 4 for any particular application.

[0068] The Motor Driven Pump 1: The incoming liquid may be provided to the motor driven pump 1 in FIG. 3 via rigid tubing or flexible tubing or hose and fittings used in standard beverage dispense applications and plumbing systems. The motor driven pump 1 functions to manipulate the flow and pressure characteristics of the incoming liquid stream based on electronic communication received from the electronic control logic subsystem or controller 4. The motor driven pump 1 can be any type of pump that is suitable for the liquid and performance desired. Example types may include pumps like Diaphragm, Gear, Lobe, Flexible Impeller, Vane, Centrifugal, etc. The motor driven pump 1 provides adjusted flow and pressure conditions to the pumped incoming liquid sensed by the liquid pressure sensing device 2 and provided to the carbjet 5 where the liquid is then mixed with gas.

[0069] The Liquid Pressure Sensing Device 2: The liquid pressure sensing device 2 functions to provide liquid pressure feedback in the form of an input signal to the Electronic Control Logic Subsystem 4. The liquid pressure sensing device 2 can be a separate device in line, or can be a device that is incorporated as an integral part of the motor driven pump 1, the gas pressure sensing device 3, the electronic control logic subsystem 4, and the carbjet 5 or other external system component. The liquid pressure sensing device 2 may be directly or indirectly sensing the pressure and communicating the feedback through various types of process signal communication values and methods. The fluid is then introduced into the Inline Liquid/Gas Absorption device 5.

[0070] The Inline Liquid/Gas Absorption device 5: The inline liquid/gas absorption device 5 in the inline gas infusion system 10 functions to mix the gas and liquid streams for an end result of infusing the gas into the liquid phase. The pressure and flow characteristics of the incoming streams determine the degree of absorption of gas into the liquid at a given temperature, pressure, and flow condition. The gas input is a regulated supply typically provided by Gas storage cylinders and other types of pressurized vessels via properly rated tubing or hose, and fittings, e.g., as shown in FIGS. 4-5. The gas may consist of one or more types of gas, premixed or fed separately into the carbjet 5. The incoming gas supply flows to the Gas Pressure Sensing Device 3 prior to entering the mixing chamber of the carbjet 5.

[0071] The Gas Pressure Sensing Device 3: The gas pressure sensing device 3 functions to provide gas pressure feedback in the form of the pressure input signals to the Electronic Control Logic Subsystem 4. The Gas Pressure Sensing Device 3 may be a separate device in line, or may be a device that is incorporated as an integral part of the motor driven pump 1, the pressure sensing device 2, the Electronic Control Logic Subsystem 4, the carbjet 5, or other external system component. Item 3 may be directly or indirectly sensing the pressure and communicating the feedback through various types of process signal communication values and methods.

[0072] The Electronic Control Logic Subsystem 4: The electronic control logic subsystem 4 functions to receive input communication signaling from the liquid pressure sensing device 2 and the gas pressure sensing device 3, and or other sensors in the system and implement the control logic. The electronic control logic subsystem 4 provides output communication signaling as the output signals to the motor driven pump 1 for purposes of achieving and maintaining the differential pressure between the incoming liquid and gas feed streams for the end intent of maintaining or changing the set point target for Gas Absorption desired in the liquid output. The absorption level set point is achieved by monitoring and maintaining differential pressure between the Gas and Liquid streams at desired levels entering the carbjet 5 by varying the characteristics of the voltage signal output to the motor driven pump 1. The electronic control logic subsystem 4 may receive communication from other sensors of devices in the inline gas infusion system 10, and use the information to implement control action or output communication signaling to the motor driven pump 1, the liquid pressure sensing device 2, the gas pressure sensing device 3, and the carbjet 5, which are internal to the described system, as well as other internal or external components or devices such as valves, switches, relays, displays, lights, etc. as needed to support auxiliary functions and other system operational objectives. As one skilled in the art would appreciate, suitable control signaling may be implemented between the electronic control logic subsystem 4 and the motor driven pump 1, the liquid pressure sensing device 2, the gas pressure sensing device 3, and the carbjet 5 to implement control action or output communication signaling, e.g., via hardwiring control lines, as well as other techniques known in the art, such as wireless communications. The electronic control logic subsystem 4 may include both electronic hardware components and software program(s), parameters, variables, and logic that are needed to execute the control algorithm and support the operation of the system.

FIG. 4

[0073] FIG. 4 shows an example of a first application generally indicated as 20 having the inline gas liquid infusion system shown in FIG. 3 with an adjustable output, self-tuning application, and also having a single dispenser valve, e.g., for dispensing a nitrogen and/or CO2 infused coffee, tea, latte, or other drinks, according to some embodiments of the present invention.

[0074] As shown in FIGS. 3-4, the motor driven pump 1 may receive the incoming liquid pressure (FIG. 3) from a cold brewed coffee pressurized keg K (FIG. 4) that may be receive pressurized gas (e.g., CO2 and/or nitrogen) from a pressured gas tank T1, as shown. The pressured gas tank T1 may include a gas regulator R1 for pressurizing the liquid vessel or keg K (e.g., about 16 PSI).

[0075] As shown in FIGS. 3-4, the carbjet 5 receives pressured gas from a pressurized gas tank T2 having CO2 or nitrogen gas. The pressurized gas tank T2 may include a gas regulator R2 for providing a gas regulator pressurizing inline absorber device gas input (e.g., about 40 PSI), e.g., for regulating the pressure of the gas provided to the carbjet 5.

[0076] As shown in FIGS. 3-4, the carbjet 5 provides the gas infused liquid (FIG. 3) to a dispensing valve DV shown in FIG. 4, e.g., for dispensing the nitrogen and/or CO2 infused coffee, tea, latte, or other drinks or beverage B. Advantages of this application, e.g., include adjustable nitrogen level outputs, self-tuning variations in the system conditions, and the ability to maintain accuracy and performance with variable input pressures.

FIG. 5

[0077] FIG. 5 shows an example of a second application generally indicated as 30 having the inline gas liquid infusion system shown in FIGS. 3 and 4 with an adjustable output, self-tuning application, and also having a single or multiple dispenser valve, e.g., for dispensing a water carbonation to/for beverages like soda, according to some embodiments of the present invention.

[0078] As shown in FIGS. 3-5, the motor driven pump 1 may receive the incoming liquid pressure (FIG. 3) from a commercial incoming water pressure fixture F (FIG. 4, as shown. The pressured gas tank T1 may include a gas regulator R1 for pressurizing the liquid vessel or keg K (e.g., about 16 PSI).

[0079] As shown in FIGS. 3-5, the carbjet 5 receives pressured gas from a pressurized gas tank T2 having CO2 or nitrogen gas. The pressurized gas tank T2 may include a gas regulator R2 for providing a gas regulator pressurizing inline absorber device gas input (e.g., about 0 to 100 PSI), e.g., for regulating the pressure of the gas provided to the carbjet 5.

[0080] As shown in FIGS. 3-5, the carbjet 5 provides the gas infused liquid (FIG. 3) to a dispensing valve D shown in FIG. 5, e.g., for dispensing the nitrogen and/or CO2 infused syrup-based drinks or beverage. The dispenser D receives the syrup/concentrate, e.g., from a combination of a bag-in-box syrup pump 32, a bag-in-box beverage concentrate container 34 and a pressured gas tank T1, as shown. The pressured gas tank T1 may include a gas regulator R1 for pressurizing gas (e.g. typically 65 PSI) to the bag-in-box syrup pump 32 for driving the same. The bag-in-box beverage concentrate container 34 contain the syrup/concentrate being pumped to the dispenser D.

FIG. 6

[0081] By way of example, FIG. 6 shows an electronic control logic subsystem generally indicated as 10, e.g. having at least one signal processor or signal processor or processing module 12 (hereinafter signal processor) for implementing the signal processing functionality according to some embodiments of the present invention. In operation, the signal processor 12 may be configured to: [0082] receive signaling containing information about a liquid pressure of an incoming liquid provided from a pump to an inline gas liquid absorption device and about a gas pressure of an incoming gas provided to the inline gas liquid absorption device; and [0083] determine corresponding signaling containing information to control the liquid pressure of the incoming liquid provided from the pump to the inline gas liquid absorption device in order to provide real time adjustable set point output levels of gas absorption in the inline gas liquid absorption device, based upon the signaling received.

[0084] By way of further example, the signal processor may be configured to provide the corresponding signaling as output signals or control signaling to control the pump.

[0085] The functionality of the signal processor 12 may be implemented using hardware, software, firmware, or a combination thereof. In a typical software implementation, the processor module may include one or more microprocessor-based architectures having a microprocessor, a random access memory (RAM), a read only memory (ROM), input/output devices and control, data and address buses connecting the same, e.g., consistent with that shown in FIG. 3, e.g., see element 14. A person skilled in the art would be able to program such a microprocessor-based architecture(s) to perform and implement such signal processing functionality described herein without undue experimentation. The scope of the invention is not intended to be limited to any particular implementation using any such microprocessor-based architecture or technology either now known or later developed in the future.

[0086] By way of example, the electronic control logic subsystem 4 may also include, e.g., other signal processor circuits or components 14 that do not form part of the underlying invention, e.g., including input/output modules, one or more memory modules, data, address and control busing architecture, etc. In operation, the signal processor 12 may cooperation and exchange suitable data, address and control signaling with the other signal processor circuits or components 14 in order to implement the signal processing functionality according to the present invention. By way of example, the signaling may be received by such an input module, provided along such a data bus and stored in such a memory module for later processing, e.g., by the signal processor 12. After such later processing, processed signaling resulting from any such determination may be stored in such a memory module, provided from such a memory module along such a data bus to such an output module, then provided from such an output module as the primary control C, e.g., by the at least one signal processor 12.

Possible Applications

[0087] The possible applications may include the following: [0088] Infusing CO2 or other Gases such as Nitrogen into liquids for beverages Water, Soda, Beer, Coffee, Tea, Milk and Yogurt Based (See FIGS. 3 and 4), and/or [0089] Infusing CO2 or other Gases such as Nitrogen into liquids for increasing the effectiveness of cleaning, sanitizing, etc. for example General Surface Cleaning, Soil extraction, Beverage Line Cleaning, Water Purification.

The Scope of the Invention

[0090] While the invention has been described with reference to an exemplary embodiment, it will be understood by those skilled in the art that various changes may be made and equivalents may be substituted for elements thereof without departing from the scope of the invention.

[0091] In addition, may modifications may be made to adapt a particular situation or material to the teachings of the invention without departing from the essential scope thereof. Therefore, it is intended that the invention not be limited to the particular embodiment(s) disclosed herein as the best mode contemplated for carrying out this invention.