Methods to nitrogen-infuse and dispense beverages
In a method for infusing a gas from a gas source into a liquid beverage, liquid beverage is driven from a beverage container into a liquid inlet port of a venturi mixing device. Nitrogen is infused into the liquid beverage by driving nitrogen through a gas inlet port of the venturi mixing device, thereby delivering nitrogen-infused liquid beverage to a discharge port of the venturi mixing device. The nitrogen-infused liquid beverage is poured from the discharge port through a faucet.
1. A method of serving nitrogen-infused liquid beverage, comprising the steps of:
(a) driving liquid beverage from a beverage container into a liquid inlet port of a venturi mixing device;
(b) driving nitrogen from a gas source through a flow restricting device thereby throttling the nitrogen so as to generate a reduced-pressure nitrogen flow;
(c) infusing the nitrogen into the liquid beverage by driving reduced-pressure nitrogen through a gas inlet port of the venturi mixing device, thereby delivering nitrogen-infused liquid beverage to a discharge port of the venturi mixing device; and
(d) pouring the nitrogen-infused liquid beverage from the discharge port through a faucet.
2. The method of claim 1 , wherein the venturi mixing device comprises a membrane-free venturi mixing device.
3. The method of claim 2 , wherein the venturi mixing device includes at least one of an orifice and a needle valve.
4. The method of claim 1 , wherein the step of driving the liquid beverage from the beverage container comprises a step selected from a list consisting of: pressurizing the beverage container so as to force liquid beverage out of the beverage container and pumping liquid beverage out of the beverage container.
5. The method of claim 1 , wherein the nitrogen is stored in a nitrogen tank and further comprising the step of regulating pressure of the nitrogen to a predetermined range using a pressure regulator.
6. The method of claim 5 , wherein the predetermined range is between 15 psi and 80 psi.
7. The method of claim 1 , further comprising the step of controlling nitrogen flow into the gas inlet port and beverage flow into the liquid inlet port so that the beverage exiting the outlet port includes nitrogen in a range of 120 ppm to 500 ppm by weight.
8. The method of claim 7 , wherein the beverage exiting the outlet port includes nitrogen in a range of 160 ppm to 260 ppm by weight.
9. A method of serving nitrogen-infused liquid beverage, comprising the steps of:
(a) driving liquid beverage from a beverage container into a liquid inlet port of a membrane-free venturi mixing device;
(b) driving nitrogen from a gas source through a flow restricting device thereby throttling the nitrogen so as to generate a reduced-pressure nitrogen flow;
(c) infusing the nitrogen into the liquid beverage by driving reduced-pressure nitrogen through a gas inlet port of the membrane-free venturi mixing device, thereby delivering nitrogen-infused liquid beverage to a discharge port of the venturi mixing device; and
(d) pouring the nitrogen-infused liquid beverage from the discharge port through a faucet.
10. The method of claim 9 , wherein the venturi mixing device includes at least one of an orifice and a needle valve.
11. The method of claim 9 , wherein the step of driving the liquid beverage from the beverage container comprises a step selected from a list consisting of: pressurizing the beverage container so as to force liquid beverage out of the beverage container and pumping liquid beverage out of the beverage container.
12. The method of claim 9 , wherein the nitrogen is stored in a nitrogen tank and further comprising the step of regulating pressure of the nitrogen to a predetermined range using a pressure regulator.
13. The method of claim 12 , wherein the predetermined range is between 15 psi and 80 psi.
14. The method of claim 9 , further comprising the step of controlling nitrogen flow into the gas inlet port and beverage flow into the liquid inlet port so that the beverage exiting the outlet port includes nitrogen in a range of 120 ppm to 500 ppm by weight.
15. The method of claim 14 , wherein the beverage exiting the outlet port includes nitrogen in a range of 160 ppm to 260 ppm by weight.
16. The method of claim 1 , wherein the liquid beverage comprises coffee.
17. The method of claim 16 , further comprising the step of cooling the coffee to a temperature of about 34° F. to 37° F. prior to pouring step.
18. The method of claim 14 , wherein the liquid beverage comprises coffee.
19. The method of claim 18 , further comprising the step of cooling the coffee to a temperature of about 34° F. to 37° F. prior to pouring step.