Abstract: A beverage system that produces a fermented beverage from two or more liquid streams, includes a first source including an ultra-high gravity beverage at a pressure of 82.7 kPa to 1034.2 kPa; a second source including a carbonated and/or nitrogenated water at a pressure of 82.7 kPa to 1034.2 kPa and and a temperature of 0° to 8°; a mixing point that allows mixing of the ultra high gravity beverage to blend with the carbonated and/or nitrogenated water to produce a fermented beverage; and a fluid line fluidly coupled to the mixing point and configured to allow the fermented beverage to flow to a dispensing tap. The fluid line has a length of 0.3048 m to 45.72 m and an inner diameter of 3.2 mm to 15.9 mm for at least a portion of the line.

Abstract: A method for producing an ethanol solution includes obtaining, from a starting liquid, a liquid feed having less than by weight of constituents and having 3% to 25% by weight of ethanol, supplying the liquid feed to a feed stream inlet of a reverse osmosis separation system having a first pass, wherein (i) each pass has an reverse osmosis membrane filtration unit, each membrane filtration unit having an ethanol rejection percentage of between 50% to 99%, and (ii) each pass has the feed stream inlet for a feed stream, a permeate stream outlet for a permeate stream, and a retentate stream outlet for a retentate stream, operating the system to maintain pressure in one of the membrane filtration units in a range of 1,200 to 4,000 psi, and obtaining retentate that is enriched with ethanol, the retentate differs from the starting liquid by absence of the removed constituents.

Abstract: A beverage system that produces a beer includes a first source comprising uHGB, a second source including a carbonated and/or nitrogenated water, a first fluid line fluidly coupled to the first source and configured to allow the uHGB to flow from the first source through the first fluid line, a second fluid line fluidly coupled to the second source and configured to allow the water to flow from the second source through the second fluid line, a mixing point, that fluidly couples the first fluid line to the second fluid line, configured to allow the uHGB to blend with the water at the mixing point to produce the beer, first and second one-way valves on either side of the mixing point, and a third fluid line fluidly coupled to the mixing point and configured to allow the beer to flow to a dispensing tap.

Abstract: A beverage system that produces a fermented beverage from two or more liquid streams, includes a first source including an ultra-high gravity beverage at a pressure of 82.7 kPa to 1034.2 kPa; a second source including a carbonated and/or nitrogenated water at a pressure of 82.7 kPa to 1034.2 kPa and and a temperature of 0° to 8°; a mixing point that allows mixing of the ultra high gravity beverage to blend with the carbonated and/or nitrogenated water to produce a fermented beverage; and a fluid line fluidly coupled to the mixing point and configured to allow the fermented beverage to flow to a dispensing tap. The fluid line has a length of 0.3048 m to 45.72 m and an inner diameter of 3.2 mm to 15.9 mm for at least a portion of the line.

Abstract: A beverage system that produces a beer includes a first source comprising uHGB, a second source including a carbonated and/or nitrogenated water, a first fluid line fluidly coupled to the first source and configured to allow the uHGB to flow from the first source through the first fluid line, a second fluid line fluidly coupled to the second source and configured to allow the water to flow from the second source through the second fluid line, a mixing point, that fluidly couples the first fluid line to the second fluid line, configured to allow the uHGB to blend with the water at the mixing point to produce the beer, first and second one-way valves on either side of the mixing point, and a third fluid line fluidly coupled to the mixing point and configured to allow the beer to flow to a dispensing tap.

Abstract: A method for producing an ethanol solution includes obtaining, from a starting liquid, a liquid feed having less than by weight of constituents and having 3% to 25% by weight of ethanol, supplying the liquid feed to a feed stream inlet of a reverse osmosis separation system having a first pass, wherein (i) each pass has an reverse osmosis membrane filtration unit, each membrane filtration unit having an ethanol rejection percentage of between 50% to 99%, and (ii) each pass has the feed stream inlet for a feed stream, a permeate stream outlet for a permeate stream, and a retentate stream outlet for a retentate stream, operating the system to maintain pressure in one of the membrane filtration units in a range of 1,200 to 4,000 psi, and obtaining retentate that is enriched with ethanol, the retentate differs from the starting liquid by absence of the removed constituents.