Production of orange juice is described. Raw orange juice is ultrafiltrated in an ultrafilter, thereby obtaining a UF retentate and a UF permeate. The UF permeate is nanofiltered in a nanofilter, thereby obtaining a NF retentate and a NF permeate. The UF retentate and the NF permeate are mixed and then pasteurized in a pasteurizer. The pasteurized mixture forms the orange juice, which is filled in packages. An orange juice having a reduced sugar content while still providing a favorable taste and color is then obtained.

Production of orange juice is described. Raw orange juice is ultrafiltrated in an ultrafilter, thereby obtaining a UF retentate and a UF permeate. The UF permeate is nanofiltered in a nanofilter, thereby obtaining a NF retentate and a NF permeate. The UF retentate and the NF permeate are mixed and then pasteurized in a pasteurizer. The pasteurized mixture forms the orange juice, which is filled in packages. An orange juice having a reduced sugar content while still providing a favorable taste and color is then obtained.

The present disclosure relates, in some embodiments, to a method including demineralizing a protein liquor (i.e., a liquid portion of a lysed microcrop (e.g., Lemna) that has been separated to generate the liquid portion and a solid portion and having a composition including a soluble microcrop protein and a Vitamin B12) to generate a demineralized protein liquor. According to some embodiments, demineralizing the protein liquor may include diafiltration, ultrafiltration, nanofiltration, reverse osmosis filtration, electrodialysis, and/or passing the protein liquor through an ion exchange resin (e.g., an anion exchange resin. a trialkyl ammonium salt having three methyl groups). In some embodiments, a method may further include concentrating a demineralized protein liquor to generate at least one of a milk base and an electrolyte drink.

A method for preparing a filtered beverage includes filtering a raw beverage using a cross-flow ultrafiltration device to produce a solids fraction and a liquid fraction; heating the solids fraction to a temperature of 60° C. or greater to produce a pasteurized solids fraction; microfiltering the liquid fraction through a microfilter having a size cut-off of 1 μm or smaller to produce a microfiltered liquid fraction; and combining the pasteurized solids fraction and the microfiltered liquid fraction to result in the filtered beverage.

A method for preparing a filtered beverage includes filtering a raw beverage using a cross-flow ultrafiltration device to produce a solids fraction and a liquid fraction; heating the solids fraction to a temperature of 60° C. or greater to produce a pasteurized solids fraction; microfiltering the liquid fraction through a microfilter having a size cut-off of 1 μm or smaller to produce a microfiltered liquid fraction; and combining the pasteurized solids fraction and the microfiltered liquid fraction to result in the filtered beverage.

A method for preparing a filtered beverage includes filtering a raw beverage using a cross-flow ultrafiltration device to produce a solids fraction and a liquid fraction; heating the solids fraction to a temperature of 60° C. or greater to produce a pasteurized solids fraction; microfiltering the liquid fraction through a microfilter having a size cut-off of 1 μm or smaller to produce a microfiltered liquid fraction; and combining the pasteurized solids fraction and the microfiltered liquid fraction to result in the filtered beverage.

A system for processing a raw juice feed to produce a final juice, and a method of using same, wherein the final juice has an extended shelf life while preserving many, if not all, of the desirable characteristics of freshly-squeezed juices including, but not limited to, the flavor, the mouthfeel, and aroma, without the need to include additives such as flavor and aroma packs. Advantageously, the final juice obtained using the method and system described herein can be stored at room temperature for at least 60 days and still retain the flavor of fresh juice, while still being sterile or having a reduced bioburden.

A system for processing a raw juice feed to produce a final juice, and a method of using same, wherein the final juice has an extended shelf life while preserving many, if not all, of the desirable characteristics of freshly-squeezed juices including, but not limited to, the flavor, the mouthfeel, and aroma, without the need to include additives such as flavor and aroma packs. Advantageously, the final juice obtained using the method and system described herein can be stored at room temperature for at least 60 days and still retain the flavor of fresh juice, while still being sterile or having a reduced bioburden.

A process for obtaining a concentrated flavour mixture from a malt-based beverage, the process comprising: —providing a malt-based fermented liquid; —subjecting the malt-based fermented liquid to a CO.sub.2 or N.sub.2-stripping step or, at least partially, degassing the malt-based liquid, thereby creating a gas stream comprising volatile flavour components; —collecting the gas stream comprising volatile flavour components; and —separating, by a carbon dioxide or N.sub.2 scrubber, at least partially, the CO.sub.2 or N.sub.2 in the gas stream from the volatile flavour components, obtaining a concentrated volatile flavour fraction; —collecting said volatile flavour fraction and packaging the volatile flavour fraction.

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.