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Functional-purpose oxygen beverage production method. RU patent 2415613.

Functional-purpose oxygen beverage production method. RU patent 2415613.

FIELD: food industry.

SUBSTANCE: one preliminarily prepares a flavouring additive by way of mixing blackcurrant syrup, maltodextrin and culinary salt of high purification degree into a homogeneous suspension. Then the suspension is dissolved during continual stirring in drinking water preliminarily heated to a temperature of 35-45°C at a ratio of 1:5. Then the produced mixture is delivered into a closed enriching chamber, spread in a thin layer across an inclined silicate base with a corrugated surface and treated with a steam blast highly-enriched with active oxygen forms (singlet oxygen, higher hydrogen peroxides etc.) supplied from an electrolyser. Oxygenation is performed in laminar mode, the flow rate being 2-3 l/s till production of the finished product with oxygen concentration 40-45 mg/l.

EFFECT: method allows to produce a beverage ensuring energy exchange intensification and organism rehydration which promotes energy resources recovery during engagement in long-term physical activities; the energy value of the beverage is 42-50 - kcal /100 ml.

1 dwg, 1 tbl, 3 ex

 


 

IPC classes for russian patent Functional-purpose oxygen beverage production method. RU patent 2415613. (RU 2415613):

A23L2/54 - Mixing with gases
Another patents in same IPC classes:
Method and device for puring of oxygen-enriched air liquids Method and device for puring of oxygen-enriched air liquids / 2391878
Method for pouring of oxygen-enriched or oxygen-gas liquid mixtures or other gases, specifically drinks into pots such as bottles or jars, provides liquid pouring into pots and the enriched liquid is held in nitrogen atmosphere during pouring process with excessive pressure, mainly in the range of 1-10 BARs, after that it is corked up gastight. The pot is being held in the nitrogen atmosphere, especially pressure which corresponds liquid filling pressure, with excessive pressure before liquid supply and before pressure treatment the pot is blown at least one time, mainly with nitrogen, or vacuumised. Also multiple combined pot treatment by blowing and preliminary vacuumisation can be held. Liquid gas, especially liquid nitrogen or oxygen can be added before vacuumisation. Also before liquid supply into the pot, extruded return gas can be collected and used for blowing treatment of the following pots. Device consists of at least one re-entry component with valve for liquid, at least one gas valve for blowing and/or pressure generation in the pot by nitrogen and partially filled with liquid ring boiler with ability to resist nitrogen pressure in the range of 1-10 BARs. The device also includes inductive sensor for consumption measuring and filling component is connected to supplying channel for liquid with lower side of the ring boiler.
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Foaming agent and oxygenated gaseous ingredient are added to the liquid base substance contained in a closed cavity. The liquid base substance is mixed with the foaming agent and the gaseous ingredient is bubbled through the resultant mixture during 6-120 s. The bubble aeration may be performed not only after the mixing but also prior to/during it. The gaseous ingredient is discharged into the liquid base substance under a pressure of 1.0-1.3 gauge atmospheres at a depth of no less than 0.95 of the liquid base substance head. Expenditure of ingredients for preparation of 1 l of the cocktail: foaming agent - 0.5-0.9 mg, oxygenated gaseous ingredient - 0.3-1.0 mg, liquid base substance - the balance. The liquid base substance may be represented by juice and/ or juice-containing beverage and/or fruit infusion and/or phytosolution or milk and/or dairy product. The foaming agent may be represented by liquorice extract and/or syrup and/or soaproot extract and/or syrup and/or gelatine and/or chicken egg white.
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Beverage oxygenation is performed by adding two-component gaseous mixture consisting of carbon dioxide and oxygen to obtain oxygen-rich beverage. Components content in the mixture is smoothly changed. First carbon dioxide content is bigger and makes 80.0-99.5%. Gradually carbon dioxide content is reduced with proportional increase of oxygen content. At the end oxygen content is bigger than carbon dioxide content and makes 80.0-99.5%. It is recommended to supply gaseous mixture under a pressure of 1-6 kg/cm2. Drinking water, mineral water, alcohol-free beverages or juices are used for oxygenation.
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Invention relates to food industry, namely to compositions for oxygen cocktails. The product with components of food foam includes a tank impermeable for gases and liquids and whose contents are a dispersion medium and gaseous phase containing a biologically active gas or a mixture of gases. The tank contents have the atmospheric pressure that the tank walls and the product shape are designed for. The tank can be either rigid or soft. The dispersion medium contains a stabiliser and/or a foaming agent for stabilisation and/or foaming of the phases and a water-holding component for improving the foam stability. The dispersion medium is in the product in a liquid or stabilised state. The product is made with a possibility of foam generation implemented through interaction of the tank walls, dispersion medium and gaseous phase with manual or hardware-controlled shaking of the product without additional mechanisms. The product is made with a possibility of supplying the food foam with fixed gas composition to the consumer's mouth and/or into a tank for taking it by squeezing the tank manually and/or by means of a spoon and/or by means of a pipe, and/or by pouring it out of a detachable spout or a hole that can be closed with a lid and/or a cork. In the product inside the tank the dispersion medium and the gaseous phase are in the form of separate phases and/or foam.
Method and device for puring of oxygen-enriched air liquids Method and device for puring of oxygen-enriched air liquids / 2391878
Method for pouring of oxygen-enriched or oxygen-gas liquid mixtures or other gases, specifically drinks into pots such as bottles or jars, provides liquid pouring into pots and the enriched liquid is held in nitrogen atmosphere during pouring process with excessive pressure, mainly in the range of 1-10 BARs, after that it is corked up gastight. The pot is being held in the nitrogen atmosphere, especially pressure which corresponds liquid filling pressure, with excessive pressure before liquid supply and before pressure treatment the pot is blown at least one time, mainly with nitrogen, or vacuumised. Also multiple combined pot treatment by blowing and preliminary vacuumisation can be held. Liquid gas, especially liquid nitrogen or oxygen can be added before vacuumisation. Also before liquid supply into the pot, extruded return gas can be collected and used for blowing treatment of the following pots. Device consists of at least one re-entry component with valve for liquid, at least one gas valve for blowing and/or pressure generation in the pot by nitrogen and partially filled with liquid ring boiler with ability to resist nitrogen pressure in the range of 1-10 BARs. The device also includes inductive sensor for consumption measuring and filling component is connected to supplying channel for liquid with lower side of the ring boiler.
Functional-purpose oxygen beverage production method Functional-purpose oxygen beverage production method / 2415613
One preliminarily prepares a flavouring additive by way of mixing blackcurrant syrup, maltodextrin and culinary salt of high purification degree into a homogeneous suspension. Then the suspension is dissolved during continual stirring in drinking water preliminarily heated to a temperature of 35-45°C at a ratio of 1:5. Then the produced mixture is delivered into a closed enriching chamber, spread in a thin layer across an inclined silicate base with a corrugated surface and treated with a steam blast highly-enriched with active oxygen forms (singlet oxygen, higher hydrogen peroxides etc.) supplied from an electrolyser. Oxygenation is performed in laminar mode, the flow rate being 2-3 l/s till production of the finished product with oxygen concentration 40-45 mg/l.
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