CN1085511C - Process for preparing CO2 aerated protein beverage - Google Patents
Process for preparing CO2 aerated protein beverage Download PDFInfo
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- CN1085511C CN1085511C CN99125161A CN99125161A CN1085511C CN 1085511 C CN1085511 C CN 1085511C CN 99125161 A CN99125161 A CN 99125161A CN 99125161 A CN99125161 A CN 99125161A CN 1085511 C CN1085511 C CN 1085511C
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- milk
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- aqueous solution
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Abstract
The present invention relates to a method for producing a protein beverage containing carbonic aid gas, which is characterized in that any known material containing protein is processed into liquid milk paste, and a stabilizing agent, an emulsifying agent and sugar are added to the liquid milk paste to prepare raw paste; then, CO2 acid water solution is added to the raw paste to prepare the protein beverage containing carbonic aid gas. A beverage containing carbonic aid gas, which is produced by the technology provided by the present invention, not only has the function of thirst quenching but also has rich nutrition. The present invention overcomes the defects that a common milk beverage is greasy, and the beverage containing carbonic aid gas is lack in nutrition.
Description
The present invention relates to a kind of manufacture method of CO 2 aerated protein beverage.
Have two big class beverages to receive an acclaim in the market, a class is a protein beverage, promptly utilizes the various milks of animal and plant protein production, as nutritive beverages such as sterilized milk, peanut milk, soymilk, coconut milks; Another kind of is CO 2 aerated beverage for diabetics, as cola, carbonated drink etc.Protein beverage is because of containing nutrition units such as protein, colloid, and viscosity is big, though nutritious not tasty and refreshing, market sale is subjected to certain limitation.There is not nutrition and soda is tasty and refreshing or nutrition is low.Need a kind of abundant nutrient protein that promptly contains in the market, tasty and refreshing again drink.
The objective of the invention is to propose a kind of CO 2 aerated protein beverage manufacture method at the defective of above-mentioned existing beverage, it can make various milk products, as generating the novel protein beverage of a class gassiness behind milk products such as milk, soymilk, peanut milk, coconut milk, almond milk, pine nut milk, the walnut milk adding carbon dioxide, to satisfy market demand.
Below narrate main contents of the present invention:
A kind of manufacture method of CO 2 aerated protein beverage, it is the liquid milk slurry that is processed into known any proteinaceous material, with the milk slurry is raw material, make magma after adding stabilizing agent, emulsifying agent, sugar material, process homogeneous, sterilization, in magma, add the carbon dioxide aqueous acid, make CO 2 aerated protein beverage.Protein content in the CO 2 aerated protein beverage of manufacturing of the present invention 〉=0.1%, best 〉=0.5%, carbon dioxide capacity the best is 〉=1 times (20 ℃ time volume number).
Milk of the present invention slurry can be mixture or its fermentate and the acidifying type material of one or two or more kinds milk among the liquid milk slurry that is processed into of milk, soymilk, peanut milk, coconut milk, almond milk, pine nut milk, walnut milk and other known any proteinaceous material.
Stabilizing agent of the present invention can be known one or two or more kinds the mixture that can be used as among the beverage stabilizer of CMC, PGA, HM, xanthans and other.
Emulsifying agent of the present invention can be known one or two or more kinds the mixture that can be used as the beverage emulsifying agent of sucrose ester, monoglyceride and other.
Sugared material of the present invention can be sucrose, granulated sugar, syrup and other known material that can be used as the sugared source of beverage.
Below be described in detail implementation process of the present invention:
(1) adding the water mill slurry with milk powder or the material that contains phytoprotein makes plant milk slurry or directly makes milk slurry (protein content 〉=0.33%) with fresh milk.
(2) will suckle slurry, sugar, stabilizing agent, emulsifying agent fully mixes, is that 60-70 ℃, pressure are to carry out under the condition of 15-25Mpa after the homogenizer homogeneous handles through colloid mill in temperature, sterilize, sterilising temp is 130-135 ℃, sterilization time is 5-20 second, sterilization back material is cooled to below 60 ℃, and is standby more than 0 ℃.
(3) in pure water, add the 0.01-0.05% citric acid, and it is fully dissolved, the above-mentioned aqueous solution is cooled to 1-5 ℃.In gas mixer, add CO
2, make carbonate aqueous solution.
(4) magma and 60-70% (volume ratio) above-mentioned (3) the step low temperature carbonate aqueous solution of getting above-mentioned (2) step of 30-40% (volume ratio) divides re-filling in container, promptly becomes CO 2 aerated protein beverage.
Evidence desires to make product provided by the present invention to reach effect preferably, promptly reaches protein content 〉=0.1% in the beverage provided by the present invention, CO
2Molten amount 〉=1 times (20 ℃ time volume number), each amount of substance is (percentage by weight):
Protein content 0.6-3% in the milk slurry; 4-16% sucrose (or granulated sugar or syrup of suitable sugariness); The pure water of 60-70%; 0.2-0.6%PGA; The 0.1-1% HM; 0.1-0.8%CMC; The 0.1-0.5% xanthans; The 0.05-0.15% sucrose ester; The 0.006-0.035% citric acid.
The present invention has following typical advantages:
One, the above-mentioned low temperature method of loading in mixture of the present invention's employing has solved and added the big problem of carbon dioxide difficulty in protein beverage.Owing to contain amounts of protein, stabilizing agent, sugar in the protein beverage, when inflation, easily produce foam, increased the difficulty of mixing with carbon dioxide.Method provided by the invention has solved this difficulty.
Two, protein stabilization of the present invention is finished dealing with by using stabilizing agent, emulsifying agent and high-temperature sterilization and homogeneous.Owing to contain certain calcium ion in the milk and in the water, can directly influence the stabilization of protein and stabilizing agent.The present invention makes the protein drink structural state stable by the following method:
(1) uses stabilizing agents such as PGA, CMC, HM, xanthans that the viscosity of milk is increased, form the stability structure of stabilizing agent and protein.Form with negative electrical charge between this micrograined texture is repelled, and forms stable colloidal dispersion system, prevents the cohesion and the precipitation of albumen.Along with the reduction of pH value, especially effect is more obvious in the pH3.8-5.0 scope.
(2) homogeneous is handled: it is another effective measures that guarantee stability that homogeneous is handled.Mixed milk liquid is handled under the 15-60Mpa condition at 60-70 ℃, and by impacting with high pressure, shearing-crushing makes big particle form tiny particulate.Especially smash fat globule, make it to combine effectively, form homodisperse system, avoid causing precipitation because particle is excessive with emulsifying agent.
(3) the present invention uses pure water, reduces the calcium ions and magnesium ions in the solution, guarantees the stability of protein.
Three, the aerating drink of the present invention's production, the existing effect of quenching one's thirst, nutritious again property, it is extremely helpful that its people are replenished protein, and it has overcome the shortcoming of common milk beverage soapy feeling and carbonic acid drink shortage trophism.
Below narrate embodiments of the invention
Embodiment 1
Get milk powder 2.4kg, add pure water, be heated to after the dissolving more than 90 ℃ to 50kg, constant temperature 5 minutes is made the milk slurry, adds PGA150g in the milk slurry, CMC150g, high methyl pectin 150g, sucrose ester 80g, sucrose 12kg, after stirring, behind the employing colloid mill homogeneous first time, be cooled to 60-65 ℃, through the homogenizer homogeneous, homogenization pressure is 15-25Mpa.Material is cooled to below 60 ℃ after the sterilization through being heated to 130 ℃ of insulations 5 seconds behind the homogeneous, and this slurry is stand-by for magma.
Get pure water 100kg, add citric acid 300g, fully after the dissolving, sour water (pH value is between 3.8-4.2) is cooled to 1-5 ℃, carbon dioxide is squeezed in the above-mentioned sour water, make carbonate aqueous solution with pressure filling machine.
Magma and carbonated water are added in the container, and its ratio is 1: 2; Promptly make CO 2 aerated protein beverage, can be described as and add vapour milk or milk is laughable.
Embodiment 2
Get soybean 6kg, soaked 8-12 hour, add the water mill slurry, the ratio of water and beans is 1: 7, filters the back with 80 order mesh screens and adds milk powder 1.2kg, and fully the heating of dissolving back was boiled 10-20 minute, made the soymilk slurry.Add CMC100g, xanthans 100g, PGA200g, sucrose ester 100g, monoglyceride 100g, sucrose 10kg in the soymilk slurry, after fully mixing, behind the colloid mill mill, use the homogenizer homogeneous, homogenizing temperature is 60-70 ℃, and homogenization pressure is 15-25Mpa.This slurry material is through being heated to 135 ℃, after be incubated 20 seconds and sterilizing, is cooled to below 60 ℃ standby as magma again.
The method for making of carbonated water is with embodiment 1.
Get magma and carbonated water and add in the container, its ratio is promptly to make CO 2 aerated protein beverage at 2: 3.Can claim aerating soymilk or soymilk cola.
Embodiment 3:
Get peanut 6kg, take off scarlet after, add water mill slurry (ratio of peanut and water is 1: 16), in slurry, add 1kg milk powder, be heated to after stirring more than 90 ℃, be incubated 5 minutes, make peanut and suckle and starch.Add CMC80g, xanthans 70g, PGA150g, sucrose ester 200g, monoglyceride 150g, sucrose 10kg in peanut milk slurry, after fully mixing, behind the colloid mill mill, use the homogenizer homogeneous, homogenizing temperature is 70-75 ℃, and homogenization pressure is 15-25Mpa.Above-mentioned slurry is heated to 130 ℃, keeps sterilizing in 10 seconds, is cooled to below 60 ℃ standby as magma again.
The method for making of carbonated water is with embodiment 1
Get magma and carbonated water and add in the container, its ratio is promptly to make CO 2 aerated protein beverage at 3: 7, can be described as aerating peanut milk or peanut milk is laughable.
Claims (1)
1, a kind of manufacture method of CO 2 aerated protein beverage is characterized in that the procedure of processing of this method is:
(1) adding the water mill slurry with milk powder or the material that contains phytoprotein makes plant milk slurry or directly makes milk slurry, its protein content 〉=0.33% with fresh milk;
(2) will suckle slurry, sugar, stabilizing agent, emulsifying agent fully mixes, after milling treatment of colloid, in temperature is that 60-75 ℃, pressure are to carry out the homogenizer homogeneous under the condition of 15-25Mpa to handle, homogeneous is promptly sterilized after handling, sterilising temp is 130-135 ℃, sterilization time is 5-20 second, and sterilization back material is cooled to below 60 ℃, standby more than 0 ℃;
(3) in pure water, add the 0.01-0.05% citric acid, it is fully dissolved, and to make pH value of aqueous solution be 3.8-4.2, the above-mentioned aqueous solution is cooled to 1-5 ℃, in gas mixer, add CO
2, make carbonate aqueous solution;
(4) magma and 60-70% (volume ratio) above-mentioned (3) the step low temperature carbonate aqueous solution of getting above-mentioned (2) step of 30-40% (volume ratio) divides re-filling in container, promptly becomes CO 2 aerated protein beverage.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN99125161A CN1085511C (en) | 1999-11-26 | 1999-11-26 | Process for preparing CO2 aerated protein beverage |
Applications Claiming Priority (1)
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CN99125161A CN1085511C (en) | 1999-11-26 | 1999-11-26 | Process for preparing CO2 aerated protein beverage |
Publications (2)
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CN1254533A CN1254533A (en) | 2000-05-31 |
CN1085511C true CN1085511C (en) | 2002-05-29 |
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CN99125161A Expired - Fee Related CN1085511C (en) | 1999-11-26 | 1999-11-26 | Process for preparing CO2 aerated protein beverage |
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Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US9427015B2 (en) * | 2008-04-07 | 2016-08-30 | Santasti, Inc. | Palate cleansing beverage and method of making and using the same |
CN103283846A (en) * | 2012-03-02 | 2013-09-11 | 乔治.H.克拉克 | Carbonated milk beverage for providing qualitative nutrition of skim milk in people diet and method for preparing carbonated milk beverage |
CN103462141A (en) * | 2013-09-25 | 2013-12-25 | 四川梨梨生物工程有限公司 | Corn germ protein peptide beverage and production method thereof |
TW201815291A (en) * | 2016-10-17 | 2018-05-01 | 王雍驊 | Method for preparing flavored milk soda and passivation method for reducing coagulated agglomerates thereof in which the passivation method is implemented before casein in the milk comes in contact with acidic substances |
CN112352889A (en) * | 2020-11-09 | 2021-02-12 | 光明乳业股份有限公司 | Whey protein bubble water and preparation method thereof |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1123607A (en) * | 1995-08-06 | 1996-06-05 | 徐迤 | Aerated milk drink and its production |
CN1146879A (en) * | 1996-01-16 | 1997-04-09 | 张珩 | Carbonated vegetable protein beverage and its producing process |
-
1999
- 1999-11-26 CN CN99125161A patent/CN1085511C/en not_active Expired - Fee Related
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1123607A (en) * | 1995-08-06 | 1996-06-05 | 徐迤 | Aerated milk drink and its production |
CN1146879A (en) * | 1996-01-16 | 1997-04-09 | 张珩 | Carbonated vegetable protein beverage and its producing process |
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CN1254533A (en) | 2000-05-31 |
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Granted publication date: 20020529 |