CN107156309A - A kind of compound peanut beverage for refinement method production of clashing - Google Patents
A kind of compound peanut beverage for refinement method production of clashing Download PDFInfo
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- CN107156309A CN107156309A CN201710257920.5A CN201710257920A CN107156309A CN 107156309 A CN107156309 A CN 107156309A CN 201710257920 A CN201710257920 A CN 201710257920A CN 107156309 A CN107156309 A CN 107156309A
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- slurries
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
- A23C11/00—Milk substitutes, e.g. coffee whitener compositions
- A23C11/02—Milk substitutes, e.g. coffee whitener compositions containing at least one non-milk component as source of fats or proteins
- A23C11/10—Milk substitutes, e.g. coffee whitener compositions containing at least one non-milk component as source of fats or proteins containing or not lactose but no other milk components as source of fats, carbohydrates or proteins
- A23C11/103—Milk substitutes, e.g. coffee whitener compositions containing at least one non-milk component as source of fats or proteins containing or not lactose but no other milk components as source of fats, carbohydrates or proteins containing only proteins from pulses, oilseeds or nuts, e.g. nut milk
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- Oil, Petroleum & Natural Gas (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
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- Seeds, Soups, And Other Foods (AREA)
- Non-Alcoholic Beverages (AREA)
Abstract
The present invention relates to a kind of compound peanut beverage for refinement method production of clashing, the present invention comprises the following steps：The steps such as raw material refinement, slurries regulation, head-on collision disperse, Combined size-mixing, filling and sterilizing.It is the particular approach of the present invention to different from the manufacture craft of traditional protein beverage, raw material is not required to carry out colloid mill refinement and homogenizer processing, you can form the uniform and stable beverage of a kind of " albumen-stable emulsifying-grease " after particular process.
Description
Technical field
The present invention relates to a kind of compound peanut beverage for refinement method production of clashing, belong to food processing field.
Background technology
It with plant kernel, pulp etc. is primary raw material (such as shelled peanut) that vegetable protein beverage, which is, it is processed be made to plant
Thing albumen is the emulsion liquid drink of main body.Vegetable protein beverage is nutritious, not only rich in high-quality protein, also containing fat,
Indispensable nutriment in the human life activities such as vitamin, mineral matter.Compared with animal protein milk beverage, plant egg
White beverage unsaturated fatty acid content is higher and cholesterol is low, for preventing vascular sclerosis, diabetes from having positive meaning.I
State's plant protein resource extremely enriches, and exploitation vegetable protein beverage new varieties are adapted to the eating habit of China consumer, enrich drink
Expect product market.
Vegetable protein beverage is a kind of complicated thermodynamic unstable system, easily in thermal sterilization and subsequent storage
The middle rising phenomenon for producing protein and solid particle coagulation and fat, influences the quality of product.
The content of the invention
It is an object of the invention to provide a kind of compound peanut beverage for refinement method production of clashing, it is desirable to provide a kind of inexpensive thing
The good method for preparing beverage of beautiful, storage-stable.
A kind of compound peanut beverage for refinement method production of clashing, comprises the following steps：
(1) raw material is refined：60 kilograms of shelled peanut is taken, 240 kilograms of drinking water is added, slurries is refined to 220- after mixing
240 mesh；
(2) slurries are adjusted：Slurry pH value is adjusted to 5.2-5.4, temperature is adjusted to 42-44 DEG C, add cellulase, cellulose
Enzyme dosage is 24-26U/g substrates；
(3) head-on collision disperse：When being forced into 60-70MPa to slurries using supercharging equipment, slurries are from 2.2-2.4 millimeters of diameter
Micropore in spray and clashed, while slurry pressure was risen with the speed of 8MPa/ minutes, after boosting head-on collision 12-14 minutes,
Stop boosting, slurries continue to clash 6-8 minutes, then stand 2.2-2.4 hours at 42-44 DEG C, form disperse slurries；
(4) Combined size-mixing：640 kilograms of drinking water, 10-12 kilograms of carragheen, white granulated sugar 46-48 are added into disperse slurries
Kilogram, 2-3 kilograms of 2.1-2.3 kilograms of monoglyceride, the soybean oil of 7-8 kilograms of the sucrose fatty ester of HLB value 13, HLB value 3.8,
Mix, stirred 22-24 minutes at 44-46 DEG C, mixing speed is 3200-3400 revs/min；
(5) filling and sterilizing：Slurries are sterilized, are cooled down, filling, obtain product.
The innovation of the present invention is：
1st, the present invention carries out limited enzymatic hydrolysis simultaneously using the albumen of particular fineness during head-on collision of pressurizeing, both
It with good cooperative effect, can both amplify the action effect of cellulase, head-on collision dispersion can be increased again.
2nd, albumen has self-emulsifying effect after limited enzymatic hydrolysis and stage pressurization head-on collision processing, can be spontaneous shape
Guarantee is provided into, uniform and stable " albumen-stable emulsifying-grease " form.
3rd, different from the manufacture craft of traditional protein beverage, raw material is not required to carry out colloid mill refinement after particular process
With homogenizer processing, minimum energy state is can reach by way of triggering system fusion automatically, a kind of " albumen-emulsification is formed
The uniform and stable beverage of stabilization-grease ".
Embodiment
The present invention is described in more detail below by embodiment.
Embodiment 1
(1) raw material is refined：60 kilograms of shelled peanut is taken, 240 kilograms of drinking water is added, slurries is refined to 240 mesh after mixing；
(2) slurries are adjusted：Slurry pH value is adjusted to 5.4, temperature is adjusted to 44 DEG C, adds cellulase, cellulase consumption
For 26U/g substrates；
(3) head-on collision disperse：When being forced into 70MPa to slurries using supercharging equipment, slurries are from the micropore of 2.2 millimeters of diameter
Spray and clashed, while slurry pressure was risen with the speed of 8MPa/ minutes, after boosting is clashed 12 minutes, stop boosting, slurry
Liquid continues to clash 8 minutes, then stands 2.2 hours at 44 DEG C, forms disperse slurries；
(4) Combined size-mixing：Into disperse slurries add 640 kilograms of drinking water, 12 kilograms of carragheen, 48 kilograms of white granulated sugar,
8 kilograms of the sucrose fatty ester of HLB value 13,3 kilograms of 2.3 kilograms of monoglyceride, the soybean oil of HLB value 3.8, are mixed, at 46 DEG C
Stirring 24 minutes, mixing speed is 3200 revs/min；
(5) filling and sterilizing：Slurries carry out 115 DEG C sterilization, cooling, it is filling, obtain product.
Through test and appraisal, products taste is good, and average grain diameter is 231nm, and stability is good, and 10 can be preserved under 8~32 DEG C of environment
More than month.
The contrast test 1 of embodiment 2
(1) raw material is refined：60 kilograms of shelled peanut is taken, 240 kilograms of drinking water is added, slurries is refined to 240 mesh after mixing；
(2) slurries are adjusted：Slurry pH value is adjusted to 5.4, temperature is adjusted to 44 DEG C；
(3) head-on collision disperse：When being forced into 70MPa to slurries using supercharging equipment, slurries are from the micropore of 2.2 millimeters of diameter
Spray and clashed, while slurry pressure was risen with the speed of 8MPa/ minutes, after boosting is clashed 12 minutes, stop boosting, slurry
Liquid continues to clash 8 minutes, then stands 2.2 hours at 44 DEG C, forms disperse slurries；
(4) Combined size-mixing：Into disperse slurries add 640 kilograms of drinking water, 12 kilograms of carragheen, 48 kilograms of white granulated sugar,
8 kilograms of the sucrose fatty ester of HLB value 13,3 kilograms of 2.3 kilograms of monoglyceride, the soybean oil of HLB value 3.8, are mixed, at 46 DEG C
Stirring 24 minutes, mixing speed is 3200 revs/min；
(5) filling and sterilizing：Slurries carry out 115 DEG C sterilization, cooling, it is filling, obtain product.
Through test and appraisal, product average grain diameter is 495nm, and storage period is less than 3 months under 8~32 DEG C of environment.
The contrast test 2 of embodiment 3
(1) raw material is refined：60 kilograms of shelled peanut is taken, 240 kilograms of drinking water is added, slurries is refined to 240 mesh after mixing；
(2) slurries are adjusted：Slurry pH value is adjusted to 5.4, temperature is adjusted to 44 DEG C, adds cellulase degradation 2.2 hours, it is fine
The plain enzyme dosage of dimension is 26U/g substrates；
(3) Combined size-mixing：640 kilograms of drinking water, 12 kilograms of carragheen, 48 kilograms of white granulated sugar, HLB value are added into slurries
13 8 kilograms of sucrose fatty ester, 3 kilograms of 2.3 kilograms of monoglyceride, the soybean oil of HLB value 3.8, mix, 24 are stirred at 46 DEG C
Minute, mixing speed is 3200 revs/min；
(4) filling and sterilizing：Slurries carry out 115 DEG C sterilization, cooling, it is filling, obtain product.
Through test and appraisal, product average grain diameter is 563nm, and storage period is less than 2 months under 8~32 DEG C of environment.
The Product checking result of integrated embodiment 1,2 and 3 understands, each implementation steps of the invention are all linked with one another, mutual collaboration,
Indispensable, the product stability of preparation is high, in good taste；The performance of product can be greatly reduced by simplifying or ignoring committed step.
Claims (1)
1. a kind of compound peanut beverage for refinement method production of clashing, it is characterised in that comprise the following steps：
(1) raw material is refined：60 kilograms of shelled peanut is taken, 240 kilograms of drinking water is added, slurries is refined to 220-240 mesh after mixing；
(2) slurries are adjusted：Slurry pH value is adjusted to 5.2-5.4, temperature is adjusted to 42-44 DEG C, add cellulase, cellulase is used
Measure as 24-26U/g substrates；
(3) head-on collision disperse：When being forced into 60-70MPa to slurries using supercharging equipment, slurries are micro- from 2.2-2.4 millimeters of diameter
Spray and clashed in hole, while slurry pressure was risen with the speed of 8MPa/ minutes, after boosting is clashed 12-14 minutes, stopped
Boosting, slurries continue to clash 6-8 minutes, then stand 2.2-2.4 hours at 42-44 DEG C, form disperse slurries；
(4) Combined size-mixing：640 kilograms of drinking water, 10-12 kilograms of carragheen, white granulated sugar 46-48 thousand are added into disperse slurries
Gram, 2-3 kilograms of 2.1-2.3 kilograms of monoglyceride, the soybean oil of 7-8 kilograms of the sucrose fatty ester of HLB value 13, HLB value 3.8, mix
It is even, stirred 22-24 minutes at 44-46 DEG C, mixing speed is 3200-3400 revs/min；
(5) filling and sterilizing：Slurries are sterilized, are cooled down, filling, obtain product.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710257920.5A CN107156309A (en) | 2017-04-19 | 2017-04-19 | A kind of compound peanut beverage for refinement method production of clashing |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710257920.5A CN107156309A (en) | 2017-04-19 | 2017-04-19 | A kind of compound peanut beverage for refinement method production of clashing |
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| CN107156309A true CN107156309A (en) | 2017-09-15 |
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| CN201710257920.5A Pending CN107156309A (en) | 2017-04-19 | 2017-04-19 | A kind of compound peanut beverage for refinement method production of clashing |
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Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101176487A (en) * | 2007-11-28 | 2008-05-14 | 广州合诚实业有限公司 | Peanut nutrition milk and preparation method thereof |
| CN102047965A (en) * | 2009-10-27 | 2011-05-11 | 天津市恒安食品有限公司 | Peanut milk beverage and workmanship thereof |
| CN102326627A (en) * | 2011-08-23 | 2012-01-25 | 汤花荣 | Method for producing peanut beverage |
| CN102870953A (en) * | 2012-09-06 | 2013-01-16 | 广东省农业科学院农业生物技术研究所 | Processing method for solubilizing and modifying rice bran protein |
-
2017
- 2017-04-19 CN CN201710257920.5A patent/CN107156309A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101176487A (en) * | 2007-11-28 | 2008-05-14 | 广州合诚实业有限公司 | Peanut nutrition milk and preparation method thereof |
| CN102047965A (en) * | 2009-10-27 | 2011-05-11 | 天津市恒安食品有限公司 | Peanut milk beverage and workmanship thereof |
| CN102326627A (en) * | 2011-08-23 | 2012-01-25 | 汤花荣 | Method for producing peanut beverage |
| CN102870953A (en) * | 2012-09-06 | 2013-01-16 | 广东省农业科学院农业生物技术研究所 | Processing method for solubilizing and modifying rice bran protein |
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