CN106962491A - A kind of soybean almond bevertage of disperse enzymolysis Synchronos method production - Google Patents
A kind of soybean almond bevertage of disperse enzymolysis Synchronos method production Download PDFInfo
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- CN106962491A CN106962491A CN201710257024.9A CN201710257024A CN106962491A CN 106962491 A CN106962491 A CN 106962491A CN 201710257024 A CN201710257024 A CN 201710257024A CN 106962491 A CN106962491 A CN 106962491A
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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)
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Abstract
The present invention relates to a kind of soybean almond bevertage of disperse enzymolysis Synchronos method production, 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 soybean almond bevertage of disperse enzymolysis Synchronos method production, belong to food processing field.
Background technology
It with plant kernel, pulp etc. is primary raw material (such as almond) that vegetable protein beverage, which is, it is processed be made with plant
Albumen is the emulsion liquid drink of main body.Vegetable protein beverage is nutritious, not only rich in high-quality protein, also containing fat, dimension
Indispensable nutriment in the human life activities such as raw element, mineral matter.Compared with animal protein milk beverage, vegetable protein
Beverage unsaturated fatty acid content is higher and cholesterol is low, for preventing vascular sclerosis, diabetes from having positive meaning.China
Plant protein resource extremely enriches, and exploitation vegetable protein beverage new varieties are adapted to the eating habit of China consumer, enrich beverage
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 soybean almond bevertage of disperse enzymolysis Synchronos method production, it is desirable to provide a kind of valency
The method for preparing beverage that honest and clean thing is beautiful, storage-stable is good.
A kind of soybean almond bevertage of disperse enzymolysis Synchronos method production, comprises the following steps：
(1) raw material is refined：30 kilograms of soybean, 30 kilograms of almond are taken, 240 kilograms of drinking water are added, it is after mixing that slurries are thin
Change to 220-240 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 23-25U/g substrates；
(3) head-on collision disperse：When being forced into 65-75MPa to slurries using supercharging equipment, slurries are from 2.2-2.3 millimeters of diameter
Micropore in spray and clashed, while slurry pressure was risen with the speed of 8MPa/ minutes, after boosting head-on collision 9-10 minutes,
Stop boosting, slurries continue to clash 10-12 minutes, then stand 2.1-2.3 hours at 42-44 DEG C, form disperse slurries；
(4) Combined size-mixing：640 kilograms of drinking water, 6-7 kilograms of carragheen, white granulated sugar 46-48 thousand are added into disperse slurries
Gram, 2-3 kilograms of 1.6-1.8 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 21-23 minutes at 46-48 DEG C, mixing speed is 3000-3200 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：30 kilograms of soybean, 30 kilograms of almond are taken, 240 kilograms of drinking water are added, it is after mixing that slurries are thin
Change to 240 mesh；
(2) slurries are adjusted：Slurry pH value is adjusted to 5.4, temperature is adjusted to 44 DEG C, adds cellulase degradation 2.1 hours, it is fine
The plain enzyme dosage of dimension is 25U/g substrates；
(4) Combined size-mixing：640 kilograms of drinking water, 7 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 1.8 kilograms of monoglyceride, the soybean oil of HLB value 3.8, mix, 23 are stirred at 48 DEG C
Minute, 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 647nm, and storage period is less than 2 months under 8~32 DEG C of environment.
Embodiment 2
(1) raw material is refined：30 kilograms of soybean, 30 kilograms of almond are taken, 240 kilograms of drinking water are added, it is after mixing that slurries are thin
Change to 240 mesh；
(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 75MPa to slurries using supercharging equipment, slurries are from the micropore of 2.3 millimeters of diameter
Spray and clashed, while slurry pressure was risen with the speed of 8MPa/ minutes, after boosting is clashed 10 minutes, stop boosting, slurry
Liquid continues to clash 12 minutes, then stands 2.1 hours at 44 DEG C, forms disperse slurries；
(4) Combined size-mixing：Into disperse slurries add 640 kilograms of drinking water, 7 kilograms of carragheen, 48 kilograms of white granulated sugar,
8 kilograms of the sucrose fatty ester of HLB value 13,3 kilograms of 1.8 kilograms of monoglyceride, the soybean oil of HLB value 3.8, are mixed, at 48 DEG C
Stirring 23 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 551nm, and storage period is less than 3 months under 8~32 DEG C of environment.
Embodiment 3
(1) raw material is refined：30 kilograms of soybean, 30 kilograms of almond are taken, 240 kilograms of drinking water are added, it is after mixing that slurries are thin
Change to 240 mesh；
(2) slurries are adjusted：Slurry pH value is adjusted to 5.4, temperature is adjusted to 44 DEG C, adds cellulase, cellulase consumption
For 25U/g substrates；
(3) head-on collision disperse：When being forced into 75MPa to slurries using supercharging equipment, slurries are from the micropore of 2.3 millimeters of diameter
Spray and clashed, while slurry pressure was risen with the speed of 8MPa/ minutes, after boosting is clashed 10 minutes, stop boosting, slurry
Liquid continues to clash 12 minutes, then stands 2.1 hours at 44 DEG C, forms disperse slurries；
(4) Combined size-mixing：Into disperse slurries add 640 kilograms of drinking water, 7 kilograms of carragheen, 48 kilograms of white granulated sugar,
8 kilograms of the sucrose fatty ester of HLB value 13,3 kilograms of 1.8 kilograms of monoglyceride, the soybean oil of HLB value 3.8, are mixed, at 48 DEG C
Stirring 23 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 288nm, and stability is good, can be preserved 9 months under 8~32 DEG C of environment
More than.
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 soybean almond bevertage of disperse enzymolysis Synchronos method production, it is characterised in that comprise the following steps：
(1) raw material is refined：30 kilograms of soybean, 30 kilograms of almond are taken, 240 kilograms of drinking water is added, slurries is refined to after mixing
220-240 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, cellulase is used
Measure as 23-25U/g substrates；
(3) head-on collision disperse：When being forced into 65-75MPa to slurries using supercharging equipment, slurries are micro- from 2.2-2.3 millimeters of diameter
Spray and clashed in hole, while slurry pressure was risen with the speed of 8MPa/ minutes, after boosting is clashed 9-10 minutes, stopped
Boosting, slurries continue to clash 10-12 minutes, then stand 2.1-2.3 hours at 42-44 DEG C, form disperse slurries；
(4) Combined size-mixing：Into disperse slurries add 640 kilograms of drinking water, 6-7 kilograms of carragheen, 46-48 kilograms of white granulated sugar,
7-8 kilograms of the sucrose fatty ester of HLB value 13,2-3 kilograms of 1.6-1.8 kilograms of monoglyceride, the soybean oil of HLB value 3.8, are mixed,
Stirred 21-23 minutes at 46-48 DEG C, mixing speed is 3000-3200 revs/min；
(5) filling and sterilizing：Slurries are sterilized, are cooled down, filling, obtain product.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201710257024.9A CN106962491A (en) | 2017-04-19 | 2017-04-19 | A kind of soybean almond bevertage of disperse enzymolysis Synchronos method production |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201710257024.9A CN106962491A (en) | 2017-04-19 | 2017-04-19 | A kind of soybean almond bevertage of disperse enzymolysis Synchronos method production |
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| CN106962491A true CN106962491A (en) | 2017-07-21 |
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Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| 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 |
| CN103609715A (en) * | 2013-12-05 | 2014-03-05 | 惠尔康集团有限公司 | Whole grain protein beverage and preparation method thereof |
| CN103828927A (en) * | 2014-03-14 | 2014-06-04 | 安徽真心食品有限公司 | Production method for semi-degreased protein milk beverage |
| CN104738191A (en) * | 2015-04-13 | 2015-07-01 | 河北承德露露股份有限公司 | Method for improving stability of vegetable protein drinks |
| CN104824161A (en) * | 2015-05-26 | 2015-08-12 | 内蒙古蒙牛乳业（集团）股份有限公司 | Milk beverage and preparation method thereof |
-
2017
- 2017-04-19 CN CN201710257024.9A patent/CN106962491A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| 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 |
| CN103609715A (en) * | 2013-12-05 | 2014-03-05 | 惠尔康集团有限公司 | Whole grain protein beverage and preparation method thereof |
| CN103828927A (en) * | 2014-03-14 | 2014-06-04 | 安徽真心食品有限公司 | Production method for semi-degreased protein milk beverage |
| CN104738191A (en) * | 2015-04-13 | 2015-07-01 | 河北承德露露股份有限公司 | Method for improving stability of vegetable protein drinks |
| CN104824161A (en) * | 2015-05-26 | 2015-08-12 | 内蒙古蒙牛乳业（集团）股份有限公司 | Milk beverage and preparation method thereof |
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Application publication date: 20170721 |
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