CN106072666A - A kind of low ash, the production method of soybean peptide without bitter powder and production system - Google Patents
A kind of low ash, the production method of soybean peptide without bitter powder and production system Download PDFInfo
- Publication number
- CN106072666A CN106072666A CN201610389173.6A CN201610389173A CN106072666A CN 106072666 A CN106072666 A CN 106072666A CN 201610389173 A CN201610389173 A CN 201610389173A CN 106072666 A CN106072666 A CN 106072666A
- Authority
- CN
- China
- Prior art keywords
- powder
- feed liquid
- production method
- protease
- filter
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
- C12P21/00—Preparation of peptides or proteins
- C12P21/06—Preparation of peptides or proteins produced by the hydrolysis of a peptide bond, e.g. hydrolysate products
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07K—PEPTIDES
- C07K1/00—General methods for the preparation of peptides, i.e. processes for the organic chemical preparation of peptides or proteins of any length
- C07K1/14—Extraction; Separation; Purification
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07K—PEPTIDES
- C07K1/00—General methods for the preparation of peptides, i.e. processes for the organic chemical preparation of peptides or proteins of any length
- C07K1/14—Extraction; Separation; Purification
- C07K1/34—Extraction; Separation; Purification by filtration, ultrafiltration or reverse osmosis
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M21/00—Bioreactors or fermenters specially adapted for specific uses
- C12M21/18—Apparatus specially designed for the use of free, immobilized or carrier-bound enzymes
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M33/00—Means for introduction, transport, positioning, extraction, harvesting, peeling or sampling of biological material in or from the apparatus
- C12M33/14—Means for introduction, transport, positioning, extraction, harvesting, peeling or sampling of biological material in or from the apparatus with filters, sieves or membranes
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M37/00—Means for sterilizing, maintaining sterile conditions or avoiding chemical or biological contamination
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M37/00—Means for sterilizing, maintaining sterile conditions or avoiding chemical or biological contamination
- C12M37/02—Filters
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M47/00—Means for after-treatment of the produced biomass or of the fermentation or metabolic products, e.g. storage of biomass
- C12M47/12—Purification
Abstract
The present invention proposes a kind of low ash, the production method of soybean peptide without bitter powder, including step: soybean protein isolate powder mixes through water-powder mixer, and heat sterilization；Add protease hydrolysis soybean protein isolate, protease is carried out inactivation process, filter and separate, isolate the protein ingredient not hydrolyzed；Utilize nano-filtration membrane equipment to the feed liquid concentrating and desalinating after filtering；It is evaporated concentrating with double effect evaporator；To the feed liquid activated carbon decolorizing after concentrating, de-suffering reason, add stevioside and adjust taste；The feed liquid that have adjusted taste is carried out low temperature spray drying.The present invention also proposes a kind of soy peptide powder production system.The low ash of present invention offer, high-purity, the production method of soybean peptide without bitter powder, it is achieved that the industrialized production of soybean peptide.Prepare product protein content >=92%, peptide content >=90%, dissolubility=100%, NSI value=100%, the Instant Drinks that add water are true solution state, water white transparency, without any smell.
Description
Technical field
The invention belongs to beans manufacture field, be specifically related to a kind of method of isolated polypeptide from Semen sojae atricolor and setting of use
Standby.
Background technology
Soybean protein isolate is the vegetable protein of high-quality, has several functions characteristic, such as gelation, emulsibility, retentiveness
Etc. advantage.Utilize protease hydrolysis method, soybean protein hydrolysis is prepared as the soybean peptide of little molecule, separates albumen with raw material
Ratio, is more easy to be absorbed by the body.Research finds, soybean peptide molecular weight is little, has good dissolubility；It is being heated or at acid-base condition
Under, there are good anticoagulation, good stability.The maximum feature of soybean peptide is to be absorbed by the body rapidly, its infiltration rate
Faster than aminoacid.Therefore, directly supplement soybean peptide can amino acid whose absorption process in acceleration bodies, improve the body utilization to nitrogen
Rate, it is provided that the nutrient substance required for growth in humans, growth.Meanwhile, the aminoacid sequence of some soybean peptide and some life internal
Reason activity modulators is similar to, and directly participates in the regulation that organism physiology is movable, or has and irritate dividing of intestinal receptor hormone or enzyme
Secrete and human body is played many very important physiological actions.As regulate blood pressure, resist free radical, improve immunity, alleviate tired
Labor, slow down aging and preventing and treating hyperlipidemia etc., this is not available for raw foods albumen or other aminoacid.Soybean peptide has
Wide application prospect, it is no matter on functional characteristic, or has its unique distinction on threpsology, is that food industry emphasis is opened
One of soybean further process product sent out.
Soybean peptide series products the most on the market is primarily present and has a problem in that molecular weight is relatively big, pained saline taste weight.Want real
Existing soybean peptide industrialized production, it is necessary to screen suitable protease preparation, determines optimum hydrolysis bar according to the character of protease
Part, has the hydrolysis of control to soybean protein.To select isolated and purified means and desalination to go bitter method simultaneously, thus form one
Overlap perfect production technology and equipment configuration, the soybean peptide product just can produced.
Summary of the invention
It is an object of the invention to overcome the defect of prior art, propose a kind of low ash, the life of soybean peptide without bitter powder
Product method.
Second object of the present invention is the production system proposing a kind of soy peptide powder.
The technical scheme realizing above-mentioned purpose of the present invention is:
A kind of low ash, the production method of soybean peptide without bitter powder, including step:
S1, soybean protein isolate powder mix through water-powder mixer, adjust gained soybean protein isolate powder pigment mixture
Solid content is 5～10%, and heat sterilization；
S2, regulation S1 gained mixture pH value to 7.0-8.0, temperature is 45 DEG C～65 DEG C, add protease carry out water
Solving soybean protein isolate powder, described protease is alkaline protease and/or flavor protease；
By heating, protease is carried out inactivation process, heating-up temperature 70～90 DEG C, heat time heating time 10～30 after S3, hydrolysis
Minute；
S4, to through inactivation process after feed liquid carry out filter separate, isolate the protein ingredient not hydrolyzed；
S5, utilize nano-filtration membrane equipment to the feed liquid concentrating and desalinating after filtering, and cutting out partial free amino acid；
S6, the feed liquid double effect evaporator after desalination is evaporated concentrate；
S7, to the feed liquid activated carbon decolorizing after concentrating, de-suffering reason, the temperature of process is 40～80 DEG C；
S8, addition account for the feed liquid quality after S7 processes 0.1～the stevioside adjustment taste of 0.3%；
S9, the feed liquid that have adjusted taste is carried out low temperature spray drying, obtain soy peptide powder.
Preferably, in described S1, sterilising temp controls at 60 DEG C～90 DEG C, sterilization time 15～30 minutes.
It is highly preferred that in described S2, add and account for soybean protein isolate powder pigment mixture quality percentage ratio 0.2-2% alkali
Property protease and mass percent 0.1-1% flavor protease, hydrolysis time is 3～8 hours.
After enzyme digestion reaction, needing to carry out protease inactivation process, the common practice can be by the way of heating again
Being destroyed by enzyme, the temperature of heating is 70 DEG C～90 DEG C, and in order to ensure enzyme inactivation fully, heat time heating time can keep 10～30 points
Clock, certainly, concrete heat time heating time, needs the temperature considering again to heat, in certain scope, the highest mistake to enzyme of temperature
Effect of living is the strongest, and the time of heating just can correspondingly shorten, it is considered to energy consumption and cost, is not that temperature is the highest more good.
Wherein, in described S4, by inactivation process after feed liquid be cooled to 20～50 DEG C, regulation solid content be 4～
8%, pH value is 4～6, then filters.The pH value available quality mark 20 of feed liquid～40% hydrochloric acid solution regulation.
Wherein, in described S5, the feed liquid after filtration adds the deionized water that electrical conductivity is 10～30 μ S/cm and adds solid content
It is 0.5～5%, utilizes nano-filtration membrane equipment desalination.
Preferably, in described S6, the steam pressure of double effect evaporator is 0.1 ± 0.02MPa, and operating temperature is 40 DEG C～80
DEG C, 20～40% of the feed liquid quality after evaporation and concentration to desalination.
In described S7, activated carbon addition is concentrate feed liquid quality 0.2～0.5%, and the time of process is 0.5～3 little
Time.
The present invention also proposes a kind of soy peptide powder production system, and it includes water-powder mixer, enzymatic vessel, and first filters dress
Put, nano-filtration membrane equipment, evaporation equipment, the second defecator, steriliser and spray drying tower, described water-powder mixer, enzymatic vessel,
First defecator, nano-filtration membrane equipment, evaporation equipment, the second defecator, steriliser and spray drying tower are by pipeline successively
Connect.
Preferably, described enzymatic vessel is provided with and is passed through the chuck adding thermal medium or cooling medium.Described steriliser is ultraviolet
Line steriliser, or sterilizing filter；Described spray drying tower is press spray drying tower or Centrafugal spray drying tower.
The said equipment, during extracting, is provided with temporary storage tank between nano-filtration membrane equipment and double-effect falling film evaporator.
When needing liquid to carry between adjacent equipment, generally delivery pump is set between adjacent equipment, can be high-pressure pump etc..
Wherein, described first defecator and the second defecator are independently of each other selected from filter press, microporous filter
One in machine, diatomite filter.
Wherein, the molecular size range that described nano-filtration membrane equipment retains is 200～1000Dalton.
The free amino acid of below part 180Dalton can be produced, because of this patent employing in protease hydrolysis solution
Nano-filtration membrane equipment molecular cut off is more than 200Dalton, makes part free amino acid be gone out by deionized water eluting, thus carries
The high content of soybean peptide, because soybean peptide content is sour molten protein content deducts free aminoacid content, so free ammonia
The content of the base the fewest soybean peptide of acid is the highest.
The beneficial effects of the present invention is:
The low ash of present invention offer, high-purity, the production method of soybean peptide without bitter powder, it is achieved that the industry of soybean peptide
Metaplasia is produced.Prepare product protein content >=92%, peptide content >=90%, dissolubility=100%, NSI value=100%, add
Water Instant Drinks are true solution state, water white transparency, without any smell.
Accompanying drawing explanation
Fig. 1 is soy peptide powder flow sheet.
Fig. 2 is soy peptide powder operation system structure figure.
In figure, 1 is weighing balance, 2 is conveyer, 3 for water-powder mixer, and 4 is enzymatic vessel, 5 is the first defecator, 6 is
Circulating tank, 7 being nano-filtration membrane equipment, 8 is temporary storage tank, and 9 is double effect evaporator, and 10 is de-bitter tank, and 11 is the second defecator, and 12 are
Discharge tank, 13 is steriliser, and 14 is force (forcing) pump, and 15 is spray drying tower.
Detailed description of the invention
Now with following example, the present invention is described, but is not limited to the scope of the present invention.
The means used in embodiment, if no special instructions, all use the means that this area is conventional.
Embodiment 1:
See Fig. 2, a kind of soy peptide powder production system, including water-powder mixer 3, enzymatic vessel 4, the first defecator 5, receive
Filter membrane equipment 7 (molecular weight retained is more than 200Dalton), evaporation equipment, the second defecator 11, steriliser 13 and spray dried
Dry tower 15.The raw material producing soy peptide powder is firstly added weighing balance 1, sequentially passes through conveyer 2, water-powder mixer 3 by pipeline,
Enzymatic vessel 4, the first defecator 5, circulating tank 6, (nano-filtration membrane equipment is connected nano-filtration membrane equipment 7 with circulating tank 6, and this nanofiltration sets
For wanting supporting two 50m3Circulating tank), temporary storage tank 8, double effect evaporator 9, de-bitter tank 10, the second defecator 11, discharge tank 12,
Steriliser 13, force (forcing) pump 14 and spray drying tower 15.
Wherein, enzymatic vessel is provided with and is passed through the chuck adding thermal medium or cooling medium.Described steriliser is ultraviolet disinfection
Device；Described spray drying tower is press spray drying tower.Wherein, the first non-diatomite filter of defecator 5, second filters
Device 11 is filter press.
Fig. 1 is shown in production procedure, and the step that the present embodiment produces soy peptide powder is as follows:
S1, soybean protein isolate powder mix through water-powder mixer, adjust gained soybean protein isolate powder pigment mixture
Solid content is 10%, is heated to 80 DEG C, sterilizing 15 minutes.
S2, regulation S1 gained mixture pH value to 7.5, controlled enzymatic hydrolysis tank temperature is 55 DEG C, add account for soybean separation protein
The Alcalase alkaline protease of white lead pigment mixture quality percentage ratio 1% and the 500MG flavor protease of 0.5% (are all purchased
Believe from Novi) be hydrolyzed soybean protein isolate powder, hydrolysis time 5 hours.
By heating, protease is carried out inactivation process, heating-up temperature～90 DEG C, 15 minutes heat time heating times after S3, hydrolysis.
S4, inactivation is processed after feed liquid be cooled to 30 DEG C, regulation solid content is 4%, pH value is 5 (to use 30% salt
Acid solution regulates), then filter, isolate the protein ingredient not hydrolyzed；It is 10 that feed liquid after filtration adds electrical conductivity
～30 deionized waters of μ S/cm, making solid content is 1%.
S5, utilizing nano-filtration membrane equipment to the feed liquid concentrating and desalinating after filtering, and cutting out partial free amino acid, after desalination
The electrical conductivity of feed liquid is 1000us/cm.
S6, it being evaporated the feed liquid double effect evaporator after desalination concentrating, the steam pressure of double effect evaporator is 0.1 ±
0.02MPa, operating temperature is 80 DEG C, 30% of the feed liquid quality after evaporation and concentration to desalination.
S7, material to the feed liquid activated carbon decolorizing after concentrating, de-suffering reason, under temperature 60 C, in de-bitter tank 10
Liquid adds activated carbon 0.2wt%, processes 2 hours.After filtering with filter press, filtrate is released in batch can 12 temporarily.
S8, add account for S7 process after feed liquid quality 0.1% stevioside adjust taste；
S9, the feed liquid that have adjusted taste is carried out low temperature spray drying, obtain soy peptide powder.
In the soybean peptide product that the present embodiment prepares, protein content is 95%, soybean peptide is 91.5%, and ash is 1.1%,
Moisture≤5%, dissolubility=100%, NSI value=100%, be dissolved at normal temperatures water be water white transparency, without any smell
Solution.
Embodiment 2
The production system used is with embodiment 1, and the step producing soy peptide powder is as follows:
S1, soybean protein isolate powder mix through water-powder mixer, adjust gained soybean protein isolate powder pigment mixture
Solid content is 10%, and heat sterilization；Sterilising temp controls at 80 DEG C, sterilization time 30 minutes.
S2, regulation S1 gained mixture pH value to 8.0, temperature is 65 DEG C, add 1%Alcalase alkaline protease and
0.5% Novi's letter 500MG flavor protease is hydrolyzed, and hydrolysis time is 8 hours.
By heating, protease is carried out inactivation process, heating-up temperature 90 DEG C, 15 minutes heat time heating times after S3, hydrolysis；
Feed liquid after S4, inactivation process is cooled to 20 DEG C, and regulation solid content is 8%, pH value is 6 (to use 30% hydrochloric acid
Solution), then filter.
It is 0.5% that feed liquid after S5, filtration add the deionized water that electrical conductivity is 10～30 μ S/cm to add solid content, profit
Using nano-filtration membrane equipment desalination, after desalination, the electrical conductivity of feed liquid is 1200us/cm.
S6, the feed liquid double effect evaporator after desalination is evaporated concentrate；The steam pressure of double effect evaporator is 0.1 ±
0.02MPa, operating temperature is 80 DEG C, 40% of the feed liquid quality after evaporation and concentration to desalination.
S7, to the feed liquid activated carbon decolorizing after concentrating, de-suffering reason, the temperature of process is 70 DEG C；Activated carbon addition
For concentrating the 0.5% of feed liquid quality, the time of process is 3 hours.
S8, add account for S7 process after feed liquid quality 0.3% stevioside adjust taste；
S9, the feed liquid that have adjusted taste is carried out low temperature spray drying, obtain soy peptide powder.
In the soybean peptide product that the present embodiment prepares, protein content 92%, soybean peptide content 90%, ash is 2%, moisture
Be 4%, dissolubility=100%, NSI value=100%, be dissolved at normal temperatures water be water white transparency, molten without any smell
Liquid.
Embodiment 3
The production system used is with embodiment 1, and the step producing soy peptide powder is as follows:
S1, soybean protein isolate powder mix through water-powder mixer, adjust gained soybean protein isolate powder pigment mixture
Solid content is 5%, and heat sterilization；Sterilising temp controls 60 DEG C, sterilization time 30 minutes.
S2, regulation S1 gained mixture pH value to 7.0, temperature is 45 DEG C, add protease A lcalase basic protein
Enzyme and Dong Henghua road flavor protease, addition and hydrolysis time are with embodiment 1.
S3, S4 operate with embodiment 1.
It is 2% that feed liquid after S5, filtration add the deionized water that electrical conductivity is 10～30 μ S/cm to add solid content, desalination
The electrical conductivity of rear feed liquid is 1000us/cm.
S6, the feed liquid double effect evaporator after desalination is evaporated concentrate；The steam pressure of double effect evaporator is 0.1 ±
0.02MPa, operating temperature is 80 DEG C, 25% of the feed liquid quality after evaporation and concentration to desalination.
S7, to the feed liquid activated carbon decolorizing after concentrating, de-suffering reason, the temperature of process is 60 DEG C；Activated carbon addition
For concentrating the 0.3% of feed liquid quality, the time of process is 1 hour.
S8, add account for S7 process after feed liquid quality 0.2% stevioside adjust taste；
S9, the feed liquid that have adjusted taste is carried out low temperature spray drying, obtain soy peptide powder.
In the soybean peptide product that the present embodiment prepares, protein content is 94%, soybean peptide content is 92%, and ash is 2%,
Moisture is 3%, dissolubility=100%, NSI value=100%, be dissolved at normal temperatures water be water white transparency, without any smell
Solution.
Although, used general explanation, detailed description of the invention and test, the present invention made detailed retouching
Stating, but on the basis of the present invention, can make some modifications or improvements it, this is apparent to those skilled in the art
's.Therefore, these modifications or improvements without departing from theon the basis of the spirit of the present invention, belong to claimed
Scope.
Claims (10)
1. a low ash, the production method of soybean peptide without bitter powder, it is characterised in that include step:
S1, soybean protein isolate powder mix through water-powder mixer, adjust the solid of gained soybean protein isolate powder pigment mixture
Thing content is 5～10%, and heat sterilization；
S2, regulation S1 gained mixture pH value to 7.0-8.0, temperature is 45 DEG C～65 DEG C, add protease hydrolysis Semen sojae atricolor divide
From albumen, described protease is alkaline protease and/or flavor protease；
By heating, protease carried out inactivation process, heating-up temperature 70～90 DEG C, heat time heating time 10～30 points after S3, hydrolysis
Clock；
S4, to through inactivation process after feed liquid carry out filter separate, isolate the protein ingredient not hydrolyzed；
S5, utilize nano-filtration membrane equipment to filter after feed liquid concentrating and desalinating；
S6, the feed liquid double effect evaporator after desalination is evaporated concentrate；
S7, to the feed liquid activated carbon decolorizing after concentrating, de-suffering reason, the temperature of process is 40～80 DEG C；
S8, addition account for the feed liquid quality after S7 processes 0.1～the stevioside adjustment taste of 0.3%；
S9, the feed liquid that have adjusted taste is carried out low temperature spray drying, obtain soy peptide powder.
Production method the most according to claim 1, it is characterised in that in described S1, sterilising temp controls at 60 DEG C～90
DEG C, sterilization time 15～30 minutes.
Production method the most according to claim 1, it is characterised in that in described S2, adds and accounts for soybean protein isolate powder water
Powder mixture mass percent 0.2-2% alkaline protease and mass percent 0.1-1% flavor protease, hydrolysis time is
3～8 hours.
Production method the most according to claim 1, it is characterised in that in described S4, the feed liquid cooling after inactivation is processed
To 20～50 DEG C, regulation solid content be 4～8%, pH value be 4～6, then filter.
Production method the most according to claim 1, it is characterised in that in described S5, the feed liquid after filtration adds electrical conductivity
Be 10～30 μ S/cm deionized water add solid content be 0.5～5%, utilize nano-filtration membrane equipment desalination.
Production method the most according to claim 1, it is characterised in that in described S6, the steam pressure of double effect evaporator is
0.1 ± 0.02MPa, operating temperature is 40 DEG C～80 DEG C, the 20-40% of the feed liquid quality after evaporation and concentration to desalination.
Production method the most according to claim 1, it is characterised in that in described S7, activated carbon addition is for concentrating feed liquid
The 0.2～0.5% of quality, the time of process is 0.5～3 hour.
8. a soy peptide powder production system, it is characterised in that including water-powder mixer (3), enzymatic vessel (4), first filters dress
Put (5), nano-filtration membrane equipment (7), evaporation equipment, the second defecator (11), steriliser (13) and spray drying tower (15), described
Water-powder mixer (3), enzymatic vessel (4), the first defecator (5), nano-filtration membrane equipment (7), evaporation equipment, the second defecator
(11), steriliser (13) and spray drying tower (15) are sequentially connected with by pipeline.
Soy peptide powder production system the most according to claim 8, it is characterised in that described first defecator (5) and
Two defecators (11) one in filter press, microporous filter, diatomite filter independently of each other；Described receive
The molecular size range that filter membrane equipment (7) retains is 200～1000Dalton.
Soy peptide powder production system the most according to claim 8, it is characterised in that described enzymatic vessel is provided with to be passed through and adds
Thermal medium or the chuck of cooling medium；Described steriliser is ultraviolet sterilizer, or sterilizing filter；Described spray drying tower is
Press spray drying tower or Centrafugal spray drying tower.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610389173.6A CN106072666A (en) | 2016-06-03 | 2016-06-03 | A kind of low ash, the production method of soybean peptide without bitter powder and production system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610389173.6A CN106072666A (en) | 2016-06-03 | 2016-06-03 | A kind of low ash, the production method of soybean peptide without bitter powder and production system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106072666A true CN106072666A (en) | 2016-11-09 |
Family
ID=57448070
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610389173.6A Pending CN106072666A (en) | 2016-06-03 | 2016-06-03 | A kind of low ash, the production method of soybean peptide without bitter powder and production system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106072666A (en) |
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107232391A (en) * | 2017-04-14 | 2017-10-10 | 荣海生物科技有限公司 | A kind of method that use compound protease removes Soybean Peptide bitter taste |
| CN107950746A (en) * | 2018-01-16 | 2018-04-24 | 山东禹王生态食业有限公司 | A kind of high whiteness soybean protein isolate and preparation method thereof |
| CN108208309A (en) * | 2017-12-28 | 2018-06-29 | 保龄宝生物股份有限公司 | The production method of low ash content soybean peptide containing profitable probliotics |
| CN108294164A (en) * | 2018-03-29 | 2018-07-20 | 江南大学 | A kind of method and system of the 7S albumen of preparation of industrialization soybean protein |
| CN108477620A (en) * | 2017-12-28 | 2018-09-04 | 武汉天天好生物制品有限公司 | A kind of highly dissoluble soybean peptide oral liquid and its preparation process |
| CN109750074A (en) * | 2019-01-21 | 2019-05-14 | 国药肽谷有限公司 | A kind of extracting method for the royal jelly peptide improving diabetes with auxiliary |
| CN110590902A (en) * | 2019-08-26 | 2019-12-20 | 内蒙古科然生物高新技术有限责任公司 | Method for producing soybean glycopeptide by using soybean molasses and soybean protein isolate powder |
| CN111034851A (en) * | 2018-10-15 | 2020-04-21 | 徐国庆 | Production method capable of improving purity and yield of soybean peptide |
| CN111642666A (en) * | 2020-06-05 | 2020-09-11 | 内蒙古科然生物高新技术有限责任公司 | Preparation method of ginseng extract soybean peptide powder solid beverage |
| CN112841623A (en) * | 2020-12-30 | 2021-05-28 | 广州合诚实业有限公司 | Bee pupa protein peptide food composition for improving immunity and preparation method and application thereof |
| CN114158666A (en) * | 2021-12-10 | 2022-03-11 | 厦门元之道生物科技有限公司 | Preparation method and application of soybean oligopeptide |
| CN114698723A (en) * | 2022-04-21 | 2022-07-05 | 山东禹王生态食业有限公司 | High-flavor functional soybean protein isolate and production method thereof |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1932027A (en) * | 2006-09-20 | 2007-03-21 | 吉林农业大学 | Double enzyme hydrolysis process for preparing soybean peptide without bitter |
| CN205077060U (en) * | 2015-09-24 | 2016-03-09 | 武汉科泰生化科技有限公司 | Improve enzymolysis tank's hydrolysed wheat protein powder device |
| CN105420321A (en) * | 2015-12-01 | 2016-03-23 | 辽宁三合酒业有限公司 | Preparation method of weakly-alkaline soybean peptide |
| CN105506045A (en) * | 2016-01-12 | 2016-04-20 | 华隆（乳山）食品工业有限公司 | Efficient preparation technology for low-bitterness and high-quality soybean peptide |
-
2016
- 2016-06-03 CN CN201610389173.6A patent/CN106072666A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1932027A (en) * | 2006-09-20 | 2007-03-21 | 吉林农业大学 | Double enzyme hydrolysis process for preparing soybean peptide without bitter |
| CN205077060U (en) * | 2015-09-24 | 2016-03-09 | 武汉科泰生化科技有限公司 | Improve enzymolysis tank's hydrolysed wheat protein powder device |
| CN105420321A (en) * | 2015-12-01 | 2016-03-23 | 辽宁三合酒业有限公司 | Preparation method of weakly-alkaline soybean peptide |
| CN105506045A (en) * | 2016-01-12 | 2016-04-20 | 华隆（乳山）食品工业有限公司 | Efficient preparation technology for low-bitterness and high-quality soybean peptide |
Non-Patent Citations (1)
| Title |
|---|
| 倪雪朋等: "利用酶法改性技术制备大豆活性肽的研究进展", 《中国酿造》 * |
Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107232391A (en) * | 2017-04-14 | 2017-10-10 | 荣海生物科技有限公司 | A kind of method that use compound protease removes Soybean Peptide bitter taste |
| CN108208309A (en) * | 2017-12-28 | 2018-06-29 | 保龄宝生物股份有限公司 | The production method of low ash content soybean peptide containing profitable probliotics |
| CN108477620A (en) * | 2017-12-28 | 2018-09-04 | 武汉天天好生物制品有限公司 | A kind of highly dissoluble soybean peptide oral liquid and its preparation process |
| CN107950746A (en) * | 2018-01-16 | 2018-04-24 | 山东禹王生态食业有限公司 | A kind of high whiteness soybean protein isolate and preparation method thereof |
| CN108294164B (en) * | 2018-03-29 | 2022-02-01 | 江南大学 | Method and system for industrially preparing 7S protein of soybean protein |
| CN108294164A (en) * | 2018-03-29 | 2018-07-20 | 江南大学 | A kind of method and system of the 7S albumen of preparation of industrialization soybean protein |
| CN111034851A (en) * | 2018-10-15 | 2020-04-21 | 徐国庆 | Production method capable of improving purity and yield of soybean peptide |
| CN109750074A (en) * | 2019-01-21 | 2019-05-14 | 国药肽谷有限公司 | A kind of extracting method for the royal jelly peptide improving diabetes with auxiliary |
| CN110590902A (en) * | 2019-08-26 | 2019-12-20 | 内蒙古科然生物高新技术有限责任公司 | Method for producing soybean glycopeptide by using soybean molasses and soybean protein isolate powder |
| CN111642666A (en) * | 2020-06-05 | 2020-09-11 | 内蒙古科然生物高新技术有限责任公司 | Preparation method of ginseng extract soybean peptide powder solid beverage |
| CN112841623A (en) * | 2020-12-30 | 2021-05-28 | 广州合诚实业有限公司 | Bee pupa protein peptide food composition for improving immunity and preparation method and application thereof |
| CN114158666A (en) * | 2021-12-10 | 2022-03-11 | 厦门元之道生物科技有限公司 | Preparation method and application of soybean oligopeptide |
| CN114158666B (en) * | 2021-12-10 | 2023-10-13 | 厦门元之道生物科技有限公司 | Preparation method and application of soybean oligopeptide |
| CN114698723A (en) * | 2022-04-21 | 2022-07-05 | 山东禹王生态食业有限公司 | High-flavor functional soybean protein isolate and production method thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN106072666A (en) | A kind of low ash, the production method of soybean peptide without bitter powder and production system | |
| CN102115774B (en) | Method for preparing plant polypeptide by enzyme process | |
| RU2084172C1 (en) | Method of preparing the whey protein hydrolyzate | |
| JP2659105B2 (en) | How to make soy sauce | |
| CN102204620B (en) | Method for preparing bitterless protein peptides | |
| WO2016173222A1 (en) | Hypoallergenic, odor-reduced fish protein oligopeptide, industrialized preparation method for same, and applications thereof | |
| CN101104866A (en) | Technique for producing protein peptide and isoflavone extracted from bean sprout | |
| CN107753927A (en) | Chinese medicine composition of the peptide containing the membrane of a chicken's gizzard with promoting digestion and removing indigestion effect and its production and use | |
| CN105475881A (en) | Desalination method for salted egg white, salted-egg-white protein peptide powder and preparation method | |
| CA2105673C (en) | Method for production of a vegetable protein hydrolyzate and a use thereof | |
| CN102511890A (en) | Jellyfish beverage | |
| CN112760349A (en) | Method for extracting soybean peptide by enzymolysis method | |
| CN109757601B (en) | Sea cucumber peptide and production method thereof | |
| CN109984198A (en) | A kind of high protein low lactose skimmed milk powder production technology | |
| CN101773476A (en) | Preparation method for laver antihypertensive peptide particles | |
| CN112226472B (en) | Maltodextrin production process | |
| JPH0254070B2 (en) | ||
| CN112176017A (en) | Method for efficiently extracting protein peptide from sea cucumber intestines | |
| CN205774566U (en) | A kind of be raw material production maize oligopeptide with Zein powder system | |
| CN109880872A (en) | A method of extracting collagen peptide from sturgeon | |
| CN116218935A (en) | Production process of soybean oligopeptide | |
| CN116725116A (en) | Whey protein preparation method | |
| CN102987462B (en) | A kind of preparation method of instant soluble soybean oligosaccharide peptide peanut products | |
| CN109694894A (en) | The production method of active peptide of soybean protein | |
| JPH06504674A (en) | Method for producing vegetable protein hydrolyzate |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20161109 |