CN1687123A - Membrane process for extracting soybean protein peptide and technique of deep processing byproduct - Google Patents
Membrane process for extracting soybean protein peptide and technique of deep processing byproduct Download PDFInfo
- Publication number
- CN1687123A CN1687123A CN 200510046351 CN200510046351A CN1687123A CN 1687123 A CN1687123 A CN 1687123A CN 200510046351 CN200510046351 CN 200510046351 CN 200510046351 A CN200510046351 A CN 200510046351A CN 1687123 A CN1687123 A CN 1687123A
- Authority
- CN
- China
- Prior art keywords
- solution
- soybean
- protein
- soyasaponin
- utilize
- 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.)
- Granted
Links
Landscapes
- Peptides Or Proteins (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
Abstract
The present invention relates to a soybean deep-processing technique, in particular, said invention adopts a membrane method to extract soybean protein peptide and relates to a process for deep-processing its by-product. Said invention adopts the procedures of low-temperature soaking soybean cake in alkaline liquor, separation, ultrafiltering and resin adsorption to produce soybean protein peptide and by-product of soybean separation protein, soybean isoflavone, soybean saponin and soybean oligosaccharide.
Description
Technical field
The present invention relates to a kind of soybean deep processing technology field.
Background technology
Contain abundant high-quality protein in the soybean, comprising necessary eight seed amino acids of human body.At present, China existing soybean protein processing enterprise, the soy protein products of using traditional albumen processing technology production is functional relatively poor as gelation, emulsifying property, oil absorbency, water-retentivity, solvability, foaminess and froth stability etc., can't satisfy the needs of foodstuffs industry and producing high-grade food, force some large-scale meat product enterprises to have to use the soybean protein of import for the quality product that guarantees self, and, there is the protein peptide of functional performance can only dependence on import to some.
Summary of the invention
The purpose of this invention is to provide a kind of soy protein products rational membrane process for extracting soybean protein peptide of functional technology preferably and technique of deep processing byproduct thereof.
Membrane process for extracting soybean protein peptide and technique of deep processing byproduct thereof is characterized in that this technology may further comprise the steps:
1) the low temperature soybean meal was through sig water lixiviate 10-20 hour, and the alkali lye solid-liquid ratio is weight percentage 1: 10-20, pH value is 7.5-9, utilize whizzer to isolate bean dregs after the immersion after, utilize the polysulfone membrane ultrafiltration, separating whey solution and protein solution;
2) protein solution is carried out temperature 105-115 ℃, the instantaneous sterilization of time 3-5 second, after the sterilization protein solution is homogenized;
3) protein solution behind the homogeneous is concentrated, spraying drying promptly obtains the finished product soybean protein isolate;
4) protein solution behind the homogeneous is added protease hydrolysis, hydrolysis 10 hours utilizes the polysulfone membrane ultrafiltration again after the hydrolysis, and permeate is concentrated, and drying promptly obtains soybean protein peptide;
5) utilize macroporous resin to adsorb the whey solution in the step 1), adsorb the soybean isoflavones composition in the whey solution, utilize 70% ethanolic soln that macroporous resin is carried out wash-out again, obtain soybean isoflavones solution, promptly obtain soybean isoflavones after drying;
6) with the whey solution of the resin absorption of deviating from the soybean isoflavones composition in the step 5), through the selective adsorbing resin column of Soyasaponin is adsorbed, make Soyasaponin from solution, be adsorbed onto on the resin column, with 70-80 ℃ hot water the Soyasaponin adsorption column is inhaled again and taken off, obtain Soyasaponin solution, after super-dry, obtain the finished product Soyasaponin then;
7) process in the step 6) is deviate from Soyasaponin through the whey solution of adsorption column, add in the hydrochloric acid and after, transfer to PH for neutral, then by anionite-exchange resin and Zeo-karb, obtain soybean oligosaccharide solution, after soybean oligosaccharide solution concentration drying, obtain soybean oligosaccharide.
The present invention's beneficial effect compared with prior art is:
1) this technology utilization embrane method is produced soybean protein isolate and protein peptide, replace traditional alkali pickling to sink method, the soybean protein isolate protein quality height that obtains, the nitrogen soluble index height, oil absorbency, emulsifying property, the gelation of product all are better than the heavy method products obtained therefrom of alkali pickling simultaneously.
2) this technology has sepn process and does not have characteristics such as phase transformation, energy consumption are low, easy to operate, safe and reliable, good separating effect, environmentally safe.
3) behind sterilization process, homogenize, emulsifying property, water-absorbent, the oil absorbency of soybean protein isolate and protein peptide is improved.
4) adjust different types of proteolytic enzyme and ultra-filtration membrane, can produce different types of soybean protein peptide with difference in functionality characteristic.
5) this technology in a production line production, has been simplified production technique with soybean isoflavones, Soyasaponin, soybean oligosaccharide, has reduced cost, has increased working efficiency, has effectively utilized raw material.
Embodiment
Membrane process for extracting soybean protein peptide and technique of deep processing byproduct thereof, this technology may further comprise the steps:
1) the low temperature soybean meal was through sig water lixiviate 10-20 hour, and the alkali lye solid-liquid ratio is weight percentage 1: 10-20, pH value is 7.5-9, utilize whizzer to isolate bean dregs after the immersion after, utilize the polysulfone membrane ultrafiltration, separating whey solution and protein solution;
2) protein solution is carried out temperature 105-115 ℃, the instantaneous sterilization of time 3-5 second, after the sterilization protein solution is homogenized;
3) protein solution behind the homogeneous is concentrated, spraying drying promptly obtains the finished product soybean protein isolate;
4) protein solution behind the homogeneous is added protease hydrolysis, hydrolysis 10 hours utilizes the polysulfone membrane ultrafiltration again after the hydrolysis, and permeate is concentrated, and drying promptly obtains soybean protein peptide;
5) utilize macroporous resin to adsorb the whey solution in the step 1), adsorb the soybean isoflavones composition in the whey solution, utilize 70% ethanolic soln that macroporous resin is carried out wash-out again, obtain soybean isoflavones solution, will promptly obtain soybean isoflavones after the solution drying;
6) with the whey solution of the resin absorption of deviating from the soybean isoflavones composition in the step 5), through the selective adsorbing resin column of Soyasaponin is adsorbed, make Soyasaponin from solution, be adsorbed onto on the resin column, with 70-80 ℃ hot water the Soyasaponin adsorption column is inhaled again and taken off, obtain Soyasaponin solution, after super-dry, obtain the finished product Soyasaponin then;
7) process in the step 6) is deviate from Soyasaponin through the whey solution of adsorption column, add in the hydrochloric acid and after, transfer to PH for neutral, then by anionite-exchange resin and Zeo-karb, obtain soybean oligosaccharide solution, after soybean oligosaccharide solution concentration drying, obtain soybean oligosaccharide.
Claims (1)
1, membrane process for extracting soybean protein peptide and technique of deep processing byproduct thereof is characterized in that this technology may further comprise the steps:
1) the low temperature soybean meal was through sig water lixiviate 10-20 hour, and the alkali lye solid-liquid ratio is weight percentage 1: 10-20, pH value is 7.5-9, utilize whizzer to isolate bean dregs after the immersion after, utilize the polysulfone membrane ultrafiltration, separating whey solution and protein solution;
2) protein solution is carried out temperature 105-115 ℃, the instantaneous sterilization of time 3-5 second, after the sterilization protein solution is homogenized;
3) protein solution behind the homogeneous is concentrated, spraying drying promptly obtains the finished product soybean protein isolate;
4) protein solution behind the homogeneous is added protease hydrolysis, hydrolysis 10 hours utilizes the polysulfone membrane ultrafiltration again after the hydrolysis, and permeate is concentrated, and drying promptly obtains soybean protein peptide;
5) utilize macroporous resin to adsorb the whey solution in the step 1), adsorb the soybean isoflavones composition in the whey solution, utilize 70% ethanolic soln that macroporous resin is carried out wash-out again, obtain soybean isoflavones solution, will promptly obtain soybean isoflavones after the solution drying;
6) with the whey solution of the resin absorption of deviating from the soybean isoflavones composition in the step 5), through the selective adsorbing resin column of Soyasaponin is adsorbed, make Soyasaponin from solution, be adsorbed onto on the resin column, with 70-80 ℃ hot water the Soyasaponin adsorption column is inhaled again and taken off, obtain Soyasaponin solution, after super-dry, obtain the finished product Soyasaponin then;
7) process in the step 6) is deviate from Soyasaponin through the whey solution of adsorption column, add in the hydrochloric acid and after, transfer to PH for neutral, then by anionite-exchange resin and Zeo-karb, obtain soybean oligosaccharide solution, after soybean oligosaccharide solution concentration drying, obtain soybean oligosaccharide.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200510046351 CN1291999C (en) | 2005-04-30 | 2005-04-30 | Membrane process for extracting soybean protein peptide and technique of deep processing byproduct |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200510046351 CN1291999C (en) | 2005-04-30 | 2005-04-30 | Membrane process for extracting soybean protein peptide and technique of deep processing byproduct |
Publications (2)
Publication Number | Publication Date |
---|---|
CN1687123A true CN1687123A (en) | 2005-10-26 |
CN1291999C CN1291999C (en) | 2006-12-27 |
Family
ID=35305165
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 200510046351 Expired - Fee Related CN1291999C (en) | 2005-04-30 | 2005-04-30 | Membrane process for extracting soybean protein peptide and technique of deep processing byproduct |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN1291999C (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103202340A (en) * | 2013-02-21 | 2013-07-17 | 南昌市草珊瑚科技产业有限公司 | A3 subunit protein polypeptide nutritional emulsifier and preparation method thereof |
CN106615684A (en) * | 2016-09-27 | 2017-05-10 | 肖进新 | Method for preparing protein hydrolyzate by using castor-seed cakes |
CN112694515A (en) * | 2021-01-20 | 2021-04-23 | 佳木斯冬梅大豆食品有限公司 | Deep processing method for extracting soybean protein peptide by membrane method |
CN112724194A (en) * | 2021-01-18 | 2021-04-30 | 荣海生物科技有限公司 | Method for extracting peptide from protein hydrolysis by-product |
-
2005
- 2005-04-30 CN CN 200510046351 patent/CN1291999C/en not_active Expired - Fee Related
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103202340A (en) * | 2013-02-21 | 2013-07-17 | 南昌市草珊瑚科技产业有限公司 | A3 subunit protein polypeptide nutritional emulsifier and preparation method thereof |
CN103202340B (en) * | 2013-02-21 | 2015-08-05 | 南昌市草珊瑚科技产业有限公司 | A kind of A3 protein subunit polypeptide nutrition emulsifying agent and preparation method thereof |
CN106615684A (en) * | 2016-09-27 | 2017-05-10 | 肖进新 | Method for preparing protein hydrolyzate by using castor-seed cakes |
CN112724194A (en) * | 2021-01-18 | 2021-04-30 | 荣海生物科技有限公司 | Method for extracting peptide from protein hydrolysis by-product |
CN112694515A (en) * | 2021-01-20 | 2021-04-23 | 佳木斯冬梅大豆食品有限公司 | Deep processing method for extracting soybean protein peptide by membrane method |
Also Published As
Publication number | Publication date |
---|---|
CN1291999C (en) | 2006-12-27 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN108085356B (en) | Method for industrially producing high-purity walnut peptide by taking low-temperature squeezed walnut meal as raw material | |
CN101967437B (en) | Method for producing small peptide beverages by fermenting yellow serofluid produced by processing beancurd | |
CN105476030A (en) | Multi-functional composite oligopeptide nutrition powder | |
CN106720926B (en) | A kind of gadus row's delicate flavour peptide and preparation method thereof | |
CN100548150C (en) | The preparation method of coconut extractive | |
CN102154400A (en) | Method for preparing dietary fiber from bean dregs serving as raw material by combining steam explosion and enzymolysis | |
CN102994598B (en) | Weak bitter corn oligopeptide with high content of alanine and leucine, and preparation method thereof | |
CN1291999C (en) | Membrane process for extracting soybean protein peptide and technique of deep processing byproduct | |
CN103805665A (en) | Preparation method of deep-sea fishskin collagen polypeptide | |
CN103265614A (en) | Method for extracting soy protein, oligosaccharide and isoflavone from soybean wastewater by one-step process | |
CN1765921A (en) | Separated soybean protein preparation process and prepared soybean small peptide and process | |
CN101455398A (en) | Soya-dregs water soluble diet fiber preparation method using nano filtration and spray-drying method | |
CN101032312A (en) | Reagent of improving quality of tofu pieces and producing method of tofu pieces | |
CN101869169B (en) | Method for preparing fish oligopeptide from gurry by combining fermentation and membrane technology | |
CN102204620A (en) | Method for preparing bitterless protein peptides | |
CN102618607B (en) | Preparation method for sunflower seed oligopeptide with high F value | |
CN101390564A (en) | Production method of corn separation protein | |
CN103525953B (en) | Method for preparing fructo-oligose through acidolysis | |
CN101564142A (en) | Oyster juice manufacturing method | |
CN101240311B (en) | Method for producing soybean polypeptide albumen powder by biological fermentation | |
CN107385002A (en) | A kind of co-production technology of chick-pea starch and chick-pea soluble protein | |
CN102558377A (en) | Preparation method of soybean polysaccharide gum | |
CN1509625A (en) | Enzymolysized modified vegetable protein | |
CN109486884A (en) | A kind of preparation method of soybean minor peptides | |
CN101619334B (en) | Method for co-producing high-purity rice protein and malt syrup by rice |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C17 | Cessation of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20061227 Termination date: 20110430 |