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 PDF

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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
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China
Prior art keywords
solution
soybean
protein
soyasaponin
utilize
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CN 200510046351
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CN1291999C (en
Inventor
何宪超
何显军
郑贵仁
单广鑫
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HOUYING BIOLOGICAL ENGINEERING Co Ltd HAICHENG CITY
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HOUYING BIOLOGICAL ENGINEERING Co Ltd HAICHENG CITY
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Priority to CN 200510046351 priority Critical patent/CN1291999C/en
Publication of CN1687123A publication Critical patent/CN1687123A/en
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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

Membrane process for extracting soybean protein peptide and technique of deep processing byproduct thereof
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.
CN 200510046351 2005-04-30 2005-04-30 Membrane process for extracting soybean protein peptide and technique of deep processing byproduct Expired - Fee Related CN1291999C (en)

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

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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

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CN1687123A true CN1687123A (en) 2005-10-26
CN1291999C CN1291999C (en) 2006-12-27

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Cited By (4)

* Cited by examiner, † Cited by third party
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

Cited By (5)

* Cited by examiner, † Cited by third party
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

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Granted publication date: 20061227

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