CN102690322A - Method for decolorizing silkworm chrysalis protein enzymatic hydrolysis peptide - Google Patents
Method for decolorizing silkworm chrysalis protein enzymatic hydrolysis peptide Download PDFInfo
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- CN102690322A CN102690322A CN2012101840873A CN201210184087A CN102690322A CN 102690322 A CN102690322 A CN 102690322A CN 2012101840873 A CN2012101840873 A CN 2012101840873A CN 201210184087 A CN201210184087 A CN 201210184087A CN 102690322 A CN102690322 A CN 102690322A
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Abstract
The invention relates to a method for decolorizing silkworm chrysalis protein enzymatic hydrolysis peptide. The method comprises the following steps of: adjusting pH of a 1 percent silkworm chrysalis protein enzymatic hydrolysis peptide solution to be 8, adding 30g of powdery activated carbon and activated clay composite decolorizer in a ratio of 1:7 into each liter of the solution, placing in an oscillatory type water bath kettle at the temperature of 30 DEG C, adjusting the rotation speed to be 200r/min, decolorizing for 30 minutes, and centrifuging by using a disk centrifuge at the speed of 5,000 to 6,000r/min for 30 minutes, wherein the decolorization rate is 70.39 percent, the nitrogen retention rate is 91.14 percent, and the reducing power retention rate is 86.79 percent. The process is simple and easy to operate, the treatment process is mild, and the method can be widely applied to health food industry in which silkworm chrysalis polypeptide and other bioactive peptides are produced.
Description
Technical field
The present invention relates to a kind of decoloring method of pupa albumen enzymolysis anti-oxidation peptide.
Background technology
Anti-oxidation peptide is the focus of studying in recent years, discovers in vegetable-protein, animal proteinum and the microbial proteinous and can hydrolysis isolate biologically active peptidess such as blood pressure lowering peptide, immunomodulatory peptides, antibacterial peptide, OPIOIDS peptide and anti-oxidation peptide.Wherein anti-oxidation peptide can reach anti-oxidant function through reducing various radicals, inhibition lipid peroxidation and chelated metal ions in vivo.Existing research obtains anti-oxidation peptide from proteolysiss such as soybean, corn, peanut, fish-skins.
China is sericulture big country, produces 650000 tons of silk cocoons per year, accounts for 70% of the total cocoon amount in the world.As a sub product of putting down silk industry, silkworm chrysalis processing and utilization rate is extremely low, except that minority through oven dry is pulverized as nutritional additive, mostly much go out of use in addition as feed even fertilizer, cause the huge waste of resource.Pupa albumen content is high, the amino acid A wide selection of colours and designs, is a kind of good anti-oxidation peptide source.Yet the pupa albumen hydrolyzed solution has Vandyke brown, on color and luster, is difficult for being accepted by people as medicine or foodstuff additive, therefore must be to its processing of decolouring.At present research silkworm chrysalis enzymolyzing liquid or other bioactive peptide decoloring methods mainly adopt activated carbon method, dioxygen water law, organic solvent method, but problem such as these methods exist the loss of proteins rate high, and the bioactive peptide loss of activity is serious.
Summary of the invention
The object of the present invention is to provide a kind of decoloring method of pupa albumen enzymolysis anti-oxidation peptide.This method has improved percent of decolourization effectively, has kept nitrogen retention rate and reducing power retention rate simultaneously, can be widely used in the protective foods industry that silkworm chrysalis polypeptide and other bioactive peptides are produced.
For achieving the above object, following technical scheme is adopted in invention:
A kind of decoloring method of pupa albumen enzymolysis anti-oxidation peptide; The concrete steps that it is characterized in that this method are: the pH that regulates pupa albumen enzymolysis anti-oxidation peptide solution is: 7~9, add composite decoloring agent, and the mass volume ratio of this composite decoloring agent and pupa albumen enzymolysis anti-oxidation peptide is: 20~40g/L; In the oscillatory type water-bath; Adjust the temperature to 20~50 ℃, rotating speed to 150~250 r/min is behind decolouring 20~30 min; Spinning, gained supernatant are the pupa albumen enzymolysis anti-oxidation peptide of handling through decolouring.The pH of above-mentioned pupa albumen enzymolysis anti-oxidation peptide solution is 8.
Above-mentioned composite decoloring agent be Powdered Activated Carbon and atlapulgite be 1 by mass ratio: the mixture of (3~9).
Above-mentioned composite decoloring agent addition is 30 g/L of pupa albumen enzymolysis anti-oxidation peptide quality.
Above-mentioned bleaching temperature is 30 ℃.
Decoloring method technology of the present invention is simple, operation is prone to row, and treating processes is gentle, and percent of decolourization is 70.39%, and the nitrogen retention rate is 91.14%, and the reducing power retention rate is 86.79%.Can be widely used in the protective foods industry that silkworm chrysalis polypeptide and other bioactive peptides are produced.
Embodiment
To combine the embodiment form below
, foregoing of the present invention will be described further.
Embodiment one: the selection of discoloring agent
1% pupa albumen enzymolysis anti-oxidation peptide solution is regulated pH7, adds each 20 g/L of Powdered Activated Carbon and atlapulgite then respectively; Put into the oscillatory type water-bath, 30 ℃ of temperature are regulated rotating speed 200 r/min; Decolour behind 30 min centrifugal 30 min of disk centrifugal separator 5000-6000r/min.Get supernatant and survey its percent of decolourization, nitrogen retention rate, reducing power retention rate.Result such as table 1.
Can know that by table 1 Powdered Activated Carbon has good decolorizing effect, but in decolouring, also lose active polypeptide, and then influenced the anti-oxidant activity of supernatant.And atlapulgite has kept nitrogen content and reducing power ability preferably on the basis of certain decolorizing effect.
The decolorizing effect of table 1 Powdered Activated Carbon and atlapulgite
? | Powdered Activated Carbon | Atlapulgite |
Percent of decolourization (%) | 90.27 | 52.52 |
Nitrogen retention rate (%) | 14.20 | 94.86 |
Reducing power retention rate (%) | 12.95 | 91.58 |
Embodiment two: the proportioning of composite decoloring agent
1% pupa albumen enzymolysis anti-oxidation peptide solution; Transfer pH7, add the Powdered Activated Carbon and atlapulgite composite decoloring agent 20 g/L of different ratios respectively, put into the oscillatory type water-bath; 30 ℃ of temperature; Turn fast 200 r/min, behind 30 min that decolour, centrifugal 30 min of disk centrifugal separator 5000-6000 r/min.Get supernatant and survey its percent of decolourization, nitrogen retention rate, reducing power retention rate.Result such as table 2.
Can be known that by table 2 along with the minimizing of Powdered Activated Carbon ratio, the increase of atlapulgite ratio, percent of decolourization decreases, nitrogen retention rate and reducing power retention rate significantly improve.Powdered Activated Carbon: decolorizing effect was better when the atlapulgite ratio was 1:7, and still can keep nitrogen retention rate and reducing power retention rate preferably.
The decolorizing effect of the composite decoloring agent of the different proportionings of table 2
Embodiment three: the decolorization condition list factor of composite decoloring agent is optimized
1% pupa albumen enzymolysis anti-oxidation peptide solution; Transfer pH 5-9, add Powdered Activated Carbon and atlapulgite composite decoloring agent (1:7) 10-50 g/L, put into the oscillatory type water-bath; Temperature 20-100 ℃; Regulate rotating speed to 200 r/min, behind 30 min that decolour, use centrifugal 30 min of disk centrifugal separator 5000-6000 r/min.Get supernatant and survey its percent of decolourization, nitrogen retention rate, reducing power retention rate.The result is like table 3-5.
Can know that by table 3 along with pH increases, percent of decolourization reduces, but nitrogen retention rate and reducing power retention rate improve significantly.
Can know that by table 4 percent of decolourization, nitrogen retention rate and reducing power retention rate are along with the increase of temperature changes little.
Can know that by table 5 increase with addition, percent of decolourization improves, but nitrogen retention rate and reducing power retention rate reduce significantly.
Table 3 pH is to the influence of decolorizing effect
pH | 5 | 6 | 7 | 8 | 9 |
Percent of decolourization (%) | 73.69 | 70.10 | 68.78 | 62.33 | 57.55 |
Nitrogen retention rate (%) | 59.37 | 69.66 | 89.80 | 94.07 | 95.39 |
Reducing power retention rate (%) | 49.66 | 62.50 | 81.53 | 90.48 | 93.00 |
Annotate: 30 ℃ of temperature, discoloring agent adds concentration 20g/L
Table 4 temperature is to the influence of decolorizing effect
Temperature (℃) | 20 | 40 | 60 | 80 | 100 |
Percent of decolourization (%) | 68.89 | 69.87 | 65.69 | 67.11 | 70.39 |
Nitrogen retention rate (%) | 90.64 | 91.15 | 91.47 | 91.85 | 90.06 |
Reducing power retention rate (%) | 78.94 | 81.34 | 81.84 | 82.67 | 80.42 |
Annotate: pH7, discoloring agent adds concentration 20g/L
Table 5 composite decoloring agent addition is to the influence of decolorizing effect
Addition (g/L) | 10 | 20 | 30 | 40 | 50 |
Percent of decolourization (%) | 50.19 | 68.26 | 74.81 | 80.00 | 85.66 |
Nitrogen retention rate (%) | 98.19 | 90.14 | 86.15 | 83.20 | 76.52 |
Reducing power retention rate (%) | 96.15 | 80.26 | 75.40 | 70.90 | 62.81 |
Annotate: pH7,30 ℃ of temperature
Embodiment four: the decolorization condition orthogonal optimization of composite decoloring agent
Table 6 composite decoloring agent quadrature level of factor table
Factor | A(pH) | B (temperature/℃) | C (addition/g/L) |
1 | 7 | 30 | 20 |
2 | 8 | 40 | 30 |
3 | 9 | 50 | 40 |
Table 7 composite decoloring agent Orthogonal experiment results table
Drawn by table 7: the impact effect to percent of decolourization is C>A>B, percent of decolourization is best is combined as A1B1C3, i.e. pH7,30 ℃ of temperature, the composite decoloring agent addition is 40 g/L.Impact effect to the nitrogen retention rate is A>C>B, the nitrogen retention rate is best is combined as A3B2C1, i.e. pH9, temperature is 40 ℃, the composite decoloring agent addition is 20 g/L.Impact effect to the reducing power retention rate is A>C>B, the reducing power retention rate is best is combined as A3B1C1, i.e. pH9,30 ℃ of temperature, the composite decoloring agent addition is 20 g/L.
Take all factors into consideration; Retained nitrogen retention rate and reducing power retention rate preferably when improving percent of decolourization, decolorization condition is: pH8, temperature is 30 ℃; Composite decoloring agent (Powdered Activated Carbon: atlapulgite is 1:7) addition is 30 g/L; The percent of decolourization of this moment is 70.39%, and the nitrogen retention rate is 91.14%, and the reducing power retention rate is 86.79%.
Claims (5)
1. the decoloring method of a pupa albumen enzymolysis anti-oxidation peptide; The concrete steps that it is characterized in that this method are: the pH that regulates pupa albumen enzymolysis anti-oxidation peptide solution is: 7~9, add composite decoloring agent, and the mass volume ratio of this composite decoloring agent and pupa albumen enzymolysis anti-oxidation peptide is: 20~40g/L; In the oscillatory type water-bath; Adjust the temperature to 20~50 ℃, rotating speed to 150~250 r/min is behind decolouring 20~30 min; Spinning, gained supernatant are the pupa albumen enzymolysis anti-oxidation peptide of handling through decolouring.
2. the decoloring method of pupa albumen enzymolysis anti-oxidation peptide according to claim 1 is characterized in that the pH of described pupa albumen enzymolysis anti-oxidation peptide solution is 8.
3. the decoloring method of pupa albumen enzymolysis anti-oxidation peptide according to claim 1, it is characterized in that described composite decoloring agent be Powdered Activated Carbon and atlapulgite be 1 by mass ratio: the mixture of (3~9).
4. according to the decoloring method of claim 1 or 3 pupa albumen enzymolysis anti-oxidation peptides, it is characterized in that described composite decoloring agent addition is 30 g/L of pupa albumen enzymolysis anti-oxidation peptide quality.
5. according to the decoloring method of claim 1 pupa albumen enzymolysis anti-oxidation peptide, it is characterized in that described bleaching temperature is 30 ℃.
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Cited By (4)
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CN103468601A (en) * | 2013-06-27 | 2013-12-25 | 上海大学 | Method used for increasing cold stress resistance of lactococcus lactis |
CN103804466A (en) * | 2013-12-20 | 2014-05-21 | 广西大学 | Decolorizing method of silkworm chrysalis proteolysis antioxidative peptide |
CN108218958A (en) * | 2017-12-27 | 2018-06-29 | 浙江省农业科学院 | Polypeptide SVLGTGC with anti-oxidation function and application thereof |
CN110214755A (en) * | 2019-07-02 | 2019-09-10 | 上海大学 | A kind of cultural method of selenium-rich silkworm chrysalis |
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103468601A (en) * | 2013-06-27 | 2013-12-25 | 上海大学 | Method used for increasing cold stress resistance of lactococcus lactis |
CN103804466A (en) * | 2013-12-20 | 2014-05-21 | 广西大学 | Decolorizing method of silkworm chrysalis proteolysis antioxidative peptide |
CN108218958A (en) * | 2017-12-27 | 2018-06-29 | 浙江省农业科学院 | Polypeptide SVLGTGC with anti-oxidation function and application thereof |
CN108218958B (en) * | 2017-12-27 | 2020-04-17 | 浙江省农业科学院 | Polypeptide SVLGTGC with antioxidant function and application thereof |
CN110214755A (en) * | 2019-07-02 | 2019-09-10 | 上海大学 | A kind of cultural method of selenium-rich silkworm chrysalis |
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Application publication date: 20120926 |