CN111088199B - Streptomyces fuselaphus and application thereof in production of proteolytic enzyme - Google Patents

Streptomyces fuselaphus and application thereof in production of proteolytic enzyme Download PDF

Info

Publication number
CN111088199B
CN111088199B CN202010095218.5A CN202010095218A CN111088199B CN 111088199 B CN111088199 B CN 111088199B CN 202010095218 A CN202010095218 A CN 202010095218A CN 111088199 B CN111088199 B CN 111088199B
Authority
CN
China
Prior art keywords
fermentation
streptomyces
proteolytic enzyme
protein
enzymolysis
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.)
Active
Application number
CN202010095218.5A
Other languages
Chinese (zh)
Other versions
CN111088199A (en
Inventor
吴敬
颜正飞
秦琴
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Jiangnan University
Original Assignee
Jiangnan University
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Jiangnan University filed Critical Jiangnan University
Priority to CN202010095218.5A priority Critical patent/CN111088199B/en
Publication of CN111088199A publication Critical patent/CN111088199A/en
Application granted granted Critical
Publication of CN111088199B publication Critical patent/CN111088199B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12RINDEXING SCHEME ASSOCIATED WITH SUBCLASSES C12C - C12Q, RELATING TO MICROORGANISMS
    • C12R2001/00Microorganisms ; Processes using microorganisms
    • C12R2001/01Bacteria or Actinomycetales ; using bacteria or Actinomycetales
    • C12R2001/465Streptomyces
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12NMICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N1/00Microorganisms, e.g. protozoa; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
    • C12N1/20Bacteria; Culture media therefor
    • C12N1/205Bacterial isolates
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12NMICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N9/00Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
    • C12N9/14Hydrolases (3)
    • C12N9/48Hydrolases (3) acting on peptide bonds (3.4)
    • C12N9/50Proteinases, e.g. Endopeptidases (3.4.21-3.4.25)
    • C12N9/52Proteinases, e.g. Endopeptidases (3.4.21-3.4.25) derived from bacteria or Archaea
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P21/00Preparation of peptides or proteins
    • C12P21/06Preparation of peptides or proteins produced by the hydrolysis of a peptide bond, e.g. hydrolysate products

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Wood Science & Technology (AREA)
  • Zoology (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Genetics & Genomics (AREA)
  • General Engineering & Computer Science (AREA)
  • Microbiology (AREA)
  • Biotechnology (AREA)
  • General Health & Medical Sciences (AREA)
  • Biochemistry (AREA)
  • Medicinal Chemistry (AREA)
  • Molecular Biology (AREA)
  • Biomedical Technology (AREA)
  • Tropical Medicine & Parasitology (AREA)
  • Virology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)
  • Enzymes And Modification Thereof (AREA)

Abstract

The invention discloses streptomyces glaucescens and application thereof in production of proteolytic enzyme, and belongs to the technical field of microorganisms and fermentation. The invention screens out a streptomyces darkling T20, the streptomyces darkling T20 can efficiently degrade protein, the streptomyces darkling T20 is coated on a solid culture medium containing 1g/L rice protein to be cultured for 48h, and the diameter of a transparent ring of the solid culture medium can reach 25 mm. The invention screens out a streptomyces darkling T20, the streptomyces darkling T20 can produce a proteolytic enzyme with a high-yield amino acid sequence shown as SEQ ID NO.2, and the streptomyces darkling T20 is inoculated into a fermentation culture medium for fermentation for 48 hours, so that the enzyme activity of the proteolytic enzyme in a fermentation supernatant can reach 1500U/mL.

Description

Streptomyces fuselaphus and application thereof in production of proteolytic enzyme
Technical Field
The invention relates to streptomyces cinerea and application thereof in production of proteolytic enzyme, and belongs to the technical field of microorganisms and fermentation.
Background
Compared with proteins such as soybean protein, whey protein and the like, the rice protein is recognized as high-quality protein, has low content of nutrition inhibiting factors, has no anaphylactic reaction, contains amino acids required by a human body, has reasonable amino acid proportion, has far-reaching biological value, is comparable with the biological value of shrimps, beef and the like, and accords with an ideal mode recommended by the World Health Organization (WHO). After the rice protein is hydrolyzed into short peptide, the short peptide nutrient solution with higher nutrient value can be prepared, and the short peptide nutrient solution can be used as a high-value additive in the industries of health care products, beverages, cosmetics and the like.
Among rice peptides, small-molecule peptides having a molecular weight of less than 1000Da, which are collectively called "small-molecule peptides", can be rapidly absorbed by The small intestine of a human body, not only do not cause side effects such as overnutrition, but also some specific small-molecule peptides have unique physiological functions such as antioxidant ability (specifically, see references: Yan et al, Food Chemistry,2015,179: 290) improving piglet intestinal flora (specifically, see references: Yanya Entensing, Nanchang university [ M ],2018), Angiotensin Converting Enzyme (ACE) inhibitory activity (specifically, see references: Wang et al, LWT-Food Sci Technology,2017,75:93-99), and anticancer activity (specifically, see references: Kannan et al, The Open biological sources Journal,2009,2:17-20), etc., and are key indicators of The quality of rice peptides, the market competitiveness of the rice peptide product can be greatly improved by increasing the content of the small molecular peptide.
At present, the preparation method of the small molecular peptide mainly comprises an enzymolysis method, a microbial fermentation method, an acid-base hydrolysis method, a chemical synthesis method and the like, wherein the enzymolysis method is an industrially feasible method with high safety and environmental protection. However, the conventional enzymatic hydrolysis method still has many defects, for example, the preparation method described in the patent publication No. CN1102229643A can make the content of small molecule peptides in the obtained rice peptide product reach about 50%, but it needs to use multiple enzyme preparations for synergistic enzymatic hydrolysis in the preparation process, and it needs to use a hollow fiber membrane, which greatly prolongs the production period of the rice peptide product and increases the industrial production cost of the rice peptide product; patent No. CN103440949A firstly adopts the steps of crushing, size mixing, washing, size mixing, reacting, concentrating, dehydrating and the like to pretreat the rice dregs, and then adopts a plurality of proteolytic enzymes to cooperatively treat the pretreated rice dregs, however, the method mainly adopts the pretreatment mode to improve the content of the small molecular peptides in the rice peptide products, the content of the small molecular peptides in the rice peptide products does not change obviously before and after the enzymolysis process, and the method has the disadvantages of complicated preparation steps, large energy consumption, large enzyme adding amount and is not beneficial to the industrialization process.
Therefore, there is an urgent need to find a method for preparing rice peptide with simple preparation process, short preparation period, low cost and high content of small molecule peptide in the prepared rice peptide to overcome the above-mentioned disadvantages.
Disclosure of Invention
[ problem ] to
The technical problem to be solved by the invention is to provide the method for preparing the rice peptide, which has the advantages of simple preparation process, short preparation period, low cost and high content of the small molecular peptide in the prepared rice peptide.
[ solution ]
In order to solve the problems, the invention provides Streptomyces glaucous (Streptomyces canus) T20, wherein the Streptomyces glaucous (Streptomyces canus) T20 is preserved in China center for type culture collection in 11 months and 15 days in 2019, the preservation number is CCTCC NO: M2019936, and the preservation address is Wuhan, Wuhan university in China.
The Streptomyces griseus (Streptomyces canus) T20 is derived from soil samples in a flour mill plant area of a lake and coast area of Wuxi city, Jiangsu province, the strain is analyzed by sequencing, the 16SrDNA sequence of the strain is shown as SEQ ID NO.1, the sequence obtained by sequencing is compared with the nucleic acid sequence in Genbank, the similarity of the 16SrDNA sequence and the 16S rDNA sequence of the Streptomyces griseus (Streptomyces canus) DSM 40017 is up to 98.3 percent, the strain with high similarity is constructed into a phylogenetic tree (particularly shown in figure 1), and the result shows that the strain and the Streptomyces griseus (Streptomyces canus) cfcc 3169 belong to the same branch and are named as Streptomyces griseus (Streptomyces canus) T20.
The colony of the Streptomyces cinerea (Streptomyces canus) T20 on the LB solid culture medium is small, white, regular in edge, circular and 2-4 mm in diameter.
The growth temperature of the Streptomyces glaucescens (Streptomyces canus) T20 is 20-45 ℃, and the optimal growth temperature is 30 ℃.
The growth pH of the Streptomyces glaucescens (Streptomyces canus) T20 is 6.0-8.0, and the optimal growth pH is 7.0.
The Streptomyces glaucescens (Streptomyces canus) T20 can grow in a culture medium containing 5g/LNCl and has certain salt tolerance.
The invention also provides application of the Streptomyces nigrescens (Streptomyces canus) T20 in producing proteolytic enzyme.
The invention also provides a method for producing the proteolytic enzyme, which comprises the steps of inoculating the Streptomyces nigrolae (Streptomyces canus) T20 into a fermentation medium for fermentation to obtain fermentation liquor containing the proteolytic enzyme, and then extracting the fermentation liquor to obtain the proteolytic enzyme.
In one embodiment of the invention, the amino acid sequence of the proteolytic enzyme is shown in SEQ ID No. 2.
In one embodiment of the invention, the nucleotide sequence of the gene encoding the proteolytic enzyme is shown in SEQ ID No. 3.
In one embodiment of the invention, the components of the fermentation medium comprise rice protein powder, sodium dihydrogen phosphate, disodium hydrogen phosphate, magnesium sulfate and ferrous sulfate.
In one embodiment of the invention, the components of the fermentation medium comprise 2.5g/L rice protein powder, 0.1g/L sodium dihydrogen phosphate, 0.1g/L disodium hydrogen phosphate, 0.05g/L magnesium sulfate and 0.001g/L ferrous sulfate.
In one embodiment of the present invention, the fermentation temperature is 20 to 45 ℃, the rotation speed is 100 to 200rpm, and the pH is 6.0 to 8.0.
The invention also provides application of the Streptomyces nigrescens (Streptomyces canus) T20 in producing protein peptide.
The invention also provides a method for producing protein peptide, which comprises the steps of inoculating the Streptomyces nigrolae (Streptomyces canus) T20 into a fermentation culture medium for fermentation to obtain a fermentation liquor containing proteolytic enzyme, extracting the fermentation liquor to obtain proteolytic enzyme, adding the proteolytic enzyme into a reaction system containing protein for enzymolysis to obtain an enzymolysis liquid containing protein peptide, and finally extracting the enzymolysis liquid to obtain the protein peptide;
or, the method comprises the steps of inoculating the Streptomyces nigrescens (Streptomyces canus) T20 into a fermentation medium for fermentation to obtain a fermentation liquid containing proteolytic enzyme, then adding the fermentation liquid into a reaction system containing protein for enzymolysis to obtain an enzymolysis liquid containing protein peptide, and finally extracting the enzymolysis liquid to obtain the protein peptide;
or, the method comprises the steps of inoculating the Streptomyces nigrospermi (Streptomyces canus) T20 into a fermentation culture medium for fermentation to obtain a fermentation liquid containing proteolytic enzyme, centrifuging the fermentation liquid to obtain a supernatant to obtain a fermentation supernatant, adding the fermentation supernatant into a reaction system containing protein for enzymolysis to obtain an enzymolysis liquid containing protein peptide, and finally extracting the enzymolysis liquid to obtain the protein peptide.
In one embodiment of the invention, the amino acid sequence of the proteolytic enzyme is shown in SEQ ID No. 2.
In one embodiment of the invention, the nucleotide sequence of the gene encoding the proteolytic enzyme is shown in SEQ ID No. 3.
In one embodiment of the invention, the components of the fermentation medium comprise rice protein powder, sodium dihydrogen phosphate, disodium hydrogen phosphate, magnesium sulfate and ferrous sulfate.
In one embodiment of the invention, the components of the fermentation medium comprise 2.5g/L rice protein powder, 0.1g/L sodium dihydrogen phosphate, 0.1g/L disodium hydrogen phosphate, 0.05g/L magnesium sulfate and 0.001g/L ferrous sulfate.
In one embodiment of the present invention, the fermentation temperature is 20 to 45 ℃, the rotation speed is 100 to 200rpm, and the pH is 6.0 to 8.0.
In one embodiment of the invention, the concentration of the protein in the reaction system is 5-50 g/L.
In one embodiment of the invention, the addition amount of the proteolytic enzyme, the fermentation liquid or the fermentation supernatant in the reaction system is 1000-3000U/gProtein
In one embodiment of the present invention, the temperature of the enzymolysis is 30 to 40 ℃, the rotation speed is 150 to 200rpm, and the pH is 7 to 8.
In one embodiment of the invention, the protein is rice protein; the protein peptide is rice peptide.
In one embodiment of the invention, the rice peptide is a small molecule rice peptide having a molecular weight of less than 1000 Da.
[ advantageous effects ]
(1) The invention screens out a Streptomyces nigrolae (Streptomyces canus) T20 which can efficiently degrade protein, and the Streptomyces nigrolae (Streptomyces canus) T20 is coated on a solid culture medium containing 1g/L rice protein to be cultured for 48h, so that the diameter of a transparent ring of the solid culture medium can reach 25 mm.
(2) The invention screens out a Streptomyces nigrolae (Streptomyces canus) T20, the Streptomyces nigrolae (Streptomyces canus) T20 can produce proteolytic enzyme with high-yield amino acid sequence as shown in SEQ ID NO.2, the Streptomyces nigrolae (Streptomyces canus) T20 is inoculated into a fermentation culture medium for fermentation for 48 hours, and the enzyme activity of the proteolytic enzyme in the fermentation supernatant can reach 1500U/mL.
(3) The invention provides a method for producing rice peptide, which greatly improves the content of small molecular peptide in the rice peptide by using fermentation supernatant obtained by fermenting Streptomyces griseus (Streptomyces canus) T20, and the fermentation supernatant obtained by fermenting the Streptomyces griseus (Streptomyces canus) T20 has the final enzyme activity of 2400U/gProteinThe additive amount of the small molecular peptides is added into rice protein dispersion liquid with the concentration of 10g/L of rice protein for enzymolysis, and the content of the small molecular peptides in enzymolysis supernatant can reach 70.3 percent only by enzymolysis for 2 hours.
(4) The invention provides a method for producing rice peptide, which only needs to add fermentation supernatant obtained by fermenting Streptomyces nigrescens (Streptomyces canus) T20 into rice protein dispersion liquid containing rice protein for enzymolysis, thus obtaining the rice peptide rich in small molecular peptide.
Biological material preservation
Streptomyces fuscous (Streptomyces canus) is classified and named as Streptomyces canus T20, is preserved in China Center for Type Culture Collection (CCTCC) at 11.15.2019, has a preservation number of M2019936, and has a preservation address of Wuhan university, Wuhan China.
Drawings
FIG. 1: phylogenetic tree of Streptomyces glaucescens (Streptomyces canus) T20.
FIG. 2: a colony of Streptomyces griseus (Streptomyces canus) T20.
Detailed Description
The invention is further illustrated with reference to specific examples.
The rice protein powder referred to in the following examples was purchased from Wuxi Jinnong Biotech limited, and other reagent materials were purchased from the national pharmaceutical group.
The media involved in the following examples are as follows:
enrichment culture medium: 1g/L of rice protein powder.
Separating a culture medium: 1g/L of rice protein powder, 3g/L of glucose and 15g/L of agar.
Fermentation medium: 2.5g/L rice protein powder, 0.1g/L sodium dihydrogen phosphate, 0.1g/L disodium hydrogen phosphate, 0.05g/L magnesium sulfate, 0.001g/L ferrous sulfate, and pH 7.0.
LB liquid medium: 10g/L of peptone and 5g/L, NaCl 10g/L of yeast extract.
LB solid medium: 10g/L of peptone, 5g/L, NaCl 10g/L of yeast extract and 15g/L of agar.
NaCl-tolerant medium: 0-10 g/L of NaCl, 10g/L of peptone and 5g/L of yeast extract.
The detection methods referred to in the following examples are as follows:
determination of proteolytic enzyme activity:
drawing a standard curve: weighing a certain amount of paranitroaniline, dissolving the paranitroaniline by using a small amount of absolute ethyl alcohol, and diluting the paranitroaniline by using a Tris-HCl buffer solution with the pH value of 8.0 until the final concentration is 40 mu g/mL; taking the diluted paranitroaniline solution as mother liquor, respectively taking 1000, 950, 900, 850, 800, 750, 700, 650, 600, 550, 500, 450, 400, 350, 300, 250, 200, 150, 100, 50 and 0 mu L of the mother liquor, supplementing the mother liquor to 1000mL by using Tris-HCl buffer solution with the concentration of 50mM and the pH value of 9.0, and preparing a series of standard solutions with concentration gradients (0.0, 2.0, 4.0, 6.0, 8.0, 10.0, 12.0, 14.0, 16.0, 18.0, 20.0, 22.0, 24.0, 26.0, 28.0, 30.0, 32.0, 34.0, 36.0, 38.0 and 40.0 mu g/mL); taking Tris-HCl buffer solution with the pH value of 8.0 as blank control, and measuring the absorbance of the standard solution at the wavelength of 405 nm; OD is determined by taking the concentration of paranitroaniline as the abscissa and the absorbance as the ordinate405A linear graph of the concentration relation of the enzyme activity and the paranitroaniline is an enzyme activity standard curve;
and (3) measuring enzyme activity: adding 600 μ L of Tris-HCl buffer solution with the concentration of 50mM and the pH value of 8.0 and 50 μ L of solution to be detected into a 1.5mL EP tube; preheating the mixed solution in a water bath at 60 ℃ for 5min, adding 50 mu L of Leu-pNA solution with the concentration of 100mM into the mixed solution, and continuing to react in the water bath at 60 ℃ for 10 min; after the reaction is finished, completely placing the EP tube in ice to terminate the reaction, and measuring the light absorption value of the reaction solution under the wavelength of 405nm by using an enzyme-labeling instrument; calculating the enzyme activity of the proteolytic enzyme in the enzyme solution to be detected according to the light absorption value;
wherein, the calculation formula of the enzyme activity is as follows:
enzyme activity (U/mL) ═ OD405×7×D/(K×10×0.5);
The definition of enzyme activity is: the amount of the enzyme required to release 1. mu. mol of p-nitroanilide (p-nitroanilide) per minute at a pH of 8.0 and a temperature of 60 ℃ was one unit of the enzyme activity (1U).
Determination of rice peptide molecular weight distribution:
taking rice peptide as a sample, adding distilled water to dissolve the rice peptide into a solution with the concentration of 5mg/mL, centrifuging at 12000rpm for 10min, and taking 200 mu L of supernatant to perform gel chromatography analysis; the chromatographic conditions were as follows: TSKgel G2000 SWXL(7.8 mm. times.30 cm, Tosoh); a diode array detector for detecting the wavelength of 220 nm; mobile phase: v (acetonitrile): v (water): v (trichloroacetic acid) ═ 10:90: 0.1; the column temperature is 30 ℃; sample introduction amount: 20 mu L of the solution; the flow rate is 0.8 mL/min; data analysis was performed using a V2.0 english spectral gel chromatography data workstation.
Example 1: primary screen of streptomyces glaucescens T20
The method comprises the following specific steps:
taking soil in a factory area of a flour mill from a shores and lakes area of Wuxi city in Jiangsu province as a sample, weighing 10g of the sample, adding the sample into 90mL of sterilized enrichment medium, and performing shake culture at 30 ℃ and 200rpm for 48 hours to obtain a culture solution; sucking 10mL of culture solution, adding the culture solution into a new 90mL of sterilized enrichment culture medium, performing shake culture at 30 ℃ and 200rpm for 48 hours, and repeating for 2 times to obtain an enrichment solution; diluting the enrichment solution with sterile water in a gradient manner to obtain a gradient dilution solution; respectively diluting 200 μ L to 10-3、10-4、10-5、10-6、10-7、10-8The gradient diluent is coated on a separation culture medium, cultured for 48 hours at the temperature of 30 ℃, and a single colony with a transparent ring is selected; selecting a single colony with a transparent ring, streaking the single colony on an LB solid culture medium, culturing the colony for 48 hours at the temperature of 30 ℃, and repeating the steps for many times until the single-form thallus can be observed under a microscope to obtain a purified single colony; the purified single colonyInoculating to separate culture medium, culturing at 30 deg.C for 48 hr, and selecting strain with larger transparent ring (diameter)>20mm) respectively named T16, T20, T37, T39, T40, T53 (see table 1 for transparent circle diameters of strains T16, T20, T37, T39, T40, T53).
TABLE 1 transparent circle diameter of strains T16, T20, T37, T39, T40, T53
Bacterial strains Diameter of transparent ring (mm)
T16 20
T20 25
T37 20
T39 22
T40 20
T53 21
Example 2: rescreening of streptomyces glaucescens T20
The method comprises the following specific steps:
the single colonies purified from the strains T16, T20, T37, T39, T40 and T53 obtained in example 1 were inoculated into LB liquid medium at 30 ℃ and 200rCulturing for 24 hours under pm shaking to obtain seed liquid; inoculating the seed solution into fermentation medium at an inoculum size of 5% (v/v), and shake-culturing at 30 deg.C and 200rpm for 48 hr to OD of the fermentation liquid6001.2; centrifuging the fermentation liquor at 12000rpm and 4 deg.C for 20min to obtain fermentation supernatant; dissolving rice protein powder in distilled water according to a feed-liquid ratio of 10:1(w/v, g/L) to obtain a dispersion liquid; adding the fermentation supernatant into the dispersion to make the final enzyme activity of the proteolytic enzyme in the dispersion 2400U/gProteinReacting in a constant-temperature water bath shaking table at 40 ℃ and 150rpm for 2h, boiling for 15min, and inactivating enzyme to obtain enzymatic hydrolysate; centrifuging the enzymolysis solution at 5000rpm for 20min to obtain enzymolysis supernatant.
The enzymatic activity of the proteolytic enzyme in the fermentation supernatant was measured (see table 2 for the results of the measurements).
The dispersion added with the fermentation supernatant after 20min of boiling water bath treatment is used as a blank control, and the molecular weight distribution of the rice peptide in the filtrate is detected by gel chromatography analysis after the enzymolysis supernatant is filtered by a 0.45 mu M filter membrane (the detection result is shown in table 3).
As can be seen from Table 2, the highest enzyme activity of the proteolytic enzyme in the fermentation supernatant obtained by the fermentation of the strain T20 was 1500U/mL. Sequencing the obtained proteolytic enzyme, and finding that the amino acid sequence is shown as SEQ ID No.2 and the nucleotide sequence is shown as SEQ ID No. 3.
As can be seen from Table 3, the content of small-molecule peptides in the supernatant obtained by enzymolysis of the fermentation supernatant obtained by fermentation with the strain T20 is the highest, and accounts for 70.3% of the total protein content.
TABLE 2 enzymatic Activity of proteolytic enzymes in fermentation supernatants obtained by fermentation of strains T16, T20, T37, T39, T40, T53
Bacterial strains Enzymatic Activity of proteolytic enzymes (U/mL)
T16 940
T20 1500
T37 906
T39 1230
T40 920
T53 1106
TABLE 3 ratio of small molecular peptide and polypeptide content in total protein content in the fermented supernatant obtained by fermentation with strains T16, T20, T37, T39, T40 and T53
Strain numbering Small peptide (< 1000Da,%) Polypeptides (> 1000Da,%)
Blank control 24.5 75.6
T16 41.2 56.2
T20 70.3 29.19
T37 30.6 67.3
T39 49.2 49.2
T40 51.6 47.1
T53 60.3 38.4
Example 3: identification and preservation of Streptomyces griseus T20
The method comprises the following specific steps:
the strain T20 obtained in example 2 was selected, the total DNA of the strain T20 was extracted, 16SrDNA amplification and sequencing were performed (completed by Wutin Tianlin biotechnology, Inc., the nucleotide sequence of 16S rDNA of the strain T20 is shown in SEQ ID NO. 1), the sequence obtained by sequencing was subjected to nucleic acid sequence alignment in Genbank, it was found that the similarity of the 16S rDNA sequence thereof with the 16S rDNA sequence of Streptomyces griseus (Streptomyces canus) DSM 40017 was as high as 98.3%, the strain with the high similarity thereof was constructed as a phylogenetic tree (see FIG. 1 in particular), and the result showed that the strain and Streptomyces griseus (Streptomyces canus) cfcc 3169 belong to the same branch and was named as Streptomyces griseus (Streptomyces griseus) T20.
Sending Streptomyces griseus (Streptomyces canus) T20 to the China center for preservation with the preservation date as follows: 11 and 15 days in 2019, the preservation number is CCTCC NO: M2019936, and the preservation address is Wuhan, Wuhan university, China.
Example 4: culture and Observation of Streptomyces griseus T20
The method comprises the following specific steps:
a loop of purified single colonies of Streptomyces griseus (Streptomyces canus) T20 obtained in example 1 was scraped and streaked on LB solid medium, and after 24 hours of cultivation at 30 ℃, colonies were observed, and were found to be small, white, with regular edges, circular, and 2-4 mm in diameter (see FIG. 2 for details).
A loop of the purified single colony of Streptomyces griseus (Streptomyces canus) T20 obtained in example 1 was scraped and inoculated into an LB liquid medium with a pH of 7.0, and cultured at a constant temperature of 10-50 ℃ for 48 hours, respectively, and the growth temperature was found to be 20-45 ℃ and the optimum temperature was 30 ℃.
A loop of the purified single colony of Streptomyces griseus (Streptomyces canus) T20 obtained in example 1 was scraped out, inoculated into LB liquid medium with pH of 3.0-10.0, and incubated at 30 ℃ for 48 hours, and the growth pH was found to be 6.0-8.0, with the optimum pH being 7.0.
A single colony of purified Streptomyces griseus (Streptomyces canus) T20 obtained in example 1 was scraped out, inoculated into NCl-tolerant cultures each containing 0 to 10g/L of NCl, and incubated at a constant temperature of 30 ℃ at pH7.0 for 48 hours, and it was found that it can grow in the NCl-tolerant culture containing 0 to 5g/L of NCl, and that it grew most vigorously in the NCl-tolerant culture containing 1g/L of NCl.
Although the present invention has been described with reference to the preferred embodiments, it should be understood that various changes and modifications can be made therein by those skilled in the art without departing from the spirit and scope of the invention as defined in the appended claims.
Sequence listing
<110> university of south of the Yangtze river
<120> Streptomyces glaucescens strain and application thereof in production of proteolytic enzyme
<160> 3
<170> PatentIn version 3.3
<210> 1
<211> 1402
<212> DNA
<213> Streptomyces griseus
<400> 1
attacacatg cagtcgaacg atgaaccact tcggtgggga ttagtggcga acgggtgagt 60
aacacgtggg caatctgccc ttcactctgg gacaagccct ggaaacgggg tctaataccg 120
gataccacta ccgcaggcat ctgtggtggt tgaaagctcc ggcggtgaag gatgagcccg 180
cggcctatca gcttgttggt gaggtaacgg ctcaccaagg cgacgacggg tagccggcct 240
gagagggcga ccggccacac tgggactgag acacggccca gactcctacg ggaggcagca 300
gtggggaata ttgcacaatg ggcgcaagcc tgatgcagcg acgccgcgtg agggatgacg 360
gccttcgggt tgtaaacctc tttcagcagg gaagaagcgc aagtgacggt acctgcagaa 420
gaagcgccgg ctaactacgt gccagcagcc gcggtaatac gtagggcgca agcgttgtcc 480
ggaattattg ggcgtaaaga gctcgtaggc ggcttgtcac gtcgggtgtg aaagcccggg 540
gcttaacccc gggtctgcat tcgatacggg ctagctagag tgtggtaggg gagatcggaa 600
ttcctggtgt agcggtgaaa tgcgcagata tcaggaggaa caccggtggc gaaggcggat 660
ctctgggcca ttactgacgc tgaggagcga aagcgtgggg agcgaacagg attagatacc 720
ctggtagtcc acgccgtaaa cggtgggaac taggtgttgg cgacattcca cgtcgtcggt 780
gccgcagcta acgcattaag ttccccgcct ggggagtacg gccgcaaggc taaaactcaa 840
aggaattgac gggggcccgc acaagcagcg gagcatgtgg cttaattcga cgcaacgcga 900
agaaccttac caaggcttga catacaccgg aaacaattag agataggtgc ccccttgtgg 960
tcggtgtaca ggtggtgcat ggctgtcgtc agctcgtgtc gtgagatgtt gggttaagtc 1020
ccgcaacgag cgcaaccctt gtcctgtgtt gccagcaact ctttcgggag gttggggact 1080
cacaggagac cgccggggtc aactcggagg aaggtgggga cgacgtcaag tcatcatgcc 1140
ccttatgtct tgggctgcac acgtgctaca atggcaggta caatgagctg cgaaaccgtg 1200
aggtggagcg aatctcaaaa agcctgtctc agttcggatt ggggtctgca actcgacccc 1260
atgaagtcgg agttgctagt aatcgcagat cagcattgct gcggtgaata cgttcccggg 1320
ccttgtacac accgcccgtc acgtcacgaa agtcggtaac acccgaagcc ggtggcccaa 1380
ccccttgtgg gagggagctt ag 1402
<210> 2
<211> 516
<212> PRT
<213> Streptomyces griseus
<400> 2
Met His Ala Cys Arg Ser Thr Ile Val Pro Leu Arg Leu Gly Ala Phe
1 5 10 15
Val His Arg Arg Leu Ile Ala Pro Gly Ala Leu Ala Ala Ala Ser Val
20 25 30
Leu Leu Ala Ile Pro Ala Ser Ala Ala Gly Tyr Ser Pro Gly Ala Pro
35 40 45
Gly Ile Gly Asp Pro Tyr Tyr Pro Ala Tyr Gly Asn Gly Gly Tyr Asp
50 55 60
Val Ser His Tyr Asp Leu Arg Leu Lys Tyr Gln Pro Ala Thr Asp Arg
65 70 75 80
Leu Glu Gly Thr Ala Thr Leu Leu Ala Arg Thr Thr Gln Asp Leu Ser
85 90 95
Arg Phe Asn Leu Asp Phe Leu Leu Asp Val Ser Glu Val Arg Val Asn
100 105 110
Gly Val Lys Ala Ala Phe Thr Ala Ser Gly Glu His Glu Leu Glu Ile
115 120 125
Thr Pro Lys Thr Pro Leu Ala Lys Gly Ala Ala Ala Thr Ile Val Val
130 135 140
Arg Tyr Ser Gly Val Pro Ser Ser Lys Gln Ala Tyr Gly Phe Thr Ser
145 150 155 160
Trp His Arg Thr Pro Asp Gly Gly Val Gly Ala Asn Glu Pro Glu Ala
165 170 175
Ala Trp Trp Trp Phe Pro Ser Asn Asp His Pro Leu Asp Lys Ala Thr
180 185 190
Tyr Asp Val Ser Val Leu Val Pro Asp Gly Ser Gln Ala Ile Ser Asn
195 200 205
Gly Thr Leu Gln Ser Thr Ser Ser Arg Ala Gly Trp Thr Arg Phe Asn
210 215 220
Trp Arg Ser Asn Lys Pro Gln Ala Thr Tyr Leu Ala Thr Leu Ala Val
225 230 235 240
Gly Lys Phe Asp Ile Thr Thr Gly Arg Thr Glu Ser Gly Ile Pro Val
245 250 255
Val Asn Ala Tyr Ser Lys Asp Leu Gly Asp Asn Ala Gly Ala Ala Arg
260 265 270
Ala Ser Ile Glu Arg Thr Gly Glu Ile Ala Asp Trp Leu Ser Glu Tyr
275 280 285
Tyr Gly Pro Tyr Pro Tyr Asn Ala Leu Gly Gly Tyr Val Pro Asn Thr
290 295 300
Asn Thr Gly Tyr Ala Leu Glu Thr Gln Thr Arg Pro Phe Tyr Ser Pro
305 310 315 320
Arg Gln Phe Ala Gly Gly Ser Asn Val Ser Val Val Val His Glu Leu
325 330 335
Ala His Gln Trp Tyr Gly Asp Leu Val Ser Val Ala Gly Trp Lys Asp
340 345 350
Ile Trp Ile Asn Glu Gly Phe Ala Arg Tyr Ala Gln Trp Leu Trp Ser
355 360 365
Glu His Glu Asn Glu Gly Thr Ala Gln Glu Ile Ala Asp Tyr Val Tyr
370 375 380
Ala Ser His Pro Ala Asp Asp Pro Phe Trp Thr Val Lys Pro Gly Asp
385 390 395 400
Pro Gly Pro Glu Asn Gln Phe His Leu Ala Val Tyr Asp Arg Gly Gly
405 410 415
Leu Ala Leu Gln Ala Leu Arg Asn Glu Ile Gly Asp Asp Asp Phe Phe
420 425 430
Ala Ile Leu Lys Gly Trp Pro Gln Lys Tyr Ala Tyr Gly Asn Ala Thr
435 440 445
Val Ala Asp Phe Glu Lys Tyr Ala Glu Glu Val Ser Gly Gln Ser Leu
450 455 460
Ser Ala Leu Phe Asp Thr Trp Leu Phe Gln Pro Ser Lys Pro Ala Ala
465 470 475 480
Pro Ala Ala Ala Asp Ala Ser Ile Ala Arg Ala Ala Ala Ala Gly Glu
485 490 495
Thr Pro Val Arg Pro Lys Ser Trp Lys Lys Ile Ala Ala Thr Asn Asp
500 505 510
Val His Glu Arg
515
<210> 3
<211> 1551
<212> DNA
<213> Streptomyces griseus
<400> 3
ttgcacgcct gccgttcgac gattgtgccc ctacgacttg gagctttcgt gcaccgcaga 60
ctcatcgcgc ccggcgcact ggccgccgcg tccgtcctgc tggcgatccc ggcatcggcc 120
gccggctact cccccggcgc gccgggcatc ggcgacccct actacccggc ctacggcaac 180
ggcggatacg acgtctccca ctacgacctg cggctgaagt accagccggc cacggaccgg 240
ctggagggca cggcgaccct tctggcccgc accacgcagg acctgtcgcg gttcaacctg 300
gacttcctgc tcgatgtcag cgaggtgcgg gtcaacggcg tgaaggcggc gttcaccgcc 360
tccggggagc acgagctgga gatcacgccg aagaccccgc tggcgaaggg cgccgccgcg 420
acgatcgtcg tgcggtacag cggggtgccc tcgtcgaagc aggcgtacgg cttcaccagc 480
tggcaccgca ccccggacgg cggggtcggc gcgaacgagc ccgaggcggc ctggtggtgg 540
ttcccgagca acgatcatcc gctcgacaag gccacctacg acgtgtccgt actggttccg 600
gacggctccc aggccatctc caacggcacg ctccagtcga cgagttcacg ggcgggctgg 660
acccggttca actggcgctc caacaagccg caggccacct atctggcgac gctggccgtc 720
gggaagttcg acatcacgac cgggaggacc gagagcggca ttccggtcgt caacgcctac 780
agcaaggacc tcggggacaa cgcgggggcc gcgcgggcga gcatcgagcg gacaggagag 840
atcgccgact ggctgagcga gtactacggg ccgtacccgt acaacgcgct cggcgggtac 900
gtgccgaaca ccaacaccgg gtacgcgctg gagacgcaga cccggccgtt ctacagcccg 960
cggcagttcg cgggcgggtc caatgtgtcc gtggtcgtgc acgagctggc ccaccagtgg 1020
tacggcgacc tcgtctccgt cgccgggtgg aaggacatct ggatcaacga ggggttcgcg 1080
cggtacgccc agtggctgtg gtccgagcac gagaacgagg gcacggccca ggagatcgcg 1140
gactacgtgt acgcctcgca cccggccgac gacccgttct ggacggtgaa gcccggtgac 1200
cccgggccgg agaaccagtt ccacctcgcc gtctacgacc ggggcgggct ggccctgcag 1260
gcgctgcgca acgagatcgg ggacgacgac ttcttcgcga tcctgaaggg ctggccgcag 1320
aagtacgcgt acgggaacgc gacggtcgcc gacttcgaga aatacgccga ggaggtgtcc 1380
gggcagtcgc tgtcggcgct cttcgacacc tggctgttcc agccgtcgaa gccggccgcc 1440
ccggcggcgg cggacgcgtc catcgcgcgg gcggcggccg ccggggagac gccggtgcgg 1500
ccgaagtcgt ggaagaagat cgccgcgacg aatgacgtgc acgagcgctg a 1551

Claims (10)

1. A Streptomyces glaucous (Streptomyces canus) T20 is characterized in that the Streptomyces glaucous T20 is preserved in China Center for Type Culture Collection (CCTCC) at 11 months and 15 days in 2019 with the preservation number of M2019936.
2. Use of the Streptomyces glaucous T20 according to claim 1 for the production of proteolytic enzymes.
3. A method for producing proteolytic enzyme, characterized in that, the method comprises the steps of inoculating the Streptomyces griseus T20 of claim 1 into a fermentation medium for fermentation to obtain a fermentation liquor containing proteolytic enzyme, and then extracting the fermentation liquor to obtain the proteolytic enzyme.
4. The method for producing a proteolytic enzyme according to claim 3, wherein the proteolytic enzyme has the amino acid sequence shown in SEQ ID No. 2.
5. The method for producing proteolytic enzyme according to claim 3 or 4, wherein the fermentation temperature is 20 to 45 ℃, the rotation speed is 100 to 200rpm, and the pH is 6.0 to 8.0.
6. Use of the Streptomyces glaucescens T20 according to claim 1 for the production of protein peptides.
7. A method for producing protein peptide, characterized in that, the method is to inoculate the Streptomyces griseus T20 of claim 1 into a fermentation medium for fermentation to obtain a fermentation broth containing proteolytic enzyme, then extract the fermentation broth to obtain proteolytic enzyme, then add the proteolytic enzyme into a reaction system containing protein for enzymolysis to obtain an enzymolysis solution containing protein peptide, and finally extract the enzymolysis solution to obtain protein peptide;
or, the method is that the streptomyces glaucescens T20 of claim 1 is inoculated in a fermentation medium for fermentation to obtain a fermentation liquid containing proteolytic enzyme, then the fermentation liquid is added into a reaction system containing protein for enzymolysis to obtain an enzymolysis liquid containing protein peptide, and finally the enzymolysis liquid is extracted to obtain the protein peptide;
or, the method is that the streptomyces glaucescens T20 of claim 1 is firstly inoculated in a fermentation culture medium for fermentation to obtain a fermentation liquid containing proteolytic enzyme, then the fermentation liquid is centrifuged to obtain supernatant fluid, fermentation supernatant fluid is obtained, then the fermentation supernatant fluid is added into a reaction system containing protein for enzymolysis to obtain enzymolysis liquid containing protein peptide, and finally the enzymolysis liquid is extracted to obtain the protein peptide.
8. The method for producing protein peptide according to claim 7, wherein the temperature of the enzymolysis is 30-40 ℃, the rotation speed is 150-200 rpm, and the pH is 7-8.
9. The method for producing a protein peptide according to claim 7 or 8, wherein the protein is rice protein; the protein peptide is rice peptide.
10. A method of producing protein peptides as claimed in claim 9, wherein the rice peptides have a molecular weight of less than 1000 Da.
CN202010095218.5A 2020-02-14 2020-02-14 Streptomyces fuselaphus and application thereof in production of proteolytic enzyme Active CN111088199B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202010095218.5A CN111088199B (en) 2020-02-14 2020-02-14 Streptomyces fuselaphus and application thereof in production of proteolytic enzyme

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202010095218.5A CN111088199B (en) 2020-02-14 2020-02-14 Streptomyces fuselaphus and application thereof in production of proteolytic enzyme

Publications (2)

Publication Number Publication Date
CN111088199A CN111088199A (en) 2020-05-01
CN111088199B true CN111088199B (en) 2021-10-19

Family

ID=70400106

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202010095218.5A Active CN111088199B (en) 2020-02-14 2020-02-14 Streptomyces fuselaphus and application thereof in production of proteolytic enzyme

Country Status (1)

Country Link
CN (1) CN111088199B (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111172138B (en) * 2020-02-14 2022-03-25 江南大学 Proteolytic enzyme and application thereof in production of protein peptide

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104498396A (en) * 2014-12-04 2015-04-08 江苏省血吸虫病防治研究所 Deep grey streptomyces caniferus for producing molluscicidal active substances and application thereof
CN106967639A (en) * 2017-04-06 2017-07-21 南京师范大学 A kind of dull gray streptomycete and its application in degrading nicotine insecticides
CN108192843A (en) * 2018-01-18 2018-06-22 湖南农业大学 A kind of azotobacter strain and its probiotics

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104498396A (en) * 2014-12-04 2015-04-08 江苏省血吸虫病防治研究所 Deep grey streptomyces caniferus for producing molluscicidal active substances and application thereof
CN106967639A (en) * 2017-04-06 2017-07-21 南京师范大学 A kind of dull gray streptomycete and its application in degrading nicotine insecticides
CN108192843A (en) * 2018-01-18 2018-06-22 湖南农业大学 A kind of azotobacter strain and its probiotics

Also Published As

Publication number Publication date
CN111088199A (en) 2020-05-01

Similar Documents

Publication Publication Date Title
CN103695341B (en) A kind of algin catenase secreted by marine bacteria and preparation method thereof
US20190185835A1 (en) Method for High-Yield Fermentation of Recombinant Proline Aminopeptidase and Preparation of Debittered Rice Peptide
CN104830712B (en) A kind of Serratia bacterial strain of the ketone group D gluconic acids of production of high purity 2
CN108277184A (en) Produce the bacillus and its preparation method and application of algin catenase
CN110218676A (en) A kind of clostridium butyricum and its application
CN106635920B (en) Marine alternans for high yield of fucosidase and application thereof
CN111088199B (en) Streptomyces fuselaphus and application thereof in production of proteolytic enzyme
CN110511897B (en) Serratia and application thereof in protease production
CN111909881B (en) Bacillus pumilus capable of producing feruloyl esterase and application thereof
CN108203729B (en) Preparation method of kelp antioxidant peptide
CN113337495A (en) Method for improving sialic acid yield and application
CN111004730A (en) Method for producing ergothioneine
CN103898012A (en) Thalassospira sp. strain and method for preparing agarase
CN111944782B (en) Feruloyl esterase and application thereof in production of ferulic acid
CN111172138B (en) Proteolytic enzyme and application thereof in production of protein peptide
CN102433290B (en) Strain for producing citrulline and method for biologically synthesizing citrulline with same
CN102433289B (en) Strain for producing citrulline and method for biologically synthesizing citrulline with same
CN112143681B (en) Bacillus belgii capable of producing feruloyl esterase and application thereof
CN112210523B (en) Recombinant bacillus subtilis for producing feruloyl esterase and application thereof
CN112094762B (en) Corynebacteria vinifera strain and application thereof
CN114574403A (en) Method for preparing thermophilic thermus strain fermentation product by utilizing rice bran enzyme hydrolysate
CN114540216A (en) Lactobacillus plantarum for degrading oleuropein and application thereof
CN112608871A (en) Method for producing probiotic active substances by high-density fermentation of bacillus thuringiensis
CN116515795B (en) Application of Aspergillus tubingensis in preparing phytase and/or degrading phytic acid
CN114686503B (en) Coli mutant strain for stabilizing high-yield alginic acid lyase

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant