CN108048370B - Fermentation process of bacillus subtilis - Google Patents

Fermentation process of bacillus subtilis Download PDF

Info

Publication number
CN108048370B
CN108048370B CN201810080351.6A CN201810080351A CN108048370B CN 108048370 B CN108048370 B CN 108048370B CN 201810080351 A CN201810080351 A CN 201810080351A CN 108048370 B CN108048370 B CN 108048370B
Authority
CN
China
Prior art keywords
culture medium
bacillus subtilis
seeds
liquid culture
inoculating
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.)
Expired - Fee Related
Application number
CN201810080351.6A
Other languages
Chinese (zh)
Other versions
CN108048370A (en
Inventor
张伶燕
李卫军
于洪恩
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.)
Beijing Zkrz Agr Sci Techcl Co ltd
Original Assignee
Beijing Zkrz Agr Sci Techcl Co ltd
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 Beijing Zkrz Agr Sci Techcl Co ltd filed Critical Beijing Zkrz Agr Sci Techcl Co ltd
Priority to CN201810080351.6A priority Critical patent/CN108048370B/en
Publication of CN108048370A publication Critical patent/CN108048370A/en
Application granted granted Critical
Publication of CN108048370B publication Critical patent/CN108048370B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • 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
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23KFODDER
    • A23K10/00Animal feeding-stuffs
    • A23K10/10Animal feeding-stuffs obtained by microbiological or biochemical processes
    • A23K10/16Addition of microorganisms or extracts thereof, e.g. single-cell proteins, to feeding-stuff compositions
    • A23K10/18Addition of microorganisms or extracts thereof, e.g. single-cell proteins, to feeding-stuff compositions of live microorganisms

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Microbiology (AREA)
  • Health & Medical Sciences (AREA)
  • Biotechnology (AREA)
  • Zoology (AREA)
  • Polymers & Plastics (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Organic Chemistry (AREA)
  • Wood Science & Technology (AREA)
  • Biomedical Technology (AREA)
  • Biochemistry (AREA)
  • Genetics & Genomics (AREA)
  • Virology (AREA)
  • Tropical Medicine & Parasitology (AREA)
  • Molecular Biology (AREA)
  • Medicinal Chemistry (AREA)
  • Food Science & Technology (AREA)
  • Animal Husbandry (AREA)
  • General Engineering & Computer Science (AREA)
  • General Health & Medical Sciences (AREA)
  • Physiology (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)
  • Fodder In General (AREA)

Abstract

The invention relates to a fermentation process of bacillus subtilis, which belongs to the field of bacillus subtilis and aims to solve the problem of more mixed bacteria in the process of fermenting the bacillus subtilis, wherein the fermentation process of the bacillus subtilis comprises primary seed culture, secondary seed culture, tertiary seed culture and fermentation product generation, wherein the raw materials of a solid culture medium comprise straw, corn flour, bran, diethylaminoethyl cross-linked glucan gel, 1- (2- (β -D-glucopyranosyloxy) -4, 6-dihydroxyphenyl) -3- (4-hydroxyphenyl) -acetone and D-2,3,5, 6-tetrahydroxy-2-hexenoic acid-gamma-lactone.

Description

Fermentation process of bacillus subtilis
Technical Field
The invention relates to the field of bacillus subtilis, in particular to a fermentation process of bacillus subtilis.
Background
The utilization of the drug feed additive, especially the antibiotic feed additive, plays an important role in the aspects of preventing and treating diseases of animals, but simultaneously brings certain influence on the animal husbandry production and human beings, and the long-term use of the antibiotic can cause the problems of drug resistance, endogenous infection and the like of the animals, thereby causing the application of the antibiotic to be gradually limited.
The microbial feed additive is a live bacterial product containing beneficial microorganisms for animals, which is developed according to the micro-ecological theory, has multiple functions of promoting the growth and development of the animals and improving the immunity of the animal organisms by maintaining the ecological balance and volatilization of the microorganisms in the intestinal tracts of the animals, has no pollution, residue, drug resistance, no harm to the environment and the like, and is a novel green and environment-friendly feed additive. At present, the commonly used probiotic products for livestock and poultry comprise bacillus, lactobacillus, bifidobacterium and the like.
The bacillus has strong resistance to external adverse environment, can resist high temperature of over 60 ℃, has long storage time, is easy to culture, is convenient to process into various products, has stable effect and is widely used in animal husbandry. Various types of culture media for bacillus exist, and corn flour, bean cakes, bran and the like are prepared into solid culture media for fermentation on the basis of beef soup. However, in the process of fermentation on a solid medium, due to the complex components of the raw materials, the bacillus is easily infected by mixed bacteria through multi-stage culture and open fermentation, and the product quality is difficult to reach the standard.
Disclosure of Invention
The invention aims to provide a fermentation process of bacillus subtilis, which greatly reduces the pollution of mixed bacteria, and when the fermented bacillus subtilis is applied to poultry, the bacillus subtilis can greatly promote the growth of the poultry and is a feed additive with biological activity.
The above object of the present invention is achieved by the following technical solutions: a fermentation process of bacillus subtilis at least comprises the following steps:
s1, inoculating the bacillus subtilis into 20-30kg of liquid culture medium, adjusting the alkalinity of liquid culture amino acid to be neutral, and culturing for 12-18h under the aerobic condition at 28-36 ℃ to form first-grade seeds;
s2, inoculating the primary seeds into a liquid culture medium of 30-40kg, adjusting the alkalinity of the liquid culture amino acid to be neutral, and culturing for 24-32h under the aerobic condition at 28-36 ℃ to form secondary seeds;
s3, inoculating the secondary seeds into a liquid culture medium of 20-30kg for culture, culturing for 32-34h in a continuous fed-batch fermentation mode under the aerobic condition at 28-36 ℃, and standing for 12-16h at constant temperature after the culture is finished to form tertiary seeds;
s4, inoculating the third-level seeds to 68-81.6kg of solid culture medium, fermenting and culturing for 32-36h, and crushing to obtain a fermentation product of the bacillus subtilis;
wherein the solid culture medium comprises the raw materials of straws, corn flour, bran, diethylaminoethyl crosslinked glucan gel, 1- (2- (β -D-glucopyranosyloxy) -4, 6-dihydroxyphenyl) -3- (4-hydroxyphenyl) -acetone and D-2,3,5, 6-tetrahydroxy-2-hexenoic acid-gamma-lactone.
Preferably, in the solid culture medium, the mass ratio of the straw, the corn flour, the bran, the diethylaminoethyl cross-linked glucan gel mixture, the 1- (2- (β -D-glucopyranosyloxy) -4, 6-dihydroxyphenyl) -3- (4-hydroxyphenyl) -acetone and the D-2,3,5, 6-tetrahydroxy-2-hexenoic acid-gamma-lactone is 2:2:1:1:0.5: 0.3.
Preferably, in the solid fermentation step, diethylaminoethyl sephadex, 1- (2- (β -D-glucopyranosyloxy) -4, 6-dihydroxyphenyl) -3- (4-hydroxyphenyl) -acetone and D-2,3,5, 6-tetrahydroxy-2-hexenoic acid-gamma-lactone are uniformly mixed, then are added into water for soaking for 0.3 to 0.5h, then straws, corn flour and bran are added, and the solid culture medium is obtained after uniform stirring.
Preferably, the mass ratio of the diethylaminoethyl sephadex to the water is 1: 3.
Preferably, in step S1, the pH of the liquid medium is 7-8.
Preferably, in step S2, the pH of the liquid medium is 7-8.
Preferably, the liquid culture medium comprises 0.2 part of magnesium sulfate, 2 parts of ammonium sulfate, 1 part of sodium citrate, 6 parts of potassium dihydrogen phosphate, 4 parts of dipotassium hydrogen phosphate, 10 parts of peptone, 1 part of sodium chloride and 1 part of potassium dihydrogen phosphate.
Preferably, the liquid medium and the solid medium are sterilized before use.
In conclusion, the invention has the following beneficial effects:
1. the pollution of mixed bacteria in the fermentation product of the bacillus subtilis is greatly reduced, and the prepared fermentation product of the bacillus subtilis is a feed additive with biological activity.
2. According to the invention, during solid fermentation, 1- (2- (β -D-glucopyranosyloxy) -4, 6-dihydroxyphenyl) -3- (4-hydroxyphenyl) -acetone and D-2,3,5, 6-tetrahydroxy-2-hexenoic acid-gamma-lactone in a solid culture medium are firstly adsorbed in a macromolecular chain of diethylaminoethyl cross-linked glucan gel, during the process of culturing bacillus subtilis, 1- (2- (β -D-glucopyranosyloxy) -4, 6-dihydroxyphenyl) -3- (4-hydroxyphenyl) -acetone and D-2,3,5, 6-tetrahydroxy-2-hexenoic acid-gamma-lactone are oxidized, and the generated oxidation product has a bacteriostatic effect and effectively inhibits the generation of mixed bacteria, and the bacteriostatic effect is optimal by the matched use of 1- (2- (β -D-glucopyranosyloxy) -4, 6-dihydroxyphenyl) -3- (4-hydroxyphenyl) -acetone and D-2,3,5, 6-tetrahydroxy-2-hexenoic acid-gamma-lactone, so that the bacillus subtilis- (2- (β -D-hydroxyphenyloxy) -4, 6-tetrahydroxy-2-hexenoic acid-gamma-lactone and D-2,3,5, 6-tetrahydroxy-2-hexenoic acid-gamma-lactone are gradually released along with the culture of bacillus subtilis.
Detailed Description
All materials referred to in the examples of the present invention are commercially available.
First, the manufacturing embodiment
Example 1
S1, inoculating the bacillus subtilis into 25kg of liquid culture medium, adjusting the pH of the liquid culture medium to 7.5, and culturing for 15h under an aerobic condition at 32 ℃ to obtain first-stage seeds; wherein the liquid culture medium comprises 0.2 part of magnesium sulfate, 2 parts of ammonium sulfate, 1 part of sodium citrate, 6 parts of monopotassium phosphate, 4 parts of dipotassium phosphate, 10 parts of peptone, 1 part of sodium chloride and 1 part of monopotassium phosphate;
s2, inoculating the primary seeds into 35kg of liquid culture medium, adjusting the pH of the liquid culture medium to 7.5, and culturing for 28h under the aerobic condition of 32 ℃ to obtain secondary seeds;
s3, inoculating the secondary seeds into a liquid culture medium of 25kg for culture, culturing for 33h in a continuous fed-batch fermentation mode under the aerobic condition of 32 ℃, and standing for 14h at constant temperature after the culture is finished to form tertiary seeds;
s4, inoculating the third-level seeds to a solid culture medium, fermenting and culturing for 33h, and crushing to obtain a fermentation product of the bacillus subtilis;
the preparation method of the solid culture medium comprises the steps of firstly uniformly mixing 11kg of diethylaminoethyl cross-linked dextran gel, 5.5kg of 1- (2- (β -D-glucopyranosyloxy) -4, 6-dihydroxyphenyl) -3- (4-hydroxyphenyl) -acetone and 3.3kg of D-2,3,5, 6-tetrahydroxy-2-hexenoic acid-gamma-lactone, then adding 33kg of water for soaking for 0.4h, then adding 22kg of straw, 22kg of corn flour and 11kg of bran, and uniformly stirring to obtain the solid culture medium.
Example 2
S1, inoculating the bacillus subtilis into 20kg of liquid culture medium, adjusting the pH of the liquid culture medium to 7, and culturing for 18h under the aerobic condition of 28 ℃ to obtain primary seeds; wherein the liquid culture medium comprises 0.2 part of magnesium sulfate, 2 parts of ammonium sulfate, 1 part of sodium citrate, 6 parts of monopotassium phosphate, 4 parts of dipotassium phosphate, 10 parts of peptone, 1 part of sodium chloride and 1 part of monopotassium phosphate;
s2, inoculating the primary seeds into 40kg of liquid culture medium, adjusting the pH of the liquid culture medium to 7, and culturing for 32h under the aerobic condition of 32 ℃ to obtain secondary seeds;
s3, inoculating the secondary seeds into a liquid culture medium 20kg for culture, culturing for 32h in a continuous fed-batch fermentation mode under the aerobic condition at 28 ℃, and standing for 12h at constant temperature after the culture is finished to form tertiary seeds;
s4, inoculating the third-level seeds to a solid culture medium, fermenting and culturing for 36h, and crushing to obtain a fermentation product of the bacillus subtilis;
the preparation method of the solid culture medium comprises the steps of uniformly mixing 10kg of diethylaminoethyl cross-linked dextran gel, 5kg of 1- (2- (β -D-glucopyranosyloxy) -4, 6-dihydroxyphenyl) -3- (4-hydroxyphenyl) -acetone and 3kg of D-2,3,5, 6-tetrahydroxy-2-hexenoic acid-gamma-lactone, then adding 30kg of water for soaking for 0.3h, then adding 24kg of straws, 24kg of corn flour and 10kg of bran, and uniformly stirring to obtain the solid culture medium.
Example 3
S1, inoculating the bacillus subtilis into 30kg of liquid culture medium, adjusting the pH of the liquid culture medium to 7, and culturing for 18h under the aerobic condition of 28 ℃ to obtain first-level seeds; wherein the liquid culture medium comprises 0.2 part of magnesium sulfate, 2 parts of ammonium sulfate, 1 part of sodium citrate, 6 parts of monopotassium phosphate, 4 parts of dipotassium phosphate, 10 parts of peptone, 1 part of sodium chloride and 1 part of monopotassium phosphate;
s2, inoculating the primary seeds into 30kg of liquid culture medium, adjusting the pH of the liquid culture medium to 8, and culturing for 32h under the aerobic condition of 36 ℃ to obtain secondary seeds;
s3, inoculating the secondary seeds into a liquid culture medium 20kg for culture, adopting a continuous fed-batch fermentation mode for culture for 32h under an aerobic condition at 36 ℃, and standing for 12h at a constant temperature after the culture is finished to form tertiary seeds;
s4, inoculating the third-level seeds to a solid culture medium, fermenting and culturing for 36h, and crushing to obtain a fermentation product of the bacillus subtilis;
the preparation method of the solid culture medium comprises the steps of uniformly mixing 10kg of diethylaminoethyl cross-linked dextran gel, 6kg of 1- (2- (β -D-glucopyranosyloxy) -4, 6-dihydroxyphenyl) -3- (4-hydroxyphenyl) -acetone and 3kg of D-2,3,5, 6-tetrahydroxy-2-hexenoic acid-gamma-lactone, then adding 25kg of water to soak for 0.3h, then adding 24kg of straws, 20kg of corn flour and 12kg of bran, and uniformly stirring to obtain the solid culture medium.
Example 4
S1, inoculating the bacillus subtilis into 20kg of liquid culture medium, adjusting the pH of the liquid culture medium to 7, and culturing for 12h under the aerobic condition of 36 ℃ to obtain primary seeds; wherein the liquid culture medium comprises 0.2 part of magnesium sulfate, 2 parts of ammonium sulfate, 1 part of sodium citrate, 6 parts of monopotassium phosphate, 4 parts of dipotassium phosphate, 10 parts of peptone, 1 part of sodium chloride and 1 part of monopotassium phosphate;
s2, inoculating the primary seeds into 40kg of liquid culture medium, adjusting the pH of the liquid culture medium to 7.5, and culturing for 28h under the aerobic condition of 28 ℃ to obtain secondary seeds;
s3, inoculating the secondary seeds into a liquid culture medium 30kg for culture, adopting a continuous fed-batch fermentation mode for culture for 32h under an aerobic condition at 28 ℃, and standing for 16h at a constant temperature after the culture is finished to form tertiary seeds;
s4, inoculating the third-level seeds to a solid culture medium, fermenting and culturing for 32h, and crushing to obtain a fermentation product of the bacillus subtilis;
the preparation method of the solid culture medium comprises the steps of uniformly mixing 12kg of diethylaminoethyl cross-linked dextran gel, 5kg of 1- (2- (β -D-glucopyranosyloxy) -4, 6-dihydroxyphenyl) -3- (4-hydroxyphenyl) -acetone and 3kg of D-2,3,5, 6-tetrahydroxy-2-hexenoic acid-gamma-lactone, then adding 36kg of water to soak for 0.5h, then adding 20kg of straws, 24kg of corn flour and 11kg of bran, and uniformly stirring to obtain the solid culture medium.
Example 5
S1, inoculating the bacillus subtilis into 30kg of liquid culture medium, adjusting the pH of the liquid culture medium to 8, and culturing for 12h under the aerobic condition of 36 ℃ to obtain first-level seeds; wherein the liquid culture medium comprises 0.2 part of magnesium sulfate, 2 parts of ammonium sulfate, 1 part of sodium citrate, 6 parts of monopotassium phosphate, 4 parts of dipotassium phosphate, 10 parts of peptone, 1 part of sodium chloride and 1 part of monopotassium phosphate;
s2, inoculating the primary seeds into 30kg of liquid culture medium, adjusting the pH of the liquid culture medium to 7, and culturing for 28h under the aerobic condition of 32 ℃ to obtain secondary seeds;
s3, inoculating the secondary seeds into a liquid culture medium 30kg for culture, culturing for 34h in a continuous fed-batch fermentation mode under an aerobic condition at 36 ℃, and standing for 16h at a constant temperature after the culture is finished to form tertiary seeds;
s4, inoculating the third-level seeds to a solid culture medium, fermenting and culturing for 32h, and crushing to obtain a fermentation product of the bacillus subtilis;
the preparation method of the solid culture medium comprises the steps of firstly uniformly mixing 12kg of diethylaminoethyl cross-linked dextran gel, 6kg of 1- (2- (β -D-glucopyranosyloxy) -4, 6-dihydroxyphenyl) -3- (4-hydroxyphenyl) -acetone and 3.6kg of D-2,3,5, 6-tetrahydroxy-2-hexenoic acid-gamma-lactone, then adding 36kg of water for soaking for 0.5h, then adding 20kg of straws, 20kg of corn flour and 10kg of bran, and uniformly stirring to obtain the solid culture medium.
Example 6
S1, inoculating the bacillus subtilis into 20kg of liquid culture medium, adjusting the pH of the liquid culture medium to 8, and culturing for 12h under the aerobic condition of 28 ℃ to obtain primary seeds; wherein the liquid culture medium comprises 0.2 part of magnesium sulfate, 2 parts of ammonium sulfate, 1 part of sodium citrate, 6 parts of monopotassium phosphate, 4 parts of dipotassium phosphate, 10 parts of peptone, 1 part of sodium chloride and 1 part of monopotassium phosphate;
s2, inoculating the primary seeds into 40kg of liquid culture medium, adjusting the pH of the liquid culture medium to 8, and culturing for 24h under the aerobic condition of 36 ℃ to obtain secondary seeds;
s3, inoculating the secondary seeds into a liquid culture medium 30kg for culture, culturing for 34h in a continuous fed-batch fermentation mode under the aerobic condition at 28 ℃, and standing for 12h at constant temperature after the culture is finished to form tertiary seeds;
s4, inoculating the third-level seeds to a solid culture medium, fermenting and culturing for 32h, and crushing to obtain a fermentation product of the bacillus subtilis;
the preparation method of the solid culture medium comprises the steps of firstly uniformly mixing 12kg of diethylaminoethyl cross-linked dextran gel, 5kg of 1- (2- (β -D-glucopyranosyloxy) -4, 6-dihydroxyphenyl) -3- (4-hydroxyphenyl) -acetone and 3.6kg of D-2,3,5, 6-tetrahydroxy-2-hexenoic acid-gamma-lactone, then adding 36kg of water for soaking for 0.3h, then adding 20kg of straws, 24kg of corn flour and 12kg of bran, and uniformly stirring to obtain the solid culture medium.
Second, preparation of comparative example
Comparative example 1
S1, inoculating the bacillus subtilis into 25kg of liquid culture medium, adjusting the pH of the liquid culture medium to 7.5, and culturing for 15h under an aerobic condition at 32 ℃ to obtain first-stage seeds; wherein the liquid culture medium comprises 0.2 part of magnesium sulfate, 2 parts of ammonium sulfate, 1 part of sodium citrate, 6 parts of monopotassium phosphate, 4 parts of dipotassium phosphate, 10 parts of peptone, 1 part of sodium chloride and 1 part of monopotassium phosphate;
s2, inoculating the primary seeds into 35kg of liquid culture medium, adjusting the pH of the liquid culture medium to 7.5, and culturing for 28h under the aerobic condition of 32 ℃ to obtain secondary seeds;
s3, inoculating the secondary seeds into a liquid culture medium of 25kg for culture, culturing for 33h in a continuous fed-batch fermentation mode under the aerobic condition of 32 ℃, and standing for 14h at constant temperature after the culture is finished to form tertiary seeds;
s4, inoculating the third-level seeds to a solid culture medium, fermenting and culturing for 33h, and crushing to obtain a fermentation product of the bacillus subtilis;
the preparation method of the solid culture medium comprises the following steps: taking 22kg of straws, 22kg of corn flour and 11kg of bran, and uniformly stirring to obtain the solid culture medium.
Comparative example 2
S1, inoculating the bacillus subtilis into 25kg of liquid culture medium, adjusting the pH of the liquid culture medium to 7.5, and culturing for 15h under an aerobic condition at 32 ℃ to obtain first-stage seeds; wherein the liquid culture medium comprises 0.2 part of magnesium sulfate, 2 parts of ammonium sulfate, 1 part of sodium citrate, 6 parts of monopotassium phosphate, 4 parts of dipotassium phosphate, 10 parts of peptone, 1 part of sodium chloride and 1 part of monopotassium phosphate;
s2, inoculating the primary seeds into 35kg of liquid culture medium, adjusting the pH of the liquid culture medium to 7.5, and culturing for 28h under the aerobic condition of 32 ℃ to obtain secondary seeds;
s3, inoculating the secondary seeds into a liquid culture medium of 25kg for culture, culturing for 33h in a continuous fed-batch fermentation mode under the aerobic condition of 32 ℃, and standing for 14h at constant temperature after the culture is finished to form tertiary seeds;
s4, inoculating the third-level seeds to a solid culture medium, fermenting and culturing for 33h, and crushing to obtain a fermentation product of the bacillus subtilis;
the preparation method of the solid culture medium comprises the steps of uniformly mixing 11kg of diethylaminoethyl crosslinked glucan gel and 5.5kg of 1- (2- (β -D-glucopyranosyloxy) -4, 6-dihydroxyphenyl) -3- (4-hydroxyphenyl) -acetone, then adding 33kg of water, soaking for 0.4h, then adding 22kg of straws, 22kg of corn flour and 11kg of bran, and uniformly stirring to obtain the solid culture medium.
Comparative example 3
S1, inoculating the bacillus subtilis into 25kg of liquid culture medium, adjusting the pH of the liquid culture medium to 7.5, and culturing for 15h under an aerobic condition at 32 ℃ to obtain first-stage seeds; wherein the liquid culture medium comprises 0.2 part of magnesium sulfate, 2 parts of ammonium sulfate, 1 part of sodium citrate, 6 parts of monopotassium phosphate, 4 parts of dipotassium phosphate, 10 parts of peptone, 1 part of sodium chloride and 1 part of monopotassium phosphate;
s2, inoculating the primary seeds into 35kg of liquid culture medium, adjusting the pH of the liquid culture medium to 7.5, and culturing for 28h under the aerobic condition of 32 ℃ to obtain secondary seeds;
s3, inoculating the secondary seeds into a liquid culture medium of 25kg for culture, culturing for 33h in a continuous fed-batch fermentation mode under the aerobic condition of 32 ℃, and standing for 14h at constant temperature after the culture is finished to form tertiary seeds;
s4, inoculating the third-level seeds to a solid culture medium, fermenting and culturing for 33h, and crushing to obtain a fermentation product of the bacillus subtilis;
the preparation method of the solid culture medium comprises the following steps: firstly, uniformly mixing 11kg of diethylaminoethyl cross-linked dextran gel and 3.3kg of D-2,3,5, 6-tetrahydroxy-2-hexenoic acid-gamma-lactone, then adding 33kg of water to soak for 0.4h, then adding 22kg of straws, 22kg of corn flour and 11kg of bran, and uniformly stirring to obtain a solid culture medium.
The liquid medium and the solid medium used in each of the above examples and comparative examples were sterilized before use.
Third, testing the Performance results
Test subjects: 405 egg chicks were selected and randomly divided into 9 treatment groups, each group was assigned 3 replicates, each replicate 15 chicks, with a test period of 8 weeks. Of these, 9 treatment groups added 0.5% of the bacillus subtilis fermentation preparations prepared in examples 1 to 6 and comparative examples 1 to 3 to the basal diet, respectively. The feed is manually fed three times a day, and the water is freely drunk to ensure the cleanness and sanitation of water, materials, a groove and the house.
And (3) testing the production performance: and (3) respectively weighing on an empty stomach by taking the repetition as a unit at the beginning and the end of the test period, accurately recording the material consumption of each weight, and calculating the average daily gain, the material consumption and the feed weight gain ratio. The test results are shown in table 1.
TABLE 1 results of the performance tests of the examples and comparative examples of Bacillus subtilis
Daily consumption (g/only) Average daily gain (g/only) Feed/weight gain
Example 1 17.17 10.09 1.70
Example 2 16.73 9.65 1.73
Example 3 16.19 9.10 1.78
Example 4 16.94 9.87 1.72
Example 5 16.54 9.46 1.75
Example 6 16.70 9.62 1.74
Comparative example 1 15.68 7.37 2.13
Comparative example 2 16.45 8.34 1.97
Comparative example 3 16.63 8.51 1.96
As can be seen from the table, the number of mixed bacteria in the prepared bacillus subtilis fermentation product is greatly reduced, the product performance of the prepared bacillus subtilis fermentation product is greatly improved, the bacillus subtilis fermentation product has a good promotion effect on the growth of chicks, and the bacillus subtilis fermentation product is a feed additive with biological activity.
In comparative example 1, 1- (2- (β -D-glucopyranosyloxy) -4, 6-dihydroxyphenyl) -3- (4-hydroxyphenyl) -acetone, D-2,3,5, 6-tetrahydroxy-2-hexenoic acid-gamma-lactone and diethylaminoethyl cross-linked dextran gel are not added, and even if the solid culture medium is sterilized before use in the preparation process of the fermentation product of the bacillus subtilis, the amount of mixed bacteria is increased due to environment suitability in the culture process of the bacillus subtilis, so that the prepared fermentation product of the bacillus subtilis carries a large amount of mixed bacteria, and the product performance of the fermentation product of the bacillus subtilis is seriously influenced.
In comparative example 2 and comparative example 3, D-2,3,5, 6-tetrahydroxy-2-hexenoic acid-gamma-lactone and 1- (2- (β -D-glucopyranosyloxy) -4, 6-dihydroxyphenyl) -3- (4-hydroxyphenyl) -acetone are not added respectively, and the inhibition effect on mixed bacteria in the fermentation product of the bacillus subtilis is lower than that of the mixed bacteria in the fermentation product of the bacillus subtilis, so that the prepared fermentation product of the bacillus subtilis carries mixed bacteria and the product performance of the fermentation product of the bacillus subtilis is influenced.
The present embodiment is only for explaining the present invention, and it is not limited to the present invention, and those skilled in the art can make modifications of the present embodiment without inventive contribution as needed after reading the present specification, but all of them are protected by patent law within the scope of the claims of the present invention.

Claims (7)

1. A fermentation process of bacillus subtilis is characterized by at least comprising the following steps:
s1, inoculating the bacillus subtilis into 20-30kg of liquid culture medium, adjusting the alkalinity of liquid culture amino acid to be neutral, and culturing for 12-18h under the aerobic condition at 28-36 ℃ to form first-grade seeds; the liquid culture medium comprises 0.2 part of magnesium sulfate, 2 parts of ammonium sulfate, 1 part of sodium citrate, 6 parts of monopotassium phosphate, 4 parts of dipotassium phosphate, 10 parts of peptone, 1 part of sodium chloride and 1 part of monopotassium phosphate;
s2, inoculating the primary seeds into a liquid culture medium of 30-40kg, adjusting the alkalinity of the liquid culture amino acid to be neutral, and culturing for 24-32h under the aerobic condition at 28-36 ℃ to form secondary seeds;
s3, inoculating the secondary seeds into a liquid culture medium of 20-30kg for culture, culturing for 32-34h in a continuous fed-batch fermentation mode under the aerobic condition at 28-36 ℃, and standing for 12-16h at constant temperature after the culture is finished to form tertiary seeds;
s4, inoculating the third-level seeds to a solid culture medium of 68-81.6kg, fermenting and culturing for 32-36h, and crushing to obtain a fermentation product of the bacillus subtilis, wherein the solid culture medium comprises straw, corn flour, bran, diethylaminoethyl cross-linked dextran gel, 1- (2- (β -D-glucopyranosyloxy) -4, 6-dihydroxyphenyl) -3- (4-hydroxyphenyl) -acetone and D-2,3,5, 6-tetrahydroxy-2-hexenoic acid-gamma-lactone, and the addition ratio of the diethylaminoethyl cross-linked dextran gel, the 1- (2- (β -D-glucopyranosyloxy) -4, 6-dihydroxyphenyl) -3- (4-hydroxyphenyl) -acetone and the D-2,3,5, 6-tetrahydroxy-2-hexenoic acid-gamma-lactone is 10-12:5-6: 3-3.6.
2. The fermentation process of the bacillus subtilis according to claim 1, wherein in the solid culture medium, the mass ratio of straw, corn flour, bran, diethylaminoethyl sephadex mixture, 1- (2- (β -D-glucopyranosyloxy) -4, 6-dihydroxyphenyl) -3- (4-hydroxyphenyl) -acetone and D-2,3,5, 6-tetrahydroxy-2-hexenoic acid-gamma-lactone is 2:2:1:1:0.5: 0.3.
3. The fermentation process of bacillus subtilis according to claim 2, wherein in the step of solid fermentation, diethylaminoethyl cross-linked dextran gel, 1- (2- (β -D-glucopyranosyloxy) -4, 6-dihydroxyphenyl) -3- (4-hydroxyphenyl) -acetone and D-2,3,5, 6-tetrahydroxy-2-hexenoic acid-gamma-lactone are uniformly mixed, then added into water for soaking for 0.3-0.5h, then added with straw, corn flour and bran, and uniformly stirred to obtain the solid culture medium.
4. The fermentation process of bacillus subtilis according to claim 3, wherein the mass ratio of the diethylaminoethyl sephadex to the water is 1: 3.
5. The fermentation process of Bacillus subtilis according to claim 1, wherein the pH of the liquid culture medium in step S1 is 7-8.
6. The fermentation process of Bacillus subtilis according to claim 1, wherein the pH of the liquid culture medium in step S2 is 7-8.
7. The process of claim 1, wherein the liquid medium and the solid medium are sterilized before use.
CN201810080351.6A 2018-01-27 2018-01-27 Fermentation process of bacillus subtilis Expired - Fee Related CN108048370B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201810080351.6A CN108048370B (en) 2018-01-27 2018-01-27 Fermentation process of bacillus subtilis

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201810080351.6A CN108048370B (en) 2018-01-27 2018-01-27 Fermentation process of bacillus subtilis

Publications (2)

Publication Number Publication Date
CN108048370A CN108048370A (en) 2018-05-18
CN108048370B true CN108048370B (en) 2020-05-26

Family

ID=62124825

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201810080351.6A Expired - Fee Related CN108048370B (en) 2018-01-27 2018-01-27 Fermentation process of bacillus subtilis

Country Status (1)

Country Link
CN (1) CN108048370B (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111733119A (en) * 2020-08-25 2020-10-02 烟台水禾土生物科技有限公司 High-density fermentation method of bacillus subtilis

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102093939A (en) * 2010-11-29 2011-06-15 高思 Nutrition-enhanced health-care wine prepared from plant containing natural biological antioxidant
CN104480080A (en) * 2014-11-21 2015-04-01 西北农林科技大学 Recombinant apple phlorizin glycosyl transferase and separation and purification method thereof
CN105106888A (en) * 2015-09-08 2015-12-02 浙江泰康药业集团有限公司 Pharmaceutical composition capable of enhancing immunity and preparation method of pharmaceutical composition
CN106376725A (en) * 2016-08-25 2017-02-08 北京康缘益生生物科技有限公司 Biological fermented feed and preparation method thereof
CN106811424A (en) * 2015-11-27 2017-06-09 常宇菲 A kind of feed preparation method of high concentration bacillus subtilis biological agent
CN107041385A (en) * 2016-11-22 2017-08-15 吉林农业大学 A kind of bactericidal composition wettable powder, preparation method and its application in preventing and treating rice seedling blight

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102093939A (en) * 2010-11-29 2011-06-15 高思 Nutrition-enhanced health-care wine prepared from plant containing natural biological antioxidant
CN104480080A (en) * 2014-11-21 2015-04-01 西北农林科技大学 Recombinant apple phlorizin glycosyl transferase and separation and purification method thereof
CN105106888A (en) * 2015-09-08 2015-12-02 浙江泰康药业集团有限公司 Pharmaceutical composition capable of enhancing immunity and preparation method of pharmaceutical composition
CN106811424A (en) * 2015-11-27 2017-06-09 常宇菲 A kind of feed preparation method of high concentration bacillus subtilis biological agent
CN106376725A (en) * 2016-08-25 2017-02-08 北京康缘益生生物科技有限公司 Biological fermented feed and preparation method thereof
CN107041385A (en) * 2016-11-22 2017-08-15 吉林农业大学 A kind of bactericidal composition wettable powder, preparation method and its application in preventing and treating rice seedling blight

Also Published As

Publication number Publication date
CN108048370A (en) 2018-05-18

Similar Documents

Publication Publication Date Title
CN104017751B (en) Bacillus coagulans, Lactobacillus plantarum and Lactobacillus casei preparation and its preparation
CN107801837B (en) Biological fermentation process for forage-based utilization of chicken manure
CN111011627A (en) Feed additive capable of preventing diarrhea and preparation method thereof
CN113774003A (en) Lactobacillus buchneri and application thereof in preparation of low-moisture fermented feed
CN113215051A (en) Method for preparing feed probiotics by using lactobacillus through rice flour wastewater and passion fruit peel
CN105613945A (en) Fermented feed raw materials with low water content, preparation method thereof and application of fermented feed raw materials in feeds
CN106135699A (en) A kind of additive for microbe feedstuff
CN114276946B (en) Lactobacillus plantarum, microbial inoculum, feed and application of lactobacillus plantarum and microbial inoculum
KR101971241B1 (en) Feed additives improved heat resistane and method thereof
CN108048370B (en) Fermentation process of bacillus subtilis
CN106578354A (en) Piglet compound premix, preparation method and daily ration for piglet
CN116849292B (en) Fermented feed additive and preparation method and application thereof
CN113773996A (en) Preparation method and application of feeding bacillus subtilis
KR101476107B1 (en) EM fermented feed compound using fungus strain manufacturing method
CN109123221A (en) A kind of full nutrition aquaculture feed prepared using aquatic products processing leftover bits and pieces
KR20120122186A (en) Method of preparing probiotics of solid-state fermentation using korean rice wine cake for livestocks and the probiotics composition
CN103843974A (en) Compound microecologics and application thereof
CN106343201A (en) Pig feed additive for effectively increasing digestion rate of nitrogen and phosphorus
CN107772107A (en) A kind of plus microbe additive the special mixed fodder of growing and fattening pigs
CN113647518B (en) Special biological fermentation feed for fattening cattle in northern Jiang region and preparation method thereof
CN109170149A (en) A method of microecological fermented forage is produced using antibiotic milk
CN103621792A (en) Feed additive containing L-lysine composite probiotics and preparation method thereof
CN104543593A (en) Fish and shrimp attractant and preparation method thereof
CN111763638A (en) Veterinary microecological preparation and preparation method thereof
KR101101942B1 (en) Lactic acid bacteria microoganizm material using confectioneries, breads, noodle by-product

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
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20200526

Termination date: 20210127