Method for producing scleroglucan fermented liquid with Athena rosenbergii as bacterial species
A technology of Athena rosenbergii and scleroglucan, which is applied in the field of producing scleroglucan fermentation liquid, and can solve the problem of high impurity content in scleroglucan products, high impurities in scleroglucan fermentation liquid, and impurities in waste glucose mother liquor Many problems, to achieve the effect that is beneficial to the growth of bacteria, shorten the fermentation cycle, and facilitate the synthesis
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Embodiment 1
[0067] The present embodiment includes the following process steps:
[0068] The method for producing scleroglucan fermentation broth with Athelia roche as the strain is to inoculate the Athelia rolfsii CGMCC No.7760 (Athelia rolfsii) as the strain into a sterile sterile material containing carbon sources, necessary nitrogen sources and nutrients. In the nutrient solution, the pH of the nutrient solution is adjusted, and aeration and stirring fermentation is performed to obtain a scleroglucan fermentation broth; the aseptic nutrient solution is composed of the following raw materials:
[0069] Corn flakes sugar 80g / L; pea protein 3g / L; KH 2 PO 4 1.0g / L; MgSO 4 ·7H 2 O 0.3g / L; citric acid 1.3g / L; the balance is sterile water; pH=5.0-6.0.
[0070] Wherein the technological condition of each technological step in the production method is as follows:
[0071] The conditions for aeration and stirring fermentation are:
[0072] 0 hours-10 hours: ventilation volume 0.2vvm;
...
Embodiment 2
[0099] The difference between this embodiment and Embodiment 1 is:
[0100] In the present embodiment, the sterile culture liquid is made up of the following raw materials:
[0101] Corn flakes sugar 100g / L; pea protein 5g / L; KH 2 PO 4 2.5g / L; MgSO 4 ·7H 2 O 0.4g / L; citric acid 1.5g / L; the balance is sterile water; pH=5.0-6.0.
[0102] Wherein the technological condition of each technological step in the production method is as follows:
[0103] The conditions for aeration and stirring fermentation are:
[0104] 0 hours-10 hours: ventilation volume 0.3vvm;
[0105] 10 hours-20 hours: ventilation volume 0.5vvm;
[0106] 20 hours-30 hours: ventilation volume 1.0vvm;
[0107] 30 hours-40 hours: ventilation volume 0.7vvm;
[0108] 40 hours - end of fermentation: ventilation volume 0.3vvm;
[0109] During the fermentation, the temperature was 29° C., the pressure was 0.05 MPa, and the pH was 5.0-6.0; the stirring speed was 150 rpm, and the stirring was stopped for 2 hours ...
Embodiment 3
[0126] The difference between this embodiment and Embodiment 1 is:
[0127] In the present embodiment, the sterile culture liquid is made up of the following raw materials:
[0128] Corn flakes sugar 90g / L; pea protein 4g / L; KH 2 PO 4 2.0g / L; MgSO 4 ·7H 2 O 0.35g / L; citric acid 1.4g / L; the balance is sterile water; pH=5.0-6.0.
[0129] Wherein the technological condition of each technological step in the production method is as follows:
[0130] The conditions for aeration and stirring fermentation are:
[0131] 0 hours-10 hours: ventilation volume 0.25vvm;
[0132] 10 hours-20 hours: ventilation volume 0.45vvm;
[0133] 20 hours-30 hours: ventilation volume 0.9vvm;
[0134] 30 hours-40 hours: ventilation volume 0.65vvm;
[0135] 40 hours - end of fermentation: ventilation volume 0.25vvm;
[0136] During the fermentation, the temperature was 28° C., the pressure was 0.04 MPa, and the pH was 5.0-6.0; the stirring speed was 130 rpm, and the stirring was stopped for 2 ...
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