Culture medium prescription for the industrial production of rhamnolipid fermentation liquor
A medium formulation and a rhamnolipid technology are applied in the field of medium formulations for industrial production of rhamnolipid fermentation broth, and can solve problems such as failure to form an industrialized production scale, low rhamnolipid content, and optimized medium formulations. , to achieve the effect of shortening the fermentation cycle, increasing the amount of rhamnolipid, and shortening the cycle
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[0009] Example 1. Production of Rhamnolipid Biological Fermentation Liquid by Industrialized Method:
[0010] Shake flask and fermenter culture: Pseudomonas sp.VTS-1 was cultured for 30h, then transferred to 5L shake flask (filled with 2L medium), the inoculum volume was 5% (the concentration of the bacterial solution was at OD 600 =0.8~1.0), the temperature is 32±2℃, 120rpm culture for 12h, the 500-liter first-stage fermenter connected to the connection, the charging factor is 75%, the inoculum amount is 5%, the temperature is 32±2℃, and the ventilation ratio is 1:1. The pH is 6.5~7.5, the stirring speed is 100rpm, and the culture is for 12h, then it is connected to a 3.5-ton secondary fermentation tank, the charging factor is 75%, the inoculation amount is 5%, the temperature is 32±2℃, and the ventilation ratio is 1. :1. The pH is 6.5~7.5, the stirring speed is 100rpm, the culture is 12h, and it is connected to a 30-ton tertiary fermentation tank with a filling volume of 20 tons...
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[0012] Example 2. Production of Rhamnolipid Biological Fermentation Broth by Industrialized Method:
[0013] Shake flask and fermenter culture: Pseudomonas sp.VTS-1 (Pseudomonas sp.VTS-1) cultured for 30h, transferred to 5L shake flask (filled with 2L medium), inoculation volume 5%, 32±2℃, 120rpm culture for 12h , Transfer to a 500-liter one-stage fermenter, with a charging factor of 65%, an inoculum of 5%, 32±2°C, a ventilation ratio of 1:1, a pH of 6.5-7.5, and a stirring speed of 100rpm. Connected to a 3.5-ton secondary fermentation tank with a charging factor of 65%, an inoculum of 5%, 32±2°C, a ventilation ratio of 1:1, a pH of 6.5 to 7.5, and a stirring speed of 100 to 150 rpm for 12 hours of cultivation, transfer Into a 30-ton tertiary fermentation tank with a filling volume of 20 tons. The process parameters of the tertiary fermentation tank are: temperature 32±2°C, pH adjusted to about 6 before sterilization, and 0.210 tons of NaOH to control the pH above 6 in the later s...
Example Embodiment
[0015] Example 3. Industrialized method to produce rhamnolipid biological fermentation broth:
[0016] Shake flask and fermenter culture: Pseudomonas sp.VTS-1 (Pseudomonas sp.VTS-1) was cultured for 30h, then transferred to 5L shake flask (filled with 2L medium), inoculation volume 5%, 32±2℃, 120rpm culture for 14h , Transfer to a 500-liter first-level fermenter with a charging factor of 65%, an inoculum of 5%, 32±2°C, a ventilation ratio of 1:1, a pH of 6.5 to 7.5, and a stirring speed of 100 to 150 rpm for 12 hours , Transfer to 3.5 tons of secondary fermentation tank (filling coefficient is 65-75%), inoculum amount is 5%, 32±2℃, ventilation ratio is 1:1, pH is 6.5-7.5, stirring speed is 100rpm and cultivated for 12h , Switch to a 30-ton tertiary fermentation tank with a filling volume of 18 tons. The process parameters of the tertiary fermentation tank are: temperature 32±2℃, pH adjusted to about 6 before sterilization, and pH control with 0.185 tons of NaOH in the later stage ...
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