Method for improving yield of epsilon-polylysine by low pH value stress
A polylysine and yield technology, applied in the field of fermentation engineering, can solve the problem of not using ε-PL and the like, and achieve the effects of reducing extraction cost, simple operation mode and increasing economic benefits
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Embodiment 1
[0018] Embodiment 1 Two-stage pH control strategy
[0019] 3.26L of fermentation medium was installed in a 5L fermenter for batch fermentation, 0.24L of seed liquid cultivated for 24 hours was inoculated into the fermentation medium, and the pH value was adjusted to 6.8-7.5 to start fermentation. During the fermentation process, the stirring speed is controlled at 200-800rpm, the ventilation rate is controlled at 0.5-2vvm, and the dissolved oxygen is controlled at about 30%. Maintain at 5.0 until the number of bacteria doubles, and then drop the pH to 4.0 spontaneously, and maintain the pH at the set value by automatically flowing ammonia or NaOH solution until the carbon source is consumed and the fermentation ends. In the end, the ε-PL yield and cell mass were 7.83 and 26.89g / L, respectively, and the ε-PL yield was 6.12g / L / d.
[0020] If the residual glycerol or glucose concentration in the fermentation broth drops to 10g / L, automatically add sterilized pure glycerin or 500...
Embodiment 2
[0021] Example 2 The two-stage pH control strategy of falling first and then rising
[0022] 3.26L of fermentation medium was installed in a 5L fermenter for batch fermentation, 0.24L of seed liquid cultivated for 24 hours was inoculated into the fermentation medium, and the pH was adjusted to 6.8-7.5 to start fermentation. During the fermentation process, the stirring speed is controlled at 200-800rpm, the ventilation rate is controlled at 0.5-2vvm, and the dissolved oxygen is controlled at 30%; The pH is kept stable until 36 hours, then the pH is adjusted up to 3.8, and ammonia water or NaOH solution is automatically added to keep the pH stable until the carbon source is consumed and the fermentation ends. Finally, the yield of ε-PL and the amount of bacteria were 8.59 and 27.21g / L, respectively, and the yield of ε-PL was 6.42g / L / d.
[0023] If the residual glycerol or glucose concentration in the fermentation broth drops to 10g / L, automatically add sterilized pure glycerin...
Embodiment 3
[0025] 3.26L of fermentation medium was installed in a 5L fermenter for batch fermentation, 0.24L of seed liquid cultivated for 24 hours was inoculated into the fermentation medium, and the pH was adjusted to 6.8-7.5 to start fermentation. During the fermentation process, the stirring speed is controlled at 200-800rpm, the ventilation rate is controlled at 0.5-2vvm, and the dissolved oxygen is controlled at 30%. After 20 hours of fermentation, the pH is artificially lowered to 2.5 and maintained for 12 hours, and then the pH is raised to 3.5. And automatically add ammonia water to maintain the pH at the set value until the glucose is consumed and the fermentation ends. Finally, the yield of ε-PL and the amount of bacteria were 10.39 and 30.61g / L, respectively, and the yield of ε-PL was 7.12g / L / d.
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