Method of efficiently synthesizing solvents and organic acids by butanol fermentation
A butanol fermentation and organic acid technology, applied in the field of microbial fermentation, can solve the problems of low butyric acid/butanol, low butyric acid concentration, inability to obtain high value-added products of in-situ synthesis of butyl butyrate, and achieve efficient synthesis , increase production and reduce the cost of fermentation raw materials
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Embodiment approach 2
[0039] Embodiment 2: Butanol fermentation process with 0.2 g / L vanillin added
[0040] The preparation process of the activation solution is exactly the same as that in Embodiment 1, and will not be repeated here.
[0041] The preparation process of the Clostridium acetobutylicum seed solution is exactly the same as that in Embodiment 1, and will not be repeated here.
[0042] The Clostridium acetobutylicum seed solution was transferred to a 5 L anaerobic fermentation tank with an inoculum of 10% (v / v), and the anaerobic fermentation tank was filled with 3 L Clostridium fermentation medium (where the glucose concentration was 60 g / L, the vanillin concentration is 0.2 g / L), the fermentation temperature is 37°C, and the pH control strategy during the fermentation process is expressed as follows: During the acid production period (~0-15 h), the pH is automatically controlled to 5.0 by the control cabinet , using 14% (w / v) ammonia water; during the solventogenic phase (~15-48 h)...
Embodiment approach 3
[0046] Embodiment 3: Butanol fermentation process with 0.2 g / L vanillic acid added
[0047] The preparation process of the activation solution is exactly the same as that in Embodiment 1, and will not be repeated here.
[0048] The preparation process of the Clostridium acetobutylicum seed solution is exactly the same as that in Embodiment 1, and will not be repeated here.
[0049] The Clostridium acetobutylicum seed solution was transferred to a 5 L anaerobic fermentation tank with an inoculum of 10% (v / v), and the anaerobic fermentation tank was filled with 3 L Clostridium fermentation medium (where the glucose concentration was 60 g / L, the concentration of vanillic acid is 0.2 g / L), the fermentation temperature is 37°C, and the pH control strategy during the fermentation process is expressed as follows: During the acid production period (~0-15 h), the pH is automatically controlled to 5.0 by the control cabinet, 14% (w / v) ammonia was utilized; during the solventogenic pha...
Embodiment approach 4
[0053] Embodiment 4: Butanol fermentation process with addition of 0.1 g / L vanillin and 0.1 g / L vanillic acid
[0054] The preparation process of the activation solution is exactly the same as that in Embodiment 1, and will not be repeated here.
[0055] The preparation process of the Clostridium acetobutylicum seed solution is exactly the same as that in Embodiment 1, and will not be repeated here.
[0056]The Clostridium acetobutylicum seed solution was transferred to a 5 L anaerobic fermentation tank with an inoculum of 10% (v / v), and the anaerobic fermentation tank was filled with 3 L Clostridium fermentation medium (where the glucose concentration was 60 g / L, the concentration of vanillin is 0.1 g / L, the concentration of vanillic acid is 0.1 g / L), the fermentation temperature is 37°C, and the pH control strategy during the fermentation process is expressed as follows: During the acid production period (~0-15 h) , the pH is automatically controlled to 5.0 through the con...
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