Method for improving whole-cell catalytic acid production by adjusting pH
A whole-cell, acid-oxidizing technology that is applied in the field of bioengineering to achieve high substrate conversion rates, increase acid yields, and reduce by-product yields
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Embodiment 1
[0021] In a 3L bioreactor, add 1L of glucose solution, the initial glucose concentration is 100g / L, maintain the temperature of the reaction system at 30°C, the stirring speed at 450r / min and the ventilation rate at 3.0vvm, insert 2g of Gluconobacter oxidans cells (dry weight ) for whole-cell catalysis, and after the pH of the fermentation broth drops to 3.5, the pH control is started, and 50% sodium hydroxide is used to maintain the pH of the reaction system at 3.5. During the fermentation process, a semi-continuous feeding operation mode was adopted, and 50 g of glucose (based on the volume of the reaction solution) was added each time to ensure that the glucose concentration in the reaction system was not lower than 5 g / L. During the reaction process, 2 mL was sampled from the fermenter every hour, and the content of glucose, gluconic acid and 2-ketogluconic acid in the sample was analyzed by high-performance anion exchange chromatography. Chromatographic conditions: America...
Embodiment 2
[0023] In a 3L bioreactor, add 1L of glucose solution, the initial glucose concentration is 50g / L, maintain the temperature of the reaction system at 30°C, the stirring speed at 500r / min and the ventilation rate at 2.0vvm, insert 3g of Gluconobacter oxidans cells (dry weight ) for whole-cell catalysis, using 50% sodium hydroxide to maintain the pH of the reaction system at 5.5. During the fermentation process, a semi-continuous feeding operation method was adopted, and 50 g of glucose (based on the volume of the reaction solution) was added each time to control the concentration of glucose in the reaction system to not be lower than 5 g / L. During the reaction process, 2 mL was sampled from the fermenter every hour, and the content of glucose, gluconic acid and 2-ketogluconic acid in the sample was analyzed by high-performance anion exchange chromatography. Chromatographic conditions: American Thermo Fisher ICS5000 ion chromatography, equipped with CarboPac TM PA 10 (2mm×250mm)...
Embodiment 3
[0025] In a 3L bioreactor, add 1L of glucose solution, the initial glucose concentration is 50g / L, maintain the temperature of the reaction system at 30°C, the stirring speed at 500r / min and the ventilation rate at 2.0vvm, insert 5g of Gluconobacter oxidans cells (dry weight ) for whole-cell catalysis, using 50% sodium hydroxide to maintain the pH of the reaction system at 2.5. During the fermentation process, a semi-continuous feeding operation method was adopted, and 50 g of glucose (based on the volume of the reaction solution) was added each time to control the concentration of glucose in the reaction system to not be lower than 5 g / L. During the reaction process, 2 mL was sampled from the fermenter every hour, and the content of glucose, gluconic acid and 2-ketogluconic acid in the sample was analyzed by high-performance anion exchange chromatography. Chromatographic conditions: American Thermo Fisher ICS5000 ion chromatography, equipped with CarboPac TM PA 10 (2mm×250mm)...
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