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Method for producing succinic acid by utilizing Escherichia coli BA305 through fermentation

A technology of Escherichia coli and succinic acid, which is applied in the direction of microorganism-based methods, biochemical equipment and methods, fermentation, etc., can solve the problem of the decrease of yield and production intensity, the decrease of bacterial body density, the decrease of specific production intensity of cells, Insufficient supply of ATP and other problems, to reduce costs and increase the effect of practical scope

Inactive Publication Date: 2014-06-18
NANJING TECH UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

But if you consider the sugar consumed and the time spent in the aerobic stage, the yield and production intensity decrease
Andersson et al. recovered anaerobic fermentation cells in time and transformed fresh medium to continue anaerobic succinic acid production, which relieved product inhibition and extended the production time of succinic acid. Compared with two-stage fermentation in the same time period, the product concentration increased 60%; but due to the insufficient supply of ATP in the anaerobic fermentation process, the cell density and the specific production intensity of the cells are constantly declining (Bioprocess and Biosystems Engineering. 2010,33,711-718)

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  • Method for producing succinic acid by utilizing Escherichia coli BA305 through fermentation

Examples

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Embodiment 1

[0073] This example illustrates the comparison of Escherichia coli BA305, the starting strain NZN111 and the control strain AFP111 in the production of succinic acid by recycling glucose fermentation.

[0074] First use LB medium to activate the thalli, inoculate Escherichia coli BA305 into LB medium with a liquid volume of 3L in a 7.5L fermenter according to 1% (v / v) inoculum, and add 15 g / L glucose to 0.5 L / min speed into the air or pure oxygen, when aerobic culture bacteria OD 600 Induced with 0.3 mM IPTG to 0.4, cultured aerobically for 15h to OD 600 =19, stop feeding air or pure oxygen, and feed CO at a rate of 0.5 L / min 2 Anaerobic fermentation is carried out to produce acid, and the maximum concentration of glucose added does not exceed 30 g / L. At the same time, a neutralizing agent basic magnesium carbonate is added to adjust the pH value to 6.4. When the glucose consumption rate of the cells drops to 0.6 g / (L h), the glucose content in the culture medium is detected...

Embodiment 2

[0086] This example illustrates the comparison of Escherichia coli BA305, the starting strain NZN111 and the control strain AFP111 in the production of succinic acid by recycling xylose fermentation.

[0087] First use LB medium to activate the thalline, Escherichia coli BA305 is inoculated into 7.5L fermenter tank liquid volume is 3L LB medium and adds 15 g / L xylose by 1% (v / v) inoculum amount, Infuse air or pure oxygen at a rate of 0.5 L / min, when the OD of aerobic culture cells 600 Induced with 0.3 mM IPTG to 0.6, cultured aerobically for 15h to OD 600 =19, stop feeding air or pure oxygen, and feed CO at a rate of 0.5 L / min 2 Perform anaerobic fermentation to produce acid, add xylose at a maximum concentration of no more than 30 g / L, and add sodium carbonate to adjust the pH to 6.8. When the xylose consumption rate of the cells drops to 0.6 g / (L h), the xylose content in the medium is detected, and the bacterial cells are obtained by aseptic centrifugation, and the concen...

Embodiment 3

[0099] This example illustrates the comparison of Escherichia coli BA305, the starting strain NZN111 and the control strain AFP111 in the production of succinic acid by recycling fructose fermentation.

[0100] First use LB medium to activate the thalli, inoculate Escherichia coli BA305 into 7.5L fermenter with 3L LB medium and add 15 g / L fructose according to 1% (v / v) inoculum amount, to 0.5 L / min speed into the air or pure oxygen, when aerobic culture bacteria OD 600 Induced with 0.3 mM IPTG to 0.5, cultured aerobically for 15h to OD 600 =19, stop feeding air or pure oxygen, and feed CO at a rate of 0.5 L / min 2 Perform anaerobic fermentation to produce acid, add fructose at a maximum concentration of no more than 30 g / L, and add sodium bicarbonate to control the pH value to 6.6. When the fructose consumption rate of the cells drops to 0.6 g / (L h), the fructose content in the culture medium is detected, and the bacterial cells are obtained by aseptic centrifugation, and the...

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Abstract

The invention belongs to the technical field of bioengineering and relates to a method for producing succinic acid by utilizing Escherichia coli BA305 through fermentation. The production efficiency of the succinic acid is improved by increasing the supply of the Escherichia coli BA305 on the ATP in a two-stage fermentation process; and the production performance is maintained and the production ability of the succinic acid is improved in the process of producing the succinic acid by recycling cells.

Description

technical field [0001] The invention belongs to the technical field of bioengineering, and relates to a method for producing succinic acid by fermentation of Escherichia coli BA305, specifically, a method for producing succinic acid by highly efficient recycling of genetically engineered bacteria producing succinic acid by fermentation. ATP supply improves the production efficiency of succinic acid in the two-stage fermentation process, and maintains production performance and prolongs the production capacity of succinic acid in the process of recycling cells to produce succinic acid. Background technique [0002] Succinic acid, also known as succinic acid, is widely used in industries such as medicine, pesticides, dyes, spices, paints, food and plastics. As a C4 platform compound, it can be used to synthesize 1,4-butanediol, tetrahydrofuran, Organic chemicals such as γ-butyrolactone and biodegradable materials such as polybutylene succinate (PBS) are considered by the US De...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C12P7/46C12R1/19
CPCY02P20/141
Inventor 姜岷梁丽亚刘嵘明马江锋陈可泉韦萍
Owner NANJING TECH UNIV