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Mixed cultivation technology of recombinant escherichia coli for producing glutathione and application of mixed cultivation technology

A technology of recombinant Escherichia coli and Escherichia coli, which is applied in the direction of microorganism-based methods, recombinant DNA technology, peptides, etc., can solve the problems of large ATP consumption, increased production cost, and low product yield, and achieves simple and easy operation, easy control and saving Raw material cost, good biological safety effect

Active Publication Date: 2019-10-29
INNOBIO CORP LTD
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  • Abstract
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  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, in the prior art, there are still various problems hindering the industrial application of this technology. Patent CN201710543648 has obtained GshF-4 mutants with different amino acid sequences, and its synthetic activity, specific activity and optimum temperature have been improved, but there are The output is low; ATP consumption is large and the cost is high, which is not conducive to industrial production
[0005] Enzymatic synthesis of glutathione requires adenosine triphosphate (ATP) as an energy donor, but the price of ATP will greatly increase production costs, so the establishment of an ATP regeneration system is a key part of glutathione synthesis
Patent CN201310538982 overexpresses (exogenous) glutathione bifunctional enzyme (STH) and acetate kinase (ack) in E. coli cells to obtain recombinant expression cells. Although the purpose of ATP regeneration is achieved, Rosetta (DE3) is stable The sensitivity is not high, the cost of the required substrate dilithium acetyl phosphate is high, and the yield of the product is low, the broken enzyme solution increases the cost of separation, in addition, there are problems that the plasmid may be lost, and the use of antibiotics is not friendly to the environment It is difficult to carry out industrial promotion; patent CN201710452240 uses GshF enzyme, ATP regeneration enzyme (PPK enzyme and PAP enzyme) and AK enzyme to generate glutathione in the reactor, and uses adenosine to replace ATP or AMP, but the ATP in it is regenerated The enzyme system includes PPK enzyme, PAP enzyme and AK enzyme. There are problems of high cost caused by separate culture of multiple enzymes, cumbersome immobilization and separation steps, high energy consumption, and the possibility of loss of plasmids. The use of antibiotics is harmful to the environment. Unfriendly problems, etc., eventually lead to its failure to be well promoted in the industry

Method used

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  • Mixed cultivation technology of recombinant escherichia coli for producing glutathione and application of mixed cultivation technology
  • Mixed cultivation technology of recombinant escherichia coli for producing glutathione and application of mixed cultivation technology
  • Mixed cultivation technology of recombinant escherichia coli for producing glutathione and application of mixed cultivation technology

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Experimental program
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Embodiment 1

[0025] Embodiment 1. Construction of recombinant Escherichia coli

[0026] 1. Construction of recombinant expression vectors

[0027] Codon optimization was performed on the target gene GshF (SEQ ID NO.1) derived from Streptococcus thermophilus and ppk2 (Gene ID: 3718134, VERSION: CP000143.2; SEQ ID NO.3) derived from Rhodobacter sphaeroides to obtain codon optimization The GshF gene sequence (SEQ ID NO.2) and the codon-optimized ppk2 gene sequence (SEQ ID NO.4) were used to design primers based on the codon-optimized sequence, that is, to introduce a linear The terminal sequence of the linearized vector (the terminal sequence of the linearized vector is the capital letter in the primer sequence), so that the 5' and 3' ends of the insert fragment have the consensus sequence (15-25bp) at both ends of the vector, as shown in Table 1 As shown, the primers and the template sequences were paired for high-fidelity PCR and gel-cut recovery; at the same time, the plasmid pET-30a was di...

Embodiment 2

[0035] Embodiment two, the optimization of the addition amount of glutathione synthesis reaction bacteria

[0036] In order to reduce the cost, the addition amount of BL21-pET30a-GshF and BL21-pET30a-ppk2 was optimized. The reaction system is as follows: L-glycine 140mM, L-sodium glutamate 140mM MgSO 4 ·7H 2 O 70mM, L-cysteine ​​hydrochloride 120mM, ATP 5mM, 60mM sodium hexametaphosphate, 100mL deionized water. Add the wet bacteria into the reaction system, react at 42°C and pH 7 for 2.5 hours, then take samples, centrifuge at 8000 rpm for 5 minutes, and use HPLC to detect the production of glutathione and the contents of ATP, ADP and AMP in the supernatant .

[0037] When the added amount of BL21-pET30a-GshF wet cells was 50 mg, compared the wet cells of BL21-pET30a-ppk2 with different addition amounts (the mass ratio of BL21-pET30a-GshF:BL21-pET30a-ppk2 was 50:8, 50 :15, 50:25, 50:35) on the response results. like figure 2 As shown, 15-35 mg of BL21-pET30a-ppk2 wet ce...

Embodiment 3

[0040] Embodiment three, the optimization of mixed culture inoculum size

[0041] In order to obtain the same catalytic effect as the mixture of BL21-pET30a-GshF and BL21-pET30a-ppk2 at a ratio of 7:3, the inoculation ratio of the two must be controlled. BL21-pET30a-GshF and BL21-pET30a-ppk2 were respectively activated overnight and mixed according to different ratios (5:4, 3:2, 2:1, 5:2) and mixed with an inoculation volume of 10% by volume The bacteria were introduced into the fermenter (containing Kan R Antibiotic TB medium), maintain the temperature at 37°C±0.5°C, pH at 6.7±0.1, and adjust the ventilation rate (20-100L·h -1 ) and stirring speed (100-600rpm) to control the dissolved oxygen at 10%-40%, add 0.1mM IPTG as an inducer at the beginning of the logarithm, cultivate to the later stage of the logarithm, and put the cells in a tank, and the cells are centrifuged as the reaction cells spare.

[0042] Mix 50 mg of wet cells fermented with BL21-pET30a-GshF and BL21-pE...

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Abstract

The invention discloses a mixed cultivation technology of recombinant escherichia coli for producing glutathione and application of the mixed cultivation technology. According to the mixed cultivationtechnology, a DshF gene and a ppk2 gene are correspondingly integrated on a plasmid vector, escherichia coli containing the GshF gene and escherichia coli containing the ppk2 gene are obtained, and mixedly cultivated in the proportion of 5 to 4-5 to 2 to obtain a mixed bacteria cell. Under the condition of the mixed bacteria cell at37-45 DEG C with the pH of 6-7.5, reduced glutathione is catalyzed and synthesized through inducible expression. In the presence of low-cost sodium hexametaphosphate, the phosphorylation of ADP and AMP can be catalyzed, and high-energy phosphorylation bond breakingof a catalysate provides energy for the synthesis of the glutathione. The cost is saved, the problem of placement of remaining cells due to the high reaction efficiency is avoided, operation is easy,convenient and easy to control, and good application prospects are achieved.

Description

technical field [0001] The invention belongs to the technical field of biocatalysis, and in particular relates to a mixed culture process of recombinant Escherichia coli for producing glutathione and its application. Background technique [0002] Glutathione (γ-L-glutamyl-cysteinyl-glycine, GSH) is a small molecular polypeptide obtained by condensation of three amino acids, L-glutamic acid, L-cysteine ​​and glycine. In organisms, it is the most important small molecular peptide containing sulfhydryl groups in microorganisms and plant biological cells. Glutathione is an important antioxidant in the body. Reduced glutathione has many important functions in living tissues, and plays an important role in liver injury, eye diseases, substance metabolism, and regulation of cell apoptosis. In addition, it also plays an equally important role in the field of food preservation, so the demand for glutathione in the domestic and foreign pharmaceutical markets, food, and cosmetics fie...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C12N15/70C12N1/21C12N15/52C12P21/02C12R1/19
CPCC12N15/70C12N9/93C12P21/02C07K5/0215C12Y603/02002C12N2800/22
Inventor 齐佳坤洪皓范超刘军吴文忠
Owner INNOBIO CORP LTD
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