Xylose-Induced Genetically Engineered Bacteria Used for Producing Ectoine and Use Thereof

Abstract

The present disclosure relates to the field of genetic engineering, especially relates to a xylose-induced genetically engineered bacteria used for producing ectoine as well as a construction method and use thereof The genetically engineered bacteria is constructed by heterologously expressing the ectABC gene cluster from Halomonas elongata on the E. coli chromosome, using the promoter of xylose transporter coding gene xylF to control the RNA polymerase from T7 bacteriophage, reconstructing a synthesis pathway of ectoine and constructing a plasmid-free system, and enhancing the expression of target genes by a strong promoter T7; the yiled of ectoine reached 12-16 g/L after 20-28 h fermentation in shake flask, and reached 35-50 g/L after 24-40 h fermentation in a 5 L fermentor.

Description

SEQUENCE LISTING

The instant application contains a Sequence Listing which has been submitted in ASCII format via EFS-Web and is hereby incorporated by reference in its entirety. Said ASCII copy is named GBRSMJ023-POA_SequenceListing.txt, created on Aug. 22, 2021 and is 30,217 bytes in size.

TECHNICAL FIELD

The present disclosure relates to the field of genetic engineering, especially relates to a xylose-induced genetically engineered bacteria used for producing ectoine as well as a construction method and use thereof.

BACKGROUND

Ectoine(1,4,5,6-tetrahydro-2-methyl-4-pyrimidinecarboxylic acid), which is a cyclic amino acid formed by intramolecular dehydration of N-acetylated diaminobutyric acid, it was used as an osmotic pressure compensating solute at the earliest time and was found in Ectothiorhodospira halochloris capable of carrying out photosynthesis. After years of research, ectoine also has been found in different halophilic fungi by scholars.

Recently, the osmotic protection function of ectoine and its application in other fields have drawn more and more attention. It has been found that ectoine can be used as a stabilizer to protect and stabilize enzymes, nucleic acids, DNA and other biological macromolecules against high temperature, drying, high osmotic pressure, freezing and other adverse environment. At present, ectoine has important uses in the fields of enzyme preparations, genetic engineering, medical treatment and cosmetics.

The use in the field of enzyme preparations: in the industrial processes, the physical and chemical conditions cannot be ensured to be the optimal condition of the enzyme reaction all the time, so that the enzyme preparations need to keep good activity in adverse environment such as different temperatures and salinities, and ectoine can help such protein macromolecules keep good activity under adverse environment.

The use in the field of genetic engineering: at present, the genes controlling the synthesis of ectoine have been expressed in tobacco to improve the salt tolerance of tobacco to a certain extent, although its expression level is relatively low; in addition, ectoine can reduce the Tm value of DNA; and for the template double-stranded DNA with high G+C content, the PCR amplification can be promoted by adding ectoine into the reaction system.

The use in the field of medical treatment: ectoine can not only be used as a protective agent of healthy cells during chemotherapy, but also have certain preventative effect on Alzheimer's disease and Parkinson's disease.

The use in the field of cosmetics: ectoine can be added into cosmetics as humectants for its osmotic protection function, so that the skin can be prevented from being dried and aged, and the damage of UV to the skin can be reduced.

At present, the production methods of ectoine include fermentation and enzyme catalysis. Thereinto, the halophilic microorganisms are widely used in the fermentation of ectoine for possessing the ectoine synthesis pathway. The ectoine synthesis pathway of halophilic bacteria is: oxaloacetic acid—aspartate—aspartate-β-semialdehyde—L-2,4-diaminobutyrate—Nγ-acetyl-diaminobutyrate—ectoine. Grammann et al. found a permeation regulation system from the Halomonas elongate which is different from the systems ever found, it contains three genes of ectA, ectB and ectC, these three genes are organized in an operon that controlled by a common promoter to express L-2,4-diaminobutyrate acetyltransferase, L-2,4-diaminobutyrate transaminase and ectoine synthase respectively.

In the present invention, the ectoine-synthesizing gene ectABC from a halophilic bacteria is introduced into an non-halophilic bacteria to reconstruct the ectoine synthesis pathway, resulting in the recombinant strain can synthesize ectoine by taking glucose as a raw material under the stress of moderate or low salt concentration.

In addition, in the present invention, the control gene iclR is also knocked out so as to break the glyoxylate cycle and increase the accumulation amount of the precursor oxylacetic acid; the homoserine-dehydrogenase I coding gene thrA is knocked out to prevent the metabolic shunt from L-aspartate-β-semialdehyde to threonine, lysine and methionine, and make more metabolic flux flow to the ectoine pathway; the expression intensity of gene ectABC is increased by replacing a promoter with a strong promoter T7, and the activity of the key enzyme is improved so as to increase the metabolic flux of the ectoine pathway; the expression level of lysC is increased by replacing with the strong promoter T7, and the feedback inhibition of lysine to the key enzyme aspartate kinase in the ectoine synthesis route is relieved, meanwhile, aspartate kinase is introduced to complement to over-accumulate ectoine; the RNA polymerase (T7RNAP) from T7 bacteriophage is promoted by the promoter of xylose transporter coding gene xylF (PxylF), moreover, the expression of exogenous genes are enhanced by the strong promoter T7.

SUMMARY OF THE INVENTION

One of technical schemes of the invention is to provide a genetically engineered bacteria E. coli ECT06 used for producing ectoine. The E. coli ECT06 is constructed as follows: heterologously expressing the ectABC gene cluster from Halomonas elongata on the E. coli chromosome to reconstruct the synthesis pathway of ectoine and build a non-plasmid system; using the promoter of xylose transporter coding gene xylF (PxylF) to control the RNA polymerase (T7RNAP) from T7 bacteriophage, and enhancing the expression of the target genes by strong promoter T7(Pt7).

The genetically engineered bacteria used for producing ectoine contains a ectABC gene from Halomonas elongata (CGMCC 1.6329) and promoted by promoter T7; gene deficiencies of gene thrA and gene iclR; a lysC gene from Corynebacterium glutamicum and controlled by promoter T7; a ppc gene promoted by promoter trc; and a RNA polymerase (T7RNAP) from T7 bacteriophage and promoted by the promoter PxylF which is the promoter of xylose transporter coding gene xylF.

The nucleotide sequence of the ectABC gene is a sequence shown in a sequence table as SEQ ID No.1.

The nucleotide sequence of the lysC gene is a sequence shown in a sequence table as SEQ ID No.2.

The nucleotide sequence of the thrA gene is a sequence shown in a sequence table as SEQ ID No.3.

The nucleotide sequence of the iclR gene is a sequence shown in a sequence table as SEQ ID No.4.

The nucleotide sequence of the promoter T7 is a sequence shown in a sequence table as SEQ ID No.5.

The nucleotide sequence of the terminator T7 is a sequence shown in a sequence table as SEQ ID No.6.

The nucleotide sequence of the promoter trc is a sequence shown in a sequence table as SEQ ID No.7.

The nucleotide sequence of the ppc gene is a sequence shown in a sequence table as SEQ ID No.8.

The nucleotide sequence of the PxylF is a sequence shown in a sequence table as SEQ ID No.9.

The nucleotide sequence of the T7RNAP is a sequence shown in a sequence table as SEQ ID No.10.

The host cell of the genetically engineered bacteria used for producing ectoine is E. coli W3110 (ATCC 27325).

Another technical scheme of the invention is to provide a construction method of the genetically engineered bacteria used for producing ectoine, specifically comprises the following steps:

(1) knocking out the thrA and iclR genes from the starting strain E. coli W3110 (ATCC 27325);

(2) replacing the promoter of ppc gene with promoter trc;

(3) expressing the T7 RNA polymerase: a junction fragment of the promoter of xylose transporter coding gene xylF (PxylF)and T7 RNA polymerase (T7RNAP) is constructed and expressed;

(4) constructing the metabolic pathway from aspartate to ectoine:

{circle around (1)}constructing a gene fragment T7-ectABC by ligating promoter T7 and ectABC gene, and expressing it;

{circle around (2)}constructing a gene fragment T7-lysC by ligating promoter T7 and lysC gene, and expressing it.

Another technical scheme of the invention is to provide a production method of ectoine by using the genetically engineered bacteria above mentioned, details are as follows:

The shake-flask fermentation, which specifically comprises the following steps:

(1) seed culture: the slant cultured cells are inoculated into a seed culture medium, and cultured at 37° C., 200 rpm for 7 hours;

(2) shake-flask fermentation: the seed liquid is inoculated into a fermentation medium according to a inoculum size of 10-15%, and cultured for 20-28 hours at 37° C. and 200 rpm; the pH is maintained to be 7.2 by supplementing NH₄OH, and a 60% (m/v) glucose solution is used for maintaining the fermentation (the phenol red is used as an indicator, and that the color of the fermentation broth changes no longer means sugar deficiency, and then 1-2 ml of 60% glucose solution is added), the expression of the target gene is induced by adding 60% (m/v) xylose solution (final concentration of xylose in the fermentation broth is 5-15 g/L) at the initial stage of fermentation, and the fermentation period is 20-28 h.

The yield of ectoine reached 12-16 g/L after 20-28 h fermentation in shake flask.

The seed medium: sucrose 20-30 g/L, (NH₄)₂SO₄ 1-5 g/L, KH₂PO₄ 1-5 g/L, MgSO₄.7H₂O 1-2 g/L, yeast extract powder 5-10 g/L, corn steep liquor 1-3 mL/L, FeSO₄.7H₂O 1-3 mg/L, MnSO₄.H₂O 1-3 mg/L, the rest is water, pH7.0.

The fermentation medium: glucose 20-40 g/L, (NH₄)₂SO₄ 1-3 g/L, KH₂PO₄ 1-3 g/L, MgSO₄.7H₂O 1-2 g/L, yeast extract powder 0.1-0.3 g/L, corn steep liquor 1-2 mL/L, FeSO₄.7H₂O 80-100 mg/L, MnSO₄.7H₂O 80-100 mg/L, the rest is water, pH7.0.

The fermentor fermentation, which specifically comprises the following steps:

(1) slant culture: a loop of thallus is scraped off from the strain deposit tube stored in −80° C., and spread evenly on the agar slant culture medium to culture at 37° C. for 15-18 hours, and then transferred into a second-generation agar slant to culture for 12 hours;

(2) seed culture: proper amount of sterile water is added into the agar slant to make a bacterial suspension, then inoculated the bacterial suspension into a seed medium and cultured to a cell dry weight of 5-6 g/L, during the period the pH is stabilized to be about 7.0, the temperature is kept constantly at 36° C., and the dissolved oxygen is 25-35%.

(3) fermentor fermentation: the seed liquid is inoculated into a fermentation medium according to a inoculum size of 15-20%, and cultured for 24-40 hours, during the period the pH is stabilized to be about 7.0, the temperature is kept constantly at 36° C., and the dissolved oxygen is 25-35%;

The expression of the target gene is induced by adding xylose solution to the fermentation medium with a final concentration of 5-15 g/L at the initial stage, and when the glucose in the medium is exhausted, a 80% glucose solution is added to maintain the glucose concentration in the fermentation medium at 0-2 g/L, and the fermentation period is 24-40 hours.

The yield of ectoine reached 35-50 g/L after 24-40 hours fermentation in a 5 L fermentor.

The agar slant culture medium: sucrose 1-3 g/L, tryptone 5-10 g/L, beef extract 5-10 g/L, yeast extract 2-5 g/L, NaCl 2-5 g/L, agar 15-30 g/L, the rest is water, pH 7.0-7.2, carrying out high-pressure steam sterilization at 115° C. for 15 minutes.

The seed medium: glucose 15-30 g/L, yeast extract 5-10 g/L, tryptone 5-10 g/L, KH₂PO₄ 5-15 g/L, MgSO₄.7H₂O 2-5 g/L, FeSO₄.7H₂O 5-15 mg/L, MnSO₄.H₂O 5-15 mg/L, VB1 1-3 mg/L, VH 0.1-1 mg/L, defoamer 2 drops, the rest is water, pH 7.0-7.2, carrying out high-pressure steam sterilization at 115° C. for 15 minutes.

The fermentation medium: glucose 15-25 g/L, yeast extract 1-5 g/L, tryptone 1-5 g/L, sodium citrate 0.1-1 g/L, KH₂PO₄ 1-5 g/L, MgSO₄.7H₂O 0.1-1 g/L, FeSO₄.7H₂O 80-100 mg/L, MnSO₄.H₂O 80-100 mg/L, VB1 0.5-1 mg/L, VH 0.1-0.5 mg/L, defoamer 2 drops, the rest is water, pH 7.0-7.2, carrying out high-pressure steam sterilization at 115° C. for 15 minutes.

The beneficial effects:

1. After a series of modification, the genetically engineered bacteria used for producing ectoine disclosed in this invention has an enhanced metabolic flux of glucose to L-aspartate-β-semialdehyde, and the genetically engineered bacteria can directly utilize glucose as a raw material to produce ectoine; the yield of ectoine reached 12-16 g/L after 20-28 h fermentation in shake flasks, and reached 35-50 g/L after fermentation in a 5 L fermentor for 24-40 h.

BRIEF DESCRIPTION OF FIGURES

FIG. 1: Deletion and verification of the thrA gene

Wherein, M: Marker, 1: upstream homologous arm, 2: chloramphenicol resistance gene fragment, 3: downstream homologous arm, 4: overlapping fragment; 5: PCR fragment obtained by using original genomic DNA as template; 6: PCR fragment obtained by using genomic DNA with deletion of gene thrA as template, 7: PCR fragment obtained by using genomic DNA with deletion of chloramphenicol resistance gene as template;

FIG. 2: Deletion and verification of iclR gene

Wherein, M: Marker, 1: iclR gene deletion fragment; 2: PCR fragment obtained by using original genomic DNA as template, 3: PCR fragment obtained by using genomic DNA with deletion of iclR as template, 4: PCR fragment obtained by using genomic DNA with deletion of chloramphenicol resistance gene as template;

FIG. 3: Replacement of P_ppc with P_trc and verification

Wherein, M: Marker, 1: upstream homologous arm, 2: chloramphenicol resistance gene fragment, 3: downstream homologous arm, 4: promoter replacing fragment; 5: PCR fragment obtained before promoter replacement, 6: PCR fragment obtained after promoter replacement, 7: PCR fragment obtained by using genomic DNA with deletion of Chloramphenicol resistance gene as template;

FIG. 4: Construction and PCR verification of PxylF-T7RNAP integrated fragment

Wherein, M: Marker, 1: PxylF-T7RNAP overlapping fragment, 2: upstream homologous arm, 3: chloramphenicol resistance gene fragment, 4: downstream homologous arm, 5: PxylF-T7RNAP integrated fragment; 6: PCR fragment obtained after replacing lacZ with PxylF-T7RNAP integrated fragment, 7: PCR fragment obtained by using genomic DNA with deletion of chloramphenicol resistance gene as template;

FIG. 5: Construction and PCR verification of T7-ectABC integrated fragment

Wherein, M: Marker, 1: upstream homologous arm, 2: overlapping fragment of T7-ectABC and chloramphenicol resistance gene, 3: downstream homologous arm, 4: T7-ectABC integrated fragment; 5: the original gene fragment; 6: PCR fragment obtained after replacing ybeM gene with T7-ectABC integrated fragment;

FIG. 6: Construction and PCR verification of T7-lysC integrated fragment

Wherein, M: Marker, 1: upstream homologous arm, 2: overlapping fragment of T7-lysC and chloramphenicol resistance gene, 3: downstream homologous arm, 4: T7-lysC integrated fragment; 5: the original gene fragment, 6: PCR fragment of genomic DNA after replacing yghX gene with T7-lysC integrated fragment;

FIG. 7: The fermentation process curve of the control strain in example 4.

FIG. 8: The fermentation process curve of the test strain in example 4.

DETAILED DESCRIPTION

EXAMPLE 1

Construction of Strain E. coli ECT 06

(1) Deletions of thrA Gene and iclR Gene

Deletions of thrA gene and iclR gene were performed using the Red recombination system:

{circle around (1)} the upstream and downstream homologous arms of the thrA gene were obtained by PCR amplification using the genomic DNA of E. coli W3110 (ATCC 27325) as a template and upstream homologous arm primers (thrA-up-1, thrA-up-2) and downstream homologous arm primers (thrA-down-1, thrA-down-2) as primers which were designed according to the gene sequence of thrA gene;

{circle around (2)} a chloramphenicol resistance gene fragment was amplified by PCR using plasmid pKD3 as a template and Cm^r-thrA-up, Cm^r-thrA-down as primers;

{circle around (3)} a thrA gene deletion fragment was amplified by overlapping PCR using the amplified fragments obtained in step {circle around (1)} and {circle around (2)} as templates, and the thrA gene deletion fragment was composed of upstream and downstream homologous arms of the thrA gene and the chloramphenicol resistance gene fragment;

{circle around (4)} transforming the thrA gene deletion fragment into the E. coli W3110 harboring plasmid pKD46 to obtain positive transformants, and then the E. coli ECT01 that a bacterium with thrA gene deletion was obtained by eliminating the chloramphenicol resistance gene fragment from the positive transformants; (the verification of thrA gene deletion by electrophoresis shown in FIG. 1: the upstream homologous arm was about 500 bp, the downstream homologous arm was about 700 bp, the chloramphenicol resistance gene fragment was about 1080 bp, the thrA gene deletion fragment was about 2500 bp; the original gene was about 2000 bp, PCR fragment obtained by PCR amplification after deletion of chloramphenicol resistance gene was about 1500 bp, the electrophoretic bands were consistent with the designed size, which proved that the thrA gene was successfully deleted).

Deletion of gene iclR: a E. coli ECT02 was obtained by deleting iclR gene from E. coli ECT01 using the same method above mentioned (the primers of upstream homologous arm: iclR-up-1, iclR-up-2; the primers of downstream homologous arm: iclR-down-1, iclR-down-2; the primers of chloramphenicol resistance gene fragment: Cm^r-iclR-up, Cm^r-iclR-down). (the deletion of iclR gene was verified by electrophoresis shown in FIG. 2: the upstream homologous arm was about 500 bp, the downstream homologous arm was about 500 bp, the chloramphenicol resistance gene fragment was about 1080 bp, the thrA gene deletion fragment was about 1700 bp; the original gene was about 1200 bp, PCR fragment obtained by PCR amplication after deletion of chloramphenicol resistance gene was about 800 bp, the electrophoretic bands were consistent with the designed size, which proved that the iclR gene was successfully deleted).

(2) Replacement the Promoter of ppc Gene with Promoter trc

{circle around (1)} the upstream and downstream homologous arms of the the promoter of ppc were amplified by PCR using the genomic DNA of E. coli W3110 (ATCC 27325) as a template and the upstream homologous arm primers (p_ppc-up-1, p_ppc-up-2) and downstream homologous arm primers (p_ppc-down-1, p_ppc-down-2) as primers which were designed according to the gene sequence of ppc gene; the upstream homologous arm was located upstream of the promoter of ppc, and the downstream homologous arm was located in front of the ppc structure gene for 600 bp;

{circle around (2)} amplifying the promoter trc from plasmid pTrc99a (the forward primer: p_trc-up; the reverse primer: p_trc-down);

{circle around (3)} a chloramphenicol resistance gene fragment was amplified by PCR using plasmid pKD3 as a template and Cm^r-ppc-up, Cm^r-ppc-down as primers;

{circle around (4)} a promoter of ppc gene replacing fragment was amplified by overlapping PCR using the amplified fragments obtained in step {circle around (1)}, {circle around (2)} and {circle around (3)} as templates, and the promoter of ppc gene replacing fragment was composed of upstream and downstream homologous arms of the promoter of ppc gene, promoter trc and the chloramphenicol resistance gene fragment;

{circle around (5)} E. coli ECT03, the promoter of ppc of which was replaced with promoter trc, was obtained by transforming the promoter of ppc gene replacing fragment into the E. coli ECT02 and then eliminating the chloramphenicol resistance gene fragment; (the replacing of the promoter of ppc gene with promoter trc was verified by electrophoresis shown in FIG. 3: the upstream homologous arm was about 700 bp, the downstream homologous arm was about 800 bp, the chloramphenicol resistance gene fragment is about 1080 bp, the replacing fragment was about 2300 bp, the original gene was about 1300 bp, PCR fragment obtained by PCR amplification after deletion of chloramphenicol resistance gene was about 1500 bp. The electrophoretic bands were consistent with the designed size, which proved that the promoter was successfully replaced).

(3) Expression of T7 RNA Polymerase (T7RNAP)

{circle around (1)} a promoter PxylF of xylose transporter coding gene xylF was amplified by PCR using the genomic DNA of E. coli W3110 (ATCC 27325) as a template and PxylF-up, PxylF-down as primers which were designed according to the gene sequence of xylF;

{circle around (2)} a T7RNAP fragment was amplified by PCR using the genomic DNA of E. coli BL21(DE3) as a template and T7RNAP-up, T7RNAP-down as primers which were designed according to the gene sequence of T7RNAP;

{circle around (3)} a chloramphenicol resistance gene fragment was amplified by PCR using plasmid pKD3 as a template and Cm^r-lacZ-up, Cm^r-lacZ-down as primers;

{circle around (4)} the upstream and downstream homologous arms of the lacZ gene were amplified by PCR using the genomic DNA of E. coli W3110(ATCC27325) as a template and the upstream homologous arm primers (lacZ-up-1, lacZ-up-2), downstream homologous arm primers (lacZ-down-1, lacZ-down-2) as primers which were designed according to the gene sequence of lacZ gene; the upstream and downstream homologous arms were both located inside the lacZ gene;

{circle around (5)} an integrated fragment PxylF-T7RNAP was amplified by overlapping PCR using the amplified fragments obtained in step {circle around (1)}, {circle around (2)}, {circle around (3)} and {circle around (4)} as templates, and the integrated fragment PxylF-T7RNAP was composed of upstream and downstream homologous arms of lacZ gene, the chloramphenicol resistance gene fragment, the promoter PxylF and the T7RNAP fragment;

{circle around (6)} E. coli ECT04 was obtained by transforming the integrated fragment PxylF-T7RNAP into the E. coli ECT03 harboring plasmid pKD46 and eliminating the chloramphenicol resistance gene fragment, in which the lacZ gene was replaced with T7RNAP promoted by a promoter PxylF; (the expression of PxylF-T7RNAP integrated fragment was verified by electrophoresis shown in FIG. 4: the upstream homologous arm was about 451 bp, the downstream homologous arm was about 456 bp, the chloramphenicol resistance gene fragment was about 1024 bp, the overlapping fragment PxylF-T7RNAP was about 3000 bp, the integrated fragment PxylF-T7RNAP was about 5000 bp; the original gene fragment was about 3700 bp, PCR fragment obtained by PCR amplication after deletion of chloramphenicol resistance gene was about 4000 bp. The electrophoretic bands were consistent with the designed size, which proved that the integrated fragment PxylF-T7RNAP was successfully integrated).

(4) Construction of Metabolic Pathway from Aspartate to Ectoine

{circle around (1)} an ectABC gene was amplified by PCR using the genomic DNA of Halomonas elongata (CGMCC 1.6329) as a template and ectABC-up, ectABC-down as primers which were designed according to the gene sequence of ectABC, and a T7-ectABC fragment was obtained by PCR using primers which were performed by adding promoter T7 and terminator T7 to the 5′ and 3′ ends of the ectABC fragment amplification primers;

{circle around (2)} a chloramphenicol resistance gene fragment was amplified by PCR using plasmid pKD3 as a template and Cm^r-ybeM-up, Cm^r-ybeM-down as primers;

{circle around (3)} the upstream and downstream homologous arms of the ybeM gene were amplified by PCR using the genomic DNA of E. coli W3110(ATCC27325) as a template and the upstream homologous arm primers (ybeM-up-1, ybeM-up-2), downstream homologous arm primers (ybeM-down-1,ybeM-down-2) as primers which were designed according to the gene sequence of ybeM gene; the upstream and downstream homologous arms were both located inside the ybeM gene;

the nucleotide sequence of the ybeM gene was a sequence shown in a sequence table as SEQ ID No.11;

{circle around (4)} an integrated fragment T7-ectABC was amplified by overlapping PCR using the amplified fragments obtained in step {circle around (1)}, {circle around (2)} and {circle around (3)} as templates, and the integrated fragment T7-ectABC was composed of upstream and downstream homologous arms of ybeM gene, the promoter T7, the chloramphenicol resistance gene fragment, ectABC fragment and the terminator T7;

{circle around (5)} a E. coli ECT05 was obtained by transforming the integrated fragment T7-ectABC into the E. coli ECT04 and eliminating the chloramphenicol resistance gene fragment, in which the ybeM gene was replaced by a promoter T7 promoted ectABC; (the integration of integrated fragment T7-ectABC was verified by electrophoresis shown in FIG. 5: the upstream homologous arm was about 488 bp, the downstream homologous arm was about 645 bp, the chloramphenicol resistance gene fragment was about 1024 bp, the T7-ectABC was about 2500 bp; the integrated fragment T7-ectABC was about 4500 bp, the original gene fragment was about 2000 bp, the electrophoretic bands were consistent with the designed size, which proved that the integrated fragment T7-ectABC was successfully integrated).

(5) Introducing of lysC gene from Corynebacterium glutamicum

{circle around (1)} a lysC gene was amplified by PCR using the genomic DNA of Corynebacterium glutamicum ATCC13032 as a template and lysC-up, lysC-down as primers which were designed according to the gene sequence of lysC, and a T7-lysC fragment was obtained by PCR using primers which were performed by adding promoter T7 and terminator T7 to the 5′ and 3′ ends of the lysC fragment amplification primers;

{circle around (2)} a chloramphenicol resistance gene fragment was amplified by PCR using plasmid pKD3 as a template and Cm^r-yghX-up, Cm^r-yghX-down as primers;

{circle around (3)} the upstream and downstream homologous arms of the yghX gene were amplified by PCR using the genomic DNA of E. coli W3110(ATCC27325) as a template and the upstream homologous arm primers (yghX-up-1,yghX-up-2), downstream homologous arm primers (yghX-down-1, yghX-down-2) as primers which were designed according to the gene sequence of yghX gene; the upstream and downstream homologous arms were both located inside the yghX gene;

the nucleotide sequence of the yghX gene was a sequence shown in a sequence table as SEQ ID No.12;

{circle around (4)} an integrated fragment T7-lysC was amplified by overlapping PCR using the amplified fragments obtained in step {circle around (1)}, {circle around (2)} and {circle around (3)} as templates, and the integrated fragment T7-lysC was composed of upstream and downstream homologous arms of yghX gene, the promoter T7, the chloramphenicol resistance gene fragment, lysC gene fragment and the terminator T7;

{circle around (5)} a E. coli ECT06 was obtained by transforming the integrated fragment T7-lysC into the E. coli ECT05 and eliminating the chloramphenicol resistance gene fragment, in which the yghX gene was replaced by a promoter T7 promoted lysC; (the integration of integrated fragment T7-lysC was verified by electrophoresis shown in FIG. 6: the upstream homologous arm was about 418 bp, the downstream homologous arm was about 480 bp, the chloramphenicol resistance gene fragment was about 1024 bp, the T7-lysC was about 1500 bp, the integrated fragment T7-lysC was about 3500 bp, the original gene fragment was about 1732 bp. As can be seen in FIG. 6, the electrophoretic bands were consistent with the designed size, which proves that the T7-lysC was successfully integrated).

The primers used in the experiment are shown in the following table:

Primers	Sequence (5′-3′)	SEQ ID No.
thrA-up-1	GCAACGGGCAATATGTCTCT	13
thrA-up-2	GCTCAAGACGCCAGGTGGTTGGTGATTTTG	14
thrA-down-1	CGTTACATCCGTGAAGATTGCCGAAGTGGAT	15
thrA-down-2	AGCACCCACAGCCACTCAT	16
Cmr-thrA-up	AACCACCTGGCGTCTTGAGCGATTGTGTAGG	17
Cmr-thrA-down	CAATCTTCACGGATGTAACGCACTGAGAAGC	18
iclR-up-1	TTTCCGCCGACAGGGATT	19
iclR-up-2	GCTCAAGACGTTTCGCGGGAATGGGTG	20
iclR-down-1	CGTTACATCCAAGCGGCGAAGGAAGTGAC	21
iclR-down-2	ATAGAGGCGTCGCCAGCT	22
Cmr-iclR-up	TCCCGCGAAACGTCTTGAGCGATTGTGTAGG	23
Cmr-iclR-down	TTCGCCGCTTGGATGTAACGCACTGAGAAGC	24
pppc-up-1	GCTATGAATGCCCACCGAAT	25
pppc-up-2	GCTCAAGACGCGTCATTAAATTCACGACGCTT	26
pppc-down-1	CGTTACATCCGAAGCTGTGGTATGGCTGTGC	27
pppc-down-2	CCATTTGGCTTCATCTACCG	28
ptrc-up	GTGAATTCAGGAAACAGACCATGAACGAACA	29
	ATATTCCGCA
ptrc-down	GCATGGTACCAATATCGCCGAATGTAACGAC	30
Cmr-ppc-up	TTTAATGACGCGTCTTGAGCGATTGTGTAGG	31
Cmr-ppc-down	CCACAGCTTCGGATGTAACGCACTGAGAAGC	32
PxylF-up	GAGATAATTCACAAGTGTGCGCT	33
PxylF-down	TAGTAAATCCCATGGTGTAGGGCCTTCTGTAG	34
T7RNAP-up	CTACACCATGGGATTTACTAACTGGAAGAGGCAC	35
T7RNAP-down	CCGGCACAGTATCAAGGTATTT	36
lacZ-up-1	TCAAATTCAGCCGATAGCGG	37
lacZ-up-2	GAATTATCTCGCTTTCCAGTCGGGAAACCT	38
lacZ-down-1	CGTTACATCCCAGGTAGCAGAGCGGGTAAACT	39
lacZ-down-2	GGATTTCCTTACGCGAAATACG	40
Cmr-lacZ-up	ACTGTGCCGGCGTCTTGAGCGATTGTGTAGG	41
Cmr-lacZ-down	CTGCTACCTGGGATGTAACGCACTGAGAAGC	42
ectABC-up	AATAATCGTCTAATACGACTCACTATAGGGTCTAGAAATAATT	43
	TTGTTTAACTTTAAGAAGGAGATATACCATGAACGCAACCACA
	GAGCC
ectABC-down	GCTCAAGACGCAAAAAACCCCTCAAGACCCGTTT	44
	AGAGGCCCCAAGGGGTTATGCTAGGCTGCGAACA
	ACGAAAGAG
ybeM-up-1	ACAGCCAGAATGCCAGTGC	45
ybeM-up-2	AGTCGTATTAGACGATTATTCGGCGTTACACT	46
ybeM-down-1	CGTTACATCCTCGGCGCTTGATTCACC	47
ybeM-down-2	CGTTTGTCCGCTCTTCTTACC	48
Cmr-ybeM-up	GGGTTTTTTGCGTCTTGAGCGATTGTGTAGG	49
Cmr-ybeM-down	CAAGCGCCGAGGATGTAACGCACTGAGAAGC	50
lysC-up	CGCTTCAATCTAATACGACTCACTATAGGGTCTAGA	51
	AATAATTTTGTTTAACTTTAAGAAGGAGATATACCA
	CAAAGATGGCCCTGGTC
lysC-down	GCTCAAGACGCAAAAAACCCCTCAAGACCCGTTT	52
	AGAGGCCCCAAGGGGTTATGCTAGACTGCGATGGT
	GGTCATTGT
yghX-up-1	GCGCAACGTAGAACAGGAATT	53
yghX-up-2	AGTCGTATTAGATTGAAGCGCCTTTACTACTCC	54
yghX-down-1	CGTTACATCCGTCATAGTAATCCAGCAACTCTTGTG	55
yghX-down-2	GAGCAGGTATTTACGTGAACCG	56
Cmr-yghX-up	GGGTTTTTTGCGTCTTGAGCGATTGTGTAGG	57
Cmr-yghX-down	TTACTATGACGGATGTAACGCACTGAGAAGC	58

EXAMPLE 2

Shake-Flask Fermentation Experiment

The strain E. coli ECT 06 constructed in example 1 was used as a production strain to produce ectonie by fermentation.

(1) Seed culture: a loop of thallus was inoculated into a 500 mL erlenmeyer flask with 30 mL seed medium, and cultured for 7 hours at 37° C. and 200 rpm.

(2) Shake-flask fermentation: the seed solution was inoculated into a 500 mL baffled shake flask with 30 mL fermentation medium according to a inoculum size of 15%, and cultured for 28 hours at 37° C. and 200 rpm; the phenol red was used as an indicator, NH₄OH was supplemented through a microsyringe to kept the pH at 7.2, and 60% (m/v) glucose solution was used for maintaining the fermentation (the phenol red was used as an indicator, and it will be seen as sugar deficiency when the color of the fermentation broth no longer changed, and then 2 ml of 60% glucose solution can be added), the expression of the target gene was induced by adding 60% (m/v) xylose solution (final concentration of xylose in the fermentation broth was 15 g/L) at the initial stage of fermentation, and the fermentation period was 28 h.

(3) Collection of the fermentation broth: the fermentation broth was centrifuged at 13000 rpm, collecting the supernate phase and detecting the content of ectoine. The result showed the yield of ectoine reached 16 g/L after 28 h fermentation in shake flask.

(4) Detection method:

the supernate was diluted 200 times with deionized water and filtered by a 0.22 μm microfiltration membrane, the resulting sample was to be detected; the detection was performed by an UltiMate 3000 (Thermo Scientific) high performance liquid chromatograph using a TSK-GEL C18 chromatographic column with 2% acetonitrile at a flow rate was 1 mL/min as the mobile phase, the column temperature was 30° C., and 20 μL sample was injected by using a trace sample injection needle, the ultraviolet detection wavelength was 210 nm, and the retention time was about 2.953 min.

The seed medium: sucrose 30 g/L, (NH₄)₂SO₄ 5 g/L, KH₂PO₄ 5 g/L, MgSO₄.7H₂O 2 g/L, yeast extract powder 10 g/L, corn steep liquor 3 mL/L, FeSO₄.7H₂O 3 mg/L, MnSO₄.H₂O 3 mg/L, the rest is water, pH7.0.

The fermentation medium: glucose 40 g/L, (NH₄)₂SO₄ 3 g/L, KH₂PO₄ 3 g/L, MgSO₄.7H₂O 2 g/L, yeast extract powder 0.3 g/L, corn steep liquor 2 mL/L, FeSO₄.7H₂O 100 mg/L, MnSO₄.7H₂O 100 mg/L, the rest is water, pH7.0.

EXAMPLE 3

Shake-Flask Fermentation Experiment

The strain E. coli ECT06 constructed in example 1 was used to produce ectonie.

(1) Seed culture: a loop of thallus was inoculated into a 500 mL erlenmeyer flask with 30 mL seed medium, and cultured for 7 hours at 37° C. and 200 rpm.

(2) Shake-flask fermentation: the seed solution was inoculated into a 500 mL baffled shake flask with 30 mL fermentation medium according to a inoculum size of 10%, and cultured for 20 hours at 37° C. and 200 rpm; the phenol red was used as an indicator, and the pH was kept at 7.2 by supplementing NH₄OH, the 60% (m/v) glucose solution was used for maintaining the fermentation (the phenol red was used as an indicator, and the color of the fermentation broth no longer changed meaning sugar deficiency, and then 1 mL of 60% glucose solution was added), the expression of the target gene was induced by adding 60% (m/v) xylose solution (final concentration of xylose in the fermentation broth was 5 g/L) at the initial stage of fermentation, and the fermentation period was 20 h.

(3) Collection of the fermentation broth: the fermentation broth was centrifuged at 13000 rpm, collecting the supernate phase and detecting the content of ectoine. The result showed the yield of ectoine reached 12 g/L after 20 h fermentation in shake flask.

(4) Detection method:

the supernate was diluted 200 times with deionized water and filtered by a 0.22 μm microfiltration membrane, the resulting sample was to be detected; the detection of ectoine was performed by using an UltiMate 3000 (Thermo Scientific) high performance liquid chromatograph, and 20 μL sample was injected with a trace sample injection needle, the chromatographic column was a TSK-GEL C18 chromatographic column, and the column temperature was 30° C., the mobile phase was 2% acetonitrile, the flow rate was 1 mL/min, the ultraviolet detection wavelength was 210 nm, and the retention time was about 2.953 min.

The seed medium: sucrose 20 g/L, (NH₄)₂SO₄ 1 g/L, KH₂PO₄ 1 g/L, MgSO₄.7H₂O 1 g/L, yeast extract powder 5 g/L, corn steep liquor 1 mL/L, FeSO₄.7H₂O 1 mg/L, MnSO₄.H₂O 1 mg/L, the rest is water, pH7.0;

The fermentation medium: glucose 20 g/L, (NH₄)₂SO₄ 1 g/L, KH₂PO₄ 1 g/L, MgSO₄.7H₂O 1 g/L, yeast extract powder 0.1 g/L, corn steep liquor 1 mL/L, FeSO₄.7H₂O 80 mg/L, MnSO₄.7H₂O 80 mg/L, the rest is water, pH7.0.

EXAMPLE 4

Fermentation Experiment in a 5 L Fermentor

Test strain: the strain E. coli ECT06 constructed in example 1.

Control strain: the strain E. coli ECT06 constructed in the Chinese patent application “A Genetically Engineered Bacteria Used for Producing Ectoine as well as the Construction Method and Use Thereof”, application number: 201510410080.2.

Both of the two strains above mentioned were adopted to execute the fermentor fermentation experiment respectively under the same condition to produce ectoine, and the method specifically comprises the following steps:

(1) slant culture: a loop of thallus was scraped off from the strain deposit tube stored in −80° C., and spread evenly on the agar slant culture medium to culture for 15 hours, then transferred into a second-generation agar slant to culture for 12 hours.

(2) seed culture: proper amount of sterile water was added into four tubes of agar slant to make a bacterial suspension, then inoculated into a 7.5 L fermentor with 2 L seed medium and cultured to a cell dry weight of 6 g/L, during the period the pH was stabilized to be about 7.0 by automated addition of NH₄OH, the temperature was kept constantly at 36° C. by temperature electrode, and the dissolved oxygen was 25-35% by variation of the stirrer speed and aeration rate.

(3) fermentor fermentation: the seed liquid was inoculated into a fermentation medium according to a inoculum size of 20%, and cultured for 40 hours, during the period the pH was stabilized to be about 7.0, the temperature was kept constantly at 36° C., and the dissolved oxygen was 25-35%; and when the glucose in the medium was exhausted, a 80% (m/v) glucose solution was added to maintain the glucose concentration in the fermentation medium at 0-2 g/L;

Xylose was added to the fermentation medium at the initial fermentation stage of the test strain with a 15 g/L of final concentration in the fermentation broth to induce the expression of the target gene (there is no addition of xylose in the fermentation process of the control strain).

The slant culture medium: sucrose 3 g/L, tryptone 10 g/L, beef extract 10 g/L, yeast extract 5 g/L, NaCl 5 g/L, agar 30 g/L, the rest is water, pH 7.0-7.2, carrying out high-pressure steam sterilization at 115° C. for 15 minutes.

The seed medium: glucose 30 g/L, yeast extract 10 g/L, tryptone 10 g/L, KH₂PO₄ 15 g/L, MgSO₄.7H₂O 5 g/L, FeSO₄.7H₂O 15 mg/L, MnSO₄.H₂O 15 mg/L, VB1 3 mg/L, VH 1 mg/L, defoamer 2 drops, the rest is water, pH 7.0-7.2, carrying out high-pressure steam sterilization at 115° C. for 15 minutes.

The fermentation medium: glucose 25 g/L, yeast extract 5 g/L, tryptone 5 g/L, sodium citrate 1 g/L, KH₂PO₄ 5 g/L, MgSO₄.7H₂O 1 g/L, FeSO₄.7H₂O 100 mg/L, MnSO₄.H₂O 100 mg/L, VB1 1 mg/L, VH 0.5 mg/L, defoamer 2 drops, the rest is water, pH 7.0-7.2, carrying out high-pressure steam sterilization at 115° C. for 15 minutes.

The results are shown in the following table, FIG. 7 and FIG. 8:

					specific
		Yield of	Substrate		production
		Ectoine	Conversion	Fermentation	rate
Strains	OD600	(g/L)	(%)	Period (h)	(g/L/h)
Control	78.9	25.2	9.8	40	0.63
Strain
Test Strain	83.0	50.1	27.8	40	1.25

EXAMPLE 5

Fermentation Experiment in a 5 L Fermentor

The strain E. coli ECT06 constructed in example 1 was used as the producing strain to produce ectoine, and the method specifically comprises the following steps:

(1) slant culture: a loop of thallus was scraped off from the stain deposit tube stored in −80° C,and spread evenly on the agar slant culture medium to culture 18 hours, then transferred into a second-generation agar slant to culture 12 hours.

(2) seed culture: proper amount of sterile water was added into four tubes of agar slant to make a bacterial suspension, then inoculated into a 7.5 L fermentor with 2 L seed medium and cultured to a cell dry weight of 5 g/L, during the period the pH was stabilized to be about 7.0 by automated addition of NH₄OH, the temperature was kept constantly at 36° C. by temperature electrode, and the dissolved oxygen was 25-35% by variation of the stirrer speed and aeration rate.

(3) fermentor fermentation: the seed liquid was inoculated into a fermentation medium according to an inoculum size of 15%, and cultured for 24 hours, during the period the pH was stabilized to be about 7.0, the temperature was kept at 36° C., and the dissolved oxygen was 25-35%;

the expression of the target gene was induced by adding 5 g/L xylose to the fermentation medium at the initial fermentation stage, and when the glucose in the medium was consumed, a 80% (m/v) glucose solution was added by a mode of fed-batch to maintain the glucose concentration in the fermentation medium at 0-2 g/L.

The concentration of ectoine in the fermentation broth reached 35 g/L after 24 h culture.

The slant culture: sucrose 1 g/L, tryptone 5 g/L, beef extract 5 g/L, yeast extract 2g/L, NaCl 2 g/L, agar 15 g/L, the rest is water, pH 7.0-7.2, carrying out high-pressure steam sterilization at 115° C. for 15 minutes.

The seed medium: glucose 15 g/L, yeast extract 5 g/L, tryptone 5 g/L, KH₂PO₄ 5 g/L, MgSO₄.7H₂O 2 g/L, FeSO₄.7H₂O 5 mg/L, MnSO₄.H₂O 5 mg/L, VB1 1 mg/L, VH 0.1 mg/L, defoamer 2 drops, the rest is water, pH 7.0-7.2, carrying out high-pressure steam sterilization at 115° C. for 15 minutes.

The fermentation medium: glucose 15 g/L, yeast extract 1 g/L, tryptone 1 g/L, sodium citrate 0.1 g/L, KH₂PO₄ 1 g/L, MgSO₄.7H₂O 0.1 g/L, FeSO₄.7H₂O 80 mg/L, MnSO₄.H₂O 80 mg/L, VB1 0.5 mg/L, VH 0.1 mg/L, defoamer 2 drops, the rest is water, pH 7.0-7.2, carrying out high-pressure steam sterilization at 115° C. for 15 minutes.

Claims

1. A genetically engineered bacteria used for producing ectoine, wherein, the genetically engineered bacteria is E. coli ECT06 containing an ectABC gene promoted by a promoter T7 and from Halomonas elongata; deletions of thrA and iclR genes; a lysC gene promoted by a promoter T7 and from Corynebacterium glutamicum; a ppc gene promoted by a promoter trc; and a RNA polymerase from T7 bacteriophage and promoted by a promoter PxylF of xylose transporter coding gene xylF.

2. The genetically engineered bacteria used for producing ectoine according to claim 1, wherein, the host cell of the genetically engineered bacteria is E. coli W3110, the deposit number is ATCC 27325.

3. The genetically engineered bacteria used for producing ectoine according to claim 1, wherein, the deposit number of the Halomonas elongata is CGMCC No. 1.6329.

4. The genetically engineered bacteria used for producing ectoine according to claim 1, wherein, the nucleotide sequence of the ectABC gene is a sequence shown in a sequence table as SEQ ID No.1;the nucleotide sequence of the lysC gene is a sequence shown in a sequence table as SEQ ID No.2;the nucleotide sequence of the thrA gene is a sequence shown in a sequence table as SEQ ID No.3;the nucleotide sequence of the iclR gene is a sequence shown in a sequence table as SEQ ID No.4;the nucleotide sequence of the promoter T7 is a sequence shown in a sequence table as SEQ ID No.5;the nucleotide sequence of the promoter trc is a sequence shown in a sequence table as SEQ ID No.7;the nucleotide sequence of the ppc gene is a sequence shown in a sequence table as SEQ ID No.8;the nucleotide sequence of the PxylF is a sequence shown in a sequence table as SEQ ID No.9;the nucleotide sequence of the RNA polymerase from T7 bacteriophage is a sequence shown in a sequence table as SEQ ID No.10.

5. A construction method of the genetically engineered bacteria used for producing ectoine of claim 1, wherein, comprising the following steps: (1) knocking out the thrA and iclR genes of the starting strain E. coli W3110;(2) replacing the promoter of ppc gene with promoter trc;(3) expressing the T7 RNA polymerase: constructing a gene fragment by ligating the promoter PxylF of xylose transporter coding gene xylF and T7 RNA polymerase, and expressing it;(4) constructing the metabolic pathway from aspartate to ectoine:{circle around (1)} constructing a gene fragment T7-ectABC by ligating promoter T7 and ectABC gene, and expressing it;{circle around (2)} constructing a gene fragment T7-lysC by ligating promoter T7 and lysC gene, and expressing it.

6. A use of the genetically engineered bacteria used for producing ectoine of claim 1.

7. The use of the genetically engineered bacteria used for producing ectoine according to claim 6, wherein, a production method of ectoine by shake-flask fermentation comprises the following steps: (1) seed culture: inoculating the slant cultured cells into a seed culture medium, and culturing for 7 hours at 37° C. and 200 rpm;(2) shake-flask fermentation: inoculating the seed liquid into a fermentation medium according to a inoculum size of 10-15%, and culturing for 20-28 hours at 37° C. and 200 rpm; maintaining the pH to be 7.2, using 60% glucose solution to maintain the fermentation, adding a xylose solution with a final concentration of 5-15 g/L at the beginning of the fermentation to induce the expression of the target gene.

8. The use of the genetically engineered bacteria used for producing ectoine according to claim 7, wherein, the seed culture medium: sucrose 20-30 g/L, (NH4)2SO4 1-5 g/L, KH2PO4 1-5 g/L, MgSO4.7H2O 1-2 g/L, yeast extract powder 5-10 g/L, corn steep liquor 1-3 mL/L, FeSO4.7H2O 1-3 mg/L, MnSO4H2O 1-3 mg/L, the rest is water, pH7.0;the fermentation medium: glucose 20-40 g/L, (NH4)2SO4 1-3 g/L, KH2PO4 1-3 g/L, MgSO4.7H2O 1-2 g/L, yeast extract powder 0.1-0.3 g/L, corn steep liquor 1-2 mL/L, FeSO4.7H2O 80-100 mg/L, MnSO4.7H2O 80-100 mg/L, the rest is water, pH7.0.

9. The use of the genetically engineered bacteria used for producing ectoine according to claim 6, wherein, a production method of ectoine by fermentor fermentation comprises the following steps: (1) slant culture: scraping a loop of thallus from the tube stored in −80° C., and spreading it evenly on an agar slant culture medium to subject to a culture of 37° C. for 15-18 hours, and then transferring into a second-generation agar slant to subject to a culture for 12 hours;(2) seed culture: adding proper amount of sterile water into the agar slant to make a bacterial suspension, then inoculating into a seed medium and culturing to a cell dry weight of 5-6 g/L, during the period stabilizing the pH at 7.0, keeping the temperature constantly at 36° C., and the dissolved oxygen is 25-35%.(3) fermentor fermentation: inoculating the seed liquid into a fresh fermentation medium according to a inoculum size of 15-20%, and culturing for 24-40 hours, during the period stabilizing the pH at 7.0, keeping the temperature constantly at 36° C., and the dissolved oxygen is 25-35%;adding 5-15 g/L of xylose solution to the fermentation medium at the initial stage to induce the expression of the target gene, and adding 80% glucose solution to maintain the glucose concentration in the fermentation medium at 0-2 g/L after the glucose in the medium is consumed, and the fermentation period is 24-40 hours.

10. The use of the genetically engineered bacteria used for producing ectoine according to claim 9, wherein, the agar slant culture medium: sucrose 1-3 g/L, Tryptone 5-10 g/L, beef extract 5-10 g/L, yeast extract 2-5 g/L, NaCl 2-5 g/L, agar 15-30 g/L, the rest is water, pH 7.0-7.2, carrying out high-pressure steam sterilization at 115° C. for 15 minutes;the seed medium: glucose 15-30 g/L, yeast Extract 5-10 g/L, Tryptone 5-10 g/L, KH2PO4 5-15 g/L, MgSO4.7H2O 2-5 g/L, FeSO4.7H2O 5-15 mg/L, MnSO4.H2O 5-15 mg/L, VB1 1-3 mg/L, VH 0.1-1 mg/L, defoamer 2 drops, the rest is water, pH 7.0-7.2, carrying out high-pressure steam sterilization at 115° C. for 15 minutes;the fermentation medium: glucose 15-25 g/L, yeast extract 1-5 g/L, Tryptone 1-5 g/L, sodium citrate 0.1-1 g/L, KH2PO4 1-5 g/L, MgSO4.7H2O 0.1-1 g/L, FeSO4.7H2O 80-100 mg/L, MnSO4.H2O 80-100 mg/L, VB1 0.5-1 mg/L, VH 0.1-0.5 mg/L, defoamer 2 drops, the rest is water, pH 7.0-7.2, carrying out high-pressure steam sterilization at 115° C. for 15 minutes.