Patent Application
20220049212
The present disclosure relates to a mutant strain having enhanced L-glutamic acid productivity and a method of producing L-glutamic acid using the same, and more particularly, to a Corynebacterium sp. mutant strain having reduced production of citramalate as a by-product due to weakening or inactivation of the activity of citramalate synthase and having increased L-glutamic acid productivity, and a method of producing L-glutamic acid using the same.
L-glutamic acid is a typical amino acid that is produced by microbial fermentation. Monosodium L-glutamate (MSG) may increase the preference of foods such as meat, fish, chicken, vegetables, sauces, soups and seasonings by balancing and harmonizing the overall taste of the food, may enhance the taste of low-salt foods having a salt content reduced up to 30%, and thus is widely used as a household seasoning and a seasoning for the production of processed food.
L-glutamic acid is usually produced by fermentation using mainly Brevibacterium sp. or Corynebacterium sp. strains and mutant strains thereof. In order to increase the production of L-glutamic acid by microbial culture, there has been used a method of increasing the copy number of the gene of interest to increase the expression of the gene in the L-glutamic acid biosynthesis pathway or a method of regulating the activity of the enzyme in the biosynthesis pathway by modifying the promoter of the gene. Specifically, it was disclosed that L-glutamic acid production was increased by amplifying a specific gene such as pyc gene or fasR (U.S. Pat. No. 6,852,516) or manipulating the promoter region of each of gdh, gltA, icd, pdh and argG genes (U.S. Pat. No. 6,962,805).
Citramalate synthase (cimA) is an enzyme that synthesizes citramalate using acetyl-CoA and pyruvate as substrates. It is known that the cimA gene does not exist in Corynebacterium glutamicum, and the leuA gene having high homology to the cimA gene plays the role of citramalate synthase in Corynebacterium glutamicum.
Since acetyl-CoA is used as a substrate in the fermentation pathway of L-glutamic acid, the present inventors have attempted to weaken or inactivate the activity of citramalate synthase to save the substrate acetyl-CoA, thereby further increasing L-glutamic acid productivity.
Meanwhile, it has been reported that the yggB gene of coryneform bacteria is a homologue of the yggB gene of Escherichia coli (FEMS Microbiol Lett., 2003, 218(2), pp. 305-309, and Mol Microbiol., 2004, 54(2), pp. 420-438), and is a kind of mechanosensitive channel (EMBO J., 1999, 18(7):1730-7). As a method of imparting L-glutamic acid-producing ability to coryneform bacteria, a mutation is specifically disclosed in the present disclosure. The effect of this mutation on L-glutamic acid production has not been reported.
Accordingly, the present inventors have constructed a mutant strain in which the activity of citramalate synthase has been weakened or inactivated, and a mutant strain having an additional mutation induced in the YggB protein which is involved in glutamic acid release, and have found that the mutant strains have excellent L-glutamic acid productivity, thereby completing the present disclosure.
Korean Patent No. 10-1138289
An object of the present disclosure is to provide a Corynebacterium sp. mutant strain in which the activity of citramalate synthase has been weakened or inactivated and which has enhanced L-glutamic acid productivity.
Another object of the present disclosure is to provide a method for producing L-glutamic acid, the method comprising steps of:
(a) culturing the Corynebacterium sp. mutant strain in a medium; and
(b) recovering L-glutamic acid from the cultured mutant strain or the medium.
One aspect of the present disclosure provides a Corynebacterium sp. mutant strain in which the activity of citramalate synthase has been weakened or inactivated and which has enhanced L-glutamic acid productivity.
In the present disclosure, the term “citramalate synthase” refers to an enzyme that catalyzes the conversion of acetyl-CoA and pyruvate into citramalate and coenzyme A.
In the present disclosure, the strain having “enhanced productivity” means that L-glutamic acid productivity of the strain is higher than that of a parent strain thereof.
In the present disclosure, the term “parent strain” refers to a wild-type strain or mutant strain to be mutated, and includes a strain that is to be mutated directly or to be transformed with a recombinant vector or the like. In the present disclosure, the parent strain may be a wild-type Corynebacterium glutamicum strain or a strain mutated from the wild-type strain. Preferably, the parent strain may be a Corynebacterium glutamicum KCTC 11558BP strain.
According to one embodiment of the present disclosure, the Corynebacterium sp. mutant strain having enhanced L-glutamic acid productivity may have weakened or inactivated activity of citramalate synthase compared to the parent strain thereof.
In the present disclosure, the term “weakened activity” means that the enzymatic activity of citramalate synthase in the cell has decreased compared to that in a parent strain such as a wild-type strain or a strain before modification. The term “weakened” also includes: a case in which the activity of the enzyme itself has decreased compared to the activity of the enzyme in the parent microorganism due to a mutation in the gene encoding the enzyme; a case in which the overall activity of the enzyme in the cell is lower than that in the wild-type strain or the strain before modification, by a reduced expression level of due to inhibited transcription or translation of the gene encoding the enzyme; and a combination thereof. In addition, in the present disclosure, the term “inactivated” means that the gene encoding citramalate synthase is not expressed at all compared to that in the wild-type strain or the strain before modification, or that the gene has no activity even though it is expressed.
According to one embodiment of the present disclosure, weakening or inactivation of the enzymatic activity of citramalate synthase may be achieved by applying various methods well known in the art. Examples of these methods include, but are not limited to, a method of replacing the gene encoding the enzyme on the chromosome with a mutated gene so that the activity of the enzyme is decreased, including a case where the activity of the enzyme is completely removed; a method of introducing a mutation into the expression control sequence (e.g., a promoter) of the gene encoding the enzyme on the chromosome; a method of replacing the expression control sequence of the gene encoding the enzyme with a weakly active or inactive sequence; a method of deleting all or part of the gene encoding the enzyme on the chromosome; a method of introducing an antisense oligonucleotide (e.g., antisense RNA) that binds complementarily to the transcript of the gene on the chromosome and inhibits translation of the mRNA into the enzyme; a method of making the attachment of ribosomes impossible by artificially adding a sequence complementary to the SD sequence to the front end of the SD sequence of the gene encoding the enzyme to form a secondary structure; a reverse transcription engineering (RTE) method of adding a promoter to the 3′ end of the open reading frame (ORF) of the corresponding sequence so as to be reverse-transcribed; and combinations thereof.
According to one embodiment of the present disclosure, citramalate synthase may be encoded by 2-isopropylmalate synthase (leuA) gene.
It is known that the 2-isopropylmalate synthase (leuA) gene that is used in the present disclosure has high homology to the citramalate synthase (cimA) gene and plays the role of citramalate synthase in a Corynebacterium sp. strain. According to one embodiment of the present disclosure, the leuA gene consists of the nucleotide sequence of SEQ ID NO: 14.
According to one embodiment of the present disclosure, weakening or inactivation of the activity of citramalate synthase may be weakening or inactivation of the activity of citramalate synthase due to decreased expression of the leuA gene encoding citramalate synthase.
In the present disclosure, the term “decreased expression” means that the expression level of the gene is decreased compared to the original expression level, and includes a case where the expression is completely inhibited, so that the expression does not occur. When gene expression in a microorganism is to be deceased, the expression may be decreased by replacing the translation initiation codon of the gene or genetically manipulating the existing gene to reduce the expression level thereof. The method of modifying the sequence to control expression may be performed by inducing mutation in the expression control sequence in the nucleic acid sequence of the expression control sequence by deletion, insertion, non-conservative or conservative substitution, or a combination thereof, or by replacing the promoter with a weaker promoter. Examples of the expression control sequence includes, but is not limited to, a promoter, an operator sequence, a sequence encoding a ribosome binding site, and a sequence for controlling termination of transcription and translation. When a gene whose expression is to be decreased is present in a microorganism to be mutated, it is possible to decrease expression of the gene, for example, by replacing a native promoter that drives expression of the gene with a weak promoter or by introducing mutation. Furthermore, it is possible to decrease expression of the gene by deleting all or part of the existing gene.
According to one embodiment of the present disclosure, decreasing the expression of the leuA gene may be performed by inducing mutation into the nucleic acid sequence by deletion, insertion, non-conservative or conservative substitution, or a combination thereof, or replacing the promoter with a weaker promoter.
In the leuA gene-deleted Corynebacterium sp. mutant strain according to one embodiment of the present disclosure, the production of citramalate as a by-product may decrease compared to that in the parent strain, and L-glutamic acid production may increase by saving acetyl-CoA.
According to one embodiment of the present disclosure, the Corynebacterium sp. mutant strain may have an additional mutation caused by substitution of alanine or valine for at least one leucine selected from the group consisting of leucine at amino acid position 93 and leucine at amino acid position 109 in the amino acid sequence of a YggB protein represented by SEQ ID NO: 15.
In the present disclosure, the yggB gene refers to a gene encoding a mechanosensitive channel. The yggB gene corresponds to a sequence complementary to a sequence of 1,336,092 to 1,337,693 in the genomic sequence registered under Genbank Accession No. NC 003450 in the NCBI database, and is also called NCg11221. The YggB protein encoded by the yggB gene is registered under Genbank Accession No. NP 600492. According to one embodiment of the present disclosure, the YggB protein encoded by the yggB gene consists of the amino acid sequence of SEQ ID NO: 15.
According to one embodiment of the present disclosure, due to the mutation caused by substitution of alanine or valine for at least one leucine selected from the group consisting of leucine at amino acid position 93 and leucine at amino acid position 109 in the amino acid sequence of the YggB protein represented by SEQ ID NO: 15, a methyl group which is involved in the pore of the YggB protein, from which L-glutamic acid may be released, is removed, so that the diameter of the pore may be increased, whereby the strain having the mutation may have enhanced L-glutamic acid productivity.
Specifically, the mutant strain may include a mutant of the YggB protein due to mutation, or may be transformed with a vector containing a polynucleotide encoding the mutant of the YggB protein.
In the present disclosure, the term “vector” refers to any vehicle for the cloning of and/or transfer of a nucleic acid into a host cell. The vector may be a replicon to which another DNA fragment may be attached so as to bring about the replication of the attached fragment. The term “Replicon” refers to any genetic element (e.g., plasmid, phage, cosmid, chromosome, virus) that functions as an autonomous unit of DNA replication in vivo, i.e., capable of replication under its own control. In the present disclosure, the vector is not particularly limited as long as it may replicate in a host, and any vector known in the art may be used. The vector used for the construction of the recombinant vector may be a plasmid, cosmid, virus or bacteriophage in a native state or a recombinant state. Example of a phage vector or cosmid vector that may be used include pWE15, M13, λEMBL3, λEMBL4, λFIXII, λDASHII, λZAPII, λgt10, λgt11, Charon4A, and Charon21A, and examples of a plasmid vector that may be used include a pDZ vector, and pBR-based, pUC-based, pBluescriptll-based, pGEM-based, pTZ-based, pCL-based and pET-based vectors. A vector that may be used is not particularly limited, and a known expression vector may be used, but is not limited thereto.
In the present disclosure, the term “transformation” means introducing a gene into a host cell so that the gene may be expressed in the host cell. For the transformed gene, it does not matter whether the gene is inserted into the chromosome of the host cell or located outside of the chromosome, as long as the gene may be expressed in the host cell.
The Corynebacterium sp. mutant strain having a deletion of the leuA gene and a mutation in the YggB protein according to one embodiment of the present disclosure may have increased L-glutamic acid production than the parent strain thereof and require a shortened culturing time for L-glutamic acid production, and thus may efficiently produce L-glutamic acid.
According to one embodiment of the present disclosure, the Corynebacterium sp. strain may be Corynebacterium glutamicum.
According to one embodiment of the present disclosure, the Corynebacterium sp. strain may be, but is not limited to, Corynebacterium ammoniagenes, Corynebacterium acetoacidophilum, Corynebacterium acetoglutamicum, Corynebacterium alkanolyticum, Corynebacterium callunae, Corynebacterium lilium, Corynebacterium melassecola, Corynebacterium thermoaminogenes, Corynebacterium efficiens, or Corynebacterium herculis.
According to one embodiment of the present disclosure, the Corynebacterium sp. strain is most preferably Corynebacterium glutamicum KCTC 11558BP.
Another aspect of the present disclosure provides a method for producing L-glutamic acid, the method comprising steps of:
(a) culturing the Corynebacterium sp. mutant strain in a medium; and
(b) recovering L-glutamic acid from the cultured mutant strain or the medium.
According to one embodiment of the present disclosure, the culturing may be performed using a suitable medium and culture conditions known in the art, and any person skilled in the art may easily adjust and use the medium and the culture conditions. Specifically, the medium may be a liquid medium, but is not limited thereto. Examples of the culturing method include, but are not limited to, batch culture, continuous culture, fed-batch culture, or a combination thereof.
According to one embodiment of the present disclosure, the medium should meet the requirements of a specific strain in a proper manner, and may be appropriately modified by a person skilled in the art. For the culture medium for the Corynebacterium sp. strain, reference may be made to, but not limited to, a known document (Manual of Methods for General Bacteriology, American Society for Bacteriology, Washington D.C., USA, 1981).
According to one embodiment of the present disclosure, the medium may contain various carbon sources, nitrogen sources, and trace element components. Examples of carbon sources that may be used include: sugars and carbohydrates such as glucose, sucrose, lactose, fructose, maltose, starch, and cellulose; oils and fats such as soybean oil, sunflower oil, castor oil, and coconut oil; fatty acids such as palmitic acid, stearic acid, and linoleic acid; alcohols such as glycerol and ethanol, and organic acids such as acetic acid. These substances may be used individually or as a mixture, but are not limited thereto. Examples of nitrogen sources that may be used include peptone, yeast extract, meat extract, malt extract, corn steep liquor, soybean meal, urea, or inorganic compounds such as ammonium sulfate, ammonium chloride, ammonium phosphate, ammonium carbonate, and ammonium nitrate. The nitrogen sources may also be used individually or as a mixture, but are not limited thereto. Examples of phosphorus sources that may be used include, but are not limited to, potassium dihydrogen phosphate or dipotassium hydrogen phosphate or the corresponding sodium salts. In addition, the culture medium may contain, but is not limited to, metal salts such as magnesium sulfate or iron sulfate, which are required for growth. In addition, the culture medium may contain essential growth substances such as amino acids and vitamins. Moreover, suitable precursors may be used in the culture medium. The medium or individual components may be added to the culture medium batchwise or in a continuous manner by a suitable method during culturing, but are not limited thereto.
According to one embodiment of the present disclosure, the pH of the culture medium may be adjusted by adding compounds such as ammonium hydroxide, potassium hydroxide, ammonia, phosphoric acid and sulfuric acid to the microorganism culture medium in an appropriate manner during the culturing. In addition, during the culturing, foaming may be suppressed using an anti-foaming agent such as a fatty acid polyglycol ester. Additionally, to keep the culture medium in an aerobic condition, oxygen or an oxygen-containing gas (for example, air) may be injected into the culture medium. The temperature of the culture medium may be generally 20° C. to 45° C., for example, 25° C. to 40° C. The culturing may be continued until a desired amount of a useful substance is produced. For example, the culturing time may be 10 hours to 160 hours.
According to one embodiment of the present disclosure, in the step of recovering L-glutamic acid from the cultured mutant strain and the culture medium, the produced L-glutamic acid may be collected or recovered from the medium using a suitable method known in the art depending on the culture method. Examples of the method for collecting or recovering L-glutamic acid include, but are not limited to, centrifugation, filtration, extraction, spraying, drying, evaporation, precipitation, crystallization, electrophoresis, fractional dissolution (e.g., ammonium sulfate precipitation), chromatography (e.g., ion exchange, affinity, hydrophobicity and size exclusion).
According to one embodiment of the present disclosure, the step of recovering L-glutamic acid may be performed by centrifuging the culture medium at a low speed to remove biomass and separating the obtained supernatant through ion-exchange chromatography.
According to one embodiment of the present disclosure, the step of recovering L-glutamic acid may include a process of purifying L-glutamic acid.
The mutant strain according to one embodiment of the present disclosure has reduced production of citramalate as a by-product due to weakening or inactivation of the activity of citramalate synthase and has excellent L-glutamic acid productivity. In addition, the strain having an additional mutation in the YggB protein may produce L-glutamic acid in an improved yield due to enhancement of glutamic acid release. Thus, when the mutant strain is used, it is possible to more effectively produce L-glutamic acid.
Hereinafter, one or more embodiments will be described in more detail with reference to examples. However, these examples serve to illustratively describe one or more embodiments, and the scope of the present disclosure is not limited to these examples.
The Corynebacterium glutamicum KCTC 11558BP strain, which is a mutant strain obtained by chemically treating an strain with nitrosoguanidine (NTG) that causes DNA mutation, has molasses resistance, and thus may produce L-glutamic acid in high yield by using inexpensive molasses as a main carbon source (Korean Patent Application Publication No. 10-2011-0034718).
Corynebacterium glutamicum 16 (hereinafter referred to as 16) and Corynebacterium glutamicum KCTC 11558BP (hereinafter referred to as KCTC 11558BP) having the ability to produce glutamic acid were analyzed for the amount of metabolites and L-glutamic acid in the cells.
Each of KCTC 11558BP and 16 was inoculated into 25 ml of CM liquid medium (containing, per liter, 1% glucose, 1% polypeptone, 0.5% yeast extract, 0.5% beef extract, 0.25% NaCl, 0.2% urea, 50% NaOH 100 l, pH 6.8), and then cultured with shaking at 200 rpm at 30° C. When cell growth reached an exponential phase during culture, cells were separated from the culture medium by rapid vacuum filtration (Durapore HV, 0.45 m; Millipore, Billerica, Mass.). The filter having the cells adsorbed thereon was washed twice with 10 ml of cooling water, and then immersed in methanol containing 5 M morpholine ethanesulfonic acid and 5 M methionine sulfone for 10 minutes to stop the reaction. The extract obtained therefrom was mixed with the same amount of chloroform and a 0.4-fold volume of water, and then only the aqueous phase was applied to a spin column to remove protein contaminants. The relative amount of citramalate in the filtered extract was analyzed using capillary electrophoresis mass spectrometry, and the results are shown in Table 1 below.
In addition, L-glutamic acid production was analyzed by performing high performance liquid chromatography (HPLC; Agilent, USA) using a C18 column (Apollo C18, 5 μm, 150 mm×4.6 mm). The results are shown in Table 1 below. An analysis buffer containing 8.85 g/L of KH2PO4, 1.652 g/L of tetrabutyl ammonium hydroxide solution, 10 ml/L of acetonitrile and 12.5 mg/L of sodium azide and having a pH of 3.15 (adjusted with phosphoric acid) was used after filtration through a 0.45 μm membrane-filter (HA).
As shown in Table 1 below, it was confirmed that the amount of citramalate produced by KCTC 11558BP increased by about 3 times compared to that produced by the control 16.
Corynebacterium glutamicum KCTC 11558BP having L-glutamic acid-producing ability was used for disruption of the leuA gene (NCg10245) in Corynebacterium glutamicum.
The chromosomal DNA of the Corynebacterium glutamicum KCTC 11558BP strain was isolated. Using the isolated DNA as a template, PCR was performed using each of a set of primers 1 and 2 and a set of primers 3 and 4 for 30 cycles, each consisting of 95° C. for 30 sec, 57° C. for 30 sec, and 72° C. for 60 sec. The obtained PCR products (H1 and H2 in
The purified PCR products were then used as a template for crossover polymerase chain reaction (PCR) and amplified again using a set of primers 1 and 4.
The 1600-bp crossover PCR product for deleting the leuA gene was purified, digested with Xbal and Sall restriction enzymes (Takara, Japan), and then cloned into a pK19mobSacB vector (Gene, 145: 69-73, 1994) digested with the same restriction enzymes, thereby constructing a vector for disruption of the leuA gene. The constructed vector was named pKLA.
Using the method of van der Rest (Appl. Microbiol. Biotechnol., 52, 541-545, 1999), the vector pKLA constructed in Example 2-1 was introduced by electroporation into the Corynebacterium glutamicum KCTC 11558BP strain (hereinafter referred to as KCTC 11558BP) made electrocompetent by an electrocompetent cell preparation.
Specifically, the KCTC 11558BP strain was first cultured in 100 ml of a 2YT medium (16 g/l tryptone, 10 g/l yeast extract, 5 g/l sodium chloride) supplemented with 2% glucose, and 1 mg/ml of isonicotinic acid hydrazine and 2.5% glycine were added to the same medium free of glucose. Then, the seed culture medium was inoculated to reach an OD610 value of 0.3, and then cultured for at 18° C. and 180 rpm for 12 to 16 hours until the OD610 value reached 1.2 to 1.4. After keeping on ice for 30 minutes, centrifugation was performed at 4,000 rpm at 4° C. for 15 minutes. Thereafter, the supernatant was discarded and the precipitated KCTC 11558BP strain was washed 4 times with a 10% glycerol solution and finally re-suspended in 0.5 ml of a 10% glycerol solution. Electroporation was performed using a Bio-Rad electroporator. The competent cells prepared by the above-described method were placed in an electroporation cuvette (0.2 mm), and the pKLA vector constructed in Example 2-1 was added thereto, followed by electroporation under the conditions of 2.5 kV, 200Ω and 12.5 ρF. Immediately after completion of the electroporation, 1 ml of a regeneration medium (18.5 g/l brain heart infusion, 0.5 M sorbitol) was added to the cells which were then heat-treated at 46° C. for 6 minutes. Next, the cells were cooled at room temperature, transferred into a 15-ml cap tube, incubated at 30° C. for 2 hours, and plated on a selection medium (5 g/l tryptone, 5 g/l NaCl, 2.5 g/l yeast extract, 18.5 g/l brain heart infusion powder, 15 g/l agar, 91 g/l sorbitol, 20 μg/l kanamycin). The cells were cultured at 30° C. for 72 hours, and the generated colonies were cultured in BHI medium until a stationary phase to induce secondary recombination. Then, the cells were diluted to 10−5 to 10−7 cells, and plated on an antibiotic-free plate (containing 10% sucrose), and a strain having no kanamycin resistance and grown in the medium containing 10% sucrose was selected. The selected strain was confirmed to be an leuA gene-deleted Corynebacterium glutamicum strain using a set of primers 1 and 4 described in Table 2 above, and the leuA gene-deleted strain was name “I10”.
The leuA-deleted strain (hereinafter referred to as I10) constructed in Example 2-2 becomes a leucine auxotrophic strain due to deletion of the leuA gene. To confirm this fact, the strain was plated in each of a minimal medium prepared to have the composition shown in Table 3 below and the minimal medium supplemented with leucine and then was cultured at 30° C. for 24 hours, and the degree of growth thereof was measured. The results are shown in Table 4 below.
As shown in Table 4 below, the growth of the 110 strain decreased rapidly compared to the growth of the parent strain Corynebacterium glutamicum KCTC 11558BP strain in the minimal medium not supplemented with leucine, and was restored in the minimal medium supplemented with leucine. Thus, the deletion of the leuA gene in the 110 strain was confirmed.
Using an active plate medium prepared to have the composition shown in Table 5 below, each of the leuA-deleted strain (hereinafter referred to as I10) and Corynebacterium glutamicum KCTC 11558BP (hereinafter referred to as KCTC 11558BP) was cultured at 30° C. for 24 hours. Thereafter, 10 ml of an L-glutamic acid flask medium prepared to have the composition shown in Table 6 below was placed in a 100-ml flask and inoculated with a loop of each of the cultured strains which were then cultured at 30° C. and 200 rpm for 48 hours. After completion of culture, the cultures were used to perform the analysis of L-glutamic acid production and intracellular metabolites. The analysis of L-glutamic acid production and relative citramalate amount was performed in the same manner as described in Example 1.
Table 7 below shows the L-glutamic acid production and relative citramalate amount in each of I10 and KCTC 11558BP. As shown in Table 7, it could be confirmed that, in the I10 strain, the L-glutamic acid production increased and the relative citramalate amount significantly decreased.
Since it was confirmed from the results of metabolite analysis of the leuA-deleted strain (I10) that a lot of L-glutamic acid was accumulated inside the cells, the present inventors attempted to enhance the release of L-glutamic acid.
It is known that YggB is a mechanosensitive channel homolog and plays an important role in the release of L-glutamic acid in Corynebacterium glutamicum. The amino acid sequence of YggB protein is set forth in SEQ ID NO: 15.
As shown in
The chromosomal DNA of the Il0 strain constructed in Example 2-2 was isolated. Using the isolated DNA as a template, PCR was performed using each of a set of primers 5 and 6 and a set of primers 7 and 8 for 30 cycles, each consisting of 95° C. for 30 sec, 57° C. for 30 sec, and 72° C. for 60 sec. The obtained PCR products were purified. The purified PCR products were used as a template and amplified by crossover PCR using primers 5 and 8. The amplified product was sequenced to confirm mutation, and then digested with Xbal and Sall restriction enzymes (Takara, Japan). A pK19mobSacB vector was digested with the same restriction enzymes and ligated with the amplified crossover PCR product, thereby constructing a vector. The constructed vector was named pKY93. The primer sequences used are shown in Table 8 below.
In the same manner as in Example 2-2, the pKY93 vector was introduced into the 110 strain, and the transformed strain was selected and named 110-93. The 110-93 mutant strain had a substitution of alanine for leucine at amino acid position 93 in the YggB protein.
As shown in
The chromosomal DNA of the I10 strain constructed in Example 2-2 was isolated. Using the isolated DNA as a template, PCR was performed using each of a set of primers 5 and 9 and a set of primers 10 and 8 for 30 cycles, each consisting of 95° C. for 30 sec, 57° C. for 30 sec, and 72° C. for 60 sec. The obtained PCR products were purified. The purified PCR products were used as a template and amplified by crossover PCR using primers 5 and 8. The amplified product was sequenced to confirm mutation, and then digested with Xbal and Sall restriction enzymes (Takara, Japan). A pK19mobSacB vector was digested with the same restriction enzymes and ligated with the amplified crossover PCR product, thereby constructing a vector. The constructed vector was named pKY109. The primer sequences used are shown in Table 8 above.
In the same manner as in Example 2-2, the pKY109 vector was introduced into the I10 strain, and the transformed strain was selected and named 110-109. The 110-109 mutant strain had a substitution of alanine for leucine at amino acid position 109 in the YggB protein.
The amount of L-glutamic acid produced by each of the I10, 110-93 and 110-109 strains at the flask scale and the time required for production of L-glutamic acid were measured in the same manner as in Examples 1 and 3, and the results are shown in Table 9 below.
As shown in Table 9 above, the L-glutamic acid production in each of the 110-93 and 110-109 mutant strains in which enlargement of the pore of the YggB protein was induced increased compared to that in the I10 strain. In particular, in the case of the 110-109 strain, the L-glutamic acid production significantly increased compared to that in the I10 strain, and the fermentation time was also shortened from 48 hours to 44 hours, indicating that the 110-109 strain may efficiently produce L-glutamic acid.
| Number | Date | Country | Kind |
|---|---|---|---|
| 10-2018-0161190 | Dec 2018 | KR | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/KR2019/017124 | 12/5/2019 | WO | 00 |
