Native promoters of <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis> and its application in <Emphasis Type="SmallCaps">l</Emphasis>-lysine production

Objective

To identify useful native promoters of Corynebacterium glutamicum for fine-tuning of gene expression in metabolic engineering.

Results

Sixteen native promoters of C. glutamicum were characterized. These promoters covered a strength range of 31-fold with small increments and exhibited relatively stable activity during the whole growth phase using β-galactosidase as the reporter. The mRNA level and enzymatic activity of the lacZ reporter gene exhibited high correlation (R ² = 0.96) under the control of these promoters. Sequence analysis found that strong promoters had high similarity of the -10 hexamer to the consensus sequence and preference of the AT-rich UP element upstream the -35 region. To test the utility of the promoter library, the characterized native promoters were applied to modulate the sucCD-encoded succinyl-CoA synthetase expression for l-lysine overproduction.

Conclusions

The native promoters with various strengths realize the efficient and precise regulation of gene expression in metabolic engineering of C. glutamicum.

     

Genome shuffling and high-throughput screening of <Emphasis Type="Italic">Brevibacterium flavum</Emphasis> MDV1 for enhanced <Emphasis Type="SmallCaps">l</Emphasis>-valine production

l-valine is an essential branched-amino acid that is widely used in multiple areas such as pharmaceuticals and special dietary products and its use is increasing. As the world market for l-valine grows rapidly, there is an increasing interest to develop an efficient l-valine-producing strain. In this study, a simple, sensitive, efficient, and consistent screening procedure termed 96 well plate-PC-HPLC (96-PH) was developed for the rapid identification of high-yield l-valine strains to replace the traditional l-valine assay. l-valine production by Brevibacterium flavum MDV1 was increased by genome shuffling. The starting strains were obtained using ultraviolet (UV) irradiation and binary ethylenimine treatment followed by preparation of protoplasts, UV irradiation inactivation, multi-cell fusion, and fusion of the inactivated protoplasts to produce positive colonies. After two rounds of genome shuffling and the 96-PH method, six l-valine high-yielding mutants were selected. One genetically stable mutant (MDVR2-21) showed an l-valine yield of 30.1 g/L during shake flask fermentation, 6.8-fold higher than that of MDV1. Under fed-batch conditions in a 30 L automated fermentor, MDVR2-21 accumulated 70.1 g/L of l-valine (0.598 mol l-valine per mole of glucose; 38.9% glucose conversion rate). During large-scale fermentation using a 120 m³ fermentor, this strain produced?>?66.8 g/L l-valine (36.5% glucose conversion rate), reflecting a very productive and stable industrial enrichment fermentation effect. Genome shuffling is an efficient technique to improve production of l-valine by B. flavum MDV1. Screening using 96-PH is very economical, rapid, efficient, and well-suited for high-throughput screening.     

Characterization of aspartate kinase and homoserine dehydrogenase from <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis> IWJ001 and systematic investigation of <Emphasis Type="SmallCaps">l</Emphasis>-isoleucine biosynthesis

Previously we have characterized a threonine dehydratase mutant TD^F383V (encoded by ilvA1) and an acetohydroxy acid synthase mutant AHAS^{P176S, D426E, L575W} (encoded by ilvBN1) in Corynebacterium glutamicum IWJ001, one of the best l-isoleucine producing strains. Here, we further characterized an aspartate kinase mutant AK^A279T (encoded by lysC1) and a homoserine dehydrogenase mutant HD^G378S (encoded by hom1) in IWJ001, and analyzed the consequences of all these mutant enzymes on amino acids production in the wild type background. In vitro enzyme tests confirmed that AK^A279T is completely resistant to feed-back inhibition by l-threonine and l-lysine, and that HD^G378S is partially resistant to l-threonine with the half maximal inhibitory concentration between 12 and 14 mM. In C. glutamicum ATCC13869, expressing lysC1 alone led to exclusive l-lysine accumulation, co-expressing hom1 and thrB1 with lysC1 shifted partial carbon flux from l-lysine (decreased by 50.1 %) to l-threonine (4.85 g/L) with minor l-isoleucine and no l-homoserine accumulation, further co-expressing ilvA1 completely depleted l-threonine and strongly shifted carbon flux from l-lysine (decreased by 83.0 %) to l-isoleucine (3.53 g/L). The results demonstrated the strongly feed-back resistant TD^F383V might be the main driving force for l-isoleucine over-synthesis in this case, and the partially feed-back resistant HD^G378S might prevent the accumulation of toxic intermediates. Information exploited from such mutation-bred production strain would be useful for metabolic engineering.     

Metabolic evolution and a comparative omics analysis of <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis> for putrescine production

Putrescine is widely used in the industrial production of bioplastics, pharmaceuticals, agrochemicals, and surfactants. Because the highest titer of putrescine is much lower than that of its precursor l-ornithine reported in microorganisms to date, further work is needed to increase putrescine production in Corynebacterium glutamicum. We first compared 7 ornithine decarboxylase genes and found that the Enterobacter cloacae ornithine decarboxylase gene speC1 was most suitable for putrescine production in C. glutamicum. Increasing NADPH availability and blocking putrescine oxidation and acetylation were chosen as targets for metabolic engineering. The putrescine producer C. glutamicum PUT4 was first constructed by deleting puo, butA and snaA genes, and replacing the fabG gene with E. cloacae speC1. After adaptive evolution with C. glutamicum PUT4, the evolved strain C. glutamicum PUT-ALE, which produced an 96% higher amount of putrescine compared to the parent strain, was obtained. The whole genome resequencing indicates that the SNPs located in the odhA coding region may be associated with putrescine production. The comparative proteomic analysis reveals that the pentose phosphate and anaplerotic pathway, the glyoxylate cycle, and the ornithine biosynthetic pathway were upregulated in the evolved strain C. glutamicum PUT-ALE. The aspartate family, aromatic, and branched chain amino acid and fatty acid biosynthetic pathways were also observed to be downregulated in C. glutamicum PUT-ALE. Reducing OdhA activity by replacing the odhA native start codon GTG with TTG and overexpression of cgmA or pyc458 further improved putrescine production. Repressing the carB, ilvH, ilvB and aroE expression via CRISPRi also increased putrescine production by 5, 9, 16 and 19%, respectively.     

Functional analysis of arabinofuranosidases and a xylanase of <Emphasis Type="Italic">Corynebacterium alkanolyticum</Emphasis> for arabinoxylan utilization in <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis>

Xylooligosaccharides (XOSs) and arabinoxylooligosaccharides (AXOSs) are major oligosaccharides derived from arabinoxylan. In our previous report, Corynebacterium glutamicum was engineered to utilize XOSs by introducing Corynebacterium alkanolyticum xyloside transporter and β-xylosidase. However, this strain was unable to consume AXOSs due to the absence of α-l-arabinofuranosidase activity. In this study, to confer AXOS utilization ability on C. glutamicum, two putative arabinofuranosidase genes (abf51A and abf51B) were isolated from C. alkanolyticum by the combination of degenerate PCR and genome walking methods. Recombinant Abf51A and Abf51B heterologously expressed in Escherichia coli showed arabinofuranosidase activities toward 4-nitrophenyl-α-l-arabinofuranoside with k _cat values of 150 and 63, respectively, with optimum at pH 6.0 to 6.5. However, Abf51A showed only a slight activity toward AXOSs and was more susceptible to product inhibition by arabinose and xylose than Abf51B. Introduction of abf51B gene into the C. glutamicum XOS-utilizing strain enabled it to utilize AXOSs as well as XOSs. The xylI gene encoding a putative xylanase was found upstream of the C. alkanolyticum xyloside transporter genes. A signal peptide was predicted at the N-terminus of the xylI-encoding polypeptide, which indicated XylI was a secreted protein. Recombinant mature XylI protein heterologously expressed in E. coli showed a xylanase activity toward xylans from various plant sources with optimum at pH 6.5, and C. glutamicum recombinant strain expressing native XylI released xylose, xylobiose, xylotriose, and arabino-xylobiose from arabinoxylan. Finally, introduction of the xylI gene into the C. glutamicum AXOS-utilizing strain enabled it to directly utilize arabinoxylan.     

<Emphasis Type="SmallCaps">l</Emphasis>-Serine overproduction with minimization of by-product synthesis by engineered <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis>

The direct fermentative production of l-serine by Corynebacterium glutamicum from sugars is attractive. However, superfluous by-product accumulation and low l-serine productivity limit its industrial production on large scale. This study aimed to investigate metabolic and bioprocess engineering strategies towards eliminating by-products as well as increasing l-serine productivity. Deletion of alaT and avtA encoding the transaminases and introduction of an attenuated mutant of acetohydroxyacid synthase (AHAS) increased both l-serine production level (26.23 g/L) and its productivity (0.27 g/L/h). Compared to the parent strain, the by-products l-alanine and l-valine accumulation in the resulting strain were reduced by 87 % (from 9.80 to 1.23 g/L) and 60 % (from 6.54 to 2.63 g/L), respectively. The modification decreased the metabolic flow towards the branched-chain amino acids (BCAAs) and induced to shift it towards l-serine production. Meanwhile, it was found that corn steep liquor (CSL) could stimulate cell growth and increase sucrose consumption rate as well as l-serine productivity. With addition of 2 g/L CSL, the resulting strain showed a significant improvement in the sucrose consumption rate (72 %) and the l-serine productivity (67 %). In fed-batch fermentation, 42.62 g/L of l-serine accumulation was achieved with a productivity of 0.44 g/L/h and yield of 0.21 g/g sucrose, which was the highest production of l-serine from sugars to date. The results demonstrated that combined metabolic and bioprocess engineering strategies could minimize by-product accumulation and improve l-serine productivity.     

Efficient production of α-ketoglutarate in the <Emphasis Type="Italic">gdh</Emphasis> deleted <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis> by novel double-phase pH and biotin control strategy

Production of l-glutamate using a biotin-deficient strain of Corynebacterium glutamicum has a long history. The process is achieved by controlling biotin at suboptimal dose in the initial fermentation medium, meanwhile feeding NH₄OH to adjust pH so that α-ketoglutarate (α-KG) can be converted to l-glutamate. In this study, we deleted glutamate dehydrogenase (gdh1 and gdh2) of C. glutamicum GKG-047, an l-glutamate overproducing strain, to produce α-KG that is the direct precursor of l-glutamate. Based on the method of l-glutamate fermentation, we developed a novel double-phase pH and biotin control strategy for α-KG production. Specifically, NH₄OH was added to adjust the pH at the bacterial growth stage and NaOH was used when the cells began to produce acid; besides adding an appropriate amount of biotin in the initial medium, certain amount of additional biotin was supplemented at the middle stage of fermentation to maintain a high cell viability and promote the carbon fixation to the flux of α-KG production. Under this control strategy, 45.6 g/L α-KG accumulated after 30-h fermentation in a 7.5-L fermentor and the productivity and yield achieved were 1.52 g/L/h and 0.42 g/g, respectively.     

Overexpression of <Emphasis Type="Italic">ppc</Emphasis> or deletion of <Emphasis Type="Italic">mdh</Emphasis> for improving production of γ-aminobutyric acid in recombinant <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis>

l-Glutamate decarboxylase (GAD) transforms l-glutamate into γ-aminobutyric acid (GABA). Corynebacterium glutamicum that expresses exogenous GAD gene(s) can synthesize GABA from its own produced l-glutamate. To enhance GABA production in recombinant C. glutamicum strain SH, metabolic engineering strategies were used to improve the supply of the GABA precursor, l-glutamate. Five new strains were constructed here. First, the ppc gene was coexpressed with two GAD genes (gadB1 and gadB2). Then, the mdh gene was deleted in C. glutamicum SH. Next, gadB1-gadB2 and gadB1-gadB2-ppc co-expression plasmids were transformed into C. glutamicum strains SH and Δmdh, resulting in four recombinant GAD strains SE1, SE2, SDE1, and SDE2, respectively. Finally, the mdh gene was overexpressed in mdh-deleted SDE1, generating the mdh-complemented GAD strain SDE3. After fermenting for 72 h, GABA production increased to 26.3?±?3.4, 24.8?±?0.7, and 25.5?±?3.3 g/L in ppc-overexpressed SE2, mdh-deleted SDE1, and mdh-deleted ppc-overexpressed SDE2, respectively, which was higher than that in the control GAD strain SE1 (22.7?±?0.5 g/L). While in the mdh-complemented SDE3, GABA production decreased to 20.0?±?0.6 g/L. This study demonstrates that the recombinant strains SE2, SDE1, and SDE2 can be used as candidates for GABA production.     

Characterization of a flavin-containing monooxygenase from <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis> and its application to production of indigo and indirubin

Objective

To examine the role of a gene encoding flavin-containing monooxygenase (cFMO) from Corynebacterium glutamicum ATCC13032 when cloned and expressed in Escherichia coli for the production of indigo pigments.

Results

The blue pigments produced by recombinant E. coli were identified as indigo and indirubin. The cFMO was purified as a fused form with maltose-binding protein (MBP). The enzyme was optimal at 25 °C and pH 8. From absorption spectrum analysis, the cFMO was classified as a flavoprotein. FMO activity was strongly inhibited by 1 mM Cu²⁺ and recovered by adding 1–10 mM EDTA. The enzyme catalyzed the oxidation of TMA, thiourea, and cysteamine, but not glutathione or cysteine. MBP-cFMO had an indole oxygenase activity through oxygenation of indole to indoxyl. The recombinant E. coli produced 685 mg indigo l^?1 and 103 mg indirubin l^?1 from 2.5 g l-tryptophan l^?1.

Conclusion

The results suggest the cFMO can be used for the microbial production of both indigo and indirubin.

     

l-Valine production with minimization of by-products’ synthesis in Corynebacterium glutamicum and Brevibacterium flavum

Corynebacterium glutamicum ATCC13032 and Brevibacterium flavum JV16 were engineered for l-valine production by over-expressing ilvEBN ^r C genes at 31?°C in 72?h fermentation. Different strategies were carried out to reduce the by-products’ accumulation in l-valine fermentation and also to increase the availability of precursor for l-valine biosynthesis. The native promoter of ilvA of C. glutamicum was replaced with a weak promoter MPilvA (P-ilvAM1CG) to reduce the biosynthetic rate of l-isoleucine. Effect of different relative dissolved oxygen on l-valine production and by-products’ formation was recorded, indicating that 15?% saturation may be the most appropriate relative dissolved oxygen for l-valine fermentation with almost no l-lactic acid and l-glutamate formed. To minimize l-alanine accumulation, alaT and/or avtA was inactivated in C. glutamicum and B. flavum, respectively. Compared to high concentration of l-alanine accumulated by alaT inactivated strains harboring ilvEBN ^r C genes, l-alanine concentration was reduced to 0.18?g/L by C. glutamicum ATCC13032MPilvA△avtA pDXW-8-ilvEBN ^r C, and 0.22?g/L by B. flavum JV16avtA::Cm pDXW-8-ilvEBN ^r C. Meanwhile, l-valine production and conversion efficiency were enhanced to 31.15?g/L and 0.173?g/g by C. glutamicum ATCC13032MPilvA△avtA pDXW-8-ilvEBN ^r C, 38.82?g/L and 0.252?g/g by B. flavum JV16avtA::Cm pDXW-8-ilvEBN ^r C. This study provides combined strategies to improve l-valine yield by minimization of by-products’ production.     

<Emphasis Type="Italic">C7</Emphasis>-prenylation of tryptophanyl and <Emphasis Type="Italic">O</Emphasis>-prenylation of tyrosyl residues in dipeptides by an <Emphasis Type="Italic">Aspergillus terreus</Emphasis> prenyltransferase

During our search for novel prenyltransferases, a putative gene ATEG_04218 from Aspergillus terreus raised our attention and was therefore amplified from strain DSM 1958 and expressed in Escherichia coli. Biochemical investigations with the purified recombinant protein and different aromatic substrates in the presence of dimethylallyl diphosphate revealed the acceptance of all the tested tryptophan-containing cyclic dipeptides. Structure elucidation of the main enzyme products by NMR and MS analyses confirmed the attachment of the prenyl moiety to C-7 of the indole ring, proving the identification of a cyclic dipeptide C7-prenyltransferase (CdpC7PT). For some substrates, reversely C3- or N1-prenylated derivatives were identified as minor products. In comparison to the known tryptophan-containing cyclic dipeptide C7-prenyltransferase CTrpPT from Aspergillus oryzae, CdpC7PT showed a much higher substrate flexibility. It also accepted cyclo-l-Tyr-l-Tyr as substrate and catalyzed an O-prenylation at the tyrosyl residue, providing the first example from the dimethylallyltryptophan synthase (DMATS) superfamily with an O-prenyltransferase activity towards dipeptides. Furthermore, products with both C7-prenyl at tryptophanyl and O-prenyl at tyrosyl residue were detected in the reaction mixture of cyclo-l-Trp-l-Tyr. Determination of the kinetic parameters proved that (S)-benzodiazepinedione consisting of a tryptophanyl and an anthranilyl moiety was accepted as the best substrate with a K _M value of 204.1 μM and a turnover number of 0.125 s^?1. Cyclo-l-Tyr-l-Tyr was accepted with a K _M value of 1,411.3 μM and a turnover number of 0.012 s^?1.     

Updates on industrial production of amino acids using <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis>

l-Amino acids find various applications in biotechnology. l-Glutamic acid and its salts are used as flavor enhancers. Other l-amino acids are used as food or feed additives, in parenteral nutrition or as building blocks for the chemical and pharmaceutical industries. l-amino acids are synthesized from precursors of central carbon metabolism. Based on the knowledge of the biochemical pathways microbial fermentation processes of food, feed and pharma amino acids have been developed. Production strains of Corynebacterium glutamicum, which has been used safely for more than 50 years in food biotechnology, and Escherichia coli are constantly improved using metabolic engineering approaches. Research towards new processes is ongoing. Fermentative production of l-amino acids in the million-ton-scale has shaped modern biotechnology and its markets continue to grow steadily. This review focusses on recent achievements in strain development for amino acid production including the use of CRISPRi/dCas9, genome-reduced strains, biosensors and synthetic pathways to enable utilization of alternative carbon sources.     

Model-based reconstruction of synthetic promoter library in <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis>

Objective

To develop an efficient synthetic promoter library for fine-tuned expression of target genes in Corynebacterium glutamicum.

Results

A synthetic promoter library for C. glutamicum was developed based on conserved sequences of the ??10 and ??35 regions. The synthetic promoter library covered a wide range of strengths, ranging from 1 to 193% of the tac promoter. 68 promoters were selected and sequenced for correlation analysis between promoter sequence and strength with a statistical model. A new promoter library was further reconstructed with improved promoter strength and coverage based on the results of correlation analysis. Tandem promoter P70 was finally constructed with increased strength by 121% over the tac promoter. The promoter library developed in this study showed a great potential for applications in metabolic engineering and synthetic biology for the optimization of metabolic networks.

Conclusions

To the best of our knowledge, this is the first reconstruction of synthetic promoter library based on statistical analysis of C. glutamicum.

     

Rational design and analysis of an <Emphasis Type="Italic">Escherichia coli</Emphasis> strain for high-efficiency tryptophan production

l-tryptophan (l-trp) is a precursor of various bioactive components and has great pharmaceutical interest. However, due to the requirement of several precursors and complex regulation of the pathways involved, the development of an efficient l-trp production strain is challenging. In this study, Escherichia coli (E. coli) strain KW001 was designed to overexpress the l-trp operator sequences (trpEDCBA) and 3-deoxy-D-arabinoheptulosonate-7-phosphate synthase (aroG ^fbr ). To further improve the production of l-trp, pyruvate kinase (pykF) and the phosphotransferase system HPr (ptsH) were deleted after inactivation of repression (trpR) and attenuation (attenuator) to produce strain KW006. To overcome the relatively slow growth and to increase the transport rate of glucose, strain KW018 was generated by combinatorial regulation of glucokinase (galP) and galactose permease (glk) expression. To reduce the production of acetic acid, strain KW023 was created by repressive regulation of phosphate acetyltransferase (pta) expression. In conclusion, strain KW023 efficiently produced 39.7 g/L of l-trp with a conversion rate of 16.7% and a productivity of 1.6 g/L/h in a 5 L fed-batch fermentation system.     

High-level intra- and extra-cellular production of <Emphasis Type="SmallCaps">d</Emphasis>-psicose 3-epimerase via a modified xylose-inducible expression system in <Emphasis Type="Italic">Bacillus subtilis</Emphasis>

d-Psicose 3-epimerase (DPEase) converts d-fructose into d-psicose which exists in nature in limited quantities and has key physiological functions. In this study, RDPE (DPEase from Ruminococcus sp. 5_1_39BFAA) was successfully constitutively expressed in Bacillus subtilis, which is the first report of its kind. Three sugar-inducible promoters were compared, and the xylose-inducible promoter P _xylA was proved to be the most efficient for RDPE production. Based on the analysis of the inducer concentration and RDPE expression, we surmised that there was an extremely close correlation between the intracellular RDPE expression and xylose accumulation level. Subsequently, after the metabolic pathway of xylose was blocked by deletion of xylAB, the intra- and extra-cellular RDPE expression was significantly enhanced. Meanwhile, the optimal xylose induction concentration was reduced from 4.0 to 0.5 %. Eventually, the secretion level of RDPE reached 95 U/mL and 2.6 g/L in a 7.5-L fermentor with the fed-batch fermentation, which is the highest production of DPEase by a microbe to date.     

OhsR acts as an organic peroxide-sensing transcriptional activator using an <Emphasis Type="Italic">S</Emphasis>-mycothiolation mechanism in <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis>

Background

Corynebacterium glutamicum is a well-known producer of various l-amino acids in industry. During the fermenting process, C. glutamicum unavoidably encounters oxidative stress due to a specific reactive oxygen species (ROS) produced by consistent adverse conditions. To combat the ROS, C. glutamicum has developed many common disulfide bond-based regulatory devices to control a specific set of antioxidant genes. However, nothing is known about the mixed disulfide between the protein thiol groups and the mycothiol (MSH) (S-mycothiolation)-based sensor. In addition, no OhrR (organic hydroperoxide resistance regulator) homologs and none of the organic hydroperoxide reductase (Ohr) sensors have been described in the alkyl hydroperoxide reductase CF-missing C. glutamicum, while organic hydroperoxides (OHPs)-specific Ohr was a core detoxification system.

Results

In this study, we showed that the C. glutamicum OhsR acted as an OHPs sensor that activated ohr expression. OhsR conferred resistance to cumene hydroperoxide (CHP) and t-butyl hydroperoxide but not H₂O₂, hypochlorous acid, and diamide; this outcome was substantiated by the fact that the ohsR-deficient mutant was sensitive to OHPs but not inorganic peroxides. The DNA binding activity of OhsR was specifically activated by CHP. Mutational analysis of the two cysteines (Cys125 and Cys261) showed that Cys125 was primarily responsible for the activation of DNA binding. The oxidation of Cys125 produced a sulfenic acid (C125-SOH) that subsequently reacted with MSH to generate S-mycothiolation that was required to activate the ohr expression. Therefore, OhsR regulated the ohr expression using an S-mycothiolation mechanism in vivo.

Conclusion

This is the first report demonstrating that the regulatory OhsR specifically sensed OHPs stress and responded to it by activating a specific ohr gene under its control using an S-mycothiolated mechanism.

     

A method for simultaneous gene overexpression and inactivation in the <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis> genome

The gene integration method is an important tool to stably express desirable genes in bacteria. To avoid heavy workload and cost, we constructed a rapid and efficient method for genome modification. This method depended on a mobilizable plasmid, which contains a P _tac promoter, an introduced multiple cloning site (iMCS), and rrnBT1T2 terminator. Briefly, the mobilizable plasmid pK18-MBPMT with the P _tac-iMCS-rrnBT1T2 cartridge derived from pK18mobsacB was prepared to directly integrate hetero-/homologous DNA into the Corynebacterium glutamicum genome. Like our previous method, this method was based on insertional inactivation and double-crossover homologous recombination, which simultaneously achieved gene overexpression and inactivation in the genome without the use of genetic markers. Compared to the previous method, this protocol omitted the construction of a recombinant expression plasmid and clone of the target gene(s) cassette, which significantly decreased the workload, cost, and operational time. Using this method, the heterologous gene amy and the homologous gene lysC ^T311I were successfully integrated into the C. glutamicum genome at alaT and avtA loci, respectively. Moreover, the operation time of this method was shorter than that of the previous method, especially for repeated integration. This method, which is based on the mobilizable plasmid pK18-MBPMT, thus represents a potentially attractive protocol for the integration of genes in the course of genetic modification of C. glutamicum.