- Open Access
A seamless and iterative DNA assembly method named PS-Brick and its assisted metabolic engineering for threonine and 1-propanol production
Biotechnology for Biofuelsvolume 12, Article number: 180 (2019)
DNA assembly is an essential technique enabling metabolic engineering and synthetic biology. Combining novel DNA assembly technologies with rational metabolic engineering can facilitate the construction of microbial cell factories. Amino acids and derived biochemicals are important products in industrial biotechnology with wide application and huge markets. DNA assembly scenarios encountered in metabolic engineering for the construction of amino acid and related compound producers, such as design-build-test-learn cycles, construction of precise genetic circuits and repetitive DNA molecules, usually require for iterative, scarless and repetitive sequence assembly methods, respectively.
Restriction endonuclease (RE)-assisted strategies constitute one of the major categories of DNA assembly. Here, we developed a Type IIP and IIS RE-assisted method named PS-Brick that comprehensively takes advantage of the properties of PCR fragments and REs for iterative, seamless and repetitive sequence assembly. One round of PS-Brick reaction using purified plasmids and PCR fragments was accomplished within several hours, and transformation of the resultant reaction product from this PS-Brick assembly reaction exhibited high efficiency (104–105 CFUs/µg DNA) and high accuracy (~ 90%). An application of metabolic engineering to threonine production, including the release of feedback regulation, elimination of metabolic bottlenecks, intensification of threonine export and inactivation of threonine catabolism, was stepwise resolved in E. coli by rounds of “design-build-test-learn” cycles through the iterative PS-Brick paradigm, and 45.71 g/L threonine was obtained through fed-batch fermentation. In addition to the value of the iterative character of PS-Brick for sequential strain engineering, seamless cloning enabled precise in-frame fusion for codon saturation mutagenesis and bicistronic design, and the repetitive sequence cloning ability of PS-Brick enabled construction of tandem CRISPR sgRNA arrays for genome editing. Moreover, the heterologous pathway deriving 1-propanol pathway from threonine, composed of Lactococcus lactis kivD and Saccharomyces cerevisiae ADH2, was assembled by one cycle of PS-Brick, resulting in 1.35 g/L 1-propanol in fed-batch fermentation.
To the best of our knowledge, the PS-Brick framework is the first RE-assisted DNA assembly method using the strengths of both Type IIP and IIS REs. In this study, PS-Brick was demonstrated to be an efficient DNA assembly method for pathway construction and genome editing and was successfully applied in design-build-test-learn (DBTL) cycles of metabolic engineering for the production of threonine and threonine-derived 1-propanol. The PS-Brick presents a valuable addition to the current toolbox of synthetic biology and metabolic engineering.
Current challenges of metabolic engineering focus on developing cell factories for specific metabolites that can be produced with titres, yields and productivities as high as possible for industrial application [1,2,3]. Developing new strains that meet the economic requirements for industrial scale production typically requires 6–8 years and over $50 million . The time- and cost-intensive processes of strain development are in part due to the limitations of our knowledge of genetics, physiology and metabolism. It is necessary to perform many rounds of proof-of-concept studies that first implement specific metabolic designs and then generate new knowledge for improved design. The iterative rounds of strain construction and subsequent phenotypic characterization are also called DBTL cycles [4,5,6]. In each DBTL cycle of metabolic engineering, enzyme screening, chimeric pathway reconstruction, fine-tuning optimization or metabolic bottleneck elimination is performed one by one, and the titre, yield or productivity of the desired metabolites for engineered strains is stepwise improved to high levels.
Amino acids and amino acid-derived biochemicals are widely used in foods, pharmaceuticals, animal feeds, cosmetics, biofuels and materials. With a constantly increasing market of millions of tons and billions of USD per year, amino acid manufacturing is one of the major pillars of industrial biotechnology [7,8,9]. Amino acids are important building blocks with complex network regulation. Recently, DBTL cycles of rational metabolic engineering have been successfully conducted to construct producers of amino acids and related compounds [10, 11].
The iterative DBTL cycles of metabolic engineering require enabling technologies for iterative DNA assembly, which introduce additional bio-parts into already assembled constructs [12, 13]. DNA assembly methods can be generally classified into two broad categories: RE-based and homology-directed strategies [13,14,15,16], the former being more frequently used for iterative DNA assembly [17, 18]. The BioBrick™ standard of RE-based methods is the first DNA assembly strategy that sequentially integrates small basic parts into a large DNA construct [19, 20]. The basic parts are flanked by Type IIP EcoRI and XbaI restriction sites in the upstream end and by SpeI and PstI restriction sites in the downstream end, where XbaI and SpeI are isocaudomers with two compatible sticky ends. The ligation of the digested parts generates scar sequences that are different from the sequences of both original sites and thus cannot be cut in subsequent digestions with either XbaI or SpeI. The assembled construct is flanked by the same active cloning sites as the two parent parts, from which the next round of insertion can be repeated. The reusability and simplicity of BioBricks make them the standard DNA assembly framework for the iGEM (international Genetic Engineered Machine) competition. The assembly of genetic parts conforming to BioBrick standards has become a key part of bioengineering [21,22,23]. Similar to the BioBrick standard, various Type IIP RE-based strategies have been developed, such as BglBrick , ePathBrick , iBrick , C-Brick , Bacillus BioBrick Box , QGA , CCTL  and YaliBrick .
Although the Type IIP RE-based schemes are easy and straightforward to be performed for iterative DNA assembly, the recognition site remains a scar between the joined fragments and is not considered for seamless cloning. The original BioBrick™ design generates an 8-nucleotide scar between parts joined together, which hampers its application for protein fusions. The modified BglBrick standard  uses BglII and BamHI as the isocaudomers instead of XbaI and SpeI, and thus generates a 6-nucleotide scar sequence (GGATCT) encoding glycine-serine that is suitable for the in-frame fusion of coding sequences. The currently developed assembly schemes derived from BioBrick also leave behind 6–21 bp scars [1, 14, 25, 27,28,29].
Compared to assembly schemes using Type IIP REs that recognize and cut within a palindromic sequence, Golden Gate assembly  utilizes Type IIS enzymes that cut outside of recognition site in a variable sequence that can be customized as overlapping regions for fusions of multiple parts in a predefined order. Despite its multi-part advantage, Golden Gate is limited in reusability. MoClo and Golden Braid variants brought breakthroughs to Golden Gate assembly that enable full reusability of composite parts [12, 31, 32]. Golden Braid frameworks adopt a double loop topology of multi-vector levels to achieve multipartite expansion. On the other hand, the MoClo uses more levels of topology and a complex workflow. To make the resulting parts fully reusable, an indefinite number of additional destination plasmids for subsequent hierarchy levels would be required. The MoClo toolkit was then adapted with modifications to the vectors and schemes for Escherichia coli , yeast , plants  and mammalian cells . Taken together, both MoClo and Golden Braid frameworks enable an iterative workflow; however, it requires elaborate plasmid libraries and/or sacrifices multipart assembly .
The interstitial scar sequences between joined DNA fragments can be problematic for maintaining DNA integrity and for mRNA folding, increasing the difficulty for sequence design [38, 39]. For precise DNA assembly into genes, circuits, metabolic pathways and even metabolic modules, the consecutive combinations of genetic context-dependent elements (such as enhancers, promoters, RBSs, spacers, genes and terminators) require the development of scar-free ‘seamless’ assembly techniques [6, 15, 40,41,42].
Here, we developed a Type IIP and IIS restriction endonuclease-assisted BioBrick (PS-Brick) for both iterative and seamless assembly. With the use of the PS-Brick method, we showcase here the successful achievement of iterative DBTL cycles of metabolic engineering for threonine and 1-propanol production, including the release of feedback regulation of the threonine operon, elimination of a metabolic bottleneck, intensification of threonine export, inactivation of threonine catabolism and construction of a 1-propanol pathway. In addition to the iterative character of PS-Brick for sequential strain engineering, the seamless property enabled precise in-frame fusion for codon saturation mutagenesis and bicistronic design. Moreover, the repetitive sequence cloning of PS-Brick enabled the construction of tandem CRISPR sgRNA arrays with the same promoter and terminator.
Design and proof-of-concept of PS-Brick assembly scheme
The design principles of PS-Brick
Compared to the original BioBrick standard (using only type IIP REs) and Golden Gate assembly (using only type IIS REs), PS-Brick applies both of them in the assembly reaction (Fig. 1a). The available digested ends created by Type IIS REs include overhangs of up to 4 bp, single base pair overhangs and blunt ends. The PS-Brick scheme adopts Type IIS endonucleases that can generate single base overhangs or blunt ends. Three commercially available Type IIS REs with a single base digestion overhangs (BmrI, BciVI and HphI) have been tested to show sufficient cleavage efficiencies . MlyI is the unique Type IIS RE with one recognition site and a blunt digestion product. Considering the frequency and location of these restriction sites in the pUC19 base vector, BmrI (generating 1 nt cohesive end) and MlyI (generating blunt end) are used as Type IIS REs for the proof-of-concept of the PS-Brick assembly strategy (Fig. 1bc).
One BmrI site and three MlyI sites located in the pUC19 vector backbones were removed through overlap extension PCR . One entrance site of adjacent SphI/BmrI or SphI/MlyI at the end of truncated mCherry was introduced into the mutated pUC19 vector, generating the original PS-Brick vectors pOB and pOM, respectively (see “Methods” section). The truncated site of the mCherry gene was located in the unique inverted MlyI recognition sequence “GACTC” (Figs. 1 and 2a), and the introduced PCR parts were free of internal SphI, BmrI and MlyI sites. The original PS-Brick vectors were double digested using the corresponding REs pair, respectively. The recognition site of the Type IIS REs BmrI or MlyI and half of SphI recognition site were detached from the original vector backbones, leaving behind one 1 nt cohesive end generated by BmrI or one blunt end generated by MlyI and the other cohesive end (4 nt), which is generated by SphI (Fig. 1b, c). The genetic parts to be joined were defined as donor fragments and were supplied in the form of PCR products. Compared to certain high-fidelity DNA polymerases generating blunt end PCR products, Taq polymerase can add a single non template-directed deoxyadenosine (dA) residue to the 3′ end of duplex PCR products . The dA overhang of amplified DNA fragments can be directly ligated into a single 3′ deoxythymidine (dT) overhang at the end of BmrI-digested pOB (Fig. 1b). The blunt end of donor PCR fragments amplified by high-fidelity polymerase can be ligated to the blunt end of MlyI digested vector pOM (Fig. 1c).
Compared to the previous BioBrick system and its derivatives that use donor parts prefixed and suffixed with restriction enzyme sites at both ends, donor PCR fragments in PS-Brick are only single-end flanked by adjacent Type IIP and Type IIS restriction sites (Figs. 1and 2a). The required extensions of adjacent SphI/BmrI, or adjacent SphI/MlyI, were designed in primer extensions. The PCR products flanked by the adjacent RE pairs (SphI/BmrI or SphI/MlyI) on one end were digested by only SphI, and then linked to the 4-nt complementary cohesive end of the SphI/BmrI double-digested pOB or SphI/MlyI digested pOM vector backbones. Meanwhile, the other end of the digested vector backbones with a 1 nt cohesive end or a blunt end is linked with an uncut end of the PCR products through TA cloning or blunt end ligations, respectively. After ligation, the joint between the Type IIS endonuclease (BmrI or MlyI) digested end of the vector and the PCR product end without restriction enzyme sites contains no additional scar sequences (Figs. 1b, c and 2a); the other joint, between the vector end and PCR product end that had been both digested by SphI, once again contains the same adjacent SphI and BmrI sites, or adjacent SphI and MlyI sites and could, therefore, be used for next round of part incorporation (Fig. 1). Taken together, these results indicate that a seamless and iterative assembly scheme was achieved through the PS-Brick strategy.
Compared to the previous restriction-ligation methods, the novel designs of PS-Brick are as follows: (i) Two types of REs (Type IIP and IIS) are used in PS-Brick, whereas only one Type of REs is applied in BioBrick-like standards or Golden Gate-like assembly, respectively. (ii) The BioBrick standard (SpeI, PstI, XbaI and EcoRI) and methods similar to it, such as BglBrick (EcoRI, BglII, BamHI, and XhoI) , ePathBrick (SpeI, XbaI, NheI, and AvrII)  and YaliBrick (SpeI, SalI, XbaI, and AvrII)  use four defined Type IIP REs in each method (Table 1), whereas PS-Brick can use all the Type IIP REs cleaving to sticky end, which provides broad options. (iii) The PS-Brick standard adopts Type IIS endonucleases generating single base overhangs or blunt ends to match the PCR products with an unpaired dA extension or a blunt end, respectively, while the most frequently used Type IIS REs for DNA assembly have long cohesive ends (usually 4 nt) [12, 30, 32, 46]. (iv) The donor PCR fragments in PS-Brick are only flanked on one end by restriction sites, allowing for simultaneous utilization of the properties of PCR and REs, whereas the donor PCR fragments are fixed with restriction enzyme sites at both ends in BioBrick and Golden Gate-like restriction-ligation standards. (v) The seamless character of PS-Brick is achieved via blunt end cloning or tailorable TA cloning combining the properties of PCR and Type IIS REs. The blunt end or one-base cohesive end of the insert DNA fragments can be generated by PCR with high-fidelity polymerase or Taq polymerase, respectively, while the complementary ends of the linear receptor vector can be generated by Type IIS REs with a blunt or one-base overhang digestion site, respectively. And (vi) the iterative assembly character of PS-Brick is achieved via one uncleavable joint of blunt end cloning or TA cloning along with a cleavable junction between the Type IIP digested end of receptor plasmid and donor PCR fragments. The recognition site of the Type IIS REs and portions of the Type IIP RE site nucleotides detached from the original vector backbones after double REs digestion. The same adjacent Type IIP and IIS restriction pair site is incorporated into the primer design as the unique entrance used for the next round of assembly.
Optimization of the PS-Brick
The cutting efficiencies of the Type IIS REs BmrI and MlyI presented in vectors pOB and pOM were tested through gel electrophoresis with a cutting time ranging from 15 to 180 min. As shown in Fig. 2bc, almost all of the vectors were digested by BmrI and MlyI at 15 min as recommended by the Time-Saver RE protocol. Due to very small amounts of uncut plasmid having a significant impact on transformation, the cutting efficiency of BmrI and MlyI was further differentiated by a transformation test. The BmrI-digested pOB and MlyI digested pOM were transformed into E. coli DH5α competent cells (transformation efficiency with circular pUC19 plasmids: (1.17 ± 0.19) × 106 CFU/µg DNA). As expected, the transformation efficiency gradually reduced (Fig. 2b), indicating that the unobservable uncut plasmids were digested over time. Therefore, the bands of BmrI cleaved pOB and MlyI cleaved pOM at 30 min in the gel (Additional file 1: Fig. S1) were recovered for the second SphI digestion. The cutting efficiency of SphI was investigated using the assembly efficiency and correct ligation rate. The vector backbones of the BmrI-cleaved pOB and MlyI cleaved pOM were digested with SphI for 15 min to 180 min, and then inactivated at 65 °C, recovered and linked to PCR products digested by SphI for 180 min. The ligation mix was chemically transformed into competent cells. The total colony-forming units (CFUs) after transformation was recorded as assembly efficiency, and the percentage of the correct colonies by DNA sequencing among the total colonies was calculated as the assembly accuracy (also called fidelity or the positive rate) [47, 48]. In both cases, SphI digestion from 15 to 180 min resulted in similar assembly efficiency, approximately 4 ~ 8×104 colony-forming units CFU/µg DNA (Fig. 2c). The accuracy of PS-Brick assembly was measured by DNA sequencing of 20 clones and ranged from 88.2 to 95.1% with varying cutting times for both TA PS-Brick with pOB and blunt end ligations PS-Brick with pOM (Fig. 2d). The seamless joint between the vector and insert was confirmed by DNA sequencing and did not show any mutations. The cutting time course analysis of electrophoresis, assembly efficiency and accuracy indicated that 15 min was enough for both Type IIS REs and the following Type IIP REs digestion in PS-Brick. Considering the two DNA recoveries for 30 min each, RE inactivation for 20 min, DNA ligation for 30 min, E. coli transformation for 30 min and incubation for 40 min, the PS-Brick workflow can be performed within half of a working day (Additional file 1: Fig. S2). Each round of PS-Brick (from amplification of DNA fragments to clone verification by PCR) can be finished in two working days (Additional file 1: Fig. S2).
To compare this method with the traditional Type IIP RE-based cloning methods, the same mCherry fragment and the SphI and XbaI sites present in the MCS sequence of the pUC19 vector were used in the PS-Brick assembly standard. The assembly efficiency and accuracy of traditional clone method with SphI and XbaI were similar to those of the PS-Brick (Fig. 2e). The three methods used the same SphI site at one end of both PCR products and linearized vector, so the other end with 4 nt overhangs generated by XbaI, 1 nt overhangs generated by BmrI and blunt ends generated by MlyI resulted in similar ligation efficiency. However, cohesive end ligation and TA cloning were expected to be more efficient than blunt end ligation . The difference may arise from the different enzymes used for vector preparation . Preferably, enzymes with extensive usage history, high efficiency and non-methylation are suggested to be adopted in the PS-Brick standard.
A single TA base pair can be easily found in most DNA. Seamless TA fusions require the design of the cutting sites of BmrI to contain dT/dA bases in the insert/vector transition (Fig. 1b, c), whereas the blunt end/MlyI-based PS-BioBrick strategy allows complete seamless assembly. The blunt end/MlyI-based ligations require no A-tailing step of PCR products but reach similar ligation efficiencies as TA cloning and allow complete sequence-independent fusions. In this respect, blunt end ligation-based PS-Brick is completely sequence-independent and thus better suited for universal application. In another respect, only one Type IIS Re MlyI can be used for blunt end ligation-based PS-Brick, whereas three REs (BmrI, BciVI, HphI) can be used for TA clone-based PS-Brick, suggesting that TA clone-based PS-Brick has more options for RE selection. Taken together, these requirements indicate that the user can apply alternative PS-Brick schemes according to the practical demands of their projects.
The clones that failed to assemble an insert were also confirmed by DNA sequencing and showed the same sequence as the original vectors pOB and pOM, indicating that the linearized vectors after digestion by BmrI and SphI were not thoroughly digested by SphI and then self-ligated. To improve the assembly accuracy, dephosphorylation by alkaline phosphatase is necessary to counteract the self-ligation of the vector; however, it would prolong the durance and complicate the workflow of PS-Brick. The 5′-phosphorylated on the non-cut PCR end as another method can be used for efficient ligation, but the accuracy of PS-Brick was not found to improve when primers for insert amplification were phosphorylated prior to ligation (Fig. 2e). Moreover, the price of a 5′-phosphorylated primer was 5.9–7.9 times higher than that of the non-phosphorylated primer containing the same 23 nucleotides synthesized by Thermo Fisher Inc. Considering that the assembly efficiency and accuracy for PCR insertion without phosphorylation and with dephosphorylation for vector backbones were still sufficient for most projects, the PS-Brick scheme did not include these two steps and made it simpler and more cost effective.
DBTL cycles for pathway engineering for the production of threonine and its derivate 1-propanol through PS-Brick
Many optimal solutions of metabolic engineering are resolved in a stepwise manner by repeated DBTL cycles [4, 5]. As a showcase for the PS-Brick method, we constructed cell factories overproducing threonine with iterative DBTL cycles. The general strategy for the development of a genetically defined threonine overproducing strain includes release of feedback regulation on the threonine operon, intensification of biosynthesis pathways, elimination of rate-limiting steps, inactivation of threonine catabolism, modification of product transport and finally reinforcement of the regeneration of coenzymes (Fig. 3a) [10, 11, 49]. The optimal solutions of each procedure of the metabolic engineering strategy were resolved by one DBTL cycle. Four rounds of the DBTL cycle were performed step by step through six cycles of PS-Brick reactions, and the threonine production with engineering strains gradually increased to higher levels.
Site-directed mutagenesis for feedback-resistant ThrA
The seamless assembly of PS-Brick was expected to perform codon saturation mutagenesis (mutagenesis that causes a change from a wild-type amino acid to all other amino acids) by varying the sequence in the primer of the PCR insert. To demonstrate the feasibility, we edited the bifunctional enzyme aspartokinase I–homoserine dehydrogenase I (AC1–HDH1), encoded by the thrA gene, to relieve the feedback inhibition by threonine (Fig. 3a). Mutations in ThrA to release feedback inhibition are the most important modification for threonine production in E. coli [11, 49]. A feedback-resistant ThrA variant (Gly433Arg) derived from the threonine hyper-producer ATCC 21277  has been widely used for the production of threonine and its derivatives [51,52,53]. In addition to the wild-type Gly and the mutated Arg at the 433th residue of ThrA, all other 18 amino acids, encoding by the codons with high usage frequency in E. coli K12 MG1655, were designed as the alternatives in this study (Fig. 3b).
For PS-Brick assembly, the Type IIP RE HindIII and the Type IIS RE MlyI were used as the iterative RE pair. There are four MlyI sites located in the pACYC184; thus, this vector cannot be directly used for PS-Brick assembly. The entrance site of HindIII/MlyI was introduced into the medium-copy-number plasmid pACYC184 to generate original vector pOthr for PS-Brick assembly. Three MlyI sites located in the pACYC184 vector backbones were mutated through overlap extension PCR with primers AC3211-F/AC727-R and AC727-F/AC1143-R. Another MlyI site located in the MCS sequence of the pACYC184 vector was removed by HindIII and NruI digestion. The remaining pACYC184 vector backbone without the MlyI site was linked with PCR products of the truncated thrABC operon (a part of thrA and the entire thrBC with the native terminator) by primers TAB-F/TAB-R, TBC-F/TBC-R and TC-F/TC-R. The NruI site was designed in a primer outside of the terminator of the thrC gene, and the HindIII site was designed outside of the truncated thrA and internally adjacent to the MlyI site (Fig. 3b). After ligation and sequencing verification, the newly obtained vector pOthr, containing adjacent HindIII/MlyI entrance sites, was used for subsequent in-frame fusion of ThrA (Fig. 3b).
The truncated site of the thrABC operon is located in the target thrAGly433 codon sequence. The sites of codon saturation mutagenesis of the 433th residue of ThrA were designed in 20 inverse primers of the PCR donors, and the adjacent HindIII/MlyI site was designed in the extension of one forward primer (Fig. 3b). The 20 PCR donor fragments, including promotor and different mutated thrAGly433, were incorporated into the acceptor vector pOthr. Thus, 20 mutants (including promoter, RBS, thrAGly433BC and terminator) were generated by one cycle of PS-Brick assembly. Meanwhile, the joint between vector end and the PCR product end that were both digested by HindIII once again contains the same adjacent HindIII/MlyI sites and could, therefore, be used for next round of parts incorporation (Fig. 3b).
After verification by DNA sequencing, the correct plasmids harbouring the thrABC operon containing the saturation mutated thrA gene (pACYC184-thrA433BC) were transformed into the E. coli K12 MG1655 strain. The overexpression of 20 ThrA variants resulted in a significant difference in threonine production after 12 h of shake flask fermentation (Fig. 3c). Remarkably, the thrAGly433Phe mutant resulted in the highest concentration of threonine, 48-fold higher than that of the wild-type control. The efficient desensitized ThrAGly433 variant identified through saturation mutagenesis can be widely used for the development of a producer of threonine and its derivatives.
Identification of the metabolic bottleneck for threonine synthesis
It is well known that overexpression of deregulated thrABC is usually the most productive strategy for metabolic engineering of threonine [49, 54, 55]. However, the metabolic bottleneck after overexpression of thrABC for efficient threonine synthesis was unclear. The production of threonine could be increased through up-modulation of the following genes directly related to the threonine-synthesis pathway (Fig. 3a): the ppc gene encoding phosphoenolpyruvate carboxylase, the pntAB operon responsible for the regeneration of reduced NADPH in E. coli, the aspC gene encoding aspartate aminotransferase for transferring the amino group, the aspA gene encoding aspartase responsible for the return of carbon from the threonine biosynthetic branch to the tricarboxylic acid cycle and the asd gene encoding aspartyl semialdehyde dehydrogenase. However, the contributions of these genes to threonine accumulation were not simultaneously compared under the same experimental conditions. Here, ppc, aspA, aspC, asd and pntAB with their native promoters, RBSs and terminators were amplified as donor PCR fragments and then assembled in parallel into the last round assembled vector pACYC184-thrA433BC using PS-Brick to investigate the potential rate-limiting step for threonine accumulation (Fig. 3b).
The metabolic bottleneck after overexpression of thrABC was identified through the second round of PS-Brick assembly. After sequencing verification, the correct plasmids pACYC184-thrA433BC-ppc/aspA/aspC/asd/pntAB were transformed into the E. coli K12 MG1655 strain. Transcriptional analysis of the ppc, aspA, aspC, asd and pntAB genes by real-time RT-PCR indicated that the transcriptional levels of all these genes were significantly increased (Additional file 1: Fig. S3). Among the proposed five rate-limiting steps, only overexpression of the asd gene led to a 56.7% increase in threonine production, compared to that obtained with the control strain (Fig. 3d). By contrast, the high expression of Asd had little effect on threonine accumulation in Corynebacterium glutamicum . The asd gene encoding aspartyl semialdehyde dehydrogenase was first demonstrated as the metabolic bottleneck after thrABC overexpression in this study. This engineering target was unable to be predicted purely though metabolic analysis, mainly due to a significant lack of a priori knowledge about the interactions between the target reaction and the intricate metabolic network with its innumerable components [6, 54, 57]. Therefore, it is often necessary to try several versions of a construct to find the optimal configuration. The iterative nature of PS-Brick enables one to subsequently identify major bottlenecks and gradually optimize strain performance, while simultaneously conserving the positive construct.
However, threonine production with strains overexpressing ppc, aspC, aspA and pntAB decreased by 60.8%, 43.3%, 16.7% and 35.9%, respectively, compared to production with the control strain MG1655/pACYC184-thrA433BC (Fig. 3d), which is consistent with the previous report that overexpression of the ppc gene in a plasmid decreased threonine production . The increased activity of anaplerotic phosphoenolpyruvate carboxylase coupled with the simultaneous activity of gluconeogenic reactions will make up ATP-dissipating futile cycles , which was assumed to deteriorate threonine synthesis with its high energetic costs . In the case of pntAB overexpression, the pathways of NADPH oxidation can be activated and lead to the formation of futile cycles in E. coli, which also consumes energy required for both cell growth and threonine synthesis . The negative effects of overexpression of the four genes suggested that upregulation of the non-rate-limiting reaction step of pathway inversely decreases threonine accumulation.
Prioritization of isoenzymes for threonine efflux
As another case of trial and test, PS-Brick was used to prioritize isoenzymes for threonine efflux. Efficient export of threonine is also important to further increase its production. The intracellular concentration of threonine was tenfold higher than that observed in the medium during the growth phase, implying the necessity for accelerating threonine export . Overexpressing the exporter genes not only accelerates threonine secretion, but also reduces its consumption [55, 62]. Three exporter genes, rhtA, rhtB and rhtC, have been overexpressed together in a plasmid for development of a threonine producer [58, 63], but data for comparing the capacity of these transporters in E. coli are scarce . In our previous work, we found that the high expression level of membrane transporter would inhibit cell growth (PCT Patent WO2015197014A1). Here, mid-strength transcription and translation initiation elements were used for expression of the membrane exporters. Four threonine exporters under the same standard initiation element (a mid-strength promoter (PT) from a constitutive bacteriophage PL promoter library  along with a mid-strength bicistronic design (BCD1) RBS ) were assembled into the last round PS-Brick plasmids pACYC184-thrA433BC-asd through two cycles of PS-Brick reaction, respectively. First, each coding sequence of the rhtA, rhtB, rhtC and yeaS genes with their native terminator was amplified as one donor PCR fragment and inserted into the pACYC184-thrA433BC-asd vector through PS-Brick. Second, PT and BCD1 [65, 66] were amplified as donor PCR fragments, and inserted in front of the ATG start codon of the four exporter genes in the last round assembled vectors, generating the corresponding vectors pACYC184-thrA433BC-asd-PTBCD1-rhtA/rhtB/rhtC/yeaS (Fig. 3b). Remarkably, the seamless character of PS-Brick guaranteed precise fusion between the BCD translation initiation element and the downstream coding sequence. The stop codon UAA in a first cistron of BCD1 overlaps the start codon AUG of the downstream coding sequence of the four exporters by 1 base pair, leading to both a stop and start codon via a − 1 frame shift (UAAUG) .
After sequencing verification, the correct plasmids containing threonine efflux genes were completed by a fourth cycle of PS-Brick. Transcriptional analysis of the rhtA, rhtB, rhtC and yeaS genes by real-time RT-PCR indicated that expression of all the genes was significantly upregulated (Additional file 1: Fig. S4). The result of shake flask culture showed that the overexpression of each of the four exporter genes resulted in a distinct increase in threonine production. Among them, the overexpression of the rhtC gene increased threonine production from 0.9 g/L to 3.7 g/L (Fig. 3e), which was consistent with previous results showing that the heterologous expression of E. coli exporters could increase threonine production in C. glutamicum strains . Thus, the assembled plasmid containing rhtC was used for the following threonine production.
Construction of a CRISPR array containing sequence repeats
In the above case studies, the blunt end/MlyI based PS-Brick strategy was used to gradually combine the positive effects of the key genes for threonine accumulation. In this case study, a TA clone/BciVI-based PS-Brick strategy was used to create sgRNA arrays to delete the genes responsible for threonine catabolism. In E. coli, threonine catabolism is mainly catalysed by threonine dehydrogenase (encoded by tdh gene) and threonine deaminase (encoded by ilvA). The deletion of the tdh [53, 58, 68] and ilvA genes  is used in creating threonine producers. To this end, we extended the application to a CRISPR–Cas9 genome editing system for gene deletion. This system included two plasmids, pCas (harbouring the cas9 gene) and pTarget (carrying the sgRNA recognizing the targeted region) . The pTarget vector consisted of a strong constitutive promoter pJ23119 (http://parts.igem.org/Part:BBa J23119), an N20 sequence and an sgRNA scaffold sequence (Fig. 4a). For double gene deletion, two sgRNA arrays with the same promoter and sgRNA scaffolds are required to be constructed into the pTarget vector.
Homology-based assembly methods often fail to construct vectors containing extensive repeated sequences [13, 24, 71]. In this study, the PS-Brick scheme was used to assemble repetitive sgRNA arrays, and the Type IIP RE HindIII and the Type IIS RE BciVI were used as the iterative RE pair. The entrance site of HindIII/BciVI and the editing template was introduced into pTargetF to generate the original vector ptargetET for PS-Brick assembly. The N20 sequences of tdh and ilvA with the same promoter and sgRNA at each end were sequentially inserted into ptargetET through two cycles of the PS-Brick reaction, resulting in ptargetET-tdh-ilvA consisting of double sgRNAs (Fig. 4a, b).
Following the genome editing protocol , we transformed ptargetET-tdh-ilvA into a strain expressing Cas9, and the double mutation strain E. coli MG1655△tdh△ilvA was obtained (Fig. 4c). After three rounds of iterative digestion and ligation, we successfully assembled up to three copies of sgRNA arrays (Additional file 1: Fig. S5), but the triple mutation was not screened. The recombinant plasmid pACYC184-thrA433BC-asd-PTBCD1-rhtC, integrating the positive effects accumulated through four rounds of PS-Brick, was transformed into the E. coli MG1655△tdh△ilvA strain. Batch culture of this engineered strain in a 7.5-L fermenter allowed production of 45.71 g/L threonine, 28.7% higher than the production of control strains retaining the tdh and ilvA genes (35.52 g/L), and no isoleucine was detected during the fermentation process (Fig. 4d), suggesting that the prevention of threonine consumption is an effective strategy for its accumulation.
Construction of the heterologous 1-propanol pathway
1-propanol serves as a promising alternative biofuel and an important solvent and chemical for industrial applications [72, 73]. However, the production of 1-propanol is still dependent on petroleum. In this study, we assembled a heterologous route for 1-propanol production from threonine in E. coli  (Fig. 5a). Lactococcus lactis kivD (encoding 2-keto-acid decarboxylase) and Saccharomyces cerevisiae ADH2 (encoding alcohol dehydrogenase) under the Ptrc and BCD1  control in an artificial operon were assembled in threonine-producing vector phrA433BC-asd through one cycle of PS-Brick (Fig. 5b). After sequencing verification, the correct plasmid pthrA433BC-asd-kivD-ADH2 was transformed in E. coli MG1655. The expression of kivD and ADH2 genes gave rise to the accumulation of 1.35 g/L 1-propanol in 36 h (Fig. 5c). Meanwhile, the precursor threonine and 2-ketobutyrate accumulated at relatively high concentrations of 21.01 g/L and 0.89 g/L, respectively, which suggests that the activity of heterologous KivD and ADH2 was not high enough. In future work, further effort should be made to obtain 2-keto-acid decarboxylase and alcohol dehydrogenase with high efficiency.
DNA synthesis and assembly are the major enabling technologies that contribute to the foundational innovations of synthetic biology [6, 16, 74]. Here we have developed a novel PS-Brick framework that enables iterative, seamless and sequence-repeat DNA assembly. The core principle of PS-Brick is the comprehensive exploitation of the properties of PCR products and Type IIP and IIS REs. To the best of our knowledge, the PS-Brick framework is the first restriction-ligation assembly method using both Type IIP and IIS REs (Table 1). Type IIP RE-assisted BioBrick standards and variants are limited in scarless assembly, whereas Golden Gate assembly  utilizes only Type IIS enzymes and is limited in reusability. Although MoClo and Golden Braid variants brought breakthroughs into the Golden Gate assembly that enabled iterative workflows, they require substantial efforts to prepare elaborate assembly vectors and complex protocols [12, 32], which poses a barrier to their widespread adoption . PS-Brick assembly is an attempt to extend the capabilities of the previously described RE-based strategies to satisfy the requirements of synthetic biology and metabolic engineering.
First, there is a requirement for iterative assembly. Due to the high complexity of the extensive regulation and interactions among the metabolic, gene regulatory and signalling networks, and the limited a priori knowledge for predicting how well a given DNA construct will work once introduced into a cell, it is often necessary to test numerous versions of the construct to find the optimal version [6, 57]. Therefore, it is crucially important to perform sequential DBTL engineering cycles in a proof-of-concept study, which requires a simple and streamlined DNA assembly framework with iterative properties.
Second, there is a requirement for seamless assembly. The interstitial scar sequences between joined DNA fragments can be problematic for maintaining DNA integrity and mRNA folding, which increases the difficulty of sequence design [38, 39]. When a large DNA molecule is assembled stepwise into a backbone plasmid in a random piecewise manner, the scars damage the structure of the original DNA sequence in the final assembled plasmids . The precise combinations of genetic context-dependent elements (such as enhancers, promoters, RBSs, spacers, protein domains and terminators) require the development of scarless assembly processes [6, 15, 40,41,42].
Third, there is a requirement for the assembly of repetitive sequences. DNA molecules with repetitive sequences, such as the TALEN DNA-binding modules , polyketide modules , CRISPR array  and any DNA sequence that appears more than once in insertions . Assembly of these tandem repeat sequence can be problematic for cloning techniques based on PCR and sequence homology [13, 24, 71]. There are two main reasons for this limitation. On the one hand, misalignment and erroneous annealing of primers makes it difficult to create repetitive sequences using PCR-based methods. However, parts containing approximately the same sequence can be targets for recombination, which can often lead to deleted and/or rearranged DNA components . RE-based assembly is a particularly attractive strategy for the construction of DNA components with identical elements.
As a demonstration for iterative, seamless and repetitive sequence assembly, we applied PS-Brick to design iterative DBTL cycles of metabolic pathway construction and optimization for cell factories overproducing threonine and its derivate 1- propanol. An expression vector was assembled in four rounds of PS-Brick reactions, among which seamless character was highlighted when the in-frame fusion of ThrA for codon saturation mutagenesis and precise BCD assemble between a stop codon and an initiation codon. We have also succeeded in assembling a CRISPR-Cas9 genome editing plasmid containing three sequence repeats of sgRNA arrays in three rounds of reactions. The highest titres of threonine with C. glutamicum and E. coli engineered from the wild-type strains reached 12.8 g/L and 82.4 g/L, respectively [56, 58]. In this study, 45.71 g/L threonine was obtained by deleting two genes and overexpressing two genes and one operon. The 1-propanol titre was still relatively low than the highest concentration of 10.8 g/L obtained in 120 h with engineered E. coli . In future studies, efficient technologies, such as biosensors, chromosomal integration, combinatorial and fine-tuning strategies [9, 10], should be applied to improve the yield of the strains.
In addition to the three key properties of seamless, iterative and repetitive sequence assembly, PS-Brick technology has the following advantages. A first comparative advantage is its efficiency and accuracy: many restriction endonucleases fail to cleave when their recognition sequences are located within a few base pairs of the end of a DNA fragment . Here, the frequently used and high-efficiency Type IIP REs (e.g. HindIII and SphI) that generate long sticky ends were used for cutting the donor PCR fragments and linear recipient vector, the end of which contained the corresponding recognition sequences. Furthermore, the infrequent Type IIS REs (MlyI, BmrI and BciVI) were used only for digesting the circular plasmid, and the thoroughly linearized plasmid was used for the second digestion with the above high-efficiency Type IIP REs. The intrinsic robustness of the restriction enzymes involved in the PS-Brick reaction might lead to both high efficiency (104–105 CFU/µg DNA) and accuracy (~ 90%). A second advantage is low-cost and speed: long oligonucleotides, phosphorylated or methylated PCR products and dephosphorylated vector backbones are unnecessary in this method, which reduces the cost of the PS-Brick process. The time-saving commercial REs, such as FastDigest REs from New England Biolabs Inc., QuickCut REs from TaKaRa Bio Inc. and Time-Saver REs from Thermo Fisher Inc., could digest the DNA substrate in 5–15 min. Although gel extraction is necessary, we have shown that one round of the PS-Brick reaction from PCR and plasmid isolation to transformation can be performed in less than a single working day (Additional file 1: Fig. S2). A third distinctive characteristic of the PS-Brick scheme is its simplicity and convenience: sophisticated Golden Braid and MoClo frameworks required elaborate plasmid libraries to prepare donor DNA in the defined format [12, 32], which poses a barrier to their straightforward application and widespread adoption. PS-Brick only requires one acceptor vector with simple assembly rules, which can be easily mastered and applied by researchers.
The definition of technical standards for donor parts is the first step in implementing an idempotent assembly strategy . The insertion parts of PS-Brick are prepared through direct PCR amplification, which adds appropriate adjacent RE site extensions to one of the primer pairs. PCR is generally recognized as the first and the foremost important tool in molecular biology and biotechnology . A number of efficient and flexible PCR-based cloning methods have been developed, including OE PCR , In-Fusion BioBrick , QGA , SSEA ,TAP  and 3G assembly . PCR can be used to produce the desired DNA fragment in vitro and in large quantity from any form of available template DNA source, especially those stored in a community-wide collection. This means that the parts of a community-wide DNA assembly standard can easily be reused in PS-Brick assembly through PCR modification with newly synthesized primers, facilitating flexibility and universality in design and construction.
The need for elimination of internal restriction sites is still a general limitation for the RE-based strategies of DNA assembly. Compared with BioBrick methods with four given REs, PS-Brick can adopt two categories of REs, Type IIP (generating long stick overhangs) and Type IIS (generating blunt ends or one base overhangs). Hundreds of candidates for the Type IIP REs generate long sticky overhangs and four candidates (BmrI, BciVI, HphI and MlyI) for the Type IIS REs used in PS-Brick assembly provide broad available options (Table 1). However, due to the limited number of commercial Type IIS endonucleases, it is often difficult to find an appropriate enzyme to avoid naturally occurring Type IIS sites within DNA parts. Thus, additional efforts, such as overlapping-PCR , directed mutagenesis, or direct DNA synthesis, will be needed to eliminate RE sites present in the DNA sequence prior to its use in the assembly system.
Combinatorial pathway engineering has been successfully used to produce various biochemicals [82, 83]. In a combinatorial strategy, multiple metabolic pathways with different expression levels are simultaneously assembled to generate a strain library. High-producing strains with balanced metabolic flux can be efficiently identified through one round of screening a strain library. However, PS-Brick is unfit for combinatorial pathway engineering because of its limitations in multi-part assembly. Golden Gate based methods such as Ecoflex , MoClo  and Start-Stop Assembly  can assemble more than 60 parts over two or three levels. In this study, the promotor PT and RBS were combined as one donor fragment (PT-BCD1) through overlap PCR, and the two genetic elements were assembled into an acceptor plasmid through one round of the PS-Brick reaction. In addition, five genetic fragments were synthesized as one donor DNA fragment Ptrc-BDC1-kivD-ADH2-Ter (Fig. 5b), and the five fragments were assembled into the acceptor plasmid through one round of the PS-Brick. Similarly, another multi-part assembly scheme of donor fragments was expected to be incorporated into the PS-Brick framework, generating improved technical features.
Golden Gate and its derivatives use only Type IIS REs cleaving outside of their recognition site, which allows for restriction and ligation to be performed in a one-pot reaction . For the PS-Brick and BioBrick-like methods, the reactions of REs and T4 ligation were performed separately in different buffers and at different temperature. The assembly workflow of PS-Brick was more complex than that of the one-pot method.
Each common assembly method has significant advantages, but also limitations. Therefore, a combination of these methods could potentially fulfil the ideal goals while integrating their merits. For example, Golden Gate and Gibson assembly , multisite gateway recombination and Gibson Assembly  and multisite gateway cloning and homing endonucleases  have been successfully combined for developing novel hybrid technologies. PS-Brick provides a framework to assemble the recipient vector and the donor fragment DNA. Certain assembly schemes with one-pot or multi-part merits are expected to be incorporated into the PS-Brick scheme to generate a holistic framework.
RE-assisted DNA assembly methods are widely used for their simple workflows, which can be easily mastered and applied by researchers. To the best of our knowledge, the PS-Brick framework is the first RE-assisted DNA assembly method using both Type IIP and IIS REs, which retains both the iterative strength of the IIP RE-assisted method and the seamless strength of the IIS RE-assisted method. We have developed an efficient and simple assembly method that simultaneously addresses these three highly desirable features. We assert that these characteristics will make PS-Brick a valuable addition to the toolbox of synthetic biologists and metabolic engineers.
Bacterial strains, plasmids and reagents
All bacterial strains and plasmids used in this study are listed in Additional file 1: Table S1. E. coli DH5α was used as a cloning host for PS-Brick assembly methods, and E. coli MG1655 was used for metabolic engineering. All primers used in this study were ordered from Thermo Fisher Scientific (Additional file 1: Table S2). The restriction enzyme BciVI was purchased from Thermo Fisher Scientific, and all the other restriction enzymes and T4 DNA ligase were purchased from New England Biolabs (NEB) (Ipswich, MA, USA). KAPA Hot Start high-fidelity polymerase (Kapa Biosystems, Wilmington, MA) and Ex-Taq DNA Polymerase (TaKaRa-Bio, Japan) were used for amplification of donor parts. A DNA Purification Kit, Bacteria DNA Kit, Mini Plasmid Kit, RNAprep pure Kit and FastQuant RT Kit from TIANGEN BIOTECH were used for DNA preparation. GoTaq® qPCR Master Mix (Promega, USA) was used for quantitative PCR. In addition, 2 × PCR Master Mix (TSINGKE, Beijing) was used for clone PCR. Tryptone and yeast extract were supplied from OXOID. Amino acids and antibiotics were acquired from Sigma-Aldrich. All other chemicals were purchased from Beijing Chemical Works unless otherwise stated.
Construction of the original plasmids for PS-Brick
The plasmid pUC19 was used as the base vector for demonstration of the PS-Brick scheme. One BmrI site and three MlyI sites located in the pUC19 vector backbones are removed through overlap extension PCR . DNA fragments amplified with UC709-F/UC1179-R and UC1179-F/UC1695-R were fused by overlap PCR with primers UC709-F/UC1746-R (Additional file 1: Table S2) and then taken as the long primer for the pUC19 vector mutation. Another two BmrI and MlyI sites present in the MCS sequence of the pUC19 vector were removed by SphI and NdeI digestion. Two types of truncated mCherry fragments were amplified from the pSEVA237R vector  by the same forward primer mC-F flanked with an NdeI site, and a reverse primer mCB-R flanked by a SphI/BmrI site and another forward primer mCM-R flanked with SphI/MlyI site, respectively. PCR products were column-purified and eluted with 35 μL of MilliQ grade water. The purified PCR product was digested with SphI and NdeI and ligated with the same REs digested pUC19 vector backbones. After ligation and sequencing verification, the newly obtained vectors pOB and pOM from pUC19, containing the entrance sites SphI/MlyI and SphI/BmrI, respectively, were taken as the original PS-Brick vectors for subsequent assembly. Primers UC1-6 listed in supplementary Table S2 were used for sequencing verification.
Three MlyI sites located in the pACYC184 vector backbones were mutated through overlap extension PCR with primers AC3211-F/AC727-R and AC727-F/AC1143-R. Another MlyI site located in the MCS sequence of the pACYC184 vector was removed by HindIII and NruI digestion. The remaining pACYC184 vector backbone without the MlyI site was linked with the PCR products of truncated thrABC operon genes by primers TAB-F/TAB-R, TBC-F/TBC-R and TC-F/TC-R. A NruI site was designed in the primer outside of the terminator of the thrC gene, and a HindIII site was designed outside of the truncated thrA and internally adjacent to the MlyI site. After ligation and sequencing verification, the newly obtained vector pOthr containing adjacent HindIII/MlyI entrance sites was used for subsequent metabolic pathway assembly.
The workflow of PS-Brick assembly
PS-Brick assembly with SphI/MlyI entrance site
The primer FM-R flanked by the SphI/MlyI site and the primer FM-F were used to amplify the donor fragment FM by KAPA Hot Start high-fidelity polymerase. PCR procedures with KAPA Hot Start high-fidelity polymerase consisted of one cycle of 95 °C for 3 min, 27 cycles of 98 °C for 20 s, 65 °C for 20 s and 72 °C for 30 s and one cycle of 72 °C for 1 min. The PCR product was run out on a 1% agarose gel stained with GelSafe (TSINGKE, Beijing), and amplicons of interest were column-purified and eluted with 35 μL of MilliQ grade water. The purified PCR products were digested with SphI only for 30 min, heat-inactivated at 60 °C for 20 min and then column-purified for ligation.
The original PS-Brick vector pOM containing the SphI/MlyI entrance site was cleaved by SphI and MlyI for 30 min in the same buffer. All RE-digestion reactions were performed at 37 °C in a 50-µL volume containing 20 units of enzyme and 1 µg of DNA. The double-digested vectors were heat-inactivated at 60 °C for 20 min and then column-purified for ligation with the SphI-digested PCR fragments. The DNA concentration was determined by a Nanodrop 2000c (Thermo Fisher Scientific, Waltham, MA).
Aligation reaction mix of 10 μL, containing 1 μL of T4 DNA ligase, 20 ng of linearized vector and fivefold molar excess of insert DNA, was incubated at 25 °C for 15 min and chilled on ice and then transformed into 100 μL of E. coli DH5α competent cells. Finally, the mixture was spread onto a selection plate and incubated overnight at 37 °C. The colonies were verified by DNA sequencing, and the correct plasmids were used as the acceptor vector for the next round of PS-Brick.
PS-Brick assembly with HindIII/MlyI entrance site
Except for the use of the Type IIP RE HindIII and the original vector pOthr, all the conditions were same as above.
PS-Brick assembly with SphI/BmrI and HindIII/BciVI entrance sites
The primers flanked with SphI/BmrI or HindIII/BciVI sites were used to amplify the donor fragment by Ex-Taq DNA Polymerase. PCR procedures with Ex-Taq Polymerase were set as follows: one cycle of 94 °C for 5 min, 27 cycles of 94 °C for 30 s, 54 °C for 30 s and 72 °C for 30 s and a final extension of 5 min. All the other conditions were the same as above except for the REs and the original vectors.
CRISPR–Cas9 genome editing
The editing process was performed as previously described . In short, MG1655 competent cells harbouring pCas9 were prepared, and arabinose (10 mM final concentration) was added to the culture for λ-Red induction. For electroporation, 50 μL of cells was mixed with 200 ng of ptargetET-tdh-ilvA. Electroporation was performed in a 2-mm Gene Pulser cuvette (Bio-Rad) at 2.5 kV and the product was suspended immediately in 1 mL of LB medium. Cells were recovered at 30 °C for 1 h before being spread onto LB agar containing kanamycin (50 mg/L) and spectinomycin (50 mg/L) and incubated overnight at 30 °C. Transformants were identified by colony PCR and DNA sequencing with primer pairs ilvA-I-F/R and tdh-I-F/R for ilvA and tdh, respectively. For the curing of ptargetET-tdh-ilvA, the edited colony was inoculated into 2 mL of LB medium containing kanamycin (50 mg/L) and IPTG (isopropyl-D-thiogalactopyranoside; 0.5 mmol/L). The culture was incubated for 8 to 16 h, diluted and spread onto LB plates containing kanamycin (50 mg/L). The colonies were confirmed as cured by determining their sensitivity to spectinomycin (50 mg/L). pCas was cured by non-selectively growing the colonies overnight at 37 °C.
Media, culture conditions and fed-batch fermentation in the bioreactor
Lysogeny Broth (LB) was used during cloning work, consisting of tryptone 10 g/L, yeast extract 5 g/L and NaCl 10 g/L. The composition of solid culture medium, Lysogeny Agar (LA), was identical, except for the addition of 15 g/L agar. If required, media were supplemented with the antibiotics ampicillin (100 μg/mL), kanamycin (50 μg/mL) or chloramphenicol (34 μg/mL).
Shake-flask fermentation medium: MOPS 80 g/L, glucose 20 g/L, (NH4)2SO4 20 g/L, KH2PO4 2 g/L, MgSO4·7H2O 2 g/L, yeast extract 4 g, betaine 2 g, trace element solution 5 mL.
Seed medium for fed-batch fermentation : glucose 40 g/L, (NH4)2SO4 15 g/L, KH2PO4 2 g/L, MgSO4·7H2O 2 g/L, yeast extract 2 g/L, l-isoleucine 0.1 g/L, CaCO3 10 g/L, trace element solution 5 mL/L.
Fed-batch fermentation medium : glucose 10 g/L, (NH4)2SO4 10 g/L, KH2PO4 2 g/L, MgSO4·7H2O 2 g/L, yeast extract 2 g/L, trace element solution 10 mL/L. The trace element solution (per litre): FeSO4·7H2O 6 g, CaCl2 1.35 g, ZnSO4·7H2O 0.8 g, MnSO4·4H2O 1.5 g, CuSO4·5H2O 0.15 g, (NH4)6Mo7O24·4H2O 0.2 g, H3BO3 0.1 g, CoCl2·6H2O 0.25 g, 35% HCl 10 mL.
Strains cultured on LB plates were incubated at 37 °C for 12 h. For preculture, one loop of cells was inoculated into a tube with 3 mL of LB medium and incubated for 8 h at 37 °C with shaking at 220 rpm on a rotary shaker. For the seed culture, 1.0 mL of the obtained preculture broth was inoculated into 30 mL of seed culture with the same culture conditions for 8 h. Two copies of the obtained seed culture were then inoculated into 2 L of fermentation medium for fed-batch culture.
Fed-batch fermentation was performed in a BioFlo® 115 Fermentor System (New Brunswick Scientific, Edison, NJ, USA) consisting of 7.5-L double-jacketed glass vessels with a working volume of 2–3 L. Data logging and operational parameters were controlled by the BioCommand Plus BioProcessing Software (New Brunswick Scientific). The temperature was maintained at 37 °C, and the pH was maintained at 6.9 by addition of 25% ammonia. Dissolved oxygen tension was maintained at 50% of air saturation by automatically cascading with stirrer speeds ranging from 200 to 1000 rpm. Pure oxygen was mixed with air to afford sufficient dissolved oxygen when the stirrer speed exceeded 1000 rpm. A silicone-based antifoaming agent was added as required. The concentration of glucose over all of the fed-batch cultures was maintained within the range of 10 ± 5 g/L by supplying 700 g/L of glucose reservoir. The continuous feeding rate of the glucose reservoir was regulated according to the residual glucose concentration. For isoleucine auxotroph strains, isoleucine was continuously supplied according to our previous report .
Preparation and transformation of chemically competent E. coli cells
For the preparation of chemically competent E. coli cells, inoculated a single colony into 5 mL of LB medium with or without appropriate antibiotics and rotated the culture overnight at 37 °C. Then, used 1% overnight culture to inoculate 50 mL of LB medium and incubated at 37 °C until the absorbance at 600 nm was between 0.4 and 0.5. Spun the cell suspension for 10 min at 6000 rpm, discarded the supernatant and gently resuspended the pellet in 20 mL ice-cold buffer solution I (including 1.33 g of CaCl2, 30 mL of glycerine and 142 mL of MilliQ grade water). After incubation on ice for 30 min, cells were spun down at 4000 rpm for 5 min and being gently resuspended in 2 mL of buffer solution I. Distributed the cell suspension in 100 μL aliquots in 0.2 mL microfuge tubes and stored the tubes at − 80 °C.
For transformation, a tube of 100 μL chemically competent E. coli cells was thawed on ice. 50 ng plasmid DNA was added to the cell mixture and being mixed carefully with cells. The mixture was then placed on ice for 30 min, heat shock treated at 42 °C for 90 s and chilled on ice for another 3 min. 900 μL LB was added to the tube and the cells were recovered at 37 °C with shake vigorously for 1 h. Finally, 50–100 μL mixture was spread onto selection plate and incubated overnight at 37 °C.
The biomass concentration was monitored by measuring the optical density at 600 nm (OD600). Dry cell weight (DCW) was calculated on the basis of OD600 (1 OD600 = 0.42 g DCW/L) .
Quantitative PCR was performed using GoTaq qPCR master mix (Promega, USA) in a 20-μL mixture with a LightCycler® 96 RealTime PCR System (Roche, Switzerland) according to our previous report .
Fermentation samples were centrifuged at 8000g for 5 min, and the supernatants were used for analysis of the substrate and product concentrations. The concentration of glucose was assayed with an enzyme electrode analyser (SBA-40D; Institute of Biology, Shandong, China) containing glucose oxidase.
Amino acids were quantified by an HPLC (1200 series; Agilent Technologies, USA) equipped with an Eclipse XDB-C18 column (4.6 mm × 150 mm; Agilent Technologies, USA). UV absorption was performed at 360 nm. Samples were pre-column derivatized with 2,4-dinitrofluorobenzene as the derivatization reagent. The gradient mobile phase was set as in our previous report . In addition, 2-ketobutyrate was quantified by an HPLC equipped with a Zorbax SB-Aq column (4.6 × 250 mm; Agilent Technologies, USA), and 20 mM KH2PO4 (pH 2.2) was used as a mobile phase with a flow rate of 0.5 mL/min. UV absorption was measured at 210 nm. The 1-propanol was analysed using a Gas Chromatograph Mass Spectrometer (GCMSQP2010 Ultra, Shimadzu, Japan) connected to an AOC-20i Auto-sample using a TG-WAXMS (length: 30 m; I.D.: 0.25 mm; film: 0.25 μm) (Thermo Scientific, USA). The samples were directly diluted 1:10 with methanol and the operating set up followed as the previous report . The concentration was determined according to a calibration curve with an external standard. The peaks were identified by retention time and quantified using the intensity of the peak at one specific m/z value according to our previous report .
Availability of supporting data
All data generated or analysed during this study are included in this published article (and its additional file).
international Genetic Engineered Machine
clustered regularly interspaced short palindromic repeat
- E. coli :
high-performance liquid chromatography
- NADPH and NADP:
reduced and oxidized form of nicotinamide adenine dinucleotide phosphate, respectively
- OD600 :
optical density at wavelength (λ) 600 nm
Li ZJ, Qiao KJ, Che XM, Stephanopoulos G. Metabolic engineering of Escherichia coli for the synthesis of the quadripolymer poly(glycolate-co-lactate-co-3-hydroxybutyrate-co-4-hydroxybutyrate) from glucose. Metab Eng. 2017;44:38–44.
Lee SY, Kim HU. Systems strategies for developing industrial microbial strains. Nat Biotechnol. 2015;33:1061–72.
Shaw AJ, Lam FH, Hamilton M, Consiglio A, MacEwen K, Brevnova EE, Greenhagen E, LaTouf WG, South CR, van Dijken H, et al. Metabolic engineering of microbial competitive advantage for industrial fermentation processes. Science. 2016;353:583–6.
Nielsen J, Keasling JD. Engineering Cellular Metabolism. Cell. 2016;164:1185–97.
Chao R, Mishra S, Si T, Zhao HM. Engineering biological systems using automated biofoundries. Metab Eng. 2017;42:98–108.
Hughes RA, Ellington AD. Synthetic DNA synthesis and assembly: putting the synthetic in synthetic biology. Cold Harb Spring Lab Perspect Biol. 2017;9:a023812.
Becker J, Wittmann C. Systems and synthetic metabolic engineering for amino acid production—the heartbeat of industrial strain development. Curr Opin Biotechnol. 2012;23:718–26.
D’Este M, Alvarado-Morales M, Angelidaki I. Amino acids production focusing on fermentation technologies—a review. Biotechnol Adv. 2018;36:14–25.
Wendisch VF. Metabolic engineering advances and prospects for amino acid production. Metab Eng. 2019. https://doi.org/10.1016/j.ymben.2019.03.008
Hirasawa T, Shimizu H. Recent advances in amino acid production by microbial cells. Curr Opin Biotechnol. 2016;42:133–46.
Ma Q, Zhang Q, Xu Q, Zhang C, Li Y, Fan X, Xie X, Chen N. Systems metabolic engineering strategies for the production of amino acids. Synth Syst Biotechnol. 2017;2:87–96.
Sarrion-Perdigones A, Falconi EE, Zandalinas SI, Juarez P, Fernandez-del-Carmen A, Granell A, Orzaez D. GoldenBraid: an iterative cloning system for standardized assembly of reusable genetic modules. Plos ONE. 2011;6:e21622.
Van Hove B, Guidi C, De Wannemaeker L, Maertens J, De Mey M. Recursive DNA assembly using Protected Oligonucleotide Duplex Assisted Cloning (PODAC). Acs Synth Biol. 2017;6:943–9.
Yamazaki K-i, de Mora K, Saitoh K. BioBrick-based ‘Quick Gene Assembly’ in vitro. Synth Biol. 2017;2:ysx003.
Basitta P, Westrich L, Rosch M, Kulik A, Gust B, Apel AK. AGOS: a plug-and-play method for the assembly of artificial gene operons into functional biosynthetic gene clusters. Acs Synth Biol. 2017;6:817–25.
Weninger A, Killinger M, Vogl T. Key methods for synthetic biology: genome engineering and DNA assembly. Cham: Springer; 2016.
Li SY, Zhao GP, Wang J. C-Brick: a new standard for assembly of biological parts using Cpf1. ACS Synth Biol. 2016;5:1383–8.
Andreou AI, Nakayama N. Mobius Assembly: a versatile Golden-Gate framework towards universal DNA assembly. Plos ONE. 2018;13:e0189892.
Shetty RP, Endy D, Knight TF Jr. Engineering BioBrick vectors from BioBrick parts. J Biol Eng. 2008;2:5.
Smolke CD. Building outside of the box: iGEM and the BioBricks Foundation. Nat Biotechnol. 2009;27:1099–102.
Vick JE, Johnson ET, Choudhary S, Bloch SE, Lopez-Gallego F, Srivastava P, Tikh IB, Wawrzyn GT, Schmidt-Dannert C. Optimized compatible set of BioBrick(™) vectors for metabolic pathway engineering. Appl Microbiol Biotechnol. 2011;92:1275–86.
Xu P, Vansiri A, Bhan N, Koffas MAG. ePathBrick: a synthetic biology platform for engineering metabolic pathways in E. coli. ACS Synth Biol. 2012;1:256–66.
Pasini M, Fernandez-Castane A, Jaramillo A, de Mas C, Caminal G, Ferrer P. Using promoter libraries to reduce metabolic burden due to plasmid-encoded proteins in recombinant Escherichia coli. New Biotechnol. 2016;33:78–90.
Anderson JC, Dueber JE, Leguia M, Wu GC, Goler JA, Arkin AP, Keasling JD. BglBricks: a flexible standard for biological part assembly. J Biol Eng. 2010;4:1.
Liu JK, Chen WH, Ren SX, Zhao GP, Wang J. iBrick: A new standard for iterative assembly of biological parts with homing endonucleases. Plos ONE. 2014;9:e110852.
Popp PF, Dotzler M, Radeck J, Bartels J, Mascher T. The Bacillus BioBrick Box 2.0: expanding the genetic toolbox for the standardized work with Bacillus subtilis. Sci Rep. 2017;7:15058.
Lei C, Li SY, Liu JK, Zheng X, Zhao GP, Wang J. The CCTL (Cpf1-assisted Cutting and Taq DNA ligase-assisted Ligation) method for efficient editing of large DNA constructs in vitro. Nucleic Acids Res. 2017;45:e74.
Wong L, Engel J, Jin E, Holdridge B, Xu P. YaliBricks, a versatile genetic toolkit for streamlined and rapid pathway engineering in Yarrowia lipolytica. Metab Eng Commun. 2017;5:68–77.
Sleight SC, Bartley BA, Lieviant JA, Sauro HM. In-Fusion BioBrick assembly and re-engineering. Nucleic Acids Res. 2010;38:2624–36.
Engler C, Kandzia R, Marillonnet S. A one pot, one step, precision cloning method with high throughput capability. Plos ONE. 2008;3:e3647.
Vazquez-Vilar M, Quijano-Rubio A, Fernandez-del-Carmen A, Sarrion-Perdigones A, Ochoa-Fernandez R, Ziarsolo P, Blanca J, Granell A, Orzaez D. GB3.0: a platform for plant bio-design that connects functional DNA elements with associated biological data. Nucleic Acids Res. 2017;45:2196–209.
Weber E, Engler C, Gruetzner R, Werner S, Marillonnet S. A Modular Cloning system for standardized assembly of multigene constructs. Plos ONE. 2011;6:e16765.
Iverson SV, Haddock TL, Beal J, Densmore DM. CIDAR MoClo: Improved MoClo assembly standard and new E. coli Part Library enable rapid combinatorial design for synthetic and traditional Biology. Acs Synth Biol. 2016;5:99–103.
Obst U, Lu TK, Sieber V. A Modular toolkit for generating Pichia pastoris secretion libraries. Acs Synth Biol. 2017;6:1016–25.
Engler C, Youles M, Gruetzner R, Ehnert TM, Werner S, Jones JDG, Patron NJ, Marillonnet S. A Golden Gate modular cloning toolbox for plants. Acs Synth Biol. 2014;3:839–43.
Duportet X, Wroblewska L, Guye P, Li YQ, Eyquem J, Rieders J, Rimchala T, Batt G, Weiss R. A platform for rapid prototyping of synthetic gene networks in mammalian cells. Nucleic Acids Res. 2014;42:13440–51.
Hillson NJ, Rosengarten RD, Keasling JD. j5 DNA Assembly design automation software. Acs Synth Biol. 2012;1:14–21.
Crook NC, Freeman ES, Alper HS. Re-engineering multicloning sites for function and convenience. Nucleic Acids Res. 2011;39:e92.
Casini A, Storch M, Baldwin GS, Ellis T. Bricks and blueprints: methods and standards for DNA assembly. Nat Rev Mol Cell Biol. 2015;16:568–76.
Ellis T, Adie T, Baldwin GS. DNA assembly for synthetic biology: from parts to pathways and beyond. Integr Biol. 2011;3:109–18.
Smanski MJ, Bhatia S, Zhao DH, Park Y, Woodruff LBA, Giannoukos G, Ciulla D, Busby M, Calderon J, Nicol R, et al. Functional optimization of gene clusters by combinatorial design and assembly. Nat Biotechnol. 2014;32:1241.
Taylor GM, Mordaka PM, Heap JT. Start-Stop Assembly: a functionally scarless DNA assembly system optimized for metabolic engineering. Nucleic Acids Res. 2018;47:e17.
Vogl T, Ahmad M, Krainer FW, Schwab H, Glieder A. Restriction site free cloning (RSFC) plasmid family for seamless, sequence independent cloning in Pichia pastoris. Microb Cell Fact. 2015;14:103.
Ho SN, Hunt HD, Horton RM, Pullen JK, Pease LR. Site-directed mutagenesis by overlap extension using the Polymerase Chain-Reaction. Gene. 1989;77:51–9.
Mead DA, Pey NK, Herrnstadt C, Marcil RA, Smith LM. A Universal method for the direct cloning of PCR Amplified Nucleic Acid. Bio-Technol. 1991;9:657–63.
Chen WH, Qin ZJ, Wang J, Zhao GP. The MASTER (methylation-assisted tailorable ends rational) ligation method for seamless DNA assembly. Nucleic Acids Res. 2013;41:e93.
Liang J, Liu ZH, Low XZ, Ang EL, Zhao HM. Twin-primer non-enzymatic DNA assembly: an efficient and accurate multi-part DNA assembly method. Nucleic Acids Res. 2017;45:e94.
Jin P, Ding WW, Du GC, Chen J, Kang Z. DATEL: a scarless and sequence-independent dna assembly method using thermostable exonucleases and ligase. Acs Synth Biol. 2016;5:1028–32.
Yuzbashev TV, Vybornaya TV, Larina AS, Gvilava IT, Voyushina NE, Mokrova SS, Yuzbasheva EY, Manukhov IV, Sineoky SP, Debabov VG. Directed modification of Escherichia coli metabolism for the design of threonine-producing strains. Appl Biochem Microbiol. 2013;49:723–42.
Shiio I NS, Sano K. Fermentative production of l-threonine. 1971.
Shen CR, Liao JC. Synergy as design principle for metabolic engineering of 1-propanol production in Escherichia coli. Metab Eng. 2013;17:12–22.
Tseng HC, Prather KLJ. Controlled biosynthesis of odd-chain fuels and chemicals via engineered modular metabolic pathways. P Natl Acad Sci USA. 2012;109:17925–30.
Lee JH, Sung BH, Kim MS, Blattner FR, Yoon BH, Kim JH, Kim SC. Metabolic engineering of a reduced-genome strain of Escherichia coli for l-threonine production. Microb Cell Fact. 2009;8:2.
Rieping M, Hermann T. l-Threonine. Microbiol Monogr (5), V F Wendisch: Amino acid biosynthesis. Springer-Verlag Berlin Heidelberg. 2006.
Dong X, Quinn PJ, Wang X. Metabolic engineering of Escherichia coli and Corynebacterium glutamicum for the production of l-threonine. Biotechnol Adv. 2010;29:11–23.
Wei L, Xu N, Wang YR, Zhou W, Han GQ, Ma YH, Liu J. Promoter library-based module combination (PLMC) technology for optimization of threonine biosynthesis in Corynebacterium glutamicum. Appl Microbiol Biot. 2018;102:4117–30.
Jeschek M, Gerngross D, Panke S. Combinatorial pathway optimization for streamlined metabolic engineering. Curr Opin Biotechnol. 2017;47:142–51.
Lee KH, Park JH, Kim TY, Kim HU, Lee SY. Systems metabolic engineering of Escherichia coli for l-threonine production. Mol Syst Biol. 2007;3:149.
Sauer U, Eikmanns BJ. The PEP-pyruvate-oxaloacetate node as the switch point for carbon flux distribution in bacteria. FEMS Microbiol Rev. 2005;29:765–94.
Akashi H, Gojobori T. Metabolic efficiency and amino acid composition in the proteomes of Escherichia coli and Bacillus subtilis. P Natl Acad Sci USA. 2002;99:3695–700.
Kruse D, Kramer R, Eggeling L, Rieping M, Pfefferle W, Tchieu JH, Chung YJ Jr, Saier MH, Burkovski A. Influence of threonine exporters on threonine production in Escherichia coli. Appl Microbiol Biotechnol. 2002;59:205–10.
Simic P, Willuhn J, Sahm H, Eggeling L. Identification of glyA (encoding serine hydroxymethyltransferase) and its use together with the exporter ThrE to increase l-threonine accumulation by Corynebacterium glutamicum. Appl Environ Microbiol. 2002;68:3321–7.
Lee JW, Choi S, Park JH, Vickers CE, Nielsen LK, Lee SY. Development of sucrose-utilizing Escherichia coli K-12 strain by cloning beta-fructofuranosidases and its application for l-threonine production. Appl Microbiol Biotechnol. 2010;88:905–13.
Eggeling L. Exporters for production of amino acids and other small molecules. Adv Biochem Eng Biotechnol. 2017;159:199–225.
Alper H, Fischer C, Nevoigt E, Stephanopoulos G. Tuning genetic control through promoter engineering. Proc Natl Acad Sci USA. 2005;102:12678–83.
Mutalik VK, Guimaraes JC, Cambray G, Lam C, Christoffersen MJ, Mai QA, Tran AB, Paull M, Keasling JD, Arkin AP, et al. Precise and reliable gene expression via standard transcription and translation initiation elements. Nat Methods. 2013;10:354–60.
Diesveld R, Tietze N, Furst O, Reth A, Bathe B, Sahm H, Eggeling L. Activity of exporters of Escherichia coli in Corynebacterium glutamicum, and their use to increase l-threonine production. J Mol Microbiol Biotechnol. 2009;16:198–207.
Lee JH, Jung SC, Bui LM, Kang KH, Song JJ, Kim SC. Improved production of l-threonine in Escherichia coli by use of a dna scaffold system. Appl Environ Microbiol. 2013;79:774–82.
Liu SW, Liang Y, Liu Q, Tao TT, Lai SJ, Chen N, Wen TY. Development of a two-stage feeding strategy based on the kind and level of feeding nutrients for improving fed-batch production of l-threonine by Escherichia coli. Appl Microbiol Biot. 2013;97:573–83.
Jiang Y, Chen B, Duan CL, Sun BB, Yang JJ, Yang S. Multigene editing in the Escherichia coli genome via the CRISPR-Cas9 system. Appl Environ Microb. 2015;81:2506–14.
Hommelsheim CM, Frantzeskakis L, Huang MM, Ulker B. PCR amplification of repetitive DNA: a limitation to genome editing technologies and many other applications. Sci Rep. 2014;4:5052.
Srirangan K, Akawi L, Liu XJ, Westbrook A, Blondeel EJM, Aucoin MG, Moo-Young M, Chou CP. Manipulating the sleeping beauty mutase operon for the production of 1-propanol in engineered Escherichia coli. Biotechnol Biofuels. 2013;6:139.
Siebert D, Wendisch VF. Metabolic pathway engineering for production of 1,2-propanediol and 1-propanol by Corynebacterium glutamicum. Biotechnol Biofuels. 2015;8:91.
Chao R, Yuan YB, Zhao HM. Recent advances in DNA assembly technologies. FEMS Yeast Res. 2015;15:1–9.
Yu D, Tan YN, Sun ZZ, Sun XW, Sheng XB, Zhou TS, Liu L, Mo Y, Jiang BB, Ouyang N, et al. In Vitro Seamless stack enzymatic assembly of dna molecules based on a strategy involving splicing of restriction sites. Sci Rep. 2017;7:14261.
Zhang F, Cong L, Lodato S, Kosuri S, Church GM, Arlotta P. Efficient construction of sequence-specific TAL effectors for modulating mammalian transcription. Nat Biotechnol. 2011;29:149.
Ridley CP, Lee HY, Khosla C. Evolution of polyketide synthases in bacteria. Proc Natl Acad Sci USA. 2008;105:4595–600.
Choi YJ, Park JH, Kim TY, Lee SY. Metabolic engineering of Escherichia coli for the production of 1-propanol. Metab Eng. 2012;14:477–86.
Kaufman DL, Evans GA. Restriction endonuclease cleavage at the termini of PCR products. Biotechniques. 1990;9:304–6.
Yao S, Hart DJ, An Y. Recent advances in universal TA cloning methods for use in function studies. Protein Eng Des Sel. 2016;29:551–6.
Halleran AD, Swaminathan A, Murray RM. Single day construction of multigene circuits with 3G assembly. Acs Synth Biol. 2018;7:1477–80.
Biggs BW, De Paepe B, Santos CNS, De Mey M, Ajikumar PK. Multivariate modular metabolic engineering for pathway and strain optimization. Curr Opin Biotechnol. 2014;29:156–62.
Chen XL, Gao C, Guo L, Hu GP, Luo QL, Liu J, Nielsen J, Chen J, Liu LM. DCEO Biotechnology: tools to design, construct, evaluate, and optimize the metabolic pathway for biosynthesis of chemicals. Chem Rev. 2017;118:4–72.
Moore SJ, Lai HE, Kelwick RJR, Ghee SM, Bell DJ, Polizzi KM, Freemont PS. EcoFlex: a multifunctional MoClo Kit for E. coli synthetic biology. Acs Synth Biol. 2016;5:1059–69.
Guye P, Li YQ, Wroblewska L, Duportet X, Weiss R. Rapid, modular and reliable construction of complex mammalian gene circuits. Nucleic Acids Res. 2013;41:156.
Li MV, Shukla D, Rhodes BH, Lall A, Shu JM, Moriarity BS, Largaespada DA. HomeRun vector assembly system: a flexible and standardized cloning system for assembly of multi-modular DNA constructs. Plos ONE. 2014;9:e100948.
Martinez-Garcia E, Aparicio T, Goni-Moreno A, Fraile S, de Lorenzo V. SEVA 2.0: an update of the Standard European Vector Architecture for de-/re-construction of bacterial functionalities. Nucleic Acids Res. 2015;43:D1183–9.
Wang L, Deng A, Zhang Y, Liu S, Liang Y, Bai H, Cui D, Qiu Q, Shang X, Yang Z, et al. Efficient CRISPR–Cas9 mediated multiplex genome editing in yeasts. Biotechnol Biofuels. 2018;11:277.
Zhang Y, Cai JY, Shang XL, Wang B, Liu SW, Chai X, Tan TW, Zhang Y, Wen TY. A new genome-scale metabolic model of Corynebacterium glutamicum and its application. Biotechnol Biofuels. 2017;10:169.
Wang B, Hu Q, Zhang Y, Shi R, Chai X, Liu Z, Shang X, Zhang Y, Wen T. A RecET-assisted CRISPR–Cas9 genome editing in Corynebacterium glutamicum. Microb Cell Fact. 2018;17:63.
We thank Prof. Jun Wang for critical reading of this manuscript and providing valuable suggestions. We also thank Dr. Guoxia Liu and Wenzhao Wang for assistance with the GC–MS and Real-Time Reverse Transcription-PCR.
This work was supported by the Strategic Priority Research Program of the Chinese Academy of Sciences (XDA17010503), National Natural Science Foundation of China (31800073), Youth Innovation Promotion Association of the Chinese Academy of Sciences (2018117).
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