- Open Access
Metabolic engineering of Escherichia coli for the production of riboflavin
Microbial Cell Factories volume 13, Article number: 104 (2014)
Riboflavin (vitamin B2), the precursor of the flavin cofactors flavin mononucleotide (FMN) and flavin adenine dinucleotide (FAD), is used commercially as an animal feed supplement and food colorant. E. coli is a robust host for various genetic manipulations and has been employed for efficient production of biofuels, polymers, amino acids, and bulk chemicals. Thus, the aim of this study was to understand the metabolic capacity of E. coli for the riboflavin production by modification of central metabolism, riboflavin biosynthesis pathway and optimization of the fermentation conditions.
The basic producer RF01S, in which the riboflavin biosynthesis genes ribABDEC from E. coli were overexpressed under the control of the inducible trc promoter, could accumulate 229.1 mg/L of riboflavin. Further engineering was performed by examining the impact of expression of zwf (encodes glucose 6-phosphate dehydrogenase) and gnd (encodes 6-phosphogluconate dehydrogenase) from Corynebacterium glutamicum and pgl (encodes 6-phosphogluconolactonase) from E. coli on riboflavin production. Deleting pgi (encodes glucose-6-phosphate isomerase) and genes of Entner-Doudoroff (ED) pathway successfully redirected the carbon flux into the oxidative pentose phosphate pathway, and overexpressing the acs (encodes acetyl-CoA synthetase) reduced the acetate accumulation. These modifications increased riboflavin production to 585.2 mg/L. By further modulating the expression of ribF (encodes riboflavin kinase) for reducing the conversion of riboflavin to FMN in RF05S, the final engineering strain RF05S-M40 could produce 1036.1 mg/L riboflavin in LB medium at 37°C. After optimizing the fermentation conditions, strain RF05S-M40 produced 2702.8 mg/L riboflavin in the optimized semi-defined medium, which was a value nearly 12-fold higher than that of RF01S, with a yield of 137.5 mg riboflavin/g glucose.
The engineered strain RF05S-M40 has the highest yield among all reported riboflavin production strains in shake flask culture. This work collectively demonstrates that E. coli has a potential to be a microbial cell factory for riboflavin bioproduction.
Riboflavin (vitamin B2) is the universal precursor of flavin mononucleotide (FMN) and flavin adenine dinucleotide (FAD), both of which act as hydrogen carriers and are essential for the activity of a wide variety of metabolic enzymes in higher eukaryotes [1,2]. Riboflavin is synthesized by all plants, fungi and most bacteria, but not by higher animals including humans. So humans and animals must obtain riboflavin through dietary sources . Traditionally, riboflavin was synthesized and produced by chemical procedures or microbial fermentation. Since chemical synthesis of riboflavin has many disadvantages such as high cost and energy wasting, the microbial fermentation method has been widely applied in industrial production.
Riboflavin biosynthesis has been studied in both gram-positive and gram-negative bacteria, extensively in Bacillus subtilis and E. coli. Riboflavin is synthesized from one molecule of GTP and two molecules of ribulose 5-phosphate (Ru-5-P) through a seven-step synthetic pathway, which is similar in all organisms (Figure 1) . Riboflavin has been produced by the filamentous fungus Ashbya gossypii, the yeast Candida famata, and the bacterium B. subtilis, all of which have been developed by using a combined approach of classical mutagenesis and rational metabolic engineering [3,5]. Thus, the genetic background of these strains was usually complicated and the mechanism of riboflavin overproduction was not fully elucidated.
In a series of previous reports, a numbers of conceivable strategies were carried out to develop B. subtilis as a riboflavin-producing strain after selection for resistance to different antimetabolites. In B. subtilis, the riboflavin production was increased by amplifying copies of rib operon or ribA gene [6,7], or by enhancing the energy generation and reducing the maintenance metabolism [8–10]. Other efforts focused on modulating precursor metabolites supply by increasing the carbon flow through the pentose phosphate pathway (PP pathway) [11–14], by deregulating the gluconeogenesis flux via inactivating the ccpN , or by enhancing the flux of purine synthesis pathway [16,17].
E. coli has been employed for efficient production of biofuels, amino acids, and bulk chemicals [18–20]. Although wild type E. coli does not accumulate riboflavin under natural conditions, it may be an efficient host for the production of riboflavin due to its clear genetic background, fast-growing, low maintenance metabolism, and the presence of convenient metabolic engineering tools. Thus, the aim of this study was to understand the metabolic capacity of E. coli for the production of riboflavin by modification of central metabolism, riboflavin biosynthesis pathway and optimization of the fermentation conditions.
In this study, the riboflavin synthetic pathway from E. coli and B. subtilis was constructed and compared in E. coli MG1655. Then, we examined the impact of overexpressing mutation type of zwf and gnd genes from C. glutamicum and pgl from E. coli on riboflavin production. Third, the glycolysis and ED pathway were modified to reroute carbon flux to the PP pathway for improving the riboflavin synthesis. Fourth, the acetate accumulation was reduced by overexpressing the acs gene. Finally, riboflavin production was significantly increased by modulating the expression of ribF. We also optimized the fermentation conditions for the riboflavin production. The final recombinant strain RF05S-M40 produced 2702.8 mg/L riboflavin with a yield of 137.5 mg riboflavin/g glucose under the optimized batch fermentation condition.
Results and discussion
Construction of riboflavin synthetic pathway
Previous researches indicated that overexpression of the genes of the riboflavin synthetic pathway contributed to the efficient production of riboflavin. In B. subtilis, introduction of multiple copies of rib operon into the chromosome resulted in improving the riboflavin production . In Pichia pastoris, overexpression of the riboflavin biosynthetic pathway caused riboflavin production increased to 175 mg/L riboflavin although the wild type P. pastoris did not accumulate riboflavin . In C. famata, overexpressing the gene related to the riboflavin production significantly increased riboflavin production .
As shown in Figure 1, the genes of the riboflavin synthetic pathway (ribA, ribB, ribD, ribE, ribC) from E. coli were assembled into an artificial operon called EC10, under the control of the inducible trc promoter (Ptrc). Since the enzymatic activity of GTP cyclohydrolase II and 3, 4-dihydroxy-2-butanone 4-phosphate synthase played a critical role in riboflavin biosynthesis [21–23], the corresponding encoding genes ribA and ribB from E. coli were rearranged as the first and second genes in the operon. To test the dosage effect of the operon on riboflavin production, EC10 was inserted into plasmids with different copy numbers, generating p5C-EC10, p15C-EC10 and p20C-EC10, which have pSC101, p15A and pBR322 replication origin, respectively. Wild type E. coli MG1655, harboring p5C-EC10, p15C-EC10 and p20C-EC10, produced 50.5±1.2, 88.6±7.0 and 229.1±5.7 mg/L riboflavin (Figure 2), respectively. These results indicated that higher copy number of riboflavin synthetic genes was beneficial for riboflavin overproduction, which was in accordance with previously published results [3,7].
The traditional gene names are different in E. coli and B. subtilis (Figure 1). For consistency, we use the E. coli gene names throughout. Thus, the B. subtilis ribA, ribD, ribH, ribE genes are renamed to ribB/A, ribD, ribE, ribC, respectively (Figure 1). To test the productivity of the riboflavin pathway from B. subtilis, plasmid p20C-BSrib was constructed by directly inserting the native rib operon from the genome of B. subtilis into p20C. MG1655 harboring p20C-BSrib produced 200.5±7.1 mg/L riboflavin (Figure 2). Moreover, to construct a synthetic operon devoid of native regulation, the riboflavin pathway genes from B. subtilis were individually amplified, rearranged according to the order in the metabolic pathway (BSrib(B/A)DEC), and assembled into p20C, creating plasmid p20C-BS15. E. coli MG1655 harboring p20C-BS15 produced 180.3±5.6 mg/L riboflavin (Figure 2), which was slightly lower than that of p20C-BSrib. Moreover, the activities of key enzymes of riboflavin synthesis, GTP cyclohydrolase II and riboflavin synthase in MG1655(p20C-BS15) were lower than that in MG1655(p20C-BSrib) (Table 1). This phenomenon may be due to that the internal promoters of native rib operon were removed after rearranging the gene order , which led to a decrease in the expression level of key genes ribB/A and ribC. Among all the tested rib gene expressing plasmids, p20C-EC10 showed the highest riboflavin productivity. Thus, strain RF01S (MG1655 harboring p20C-EC10) was selected for further engineering.
Effects of zwf, gnd, and pgl overexpression on riboflavin production
Ribulose 5-phosphate is an important precursor for riboflavin biosynthesis. Overexpressing the genes of oxidative PP pathway increased the ribulose 5-phosphate supply and improved riboflavin production by 31% in B. subtilis . Mutant genes zwf (A243T)  and gnd (S361F)  from C. glutamicum, which encode glucose 6-phosphate dehydrogenase and 6-phosphogluconate dehydrogenase with removal of feedback inhibition, were co-overexpressed by introducing plasmid p15Trc-zg into RF01S. As shown in Table 2, the enzyme activities of glucose 6-phosphate dehydrogenase and 6-phosphogluconate dehydrogenase were significantly increased. However, the resulting strain showed only a slight increase in riboflavin titer and yield, compared to that harboring p15Trc (Table 2). Due to the low endogenous activity of 6-phosphogluconolactonase in E. coli [27,28], we further overexpressed pgl (encoding 6-phosphogluconolactonase) from E. coli along with zwf and gnd by transforming p15Trc-zgp into RF01S, which led to an increase of 18.9% and 38.7% in riboflavin titer and yield, compared to that harboring p15Trc (Table 2). However, compared to strain RF01S, overexpressing PP pathway genes did not significantly increase the riboflavin production, possibly because of the complex regulation of central metabolic pathway  and a high metabolic burden of heterologous protein production .
Disruption of pgi for improving riboflavin production
Based on the results of overexpressing the genes of PP pathway, the strategy of eliminating competitive pathway for redirecting the carbon flux into the oxidative PP pathway was employed to improve the riboflavin production. The disruption of pgi encoding phosphoglucose isomerase resulted in a blocked entry into glycolysis and compelled glucose 6-phosphate to be metabolized exclusively through PP pathway . Thus, we disrupted pgi in MG1655, creating RF02. RF02 harboring p20C-EC10 (RF02S) accumulated 394.8±19.6 mg/L riboflavin, which was 72.4% higher than that of the reference strain RF01S (Table 3). In accord with previous studies, the Δpgi mutant strains showed strongly reduced glucose uptake rates and maximum specific growth rate . One possible reason for this phenomenon was that the Δpgi mutation would result in high glucose 6-phosphate pool and led to the rapid degradation of ptsG mRNA, an important member of the PTS transport systems, which would decrease the glucose uptake capacity . Moreover, the Δpgi mutation also diminishes the supply of PEP needed for PTS-mediated uptake of glucose and decreases the growth rate .
Disruption of edd and eda for improving riboflavin production
The ED pathway has been shown to be inactive with glucose as the carbon source in wild-type E. coli , but it was activated in the pgi mutant strain . Previous studies indicated that glucose was mainly metabolized through PP pathway and partially through ED pathway after pgi was disrupted .
The edd and eda transcription levels in the Δpgi strain RF02 were compared with parent strain MG1655 through RT-qPCR analysis. Consistent with previously research , the transcript abundance of edd and eda increased 2.21-fold and 2.36-fold in RF02, respectively, which indicated that ED pathway was up-regulated in Δpgi strain. Thus, edd and eda were disrupted in RF02 for further increasing the flux from 6-phosphogluconate to Ru-5-P, resulting in strain RF03. RF03 harboring p20C-EC10 (strain RF03S) produced 559.88±8.99 mg/L riboflavin, which increased by 41.8% compared to that of RF02S (Table 3). These results suggested that further increasing riboflavin precursors can be achieved via disrupting ED pathway in the pgi mutation strain.
Effect of the acs promoter insertion on riboflavin production
Acetate, which led to growth retardation, was the main byproduct of these recombinant strains. Thus, the strategy of overexpressing the acs gene encoding acetyl-CoA synthetase was selected to reduce acetate secretion. The trc promoter was inserted in the upstream of acs gene in RF03, resulting in strain RF05. RT-qPCR analysis showed that the expression of acs gene in RF05S (RF05 harboring p20C-EC10) increased 4.80-fold compared with RF03S, indicating successful overexpression of acs gene. RF05S produced 585.2±13.6 mg/L riboflavin with a yield of 59.30 mg/g glucose, which did not change significantly compared to RF03S (Table 3). However, the acetate production decreased from 4.0 g/l to 1.5 g/L in strain RF05S, which was in accordance with the results presented by Lin et al. .
Modulating the expression ribF for enhanced riboflavin production
According to previous studies, introducing a mutation in ribC gene (encoding flavokinase/flavin adenine dinucleotide synthetase) in B. subtilis could reduce enzymatic activity and resulted in riboflavin overproduction in the engineering strains . The ribC mutation of B. subtilis also reduced the synthesis of FMN, which is a negative regulatory factor of rib operon transcription . In E. coli, these enzymes were encoded by ribF, which is an essential gene for strain growth . Therefore, we speculate that reducing the expression level ribF might reduce the conversion of riboflavin to FMN/FAD and increase riboflavin production.
To modulate the expression of ribF, we designed a library of RBS sequences with varied strengths weaker than that of the native ribF RBS using RBS calculator . Then, the native RBS of ribF on the chromosome of RF05S was replaced with the designed RBS library using the method described in methods. Forty three mutants were selected and transformed with p20C-EC10 to screen for enhanced riboflavin producer. Riboflavin production of the selected strains was measured after 48 h cultivation in LB medium with 10 g/L glucose at 37°C in flasks. The majority of the selected strains exhibited increased riboflavin production compared with the parent strain (Figure 3), which demonstrated that modulating ribF expression could efficiently increase riboflavin production. Strain RF05S-M40 produced 1036.1±54.6 mg/L riboflavin, which was the highest among all selected strains, and was 77.0% higher than that of RF05S. Representative profiles of riboflavin production, biomass accumulation and glucose consumption for the strain RF05S-M40 were shown in Figure 4A. Flavokinase activity in cell-free extracts of RF05S was about 1.45±0.09 nmol/min/mg protein, while that of RF05S-M40 was about 0.94±0.04 nmol/min/mg protein, indicating that the expression level of flavokinase was decreased by modulating the RBS of ribF and this reduced expression contributed much to riboflavin overproduction.
Optimization of fermentation conditions for riboflavin production
To optimize fermentation condition, we investigated the effect of different culture temperatures on riboflavin production. Changing the fermentation temperature from 37°C to 31°C increased riboflavin titer to 1507.0±56.8 mg/L from 1036.1±54.6 mg/L (Figure 4B). Many factors may have contributed to the enhanced production. For example, growth temperature was reported to influence not only recombinant gene expression and protein folding, but also the global metabolism of the strains . In addition, low growth temperature was reported to stabilize the recombinant proteins and improve the plasmid stability .
We further evaluated the riboflavin production of RF05S-M40 in semi-synthetic medium. Two different semi-synthetic medium formulations, M9 minimal medium and MS medium, were tested with different concentration of yeast extract at 37°C or 31°C (Table 4). When cells were cultivated in M9 minimal medium with 1 g/L yeast extract at 37°C, cell growth was severely hampered (OD 600 of 4), leading to a titer of 271.8±4.9 mg/L riboflavin (Table 4). Switching to another defined semi-synthetic medium (MS medium) led to much higher titers (Table 4). Using MS medium with 5 g/L yeast extract as culture medium exhibited the highest productivity in shake flask culture at 31°C. Optimization of the composition of MS medium further increased riboflavin production. Detailed composition of the optimized MS medium and riboflavin production profile were shown in Additional file 1: Table S2. Statistical analysis indicated that the adding of glycine in the medium contributed significantly to riboflavin overproduction. The reason for the increase in the riboflavin production might be that the supplement of glycine, which is an important purine precursor and is incorporated into the riboflavin molecule, enhanced the availability of GTP and thus improved the riboflavin production . Similar phenomenon has been reported in A. gossypii and C. famata .
The time profiles of cell growth, glucose consumption and riboflavin production in the non-optimized medium and the optimized medium were shown in Figure 5. A maximal cell density was attained and residual glucose was almost exhausted after 60 h culture. A maximal riboflavin production reached 2702.8±89.9 mg/L using the optimized medium with a yield of 137.5 mg riboflavin/g glucose in shake flask cultivation, which was 2-fold higher than that of non-optimized medium. The final titer and specific production rates of RF05S-M30 were still lower than that of the industrial producers such as A. gossypii, C. famata, B. subtilis, and Corynebacterium ammoniagenes, which up to 20 g/L riboflavin can be reached with specific production rates of 20.7 mg/g CDW/h in industrial fed-batch production processes [5,13,47]. However, the yields of these industrial producers were lower than that of the recombinant E. coli (e.g. 0.138 for RF05S-M40 versus 0.100 g riboflavin/g glucose for C. famata [22,47]). In addition, the specific glucose uptake rate of RF05S-M40 was still very low. Therefore, improving the glucose uptake rate could be an effective approach to further improving riboflavin production in RF05S-M40. Moreover, several published reports have shown that enhancing the availability of GTP increased the production of in B. subtilis and A. gossypii [16,17,48,49], and thus further engineering the purine pathway might be a possible target for enhancing riboflavin production. In addition, compared with previous studies , the fermentation strategy used in our research is much rougher. The riboflavin titer and productivity of the strain constructed in this work could be further increased by fed-batch fermentation optimization.
For the first time, we constructed a genetically defined riboflavin producing E. coli strain. Riboflavin synthetic pathway, PP pathway, central metabolic pathways, and riboflavin consumption pathway were systematically engineered for direct and efficient conversion of glucose to riboflavin. The E. coli strain RF05S-M40 has the highest yield among all reported riboflavin production strains in shake flask culture. This work also demonstrates that E. coli has a potential to be a host for riboflavin bioproduction.
Strain, medium, and cultivation condition
E. coli K-12 MG1655 (Coli Genetic Stock Center) was selected for engineering of the basic riboflavin-producing strains using a unique gene manipulate method. All strains used in this study are summarized in Table 5. E. coli DH5α was used for the propagation of vector DNA. During strain construction, cultures were grown at 30°C or 37°C in Luria-Bertani (LB) broth (per liter: 10 g tryptone, 5 g yeast extract, 10 g sodium chloride) and supplemented with antibiotics as appropriate.
For the construction of p5C-EC10, p15C-EC10 and p20C-EC10 plasmids, structural genes, including ribA, ribB, ribD, ribE, and ribC, were amplified by PCR with oligonucleotide primers FuECribA-F, FuECribA-R, FuECribB-F, FuECribB-R, FuECribD-F, FuECribD-R, FuECribE-F, FuECribE-R, FuECribC-F, and FuECribC-R using the genomic DNA of E. coli MG1655 as templates. The five fragments, were spliced by overlapping extension (SOE)-PCR , constructing E. coli rib operon EC10, which was then cloned into p5C, p15C, p20C between the EcoRI and HindIII restriction sites. A fragment BSrib containing the riboflavin operon from B. subtilis was amplified with oligonucleotide primers BSrib-F/BSrib-R and cloned into p20C between the EcoRI and BamHI restriction sites, creating plasmid p20C-BSrib. To construct p20C-BS15 plasmid, structural genes, including BDribA, BSribD, BSribH, BSribE, were amplified by PCR with oligonucleotide primers FuBSribA-F, FuBSribA-R, FuBSribD-F, FuBSribD-R, FuBSribH-F, FuBSribH-R, FuBSribE-F and FuBSribE-R using the genomic DNA of B. subtilis 168 as templates. The four fragments were spliced by SOE-PCR, constructing BS15. This was then cloned into p20C, obtaining the expressing plasmid p20C-BS15. Plasmids used were listed in Table 6.
For the construction of p15Trc-zg, zwf (A243T) and gnd (S361F) from C. glutamicum were firstly cloned in a p15A origin vector under the control of Ptrc individually by CPEC  with primer sets p15Trc-1BF, p15Trc-1BR, p15Trc-zwfF, p15Trc-zwfR, p15Trc-gndF, p15Trc-gndR respectively. Then, the zwf (A243T) and gnd (S361F) genes from C. glutamicum and pgl gene from E. coli were assembled into a p15A origin vector under the control of Ptrc by CPEC, obtaining plasmid p15Trc-zgp. All primers were listed in Additional file 1: Table S1, and plasmids constructed were listed in Table 6.
Genome engineering: gene deletion, replacement, and insertion
The strategy of fragment construction and genome manipulation is outlined in Figure 6. The fragments were amplified in three rounds of PCR. In the first round of PCR (Figure 6A), the flanks and the selectable marker are amplified. E. coli chromosome was used as a PCR template to amplify the 5′ flank and the 3′ flank of the target gene. Primers U-F/U-R and L-R/L-F were used to amplify the 5' homologous arm and the 3' homologous arm, respectively. The overlapping marker fragments "tetA-U" and "tetA-L" of the tetA gene were amplified from pTKS/CS using T2/T-F and T1/T-R primers, respectively (Additional file 1: Table S1). The 5′extensions for primers U-R and L-F, containing I-sceI recognition site and 30 bp DR sequence, were complementary to the T-F and T-R primer sequences, respectively. The length of the homologous arms was 250–500 bp as indicated. The second round of PCR, the 5' homologous arm and tet-U, the 3' homologous arm and tet-L were spliced by SOE-PCR, using primer U-F/T2 and T1/L-R, respectively. The final fragment was constructed using SOE-PCR with primer U-F/L-R and electroporated into target cells carrying pTKRED, according to the method of Kuhlman . Firstly, a linear fragment consisting of tetA cassette flank by duplication regions (DRs) and I-SceI recognition sites was used to replace or insert into target site for obtaining an intermediate strain. The tetracycline resistance mutants were selected and confirmed by PCR. Then, arabinose was added to induce I-SceI endonuclease expression for cleaving the tetA and facilitating the recombination between DRs. The loss of tetA in the desired recombinant strains were selected on L-arabinose plates and verified by PCR. This method was employed to delete the pgi, edd, eda, insert trc promoter for acs gene, and modulate the expression of ribF. The primers used during construction are listed in Additional file 1: Table S1.
As mentioned above, the strategy of fragment construction and genome manipulation was used to modulate the expression of ribF. The sequence of primer ribF L_F is TACAAGGTATACTCGGACGATTTTCACTGTHKTGWRCCAGMCATG. The RBS library of ribF, design with RBS Calculator , was placed between the DR sequence (italicized) and the start codon of ribF (bold). The primers used during construction were listed in Additional file 1: Table S1.
Quantitative real-time reverse transcription (RT)-PCR analysis
The recombinant strains were cultured in LB medium with 1% glucose. Cells were harvested when OD600 reached 1. Total mRNA were extracted using the RNAprep pure Cell/Bacteria Kit (Tiangen, Beijing, China) as described by the manufacturer. The cDNA was amplified using FastQuant RT Kit (Tiangen, Beijing, China) with the total mRNA as the templates. Samples were then analyzed using a Light Cycler®480 II (Roche, Basel, Switzerland) with RealMasterMix (SYBR Green I) (Tiangen, Beijing, China). Quantity real-time PCR amplification primers were listed in Additional file 1: Table S1. The rrsA gene was selected as internal standard for normalization and three biological replicates were performed. The obtained data were analyzed by using the 2-ΔΔCt method described previously .
Enzyme assay and preparation of cell extracts
The engineering strains were cultivated in LB medium containing 1% glucose. They were cultured to mid-exponential phase and the cells were harvested by centrifugation for 10 min at 12000×g and 4°C, washed twice with 100 mM potassium phosphate (pH 7.5)-1 mM dithiothreitol-0.1 mM EDTA. The cells were resuspended and sonicated for 5 min in an ice bath (130 W, 20 kHz, pulse: 5 s on; 5 s off). After centrifugation (13,000×g, 10 min, 4°C), the supernatants were used as cell extracts. When necessary, IPTG was used at a concentration of 2 mM for induction. The activities of GTP cyclohydrolase II, riboflavin synthase and flavokinase activity were measured as previously described [54–56]. The activities of glucose 6-phosphate-1-dehydrogenase and 6-phosphogluconate dehydrogenase were determined as previously described . Total protein concentrations were determined by the Bradford method using bovine serum albumin as standard .
Production of riboflavin from glucose
For riboflavin production, LBG medium (LB medium with 1% (W/V) glucose), modified M9 medium, or modified minimal salt (MS) medium was selected. An amount of 20 g/liter glucose or 10 g/liter glucose was added as the carbon source except as indicated. The modified M9 medium contained (per liter) 6 g Na2HPO4, 3 g KH2PO4, 1 g NH4Cl, 0.5 g NaCl, 2 mM MgSO4, 0.1 mM CaCl2, and yeast extract as indicated. The MS medium contained (per liter) 3.8 g Na2HPO4, 1.5 g KH2PO4, 1.0 g (NH4)2SO4, 0.2 g MgSO4, yeast extract as indicated, and 2% (v/v) trace element solution as described in previous studies .
For fermentation, transformed strains were cultured overnight in 5 ml LB media at 37°C, then transferred into 50 ml LB media with 1% (v/v) of the seed culture. This was cultured to mid-exponential phase at 240 rpm, 37°C, and frozen at −80°C in 15% glycerol (v/v). The inoculum was prepared from frozen seed stocks in LB medium supplemented with 100 mg/L ampicillin, grown to mid-exponential phase, and then used to inoculate batch cultures with 1% (v/v) of the seed culture, at 37°C or 31°C as indicated. When appropriate, IPTG was used at a concentration of 2 mM for induction. For each strain, three parallel fermentations were performed.
Cell concentration was calculated from OD 600 nm measurements. Glucose concentration was measured enzymatically using a glucose analyzer (Model-SBA40, Shandong, China). To determine the concentration of acetate, culture samples were centrifuged at 12,000×g for 5 min and the aqueous supernatant used for HPLC analysis on an Agilent 1100 Series HPLC system equipped with an Aminex HPX-87H anion exchange column (Bio-Rad Laboratories, Richmond, CA, USA) and refractive index detector. The column was eluted with 5 mM sulfuric acid at a flow rate of 0.4 ml/min. Standards were prepared for acetate for both the refractive index detector, and calibration curves were created. For riboflavin measurements, culture samples were diluted with 0.05 M NaOH to the linear range of the spectrophotometer and the A444 was immediately measured. The results represented the means±S.D. of three independent experiments. Dry cell weight (DCW) was calculated from the optical density at 600 nm (1 OD600=0.38 g DCW/L).
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The authors thank Dr. Thomas E. Kuhlman for kindly providing requested plasmids. This work was supported by National 973 Project [2011CBA00804, 2012CB725203]; National Natural Science Foundation of China [NSFC-21176182, NSFC-21206112, NSFC-21390201]; and National High-tech R&D Program of China [2012AA02A702, 2012AA022103].
The authors declare that they have no competing interests.
ZQL designed the experiments; ZQL, ZWW, ZBX, and YFL performed the experiments; ZQL, ZWW and TC wrote the manuscript; TC and XMZ supervised the work; and all authors contributed to the discussion of the research. All authors read and approved the final manuscript.
Additional file 1: Table S1.
Primers used in this study. Table S2. Experimental design for evaluating factors influencing biomass and riboflavin production.
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Lin, Z., Xu, Z., Li, Y. et al. Metabolic engineering of Escherichia coli for the production of riboflavin. Microb Cell Fact 13, 104 (2014). https://doi.org/10.1186/s12934-014-0104-5
- Flavin Adenine Dinucleotide
- Minimal Salt Medium
- Riboflavin Production
- Riboflavin Biosynthesis