Abstract
Isopropyl β-D-thiogalactopyranoside (IPTG), while widely utilized for inducing gene expression in systems governed by T7lac and related promoters, poses significant challenges due to its toxicity and expense, prompting the exploration of alternative induction strategies. In this study, we developed a series of inducer-free vitamin B12-producing strains featuring thermally regulated pathway genes. We engineered a thermal switch by replacing the lacI promoter with the PR promoter, which is regulated by the temperature-sensitive repressor cI857 from the λ bacteriophage. As a result, target genes driven by T7lac or other lac-derived promoters containing lac operators were expressed upon lowering the temperature. Our findings indicate that culturing at 37°C and then shifting to 32°C when the optical density at 600 nm reaches 2 is the most effective strategy for vitamin B12 production. Additionally, the vitamin B12 titer increased by 37.96% after introducing an ssrA degradation tag at the C-terminus of lacI. This study introduces a novel strategy for vitamin B12 production that circumvents the need for IPTG by implementing a thermal switch. This approach may have significant implications for chemical bioproduction processes that have traditionally relied on IPTG for gene induction.
Keywords: cI857 Repressor, Escherichia coli, lacI, thermal switch, vitamin B12
Introduction
Vitamin B12 is the most complex vitamin in terms of its structure and synthesis pathway. In nature, its synthesis primarily takes place in microorganisms, with subsequent accumulation in animals through the food chain. The active forms of vitamin B12 include adenosylcobalamin and methylcobalamin. As an essential coenzyme, vitamin B12 plays a critical role in human metabolism, particularly in DNA synthesis, erythrocyte formation, and the maintenance of nerve function [1]. Despite its significance in physiological processes, traditional methods for vitamin B12 production are often characterized by high costs and low efficiency, necessitating the exploration of more effective and economical production techniques by the scientific community. The rapid advancements in synthetic biology and metabolic engineering have shifted attention towards utilizing microbial cell factories for the production of high-value compounds [2]. Escherichia coli is frequently employed as a model organism in metabolic engineering due to its well-characterized genome, rapid growth rate, and ease of genetic manipulation. Recently, we developed 14 antibiotic-free, plasmid-free producers by integrating vitamin B12 pathway genes under the regulation of the T7lac and tac promoters into the E. coli chromosome [3]. The lac operon system, a widely used gene expression regulation mechanism in bacteria, comprises a lac promoter, an operator sequence (lacO), and structural genes (lacZ, lacY, lacA), which can be induced through the addition of IPTG [4, 5]. The T7lac promoter is a hybrid that combines elements from the T7 bacteriophage promoter with lacO, and it is also activated by IPTG. However, the induction of the T7 system with IPTG facilitates rapid protein overexpression, which can overwhelm cellular folding mechanisms and result in the aggregation of misfolded proteins [6, 7]. Studies have indicated that IPTG can heighten cellular sensitivity to various toxic substances, potentially leading to damage in host cells [8-11].
Temperature-sensitive promoters, such as the PR and PL promoters, enable precise regulation of gene expression across varying temperature conditions [12]. The low-temperature induction of cI857 represents an effective strategy for regulating gene expression, particularly in the production of recombinant proteins [13, 14]. The cI857 protein, a temperature-sensitive repressor in the l phage, operates in conjunction with the PL and PR promoters. These promoters inhibit the transcription of downstream genes when the cI857 repressor binds. Specifically, at temperatures below 37°C, the cI857 repressor tightly associates with the promoter, preventing RNA polymerase from binding and thus inhibiting gene transcription. Conversely, when the temperature exceeds 37°C, the cI857 repressor becomes less stable and dissociates from the promoter, allowing RNA polymerase to bind and initiate the transcription of the target gene. This temperature-induced mechanism not only significantly enhances the yield of recombinant proteins but also minimizes issues related to non-specific expression and protein misfolding that may occur at lower temperatures. Furthermore, the design of a thermoinducible T7lac promoter circumvents the toxicity associated with IPTG and enhances the flexibility of gene expression [15]. Although several studies have investigated the expression of the T7 RNA polymerase gene under the heat-inducible l PL promoter to boost recombinant protein yields [16-18], elevated temperatures ranging from 37°C to 42°C are detrimental to vitamin B12 production, while 32°C is identified as the optimal temperature due to the expression of 28 heterologous genes involved in the vitamin B12 biosynthetic pathway [19]. Recently, a low-temperature inducible system for activating the T7lac promoter has been developed [20]. However, the evaluation of this system was conducted in a Luria−Bertani (LB) medium. Previous studies have shown that the presence of lactose in yeast extract promotes the autoinduction of the lacUV5 promoter [21], which complicates the assessment of the precise control afforded by the low-temperature inducible system. Furthermore, it remains to be investigated whether this system can be applied to other promoters.
In this study, we aimed to regulate the genes involved in the vitamin B12 synthesis pathway driven by the T7lac promoter using a thermal switch in E. coli, thereby replacing IPTG induction. We evaluated this system using recombinant strains cultured in minimal media to eliminate the confounding effects of lactose. This approach allowed for clearer insights into the direct impact of temperature on promoter activity. We achieved this by expressing the lacI gene via the PR or tandem PR and PL promoters, under the control of the thermolabile mutant repressor cI857, allowing the transcription of the T7lac promoter and other lac-derived promoters containing lac operators to be controlled by temperature. Subsequently, this thermal switch was utilized to manipulate the genes involved in the vitamin B12 biosynthetic pathway, ultimately identifying optimal conditions for enhancing vitamin B12 production. This research offers novel insights for the industrial production of vitamin B12 and establishes a foundation for the future synthesis of other high-value compounds through thermal switches for pathway gene regulation.
Materials and Methods
Materials
Vitamin B12 (purity >99%) was obtained from Aladdin Scientific. For routine polymerase chain reaction (PCR) experiments, Q5 High-Fidelity DNA Polymerase from New England Biolabs (USA) was utilized. In colony PCR experiments, we employed 2× SuperTaq PCR StarMix (Dye) reagents provided by Genstar (China). Additionally, other molecular cloning reagents, such as restriction endonuclease, T4 DNA ligase, and T4 polynucleotide kinase, were procured from Thermo Fisher Scientific (USA). The ClonExpress Ultra One-Step Cloning Kit V2 was acquired from Vazyme (China). The tandem PR and PL promoters were synthesized by GENEWIZ (China) to serve as templates for gene cloning.
Bacterial Strains and Plasmids
The bacterial strains and plasmids utilized in this study are specified in Table S1, while the primers employed for amplification are detailed in Table S2. The endA gene in MG1655 (DE3) was successfully knocked out using CRISPR/Cas9 technology [22], resulting in the strain designated as FH224. The superfolder green fluorescent protein (sfGFP) gene was cloned into the XbaI site of pCas9-hsdR using the ClonExpress Ultra One Step Cloning Kit, producing the construct pCas9-hsdR-sfGFP. This plasmid was amplified with inverse primers; the resulting gene fragments were phosphorylated using T4 polynucleotide kinase and subsequently re-circularized, yielding the plasmids pCas9-hsdR-lac-sfGFP, pCas9-hsdR-tac-sfGFP, pCas9-hsdR-trc-sfGFP, and pCas9-hsdR-lacUV5-sfGFP. Following this, the sfGFP gene, driven by the T7lac promoter, was integrated into the genome of FH224 via CRISPR/Cas9 [22], generating the strain FH663. Further genetic modifications were made to the lacI gene using the CRISPR/Cas9 system [22].
The plasmid backbone of pRed_Cas9 was divided into two segments and amplified with the primer pairs Pcas9-1-F-Pr-lacI/Pcas9-1-R-Pr-lacI and Pcas9-2-F-Pr-lacI/Pcas9-2-R-Pr-lacI, followed by digestion with DpnI to eliminate the plasmid template. The upstream and downstream homology arms of the lacI gene were amplified from the E. coli MG1655 genome, using the primers Pr-lacI-up-F/Pr-lacI-up-R and Pr-lacI-dn-F/Pr-lacI-dn-R, respectively. The cI857 gene and PR promoter were amplified from the pCP20 plasmid and fused into a single fragment with the upstream and downstream homology arms using overlapping extension PCR with the primers PR-lacI-up-F and PR-lacI-dn-R. Subsequently, the plasmid backbones, upstream homology arm, cI857 gene, PR promoter, and downstream homology arm were assembled using the ClonExpress Ultra One Step Cloning Kit. Additional plasmids, including pCas9-RBS-lacI, pCas9-PRPL, pCas9-lacI-LVA tag, pCas9-lacI-LAA tag, and pCas9-lacI-ASV tag, were constructed in a similar fashion. These plasmids were transformed into the respective host strains for genome editing, resulting in the recombinant strains listed in Table S1.
Medium and Growth Conditions
Bacterial cultures from frozen storage tubes were streaked onto LB solid medium supplemented with the appropriate antibiotics and incubated at 37°C for 12 to 14 h. A single colony was subsequently selected and inoculated into 5 ml of LB liquid medium, which was then incubated at 37°C overnight with shaking at 200 rpm. The overnight cultures were transferred into 250 ml sterile conical flasks containing 30 ml of modified M9 minimal (MM9) medium, composed of 6.78 g/l Na2HPO4, 3.0 g/l KH2PO4, 0.5 g/l NaCl, 2.0 g/l NH4Cl, 1.0 g/l (NH4)2SO4, 1 mM MgSO4, 0.1 mM CaCl2, 20 g/l glycerol, with an initial optical density at 600 nm (OD600) of 0.1. The cultures were then incubated at 37°C with shaking at 200 rpm. Once the OD600 reached 0.8, the temperature was reduced to 32°C to induce sfGFP expression, and 1 mM IPTG was added to the control strain FH663. After induction, the cultures continued to be incubated at 37°C with shaking at 200 rpm for 48 h. Three biological replicates were conducted for each experimental group. After fermentation, an appropriate volume of the fermentation broth was collected, and cells were harvested by centrifugation and washed twice with PBS. The cells were then resuspended in PBS, adjusting the OD600 to approximately 0.2. The fluorescence intensity of the resuspended cell culture was measured using a Synergy Neo2 multifunctional microplate reader (BioTek, USA), with the fluorescence intensity of the green fluorescent protein (GFP) recorded using an excitation wavelength of 485 nm and an emission wavelength of 525 nm. The OD600 of the cells was assessed using a spectrophotometer (AOELAB UV-1000, China). The measured fluorescence intensity was normalized to the OD600 to calculate the specific fluorescence.
For flask cultivation of vitamin B12 production, overnight cultures of recombinant E. coli strains were inoculated into 250 ml Erlenmeyer flasks containing 30 ml of MR01 medium, with an initial OD600 of 0.05. The MR01 medium (pH 7.0) consists of 20 g/l glycerol, 6.67 g/l KH2PO4, 4 g/l (NH4)2HPO4, 0.8 g/l MgSO4·7H2O, 0.8 g/l citric acid, 20 mg/l CoCl2·6H2O, 90 mg/l 5,6-dimethylbenzimidazole (DMBI), 2 g/l glycine, 10 g/l succinic acid, 0.5 g/l betaine, and 0.5% trace metal solution (V/V). The trace metal solution included (per liter) the following components: 10 g FeSO4·7H2O, 2 g CaCl2, 2.2 g ZnSO4·7H2O, 0.5 g MnSO4·4H2O, 1 g CuSO4·5H2O, 0.1 g (NH4)6Mo7O24·4H2O, and 0.02 g Na2B4O7·10H2O, in a 0.5 M HCl solution. Gene expression was induced by shifting the temperature to 32°C.
Real-Time Online Monitoring of sfGFP in the BioLector Microbioreactor
Fresh single colonies were selected from the activation plate, inoculated in 5 ml of LB liquid medium, and incubated at 37°C with shaking at 200 rpm for 12-15 h to obtain overnight cultures. The overnight culture was transferred to a sterile 10 ml centrifuge tube and centrifuged at 4,000 rpm for 10 min. The supernatant was discarded, and the bacterial pellet was retained. The bacteria were resuspended in 5 ml of sterile water, and the centrifugation step was repeated three times to eliminate residual medium. Subsequently, 5 ml of fresh fermentation medium was added to resuspend cells, and a 10-fold dilution was performed to determine the initial OD600 value of the seed solution. The seed solution was inoculated into a sterile 10 ml centrifuge tube containing 5 ml of the corresponding fermentation medium, achieving an initial OD600 of 0.05. Following thorough mixing, 900 ml aliquots from each tube were transferred into a 48-well FlowerPlate. After sealing the plate, it was placed in a BioLector XT micro bioreactor and incubated at 37°C with agitation set at 1,400 rpm. When the bacterial biomass reached an OD600 of approximately 0.8, isopropyl b-D-1-thiogalactopyranoside (IPTG) was introduced into the culture system to a final concentration of 0.2 mM, inducing the expression of the target protein. Subsequently, when the bacterial OD600 reached approximately 1.0, the cultivation temperature was lowered to 32°C to promote the expression of sfGFP. The biomass values were measured using a gain setting of 1 on the BioLector XT micro bioreactor.
Fed-Batch Fermentation in a Bioreactor
Recombinant E. coli strains stored at -80°C were streak-inoculated onto LB solid plates and incubated at 37°C for 12 h to revive the cultures. Individual colonies were then selected and inoculated into 10 ml of LB liquid medium, followed by incubation at 37°C with shaking at 200 rpm for 12-14 h to obtain a seed culture. The seed culture was subsequently transferred into a 250 ml sterile conical flask containing 30 ml of LB liquid medium, utilizing an inoculation ratio of 1:10, and incubated at 37°C with shaking at 220 rpm for 16 h to establish a secondary seed culture. This secondary seed culture was then used to prepare a tertiary seed culture by inoculating into two 2 L sterile conical flasks, each containing 200 ml of MR fermentation medium as previously described [23], again with an inoculation ratio of 1:10. The culture was incubated at a constant temperature of 37°C with shaking at 220 rpm for 12-15 h. Finally, the tertiary seed culture was inoculated into a 5-L fermenter (Baoxing, China) containing 2 L of MR01 medium at the same inoculation ratio of 1:10. The pH of the fermentation broth was maintained at 7.0 through the addition of 30% phosphoric acid and ammonia, while the dissolved oxygen level was consistently kept between 30% and 40% by adjusting the agitation rate and aeration (3 l/min). During the initial phase of fermentation (0-12 h), the temperature was maintained at 37°C. Upon reaching a cell density of OD600 =10, heterologous vitamin B12 pathway genes were induced by lowering the temperature to 32°C. A sterile glycerol solution (40%, w/v) was automatically added when glycerol levels were depleted, ensuring residual glycerol levels remained below 5 g/l. Samples were collected periodically at specified intervals to assess cell growth, residual glycerol concentration, and the production of the target product, vitamin B12.
Analytical Methods
The quantification of vitamin B12 in the fermentation broth was conducted using high-performance liquid chromatography (HPLC). The procedure involved the following steps: 20 ml of fermentation broth was diluted with double-distilled water (ddH2O) to achieve a final volume of 2 ml, resulting in a 10-fold dilution. Subsequently, 200 ml of an 8% sodium nitrite solution and 200 ml of glacial acetic acid were added to the diluted solution. After thorough mixing, the solution was autoclaved at 100°C for 30 min. to release the bound form of vitamin B12. Following the reaction, the sample was allowed to cool naturally to room temperature and then centrifuged at 5,000 rpm for 5 min. to separate the supernatant. The supernatant was filtered through a 0.22 mm membrane to eliminate impurities. Finally, the filtered solution was analyzed using an Agilent 1260 series HPLC system equipped with a C18 column (Agilent, 5 µm × 250 × 4.6 mm) and a UV detector set at 320 nm. The mobile phase A was composed of ddH2O, while mobile phase B consisted of pure methanol. The elution gradient was set to a ratio of A to B at 3:7, and the analysis was conducted at a temperature of 35°C with a flow rate of 0.8 ml/min. The quantification of vitamin B12 was based on a standard curve.
Statistical Analysis
Significant variations among the experimental factors were assessed using one-way ANOVA, followed by Tukey's multiple comparisons test, with a significance level set at p < 0.05. All analyses were conducted using GraphPad Prism software (Version 10.1.0).
Results and Discussion
Design of T7lac and lac-Derived Promoters Based on a Thermal Switch
The T7lac promoter, a robust construct derived from the T7 phage and lactose operon promoters [17], is extensively utilized in recombinant protein expression systems. In the absence of IPTG, the LacI protein binds to the lacO site of the T7lac promoter, effectively blocking the transcription of the downstream gene. Conversely, in the presence of IPTG, LacI is released upon binding IPTG, allowing for the transcription of the downstream gene. This regulatory mechanism is also applicable to other promoters, such as the tac and lacUV5 promoters, which contain lacO and are similarly regulated by LacI.
Cell lysis was observed during the fermentation of recombinant vitamin B12-producing strains, which was attributed to the toxicity of IPTG (Fig. S1) [5]. To eliminate the reliance on IPTG, we aimed to design a thermal switch to regulate genes driven by the T7lac promoter. Previous studies have presented a thermo-regulated T7 expression system; however, the operational temperature range of 39°C to 37°C is considered too high for the effective expression of heterologous genes. Consequently, we positioned the lacI gene under the control of the PR, or tandem PR and PL promoters, which are regulated by the temperature-sensitive repressor cI857 (Fig. 1). At elevated temperatures (37°C), which corresponds to the optimal growth conditions for E. coli, the cI857 repressor is inactive, leading to the transcription of the lacI gene as shown in Fig. 1A. Consequently, the transcription of downstream T7lac genes, including gene 1, which encodes T7 RNA polymerase, is effectively inhibited. For instance, under these conditions, the target gene sfGFP, which is regulated by the T7lac promoter, remains untranscribed, as do the genes related to the vitamin B12 pathway that are governed by the T7lac, tac, and lacUV5 promoters. Upon shifting to a lower temperature of 32°C, which is conducive to the expression of heterologous proteins, the cI857 repressor becomes active, and transcription of the lacI gene ceases (Fig. 1B). This change facilitates the transcription of sfGFP and the vitamin B12 pathway genes. By modulating lacI gene expression via the PR, or PRPL promoters, we enable temperature-based regulation of all promoters that fall under the control of LacI.
Fig. 1. An overview of the thermal switch mechanism used to control gene expression.
(A) At elevated temperatures (37°C), the PR, or tandem PR, PL promoter becomes dissociated from the inactive temperature-sensitive repressor CI857, allowing LacI to bind to the lacO site of the lacUV5 and T7lac promoters. As a result, the gene of interest is not expressed. (B) Conversely, at lower temperatures (32°C), transcription of the PR, or tandem PR, PL promoter is inhibited by the temperaturesensitive repressor CI857. Consequently, the lacUV5 and T7lac promoters are liberated from LacI, which enables the expression of the gene of interest (GOI).
Characterization of the Thermoregulated Promoters
We employed the SfGFP as a reporter to assess the thermoregulated expression system. Two chassis cells, FH478 and CFT81, were engineered by substituting the promoter of the lacI gene in the chromosome with the PR and PRPL promoters, respectively. Subsequently, the sfGFP gene, regulated by the T7lac promoter, was integrated into the hsdR locus of both FH478 and CFT81, resulting in the creation of FH659 and CFT64, respectively (Fig. 2A).
Fig. 2. Characterization of the thermal switch using the sfGFP reporter.
(A) Characteristics of FH663 controlled by IPTG, along with strains regulated by the thermal switch. The lacI gene is regulated by the PR promoter (FH659) or the tandem PR, PL promoter (CFT64), respectively. (B) Fluorescence curves for FH663, FH659, and CFT64 at varying temperatures. The sfGFP in strain FH663 was induced by 1 mM IPTG when the temperature increased to 32°C. Conversely, the sfGFP in strains FH659 and CFT64 was induced at lower temperatures before shifting to 32°C. (C) Growth curves for FH663, FH659, and CFT64 under the same conditions as described in (B). Biomass values were recorded with a gain setting of 1 on the BioLector XT micro bioreactor. (D) Fluorescence curves for strains with the sfGFP gene regulated by lac, tac, trc, and lacUV5 promoters under the control of the thermal switch. (E) A comparison of the fluorescence curves of FH663, CFT64, and CFT96 (with down-regulation of lacI under the control of the PRPL promoter). The FH663 strain was induced with varying concentrations of IPTG when the temperature shifted to 32°C, while the CFT64 and CFT96 strains were induced by the lower temperature (32°C). Error bars indicate standard deviations from triplicate (Fig. 2B-2D) or quadruplicate (Fig. 2E) biological replicates.
Microbioreactor cultivations of the strains FH659, CFT64, and the control strain FH663 were utilized to monitor green fluorescent protein (GFP) fluorescence and biomass. Following a temperature downshift to 32°C, the fluorescence levels of FH659 and CFT64 gradually increased, peaking at 33 h and 29 h, respectively (Fig. 2B), thereby indicating effective operation of the thermo-regulated expression system. The relative fluorescence of FH659 and CFT64 was lower than that of the control strain FH663, which was induced with 1 mM IPTG, with the maximum relative fluorescence of CFT64 reaching 19.69% of the control. However, the biomasses of the strains utilizing the thermo-regulated expression system were significantly greater than that of the control at the 16-h mark (Fig. 2C), suggesting that the thermo-regulated expression system mitigates the negative effects associated with IPTG induction. Furthermore, the efficacy of the thermo-regulated expression system was maintained when the sfGFP gene was regulated by the lac, tac, trc, and lacUV5 promoters containing lac operator (lacO) (Fig. 2D). The versatility of such a system could enable researchers to manipulate gene expression across various pathways and applications, including metabolic engineering, protein production, and synthetic circuit design. Given that the dynamic range of the thermo-regulated expression system is narrower than that of the IPTG-regulated expression system, we aimed to enhance the dynamic range. We hypothesized that the ratio of LacI to cI857 significantly impacts the expression of thermo-regulated target genes. To test this hypothesis, we modified the RBS of CFT64 to create a strain designated CFT96 with a weaker RBS. Notably, the relative fluorescence of CFT96, when lacI expression was downregulated, reached levels comparable to the control induced by 0.01 mM IPTG (Fig. 2E). However, the decrease in lacI expression led to undesired leaky expression of sfGFP, as evidenced by the increasing trend of relative fluorescence at 37°C.
Biosynthesis of Vitamin B12 Using Pathway Genes Controlled by the Thermal Switch
While the dynamic range of the thermo-regulated expression system is narrower than that of the IPTG-regulated expression system, it remains promising due to its ability to mitigate the negative effects associated with IPTG, reduce costs, and enhance biomass production. To optimize the production of the target compound, the transcriptional levels of genes must be maintained within appropriate ranges rather than at maximal levels [5, 24]. In this study, we employed the thermo-regulated expression system using two plasmid-free recombinant E. coli strains, specifically JH03 [3] and JPTB38. However, we were only able to successfully obtain the strains B58 and B54, which feature lacI driven by the PR promoter. Attempts to develop strains with lacI driven by the PRPL promoter were unsuccessful, likely due to the significant burden of heterologous protein expression imposed by that configuration. In both strains B58 and B54, five modules comprising 28 heterologous genes involved in the vitamin B12 biosynthetic pathway were driven by T7lac, tac, and trc promoters, thereby placing these genes under the control of the thermal switch (Fig. S2).
The thermal switch was subsequently assessed in these two strains. They were initially cultured at 37°C, and upon reaching an OD600 of 0.8-1.0-which corresponds to the IPTG-inducing time point—the temperature was lowered to 32°C to facilitate vitamin B12 production. The strains B58 and B54 yielded production levels of 0.166 mg/l and 0.495 mg/l of vitamin B12, respectively (Fig. 3A). Following this, we sought to enhance the vitamin B12 titer in the B54 strain. Given that reducing lacI expression at the translational level resulted in leaky expression, we decided to decrease lacI expression at the post-translational level instead. Bacteria can recognize and degrade proteins tagged with the ssrA degradation tag—an 11-residue peptide-using proteases such as ClpXP and ClpAP [25]. We introduced three ssrA degradation tags with varying strengths (LVA, LAA, and ASV) co-translationally to the C-terminus of the lacI gene in the B54 strain, resulting in strains B55, B56, and B57. The vitamin B12 titers in all three strains carrying lacI-ssrA tags were increased (Fig. 3A). Notably, the B57 strain, which carried the ASV tag (the weakest of the three), exhibited the highest increase in vitamin B12 titer, rising by 37.96%.
Fig. 3. Optimization of the thermal switch for vitamin B12 production.
(A) The vitamin B12 titers of recombinant E. coli strains B58 and B54, which were derived from different host organisms. Strains B55, B56, and B57 were engineered by incorporating ssrA degradation tags, specifically LVA, LAA, and ASV tags, at the C terminus of the lacI gene of the B54 strain. The B57 strain was initially cultivated at temperatures of 42°C (B) 39°C (C) and 37°C (D). Temperature shifts to 32°C were executed once the OD600 reached the corresponding values indicated on each x-coordinate. Error bars indicate standard deviations from triplicate biological replicates.
The implementation of the thermal switch segregated the fermentation process into two distinct phases: a high-temperature phase and a low-temperature phase. Three critical parameters-growing temperature, producing temperature, and switching time point-significantly influenced vitamin B12 production. Given that 32°C is recognized as the optimal temperature for vitamin B12 production [19], we focused on optimizing the growing temperature and switching timepoint to enhance production outcomes. The B57 strain was initially cultivated at various temperatures (42°C, 39°C, and 37°C) and subsequently transitioned to 32°C at different time points, as indicated by OD600 readings. At an initial temperature of 42°C, vitamin B12 titers did not exhibit significant variation when switching timepoint (OD600) increased from 0.8 to 1.5 (p > 0.05) (Fig. 3B). Conversely, the vitamin B12 titers at an initial temperature of 39°C remained relatively stable across different timepoints (Fig. 3C). Overall, the optimal initial temperature for vitamin B12 production was determined to be 37°C based on the highest vitamin B12 titers observed in each group (p < 0.05), which corresponds with the optimal growth temperature of 37°C. In conclusion, the optimal initial temperature for vitamin B12 production (approximately 0.7 mg/l) was determined to be 37°C, as it resulted in the highest vitamin B12 titers across all groups (p < 0.05) despite the highest biomass being recorded at 39°C (p < 0.05). The optimal switch time points across OD600 values ranging from 0.8 to 4 did not reveal any statistically significant differences (p > 0.05) (Fig. 3D). The highest vitamin B12 titer was achieved at a switch time point of OD600 = 2, although this result was not statistically significant. Notably, the lowest biomass was statistically observed at the highest OD600 across all groups during temperature shifts (p < 0.01), with the exception of the group with a switch point of OD600 = 2 at an initial temperature of 39°C (p = 0.0512), likely attributable to the burden of heterologous proteins expressed at lower temperatures.
Fed-Batch Fermentation for Vitamin B12 in a 5-L Bioreactor
To assess the impact of the thermal switch on scaled-up vitamin B12 production, fed-batch fermentation of strain B57 was performed in a 5-L bioreactor. Consistent with the shake-flask fermentation, the strain was initially cultivated at 37°C and subsequently transitioned to 32°C upon reaching the mid-logarithmic phase after 12 h. Strain B57 experienced a lag phase of up to 12 h at the onset of fermentation, followed by the logarithmic phase, during which it achieved a maximum biomass of 55.8 approximately 32 h into the process (see Fig. 4). vitamin B12 production paralleled biomass accumulation, gradually increasing from 24 h to 36 h, ultimately reaching a maximum titer of 1.79 mg/l at 36 h. Following this peak, production declined in tandem with the deterioration of the strain.
Fig. 4. Fed-batch production of vitamin B12 utilizing B57 in a 5-L bioreactor.
The time courses of vitamin B12 titer, OD600, and residual glycerol concentrations are illustrated.
In conclusion, this study successfully demonstrates the design and implementation of a thermal switch based on the phage l Promoter and lacI, enabling regulation of gene expression in metabolic pathway engineering without the need for IPTG. The most effective approach for producing vitamin B12 involves initially culturing at 37°C and then transferring to 32°C once the optical density at 600 nm reaches 2. Furthermore, the introduction of an ASV degradation tag at the C-terminus of lacI has been shown to enhance the vitamin B12 titer.
Supplemental Materials
Supplementary data for this paper are available on-line only at http://jmb.or.kr.
Acknowledgments
This work was supported by the National Key R&D Program of China (2022YFC2106100), the National Science Fund for Distinguished Young Scholars (22325807), the National Natural Science Foundation of China (22178372, 22208367, 32300069), and the Tianjin Synthetic Biotechnology Innovation Capacity Improvement Project (TSBICIP-KJGG-011 and TSBICIP-CXRC-055).
Footnotes
Conflict of Interest
The authors have no financial conflicts of interest to declare.
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