http://orcid.org/0000-0002-8498-8460
Figures
Abstract
1,3-Propanediol (1,3-PDO) is an important compound that is mainly used in industry for polymer production. Fermentation of 1,3-PDO from glycerol by Klebsiella pneumoniae is accompanied by formation of 2,3-butanediol (2,3-BDO) as one of the main byproduct. The first step in the formation of 2,3-BDO from pyruvate is catalyzed by acetolactate synthase (ALS), an enzyme that competes with 1,3-PDO oxidoreductase for the cofactor NADH. This study aimed to analyze the impact of engineering the 2,3-BDO formation pathway via inactivation of ALS on 1,3-PDO fermentation by K. pneumoniae HSL4. An ALS mutant was generated using Red recombinase assisted gene replacement. The ALS specific activities of K. pneumoniae ΔALS were notably lower than that of the wild-type strain. Fed-batch fermentation of the mutant strain resulted in a 1,3-PDO concentration, productivity and conversion of 72.04 g L–1, 2.25 g L–1 h–1, and 0.41 g g–1, increase by 4.71%, 4.65% and 1.99% compared with the parent strain. Moreover, inactivation of ALS decreased meso-2,3-BDO formation to trace amounts, significantly increased 2S,3S-BDO and lactate production, and a pronounced redistribution of intracellular metabolic flux was apparent.
Citation: Zhou S, Huang Y, Mao X, Li L, Guo C, Gao Y, et al. (2019) Impact of acetolactate synthase inactivation on 1,3-propanediol fermentation by Klebsiella pneumoniae. PLoS ONE 14(4): e0200978. https://doi.org/10.1371/journal.pone.0200978
Editor: Daniel Olson, Dartmouth College, UNITED STATES
Received: July 4, 2018; Accepted: March 20, 2019; Published: April 24, 2019
Copyright: © 2019 Zhou et al. This is an open access article distributed under the terms of the Creative Commons Attribution License, which permits unrestricted use, distribution, and reproduction in any medium, provided the original author and source are credited.
Data Availability: All relevant data are within the paper.
Funding: This work was supported by grants from China Agriculture Research System (CARS-47-G16), Guangdong Provincial Natural Science Foundation (2017A030313180 and 2015A030313854), National Natural Science Foundation of China (31502207) and Administration of Ocean and Fisheries of Guangdong Province (GD2012-D01-002). The funders had no role in study design, data collection and analysis, decision to publish, or preparation of the manuscript.
Competing interests: The authors have declared that no competing interests exist.
1 Introduction
1,3-Propanediol (1,3-PDO) is an important industrial chemical intermediate that is used in the synthesis polymers [1, 2]. 1,3-PDO can be produced by both chemical synthesis and microbial fermentation. While chemical methods are troubled by poor selectivity and high energy consumption, microbial fermentation has a number of advantages including mild reaction conditions that are more environmentally favourable, greater sustainability, and easier operation [3, 4]. Numerous microorganisms produce 1,3-PDO including Klebsiella pneumoniae, Citrobacter freundii, Clostridium butyricum, and Clostridium acetobutylicum [5–7]. Of these, K. pneumoniae has been most widely explored since it achieves a higher concentration of 1,3-PDO, greater productivity, and a higher rate of conversion using glycerol as the carbon source [8, 9].
In K. pneumoniae metabolism, glycerol is dissimilated through coupled reductive and oxidative pathways (Fig 1). 1,3-PDO is synthesized in the reductive pathway, whereas in the oxidative pathway, pyruvate-derived by-products such as 2,3-butanediol (2,3-BDO), acetate (AC), lactate (LAC), succinate (SUC) and ethanol (ETH) are generated through the channeling of glycerol into glycolysis [10]. Generation of by-products can compete with the biosynthesis of 1,3-PDO for carbon flow and NADH, which can lower the yield of 1,3-PDO. Blocking both the ETH and LAC pathways can reduce the production of ethanol and lactate and can increase the production of 1,3-PDO [11–13].
The glycerol substrate and major product metabolites are boxed. UE: Unknown enzyme; ALS: acetolactate synthase (mutated in this study); ALD: α-acetolactate decarboxylase; DAR: diacetyl reductase; E1: meso-2,3-BDO dehydrogenase (R-acetoin forming); E2: meso-2,3-BDO dehydrogenase (S-acetoin forming); E3: (S,S)-2,3-BDO dehydrogenase; dhaD: Glycerol dehydrogenase; DHA: Dihydroxyacetone, DHAP: Dihydroxyacetone phosphate; G-3-P: glycerol-3-Phosphate; PEP: phosphoenolpyruvate; GDHt: glycerol dehydratase; PDOR: 1,3-propanediol oxidoreductase; 3-HPA: 3-hydroxypropionaldehyde; TCA: tricarboxylic acid cycle.
2,3-BDO is one of the the main byproducts generated alongside 1,3-PDO in the oxidative catabolism of glycerol, and both compounds share a similar high boiling point and water solubility. Therefore, 2,3-BDO not only competes for carbon flow, but also complicates 1,3-PDO recovery and purification [14]. Minimizing 2,3-BDO production would therefore improve the yield of 1,3-PDO and simplify the downstream processing [15, 16].
2,3-BDO is a metabolite derived from pyruvate (Fig 1). In the Enterobacteriaceae family, pyruvate from glycolysis can be converted into either LAC in an NADH-dependent reaction catalyzed by L-/D-LAC dehydrogenase (LDH) or, after decarboxylation, into acetolactate in a reaction catalyzed by acetolactate synthase (ALS), encoded by the budB gene. Acetolactate is mostly produced when NADH availability is low, and under aerobic conditions, it can be converted to acetoin by acetolactate decarboxylase (ALD), encoded by the budA gene. Under aerobic conditions, acetolactate can undergo spontaneous decarboxylation to produce diacetyl, and diacetyl reductase (DAR; also known as acetoin dehydrogenase) converts diacetyl to acetoin. Finally, butanediol dehydrogenase (BDH), encoded by the budC gene, also known as acetoin reductase, reduces acetoin to 2,3-BDO [17].
In this study, a 2,3-BDO pathway-deficient mutant of K. pneumoniae was constructed by knocking out the budB gene to generate a variant strain lacking ALS. The physiological and fermentation properties of the mutant strain, including the distribution and yield of various metabolites and products, were subsequently investigated. In particular, the influence that blocking the 2,3-BDO pathway has on glycerol metabolism and 1,3-PDO production was studied.
2 Materials and methods
2.1 Strains, plasmids and culture media
Strains and plasmids used in this study are listed in Table 1. Klebsiella pneumoniae HSL4, used for the biosynthesis of 1,3-PDO in this work, was previously isolated from mangrove sediment samples [9]. Basic culture media contained the following components (L–1): 16 g pure glycerol (mass percent > 99%), 1.5 g yeast extract, 4 g (NH4)2SO4, 0.69 g K2HPO4, 0.25 g KH2PO4, 0.2 g MgSO4·7H2O, 1 ml trace element solution, and 1 ml Fe2+ solution. The trace element solution contained (L–1): 100 mg MgSO4·4H2O, 70 mg ZnCl2, 35 mg Na2MoO4·2H2O, 60 mg H3BO3, 200 mg CoCl2·6H2O, 29.28 mg CuSO4·5H2O, 25 mg NiCl2·6H2O, and 0.9 ml HCl (37%).
When necessary, the medium was supplemented with antibiotics at the following final concentrations: 50 μg mL–1 kanamycin (Kan), 100 μg mL–1 ampicillin (Amp), 50 μg mL–1 apramycin (Apra) or 25 μg mL–1 chloramphenicol (Cm).
2.2 Construction of mutant strain K. pneumoniae ΔALS
The ALS mutant strain K. pneumoniae ΔALS was constructed following a method described by Wei et al. [18]. Briefly, the ALS gene of K. pneumoniae HSL4 was amplified by PCR using primer pair ALS-F1/ALS-R1. The PCR product was ligated into the pMD18-T simple vector to generate pMD18-T-ALS. A linear portion of DNA with both 40 nt homologous extensions flanking the apramycin resistance gene aac(3)IV was amplified using plasmid pIJ773 as the template with primer pair ALS-F2/ALS-R2. The pMD18-T-ΔALS construct was engineered by replacing part of the ALS gene in plasmid pMD18-T-ALS with the aac(3)IV cassette using the Red/ET system in Escherichia coli [20]. The pMD18-T-ΔALS vector was used as a template for the PCR-based preparation of a linear DNA containing the apramycin resistance gene aac(3)IV with 468 bp upstream and 714 bp downstream homologous regions (long homologous flanking). Finally, the long homologous flanking linear DNA product was transformed into K. pneumoniae-pDK6-red, which already hosted the pDK6-red plasmid. Homologous recombination between the introduced linear DNA and chromosomal DNA was facilitated by Red recombinase and led to the deletion of ALS (Fig 2). The ALS-deficient strains were selected on apramycin plates, and primer pairs Apra-F/Apra-R and ALS-F3/ALS-R3 were used for PCR confirmation. Primers used in this study are listed in Table 2.
BudA (ALD) and budC (BDH) are upstream and downstream of ALS on the K. pneumoniae HSL4 chromosome, respectively. ALS-F1/R1, ALS-F2/R2, ALS-F3/R3, and Apra F/R were the primer pairs used.
2.3 Batch and fed-batch fermentation
For batch fermentation and preparation of seed cultures for fed-batch fermentation, 250 mL flasks containing 100 mL of basic culture medium (glycerol adjusted to 30 g L–1) were inoculated with a single colony and incubated at 37°C in a rotatory shaker at 200 rpm for 12 h. For fed-batch fermentation, a 3% (v/v) inoculum was added aseptically to a 5 L fermenter (Zheng Jiang Dong Fang, China) containing 3 L of media. NaOH (8 M) was used to maintain the pH. Aerobic fermentation according to Hao et al. [22] was carried out at 37°C, pH 6.8, 200 rpm with an air flow of 0.5 vvm (volume per volume per minute). The glycerol concentration was 16–18 g L–1 in the culture medium at the beginning of fermentation, and the consumption of glycerol was slow during fermentation for 0–5 h, when the glycerol concentration dropped below 5 g L–1, additional pure glycerol was added to the culture medium to maintain the concentration of glycerol was between 2 to 20 g L–1 in subsequent fed-batch cultures at 5–32 h. Total amount of glycerol consumption was calculated after the fermentation was completed.
2.4 The ALS activity assays
The ALS assay was based on enzymatic conversion of pyruvate to acetolactate and acetolactate converts to acetoin by acid hydrolysis. The assay was conducted as described by Yang et al. [23]. Cell samples were collected every 1–4 h during the fermentation and centrifuged at 5000 × g, 4°C for 10 min and pellets were stored at 4°C until needed for analysis. Pellets were washed with cold 50 mM acetate buffer pH 6, centrifuged at 5000 × g, 4°C for 10 min, resuspended in the same buffer at 4°C, and crude cell extracts (for use in enzyme assays) were obtained by sonication with an ultrasonic cell disrupter. Reaction mixtures contained 20 mM sodium pyruvate, 50 mM acetate buffer pH 6, 1 mM MgCl2, and 80 mL of cocarboxylase. Reactions were initiated by the addition of 100 μL of crude extract to 1 mL of reaction buffer and followed for 20 min at 37°C. Reactions were terminated by addition of 0.1 mL of 50% H2SO4. Mixtures were incubated for an additional 25 min at 37°C to allow acid hydrolysis of acetolactate to acetoin, and acetoin was measured using the Voges–Proskauer test. Briefly, a 0.2 mL aliquot of the aforementioned mixture was transferred to a tube with 0.8 mL of 0.45 M NaOH, and 1 mL of α-naphthol (5% in 2.5 M NaOH) and 0.5% creatine (1:1) was added. Reactions were incubated at room temperature for 30 min with slightly shaking, and the absorbance at 535 nm was measured. Calibration with pure acetoin showed a correlation of 1 OD535 unit to 0.15 mM acetoin. One specific unit of ALS activity corresponds to the formation of 1 mmol of acetoin per mg of protein per minute. All the data were expressed as means from three biological replicate experiments.
2.5 Biomass and fermentation broth analysis
Cell density was monitored using a spectrophotometer at 600 nm (OD600nm). Cell density was expressed as OD600nm or by converting OD600nm to biomass (g L–1) according to the curve set up previously in our labortory. Glycerol, 1,3-PDO, 2,3-BDO, LAC, SUC, AC, ETH, 2S,3S-BDO and meso-2,3-BDO were determined using a Shimadzu 20AT HPLC system with an RID-10A refractive index detector and equipped with a 300 × 7.8mm2 Aminex HPX-87H column (Bio-Rad, USA) running at 0.8 ml min–1 after adding 5 mM H2SO4. The column temperature was controlled at 65°C. All the data were expressed as means from three biological replicate experiments.
3 Results
3.1 Inactivation of the ALS gene in K. pneumoniae HSL4
A Red recombination approach was used to knock-out the ALS gene in K. pneumoniae HSL4 (Fig 2). A positive recombinant was selected from the apramycin plate, confirmed by PCR and named K. pneumoniae ΔALS.
3.2 Effect of ALS inactivation on cell growth, glycerol consumption and ALS enzymatic activity
The effect of ALS inactivation on cell growth was examined during fermentation (Fig 3A). The maximum OD600nm (biomass) reached was 6.80, and the growth of K. pneumoniae ΔALS was unaffected compared with the wild-type strain. Consumption of glycerol by K. pneumoniae ΔALS and K. pneumoniae HSL4 were also monitored in a fed-batch culture, and the glycerol consumption rate (5.50 g L–1 h–1) of K. pneumoniae ΔALS was slightly higher than that of K. pneumoniae HSL4 (5.34 g L–1 h–1), as shown in Fig 3B. Further investigation revealed a notably lower ALS specific activity in the crude cell extract of K. pneumoniae ΔALS than the wild-type strain (Fig 3C). These results indicated that the consumption of glycerol was slightly promoted by inactivation of ALS.
Time course of cell growth (OD600nm) (A), glycerol consumption rate (B), and ALS specific activity(C) of K. pneumoniae ΔALS and K. pneumoniae HSL4 in fed-batch culture. Enzyme activities are expressed in mM mg–1 min–1 (U mg–1). Data were expressed as means from three biological replicate experiments.
3.3 Fed-batch fermentation of glycerol to 1,3-PDO by K. pneumoniae ΔALS
Fed-batch cultures were carried out in a 5 L fermenter to further investigate the fermentation of glycerol to 1,3-PDO by K. pneumoniae ΔALS, and the results after 32 h are shown in Table 3 and Fig 4. After 5–16 h, the substrate was consumed fast and 1,3-PDO was rapidly synthesized by both K. pneumoniae ΔALS and the wild-type strain. However between 16–26 h, substrate uptake and the 1,3-PDO synthesis were slower, and both LAC and meso-2,3-BDO were rapidly accumulated by K. pneumoniae HSL4, while only LAC was rapidly accumulated by K. pneumoniae ΔALS. After 32 h, 1,3-PDO was the main product and reached a concentration of 72.04 g L–1 in the broth by K. pneumoniae ΔALS and 68.76 g L–1 in the broth of the wild-type strain. Fermentation by K. pneumoniae ΔALS produced five other main metabolites including 31.50 g L–1 LAC, 8.30 g L–1 SUC, 9.60 g L–1 AC, 7.60 g L–1 ETH, and 2.16 g L–1 2S,3S-BDO. In comparison, K. pneumoniae HSL4 produced 15.42 g L–1 LAC, 7.76 g L–1 SUC, 7.02 g L–1 AC, 9.23 g L–1 ETH, and 13.75 g L–1 meso-2,3-BDO.
1,3-PDO, 1,3-propanediol; LAC, Lactate; SUC, Succinate; ACE, Acetate; 2,3-BDO, 2,3-Butanediol; ETH, Ethanol. Data were expressed as means from three biological replicate experiments.
As shown in Table 3, glycerol consumption by K. pneumoniae ΔALS was slightly higher than that of the parent strain. 1,3-PDO reached a final concentration of 72.04 g L–1 in K. pneumoniae ΔALS, which was an slightly increase of 4.71% compared to the parent strain. 1,3-PDO productivity was 2.25 g L–1h–1 with K. pneumoniae ΔALS, higher than K. pneumoniae HSL4 (2.15 g L–1h–1). Similarly, there was an slightly increase in 1,3-PDO conversion of K. pneumoniae ΔALS comparing to the parent strain. Therefore, as expected, ALS inactivation decreased meso-2,3-BDO generation, although K. pneumoniae ΔALS produced increased LAC (31.50 g L–1) than the parent strain (15.42 g L–1). This suggests that ALS deletion shifted the carbon flux away from the biosynthesis of meso-2,3-BDO towards the production of LAC and made 1,3-PDO production, productivity and conversion (yield) slightly increased but none of these parameters were changed significantly.
3.4 Metabolic profiling of fed-batch fermentation by K. pneumoniae ΔALS
Based on the results of cell growth, substrate consumption and metabolite formation profiles (Figs 3–4), fed-batch fermentations were divided into four periods; (I) Initial phase (0–5 h), (II) exponential growth phase (5–16 h), (III) stationary phase (16–26 h) and (IV) decline phase (26–32 h). Metabolic flux during different phases of the K. pneumoniae ΔALS and HSL4 fed-batch fermentations showed that during period I, the cell biomass was low but increase rapidly (Fig 3A and Table 4). In this period, cells soon adapted to the new culture conditions, and the rate of substrate consumption and 1,3-PDO formation was high. Unfortunately, only a small amount of 1,3-PDO was synthesized due to the low biomass. During period II, cells grew exponentially, and both biomass and 1,3-PDO concentration increased sharply. Other metabolites were also synthesized steadily, but 1,3-PDO was the main product during this period. Acetate increased rapidly during the exponential growth period (5–16 h) and carbon flux was diverted to LAC synthesis in the stationary growth period (16–26 h), whereas 1,3-PDO synthesis slowed down during this phase. During periods III and IV, large amounts of LAC accumulated in K. pneumoniae ΔALS. Period IV is known as the decline phase, during which cell growth ceases, cells begin to die, and substrate uptake and metabolite formation decrease, although LAC synthesis continued in both K. pneumoniae ΔALS and K. pneumoniae HSL4. Other metabolites exhibited a similar flux distribution, although ethanol and acetate synthesis was negative due to volatilization and reutilization, respectively.
The distribution of metabolites in fed-batch fermentations by K. pneumoniae ΔALS and K. pneumoniae HSL4 (Table 4) clearly showed that the flow of glycerol to 1,3-PDO and byproducts other than meso-2,3-BDO and ETH was increased in the mutant K. pneumoniae ΔALS compared with the parent strain. It is worth noting that LAC increased strikingly in K. pneumoniae ΔALS, and it was reported that meso-2,3-BDO increased notably in a LAC-deficient mutant [12, 13]. In glycerol metabolism, LAC and meso-2,3-BDO reside on separate branches downstream from pyruvate and both depend on the action of dehydrogenase enzymes that use NADH as a cofactor. In general, one pathway is likely to be strengthened when the other is blocked, therefore it is logical that blocking meso-2,3-BDO biosynthesis resulted in the promotion of LAC biosynthesis in this study.
3.5 2,3-BDO stereoisomers in K. pneumoniae ΔALS and K. pneumoniae HSL4
Klebsiella pneumoniae synthesizes both meso-2,3-BDO and 2S,3S-BDO through fermentation of glycerol [17]. In this study, both mutant and the wild-type strains were cultured with glycerol (30 g L–1) as the carbon source, and 1,3-PDO was the main product with both strains (Fig 5). However, the strains produced different amounts of 2,3-BDO of isomers; wild-type K. pneumoniae HSL4 produced 3.8 g L–1 meso-2,3-BDO and 0.20 g L–1 2S,3S-BDO after fermentation for 12 h, whereas K. pneumoniae ΔALS produced 0.16 g L–1 and 0.85 g L–1, respectively. A distinguishing characteristic of the mutant strain was the low level of meso-2,3-BDO and high level of 2S,3S-BDO produced, suggesting synthesis of meso-2,3-BDO was inhibited while the formation of 2S,3S-BDO was stimulated in the absence of ALS.
HPLC analysis of K. pneumoniae ΔALS (A) and K. pneumoniae HSL4 (B) fermentation broth following growth on glycerol. The arrows pointing to the peaks in (A) and (B) indicate 2S,3S-BDO and meso-2,3-BDO, respectively. Standards of 2S,3S-BDO and meso-2,3-BDO were showed by arrows pointing to the peaks in (C) and (D), respectively. Peaks corresponding to other metabolites and substrates are not indicated.
4 Discussion
During growth on glycerol in K. pneumoniae, considerable amounts of metabolites are produced via the activities of oxidative branch enzymes [10]. Lactate, 2,3-BDO, ETH, SUC and AC are among the major by-product metabolites generated, and these can account for 40%–45% of the total metabolites. In this study, LAC (15.42 g L–1) and 2,3-BDO (13.75 g L–1) were the two most abundant by-products and reached 22.4% and 20.0% (w/w) that of 1,3-PDO (68.76 g L–1), which were the major products in the fermentation broth of the wild-type strain. Minimizing the production of by-products is an effective way to engineer the microbial strain to synthesize more 1,3-PDO. Both ETH [11] and LAC pathways of K. pneumoniae [13] and Klebsiella oxytoca [12] have been successfully disrupted by knocking out genes encoding key enzymes in these pathways. Inactivation of the ETH pathway by knocking-out ALDH in K. pneumoniae YMU2 almost abolished ETH formation and significantly increased 1,3-PDO production [11]. Similarly, Yang et al. [12] reported that LAC-deficient mutants of K. oxytoca were obtained by knocking out the gene encoding LDH. Their results showed that 1,3-PDO concentration, productivity, and conversion rate can enhanced above levels achieved by wild-type strains, and LAC production can be diminished. However in their study, the distribution of metabolites was altered and over 60 g L–1 2,3-BDO was produced as the major byproduct. Previously, the D-LAC pathway of K. pneumoniae HR526 was disrupted by knocking out D-LAC dehydrogenase [13], which increased conversion of 1,3-PDO and 2,3-BDO from 0.55 mol mol–1 to 0.65 mol mol–1, and the final LAC concentration decreased dramatically from more than 40 g L–1 to less than 3 g L–1.
To improve both the yield and productivity of 1,3-PDO from glycerol, disruption of the 2,3-BDO pathway is an alternative strategy. In K. pneumoniae, the genes coding acetolactate decarboxylase (ALD, encoded by the budA gene), acetolactate synthase (ALS, encoded by the budB gene) and butanediol dehydrogenase (BDH, encoded by the budC gene) catalyse the synthesis of 2,3-BDO [17]. The results of previous studies revealed that mutation of ALD not only decreased carbon flux to 2,3-BDO, but also increased the ratio of NADH to NAD+ by decreasing NADH consumption due to 2,3-BDO synthesis. Consequently, carbon flux was diverted towards the biosynthesis of 1,3-PDO [15]. Similarly, inactivation of BDH and expression of formate dehydrogenase reduced 2,3-BDO production and increased 1,3-PDO production [24], and disruption of the budC gene in K. pneumoniae ZG38 produced the same result [16]. Cui et al. [25] reported an improvement in the intracellular redox state in 2,3-BDO-deficient mutants lacking budA and B. Additionally, excess NADH was produced in the LAC-deficient mutant overexpressing dhaT. Since the synthesis of 2,3-BDO is catalysed procedurally by bud B, A and C and taking into account the reports that the mutation of budA and C promoted 1,3-PDO production, it is deductive that budB disruption should also be beneficial to the 1,3-PDO production. However, Oh et al. [26] reported the deletion of ALS gene (budB), hampering efficient 1,3-PDO production. The logical prediction was contradicted with the results by Oh et al. [26]. That implied the function of ALS gene (budB) refering to glycerol metabolism was deserved to be further investigated. The results from this work were disagreed with the results by Oh et al. [26]. There may difference in fermentation condition between Oh et al. [26] and our study. In addition, the isomers of 2,3-BDO have been distinguished in our study but not in Oh et al. [26]
In this study, an ALS-deficient strain was constructed using the Red recombination system, and fermentation tests showed that inactivation of ALS caused a redistribution of metabolic flux, resulting in a decrease in the synthesis of 2,3-BDO and an increase in the synthesis of 1,3-PDO and LAC. Fermentation of K. pneumoniae ΔALS using glycerol as a substrate resulted in the production of 72.04 g L−1 of 1,3-PDO, which was a slightly higher than that of the parent strain (Table 3; Fig 4). Inactivation of the 2,3-BDO pathway was speculatively associated with a decrease in the consumption of NADH under aerobic conditions (Fig 1). This increases the available energy (NADH) supply that would otherwise be used by the competing 2,3-BDO pathway under anaerobic conditions. Moreover, LAC was the most abundant byproduct and reached 31.50 g L−1, double that of the parent strain. Cell growth was slightly decreased and glycerol utilization was slightly promoted compared to the parent strain. Interestingly, synthesis of meso-2,3-BDO was markedly inhibited in the mutant strain but synthesis of 2S,3S-BDO was increased (Fig 5). This indicates that an unknown enzyme catalyzes the conversion of pyruvate to diacetyl. The mutant strain retained ~20% of the ALS activity of the parent strain, and this unexpected residual activity may have contributed to the results. However, the ALS enzyme assay is based on measuring acetoin but not in the presence of acetolactate. The acetoin could be generated by the ALD and this could confound the readout.
Although the yield of 1,3-PDO was increased, the conversion was not promoted to a great degree, mainly due to the accompanying increase in LAC synthesis. Therefore, we predict that blocking LAC synthesis may be the preferred strategy when engineering 1,3-PDO production in K. pneumoniae. Our results indicate that 2,3-BDO synthesis competes with the synthesis of 1,3-PDO and LAC. Moreover, since blocking the formation of LAC stimulated 1,3-PDO and 2,3-BDO production in Klebsiella species [12, 13], we predict that knocking out ALS in combination with engineering of the LAC pathway would result in a mutant with lower LAC and 2,3-BDO by-products. This was proved by Oh et al. [26] but they did not get even higher 1,3-PDO production with the LAC-ALS dual-mutant. Heterologous expression of pyruvate decarboxylase and aldehyde dehydrogenase efficiently recovered glycerol metabolism in the 2,3-BDO synthesis-defective mutant [27]. They suggested the production of 1,3-PDO could be enhanced by preventing the accumulation of pyruvate.
Three enzymes in the butanediol synthesis pathway are encoded by budB, budA, and budC. Klebsiella spp. produces meso-2,3-BDO together with a small amount of 2S,3S-BDO. 2S,3S-BDO formation depends on the activity of budC. Butanediol dehydrogenase can catalyze the conversion of diacetyl to S-acetoin and further to 2S,3S-BDO as well as R-acetoin to meso-BDO. Diacetyl is a nonenzymatic catalyzed product of α-acetolactate. BudC is the only known enzyme that catalyzes the conversion of diacetyl to S-acetoin and further to 2S,3S-BDO [28]. The metabolic pathway of the two isomers of 2,3-BDO synthesis in K. pneumoniae is shown in Fig 1. In this study, deleting the budB gene not only decreased the activity of ALS, but also decreased meso-2,3-BDO and increased 2S,3S-BDO. This phenotype indicates that meso-2,3-BDO formation is dependent on the activity of ALS whereas 2S,3S-BDO formation is inhibited by the activity of ALS. ALS is the first enzyme in the biosynthetic pathways of meso-2,3-BDO and 2S,3S-BDO in Enterobacteriaceae [17], and catalyzes the conversion of pyruvate to 2,3-BDO. Thus, it was not unexpected to observe a decrease in the formation of meso-2,3-BDO in the ALS-deficient mutant strain. The observed increase in 2S,3S-BDO in the mutant strain could be explained by an unknown enzyme that catalyzes the conversion of pyruvate to diacetyl and 2S,3S-BDO. Significantly, the mutation of ALS resulted in the accumulation of a greater amount of 2S,3S-BDO, suggesting this phenomenon could be helpful for 2S,3S-BDO production.
Glycerol metabolism is a typical biological redox pathway. In this study, a 2,3-BDO pathway-deficient mutant of K. pneumoniae HLS4 was constructed by knocking out the ALS gene. To investigate the influence of the ALS mutation on glycerol metabolism, ALS activity and various physiological properties including the yield of products and the distribution of metabolites and 2,3-BDO isomers was compared in the ΔALS and wild-type strains. Both the glycerol flux and distribution of metabolites were profoundly altered in the mutant strain in which the biosynthesis of meso-2,3-BDO was suppressed but 2S,3S-BDO synthesis was increased, while 1,3-PDO synthesis were slightly increased and LAC synthesis were largely increased. 1,3-PDO concentration and productivity were slightly increased by 4.71% and 4.65%, respectively. The overall conversion of glycerol to 1,3-PDO was not increased significantly due to an accompanying increase in the synthesis of LAC. Further engineering preventing the accumulation of pyruvate may be beneficial to improve 1,3-PDO production and reduce byproducts.
Acknowledgments
This work was supported by grants from China Agriculture Research System (CARS-47-G16), Guangdong Provincial Natural Science Foundation (2017A030313180 and 2015A030313854), National Natural Science Foundation of China (31502207) and Administration of Ocean and Fisheries of Guangdong Province (GD2012-D01-002).
The funders had no role in study design, data collection and analysis, decision to publish, or preparation of the manuscript.
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