The metabolic flux regulation of klebsiella pneumoniae based on quorum sensing system
The metabolic flux regulation of klebsiella pneumoniae based on quorum sensing system"
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ABSTRACT Quorum-sensing (QS) systems exist universally in bacteria to regulate multiple biological functions. _Klebsiella pneumoniae_, an industrially important bacterium that produces
bio-based chemicals such as 2,3-butanediol and acetoin, can secrete a furanosyl borate diester (AI-2) as the signalling molecule mediating a QS system, which plays a key regulatory role in
the biosynthesis of secondary metabolites. In this study, the molecular regulation and metabolic functions of a QS system in _K. pneumoniae_ were investigated. The results showed that after
the disruption of AI-2-mediated QS by the knockout of _luxS_, the production of acetoin, ethanol and acetic acid were relatively lower in the _K. pneumoniae_ mutant than in the wild type
bacteria. However, 2,3-butanediol production was increased by 23.8% and reached 54.93 g/L. The observed enhancement may be attributed to the improvement of the catalytic activity of
2,3-butanediol dehydrogenase (BDH) in transforming acetoin to 2,3-butanediol. This possibility is consistent with the RT-PCR-verified increase in the transcriptional level of _budC_, which
encodes BDH. These results also demonstrated that the physiological metabolism of _K. pneumoniae_ was adversely affected by a QS system. This effect was reversed through the addition of
synthetic AI-2. This study provides the basis for a QS-modulated metabolic engineering study of _K. pneumoniae_. SIMILAR CONTENT BEING VIEWED BY OTHERS PYRUVATE-RESPONSIVE GENETIC CIRCUITS
FOR DYNAMIC CONTROL OF CENTRAL METABOLISM Article 07 September 2020 REDESIGNING REGULATORY COMPONENTS OF QUORUM-SENSING SYSTEM FOR DIVERSE METABOLIC CONTROL Article Open access 21 April 2022
AGR QUORUM SENSING INFLUENCES THE WOOD-LJUNGDAHL PATHWAY IN _CLOSTRIDIUM AUTOETHANOGENUM_ Article Open access 10 January 2022 INTRODUCTION A communication system among bacteria was first
discovered in the 1970s while studying the luminescence mechanism of _Photobacterium fischeri_1. This phenomenon was observed in the luminescence organs of marine organisms and was named
quorum sensing (QS)2. In bacterial cells, QS consists of small, diffusible signalling molecules (autoinducers) capable of sensing the density of bacterial cells and subsequently initiating
the coordinated expression of several key genes throughout the entire bacterial community when the autoinducer concentration exceeds a critical threshold in the cells3,4. Recent research has
led to the discovery of some new autoinducers in bacteria, illustrated how these autoinducers are recognized by cognate receptors, revealed new regulatory components embedded in canonical
signalling circuits and identified novel regulatory network designs5. At the same time, QS is also a mechanism for bacterial adaptation to the environment. QS systems exist in multiple
bacterial species3, and the luxR family of proteins in this system play a key role as transcription regulators2. With LuxI protein and signalling molecules, QS systems can modulate a variety
of physiological functions, such as bioluminescence1, symbiosis6, Ti plasmid conjugative transfer7, biofilm formation8, group mobility, pathogenesis9, among others. Notably, the QS system
in _Pseudomonas aeruginosa_ involves two discrete acyl-homoserine lactone (AHL) molecules (OdDHL and BHL) that are generated and sensed by two different signalling systems (LasIR and RhlIR),
which control the production of a diverse variety of virulence factors and biofilm formation, respectively4. Recently, the emergence and worldwide spread of antibiotic-resistant bacteria
have increased the importance of finding therapeutic alternatives to compensate for the reduced effectiveness of antibiotics10. QS systems have also been suggested as promising targets for
developing new anti-infective compounds based on the regulatory function of these systems in the pathogenesis of bacteria11. It is reasonable to consider that targeting the QS system would
put less selective pressure on pathogens, thus avoiding the development of resistant bacteria and combating some of the most hard-to-treat infections that are resistant to powerful
antibiotics11. Fundamental research into the QS mechanism has revealed suprising discoveries4. For example, the signalling molecule _N_-(3-oxododecanoyl)-l-homoserine lactone can cause
inflammation and induce immunomodulatory activity12, which may reveal new drug targets. Currently, the gradual exhaustion of petroleum has revived significant interest in producing bio-based
bulk chemicals, including 2,3-butanediol, from biomass13. The demand and manufacture of 2,3-butanediol are increasing worldwide due to the extensive industrial applications of this
chemical14. For example, 2,3-butanediol can be used as a liquid fuel additive because of its high combustion value (27.198 Jg−1), as an antifreeze agent due to the low freezing point of −60
°C, as a carrier for pharmaceuticals and as a precursor in the production of methyl ethyl ketone and 1,3-butadiene through dehydration. In addition, 2,3-butanediol is easily dehydrogenated
into acetoin and diacetyl, which can be used in food and cosmetics similar to flavouring agents14,15. _Klebsiella pneumoniae_16, a Gram-negative bacterium, is an industrially important
bacterium that produces bio-based chemicals, including 2,3-butanediol and acetoin17. _K. pneumoniae_ contains AI-1 type QS quenching enzymes, AHL lactonases18. The AHL lactonases in
prokaryotes can be categorized into 2 clusters: _AiiA_ and _AttA_. The lactonase from _K. pneumoniae_ belongs to the _AttA_ cluster and shares only 30% homology with lactonases from other
species18,19. In the submerged fermentation of _K. pneumonia_, because AHL lactonase is present, AHLs cannot reach the threshold concentration in the culture medium, cannot diffuse back into
the cell and cannot be recognized by the receptor protein. Therefore, an AHL-receptor protein complex cannot form, and the AHL-mediated QS system does not work. However, _K. pneumoniae_
contains _metK, pfs_ and _luxS_ genes, which all encode key enzymes in the synthesis of the signalling molecule AI-2, suggesting that _K. pneumoniae_ uses AI-2 as the signalling molecule in
a QS system to regulate group behaviours20,21. In nature, the tight regulation of AI-2 production by _K. pneumoniae_ occurs primarily at the level of _luxS_ transcription in the synthetic
pathway of AI-2, and the maximum AI-2 activity occurs during the late exponential phase, which was determined by our laboratory16. Mutations in _luxS_ induce an increase in the expression of
two lipopolysaccharide (LPS)-synthesis-related genes, _wbbM_ and _wzm_, which affect the biofilm formation of _K. pneumoniae_21. As such, this _LuxS_-dependent signal also plays a main role
in the early stages of biofilm formation by _K. pneumoniae_20. Therefore, it was concluded that AI-2 acts as a regulator of biofilm formation and LPS synthesis in _K. pneumoniae_21.
According to the primary literature, 2,3-butanediol fermentation is dependent on an AHL-dependent QS system in _Serratia_ spp.22. Although 2,3-butanediol production by _K. pneumoniae_ has
also been well studied, it was not known how 2,3-butanediol was regulated by an AI-2-mediated QS system until now. In this study, the molecular regulation and metabolic function of the QS
system in _K. pneumoniae_ was analysed based on previous studies of the cellular metabolic network of _K. pneumoniae_ and transcriptional characteristics of the QS system. Additionally, a
drift in the metabolic flux and changes in the physiological metabolic network of _K. pneumoniae_ were also investigated. The results presented here will lay the foundation for elucidating
the interplay between industrial microbial metabolism and QS systems. RESULTS REGULATION OF THE AI-2-MEDIATED QS SYSTEM IN _K. PNEUMONIAE_ The QS system of _K. pneumoniae_ is
_luxS_-dependent16; therefore, it is possible to regulate QS by inactivating a key gene, _luxS_, through mutagenesis. The gene product of _luxS_ is involved in the synthetic pathway of the
signalling molecule AI-2. Chromosomal _luxS_ was inactivated in each strain using a marker-exchange strategy based on the suicide vector pUTKm as described in the Materials and Methods. The
recombinant plasmid pUTKm-_luxS_ was introduced into _K. pneumoniae_ CICC 10018 competent cells by electrotransformation, followed by screening of the kanamycin-resistant _luxS_ mutants16.
Bacterial growth on the kanamycin plates was evident, suggesting that the _luxS_ gene was knocked out. Clones that were kanamycin-resistant were verified by PCR assays of genomic DNA. An
800-bp (as expected) fragment of the kanamycin-resistance gene was PCR-amplified with primers Kna-1 and Kna-2 (Fig. 1). Additionally, the samples were also verified by commercial sequencing.
The correct recombinant strain containing a kanamycin-resistance gene insertion in a chromosome was picked out (named _K. pneumoniae-6_) and was cultured in LB medium for further
experiments. EFFECTS OF QS QUENCHING ON THE METABOLIC FLUX OF _K. PNEUMONIAE_ As shown in Fig. 2, the production of 2,3-butanediol initially increased and then declined in both _K.
pneumoniae_ and _K. pneumoniae-6_ during fermentation. The production of 2,3-butanediol in _K. pneumoniae_ reached a peak at 12 h, whereas the peak production in _K. pneumoniae-6_ occurred
at 8 h. A possible explanation for this observation is the enhanced bioconversion to 2,3-butanediol under the catalysis of related enzymes in the metabolic flux. During this process, the
production of acetoin, acetic acid and ethanol was relatively lower in _K. pneumoniae-6_ than in _K. pneumoniae_, which may be attributed to the carbon flux shift because there was almost no
change in the catalytic activity of related enzymes involved in the biosynthesis of these compounds (data not shown). Notably, the decreased levels of these 3 compounds in the _luxS_ mutant
could be restored to the levels in the parental strain in the presence of 5 μM synthetic AI-2. Although _K. pneumoniae-6_ grew less well than its parent strain, the defective growth of _K.
pneumoniae-6_ could also be nullified by the addition of 5 μM synthetic AI-2. COMPARISON OF ENZYMATIC ACTIVITY DURING METABOLISM There are two metabolic pathways in bacteria for the
biosynthesis of 2,3-butanediol from α-acetolactic acid. In the first, α-acetolactic acid is converted to acetoin (the key precursor of 2,3-butanediol) by the catalysis of α-acetolactate
decarboxylase (α-ALDC). Next, acetoin is converted to 2,3-butanediol through the catalysis of 2,3-butanediol dehydrogenase (BDH). In the second metabolic pathway, α-acetolactic acid is
oxidized to diacetyl, and diacetyl is converted to acetoin through the catalysis of diacetyl reductase (DR). Subsequently, acetoin is converted to 2,3-butanediol through the catalysis of
BDH. Therefore, the enzymatic activities of BDH, α-ALDC and DR in _K. pneumoniae_ and _K. pneumoniae-6_ were measured at the indicated time points after preparing a crude enzyme solution.
Figure 3 shows that the activities of these 3 enzymes first increased and then declined with time in both strains. The maximal enzymatic activities of BDH, α-ALDC and DR occurred at similar
times in both strains, at 8 h, 12 h and 8 h, respectively. The enzymatic activity of α-ALDC was similar in both strains, whereas the enzymatic activity of BDH and DR was relatively lower in
_K. pneumoniae_. This lower DR activity level decreased the synthesis of acetoin from diacetyl and increased the accumulation of diacetyl in the fermentation broth of _K. pneumoniae_.
Additionally, the activity of α-acetolactate synthase, which catalyses the biosynthesis of α-acetolactic acid from pyruvic acid, was also determined, but there was no significant difference
between these two strains (data not shown). In _K. pneumoniae_, the enzymatic synthesis and metabolic control of 2,3-butanediol and acetoin were tightly regulated by QS. The knockout of
_luxS_ led to the destruction and functional disability of the QS system. As a result, 2,3-butanediol production was improved, and it was confirmed that this improvement was caused by a
change in the expression level of enzymes (BDH and DR) involved in the synthetic pathway of 2,3-butanediol. These results suggest that the knockout of _luxS_ can result in variations in
enzymatic activities and further affect 2,3-butanediol biosynthesis. According to these results, a number of conclusions can be drawn. After quenching the QS system in _K. pneumoniae-6_, the
activity of DR improved significantly, promoting the conversion from diacetyl to acetoin. The increased activity of BDH accelerated the biosynthesis of 2,3-butanediol using acetoin as a
substrate, and therefore, the production of 2,3-butanediol was greatly enhanced. ANALYSIS OF BUDC TRANSCRIPTION The gene _budC_ encodes BDH, which catalyses the reaction of acetoin to
2,3-butanediol. As depicted in Fig. 4, the _budC_ gene was constitutively expressed at the tested time points. Additionally, the number of _budC_ transcripts first increased and then
decreased in _K. pneumoniae-6_, and the maximal transcription levels occurred at 8 h. This result may explain why the maximal enzymatic activity of BDH and the maximal 2,3-butanediol
production took place at 8 h. During the exponential growth phase in _K. pneumoniae-6_, the _budC_ gene expression increased dramatically to a maximal value. However, _budC_ expression
decreased upon entry into the stationary growth phase. Maximal 2,3-butanediol production and _budC_ expression occurred at the same time point (8 h), which suggests that the difference in
2,3-butanediol production by _K. pneumoniae_ and _K. pneumoniae-6_ is due to changes at the transcriptional level of the _budC_ gene during the growth of these two bacteria. DISCUSSION The
chemical butanol is a four-carbon diol that has wide industrial applications for the manufacture of bulk chemicals23. In general, butanol is produced from carbohydrates in submerged
fermentation by _Klebsiella_ spp.24,25,26,27, _Enterobacter_ spp.28,29,30,31, _Bacillus_ spp.32,33,34, and _Clostridia_ spp.35,36,37,38, among others. Since butanol-producing strains were
initially screened from natural environments, the yield, titre and productivity regarding butanol were frequently low, and these strains could not be used in industrial production.
Therefore, the current focus is on finding new strains from natural reservoirs and constructing or modifying strains through mutagenesis, evolutionary engineering and metabolic engineering
strategies to improve their production performance and compliance23. _K. pneumoniae_ and _Klebsiella oxytoca_ are important bio-based chemical-producing bacteria and can ferment glucose
primarily to 2,3-butanediol as a major fermentation end-product with relatively small amounts of acetoin, ethanol and some acids under micro-aerobic conditions because a significant amount
of pyruvate from glycolysis is channelled into the butanediol pathway, through which pyruvate is transformed into butanediol by the catalysis of acetolactate synthase, α-ALDC and BDH in an
orderly fashion17,27. To improve 2,3-butanediol production by _Klebsiella_ spp., _strain_ modification by metabolic engineering has attracted a great deal of attention around the
world17,24,25,26,27. For example, Rathnasingh _et al_. improved the production of 2,3-butanediol in _K. pneumoniae_ by knocking out the genes (_ldhA, adhE and pta-ackA_) involved in the
formation of lactic acid, ethanol and acetic acid; the 2,3-butanediol production thus reached 91 g/L with a yield of 0.45 g per g glucose in batch fermentation27. Guo _et al_. constructed
_K. pneumoniae_ mutants that overexpressed α-ALS, α-ALDC, and AR to improve 2,3-butanediol production. The results revealed that 2,3-butanediol production by the recombinant _K. pneumoniae_
strain (KG-rs) that overexpressed both ALS and AR was 12% higher than that of the parental strain17. Cho _et al_. reported that 2,3-butanediol production reached 115.0 g/L in fed-batch
fermentation with pure glycerol with the construction of a double mutant (_pduC, ldhA) K. oxytoca_ strain to reduce the formation of 1,3-propanediol and lactic acid24. This group also
discovered that if acetoin reductase was overexpressed in _K. oxytoca_, acetoin accumulation was significantly reduced, and the highest titre of 2,3-butanediol (142.5 g/L) was achieved25.
Currently, metabolic engineering strategies at the gene level are commonly used by many scientists to reform certain special production strains. Additionally, there has been growing interest
in developing novel metabolic engineering strategies at the cellular level based on the QS system in bacteria39,40. For example, in bacteria of the _Serratia_ genera, 2,3-butanediol
fermentation has been shown to be affected by an _spl_I-dependent QS system, and the knockout of the _spl_I gene caused a shift towards enhanced acid production. Of course, the biosynthesis
of 2,3-butanediol is not completely shut off by eliminating QS. At the same time, QS also controls the production of extracellular enzymes, including chitinase, nuclease, and protease13,22.
In _Vibrio cholera,_ the production of 2,3-butanediol is regulated by multiple QS systems via the transcriptional activator AphA. Two QS systems use a CAI-1 autoinducer and AI-2 as
signalling molecules, respectively, and act in parallel to trigger a phosphorelay circuit41. In _Aeromonas hydrophila_, 2,3-butanediol fermentation is regulated by AHL-mediated QS because
the disruption of QS by the knockout of _ahyI_, synthesizing C4-HSL, results in medium acidification and blocks the metabolic switch to 2,3-butanediol synthesis13. Furthermore, the
inactivation of the regulatory protein AhyR in QS also suppressed 2,3-butanediol fermentation. Although 2,3-butanediol production by _K. pneumoniae_ has been well studied26,27, the data in
this report represent the first identification of a QS system regulating 2,3-butanediol production. In this study, the effects of QS on 2,3-butanediol formation in _K. pneumoniae_ were
analysed in great detail. _K. pneumoniae_ contains AI-1 type QS quenching enzymes, including AHL lactonase, and possesses _pfs_ and _luxS_ orthologues in its genome; therefore, it can be
inferred that AI-2 is the signalling molecule mediating the QS system40. In the biosynthesis of AI-2, _luxS_ and _pfs_ encode a 5′-methylthioadenosine/S-adenosylhomocysteine nucleosidase and
form an operon that utilizes SAH or MTA as a substrate for AI-2 production16. Furthermore, the tight regulation of AI-2 production is largely at the level of _luxS_ transcription.
Therefore, the molecular regulation of the QS system in _K. pneumoniae_ was established by constructing a _luxS_ mutant. Next, changes in the metabolites between _K. pneumoniae-6 (luxS_
mutant) and _K. pneumoniae_ (parental strain) were compared through shaking fermentation with glucose. The results indicated that after quenching the QS system, the production of acetoin,
ethanol and acetic acid was relatively lower in _K. pneumoniae-6_, but the 2,3-butanediol production was increased by 23.8% and reached a maximum level of 54.93 g/L. This increase suggested
that the activation of the 2,3-butanediol pathway is not QS regulated, which is different from _Serratia_ spp.22. The precise mechanism of regulation has yet to be elucidated. This
improvement effect was reversed through the addition of 5 μM synthetic AI-2. At the same time, enzymatic activity analyses revealed that there was no significant difference in α-ALDC
activity between these two strains, whereas the enzymatic activities of BDH and DR were relatively lower in _K. pneumoniae_, in accordance with the transcriptional analysis of _budC._ These
findings should be useful for improving 2,3-butanediol production via QS-based metabolic engineering. Furthermore, this study provides a solid basis for investigating the link between QS and
bacterial physiology. Although the development of butanol-producing microorganisms and fermentation processes has seen remarkable progress, the recovery of butanol from the fermentation
broth still remains a challenging problem under industrial production conditions23. To develop commercially applicable techniques for the recovery of 2,3-butanediol, numerous methods have
been proposed42, _including_ ion exchange, electrodialysis, membrane filtration, pervaporation, reactive extraction and liquid-liquid extraction43,44. However, these methods have inherent
drawbacks that must be overcome, such as generating a large amount of wastewater for resin regeneration, requiring expensive membranes, increasing filtration steps and decreasing the
recovery yield of 2,3-butanediol42. In recent years, many scientists have been developing _in situ_ product recovery techniques, especially for the low concentration of 2,3-butanediol in
fermentation broth. Jeon _et al_. established a four-step recovery process through alcohol precipitation and vacuum distillation, and a recovery yield of 76.2% and a purity of 96.1% were
obtained from fermentation broth containing approximately 90 g/L of 2,3-butanediol produced by the _ldhA_-deficient _K. pneumoniae_42. Xue _et al_. reported a succession of various methods
for the recovery of butanol produced by _Clostridium acetobutylicum_, such as gas stripping37,38, adsorption35, and a vapour stripping-vapour permeation (VSVP) process36. When gas stripping
was applied intermittently in fed-batch fermentation, 195.9 g/L acetone-butanol-ethanol or 150.5 g/L butanol was obtained, and furthermore, energy consumption and water usage was reduced by
at least 90%. Two-stage gas stripping was more effective for producing high-titre butanol, and a highly concentrated product containing 420.3 g/L butanol (532.3 g/L acetone-butanol-ethanol)
can be obtained with this strategy. At the same time, this purification process consumed much less energy. Compared to pervaporation and gas stripping, the VSVP process produced a condensate
containing 212.0–232.0 g/L butanol from a fermentation broth containing ~10 g/L butanol, which suggests that the VSVP process has great potential for efficient butanol recovery. In
acetone-butanol-ethanol fermentation, the _in situ_ product recovery process with activated carbon was also carried out. The results indicated that immobilized-cell fermentation with
adsorption produced 54.6 g/L butanol with a productivity of 0.45 g/L·h, and a condensate containing approximately 167 g/L butanol was obtained after thermal desorption. Furthermore, this
liquid phase _adsorption using_ activated carbon was energy efficient and can be easily applied in butanol fermentation. In the future, integrated downstream processing technologies for
fermentative 2,3-butanediol are especially required regarding yield, purity, and energy consumption. MATERIALS AND METHODS BACTERIAL STRAINS, PLASMIDS, PRIMERS AND REAGENTS The bacterial
strains, plasmids and primers used in this study are listed in Table 1. All _E. coli_ and _K. pneumoniae_ strains were grown in Luria-Bertani (LB) growth medium (0.5% yeast extract, 1%
tryptone, and 1% NaCl) at 37 °C and 30 °C, respectively. Antibiotics were added in the following amounts (per mL) when necessary: 100 μg ampicillin and 50 μg kanamycin for _E. coli_ and _K.
pneumoniae_, respectively. All enzymes, DNA and protein markers, and Kits were from TaKaRa Biotech (Dalian, China). Other chemicals were analytical reagent grade. All the oligonucleotide
primers were synthesized in Bioasia Biotech (Shanghai, China). QUENCHING THE QS SYSTEM IN _K. PNEUMONIAE_ The QS mechanism of _K. pneumoniae_ through the _LuxS_/_AI-2 signalling system_ has
played an important role in understanding the functions of QS systems. Therefore, the regulation of the QS system was determined by constructing a QS _luxS_ knockout mutant strain. A 260-bp
fragment from the _luxS_ gene encoding a key enzyme for AI-2 synthesis was amplified from the genomic DNA of _K. pneumoniae_ CICC 10018 using a PCR technique with the primers luxS-1 and
luxS-2. Commercial sequencing was used to verify these mutants. The _luxS_ fragment and the pUTKm plasmid were double digested with _Kpn_ I and _Sca_ I and then ligated between the _Kpn_ I
and _Sca_ I sites in the plasmids. Successful ligation resulted in generating a marker-exchange plasmid, pUTKm-_luxS_, which was transformed into _E. coli_ cc118 competent cells. The
recombinant pUTKm-_luxS_ cells were selected and confirmed using DNA sequencing and double enzyme digestion. Subsequently, the suicide vector pUTKm-_luxS_ was transformed into _K.
pneumoniae_ CICC 10018 competent cells by electroporation. Mutants were selected on NB medium containing 800 μg/mL ampicillin and 200 μg/mL kanamycin. For each strain with a
kanamycin-resistance gene inserted into the chromosome, the disruption of the locus was confirmed by PCR analysis using the primers Kan-1 and Kan-2 complementary to the KnR cassette. This
mutant was named _K. pneumoniae-6_. GENE EXPRESSION AND METABOLIC FLUX ANALYSIS The _budC_ gene encodes BDH, which is involved in the biosynthetic pathway of 2,3-butanediol. An RT-PCR
analysis was performed with SYBR Green technology to confirm changes in the transcription level of the _budC_ gene. To prepare an external plasmid standard curve, the plasmid pGM-T-_budC_
was constructed. The _budC_ gene was amplified from _K. pneumoniae_ with the primers budC-1 and budC-2 using genomic DNA as a template and was cloned into vector pGM-T to generate the
standard plasmid pGM-T. The purified plasmid pGM-T-_budC_ was serially diluted (1:10) over the appropriate concentration range (usually 105–109). To achieve a reliable standard curve for
each measured parameter, the plasmid was PCR-amplified in five replicates for each standard dilution point over the complete standard curve range. Figure 4A shows the standard curves for the
_budC_ gene, which were used for the determination of _budC_ gene transcription. After preparing the standard, total RNA was isolated from the _K. pneumoniae-6_ sample during growth in the
fermentation medium and was reverse transcribed. The resulting cDNA was directly subjected to real-time PCR with the primers F-budC and R-budC. At the same time, the production of the
primary metabolites (acetic acid, ethanol, acetoin and 2,3-butanediol) by _K. pneumoniae_ was assessed with the corresponding methods listed in the “Analytical methods” section. BATCH
FERMENTATION AT BIOREACTOR SCALE Submerged fermentation experiments were carried out in a bioreactor to investigate the changes in metabolic flux in _K. pneumoniae_. The fermentation medium
was composed of 90 g/L glucose, 13.6 g/L KH2PO4, 5 g/L (NH4)2SO4, 4 g/L MgSO4·7H2O, 4 g/L Citric acid, 15 g/L yeast extract, 4 g/L NaCl, 0.4 g/L CaCl2, 0.08 g/L FeSO4 and 0.3 mL of trace
elements prepared as described. The trace elements consisted of 34.2 g of ZnCl2, 2.7 g of FeCl3·6H2O, 10 g of MnCl2·4H2O, 0.85 g of CuCl2·2H2O, 23.8 g of CoCl2·6H2O, 0.31 g of H3BO3 and 0.25
g of Na2MoO4·2H2O in 1 L of deionized water. Unless otherwise specified, the submerged cultures of _K. pneumoniae_ for the production of 2,3-butanediol were maintained under the following
culture conditions: temperature, 30 °C; aeration rate, 4 vvm; initial pH, 7.0; and a working volume of 3.5 L. All experiments were performed in triplicate. ANALYTICAL METHODS The primary
components, ethanol, acetic acid, acetoin, and 2,3-butanediol, and other metabolites in the fermentation broth of _K. pneumonia_ were detected using gas chromatography as summarized in the
following steps: (1) An Agilent7890A DB-TPH column was used; (2) the detector temperature was set at 250 °C; (3) the column temperature was set at 100 °C for 2 min; (4) the temperature was
increased to 180 °C at 20 °C/min and maintained for 1 min, then (5) the temperature was increased to 220 °C at 30 °C/min and was maintained for 2 min; finally, (6) the sample was injected in
a volume of 1 μL. DETERMINATION OF ENZYMATIC ACTIVITY * 1 Preparation of crude enzyme Thirty millilitres of bacterial suspension collected at the indicated time points during fermentation
was centrifuged at 8000 rpm for 5 min at 4 °C. The pellet was re-suspended twice with PBS and centrifuged at 8000 rpm for 5 min at 4 °C. Subsequently, 6 mL of buffer was added, and the
mixture was ultrasonicated 99 × for 2s with 5-s intervals. The sonication procedure was repeated three times, followed by centrifugation at 8000 rpm for 20 min at 4 °C. The supernatant was
the crude enzyme. * 2 Determination of α-ALDC activity The amount of enzyme required to convert α-acetolactic acid into 1 μmol of acetoin at 37 °C within a unit interval (min) is defined as
a unit of enzymatic activity. The procedure was as follows: 25 μL of α-acetoxy-α-methyl-ethyl acetate was sufficiently mixed with 750 μL of 1 M NaOH and 750 μL of deionized water and
incubated at room temperature for 20 min. The volume was then adjusted to 10 mL with PBS (pH 6). The pH was adjusted to pH 6 with 0.5 M HCl, and the volume was adjusted to 12.5 mL with PBS
(pH 6). Two hundred microlitres of the final solution was mixed with 200 μL of crude enzyme and 100 μL of PBS (pH 6, containing 0.05% (w/v) Tween 80 and 600 mM NaCl). After sufficient
mixing, the mixture was incubated in a 37 °C water bath for 20 min. Afterwards, 4.5 mL of a chromogenic agent (2.5 g of α-naphthol and 0.25 g of creatine in a volume of 250 mL of 1 M NaOH)
was added to the mixture, which was then incubated for 40 min at room temperature, followed by OD measurement at 522 nm. * 3 Determination of BDH activity The sample solution contained 2330
μL of PBS buffer (1 mmol of ZnSO4, 20 μL of crude enzyme and 300 μL of 10 mM NAD+). This solution was the same as the control solution. Following the baseline determination, 30 μL of 1 mM
2,3-butanediol solution was added to the sample solution, while 300 μL of deionized water was added to the blank control solution. After mixing, the change in OD was measured at 340 nm. * 4
Determination of DR activity The sample solution contained 2330 μL of PBS buffer, 20 μL of crude enzyme and 300 μL of 10 mM diacetyl solution. To balance the baseline, 300 μL of 10 mM NADH
solution was added to the sample solution, while 300 μL of deionized water was added to the blank control solution. After mixing the solutions, OD measurements were performed at 340 nm.
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Biotechnology 36, 313–317, doi: 10.1007/s10295-008-0501-z (2009). Article CAS Google Scholar Download references AUTHOR INFORMATION AUTHORS AND AFFILIATIONS * College of Life Sciences,
Fujian Agriculture and Forestry University, Fuzhou, 350002, P.R. China Shujing Sun, Haiyang Zhang, Shuyi Lu & Chunfen Lai * Centre for Bioengineering and Biotechnology, China University
of Petroleum (East China), Qingdao, 266580, P.R. China Huijun Liu & Hu Zhu * College of Plant Protection, Fujian Agriculture and Forestry University, Fuzhou, 350002, P.R. China Hu Zhu
Authors * Shujing Sun View author publications You can also search for this author inPubMed Google Scholar * Haiyang Zhang View author publications You can also search for this author
inPubMed Google Scholar * Shuyi Lu View author publications You can also search for this author inPubMed Google Scholar * Chunfen Lai View author publications You can also search for this
author inPubMed Google Scholar * Huijun Liu View author publications You can also search for this author inPubMed Google Scholar * Hu Zhu View author publications You can also search for
this author inPubMed Google Scholar CONTRIBUTIONS S.J.S. and H.Z. designed the experiments. S.J.S., H.Y.Z., S.Y.L., C.F.L. and H.J.L. performed the experiments. S.J.S. and H.Z. analysed the
data and prepared the figures and tables. S.J.S. and H.Z. wrote the main manuscript. All the authors reviewed the manuscript. ETHICS DECLARATIONS COMPETING INTERESTS The authors declare no
competing financial interests. RIGHTS AND PERMISSIONS This work is licensed under a Creative Commons Attribution 4.0 International License. The images or other third party material in this
article are included in the article’s Creative Commons license, unless indicated otherwise in the credit line; if the material is not included under the Creative Commons license, users will
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THIS ARTICLE CITE THIS ARTICLE Sun, S., Zhang, H., Lu, S. _et al._ The metabolic flux regulation of _Klebsiella pneumoniae_ based on quorum sensing system. _Sci Rep_ 6, 38725 (2016).
https://doi.org/10.1038/srep38725 Download citation * Received: 04 August 2016 * Accepted: 11 November 2016 * Published: 07 December 2016 * DOI: https://doi.org/10.1038/srep38725 SHARE THIS
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