Isolation and characterization of acetamidocinnamate acylase,a new enzyme suitable for production of l-phenylalanine

Summary A new acylase catalyzing the deacetylation of acetamidocinnamic acid (ACA) was found in strains of Brevibacterium sp. Such strains could be isolated from soil samples by their ability to grow on ACA as well as on l-phenylalanine. A 110-fold enrichment of the enzyme with an over-all yield of 48% was obtained in 4 steps resulting in an electrophoretically pure preparation of 28.6 U·mg^-1. Important enzymological data concerning the application of the enzyme are: K _M (ACA) 0.45 mM, pH-optimum 7.5, heat stability up to 52°C, molecular weight of 50.000 Dalton, two subunits. Deacetylation of ACA resulted in phenylpyruvate via the unstable enamine-imine derivative. Coupling the acylase with l-phenylalanine dehydrogenase proved to be an alternative route for l-phenylalanine production avoiding substrate inhibition by phenylpyruvate and its instability. The substrate specifity of ACA-acylase revealed that the enzyme probably acts as a dipeptidase in its biological function.Abbreviations ACA acetamidocinnamate, acetamidocinnamic acid - FPLC fast protein liquid chromatography - pheDH l-Phenylalanine dehydrogenase - HicDH Hydroxyisocaproate dehydrogenase - OD optical density - BSA bovine serum albumin - FDH formate dehydrogenase Dedicated to Professor Dr. H. J. Rehm on the occasion of his 60th birthday     

Biotransformation of phenylpyruvic acid to l-phenylalanine using a strain of Pseudomonas fluorescens ATCC 11250 with high transaminase activity

The rate of l-phenylalanine production from phenylpyruvic acid by whole cells of Pseudomonas fluorescens strain ATCC 11250 was greater than 3 g·l^-1 h^-1. Synthesis of transaminase was constitutive but activity was greatest in medium containing d- or l- phenylalanine as sole nitrogen source. Maximum conversion was observed at 34–40° C and at alkaline pH, with over six times initial rate of conversion at pH 12 than at pH 5. The optimum catalyst (cell) concentration was between 10–20 mg ml^-1 dry weight. The initial rate of conversion was directly proportional to phenylpyruvate concentration, up to 4%, but the conversion yield steadily decreased between 2% and 4% substrate concentration. The rate of conversion, as expected, increased as the concentration of glutamate increased. Whole cells were still capable of over 63% conversion after 40 days providing reactions were supplemented with pyridoxal phosphate. Immobilisation of cells in calcium alginate and operation of a packed bed bioreactor enabled the continuous production of l-phenylalanine in concentrations greater than 15 g·l^-1 after 60 days operation.     

Purification,characterization and regulation of a monomeric l-phenylalanine dehydrogenase from the facultative methylotroph Nocardia sp. 239

In Nocardia sp. 239 d-phenylalanine is converted into l-phenylalanine by an inducible amino acid racemase. The further catabolism of this amino acid involves an NAD-dependent l-phenylalanine dehydrogenase. This enzyme was detected only in cells grown on l- or d-phenylalanine and in batch cultures highest activities were obtained at relatively low amino acid concentrations in the medium. The presence of additional carbon- or nitrogen sources invariably resulted in decreased enzyme levels. From experiments with phenylalanine-limited continuous cultures it appeared that the rate of synthesis of the enzyme increased with increasing growth rates. The regulation of phenylalanine dehydrogenase synthesis was studied in more detail during growth of the organism on mixtures of methanol and l-phenylalanine. Highest rates of l-phenylalanine dehydrogenase production were observed with increasing ratios of l-phenylalanine/methanol in the feed of chemostat cultures. Characteristic properties of the enzyme were investigated following its (partial) purification from l- and d-phenylalanine-grown cells. This resulted in the isolation of enzymes with identical properties. The native enzyme had a molecular weight of 42 000 and consisted of a single subunit; it showed activity with l-phenylalanine, phenylpyruvate, 4-hydroxyphenyl-pyruvate, indole-3-pyruvate and -ketoisocaproate, but not with imidazolepyruvate, d-phenylalanine and other l-amino acids tested. Maximum activities with phenylpyruvate (310 mol min^-1 mg^-1 of purified protein) were observed at pH 10 and 53°C. Sorbitol and glycerol stabilized the enzyme.Abbreviations RuMP ribulose monophosphate - HPS hexulose-6-phosphate synthase - HPT hexulose-6-phosphate isomerase - FPLC fast protein liquid chromatography     

l-Phenylalanine dehydrogenase from Brevibacterium sp. for production of l-phenylalanine by reductive amination of phenylpyruvate

Summary For production of l-phenylalanine the reductive amination of phenylpyruvate, catalyzed by phenylalanine-dehydrogenase was examined. To reach high levels and a sufficient stability of the inducible intracellular enzyme, growth conditions of Brevibacterium sp. are optimized. For continuous production of l-phenylalanine in an enzyme membrane reactor, the kinetic parameters of the partially purified enzyme are determined.In continuous production a space time yield of 37.4 g l-Phe l^-1 d^-1 can be reached.By means of the measured kinetic parameters and simultaneous calculation of the mass balances of all reaction components the behaviour of the reactor can be simulated. For certain conditions the multi-enzyme-system shows multiple steady-states.Abbreviations l-phe l-phenylalanine - phepy phenylpyruvate - PEG polyethylenglycol - pheDH l-phenylalanine dehydrogenase     

Anaerobic acetate oxidation to CO2 by Desulfotomaculum acetoxidans

Desulfotomaculum acetoxidans has been proposed to oxidize acetate to CO₂ via an oxidative acetyl-CoA/carbon monoxide dehydrogenase pathway rather than via the citric acid cycle. We report here the presence of the enzyme activities required for the operation of the novel pathway. In cell extracts the following activities were found (values in brackets=specific activities and apparent K _m; 1 U·mg^-1=1 mol·min^-1·mg protein^-1 at 37°C): Acetate kinase (6.3 U·mg^-1; 2 mM acetate; 2.4 mM ATP); phosphate acetyltransferase (60 U·mg^-1, 0.4 mM acetylphosphate; 0.1 mM CoA); carbon monoxide dehydrogenase (29 U·mg^-1; 13% carbon monoxide; 1.3 mM methyl viologen); 5,10-methylenetetrahydrofolate reductase (3 U·mg^-1, 0.06 mM CH₃–FH₄); methylenetetrahydrofolate dehydrogenase (3.6 U·mg^-1, 0.9 mM NAD, 0.1 mM CH₂=FH₄); methenyltetrahydrofolate cyclohydrolase (0.3 U·mg^-1); formyltetrahydrofolate synthetase (3 U·mg^-1, 1.4 mM FH₄, 0.4 mM ATP, 13 mM formate); and formate dehydrogenase (10 U·mg^-1, 0.4 mM formate, 0.5 mM NAD). The specific activities are sufficient to account for the in vivo acetate oxidation rate of 0.26 U·mg^-1.Non-standard abbreviations FH₄ Tetrahydrofolate - CHO-FH₄ N¹⁰-formyltetrahydrofolate - CHFH₄ N⁵,N¹⁰-methenyltetrahydrofolate - CH₂=FH₄ N⁵,N¹⁰-methylenetetrahydrofolate - CH₃–FH₄ N⁵-methyltetrahydrofolate - MOPS morpholinopropane sulfonic acid - DTT d,l-1,4-dithiothreitol - TRIS tris-(hydroxymethyl)-aminomethane - Ap₅A p¹,P⁵-di(adenosine-5)pentaphosphate - MV methyl viologen     

Regulation of phospho(enol)-pyruvate-and oxaloacetate-converting enzymes in Corynebacterium glutamicum

The presence and properties of the enzymes involved in the synthesis and conversion of phospho(enol)pyruvate (PEP) and oxaloacetate (OAA), the precursors for aspartate-derived amino acids, were investigated in three different Corynebacterium strains. This study revealed the presence of both PEP carboxykinase 0.29 mol·min^–1·mg^–1 of protein [units (U)·mg^–1] and PEP synthetase (0.13 U·mg^–1) in C. 2 glutamicum as well as pyruvate kinase (1.4 U·mg^–1) and PEP carboxylase (0.16 U·mg^–1). With the exception of PEP carboxykinase these activities were also present in glucose-grown C. flavum and C. lactofermentum. Pyruvate carboxylase activity was not detected in all three species cultivated on glucose or lactate. At least five enzyme activities that utilize OAA as a substrate were detected in crude extracts of C. glutamicum: citrate synthase (2 U·mg^–1), malate dehydrogenase (2.5 U·mg^–1), glutamate: OAA transaminase (1 U·mg^–1), OAA-decarboxylating activity (0.89 U·mg^–1) and the previously mentioned PEP carboxykinase (0.29 U·mg^–1). The partially purified OAA-decarboxylase activity of C. glutamicum was completely dependent on the presence of inosine diphosphate and Mn²⁺, had a Michaelis constant (K _m) of 2.0mm for OAA and was inhibited by ADP and coenzyme A (CoA). Examination of the kinetic properties showed that adenine nucleotides and CoA derivatives have reciprocal but reinforcing effects on the enzymes catalyzing the interconversion of pyruvate, PEP and OAA in C. glutamicum. A model for the regulation of the carbon flow based on these findings is presented.Correspondence to: M. S. M. Jetten     

Enzymatic production of l-phenylalanine from the racemic mixture of d,l-phenyllactate

Summary The production of l-phenylalanine from the racemate d,l-phenyllactate in an enzyme membrane reactor has been examined. In a first step the racemate is dehydrogenated to the prochiral intermediate phenylpyruvate by the enzymes d-and l-hydroxyisocaproate dehydrogenase. In a second step phenylpyruvate is reductively aminated to l-phenylalanine by l-phenylalanine dehydrogenase. Both steps are dependent on coenzyme, the first one requires NAD, the second one NADH in stoichiometric amounts; in this way the coenzyme is regenerated and only required catalytically. The coenzyme is covalently bound to polyethylene glyco-20 000 and can thus be retained in the reactor analogously to the three enzymes. In order to optimize the continuous production of l-phenylalanine from d,l-phenyllactate, models of the reaction kinetics and of the reactor system have been set up. By means of the reactor model, we can calculate the optimum ratio of the three enzymes, the optimum coenzyme concentration and the optimum phenylpyruvate concentration in the feed.In this process, at a substrate concentration of 50 mM d,l-phenyllactate we reached a spacetime-yield of 28 g l-Phe/(l*d).Abbreviations PEG polyethylene glycol - d-HicDH d-hydroxyisocaproate dehydrogenase - l-HicDH l-hydroxyisocaproate dehydrogenase - PheDH l-phenylalanine dehydrogenase - V _max maximum velocity - K _M Michaelis-Menten constant - K _l inhibition constant - R₁ reaction rate of the d-HicDH forward reaction - R₂ reaction rate of the d-HicDH reverse reaction - R₃ reaction rate of the l-HicDH forward reaction - R₄ reaction rate of the l-HicDH reverse reaction - R₅ reaction rate of the PheDH forward reaction - R₆ reaction rate of the PheDH reverse reaction - d-PLac d-phenyllactate - l-PLac l-phenyllactate - PPy phenylpyruvate - l-Phe l-phenylalanine - NH₄ ammonium - residence time     

Production of l-phenylalanine from phenylpyruvate by Paracoccus denitrificans containing aminotransferase activity

Summary To establish an efficient production method for l-phenylalanine, the production of l-phenylalanine from phenylpyruvate by Paracoccus denitrificans pFPr-1 containing aminotransferase activity was investigated. By using intact cells, 0.74M l-phenylalanine was produced from 0.8M phenylpyruvate (conversion yield, 92.5%). Moreover, by using immobilized cells with -carrageenan, when the space velocity was 0.1 h^-1 at 30°C, 0.135 M l-phenylalanine was produced from 0.15 M phenylpyruvate (conversion yield, 90%). The half-life of the l-phenylalanine-forming activity of the column was estimated to be about 30 days at 30°C.     

Comparison of the production of intracellular l-phenylalanine dehydrogenase by Rhodococcus species M4 and Sporosarcina ureae at 50 liter scale

Summary The production of l-phenylalanine dehydrogenase by Rhodococcus spec. M4 (DSM 3041) and Sporosarcina urea (DSM 317) at 50 1 scale was compared. Also at 50 1 scale Rhodococcus spec. M4 (DSM 3041) turns out to be a superior producer: max. 3×10⁴ U/l. Sporosarcina ureae (DSM 317) produces l-phenylalanine dehydrogenase at lower but still very acceptable level: max. 3.7×10³ U/l and 26.4% of the production capacity of Rhodococcus spec. M4 (DSM 3041) based on dry cell matter.     

Substrate specificity of a recombinant ribose-5-phosphate isomerase from <Emphasis Type="Italic">Streptococcus pneumoniae</Emphasis> and its application in the production of <Emphasis Type="SmallCaps">l</Emphasis>-lyxose and <Emphasis Type="SmallCaps">l</Emphasis>-tagatose

A putative ribose-5-phosphate isomerase (RpiB) from Streptococcus pneumoniae was purified with a specific activity of 26.7 U mg⁻¹ by Hi-Trap Q HP anion exchange and Sephacryl S-300 HR 16/60 gel filtration chromatographies. The native enzyme existed as a 96-kDa tetramer with activity maxima at pH 7.5 and 35°C. The RpiB exhibited isomerization activity with l-lyxose, l-talose, d-gulose, d-ribose, l-mannose, d-allose, l-xylulose, l-tagatose, d-sorbose, d-ribulose, l-fructose, and d-psicose and exhibited particularly high activity with l-form monosaccharides such as l-lyxose, l-xylulose, l-talose, and l-tagatose. With l-xylulose (500 g l⁻¹) and l-talose (500 g l⁻¹) substrates, the optimum concentrations of RpiB were 300 and 600 U ml⁻¹, respectively. The enzyme converted 500 g l⁻¹ l-xylulose to 350 g l⁻¹ l-lyxose after 3 h, and yielded 450 g l⁻¹ l-tagatose from 500 g l⁻¹ l-talose after 5 h. These results suggest that RpiB from S. pneumoniae can be employed as a potential producer of l-form monosaccharides.     

Supramolecular-mediated immobilization of l-phenylalanine dehydrogenase on cyclodextrin-coated Au electrodes for biosensor applications

A supramolecular approach was used for adsorbing a monolayer of adamantane-modified phenylalanine dehydrogenase on β-cyclodextrin-coated Au electrodes. The enzyme electrode (poised at +200 mV vs. Ag/AgCl) showed a linear amperometric response up to 3 mM l-phenylalanine (l-Phe) with a lower detection limit of 15 μM. The reversible nature of this immobilization approach was confirmed.     

Kinetics of α-amylase production in a batch and fed-batch culture of Bacillus subtilis with caseinate as nitrogen source and starch as carbon source

Summary Analysis of a large number of experimental data from the cultivation of Bacillus subtilis formed the basis for a kinetic model of the process explaining the effect of composition of the culture medium and of the growth rate on the rate of enzyme production. The resulting rate of formation of -amylase (EC 3.2.1.1) reflects the sum of the rate of enzyme production and the rate of its degradation as affected by the environment. The kinetic dependence confirms the previously described mechanism of regulation of enzyme biosynthesis. The mathematical model of the process served here to determine the optimal conditions for enzyme biosynthesis which were then verified in a fed-batch cultivation. The production of the enzyme in fed-batch culture was found to be twice that found in a batch cultivation.Symbols X biomass concentration, g·l^-1 - t time, h - S ₁ caseinate concentration, g·l^-1 - S ₂ starch concentration, g·l^-1 - P product concentration, U·ml^-1 - r _P specific rate of product formation, U·g^-1·h^-1 - R _P total rate of product formation, U·l^-1·h^-1 - Y yield coefficient - specific growth rate, h^-1     

Production of sorbitol and gluconic acid by permeabilized cells of Zymomonas mobilis

Summary Zymomonas mobilis is able to convert glucose and fructose to gluconic acid and sorbitol. The enzyme, glucose-fructose oxidoreductase, catalysing the intermolecular oxidation-reduction of glucose and fructose to gluconolactone and sorbitol, was formed in high amounts [1.4 units (U)·mg^-1] when Z. mobilis was grown in chemostats with glucose as the only carbon source under non-carbon-limiting conditions. The activity of a gluconolactone-hydrolysing lactonase was constant at 0.2 U·mg^-1. Using glucose-grown cells for the conversion of equimolar fructose and glucose mixtures up to 60% (w/v), a maximum product concentration of only 240 g·1^-1 of sorbitol was found. The gluconic acid accumulated was further metabolized to ethanol. After permeabilizing the cells using cationic detergents, maximum sorbitol and gluconic acid concentrations of 295 g·1^-1 each were reached; no ethanol production occurred. In a continuous process with -carrageenan-immobilized and polyethylenimin-hardened, permeabilized cells no significant decrease in the conversion yield was observed after 75 days. The specific production rates for a high yield conversion ( > 98%) in a continuous two-stage process were 0.19 g·g^-1·h^-1 for sorbitol and 0.21 g·g^-1·h^-1 for gluconic acid, respectively. For the sugar conversion of cetyltrimethylammonium bromide-treated -carrageenan-immobilized cells a V _max of 1.7 g·g^-1·h^-1 for sorbitol production and a K _m of 77.2 g·1^-1 were determinedOffprint requests to: B. Rehr     

Enzymic arrangement and allosteric regulation of the aromatic amino acid pathway in Neisseria gonorrhoeae

The pathway construction and allosteric regulation of phenylalanine and tyrosine biosynthesis was examined in Neisseria gonorrhoeae. A single 3-deoxy-d-arabino-heptulosonate 7-phosphate (DAHP) synthase enzyme sensitive to feedback inhibition by l-phenylalanine was found. Chorismate mutase and prephenate dehydratase appear to co-exist as catalytic components of a bifunctional enzyme, known to be present in related genera. The latter enzyme activities were both feedback inhibited by l-phenylalanine. Prephenate dehydratase was strongly activated by l-tyrosine. NAD⁺-linked prephenate dehydrogenase and arogenate dehydrogenase activities coeluted following ion-exchange chromatography, suggesting their identity as catalytic properties of a single broad-specificity cyclohexadienyl dehydrogenase. Each dehydrogenase activity was inhibited by 4-hydroxyphenylpyruvate, but not by l-tyrosine. Two aromatic aminotransferases were resolved, one preferring the l-phenylalanine:2-ketoglutarate substrate combination and the other preferring the l-tyrosine: 2-ketoglutarate substrate combination. Each aminotransferase was also able to transaminate prephenate. The overall picture of regulation is one in which l-tyrosine modulates l-phenylalanine synthesis via activation of prephenate dehydratase. l-Phenylalanine in turn regulates early-pathway flow through inhibition of DAHP synthase. The recent phylogenetic positioning of N. gonorrhoeae makes it a key reference organism for emerging interpretations about aromatic-pathway evolution.     

Molecular breeding of a Brevibacterium lactofermentum l-phenylalanine producer using a cloned prephenate dehydratase gene

Summary The prephenate dehydratase gene was cloned from a mutant of Brevibacterium lactofermentum, AJ11957 that produced enzyme free from feedback inhibition. The recombinant plasmids pPH11 and pPH14 complemented a phenylalanine auxotroph of B. lactofermentum, A-15, provided the transformant with the desensitized enzyme and caused an increased level of the enzyme compared to that of a wild strain. Plasmid pPH14 was introduced into l-phenylalanine producers genetically induced from B. lactofermentum; MF358 and FP-1 excreting l-tyrosine and anthranilate, respectively, as by-products. Both transformants predominantly accumulated l-phenylalanine at the expense of by-product formation. Co-existence of pPH14 and pTAR16, a recombinant plasmid expressing desensitized 3-deoxy-d-arabino-hepturosonate-7-phosphate synthase had a marked effect on further improvement in l-phenylalanine productivity, accompanied by an increase in the corresponding enzyme activity. The parent, MF358, accumulating 5.5 g/l l-phenylalanine, 6.8 g/l l-tyrosine and 0.3 g/l anthranilate turned into a potent l-phenylalanine producer producing 18.2 g/l l-phenylalanine and 1.0 g/l l-tyrosine by-product. Offprint requests to: Hisao Ito     

Production of <Emphasis Type="SmallCaps">l</Emphasis>-phenylalanine from glycerol by a recombinant <Emphasis Type="Italic">Escherichia coli</Emphasis>

The production of l-phenylalanine is conventionally carried out by fermentations that use glucose or sucrose as the carbon source. This work reports on the use of glycerol as an inexpensive and abundant sole carbon source for producing l-phenylalanine using the genetically modified bacterium Escherichia coli BL21(DE3). Fermentations were carried out at 37°C, pH 7.4, using a defined medium in a stirred tank bioreactor at various intensities of impeller agitation speeds (300–500 rpm corresponding to 0.97–1.62 m s⁻¹ impeller tip speed) and aeration rates (2–8 L min⁻¹, or 1–4 vvm). This highly aerobic fermentation required a good supply of oxygen, but intense agitation (impeller tip speed ~1.62 m s⁻¹) reduced the biomass and l-phenylalanine productivity, possibly because of shear sensitivity of the recombinant bacterium. Production of l-phenylalanine was apparently strongly associated with growth. Under the best operating conditions (1.30 m s⁻¹ impeller tip speed, 4 vvm aeration rate), the yield of l-phenylalanine on glycerol was 0.58 g g⁻¹, or more than twice the best yield attainable on sucrose (0.25 g g⁻¹). In the best case, the peak concentration of l-phenylalanine was 5.6 g L⁻¹, or comparable to values attained in batch fermentations that use glucose or sucrose. The use of glycerol for the commercial production of l-phenylalanine with E. coli BL21(DE3) has the potential to substantially reduce the cost of production compared to sucrose- and glucose-based fermentations.     

Isolation,identification and characterisation of a soil bacterium producing an enzyme with l-phenylalanine oxidase activity

A gram-positive, mesophilic bacterium which assimilated l-phenylalanine but which failed to utilise l-tyrosine was isolated from soil. The isolate, identified as a strain of Bacillus carotarum, converted l-phenylalanine to phenylpyruvate with the initial step catalysed by an inducible, intracellular enzyme which possessed l-phenylalanine oxidase activity. Phenylalanine oxidase has not been previously reported in Gram-positive bacteria, although there are a few examples of non-specific l-amino acid oxidases with activity towards l-phenylalanine. The isolate grew abundantly on complex media but failed to synthesise significant amounts of the enzyme in the absence of l-phenylalanine. The highest enzyme levels were achieved in a chemically defined minimal salts medium containing the amino acid at 10 g/l as the primary carbon and energy source.     

The fermentation process for l-phenylalanine production using an auxotrophic regulatory mutant of Escherichia coli

Summary A process for l-phenylalanine production was studied using a tyrosine auxotrophic regulatory mutant of Escherichia coli, resistant to both -2-thienyl-dl-alanine and p-fluoro-dl-phenylalanine. Fermentations were carried out in a 30-1 fermentor with intermittent feeding of glucose plus phosphate. The mutant accumulated l-phenylalanine in the fermentation broth up to 15 g/l at pH 7.0 and 33°C. Column chromatography on a strong cation exchanger was employed as the most effective step in the purification of l-phenyl-alanine from the broth. This step brought about 4-fold concentration of the product with 96% recovery.     

Comparative study of the enzymatic synthesis of l-valine by purified enzymes,crude extract,intact or permeabilized cells from Bacillus megaterium

Summary A detailed study on the reductive amination of -ketoisovalerate to l-valine by l-valine dehydrogenase using glucose dehydrogenase as an NADH regeneration enzyme was performed. The presence of both enzyme activities in Bacillus megaterium ATCC 39 118 permitted a direct and systematic comparison of the performances (initial l-valine production rate, productivity, molar conversion yield) of different types of conversion systems: purified enzymes or crude extract and whole cells, intact or permeabilized. A maximal l-valine productivity of 8 mmol·l^–1 · h^–1 was obtained using purified enzymes which constituted the most efficient system with a maximal rate of 0.87 mol · ml^–1 · min^–1 and a molar conversion yield of 0.91. Permeabilized cells were also an attractive system because of their easy preparation and of the good performances attained.Offprint requests to: F. Monot     

Dielectric barrier discharge plasma as a novel approach for improving 1,3-propanediol production in <Emphasis Type="Italic">Klebsiella pneumoniae</Emphasis>

Dielectric barrier discharge plasma was used to generate a stable strain of Klebsiella pneumoniae (designated to as Kp-M2) with improved 1,3-propanediol production. The specific activities of glycerol dehydrogenase, glycerol dehydatase and 1,3-propanediol oxidoreductase in the crude cell extract increased from 0.11, 9.2 and 0.15 U mg⁻¹, respectively, for wild type to 0.67, 14.4 and 1.6 U mg⁻¹ for Kp-M2. The glycerol flux of Kp-M2 was redistributed with the flux to the reductive pathway being increased by 20% in batch fermentation. The final 1,3-propanediol concentrations achieved by Kp-M2 in batch and fed-batch fermentations were 19.9 and 76.7 g l⁻¹, respectively, which were higher than those of wild type (16.2 and 49.2 g l⁻¹). The results suggested that dielectric barrier discharge plasma could be used as an effective approach to improve 1,3-propanediol production in K. pneumoniae.