Direct production of cadaverine from soluble starch using <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis> coexpressing α-amylase and lysine decarboxylase

Here, we demonstrated the one-step production of cadaverine from starch using a Corynebacterium glutamicum strain coexpressing Streptococcus bovis 148 α-amylase (AmyA) and Escherichia coli K-12 lysine decarboxylase (CadA). We constructed the E. coli–C. glutamicum shuttle vector, which produces CadA under the control of the high constitutive expression (HCE) promoter, and transformed this vector into C. glutamicum CSS secreting AmyA. The engineered C. glutamicum expressed both CadA and AmyA, which retained their activity. We performed cadaverine fermentation using 50 g/l soluble starch as the sole carbon source without pyridoxal-5’-phosphate, which is the coenzyme for CadA. C. glutamicum coexpressing AmyA and CadA successfully produced cadaverine from soluble starch and the yield of cadaverine was 23.4 mM after 21 h. CadA expression levels under the control of the HCE promoter were assumed to be sufficient to convert l-lysine to cadaverine, as there was no accumulation of l-lysine in the culture medium during fermentation. Thus, we demonstrated that C. glutamicum has great potential to produce cadaverine from biomass resources.     

Production of <Emphasis Type="SmallCaps">l</Emphasis>-Lysine from starch by <Emphasis Type="BoldItalic">Corynebacterium glutamicum</Emphasis> displaying α-amylase on its cell surface

We engineered a Corynebacterium glutamicum strain displaying α-amylase from Streptococcus bovis 148 (AmyA) on its cell surface to produce amino acids directly from starch. We used PgsA from Bacillus subtilis as an anchor protein, and the N-terminus of α-amylase was fused to the PgsA. The genes of the fusion protein were integrated into the homoserine dehydrogenase gene locus on the chromosome by homologous recombination. l-Lysine fermentation was carried out using C. glutamicum displaying AmyA in the growth medium containing 50 g/l soluble starch as the sole carbon source. We performed l-lysine fermentation at various temperatures (30–40°C) and pHs (6.0–7.0), as the optimal temperatures and pHs of AmyA and C. glutamicum differ significantly. The highest l-lysine yield was recorded at 30°C and pH 7.0. The amount of soluble starch was reduced to 18.29 g/l, and 6.04 g/l l-lysine was produced in 24 h. The l-lysine yield obtained using soluble starch as the sole carbon source was higher than that using glucose as the sole carbon source after 24 h when the same amount of substrates was added. The results shown in the current study demonstrate that C. glutamicum displaying α-amylase has a potential to directly convert soluble starch to amino acids.     

Development of novel cell surface display in <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis> using porin

We have developed a novel cell surface display in Corynebacterium glutamicum using porin proteins as anchor proteins. Porins are localized at C. glutamicum mycolic acid layer and exist as a hexamer. We used α-amylase from Streptococcus bovis 148 (AmyA) as a model protein to be displayed on the C. glutamicum cell surface. AmyA was fused to the C terminus of the porins PorB, PorC, or PorH. Expression vectors using fused proteins under the control of the cspB promoter were constructed and introduced into the C. glutamicum Cm strain. Immunostaining microscopy and flow cytometric analysis revealed that PorB-AmyA, PorC-AmyA, and PorH-AmyA were displayed on the C. glutamicum cell surface. AmyA activity was only detected in the cell fraction of C. glutamicum cells that displayed AmyA fused to PorB, PorC or PorH and AmyA activity was not detected in the supernatants of C. glutamicum culture broths after 72 h cultivation. Thus, we have demonstrated that C. glutamicum porins are very efficient anchor proteins for protein display in C. glutamicum.     

Lysine degradation in Candida maltosa: occurrence of a novel enzyme,acetyl-CoA: L-lysine N-acetyltransferase

The yeast Candida maltosa can utilize L-lysine as sole nitrogen and sole carbon source accompanied by accumulation of -N-acetyl-L-lysine, indicating that lysine is metabolized by way of N-acetylated intermediates. A novel lysine acetyltransferase catalyzing the first step in this pathway, the N-acetylation of the -amino group of L-lysine, was found in this yeast. The enzyme, acetyl-CoA:L-lysine N-acetyltransferase, is strongly induced in cells grown on L-lysine as sole carbon source. The enzyme is specific for both L-lysine and acetyl-CoA. The K _m values are 10 mM for L-lysine and 0.33 mM for acetyl-CoA. The enzyme has a maximum activity at pH 8.1.Dedicated to Prof. Dr. F. Böttcher in occasion of his 60th birthday     

Effect of pyruvate dehydrogenase complex deficiency on <Emphasis Type="SmallCaps">l</Emphasis>-lysine production with <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis>

Intracellular precursor supply is a critical factor for amino acid productivity of Corynebacterium glutamicum. To test for the effect of improved pyruvate availability on l-lysine production, we deleted the aceE gene encoding the E1p enzyme of the pyruvate dehydrogenase complex (PDHC) in the l-lysine-producer C. glutamicum DM1729 and characterised the resulting strain DM1729-BB1 for growth and l-lysine production. Compared to the host strain, C. glutamicum DM1729-BB1 showed no PDHC activity, was acetate auxotrophic and, after complete consumption of the available carbon sources glucose and acetate, showed a more than 50% lower substrate-specific biomass yield (0.14 vs 0.33 mol C/mol C), an about fourfold higher biomass-specific l-lysine yield (5.27 vs 1.23 mmol/g cell dry weight) and a more than 40% higher substrate-specific l-lysine yield (0.13 vs 0.09 mol C/mol C). Overexpression of the pyruvate carboxylase or diaminopimelate dehydrogenase genes in C. glutamicum DM1729-BB1 resulted in a further increase in the biomass-specific l-lysine yield by 6 and 56%, respectively. In addition to l-lysine, significant amounts of pyruvate, l-alanine and l-valine were produced by C. glutamicum DM1729-BB1 and its derivatives, suggesting a surplus of precursor availability and a further potential to improve l-lysine production by engineering the l-lysine biosynthetic pathway. This study is dedicated to Prof. Dr. Hermann Sahm on the occasion of his 65th birthday.     

Production of a novel raw-starch-digesting glucoamylase by <Emphasis Type="Italic">Penicillium</Emphasis> sp. X-1 under solid state fermentation and its use in direct hydrolysis of raw starch

Penicillium sp. X−1, isolated from decayed raw corn, produced high level of raw-starch-digesting glucoamylase (RSDG) under solid state fermentation (SSF). Maximum enzyme yield of 306.2 U g⁻¹ dry mouldy bran (DMB) was obtained after 36 h of culture upon optimized production. The enzyme could hydrolyse both small and large granule starches but did not adsorb on raw starch. The enzyme exhibited maximum activity at 65°C and pH 6.5, which provided an opportunity of synergism with α-amylase. It significantly hydrolysed 15% (w/v) raw corn starch slurry in synergism with the commercial α-amylase and a degree of hydrolysis of 92.4% was obtained after 2 h of incubation.     

Metabolic Engineering of Corynebacterium glutamicum for Cadaverine Fermentation

Cadaverine, the expected raw material of polyamides, is produced by decarboxylation of L-lysine. If we could produce cadaverine from the cheapest sugar, and as a renewable resource, it would be an effective solution against global warming, but there has been no attempt to produce cadaverine from glucose by fermentation. We focused on Corynebacterium glutamicum, whose L-lysine fermentation ability is superior, and constructed a metabolically engineered C. glutamicum in which the L-homoserine dehydrogenase gene (hom) was replaced by the L-lysine decarboxylase gene (cadA) of Escherichia coli. In this recombinant strain, cadaverine was produced at a concentration of 2.6 g/l, equivalent to up to 9.1% (molecular yield) of the glucose transformed into cadaverine in neutralizing cultivation. This is the first report of cadaverine fermentation by C. glutamicum.     

Improvement in lactic acid production from starch using α-amylase-secreting <Emphasis Type="Italic">Lactococcus lactis</Emphasis> cells adapted to maltose or starch

To achieve direct and efficient lactic acid production from starch, a genetically modified Lactococcus lactis IL 1403 secreting α-amylase, which was obtained from Streptococcus bovis 148, was constructed. Using this strain, the fermentation of soluble starch was achieved, although its rate was far from efficient (0.09 g l⁻¹ h⁻¹ lactate). High-performance liquid chromatography revealed that maltose accumulated during fermentation, and this was thought to lead to inefficient fermentation. To accelerate maltose consumption, starch fermentation was examined using L. lactis cells adapted to maltose instead of glucose. This led to a decrease in the amount of maltose accumulation in the culture, and, as a result, a more rapid fermentation was accomplished (1.31 g l⁻¹ h⁻¹ lactate). Maximum volumetric lactate productivity was further increased (1.57 g l⁻¹ h⁻¹ lactate) using cells adapted to starch, and a high yield of lactate (0.89 g of lactate per gram of consumed sugar) of high optical purity (99.2% of l-lactate) was achieved. In this study, we propose a new approach to lactate production by α-amylase-secreting L. lactis that allows efficient fermentation from starch using cells adapted to maltose or starch before fermentation.     

Display of α-amylase on the surface of <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis> cells by using NCgl1221 as the anchoring protein,and production of glutamate from starch

We developed a new cell surface display system in Corynebacterium glutamicum based on the C-terminally truncated NCgl1221 anchor protein to increase l-glutamate production from starch directly. The C-terminally truncated NCgl1221 protein is a mutant NCgl1221 and leads to the constitutive export of l-glutamate. The N terminus of α-amylase (AmyA) was fused to truncated NCgl1221, and the resulting fusion protein was expressed on the cell surface by IPTG induction. Localization of the fusion protein was confirmed by immunofluorescence microscopy and flow cytometric analysis. The results of l-glutamate fermentation showed that the soluble starch was utilized to grow and produce l-glutamate by the recombinant strain displaying AmyA. The amount of soluble starch was reduced from 30.0 ± 2.8 to 4.5 ± 0.7 g/l under non-inducing condition and from 50.0 ± 2.4 to 12.5 ± 1.1 g/l under biotin limitation in 36 h. The glutamate concentration in the medium was transiently increased in 14 h under no induction, while under biotin-limiting condition, glutamate production was continuously elevated during fermentation. The amount of glutamate reached 19.3 ± 2.1 g/l after 26 h of fermentation with biotin limitation, which was greater than that produced by the strain using PgsA, one of the poly-γ-glutamate synthetase complexes, as the anchor protein under the same condition. Therefore, the truncated NCgl1221 anchor protein has more advantages than the PgsA anchor protein in glutamate fermentation because truncated NCgl1221 leads to the constitutive export of l-glutamate without any treatments.     

Characterization of acetyl-CoA: l-lysine N6-acetyltransferase,which catalyses the first step of carbon catabolism from lysine in Saccharomyces cerevisiae

The carbon catabolism of l-lysine starts in Saccharomyces cerevisiae with acetylation by an acetyl-CoA: l-lysine N⁶-acetyltransferase. The enzyme is strongly induced in cells grown on l-lysine as sole carbon source and has been purified about 530-fold. Its activity was specific for acetyl-CoA and, in addition to l-lysine, 5-hydroxylysine and thialysine act as acetyl acceptor. The following apparent Michaelis constants were determined: acetyl-CoA 0.8 mM, l-lysine 5.8 mM, dl-5-hydroxylysine 2.8 mM, l-thialysine 100 mM. The enzyme had a maximum activity at pH 8.5 and 37°C. Its molecular mass, estimated by sodium dodecyl sulphate-polyacrylamide gel electrophoresis, was 52 kDa. Since the native molecular mass, determined by gel filtration, was 48 kDa, the enzyme is a monomer.     

Expression of the <Emphasis Type="BoldItalic">Escherichia coli pntAB</Emphasis> genes encoding a membrane-bound transhydrogenase in <Emphasis Type="BoldItalic">Corynebacterium glutamicum</Emphasis> improves <Emphasis Type="SmallCaps">l</Emphasis>-lysine formation

A critical factor in the biotechnological production of l-lysine with Corynebacterium glutamicum is the sufficient supply of NADPH. The membrane-integral nicotinamide nucleotide transhydrogenase PntAB of Escherichia coli can use the electrochemical proton gradient across the cytoplasmic membrane to drive the reduction of NADP⁺ via the oxidation of NADH. As C. glutamicum does not possess such an enzyme, we expressed the E. coli pntAB genes in the genetically defined C. glutamicum lysine-producing strain DM1730, resulting in membrane-associated transhydrogenase activity of 0.7 U/mg protein. When cultivated in minimal medium with 10% (w/v) carbon source, the presence of transhydrogenase slightly reduced glucose consumption, whereas the consumption of fructose, glucose plus fructose, and, in particular, sucrose was stimulated. Biomass was increased by pntAB expression between 10 and 30% on all carbon sources tested. Most importantly, the lysine concentration was increased in the presence of transhydrogenase by ∼10% on glucose, ∼70% on fructose, ∼50% on glucose plus fructose, and even by ∼300% on sucrose. Thus, the presence of a proton-coupled transhydrogenase was shown to be an efficient way to improve lysine production by C. glutamicum. In contrast, pntAB expression had a negative effect on growth and glutamate production of C. glutamicum wild type.     

Anaerobic fermentation of gelatinized sago starch-derived sugars to acetone—1-butanol—Ethanol solvent byClostridium acetobutylicum

A study of the kinetics and performance of solvent-yielding batch fermentation of individual sugars and their mixture derived from enzymic hydrolysis of sago starch byClostridium acetobutylicum showed that the use of 30 g/L gelatinized sago starch as the sole carbon source produced 11.2 g/L total solvent,i.e. 1.5–2 times more than with pure maltose or glucose used as carbon sources. Enzymic pretreatment of gelatinized sago starch yielding maltose and glucose hydrolyzates prior to the fermentation did not improve solvent production as compared to direct fermentation of gelatinized sago starch. The solvent yield of direct gelatinized sago starch fermentation depended on the activity and stability of amylolytic enzymes produced during the fermentation. The pH optima for α-amylase and glucoamylase were found to be at 5.3 and 4.0–4.4, respectively. α-Amylase showed a broad pH stability profile, retaining more than 80% of its maximum activity at pH 3.0–8.0 after a 1-d incubation at 37°C. SinceC. acetobutylicum α-amylase has a high activity and stability at low pH, this strain can potentially be employed in a one-step direct solvent-yielding fermentation of sago starch. However, theC. acetobutylicum glucoamylase was only stable at pH 4–5, maintaining more than 90% of its maximum activity after a 1-d incubation at 37°C.     

Development of strains of the thermotolerant yeast Hansenula polymorpha capable of alcoholic fermentation of starch and xylan

The thermotolerant yeast Hansenula polymorpha ferments glucose and xylose to ethanol at high temperatures. However, H. polymorpha cannot utilize starchy materials or xylans. Heterologous amylolytic and xylanolytic enzymes have to be expressed in this yeast to provide for utilization and growth on starch and xylan. Genes SWA2 and GAM1 from the yeast Schwanniomyces occidentalis, encoding α-amylase and glucoamylase, respectively, were expressed in H. polymorpha. The expression was achieved by integration of the SWA2 and GAM1 genes under the strong constitutive promoter of the H. polymorpha glyceraldehyde-3-phosphate dehydrogenase gene (HpGAP) into H. polymorpha genome. Resulting transformants acquired the ability to grow on a minimal medium containing soluble starch as a sole carbon source. Ethanol production at high-temperature fermentation from starch by the recombinant strains was up to 10 g/L. The XYN2 gene encoding endoxylanase of the fungus Trichoderma reseei was expressed in H. polymorpha. Co-expression of xlnD gene coding for β-xylosidase of the fungus Aspergillus niger and the XYN2 gene in H. polymorpha was achieved by integration of these genes under control of the HpGAP promoter. Resulting transformants were capable of growth and alcoholic fermentation on a minimal medium supplemented with birchwood xylan as a sole carbon source at 48 °C.     

Engineering of an <Emphasis Type="SmallCaps">l</Emphasis>-arabinose metabolic pathway in <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis>

Corynebacterium glutamicum was metabolically engineered to broaden its substrate utilization range to include the pentose sugar l-arabinose, a product of the degradation of lignocellulosic biomass. The resultant CRA1 recombinant strain expressed the Escherichia coli genes araA, araB, and araD encoding l-arabinose isomerase, l-ribulokinase, and l-ribulose-5-phosphate 4-epimerase, respectively, under the control of a constitutive promoter. Unlike the wild-type strain, CRA1 was able to grow on mineral salts medium containing l-arabinose as the sole carbon and energy source. The three cloned genes were expressed to the same levels whether cells were cultured in the presence of d-glucose or l-arabinose. Under oxygen deprivation and with l-arabinose as the sole carbon and energy source, strain CRA1 carbon flow was redirected to produce up to 40, 37, and 11%, respectively, of the theoretical yields of succinic, lactic, and acetic acids. Using a sugar mixture containing 5% d-glucose and 1% l-arabinose under oxygen deprivation, CRA1 cells metabolized l-arabinose at a constant rate, resulting in combined organic acids yield based on the amount of sugar mixture consumed after d-glucose depletion (83%) that was comparable to that before d-glucose depletion (89%). Strain CRA1 is, therefore, able to utilize l-arabinose as a substrate for organic acid production even in the presence of d-glucose.     

Cloning of α-amylase gene from Schwanniomyces occidentalis and expression in Saccharomyces cerevisiae

The cloning of α-amylase gene ofS. occidentalis and the construction of starch digestible strain of yeast,S. cerevisiae AS. 2. 1364 with ethanol-tolerance and without auxotrophic markers used in fermentation industry were studied. The yeast/E.coli shuttle plasmid YCEp1 partial library ofS. occidentalis DNA was constructed and α-amylase gene was screened in S.cerevisiae by amylolytic activity. Several transformants with amylolysis were obtained and one of the fusion plasmids had an about 5.0 kb inserted DNA fragment, containing the upstream and downstream sequences of α-amylase gene fromS. occidentalis. It was further confirmed by PCR and sequence determination that this 5.0 kb DNA fragment contains the whole coding sequence of α-amylase. The amylolytic test showed that when this transformant was incubated on plate of YPDS medium containing 1 % glum and 1 % starch at 30°C for 48 h starch degradation zones could be visualized by staining with iodine vapour. α-amylase activity of the culture filtratate is 740–780 mU/mL and PAGE shows that the yeast harboring fusion plasmids efficiently secreted α-amylase into the medium, and the amount of the recombinant α-amylase is more than 12% of the total proteins in the culture filtrate. These results showed that α-amylase gene can be highly expressed and efficiently secreted inS. cerevisiae AS. 2.1364, and the promotor and the terminator of α-amylase gene fromS. occidentalis work well inS. cercvisiac AS. 2.1364.     

Production of the raw-starch digesting amylase of Aspergillus sp. K-27

Summary Aspergillus sp. K-27, isolated from soil, produced extracellular glucoamylase and -amylase using wheat starch as a carbon source, and its productivity was doubled by the addition of -methyl-d-glucoside to the medium. The crude enzyme preparation, which was found to be a mixture of 70% glucoamylase and 30% -amylase, well degraded not only cereal starches but also tuber and root starches, and the initial velocity for potato starch was 72% of that for corn starch.     

Some physiological functions of the L-leucine dehydrogenase in Bacillus subtilis

Mutants of Bacillus subtilis constitutive for L-leucine dehydrogenase synthesis were selected. Using these mutants we could determine two functional roles for the L-leucine dehydrogenase. This enzyme liberates ammonium ions from branched chain amino acids when supplied as the sole nitrogen source. Another function is to synthesize from L-isoleucine, L-leucine, and L-valine the branched chain -keto acids which are precursors of branched chain fatty acid biosynthesis. These results together with the inducibility of the enzyme suggest that the L-leucine dehydrogenase has primarily a catabolic rather than an anabolic function in the metabolism of Bacillus subtilis.     

Direct fermentation of gelatinized sago starch to acetone–butanol–ethanol by Clostridium acetobutylicum

Direct fermentation of gelatinized sago starch into solvent (acetone–butanol–ethanol) by Clostridium acetobutylicum P262 was studied using a 250 ml Schott bottle anaerobic fermentation system. Total solvent production from fermentation using 30 g sago starch/l (11.03g/l) was comparable to fermentation using corn starch and about 2-fold higher than fermentation using potato or tapioca starch. At the range of sago starch concentration investigated (10–80 g/l), the highest total solvent production (18.82 g/l) was obtained at 50 g/l. The use of a mixture of organic and inorganic nitrogen source (yeast extract + NH₄NO₃) enhanced growth of C. acetobutylicum, starch hydrolysis and solvent production (24.47 g/l) compared to the use of yeast extract alone. This gave the yield based on sugar consumed of 0.45 g/g. Result from this study also showed that the individual concentrations of nitrogen and carbon influenced solvent production to a greater extent than did carbon to nitrogen (C/N) ratio.     

13C NMR studies of the fluxes in the central metabolism of Corynebacterium glutamicum during growth and overproduction of amino acids in batch cultures

The carbon flux distribution in the central metabolism of Corynebacterium glutamicum was studied in batch cultures using [1-¹³C]- and [6-¹³C]glucose as substrate during exponential growth as well as during overproduction of l-lysine and l-glutamate. Using the ¹³C NMR data in conjunction with stoichiometric metabolite balances, molar fluxes were quantified and normalised to the glucose uptake rate, which was set to 100. The normalised molar flux via the hexose monophosphate pathway was 40 during exponential growth, whereas it was only 17 during l-glutamate production. During l-lysine production, the normalised hexose monophosphate pathway flux was elevated to 47. Thus, the carbon flux via this pathway correlated with the NADPH demand for bacterial growth and l-lysine overproduction. The normalised molar flux in the tricarboxylic acid cycle at the level of 2-oxoglutarate dehydrogenase was 100 during exponential growth and 103 during l-lysine secretion. During l-glutamate formation, the normalised flux through the tricarboxylic acid cycle was reduced to 60. In contrast to earlier NMR studies with C. glutamicum, no significant activity of the glyoxylate pathway could be detected. All experiments indicated a strong in vivo flux from oxaloacetate back to phosphoenolpyruvate and/or pyruvate, which might be due to phosphoenolpyruvate carboxykinase activity in C. glutamicum.     

Raw starch fermentation to ethanol by an industrial distiller’s yeast strain of <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> expressing glucoamylase and α-amylase genes

Industrial strains of a polyploid, distiller’s Saccharomyces cerevisiae that produces glucoamylase and α-amylase was used for the direct fermentation of raw starch to ethanol. Strains contained either Aspergillus awamori glucoamylase gene (GA1), Debaryomyces occidentalis glucoamylase gene (GAM1) or D. occidentalis α-amylase gene (AMY), singly or in combination, integrated into their chromosomes. The strain expressing both GA1 and AMY generated 10.3% (v/v) ethanol (80.9 g l⁻¹) from 20% (w/v) raw corn starch after 6 days of fermentation, and decreased the raw starch content to 21% of the initial concentration.