A Bacillus megaterium Plasmid System for the Production, Export, and One-Step Purification of Affinity-Tagged Heterologous Levansucrase from Growth Medium

A multiple vector system for the production and export of recombinant affinity-tagged proteins in Bacillus megaterium was developed. Up to 1 mg/liter of a His₆-tagged or Strep-tagged Lactobacillus reuteri levansucrase was directed into the growth medium, using the B. megaterium esterase LipA signal peptide, and recovered by one-step affinity chromatography.     

A Bacillus megaterium plasmid system for the production, export, and one-step purification of affinity-tagged heterologous levansucrase from growth medium

A multiple vector system for the production and export of recombinant affinity-tagged proteins in Bacillus megaterium was developed. Up to 1 mg/liter of a His6-tagged or Strep-tagged Lactobacillus reuteri levansucrase was directed into the growth medium, using the B. megaterium esterase LipA signal peptide, and recovered by one-step affinity chromatography.     

Molecular chaperones facilitate the soluble expression of <Emphasis Type="Italic">N</Emphasis>-acyl-<Emphasis Type="SmallCaps">d</Emphasis>-amino acid amidohydrolases in <Emphasis Type="Italic">Escherichia coli</Emphasis>

The overproduction of d-aminoacylase (d-ANase, 233.8 U/mg), N-acyl-d-glutamate amidohydrolase (d-AGase, 38.1 U/mg) or N-acyl-d-aspartate amidohydrolase (d-AAase, 6.2 U/mg) in Escherichia coli is accompanied by aggregation of the overproduced protein. To facilitate the expression of active enzymes, the molecular chaperones GroEL-GroES (GroELS), DnaK-DnaJ-GrpE (DnaKJE), trigger factor (TF), GroELS and DnaKJE or GroELS and TF were coexpressed with the enzymes. d-ANase (313.3 U/mg) and d-AGase (95.8 U/mg) were overproduced in an active form at levels 1.3- and 1.8-fold higher, respectively, upon co-expression of GroELS and TF. An E. coli strain expressing the d-AAase gene simultaneously with the TF gene exhibited a 4.3-fold enhancement in d-AAase activity (32.0 U/mg) compared with control E. coli expressing the d-AAase gene alone.     

Production of <Emphasis Type="SmallCaps">d</Emphasis>-arabitol by a newly isolated <Emphasis Type="Italic">Zygosaccharomyces rouxii</Emphasis>

A newly isolated Zygosaccharomyces rouxii NRRL 27,624 produced d-arabitol as the main metabolic product from glucose. In addition, it also produced ethanol and glycerol. The optimal conditions were temperature 30°C, pH 5.0, 350 rpm, and 5% inoculum. The yeast produced 83.4 ± 1.1 g d-arabitol from 175 ± 1.1 g glucose per liter at pH 5.0, 30°C, and 350 rpm in 240 h with a yield of 0.48 g/g glucose. It also produced d-arabitol from fructose, galactose, and mannose. The yeast produced d-arabitol and xylitol from xylose and also from a mixture of xylose and xylulose. Resting yeast cells produced 63.6 ± 1.9 g d-arabitol from 175 ± 1.8 g glucose per liter in 210 h at pH 5.0, 30°C and 350 rpm with a yield of 0.36 g/g glucose. The yeast has potential to be used for production of xylitol from glucose via d-arabitol route. Mention of trade names or commercial products in this article is solely for the purpose of providing specific information and does not imply recommendation or endorsement by the U.S. department of Agriculture.     

Heterologous expression,purification, and characterization of xylose reductase from <Emphasis Type="Italic">Candida shehatae</Emphasis>

The xylose reductase (XR) gene (xyl1) from Candida shehatae was cloned and expressed in Escherichia coli, and purified as a His₆-tagged fusion protein. The recombinant XR had K_m values for NADH than NADPH of 150 μM and 20 μM, respectively. The optimal reaction was at pH 6.5 and 35°C. The enzyme was specific for d-xylese.     

Production of <Emphasis Type="SmallCaps">l</Emphasis>-alanine by metabolically engineered <Emphasis Type="Italic">Escherichia coli</Emphasis>

Escherichia coli W was genetically engineered to produce l-alanine as the primary fermentation product from sugars by replacing the native d-lactate dehydrogenase of E. coli SZ194 with alanine dehydrogenase from Geobacillus stearothermophilus. As a result, the heterologous alanine dehydrogenase gene was integrated under the regulation of the native d-lactate dehydrogenase (ldhA) promoter. This homologous promoter is growth-regulated and provides high levels of expression during anaerobic fermentation. Strain XZ111 accumulated alanine as the primary product during glucose fermentation. The methylglyoxal synthase gene (mgsA) was deleted to eliminate low levels of lactate and improve growth, and the catabolic alanine racemase gene (dadX) was deleted to minimize conversion of l-alanine to d-alanine. In these strains, reduced nicotinamide adenine dinucleotide oxidation during alanine biosynthesis is obligately linked to adenosine triphosphate production and cell growth. This linkage provided a basis for metabolic evolution where selection for improvements in growth coselected for increased glycolytic flux and alanine production. The resulting strain, XZ132, produced 1,279 mmol alanine from 120 g l⁻¹ glucose within 48 h during batch fermentation in the mineral salts medium. The alanine yield was 95% on a weight basis (g g⁻¹ glucose) with a chiral purity greater than 99.5% l-alanine. Electronic supplementary material The online version of this article (doi:) contains supplementary material, which is available to authorized users.     

Secretory Expression of Nattokinase from <Emphasis Type="Italic">Bacillus subtilis</Emphasis> YF38 in <Emphasis Type="Italic">Escherichia coli</Emphasis>

Nattokinase producing bacterium, B. subtilis YF38, was isolated from douchi, using the fibrin plate method. The gene encoding this enzyme was cloned by polymerase chain reaction (PCR). Cytoplasmic expression of this enzyme in E. coli resulted in inactive inclusion bodies. But with the help of two different signal peptides, the native signal peptide of nattokinase and the signal peptide of PelB, active nattokinase was successfully expressed in E. coli with periplasmic secretion, and the nattokinase in culture medium displayed high fibrinolytic activity. The fibrinolytic activity of the expressed enzyme in the culture was determined to reach 260 urokinase units per micro-liter when the recombinant strain was induced by 0.7 mmol l⁻¹ isopropyl-β-D- thiogalactopyranoside (IPTG) at 20°C for 20 h, resulting 49.3 mg active enzyme per liter culture. The characteristic of this recombinant nattokinase is comparable to the native nattokinase from B. subtilis YF38. Secretory expression of nattokinase in E. coli would facilitate the development of this enzyme into a therapeutic product for the control and prevention of thrombosis diseases.     

Stabilization of native and double <Emphasis Type="SmallCaps">d</Emphasis>-amino acid oxidases from <Emphasis Type="Italic">Rhodosporidium toruloides</Emphasis> and <Emphasis Type="Italic">Trigonopsis variabilis</Emphasis> by immobilization on streptavidin-coated magnetic beads

Double d-amino acid oxidases (dRtDAO and dTvDAO) were previously genetically constructed by linking the C-terminus of one subunit of their corresponding native DAOs from Rhodosporidium toruloides and Trigonopsis variabilis (RtDAO and TvDAO) to the N-terminus of the other identical subunit. We have now immobilized these double DAOs and their native counterparts onto streptavidin-coated magnetic beads through the interaction between biotin and streptavidin. The catalytic efficiencies (k_cat/K_M) of immobilized DAOs toward d-alanine and cepharosporin C remained similar to those of their soluble forms, except the catalytic efficiency of immobilized TvDAO toward d-alanine was decreased by 56%. After immobilization, the T_m value for RtDAO was shifted 15°C higher to 60°C, while those for dRtDAO, TvDAO and dTvDAO were increased by 5–8°C to 56, 60 and 60°C, respectively. In the presence of 10 mM H₂O₂, immobilized RtDAO, dRtDAO, TvDAO and dTvDAO exhibited half-lives of about 8, 10, 3 and 5 h, respectively, giving 16-, 10-, 6- and 7-fold greater stability than their soluble forms, respectively. Therefore, immobilization through biotin–streptavidin affinity binding enhances the thermal and oxidative stability of native and double DAOs studied, especially RtDAO. The additive stabilizing effect of subunit fusion and immobilization was more pronounced in the case of RtDAO than TvDAO.     

Membrane-bound <Emphasis Type="SmallCaps">l</Emphasis>- and <Emphasis Type="SmallCaps">d</Emphasis>-lactate dehydrogenase activities of a newly isolated <Emphasis Type="Italic">Pseudomonas stutzeri</Emphasis> strain

Pseudomonas stutzeri SDM was newly isolated from soil, and two stereospecific NAD-independent lactate dehydrogenase (iLDH) activities were detected in membrane of the cells cultured in a medium containing dl-lactate as the sole carbon source. Neither enzyme activities was constitutive, but both of them might be induced by either enantiomer of lactate. P. stutzeri SDM preferred to utilize lactate to growth, when both l-lactate and glucose were available, and the consumption of glucose was observed only after lactate had been exhausted. The Michaelis–Menten constant for l-lactate was higher than that for d-lactate. The l-iLDH activity was more stable at 55°C, while the d-iLDH activity was lost. Both enzymes exhibited different solubilization with different detergents and different oxidation rates with different electron acceptors. Combining activity staining and previous proteomic analysis, the results suggest that there are two separate enzymes in P. stutzeri SDM, which play an important role in converting lactate to pyruvate. Ma and Gao contributed equally to this work.     

Purification and characterization of <Emphasis Type="SmallCaps">l</Emphasis>-arabinose isomerase from <Emphasis Type="Italic">Lactobacillus plantarum</Emphasis> producing <Emphasis Type="SmallCaps">d</Emphasis>-tagatose

l-arabinose isomerase (EC5.3.1.4. AI) mediates the isomerization of d-galactose into d-tagatose as well as the conversion of l-arabinose into l-ribulose. The AI from Lactobacillus plantarum SK-2 was purified to an apparent homogeneity giving a single band on SDS–PAGE with a molecular mass of 59.6 kDa. Optimum activity was observed at 50°C and pH 7.0. The enzyme was stable at 50°C for 2 h and held between pH 4.5 and 8.5 for 1 h. AI activity was stimulated by Mn²⁺, Fe³⁺, Fe²⁺, Ca²⁺ and inhibited by Cu²⁺, Ag⁺, Hg²⁺, Pb²⁺. d-galactose and l-arabinose as substrates were isomerized with high activity. l-arabitol was the strongest competitive inhibitor of AI. The apparent Michaelis–Menten constant (K _m), for galactose, was 119 mM. The first ten N-terminal amino acids of the enzyme were determined as MLSVPDYEFW, which is identical to L. plantarum (Q88S84). Using the purified AI, 390 mg tagatose could be converted from 1,000 mg galactose in 96 h, and this production corresponds to a 39% equilibrium.     

<Emphasis Type="SmallCaps">d</Emphasis>-Psicose production from <Emphasis Type="SmallCaps">d</Emphasis>-fructose using an isolated strain, <Emphasis Type="Italic">Sinorhizobium</Emphasis> sp.

Sinorhizobium sp., which can convert d-fructose into d-psicose, was isolated from soil. The optimal pH, temperature, and cell concentration for d-psicose production with the isolated strain were 8.5, 40°C, and 60 mg/ml, respectively. The toluene-treated cells showed 2.5- and 4.8-fold increases in the d-psicose concentration and productivity compared with untreated washed cells. Under the optimal conditions, the toluene-treated cells produced 37 g d-psicose/l from 70% (w/v) (3.9 M) d-fructose after 15 h.     

Cloning,sequencing, overexpression and characterization of <Emphasis Type="SmallCaps">l</Emphasis>-rhamnose isomerase from <Emphasis Type="Italic">Bacillus pallidus</Emphasis> Y25 for rare sugar production

The l-rhamnose isomerase gene (L -rhi) encoding for l-rhamnose isomerase (l-RhI) from Bacillus pallidus Y25, a facultative thermophilic bacterium, was cloned and overexpressed in Escherichia coli with a cooperation of the 6×His sequence at a C-terminal of the protein. The open reading frame of L -rhi consisted of 1,236 nucleotides encoding 412 amino acid residues with a calculated molecular mass of 47,636 Da, showing a good agreement with the native enzyme. Mass-produced l-RhI was achieved in a large quantity (470 mg/l broth) as a soluble protein. The recombinant enzyme was purified to homogeneity by a single step purification using a Ni-NTA affinity column chromatography. The purified recombinant l-RhI exhibited maximum activity at 65°C (pH 7.0) under assay conditions, while 90% of the initial enzyme activity could be retained after incubation at 60°C for 60 min. The apparent affinity (K _m) and catalytic efficiency (k _cat/K _m) for l-rhamnose (at 65°C) were 4.89 mM and 8.36 × 10⁵ M⁻¹ min⁻¹, respectively. The enzyme demonstrated relatively low levels of amino acid sequence similarity (42 and 12%), higher thermostability, and different substrate specificity to those of E. coli and Pseudomonas stutzeri, respectively. The enzyme has a good catalyzing activity at 50°C, for d-allose, l-mannose, d-ribulose, and l-talose from d-psicose, l-fructose, d-ribose and l-tagatose with a conversion yield of 35, 25, 16 and 10%, respectively, without a contamination of by-products. These findings indicated that the recombinant l-RhI from B. pallidus is appropriate for use as a new source of rare sugar producing enzyme on a mass scale production.     

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.     

Isolation of a Novel <Emphasis Type="Italic">N</Emphasis>-acetyl-<Emphasis Type="SmallCaps">d</Emphasis>-lactosamine Specific Lectin from <Emphasis Type="Italic">Alocasia cucullata</Emphasis> (Schott.)

An N-acetyl-d-lactosamine (LacNAc) specific lectin from tubers of Alocasia cucullata was purified by affinity chromatography on asialofetuin-linked amino activated silica. The pure lectin showed a single band in SDS-PAGE at pH 8.8 and was a homotetramer with a subunit molecular mass of 13.5 kDa and native molecular mass of 53 kDa. It was heat stable up to 55 °C for 15 min and showed optimum hemagglutination activity from pH 2 to 11. The lectin was affected by denaturing agents such as urea (2 m), thiourea (2 m) and guanidine–HCl (0.5 m) and did not require Ca²⁺ and Mn²⁺ for its activity. It was a potent mitogen at 10 μg/ml towards human peripheral blood mononuclear cells with 50% growth inhibitory potential towards SiHa (human cervix ) cancer cell line at 100 μg/ml.     

Production of <Emphasis Type="SmallCaps">d</Emphasis>-lactic acid by <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis> under oxygen deprivation

In mineral salts medium under oxygen deprivation, Corynebacterium glutamicum exhibits high productivity of l-lactic acid accompanied with succinic and acetic acids. In taking advantage of this elevated productivity, C. glutamicum was genetically modified to produce d-lactic acid. The modification involved expression of fermentative d-lactate dehydrogenase (d-LDH)-encoding genes from Escherichia coli and Lactobacillus delbrueckii in l-lactate dehydrogenase (l-LDH)-encoding ldhA-null C. glutamicum mutants to yield strains C. glutamicum ΔldhA/pCRB201 and C. glutamicum ΔldhA/pCRB204, respectively. The productivity of C. glutamicum ΔldhA/pCRB204 was fivefold higher than that of C. glutamicum ΔldhA/pCRB201. By using C. glutamicum ΔldhA/pCRB204 cells packed to a high density in mineral salts medium, up to 1,336 mM (120 g l⁻¹) of d-lactic acid of greater than 99.9% optical purity was produced within 30 h.     

Heterologous expression of the <Emphasis Type="Italic">msp2 gene</Emphasis> from <Emphasis Type="Italic">Marasmius scorodonius</Emphasis>

For the heterologous expression of the msp2 gene from the edible mushroom Marasmius scorodonius in Escherichia coli the cDNA encoding the extracellular Msp2 peroxidase was cloned into the pBAD III expression plasmid. Expression of the protein with or without signal peptide was investigated in E. coli strains TOP10 and LMG194. Different PCR products were amplified for expression of the native target protein or a protein with a signal peptide. Omitting the native stop codon and adding six His-residues resulted in a fusion protein amenable to immune detection and purification by immobilised metal affinity chromatography. In E. coli the recombinant protein was produced in high yield as insoluble inclusion bodies. The influence of different parameters on MsP2 refolding was investigated. Active enzyme was obtained by glutathione-mediated oxidation in a medium containing urea, Ca²⁺, and hemin.     

Overproduction and characterization of a recombinant <Emphasis Type="SmallCaps">D</Emphasis>-amino acid oxidase from <Emphasis Type="Italic">Arthrobacter protophormiae</Emphasis>

A screening of soil samples for d-amino acid oxidase (d-AAO) activity led to the isolation and identification of the gram-positive bacterium Arthrobacter protophormiae. After purification of the wild-type d-AAO, the gene sequence was determined and designated dao. An alignment of the deduced primary structure with eukaryotic d-AAOs and d-aspartate oxidases showed that the d-AAO from A. protophormiae contains five of six conserved regions; the C-terminal type 1 peroxisomal targeting signal that is typical for d-AAOs from eukaryotic origin is missing. The dao gene was cloned and expressed in Escherichia coli. The purified recombinant d-AAO had a specific activity of 180 U mg protein⁻¹ for d-methionine and was slightly inhibited in the presence of l-methionine. Mainly, basic and hydrophobic d-amino acids were oxidized by the strictly enantioselective enzyme. After a high cell density fermentation, 2.29 × 10⁶ U of d-AAO were obtained from 15 l of fermentation broth.     

Identification and characterization of the bacterial <Emphasis Type="SmallCaps">d</Emphasis>-gluconate dehydratase in <Emphasis Type="Italic">Achromobacter xylosoxidans</Emphasis>

Achromobacter xylosoxidans is known to utilize d-glucose via the modified Entner-Doudoroff pathway. Although d-gluconate dehydratase produced from this bacterium was purified and partially characterized previously, a gene that encodes this enzyme has not yet been identified. To obtain protein information on bacterial d-gluconate dehydratase, we partially purified d-gluconate dehydratase in A. xylosoxidans and investigated its biochemical properties. Two degenerate primers were designed based on the N-terminal amino acid sequence of the partially purified d-gluconate dehydratase. Through PCR performed using degenerate primers, a 1,782-bp DNA sequence encoding the A. xylosoxidans d-gluconate dehydratase (gnaD) was obtained. The deduced amino acid sequence of A. xylosoxidans gnaD showed strong similarity with that of proteins belonging to the dihydroxy-acid dehydratase/phosphogluconate dehydratase family (COG0129). This is in contrast to the archaeal d-gluconate dehydratase, which belongs to the enolase superfamily (COG4948). The phylogenetic tree showed that A. xylosoxidans d-gluconate dehydratase is closer to the 6-phosphogluconate dehydratase than the dihydroxy-acid dehydratase. Interestingly, a clade containing A. xylosoxidans enzyme was clustered with proteins annotated as a second and a third dihydroxy-acid dehydratase in the genomes of Clostridium acetobutylicum (Cac_ilvD2) and Streptomyces ceolicolor (Sco_ilvD2, Sco_ilvD3), indicating that the function of these enzymes is the dehydration of d-gluconate.     

Characterization of ribose-5-phosphate isomerase of <Emphasis Type="Italic">Clostridium thermocellum</Emphasis> producing <Emphasis Type="SmallCaps">d</Emphasis>-allose from <Emphasis Type="SmallCaps">d</Emphasis>-psicose

The rpiB gene, encoding ribose-5-phosphate isomerase (RpiB) from Clostridium thermocellum, was cloned and expressed in Escherichia coli. RpiB converted d-psicose into d-allose but it did not convert d-xylose, l-rhamnose, d-altrose or d-galactose. The production of d-allose by RpiB was maximal at pH 7.5 and 65°C for 30 min. The half-lives of the enzyme at 50°C and 65°C were 96 h and 4.7 h, respectively. Under stable conditions of pH 7.5 and 50°C, 165 g d-allose l⁻¹ was produced without by-products from 500 g d-psicose l⁻¹ after 6 h.     

Continuous <Emphasis Type="SmallCaps">d</Emphasis>-lactic acid production by a novelthermotolerant <Emphasis Type="Italic">Lactobacillus delbrueckii</Emphasis> subsp. <Emphasis Type="Italic">lactis</Emphasis> QU 41

We isolated and characterized a d-lactic acid-producing lactic acid bacterium (d-LAB), identified as Lactobacillus delbrueckii subsp. lactis QU 41. When compared to Lactobacillus coryniformis subsp. torquens JCM 1166 ^T and L. delbrueckii subsp. lactis JCM 1248 ^T, which are also known as d-LAB, the QU 41 strain exhibited a high thermotolerance and produced d-lactic acid at temperatures of 50 °C and higher. In order to optimize the culture conditions of the QU 41 strain, we examined the effects of pH control, temperature, neutralizing reagent, and initial glucose concentration on d-lactic acid production in batch cultures. It was found that the optimal production of 20.1 g/l d-lactic acid was acquired with high optical purity (>99.9% of d-lactic acid) in a pH 6.0-controlled batch culture, by adding ammonium hydroxide as a neutralizing reagent, at 43 °C in MRS medium containing 20 g/l glucose. As a result of product inhibition and low cell density, continuous cultures were investigated using a microfiltration membrane module to recycle flow-through cells in order to improve d-lactic acid productivity. At a dilution rate of 0.87 h⁻¹, the high cell density continuous culture exhibited the highest d-lactic acid productivity of 18.0 g/l/h with a high yield (ca. 1.0 g/g consumed glucose) and a low residual glucose (<0.1 g/l) in comparison with systems published to date.