Characterization of NADP<Superscript>+</Superscript>-specific <Emphasis Type="SmallCaps">l</Emphasis>-rhamnose dehydrogenase from the thermoacidophilic Archaeon <Emphasis Type="Italic">Thermoplasma acidophilum</Emphasis>

Thermoplasma acidophilum utilizes l-rhamnose as a sole carbon source. To determine the metabolic pathway of l-rhamnose in Archaea, we identified and characterized l-rhamnose dehydrogenase (RhaD) in T. acidophilum. Ta0747P gene, which encodes the putative T. acidophilum RhaD (Ta_RhaD) enzyme belonging to the short-chain dehydrogenase/reductase family, was expressed in E. coli as an active enzyme catalyzing the oxidation of l-rhamnose to l-rhamnono-1,4-lactone. Analysis of catalytic properties revealed that Ta_RhaD oxidized l-rhamnose, l-lyxose, and l-mannose using only NADP⁺ as a cofactor, which is different from NAD⁺/NADP⁺-specific bacterial RhaDs and NAD⁺-specific eukaryal RhaDs. Ta_RhaD showed the highest activity toward l-rhamnose at 60 °C and pH 7. The K _m and k _cat values were 0.46 mM, 1,341.3 min⁻¹ for l-rhamnose and 0.1 mM, 1,027.2 min⁻¹ for NADP⁺, respectively. Phylogenetic analysis indicated that branched lineages of archaeal RhaD are quite distinct from those of Bacteria and Eukarya. This is the first report on the identification and characterization of NADP⁺-specific RhaD.     

Stimulation of reductive glycerol metabolism by overexpression of an aldehyde dehydrogenase in a recombinant <Emphasis Type="Italic">Klebsiella pneumoniae</Emphasis> strain defective in the oxidative pathway

Previously, we constructed a glycerol oxidative pathway-deficient mutant strain of Klebsiella pneumoniae by inactivation of glycerol dehydrogenase (dhaD) to eliminate by-product synthesis during production of 1,3-propanediol (1,3-PD) from glycerol. Although by-product formation was successfully blocked in the resultant strain, the yield of 1,3-PD was not enhanced, probably because dhaD disruption resulted in insufficient regeneration of the cofactor NADH essential for the activity of 1,3-PD oxidoreductase (DhaT). To improve cofactor regeneration, in the present study we overexpressed an NAD⁺-dependent aldehyde dehydrogenase in the recombinant strain. To this end, an aldehyde dehydrogenase AldHk homologous to E. coli AldH but with NAD⁺-dependent propionaldehyde dehydrogenase activity was identified in K. pneumoniae. Functional analysis revealed that the substrate specificity of AldHk embraced various aldehydes including propionaldehyde, and that NAD⁺ was preferred over NADP⁺ as a cofactor. Overexpression of AldHk in the glycerol oxidative pathway-deficient mutant AK/pVOTHk resulted in a 3.6-fold increase (0.57 g l⁻¹ to 2.07 g l⁻¹) in the production of 3-hydroxypropionic acid (3-HP), and a 1.1-fold enhancement (8.43 g l⁻¹ to 9.65 g l⁻¹) of 1,3-PD synthesis, when glycerol was provided as the carbon source, compared to the levels synthesized by the control strain (AK/pVOT). Batch fermentation using AK/pVOTHk showed a significant increase (to 70%, w/w) in conversion of glycerol to the reductive metabolites, 1,3-PD and 3-HP, with no production of by-products except acetate.     

Production of ectoine through a combined process that uses both growing and resting cells of <Emphasis Type="Italic">Halomonas salina</Emphasis> DSM 5928<Superscript>T</Superscript>

Using ectoine-excreting strain Halomonas salina DSM 5928^T, we developed a new process for high-efficiency production of ectoine, which involved a combined process of batch fermentation by growing cells and production by resting cells. In the first stage, batch fermentation was carried out using growing cells under optimal fermentation conditions. The second stage was the production phase, in which ectoine was synthesized and excreted by phosphate-limited resting cells. Optimal conditions for synthesis and excretion of ectoine during batch fermentation in a 10 l fermentor were 0.5 mol l⁻¹ NaCl and an initial monosodium glutamate concentration of 80 g l⁻¹ respectively. The pH was adjusted to 7.0 and the temperature was maintained at 33°C. In phosphate-limited resting cells medium, monosodium glutamate and NaCl concentration was 200 g l⁻¹ and 0.5 mol l⁻¹, respectively, as well as pH was 7.0. The total concentration of ectoine produced was 14.86 g l⁻¹, the productivity and yield of ectoine was 7.75 g l⁻¹ day⁻¹ and 0.14 g g⁻¹, respectively, and the percentage of ectoine excreted was 79%. These levels of ectoine production and excretion are the highest reported to date.     

Enhanced production of GDP-<Emphasis Type="SmallCaps">l</Emphasis>-fucose by overexpression of NADPH regenerator in recombinant <Emphasis Type="Italic">Escherichia coli</Emphasis>

Biosynthesis of guanosine 5′-diphosphate-l-fucose (GDP-l-fucose) requires NADPH as a reducing cofactor. In this study, endogenous NADPH regenerating enzymes such as glucose-6-phosphate dehydrogenase (G6PDH), isocitrate dehydrogenase (Icd), and NADP⁺-dependent malate dehydrogenase (MaeB) were overexpressed to increase GDP-l-fucose production in recombinant Escherichia coli. The effects of overexpression of each NADPH regenerating enzyme on GDP-l-fucose production were investigated in a series of batch and fed-batch fermentations. Batch fermentations showed that overexpression of G6PDH was the most effective for GDP-l-fucose production. However, GDP-l-fucose production was not enhanced by overexpression of G6PDH in the glucose-limited fed-batch fermentation. Hence, a glucose feeding strategy was optimized to enhance GDP-l-fucose production. Fed-batch fermentation with a pH-stat feeding mode for sufficient supply of glucose significantly enhanced GDP-l-fucose production compared with glucose-limited fed-batch fermentation. A maximum GDP-l-fucose concentration of 235.2 ± 3.3 mg l⁻¹, corresponding to a 21% enhancement in the GDP-l-fucose production compared with the control strain overexpressing GDP-l-fucose biosynthetic enzymes only, was achieved in the pH-stat fed-batch fermentation of the recombinant E. coli overexpressing G6PDH. It was concluded that sufficient glucose supply and efficient NADPH regeneration are crucial for NADPH-dependent GDP-l-fucose production in recombinant E. coli.     

Engineering <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis> for the production of pyruvate

A Corynebacterium glutamicum strain with inactivated pyruvate dehydrogenase complex and a deletion of the gene encoding the pyruvate:quinone oxidoreductase produces about 19 mM l-valine, 28 mM l-alanine and about 55 mM pyruvate from 150 mM glucose. Based on this double mutant C. glutamicum △aceE △pqo, we engineered C. glutamicum for efficient production of pyruvate from glucose by additional deletion of the ldhA gene encoding NAD⁺-dependent l-lactate dehydrogenase (LdhA) and introduction of a attenuated variant of the acetohydroxyacid synthase (△C–T IlvN). The latter modification abolished overflow metabolism towards l-valine and shifted the product spectrum to pyruvate production. In shake flasks, the resulting strain C. glutamicum △aceE △pqo △ldhA △C–T ilvN produced about 190 mM pyruvate with a Y _P/S of 1.36 mol per mol of glucose; however, it still secreted significant amounts of l-alanine. Additional deletion of genes encoding the transaminases AlaT and AvtA reduced l-alanine formation by about 50%. In fed-batch fermentations at high cell densities with adjusted oxygen supply during growth and production (0–5% dissolved oxygen), the newly constructed strain C. glutamicum △aceE △pqo △ldhA △C–T ilvN △alaT △avtA produced more than 500 mM pyruvate with a maximum yield of 0.97 mol per mole of glucose and a productivity of 0.92 mmol g_(CDW)⁻¹ h⁻¹ (i.e., 0.08 g g_(CDW) ⁻¹ h⁻¹) in the production phase.     

Expression of protein engineered NADP<Superscript>+</Superscript>-dependent xylitol dehydrogenase increases ethanol production from xylose in recombinant <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis>

A recombinant Saccharomyces cerevisiae strain transformed with xylose reductase (XR) and xylitol dehydrogenase (XDH) genes from Pichia stipitis has the ability to convert xylose to ethanol together with the unfavorable excretion of xylitol, which may be due to cofactor imbalance between NADPH-preferring XR and NAD⁺-dependent XDH. To reduce xylitol formation, we have already generated several XDH mutants with a reversal of coenzyme specificity toward NADP⁺. In this study, we constructed a set of recombinant S. cerevisiae strains with xylose-fermenting ability, including protein-engineered NADP⁺-dependent XDH-expressing strains. The most positive effect on xylose-to-ethanol fermentation was found by using a strain named MA-N5, constructed by chromosomal integration of the gene for NADP⁺-dependent XDH along with XR and endogenous xylulokinase genes. The MA-N5 strain had an increase in ethanol production and decrease in xylitol excretion compared with the reference strain expressing wild-type XDH when fermenting not only xylose but also mixed sugars containing glucose and xylose. Furthermore, the MA-N5 strain produced ethanol with a high yield of 0.49 g of ethanol/g of total consumed sugars in the nonsulfuric acid hydrolysate of wood chips. The results demonstrate that glucose and xylose present in the lignocellulosic hydrolysate can be efficiently fermented by this redox-engineered strain.     

Metabolic engineering of <Emphasis Type="Italic">Escherichia coli</Emphasis> for improving <Emphasis Type="SmallCaps">l</Emphasis>-3,4-dihydroxyphenylalanine (<Emphasis Type="SmallCaps">l</Emphasis>-DOPA) synthesis from glucose

l-3,4-dihydroxyphenylalanine (l-DOPA) is an aromatic compound employed for the treatment of Parkinson's disease. Metabolic engineering was applied to generate Escherichia coli strains for the production of l-DOPA from glucose by modifying the phosphoenolpyruvate:sugar phosphotransferase system (PTS) and aromatic biosynthetic pathways. Carbon flow was directed to the biosynthesis of l-tyrosine (l-Tyr), an l-DOPA precursor, by transforming strains with compatible plasmids carrying genes encoding a feedback-inhibition resistant version of 3-deoxy-d-arabino-heptulosonate-7-phosphate synthase, transketolase, the chorismate mutase domain from chorismate mutase-prephenate dehydratase from E. coli and cyclohexadienyl dehydrogenase from Zymomonas mobilis. The effects on l-Tyr production of PTS inactivation (PTS⁻ gluc⁺ phenotype), as well as inactivation of the regulatory protein TyrR, were evaluated. PTS inactivation caused a threefold increase in the specific rate of l-Tyr production (q _l-Tyr), whereas inactivation of TyrR caused 1.7- and 1.9-fold increases in q _l-Tyr in the PTS⁺ and the PTS⁻ gluc⁺ strains, respectively. An 8.6-fold increase in l-Tyr yield from glucose was observed in the PTS⁻ gluc⁺ tyrR ⁻ strain. Expression of hpaBC genes encoding the enzyme 4-hydroxyphenylacetate 3-hydroxylase from E. coli W in the strains modified for l-Tyr production caused the synthesis of l-DOPA. One of such strains, having the PTS⁻ gluc⁺ tyrR ⁻ phenotype, displayed the best production parameters in minimal medium, with a specific rate of l-DOPA production of 13.6 mg/g/h, l-DOPA yield from glucose of 51.7 mg/g and a final l-DOPA titer of 320 mg/l. In a batch fermentor culture in rich medium this strain produced 1.51 g/l of l-DOPA in 50 h.     

<Emphasis Type="SmallCaps">l</Emphasis>-Proline nutrition and catabolism in <Emphasis Type="Italic">Staphylococcus saprophyticus</Emphasis>

Staphylococcus saprophyticus strains ATCC 15305, ATCC 35552, and ATCC 49907 were found to require l-proline but not l-arginine for growth in a defined culture medium. All three strains could utilize l-ornithine as a proline source and contained l-ornithine aminotransferase and Δ¹-pyrroline-5-carboxylate reductase activities; strains ATCC 35552 and ATCC 49907 could use l-arginine as a proline source and had l-arginase activity. The proline requirement also could be met by l-prolinamide, l-proline methyl ester, and the dipeptides l-alanyl-l-proline and l-leucyl-l-proline. The bacteria exhibited l-proline degradative activity as measured by the formation of Δ¹-pyrroline-5-carboxylate. The specific activity of proline degradation was not affected by addition of l-proline or NaCl but was highest in strain ATCC 49907 after growth in Mueller–Hinton broth. A membrane fraction from this strain had l-proline dehydrogenase activity as detected both by reaction of Δ¹-pyrroline-5-carboxylate with 2-aminobenzaldehyde (0.79 nmol min⁻¹ mg⁻¹) and by the proline-dependent reduction of p-iodonitrotetrazolium (20.1 nmol min⁻¹ mg⁻¹). A soluble fraction from this strain had Δ¹-pyrroline-5-carboxylate dehydrogenase activity (88.8 nmol min⁻¹ mg⁻¹) as determined by the NAD⁺-dependent oxidation of dl-Δ¹-pyrroline-5-carboxylate. Addition of l-proline to several culture media did not increase the growth rate or final yield of bacteria but did stimulate growth during osmotic stress. When grown with l-ornithine as the proline source, S. saprophyticus was most susceptible to the proline analogues L-azetidine-2-carboylate, 3,4-dehydro-dl-proline, dl-thiazolidine-2-carboxylate, and l-thiazolidine-4-carboxylate. These results indicate that proline uptake and metabolism may be a potential target of antimicrobial therapy for this organism.     

Biochemical properties and physiological roles of NADP-dependent malic enzyme in <Emphasis Type="Italic">Escherichia coli</Emphasis>

Malic enzymes catalyze the reversible oxidative decarboxylation of L-malate using NAD(P)⁺ as a cofactor. NADP-dependent malic enzyme (MaeB) from Escherichia coli MG1655 was expressed and purified as a fusion protein. The molecular weight of MaeB was about 83 kDa, as determined by SDS-PAGE. The recombinant MaeB showed a maximum activity at pH 7.8 and 46°C. MaeB activity was dependent on the presence of Mn²⁺ but was strongly inhibited by Zn²⁺. In order to understand the physiological roles, recombinant E. coli strains (icd ^NADP/ΔmaeB and icd ^NAD/ΔmaeB) containing NADP-dependent isocitrate dehydrogenase (IDH), or engineered NAD-dependent IDH with the deletion of the maeB gene, were constructed using homologous recombination. During growth on acetate, icd ^NAD/ΔmaeB grew poorly, having a growth rate only 60% that of the wild-type strain (icd ^NADP). Furthermore, icd ^NADP/ΔmaeB exhibited a 2-fold greater adaptability to acetate than icd ^NAD/ΔmaeB, which may be explained by more NADPH production for biosynthesis in icd ^NADP/ΔmaeB due to its NADP-dependent IDH. These results indicated that MaeB was important for NADPH production for bacterial growth on acetate. We also observed that MaeB activity was significantly enhanced (7.83-fold) in icd ^NAD, which was about 3-fold higher than that in icd ^NADP, when switching from glucose to acetate. The marked increase of MaeB activity was probably induced by the shortage of NADPH in icd ^NAD. Evidently, MaeB contributed to the NADPH generation needed for bacterial growth on two carbon compounds.     

CD133<Superscript>+</Superscript>CD44<Superscript>+</Superscript> subgroups may be human small intestinal stem cells

The identification and separation of small intestinal epithelial stem cells are still on the preliminary stage. In this study, we planned to utilize immunohistochemistry, fluorescence-activated cell sorting (FACS) and RT-PCR to investigate the possibility of CD133 and CD44 as markers of human small intestinal epithelial stem cells. The expressions of CD133, CD44 and Lgr5 were studied by immunohistochemistry. Four subgroups of CD133⁺CD44⁺, CD133⁺CD44⁻, CD133⁻CD44⁺, CD133⁻CD44⁻ were sorted out through FACS and the expression level of Lgr5 gene was measured by RT-PCR and polyacrylamide gel electropheresis (PAGE) with sliver stained. Ten cases of samples were available for analyzing. By immunohistochemical staining, few cells with positive expressions of CD133, CD44 and Lgr5 were distributed in the bottom of crypts with the expression locations somewhat overlapped. The average percentage of CD133⁺CD44⁺ cells was 0.0580 ± 0.0403%, while the corresponding contents of CD133⁺CD44⁻ cells, CD133⁻CD44⁺ cells and CD133⁻CD44⁻ cells were 0.4000 ± 0.1225%, 0.7000 ± 0.2646% and 76.5600 ± 3.5529% respectively. Ten times of positive expressions of Lgr5 were detected in the CD133⁺CD44⁺ groups, while 9/10, 8/10 and 4/10 times for CD133⁺CD44⁻, CD133⁻CD44⁺ and CD133⁻CD44⁻ subgroups respectively. With the help of Quantityone 4.62 software, the densities of corresponding place to Lgr5 and reference gene were obtained. The density ratios of corresponding place to Lgr5 to reference gene were significant difference between subgroups (P < 0.001). By means of LSD method, the density ratios in CD133⁺CD44⁺ subgroups had statistical differences from the other subgroups (P < 0.05). We concluded CD133⁺CD44⁺ cells may be human small intestinal epithelial stem cells, which need further researches to confirm.     

<Emphasis Type="Italic">Clostridium beijerinckii</Emphasis> mutant with high inhibitor tolerance obtained by low-energy ion implantation

Clostridium beijerinckii mutant strain IB4, which has a high level of inhibitor tolerance, was screened by low-energy ion implantation and used for butanol fermentation from a non-detoxified hemicellulosic hydrolysate of corn fiber treated with dilute sulfuric acid (SAHHC). Evaluation of toxicity showed C. beijerinckii IB4 had a higher level of tolerance than parent strain C. beijerinckii NCIMB 8052 for five out of six phenolic compounds tested (the exception was vanillin). Using glucose as carbon source, C. beijerinckii IB4 produced 9.1 g l⁻¹ of butanol with an acetone/butanol/ethanol (ABE) yield of 0.41 g g⁻¹. When non-detoxified SAHHC was used as carbon source, C. beijerinckii NCIMB 8052 grew well but ABE production was inhibited. By contrast, C. beijerinckii IB4 produced 9.5 g l⁻¹ of ABE with a yield of 0.34 g g⁻¹, including 2.2 g l⁻¹ acetone, 6.8 g l⁻¹ butanol, and 0.5 g l⁻¹ ethanol. The remarkable fermentation and inhibitor tolerance of C. beijerinckii IB4 appears promising for ABE production from lignocellulosic materials.     

Metagenome Cloning and Functional Analysis of Na<Superscript>+</Superscript>/H<Superscript>+</Superscript> Antiporter Genes from Keke Salt Lake in China

Na⁺/H⁺ antiporters are ubiquitous membrane proteins and play a central role in cell homeostasis including pH regulation, osmoregulation, and Na⁺/Li⁺ tolerance in bacteria. The microbial communities in extremely hypersaline soil are an important resource for isolating Na⁺/H⁺ antiporter genes. A metagenomic library containing 35,700 clones was constructed by using genomic DNA obtained from the hypersaline soil samples of Keke Salt Lake in Northwest of China. Two Na⁺/H⁺ antiporters, K1-NhaD, and K2-NhaD belonging to NhaD family, were screened and cloned from this metagenome by complementing the triple mutant Escherichia coli strain KNabc (nhaA ⁻ , nhaB ⁻ , chaA ⁻) in medium containing 0.2 M NaCl. K1-NhaD and K2-NhaD have 75.5% identity at the predicted amino acid sequence. K1-NhaD has 78% identity with Na⁺/H⁺ antiporter NhaD from Halomonas elongate at the predicted amino acid sequence. The predicted K1-NhaD is a 53.5 kDa protein (487 amino acids) with 13 transmembrane helices. K2-NhaD has 73% identity with Alkalimonas amylolytica NhaD. The predicted K2-NhaD is a 55 kDa protein (495 amino acids) with 12 transmembrane helices. Both K1-NhaD and K2-NhaD could make the triple mutant E. coli KNabc (nhaA ⁻ , nhaB ⁻ , chaA⁻) grow in the LBK medium containing 0.2–0.6 M Na⁺ or with 0.05–0.4 M Li⁺. Everted membrane vesicles prepared from E. coli KNabc cells carrying K1-NhaD or K2-NhaD exhibited Na⁺/H⁺ and Li⁺/H⁺ antiporter activities which were pH-dependent with the highest activity at pH 9.5. Little K⁺/H⁺ antiporter activity was also detected in vesicles form E. coli KNabc carrying K1-NhaD or K2-NhaD.     

Bio-hydrogen production from cellulose by sequential co-culture of cellulosic hydrogen bacteria of <Emphasis Type="Italic">Enterococcus gallinarum</Emphasis> G1 and <Emphasis Type="Italic">Ethanoigenens harbinense</Emphasis> B49

Microbial conversion of lignocellulose to hydrogen is a fascinating way to provide a renewable energy source. A mesophilic bacterium strain G1 that had high cellulose degradation and hydrogen production activity (2.38 mmol H₂ g⁻¹ cellulose) was isolated from rumen fluid and identified as the Enterococcus gallinarum. Hydrogen production from cellulose by using sequential co-cultures of a cellulosic-hydrolysis bacterium G1 and Ethanoigenens harbinense B49 was investigated. With an initial Avicel concentration of 5 g l^−l, the sequential co-culture with G1 and strain Ethanoigenens harbinense B49 produced H₂ yield approximately 2.97 mmol H₂ g⁻¹ cellulose for the co-culture system.     

Oxygen consumption rate and Na<Superscript>+</Superscript>/K<Superscript>+</Superscript>-ATPase activity in early developmental stages of the sea urchin <Emphasis Type="Italic">Paracentrotus lividus</Emphasis> Lam.

Changes in oxygen consumption rate and Na⁺/K⁺-ATPase activity during early development were studied in the sea urchin Paracentrotus lividus Lam. The oxygen consumption rate increased from 0.12 μmol O₂ mg protein⁻¹ h⁻¹ in unfertilized eggs to 0.38 μmol O₂ mg protein⁻¹ h⁻¹ 25 min after fertilization. Specific activity of the Na⁺/K⁺-ATPase was significantly stimulated after fertilization, ranging up to 1.07 μmol P_i h⁻¹ mg protein⁻¹ in the late blastula stage and slightly lower values in the early and late pluteus stages.     

Na<Superscript>+</Superscript>/H<Superscript>+</Superscript> exchange activity in the alkaliphile halotolerant cyanobacterium <Emphasis Type="Italic">Aphanothece halophytica</Emphasis>

The activity of Na⁺/H⁺ exchanger to remove toxic Na⁺ is important for growth of organisms under high salinity. In this study, the halotolerant cyanobacterium Aphanothece halophytica was shown to possess Na⁺/H⁺ exchange activity since exogenously added Na⁺ could dissipate a pre-formed pH gradient, and decrease extracellular pH. Kinetic analysis yielded apparent K _m (Na⁺) and V _max of 20.7 ± 3.1 mM and 3,333 ± 370 nmol H⁺ min⁻¹ mg⁻¹, respectively. For cells grown under salt-stress condition, the apparent K _m (Na⁺) and V _max was 18.3 ± 3.5 mM and 3,703 ± 350 nmol H⁺ min⁻¹ mg⁻¹, respectively. Three cations with decreasing efficiency namely Li⁺, Ca²⁺, and K⁺ were also able to dissipate pH gradient. Only marginal exchange activity was observed for Mg²⁺. The exchange activity was strongly inhibited by Na⁺-gradient dissipators, monensin, and sodium ionophore as well as by CCCP, a protonophore. A. halophytica showed high Na⁺/H⁺ exchange activity at neutral and alkaline pH up to pH 10. Cells grown at pH 7.6 under high salinity exhibited higher Na⁺/H⁺ exchange activity than those grown under low salinity during 15 days of growth suggesting a role of Na⁺/H⁺ exchanger for salt tolerance in A. halophytica. Cells grown at alkaline pH of 9.0 also exhibited a progressive increase of Na⁺/H⁺ exchange activity during 15 days of growth.     

Continuous butanol production with reduced byproducts formation from glycerol by a hyper producing mutant of <Emphasis Type="Italic">Clostridium pasteurianum</Emphasis>

Butanol, a four-carbon primary alcohol (C₄H₁₀O), is an important industrial chemical and has a good potential to be used as a superior biofuel. Bio-based production of butanol from renewable feedstock is a promising and sustainable alternative to substitute petroleum-based fuels. Here, we report the development of a process for butanol production from glycerol, which is abundantly available as a byproduct of biodiesel production. First, a hyper butanol producing strain of Clostridium pasteurianum was isolated by chemical mutagenesis. The best mutant strain, C. pasteurianum MBEL_GLY2, was able to produce 10.8 g l⁻¹ butanol from 80 g l⁻¹ glycerol as compared to 7.6 g l⁻¹ butanol produced by the parent strain. Next, the process parameters were optimized to maximize butanol production from glycerol. Under the optimized batch condition, the butanol concentration, yield, and productivity of 17.8 g l⁻¹, 0.30 g g⁻¹, and 0.43 g l⁻¹ h⁻¹ could be achieved. Finally, continuous fermentation of C. pasteurianum MBEL_GLY2 with cell recycling was carried out using glycerol as a major carbon source at several different dilution rates. The continuous fermentation was run for 710 h without strain degeneration. The acetone–butanol–ethanol productivity and the butanol productivity of 8.3 and 7.8 g l⁻¹ h⁻¹, respectively, could be achieved at the dilution rate of 0.9 h⁻¹. This study reports continuous production of butanol with reduced byproducts formation from glycerol using C. pasteurianum, and thus could help design a bioprocess for the improved production of butanol.     

Enhanced anti-tumor activity of interferon-alpha in SOCS1-deficient mice is mediated by CD4<Superscript>+</Superscript> and CD8<Superscript>+</Superscript> T cells

Interferon-alpha (IFN-α) is an immunomodulatory cytokine that is used clinically for the treatment of melanoma in the adjuvant setting. The cellular actions of IFN-α are regulated by the suppressors of cytokine signaling (SOCS) family of proteins. We hypothesized that the anti-tumor activity of exogenous IFN-α would be enhanced in SOCS1-deficient mice. SOCS1-deficient (SOCS1^−/−) or control (SOCS1^+/+) mice on an IFN-γ^−/− C57BL/6 background bearing intraperitoneal (i.p.) JB/MS murine melanoma cells were treated for 30 days with i.p. injections of IFN-A/D or PBS (vehicle). Log-rank Kaplan-Meier survival curves were used to evaluate survival. Tumor-bearing control SOCS1^+/+ mice receiving IFN-A/D had significantly enhanced survival versus PBS–treated mice (P = 0.0048). The anti-tumor effects of IFN-A/D therapy were significantly enhanced in tumor-bearing SOCS1^−/− mice; 75% of these mice survived tumor challenge, whereas PBS-treated SOCS1^−/− mice all died at 13-16 days (P = 0.00038). Antibody (Ab) depletion of CD8⁺ T cells abrogated the anti-tumor effects of IFN-A/D in SOCS1^−/− mice as compared with mice receiving a control antibody (P = 0.0021). CD4⁺ T-cell depletion from SOCS1^−/− mice also inhibited the effects of IFN-A/D (P = 0.0003). IFN-A/D did not alter expression of CD80 or CD86 on splenocytes of SOCS1^+/+ or SOCS1^−/− mice, or the proportion of T regulatory cells or myeloid-derived suppressor cells in SOCS1^+/+ or SOCS1^−/− mice. An analysis of T-cell function did reveal increased proliferation of SOCS1-deficient splenocytes at baseline and in response to mitogenic stimuli. These data suggest that modulation of SOCS1 function in T-cell subsets could enhance the anti-tumor effects of IFN-α in the setting of melanoma.     

Effects of macroelements and nitrogen source on biomass accumulation and withanolide-A production from cell suspension cultures of <Emphasis Type="Italic">Withania somnifera</Emphasis> (L.) Dunal

Withania somnifera is an important medicinal plant that contains withanolides and withaferins, both bioactive compounds. We have tested the effects of macroelements and nitrogen source in W. somnifera cell suspension cultures with the aim of optimizing the production of biomass and withanolide A. The effects of the macroelements NH₄NO_3, KNO_3, CaCl_2, MgSO₄ and KH₂PO₄ at concentrations of 0.0, 0.5, 1.0, 1.5 and 2.0× strength and of the nitrogen source [NH₄ ⁺/NO₃ ⁻ (mM/mM) ratio of: 0.00/18.80, 7.19/18.80, 14.38/18.80, 21.57/18.80, 28.75/18.80, 14.38/0.00, 14.38/9.40, 14.38/18.80, 14.38/28.20, and 14.38/37.60 (mM)] in Murashige and Skoog medium were tested for biomass and withanolide A production. The highest accumulation of biomass [147.81 g l⁻¹ fresh weight (FW) and 14.02 g l⁻¹ (dry weight (DW)] was recorded in the medium containing a 0.5× concentration of NH₄NO₃, and the highest production of withanolide A content was recorded in the medium with 2.0× KNO₃ (4.36 mg g⁻¹ DW). The NH₄ ⁺/NO₃ ⁻ ratio also influenced cell growth and withanolide A production, with both parameters being larger when the NO₃ ⁻ concentration was higher than that of NH₄ ⁺. Maximum biomass growth (110.45 g l⁻¹ FW and 9.29 g l⁻¹ DW) was achieved at an NH₄ ⁺/NO₃ ⁻ ratio of 7.19/18.80, while withanolide A production was greatest (3.96 mg g⁻¹ DW) when the NH₄ ⁺/NO₃ ⁻ ratio was 14.38/37.60 mM.     

Enhanced <Emphasis Type="SmallCaps">d</Emphasis>-ribose biosynthesis in batch culture of a transketolase-deficient <Emphasis Type="Italic">Bacillus subtilis</Emphasis> strain by citrate

In this study, the effects of citrate addition on d-ribose production were investigated in batch culture of a transketolase-deficient strain, Bacillus subtilis EC2, in shake flasks and bioreactors. Batch cultures in shake flasks and a 5-l reactor indicated that supplementation with 0.2–0.5 g l⁻¹ of citrate enhanced d-ribose production. When B. subtilis EC2 was cultivated in a 15-l reactor in a complex medium, the d-ribose concentration was 70.9 g l⁻¹ with a ribose yield of 0.497 mol mol⁻¹. When this strain was grown in the same medium supplemented with 0.3 g l⁻¹ of citrate, 83.4 g l⁻¹ of d-ribose were obtained, and the ribose yield was increased to 0.587 mol mol⁻¹. Addition of citrate reduced the activities of pyruvate kinase and phosphofructokinase, while it increased those of glucose-6-phosphate dehydrogenase and 6-phosphogluconate dehydrogenase. Metabolic flux distribution in the stationary phase indicated that citrate addition resulted in increased fluxes in the pentose phosphate pathway and TCA cycle, and decreased fluxes in the glycolysis and acetate pathways.     

Molecular Cloning and Characterization of a Malic Enzyme Gene from the Oleaginous Yeast <Emphasis Type="Italic">Lipomyces starkeyi</Emphasis>

The malic enzyme-encoding cDNA (GQ372891) from the oleaginous yeast Lipomyces starkeyi AS 2.1560 was isolated, which has an 1719-bp open reading frame flanked by a 290-bp 5′ untranslated sequence and a 92-bp 3′ untranslated sequence. The proposed gene, LsME1, encoded a protein with 572 amino acid residues. The protein presented 58% sequence identity with the malic enzymes from Yarrowia lipolytica CLIB122 and Aspergillus fumigatus Af293. The LsME1 gene was cloned into the vector pMAL-p4x to express a fusion protein (MBP-LsME1) in Escherichia coli TB1. The fusion protein was purified and then cleaved by Factor Xa to give the recombinant LsME1. This purified enzyme took either NAD⁺ or NADP⁺ as the coenzyme but preferred NAD⁺. The K _m values for malic acid, NAD⁺ and NADP⁺ were 0.85 ± 0.05 mM, 0.34 ± 0.08 mM, and 7.4 ± 0.32 mM, respectively, at pH 7.3.