Improvement in activity of cellulase Cel12A of Thermotoga neapolitana by error prone PCR.

Using multi-step error prone PCR (ep-PCR) of the gene encoding endoglucanase Cel12A (27 kDa) from Thermotoga neapolitana, mutants were obtained with many fold increase in the enzyme activity. The best mutant (C6, N47S/E57 K/ V88A/S157 P/K165 H) obtained after four rounds of ep-PCR showed 2.7-, 5- and 4.8-fold increase in activity against CMC, RAC and Avicel, respectively, compared with the wild type enzyme. The other characteristics of the mutated enzyme with respect to stability, optimum working pH and temperature were comparable to the wild type enzyme.C6 mutant showed higher binding efficiency towards the rice straw (∼50%) than the wild type (∼41%). The structural information obtained from the protein docking of the wild type Cel12A and its mutant showed that E57 K improved the binding affinity between enzyme and ligand by producing conformational changes in the catalytic cavity. The other mutations can facilitate the enzyme-substrate binding interactions to enhance catalytic activity although they are not directly involved in catalysis. The wild type and mutant enzyme produce cellobiose as the major products for both soluble and insoluble substrates, suggesting that this enzyme should be a cellobiohydrolase instead of endoglucanase as previously reported.

Effect of feed glucose and acetic acid on continuous biohydrogen production by Thermotoga neapolitana.

This study focused on the effect of feed glucose and acetic acid on biohydrogen production by Thermotoga neapolitana under continuous-flow conditions. Increasing the feed glucose concentration from 11.1 to 41.6 mM decreased the hydrogen yield from 3.6 (±0.1) to 1.4 (±0.1) mol H2/mol glucose. The hydrogen production rate concomitantly increased until 27.8 mM of feed glucose but remained unaffected when feed glucose was further raised to 41.6 mM. Increasing the acetic acid concentration from 0 to 240 mM hampered dark fermentation in batch bioassays, diminishing the cumulative hydrogen production by 45% and the hydrogen production rate by 57%, but induced no negative effect during continuous operation. Indeed, throughout the continuous flow operation the process performance improved considerably, as indicated by the 47% increase of hydrogen yield up to 3.1 (±0.1) mol H2/mol glucose on day 110 at 27.8 mM feed glucose.

Cloning, purification, and characterization of xylose isomerase from Thermotoga naphthophila RKU-10.

A 1.3 kb xyl-A gene encoding xylose isomerase from a hyperthermophilic eubacterium Thermotoga naphthophila RKU-10 (TnapXI) was cloned and over-expressed in Escherichia coli to produce the enzyme in mesophilic conditions that work at high temperature. The enzyme was concentrated by lyophilization and purified by heat treatment, fractional precipitation, and UNOsphere Q anion-exchange column chromatography to homogeneity level. The apparent molecular mass was estimated by SDS-PAGE to be 49.5 kDa. The active enzyme showed a clear zone on Native-PAGE when stained with 2, 3, 5-triphenyltetrazolium chloride. The optimum temperature and pH for D-glucose to D-fructose isomerization were 98 °C and 7.0, respectively. Xylose isomerase retains 85% of its activity at 50 °C (t1/2 1732 min) for 4 h and 32.5% at 90 °C (t1/2 58 min) for 2 h. It retains 90-95% of its activity at pH 6.5-7.5 for 30 min. The enzyme was highly activated (350%) with the addition of 0.5 mM Co(2+) and to a lesser extent about 180 and 80% with the addition of 5 and 10 mM Mn(2+) and Mg(2+) , respectively but it was inhibited (54-90%) in the presence of 0.5-10 mM Ca(2+) with respect to apo-enzyme. D-glucose isomerization product was also analyzed by Thin Layer Chromatography (Rf 0.65). The enzyme was very stable at neutral pH and sufficiently high temperature and required only a trace amount of Co(2+) for its optimal activity and stability. Overall, 52.2% conversion of D-glucose to D-fructose was achieved by TnapXI. Thus, it has a great potential for industrial applications.

Hydrogen Production by the Thermophilic Bacterium Thermotoga neapolitana.

As the only fuel that is not chemically bound to carbon, hydrogen has gained interest as an energy carrier to face the current environmental issues of greenhouse gas emissions and to substitute the depleting non-renewable reserves. In the last years, there has been a significant increase in the number of publications about the bacterium Thermotoga neapolitana that is responsible for production yields of H2 that are among the highest achievements reported in the literature. Here we present an extensive overview of the most recent studies on this hyperthermophilic bacterium together with a critical discussion of the potential of fermentative production by this bacterium. The review article is organized into sections focused on biochemical, microbiological and technical issues, including the effect of substrate, reactor type, gas sparging, temperature, pH, hydraulic retention time and organic loading parameters on rate and yield of gas production.

Introducing capnophilic lactic fermentation in a combined dark-photo fermentation process: a route to unparalleled H2 yields.

Two-stage process based on photofermentation of dark fermentation effluents is widely recognized as the most effective method for biological production of hydrogen from organic substrates. Recently, it was described an alternative mechanism, named capnophilic lactic fermentation, for sugar fermentation by the hyperthermophilic bacterium Thermotoga neapolitana in CO2-rich atmosphere. Here, we report the first application of this novel process to two-stage biological production of hydrogen. The microbial system based on T. neapolitana DSM 4359(T) and Rhodopseudomonas palustris 42OL gave 9.4 mol of hydrogen per mole of glucose consumed during the anaerobic process, which is the best production yield so far reported for conventional two-stage batch cultivations. The improvement of hydrogen yield correlates with the increase in lactic production during capnophilic lactic fermentation and takes also advantage of the introduction of original conditions for culturing both microorganisms in minimal media based on diluted sea water. The use of CO2 during the first step of the combined process establishes a novel strategy for biohydrogen technology. Moreover, this study opens the way to cost reduction and use of salt-rich waste as feedstock.

Recycling of carbon dioxide and acetate as lactic acid by the hydrogen-producing bacterium Thermotoga neapolitana.

The heterotrophic bacterium Thermotoga neapolitana produces hydrogen by fermentation of sugars. Under capnophilic (carbon dioxide requiring) conditions, the process is preferentially associated with the production of lactic acid, which, as shown herein, is synthesized by reductive carboxylation of acetyl coenzyme A. The enzymatic coupling is dependent on the carbon dioxide stimulated activity of heterotetrameric pyruvate:ferredoxin oxidoreductase. Under the same culture conditions, T. neapolitana also operates the unfavorable synthesis of lactic acid from an exogenous acetate supply. This process, which requires carbon dioxide (or carbonate) and an unknown electron donor, allows for the conversion of carbon dioxide into added-value chemicals without biomass deconstruction.

A kinetic study of biohydrogen production from glucose, molasses and cheese whey by suspended and attached cells of Thermotoga neapolitana.

Batch tests of H2 production from glucose, molasses and cheese whey by suspended and immobilized cells of Thermotoga neapolitana were conducted to develop a kinetic model of the process. H2 production was inhibited by neither H2 (up to 0.7 mg L(-1)) nor O2 (up to 0.2 mg L(-1)). The H2 specific rates obtained at different substrate concentrations were successfully interpolated with Andrew's inhibition model. With glucose and molasses, biofilms performed better than suspended cells. The suspended-cell process was successfully scaled-up to a 19-L bioreactor. Assays co-fed with molasses and cheese whey led to higher H2 productivities and H2/substrate yields than the single-substrate tests. The simulation of the suspended-cell continuous-flow process indicated the potential attainment of H2 productivities higher than those of the batch tests (up to 3.6 mmol H2 h(-1) L(-1) for molasses and 0.67 mmol H2 h(-1) L(-1) for cheese whey) and allowed the identification of the optimal dilution rate.

Proteomic and physiological experiments to test Thermotoga neapolitana constraint-based model hypotheses of carbon source utilization.

Constraint-based models of biochemical reaction networks require experimental validation to test model-derived hypotheses and iteratively improve the model. Physiological and proteomic analysis of Thermotoga neapolitana growth on cellotetraose was conducted to identify gene products related to growth on cellotetraose to improve a constraint-based model of T. neapolitana central carbon metabolism with incomplete cellotetraose pathways. In physiological experiments comparing cellotetraose to cellobiose and glucose as growth substrates, product formation yields on cellotetraose, cellobiose, and glucose were similar; however cell yields per mol carbon consumed were higher on cellotetraose than on cellobiose or glucose. Proteomic analysis showed increased expression of several proteins from cells grown on cellotetraose compared with glucose cell cultures, including cellobiose phosphorylase (CTN_0783), endo-1,4-ß-glucosidase (CTN_1106), and an ATP-binding protein (CTN_1296). The CTN_1296 gene product should be evaluated further for participation in cellotetraose metabolism and is included as one of two hypothetical gene-protein-reaction associations in the T. neapolitana constraint-based model to reinstate cellotetraose metabolism in model simulations.

Crystal structure of HydF scaffold protein provides insights into [FeFe]-hydrogenase maturation.

[FeFe]-hydrogenases catalyze the reversible production of H2 in some bacteria and unicellular eukaryotes. These enzymes require ancillary proteins to assemble the unique active site H-cluster, a complex structure composed of a 2Fe center bridged to a [4Fe-4S] cubane. The first crystal structure of a key factor in the maturation process, HydF, has been determined at 3 Å resolution. The protein monomer present in the asymmetric unit of the crystal comprises three domains: a GTP-binding domain, a dimerization domain, and a metal cluster-binding domain, all characterized by similar folding motifs. Two monomers dimerize, giving rise to a stable dimer, held together mainly by the formation of a continuous ß-sheet comprising eight ß-strands from two monomers. Moreover, in the structure presented, two dimers aggregate to form a supramolecular organization that represents an inactivated form of the HydF maturase. The crystal structure of the latter furnishes several clues about the events necessary for cluster generation/transfer and provides an excellent model to begin elucidating the structure/function of HydF in [FeFe]-hydrogenase maturation.

Molecular cloning and biochemical characterization of a heat-stable type I pullulanase from Thermotoga neapolitana.

The gene encoding a type I pullulanase from the hyperthermophilic anaerobic bacterium Thermotoga neapolitana (pulA) was cloned in Escherichia coli and sequenced. The pulA gene from T. neapolitana showed 91.5% pairwise amino acid identity with pulA from Thermotoga maritima and contained the four regions conserved in all amylolytic enzymes. pulA encodes a protein of 843 amino acids with a 19-residue signal peptide. The pulA gene was subcloned and overexpressed in E. coli under the control of the T7 promoter. The purified recombinant enzyme (rPulA) produced a 93-kDa protein with pullulanase activity. rPulA was optimally active at pH 5-7 and 80°C and had a half-life of 88 min at 80°C. rPulA hydrolyzed pullulan, producing maltotriose, and hydrolytic activities were also detected with amylopectin, starch, and glycogen, but not with amylose. This substrate specificity is typical of a type I pullulanase. Thin layer chromatography of the reaction products in the reaction with pullulan and aesculin showed that the enzyme had transglycosylation activity. Analysis of the transfer product using NMR and isoamylase treatment revealed it to be α-maltotriosyl-(1,6)-aesculin, suggesting that the enzyme transferred the maltotriosyl residue of pullulan to aesculin by forming α-1,6-glucosidic linkages. Our findings suggest that the pullulanase from T. neapolitana is the first thermostable type I pullulanase which has α-1,6-transferring activity.

H(2) synthesis from pentoses and biomass in Thermotoga spp.

We have investigated H(2) production on glucose, xylose, arabinose, and glycerol in Thermotoga maritima and T. neapolitana. Both species metabolised all sugars with hydrogen yields of 2.7-3.8 mol mol(-1) sugar. Both pentoses were at least comparable to glucose with respect to their qualities as substrates for hydrogen production, while glycerol was not metabolised by either species. Glycerol was also not metabolised by T. elfii. We also demonstrated that T. neapolitana can use wet oxidised wheat straws, in which most sugars are stored in glycoside polymers, for growth and efficient hydrogen production, while glucose, xylose and arabinose are consumed in parallel.

A selection that reports on protein-protein interactions within a thermophilic bacterium.

Many proteins can be split into fragments that exhibit enhanced function upon fusion to interacting proteins. While this strategy has been widely used to create protein-fragment complementation assays (PCAs) for discovering protein-protein interactions within mesophilic organisms, similar assays have not yet been developed for studying natural and engineered protein complexes at the temperatures where thermophilic microbes grow. We describe the development of a selection for protein-protein interactions within Thermus thermophilus that is based upon growth complementation by fragments of Thermotoga neapolitana adenylate kinase (AK(Tn)). Complementation studies with an engineered thermophile (PQN1) that is not viable above 75 degrees C because its adk gene has been replaced by a Geobacillus stearothermophilus ortholog revealed that growth could be restored at 78 degrees C by a vector that coexpresses polypeptides corresponding to residues 1-79 and 80-220 of AK(Tn). In contrast, PQN1 growth was not complemented by AK(Tn) fragments harboring a C156A mutation within the zinc-binding tetracysteine motif unless these fragments were fused to Thermotoga maritima chemotaxis proteins that heterodimerize (CheA and CheY) or homodimerize (CheX). This enhanced complementation is interpreted as arising from chemotaxis protein-protein interactions, since AK(Tn)-C156A fragments having only one polypeptide fused to a chemotaxis protein did not complement PQN1 to the same extent. This selection increases the maximum temperature where a PCA can be used to engineer thermostable protein complexes and to map protein-protein interactions.

Hydrogen production of the hyperthermophilic eubacterium, Thermotoga neapolitana under N2 sparging condition.

Gas sparging was found to be a useful technique to reduce hydrogen partial pressure in the liquid phase to enhance the hydrogen yields of strictly anaerobically fermentative bacteria. The effect of nitrogen (N(2)) sparging on hydrogen yield was investigated in sterile and non-sterile conditions using a pure strain of the hyperthermophilic eubacteria, Thermotoga neapolitana with glucose or xylose as a carbon source. The maximum hydrogen accumulations reached 41% of the gaseous mixtures after 30-40 h. Two applications of N(2) sparging after the H(2) content in the headspace reached the maximum levels gave an increase of H(2) production by 78% from 1.82 to 3.24 mol H(2)/mol glucose and by 56% from 1.41 to 2.20 mol H(2)/mol xylose. This result suggested that the removal of the produced H(2) from the gas headspace of the limited-volume, closed culture vial when it achieves the maximum level of H(2) tolerance of the bacterium is a necessary technique to improve its H(2) yield.

The fermentation stoichiometry of Thermotoga neapolitana and influence of temperature, oxygen, and pH on hydrogen production.

The hyperthermophilic bacterium, Thermotoga neapolitana, has potential for use in biological hydrogen (H(2)) production. The objectives of this study were to (1) determine the fermentation stoichiometry of Thermotoga neapolitana and examine H(2) production at various growth temperatures, (2) investigate the effect of oxygen (O(2)) on H(2) production, and (3) determine the cause of glucose consumption inhibition. Batch fermentation experiments were conducted at temperatures of 60, 65, 70, 77, and 85 degrees C to determine product yield coefficients and volumetric productivity rates. Yield coefficients did not show significant changes with respect to growth temperature and the rate of H(2) production reached maximum levels in both the 77 degrees C and 85 degrees C experiments. The fermentation stoichiometry for T. neapolitana at 85 degrees C was 3.8 mol H(2), 2 mol CO(2), 1.8 mol acetate, and 0.1 mol lactate produced per mol of glucose consumed. Under microaerobic conditions H(2) production did not increase when compared to anaerobic conditions, which supports other evidence in the literature that T. neapolitana does not produce H(2) through microaerobic metabolism. Glucose consumption was inhibited by a decrease in pH. When pH was adjusted with buffer addition cultures completely consumed available glucose.

Towards zirconium phosphonate-based microarrays for probing DNA-protein interactions: critical influence of the location of the probe anchoring groups.

Terminal phosphate groups on double-stranded DNA probes bind strongly to glass substrates coated with a zirconium phosphonate monolayer, and probes immobilized in this way as microarrays can be used to detect protein targets. The sensitivity of the microarray was shown to be enhanced by the use of a polyguanine segment ((G)n , n > or = 5) as a spacer between the phosphate linker and the protein interaction domain. More importantly, the presence of phosphate linkers on both ends of the dsDNA probes leads to significant enhancement of target capture. The relevant characteristics of the different probes when bound to the surface were determined, by the original use of a combination of surface characterization techniques (XPS, AFM, and Sarfus). In this context, the location of the phosphate linkers in the duplex probes was found to result in different probe surface coverage and presentation on the surface, which affect subsequent interactions with the target protein.

Evolution of mal ABC transporter operons in the Thermococcales and Thermotogales.

BACKGROUND: The mal genes that encode maltose transporters have undergone extensive lateral transfer among ancestors of the archaea Thermococcus litoralis and Pyrococcus furiosus. Bacterial hyperthermophiles of the order Thermotogales live among these archaea and so may have shared in these transfers. The genome sequence of Thermotoga maritima bears evidence of extensive acquisition of archaeal genes, so its ancestors clearly had the capacity to do so. We examined deep phylogenetic relationships among the mal genes of these hyperthermophiles and their close relatives to look for evidence of shared ancestry. RESULTS: We demonstrate that the two maltose ATP binding cassette (ABC) transporter operons now found in Tc. litoralis and P. furiosus (termed mal and mdx genes, respectively) are not closely related to one another. The Tc. litoralis and P. furiosus mal genes are most closely related to bacterial mal genes while their respective mdx genes are archaeal. The genes of the two mal operons in Tt. maritima are not related to genes in either of these archaeal operons. They are highly similar to one another and belong to a phylogenetic lineage that includes mal genes from the enteric bacteria. A unique domain of the enteric MalF membrane spanning proteins found also in these Thermotogales MalF homologs supports their relatively close relationship with these enteric proteins. Analyses of genome sequence data from other Thermotogales species, Fervidobacterium nodosum, Thermosipho melanesiensis, Thermotoga petrophila, Thermotoga lettingae, and Thermotoga neapolitana, revealed a third apparent mal operon, absent from the published genome sequence of Tt. maritima strain MSB8. This third operon, mal3, is more closely related to the Thermococcales' bacteria-derived mal genes than are mal1 and mal2. F. nodosum, Ts. melanesiensis, and Tt. lettingae have only one of the mal1-mal2 paralogs. The mal2 operon from an unknown species of Thermotoga appears to have been horizontally acquired by a Thermotoga species that had only mal1. CONCLUSION: These data demonstrate that the Tc. litoralis and P. furiosus mdx maltodextrin transporter operons arose in the Archaea while their mal maltose transporter operons arose in a bacterial lineage, but not the same lineage as the two maltose transporter operons found in the published Tt. maritima genome sequence. These Tt. maritima maltose transporters are phylogenetically and structurally similar to those found in enteric bacteria and the mal2 operon was horizontally transferred within the Thermotoga lineage. Other Thermotogales species have a third mal operon that is more closely related to the bacterial Thermococcales mal operons, but the data do not support a recent horizontal sharing of that operon between these groups.

Inhibitory effects of arbutin-beta-glycosides synthesized from enzymatic transglycosylation for melanogenesis.

To develop a new skin whitening agent, arbutin-beta-glycosides were synthesized and evaluated for their melanogenesis inhibitory activities. Three active compounds were synthesized via the transglycosylation reaction of Thermotoga neapolitana beta-glucosidase and purified by recycling preparative HPLC. As compared with arbutin (IC(50 )= 6 mM), the IC(50 )values of these compounds were 8, 10, and 5 mM for beta-D -glucopyranosyl-(1-->6)-arbutin, beta-D: -glucopyranosyl-(1-->4)-arbutin, and beta-D -glucopyranosyl-(1-->3)-arbutin, respectively. beta-D: -Glucosyl-(1-->3)-arbutin also exerted the most profound inhibitory effects on melanin synthesis in B16F10 melanoma cells. Melanin synthesis was inhibited to a significant degree at 5 mM, at which concentration the melanin content was reduced to below 70% of that observed in the untreated cells. Consequently, beta-D: -glucopyranosyl-(1-->3)-arbutin is a more effective depigmentation agent and is also less cytotoxic than the known melanogenesis inhibitor, arbutin.

Hydrogen production in anaerobic and microaerobic Thermotoga neapolitana.

We have tested the hypothesis (Van Ooteghem et al. Appl Biochem Biotechnol 2002 98-100: 177-189) that microaerobic metabolism may increase the yield of H(2) from the thermophilic bacterium Thermotoga neapolitana. In anaerobic conditions, T. neapolitana converted glucose into acetic acid and lactic acid and yielded 2.4 +/- 0.3 mol H(2) mol(-1) glucose. The bacterium tolerated low O(2) partial pressures but the H(2) yield was not improved under microaerobic conditions. Our results indicate that T. neapolitana only produces H(2) by anaerobic metabolism, and that the yield of H(2) can be maximised by minimising the production of lactic acid.

Screening of thermophilic anaerobic bacteria for solid substrate cultivation on lignocellulosic substrates.

Interest in solid substrate cultivation (SSC) techniques is gaining for biochemical production from renewable resources; however, heat and mass transfer problems may limit application of this technique. The use of anaerobic thermophiles in SSC offers a unique solution to overcoming these challenges. The production potential of nine thermophilic anaerobic bacteria was examined on corn stover, sugar cane bagasse, paper pulp sludge, and wheat bran in submerged liquid cultivation (SmC) and SSC. Production of acetate, ethanol, and lactate was measured over a 10 day period, and total product concentrations were used to compare the performance of different organism-substrate combinations using the two cultivation methods. Overall microbial activity in SmC and SSC was dependent on the organism and growth substrate. Clostridium thermocellum strains JW20, LQRI, and 27405 performed significantly better in SSC when grown on sugar cane bagasse and paper pulp sludge, producing at least 70 and 170 mM of total products, respectively. Growth of C. thermocellum strains in SSC on paper pulp sludge proved to be most favorable, generating at least twice the concentration of total products produced in SmC (p-value < 0.05). Clostridium thermolacticum TC21 demonstrated growth on all substrates producing 30-80 and 60-116 mM of total product in SmC and SSC, respectively. Bacterial species with optimal growth temperatures of 70 degrees C grew best on wheat bran in SmC, producing total product concentrations of 45-75 mM. For some of the organism-substrate combinations total end product concentrations in SSC exceeded those in SmC, indicating that SSC may be a promising alternative for microbial activity and value-added biochemical production.

H(2) production and carbon utilization by Thermotoga neapolitana under anaerobic and microaerobic growth conditions.

H(2) production by Petrotoga miotherma, Thermosipho africanus, Thermotoga elfii, Fervidobacterium pennavorans, and Thermotoga neapolitana was compared under microaerobic conditions. Contrary to these previously reported strains being strict anaerobes, all tested strains grew and produced H(2) in the presence of micromolar levels of O(2). T. neapolitana showed the highest H(2) production under these conditions. Microscopic counting techniques were used to determine growth curves and doubling times, which were subsequently correlated with optical density measurements. The Biolog anaerobic microtiter plate system was used to analyze the carbon source utilization spectrum of T. neapolitana and to select non-metabolized or poorly metabolized carbohydrates as physiological buffers. Itaconic acid was successfully used as a buffer to overcome pH-induced limitations of cell growth and to facilitate enhanced production of CO-free H(2).