934 resultados para AMMONIA-OXIDIZING ARCHAEA


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Hyperammonemia in the brain leads to poorly understood alterations of nitric oxide (NO) synthesis. Arginine, the substrate of nitric oxide synthases, might be recycled from the citrulline produced with NO by argininosuccinate synthetase (AS) and argininosuccinate lyase (AL). The regulation of AS and AL genes during hyperammonemia is unknown in the brain. We used brain cell aggregates cultured from dissociated telencephalic cortex of rat embryos to analyze the regulation of AS and AL genes in hyperammonemia. Using RNase protection assay and non-radioactive in situ hybridization on aggregate cryosections, we show that both AS and AL genes are induced in astrocytes but not in neurons of aggregates exposed to 5 mM NH4Cl. Our work suggests that the hyperammonemic brain might increase its recycling of citrulline to arginine.

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The Virulundo carbonatite in Angola, one of the biggest in the world, contains pyrochlore as an accessory mineral in all of the carbonatite units (calciocarbonatites, ferrocarbonatites, carbonatite breccias, trachytoids). The composition of the primary pyrochlore crystals is very close to fluornatrocalciopyrochlore in all these units. High-temperature hydrothermal processes caused the pseudomorphic replacement of the above crystals by a second generation of pyrochlore, characterized by lower F and Na contents. Low-temperature hydrothermal replacement of the above pyrochlores, associated with production of quartz-carbonates-fluorite veins, controled the development of a third generation of pyrochlore, characterized by high Sr contents. Finally, supergene processes produced the development of a secondary paragenesis in the carbonatite, consisting in late carbonates, goethite, hollandite and REE minerals (mainly synchysite-(Ce), britholite-(Ce), britholite-(La), cerite-(Ce)). Separation of Ce from the other REE was allowed by oxidizing conditions. Therefore, Ce4+ was also incorporated into a late generation of pyrochlore, which is also strongly enriched in Ba and strongly depleted in Ca and Na

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Amino-N is preserved because of the scarcity and nutritional importance of protein. Excretion requires its conversion to ammonia, later incorporated into urea. Under conditions of excess dietary energy, the body cannot easily dispose of the excess amino-N against the evolutively adapted schemes that prevent its wastage; thus ammonia and glutamine formation (and urea excretion) are decreased. High lipid (and energy) availability limits the utilisation of glucose, and high glucose spares the production of ammonium from amino acids, limiting the synthesis of glutamine and its utilisation by the intestine and kidney. The amino acid composition of the diet affects the production of ammonium depending on its composition and the individual amino acid catabolic pathways. Surplus amino acids enhance protein synthesis and growth, and the synthesis of non-protein-N-containing compounds. But these outlets are not enough; consequently, less-conventional mechanisms are activated, such as increased synthesis of NO∙ followed by higher nitrite (and nitrate) excretion and changes in the microbiota. There is also a significant production of N(2) gas, through unknown mechanisms. Health consequences of amino-N surplus are difficult to fathom because of the sparse data available, but it can be speculated that the effects may be negative, largely because the fundamental N homeostasis is stretched out of normalcy, forcing the N removal through pathways unprepared for that task. The unreliable results of hyperproteic diets, and part of the dysregulation found in the metabolic syndrome may be an unwanted consequence of this N disposal conflict.

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The large Cerro de Pasco Cordilleran base metal deposit in central Peru is located on the eastern margin of a middle Miocene diatreme-dome complex and comprises two mineralization stages. The first stage consists of a large pyrite-quartz body replacing Lower Mesozoic Pucara carbonate rocks and, to a lesser extent, diatreme breccia. This body is composed of pyrite with pyrrhotite inclusions, quartz, and black and red chalcedony (containing hypogene hematite). At the contact with the pyrite-quartz body, the diatreme breccia is altered to pyrite-quartz-sericite-pyrite. This body was, in part, replaced by pipelike pyrrhotite bodies zoned outward to carbonate-replacement Zn-Pb ores hearing Fe-rich sphalerite (up to 24 mol % Fes). The second mineralization stage is partly superimposed on the first and consists of zoned east-west-trending Cu-Ag-(Au-Zn-Pb) enargite-pyrite veins hosted in the diatreme breccia in the western part of the deposit and well-zoned Zn-Pb-(Bi-Ag-Cu) carbonate-replacement orebodies; in both cases, sphalerite is Fe poor and the inner parts of the orebodies show typically advanced argillic alteration assemblages, including aluminum phosphate Sulfate (APS) minerals. The zoned enargite-pyrite veins display mineral zoning, from a core of enargite-pyrite +/- alunite with traces of Au, through an intermediate zone of tennantite, chalcopyrite, and Bi minerals to a poorly developed Outer zone hearing sphalerite-galena +/- kaolinite. The carbonate-hosted replacement ores are controlled along N 35 degrees E, N 90 degrees E, N 120 degrees E, and N 170 degrees E faults. They form well-zoned upward-flaring pipelike orebodies with a core of famatinite-pyrite and alunite, an intermediate zone with tetrahedrite-pyrite, chalcopyrite, matildite, cuprobismutite, emplectite, and other Bi minerals accompanied by APS minerals, kaolinite, and dickite, and an outer zone composed of Fe-poor sphalerite (in the range of 0.05-3.5 mol % Fes) and galena. The outermost zone consists of hematite, magnetite, and Fe-Mn-Zn-Ca-Mg carbonates. Most of the second-stage carbonate-replacement orebodies plunge between 25 degrees and 60 degrees to the west, suggesting that the hydrothermal fluids ascended from deeper levels and that no lateral feeding from the veins to the carbonate-replacement orebodies took place. In the Venencocha and Santa Rosa areas, located 2.5 km northwest of the Cerro de Pasco open pit and in the southern part of the deposit, respectively, advanced argillic altered dacitic domes and oxidized veins with advanced argillic alteration halos occur. The latter veins are possibly the oxidized equivalent of the second-stage enargite-pyrite veins located in the western part of the deposit. The alteration assemblage quartz-muscovite-pyrite associated with the pyrite-quartz body suggests that the first stage precipitated at slightly, acidic fin. The sulfide mineral assemblages define an evolutionary path close to the pyrite-pyrrhotite boundary and are characteristic of low-sulfidation states; they suggest that the oxidizing slightly acidic hydrothermal fluid was buffered by phyllite, shale, and carbonate host rock. However, the presence in the pyrite-quartz body of hematite within quartz suggests that, locally, the fluids were less buffered by the host rock. The mineral assemblages of the second mineralization stage are characteristic of high- to intermediate-sulfidation states. High-sulfidation states and oxidizing conditions were achieved and maintained in the cores of the second-stage orebodies, even in those replacing carbonate rocks. The observation that, in places, second-stage mineral assemblages are found in the inner and outer zones is explained in terms of the hydrothermal fluid advancing and waning. Microthermometric data from fluid inclusions in quartz indicate that the different ores of the first mineralization stage formed at similar temperatures and moderate salinities (200 degrees-275 degrees C and 0.2-6.8 wt % NaCl equiv in the pyrite-quartz body; 192 degrees-250 degrees C and 1.1-4.3 wt % NaCl equiv in the pyrrhotite bodies; and 183 degrees-212 degrees C and 3.2-4.0 wt % NaCl equiv in the Zn-Pb ores). These values are similar to those obtained for fluid inclusions in quartz and sphalerite from the second-stage ores (187 degrees-293 degrees C and 0.2-5.2 wt % NaCl equiv in the enargite-pyrite veins: 178 degrees-265 degrees C and 0.2-7.5 wt % NaCl equiv in quartz of carbonate-replacement orebodies; 168 degrees-999 degrees C and 3-11.8 wt % NaCl equiv in sphalerite of carbonate-replacement orebodies; and 245 degrees-261 degrees C and 3.2-7.7 wt % NaCl equiv in quartz from Venencocha). Oxygen and hydrogen isotope compositions oil kaolinite from carbonate-replacement orebodies (delta(18)O = 5.3-11.5%o, delta D = -82 to -114%o) and on alunite from the Venencocha and Santa Rosa areas (delta(18)O = 1.9-6.9%o, delta D = -56 to -73%o). Oxygen isotope compositions of quartz from the first and second stages have 6180 values from 9.1 to 1.7.8 per mil. Calculated fluids in equilibrium with kaolinite have delta(18)O values of 2.0 to 8.2 and delta D values of -69 to -97 per mil; values in equilibrium with alunite are -1.4 to -6.4 and -62 to -79 per mil. Sulfur isotope compositions of sulfides from both stages have a narrow range of delta(34)S values, between -3.7 and +4.2 per mil; values for sulfates from the second stage are between 4.2 and 31.2 per mil. These results define two mixing trends for the ore-forming fluids. The first trend reflects mixing between a moderately saline (similar to 10 wt % NaCl equiv) magmatic end member that had degassed (as indicated by the low delta D values) and meteoric water. The second mixing indicates condensation of magmatic vapor with HCl and SO(2) into meteoric water, which formed alunite. The hydrothermal system at Cerro de Pasco was emplaced at a shallow depth (similar to 500 m) in the epithermal and upper part of a porphyry environment. The similar temperatures and salinities obtained for the first stage and second stages, together with the stable isotope data, indicate that both stages are linked and represent successive stages of epithermal polymetallic mineralization in the upper part of a porphyry system.

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The epithelial sodium channel ENaC is physiologically important in the kidney for the regulation of the extracellular fluid volume, and in the lungs for the maintenance of the appropriate airway surface liquid volume that lines the pulmonary epithelium. Besides the regulation of ENaC by hormones, intracellular factors such as Na(+) ions, pH, or Ca(2+) are responsible for fast adaptive responses of ENaC activity to changes in the intracellular milieu. In this study, we show that ENaC is rapidly and reversibly inhibited by internal sulfhydryl-reactive molecules such as methanethiosulfonate derivatives of different sizes, the metal cations Cd(2+) and Zn(2+), or copper(II) phenanthroline, a mild oxidizing agent that promotes the formation of disulfide bonds. At the single channel level, these agents applied intracellularly induce the appearance of long channel closures, suggesting an effect on ENaC gating. The intracellular reducing agent dithiothreitol fully reverses the rundown of ENaC activity in inside-out patches. Our observations suggest that changes in intracellular redox potential modulate ENaC activity and may regulate ENaC-mediated Na(+) transport in epithelia. Finally, substitution experiments reveal that multiple cysteine residues in the amino and carboxyl termini of ENaC subunits are responsible for this thiol-mediated inhibition of ENaC.

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For the past decade, PET and PET/CT have been widely studied for myocardial perfusion imaging. Several studies demonstrated the incremental value of PET for the diagnostic and prognostic assessment of patients with coronary artery disease. Moreover, PET allows for non-invasively quantifying myocardial blood flow and myocardial flow reserve, that both are recognized as surrogate marker of cardiac event free survival. By enabling the exploration of epicardial disease and the microvasculature, PET constitutes a unique tool to study pathophysiogical mechanisms leading to atherosclerosis genesis. The recent emergence of high-tech hybrid machines may even provide further incremental information about coronary function and morphology. By taking the best of each modality, a better assessment of patients with coronary artery disease is expected. (C) 2011 Elsevier Masson SAS. All rights reserved.

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The Liesberg Beds form the transition between the lower Oxfordian dark coloured marls (Renggeri Member and the Terrain a Chailles Member) and the middle Oxfordian reefal limestones (St-Ursanne Formation). Both lithofacies and biofacies are diverse and evolve rapidly up-section. Stable isotope studies of whole-rock samples are therefore excluded. In search for a convenient isotopic marker, we measured carbon isotope compositions of several fossil groups and chose crinoid stems of Millericrinus spp and echinoid spines of Paracidaris spp because of their abundance throughout the section and the small variations of delta(13)C within one fossil and between fossils from the same stratigraphic level. The delta(13)C values of echinoderms largely reflect earliest diagenetic conditions at the seawatersediment interface. The porous stereome structure secreted of high Mg-calcite by echinoderms has a high reactive surface/volume ratio, which triggers the precipitation of very early syntaxial cements. In the four studied sections reproducible carbon isotope shifts were observed both for Millericrinus spp stems and Paracidaris spp spines. A negative delta(13)C shift of 1-1.5 parts per thousand was observed near the base of the section, just above the transition from Terrain a Chailles Member, where the first corals occur. In the middle and upper part of the four sections, characterised by a stepwise increase of corals and the macrofossils, a positive delta(13)C Shift of about 2 parts per thousand was observed. Despite the highly variable lithologic composition of the Liesberg Beds;Member, carbon isotope shifts seem to be consistent and warrant an interpretation as an original signal, controlled by the isotopic composition of dissolved carbonic acid in seawater. We explain the heavy delta(13)C values (approximate to 2-2.3 parts per thousand) in the lower Liesberg Beds as a transition from an oxygen-limited environment (Terrain a Chailles Member) to the Liesberg Beds Member. The lowest delta(13)C values (approximate to 1-1.5 parts per thousand) correspond to a large input of dissolved nutrients to the platform under oxidizing conditions. The ensuing positive shift (between 2.5 and 3.5 parts per thousand), however, seems to correspond to a general trend of opening up of the platform and connection to open marine waters. Positive delta(13)C values in the upper Liesberg Beds is interpreted as a result of important accelareted extraction of organic carbon from the ocean reservoir, that occurred possibly during periods of warm and humid climate.

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BACKGROUND: The thiomethyl group of S-adenosylmethionine is often recycled as methionine from methylthioadenosine. The corresponding pathway has been unravelled in Bacillus subtilis. However methylthioadenosine is subjected to alternative degradative pathways depending on the organism. RESULTS: This work uses genome in silico analysis to propose methionine salvage pathways for Klebsiella pneumoniae, Leptospira interrogans, Thermoanaerobacter tengcongensis and Xylella fastidiosa. Experiments performed with mutants of B. subtilis and Pseudomonas aeruginosa substantiate the hypotheses proposed. The enzymes that catalyze the reactions are recruited from a variety of origins. The first, ubiquitous, enzyme of the pathway, MtnA (methylthioribose-1-phosphate isomerase), belongs to a family of proteins related to eukaryotic intiation factor 2B alpha. mtnB codes for a methylthioribulose-1-phosphate dehydratase. Two reactions follow, that of an enolase and that of a phosphatase. While in B. subtilis this is performed by two distinct polypeptides, in the other organisms analyzed here an enolase-phosphatase yields 1,2-dihydroxy-3-keto-5-methylthiopentene. In the presence of dioxygen an aci-reductone dioxygenase yields the immediate precursor of methionine, ketomethylthiobutyrate. Under some conditions this enzyme produces carbon monoxide in B. subtilis, suggesting a route for a new gaseous mediator in bacteria. Ketomethylthiobutyrate is finally transaminated by an aminotransferase that exists usually as a broad specificity enzyme (often able to transaminate aromatic aminoacid keto-acid precursors or histidinol-phosphate). CONCLUSION: A functional methionine salvage pathway was experimentally demonstrated, for the first time, in P. aeruginosa. Apparently, methionine salvage pathways are frequent in Bacteria (and in Eukarya), with recruitment of different polypeptides to perform the needed reactions (an ancestor of a translation initiation factor and RuBisCO, as an enolase, in some Firmicutes). Many are highly dependent on the presence of oxygen, suggesting that the ecological niche may play an important role for the existence and/or metabolic steps of the pathway, even in phylogenetically related bacteria. Further work is needed to uncover the corresponding steps when dioxygen is scarce or absent (this is important to explore the presence of the pathway in Archaea). The thermophile T. tengcongensis, that thrives in the absence of oxygen, appears to possess the pathway. It will be an interesting link to uncover the missing reactions in anaerobic environments.

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Tehokkain tapavalkaista mekaanisesti kuidutettua puumassaa on suorittaa se hapettavasti peroksidikemikaalilla vahvasti alkalisissa oloissa. Perinteisesti alkalisuus on aikaansaatu natriumhydroksidin ja -silikaatin avulla. Se kuitenkin liuottaa massasta merkittävästi ligniiniä, mikä huonontaa saantoa ja suurentaa valkaisun jätevesien orgaanisen hiilen määrää sekä kemiallista hapenkulutusta. Yhä kovenevien vaaleustavoitteiden ja tiukentuneen vedenkäytön seurauksena on syntynyt tarve etsiä parempia valkaisun alkaleja. Kirjallisuuden pohjalta valittiinkokeellisesti tutkittaviksi alkaleiksi magnesiumhydroksidi, magnesiumoksidi, kalsiumhydroksidi sekä kalsiumoksidi. Niiden toimivuutta hapettavan vetyperoksidivalkaisun alkaleina tutkittiin valkaisukokein natriumsilikaattilisäyksen kanssa sekä ilman. Näistä parhaiten toimivaksi osoittautui Mg(OH)2. Sen avulla suoritettiin jatkoksi laboratoriokoevalkaisuja korkeassa sakeudessa. Keski- ja korkeasakeusvalkaisukokeiden tulosten mukaan käytettäessä Mg(OH)2 -alkalia natriumydroksidin ja -silikaatin asemesta jää massan loppuvaaleus noin yhden ISO-prosentin verran heikommaksi. Tällöin valkaisusuodoksessa oli vain varsin vähäinen määrä massasta liuennutta orgaanista hiiliainesta, noin 45 % siitä, mitä natriumin yhdisteiden käyttö vertailukokeessa tuotti. Tulosta varmennettiin suorittamalla korkea-sakeusvalkaisukokeita hiokemassatehtaan olosuhteissa, massoilla ja kiertovesillä.Myös tehdaskokeiden mukaan valkaistun massan loppuvaaleus jää noin yhden ISO-prosentin alhaisemmaksi, mutta valkaisusuodoksen orgaanisen hiilen määrä (TOC) jääalle puoleen Na-kemikaalein suoritetusta vertailukokeesta.

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Työssä tutkittiin kaksivaiheisen typenpoistoprosessin (2-N-PRO) soveltuvuutta Joutsenon Kukkuroinmäen aluejätekeskuksen kompostointilaitoksen jätevesille pilot-kokein 12.1.- 5.4.2006. Kompostilaitoksella on jätevesien esikäsittelytarve korkeista ammoniumtyppipitoisuuksista johtuen. Pilot-laitteisto koostuu sekoitussäiliöstä, strippaustornista ja katalyyttipolttimesta. Käsiteltävän jäteveden pH nostetaan korkealle tasolle, jolloin ammoniumtyppi muuttuu ammoniakiksi. Vesi johdetaan strippaustorniin, jossa se sadetetaan tornin pohjalle. Ammoniakki erottuu sadetuksessa ilmaan, joka imetään katalyyttipolttimelle. Katalyyttinen poltin käsittelee ammoniakkia typpikaasuksi. Pilot-kokeet suoritettiin jatkuvatoimisesti. Laitteisto pystyy erottamaan jätevedestä ammoniumtyppeä ammoniakiksi ja käsittelemään ammoniakin pääosin typpikaasuksi. Lisäksi suoritettiin panoskoe, jonka tulokset tukevat jatkuvatoimisesta käytöstä saatuja tuloksia.

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The solid-rotor induction motor provides a mechanically and thermally reliable solution for demanding environments where other rotor solutions are prohibited or questionable. Solid rotors, which are manufactured of single pieces of ferromagnetic material, are commonly used in motors in which the rotationspeeds exceed substantially the conventional speeds of laminated rotors with squirrel-cage. During the operation of a solid-rotor electrical machine, the rotor core forms a conductor for both the magnetic flux and the electrical current. This causes an increase in the rotor resistance and rotor leakage inductance, which essentially decreases the power factor and the efficiency of the machine. The electromagnetic problems related to the solid-rotor induction motor are mostly associated with the low performance of the rotor. Therefore, the main emphasis in this thesis is put on the solid steel rotor designs. The rotor designs studied in thisthesis are based on the fact that the rotor construction should be extremely robust and reliable to withstand the high mechanical stresses caused by the rotational velocity of the rotor. In addition, the demanding operation environment sets requirements for the applied materials because of the high temperatures and oxidizing acids, which may be present in the cooling fluid. Therefore, the solid rotors analyzed in this thesis are made of a single piece of ferromagnetic material without any additional parts, such as copper end-rings or a squirrel-cage. A pure solid rotor construction is rigid and able to keep its balance over a large speed range. It also may tolerate other environmental stresses such as corroding substances or abrasive particles. In this thesis, the main target is to improve the performance of an induction motor equipped with a solid steel rotor by traditional methods: by axial slitting of the rotor, by selecting a proper rotor core material and by coating the rotor with a high-resistive stainless ferromagnetic material. In the solid steel rotor calculation, the rotor end-effects have a significant effect on the rotor characteristics. Thus, the emphasis is also put on the comparison of different rotor endfactors. In addition, a corrective slip-dependent end-factor is proposed. The rotor designs covered in this thesis are the smooth solid rotor, the axially slitted solid rotor and the slitted rotor having a uniform ferromagnetic coating cylinder. The thesis aims at design rules for multi-megawatt machines. Typically, mega-watt-size solidrotor machines find their applications mainly in the field of electric-motor-gas-compression systems, in steam-turbine applications, and in various types of largepower pump applications, where high operational speeds are required. In this thesis, a 120 kW, 10 000 rpm solid-rotor induction motor is usedas a small-scale model for such megawatt-range solid-rotor machines. The performance of the 120 kW solid-rotor induction motors is determined by experimental measurements and finite element calculations.

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Background: Protein domains represent the basic units in the evolution of proteins. Domain duplication and shuffling by recombination and fusion, followed by divergence are the most common mechanisms in this process. Such domain fusion and recombination events are predicted to occur only once for a given multidomain architecture. However, other scenarios may be relevant in the evolution of specific proteins, such as convergent evolution of multidomain architectures. With this in mind, we study glutaredoxin (GRX) domains, because these domains of approximately one hundred amino acids are widespread in archaea, bacteria and eukaryotes and participate in fusion proteins. GRXs are responsible for the reduction of protein disulfides or glutathione-protein mixed disulfides and are involved in cellular redox regulation, although their specific roles and targets are often unclear. Results: In this work we analyze the distribution and evolution of GRX proteins in archaea,bacteria and eukaryotes. We study over one thousand GRX proteins, each containing at least one GRX domain, from hundreds of different organisms and trace the origin and evolution of the GRX domain within the tree of life. Conclusion: Our results suggest that single domain GRX proteins of the CGFS and CPYC classes have, each, evolved through duplication and divergence from one initial gene that was present in the last common ancestor of all organisms. Remarkably, we identify a case of convergent evolution in domain architecture that involves the GRX domain. Two independent recombination events of a TRX domain to a GRX domain are likely to have occurred, which is an exception to the dominant mechanism of domain architecture evolution.

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Background: Bacterial populations are highly successful at colonizing new habitats and adapting to changing environmental conditions, partly due to their capacity to evolve novel virulence and metabolic pathways in response to stress conditions and to shuffle them by horizontal gene transfer (HGT). A common theme in the evolution of new functions consists of gene duplication followed by functional divergence. UlaG, a unique manganese-dependent metallo-b-lactamase (MBL) enzyme involved in L-ascorbate metabolism by commensal and symbiotic enterobacteria, provides a model for the study of the emergence of new catalytic activities from the modification of an ancient fold. Furthermore, UlaG is the founding member of the so-called UlaG-like (UlaGL) protein family, a recently established and poorly characterized family comprising divalent (and perhaps trivalent)metal-binding MBLs that catalyze transformations on phosphorylated sugars and nucleotides. Results: Here we combined protein structure-guided and sequence-only molecular phylogenetic analyses to dissect the molecular evolution of UlaG and to study its phylogenomic distribution, its relatedness with present-day UlaGL protein sequences and functional conservation. Phylogenetic analyses indicate that UlaGL sequences are present in Bacteria and Archaea, with bona fide orthologs found mainly in mammalian and plant-associated Gramnegative and Gram-positive bacteria. The incongruence between the UlaGL tree and known species trees indicates exchange by HGT and suggests that the UlaGL-encoding genes provided a growth advantage under changing conditions. Our search for more distantly related protein sequences aided by structural homology has uncovered that UlaGL sequences have a common evolutionary origin with present-day RNA processing and metabolizing MBL enzymes widespread in Bacteria, Archaea, and Eukarya. This observation suggests an ancient origin for the UlaGL family within the broader trunk of the MBL superfamily by duplication, neofunctionalization and fixation. Conclusions: Our results suggest that the forerunner of UlaG was present as an RNA metabolizing enzyme in the last common ancestor, and that the modern descendants of that ancestral gene have a wide phylogenetic distribution and functional roles. We propose that the UlaGL family evolved new metabolic roles among bacterial and possibly archeal phyla in the setting of a close association with metazoans, such as in the mammalian gastrointestinal tract or in animal and plant pathogens, as well as in environmental settings. Accordingly, the major evolutionary forces shaping the UlaGL family include vertical inheritance and lineage-specific duplication and acquisition of novel metabolic functions, followed by HGT and numerous lineage-specific gene loss events.

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Tässä työssä Oy Keskuslaboratoriossa sijaitsevalla kiertovesisimulaattorilla on tutkittiu ditioniittivalkaisun ja hylyn määrän vaikutusta pH:n stabiilisuuteen ja häiriöaineiden määrään neutraalissa LWC-prosessissa. Lisäksi on tutkittu ditioniitin määrän seisokkien ja valkaisuviiveiden vaikutusta. Kirjallisuusosassa tutustutaan ditioniittivalkaisuun ja valkaisun kemiaan sekä kalsiumkarbonaatin liukenemiseen. Lyhyesti selvitetään myös paperikoneen vesikiertoja sekä prosessissa olevia häiriöaineita. Karbonaatin liukenemisen osalta tarkastellaan myös mahdollisuutta mallintaa prosessia. Diplomityön aikana ajettiin yhdeksän simulaattoriajoa, jotka ajettiin kahden tai kolmen ajon sarjoissa. Ajoja ajettiin kolmella eri hylkymäärällä. Ditioniittivalkaisun lisäksi suoritettiin referenssiajoja ilman valkaisua. Lyhyen kierron pH pyrittiin pääosin säätämään seitsemään. Valkaisuviiveiden ja yli-yön kestävien seisokkien vaikutusta tutkittiin myös. Kokeissa todettiin ditioniitin alentavan pH tasoa. Tämä pH:n aleneminen johtaa kalsiumkarbonaatin liukenemiseen kalsiumkarbonaatin pyrkiessä puskuroimaan pH:n laskua. Valkaisureaktiossa syntyy negatiivisesti varauruneita yhdisteitä, jotka lisäävät prosessin anionisuutta. Ditioniitin valkaisuvaikutus näkyi lopputuotteen vaaleuden kasvuna sekä kieroveden värillisten yhdisteiden vähenemisenä. Ditioniittivalkaisu näytti poistavan myös noin 30% ligniinistä. Lipofiilisiin uuteaineisiin ditioniitilla ei ollut vaikutusta. Riittävä ditioniittiannos kokeiden perusteella on korkeintaan 1% ditioniittiä käytetyn mekaanisen massan määrästä. Korkeammalla annostuksella ei ollut vaikutusta vaaleuteen. Valkaisuaikana 30 minuuttia on riittävä. Pidempien valkaisuviiveiden ja seisokkien aikana valkaisussa syntyvän sulfiitin todettiin muuttuvan sulfaatiksi. Hylyn määrän lisääminen nosti pH:ta, varausta, johtokykyä ja liuenneen kalsiumin määrään. Hylyn määrän lisäminen paransi myös optisia ominaisuuksia, mikä johtui osin hylyn sisältämästä kalsiumkarbonaatista ja osin hylyn sisältämästä mekaanisesta massasta, joka oli valkaistua.

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Diplomityössä kehitettiin ioninvaihtoon perustuva ammoniakin talteenottoprosessi NSSC (Neutral Sulphite Semi Chemical) -prosessin haihduttamon lauhteille. Tarkoituksena oli saada aallotuskartonkitehtaan kemi-kaalikiertoa suljettua ja sitä kautta ammoniakkipäästöjä vähennettyä. Ammoniakki tuli ottaa hyötymuodossa (ammoniakkihöyry tai ammoniumsulfiitti) talteen. Ammoniumsulfiittiliuosta käytetään NSSC-prosessissa keittonesteenä. Kirjallisuusosassa selvitetään strippaukseen perustuvia ammoniakin talteenottomahdollisuuksia. Tutkitaan ioninvaihdon teoriaa ja ammoniumin talteenottoon sopivien ioninvaihtomateriaalien ominaisuuksia ioninvaihtajina. Lisäksi esitetään ioninvaihtoprosesseihin liittyviä laitteistoratkaisuja ja prosessiolosuhteita. Työn kokeellisessa osassa on yleiskuvaus Powerflute Oy Savon Sellun prosesseista ja selvitetään ammoniakin merkitystä tehtaalle. Laboratoriokokein tutkittiin orgaanisten kationihartsien sekä epäorgaanisen luonnon zeoliitin soveltuvuutta ammoniumionien vaihtoon esihaihduttamon lauhteesta. Ammoniakin talteenottoprosessin toimivuutta teollisessa mittakaavassa selvitettiin rakennetulla pilotlaitteistolla suoritettujen kokeiden avulla. Lopuksi tehtiin ammoniakin talteenottoprosessin scale-up: laskettiin prosessin talteenottokapasiteetti, arvioitiin kustannuksia sekä annettiin lausunto prosessin toteutettavuudesta. Laboratoriokokeiden perusteella luonnon zeoliitti ja heikosti hapan ioninvaihtohartsi eivät sovellu ammoniumionien vaihtoon NSSC haihduttamon lauhteista. Vahvasti hapan kationihartsi toimi ammoniumin talteenotossa parhaiten, joten se valittiin pilotkokeiden ioninvaihtomateriaaliksi. Pilotkokeissa ioninvaihtomateriaaliin saatiin sidottua ammoniumia noin 30 g NH4+ / dm3 hartsia, kun materiaalin teoreettinen ioninvaihtokapasiteetti oli 32 g NH4+ / dm3 hartsia. Ammoniumin läpäisykäyrien muotoon vaikutti suuresti syöttölauhteen virtausnopeus ja ammoniumpitoisuus. Ioninvaihtomateriaalipedin syvyydellä ei ollut niinkään merkitystä. Pilotkokeiden regenerointitavoista tehokkaimmaksi osoittautui höyrystrippaus, jossa saavutettiin noin 90 %:n talteenottotehokkuus. Rikkihapokekäsittelyllä talteenottotehokkuus jäi 50 %:iin. Teollisen mittakaavan laitoksella voidaan vuosittain regenerointitavasta riippuen ottaa talteen esihaihdut-tamon lauhteesta noin 100-150 tonnia ammoniakkia. Prosessin käyttökustannukset ovat talteenotetusta ammoniakista saataviin säästöihin verrattuna suuret ja niihin vaikuttaa merkittävästi ioninvaihtohartsin käyttöikä sekä regenerointikemikaalien kulutus. Osittaisella kemikaalikierron sulkemisella saavutetaan NSSC-prosessissa sekundäärietuja, joiden vaikutuksen merkittävyys pitäisi tarkentaa lisätutkimuksilla.