Em uma fábrica de celulose, a maioria da hemicelulose é dissolvida no licor negro e se queima no processo de recuperação de álcalis. Devido a isto, a reposição das hemiceluloses dissolvidas de volta à fibra é uma das alternativas para a retenção de hemicelulose nas polpas, o que aumenta o rendimento do processo e produz polpas de alta qualidade. O Brasil é o maior produção de cana-de-açúcar do mundo, o bagaço gerado em grande quantidade constitui uma potencial fonte barata e abundante de hemicelulose para uso em processos biotecnológicos. O aproveitamento desta fração do material lignocelulósico pode aumentar o valor comercial do bagaço de cana-de-açúcar. Nesse estudo, extraiu-se enzimaticamente a hemicelulose do bagaço visando utilizá-la como aditivos na indústria de papel e celulose. Inicialmente, o bagaço foi pré-tratado pelo processo quimiotermomecânico, em solução sulfito alcalino (10% Na2SO3 e 5% NaOH), 120 oC, 2 h. O pré-tratamento removeu 49,1% de lignina e 16,1% de xilana do bagaço, houve uma pequena solubilização de glucana (9,0%) e alto rendimento de sólidos (73,6%). A extração enzimática das xilanas a partir do bagaço pré-tratado foi feita com 5 UI de xilanase comercial (Luminase) por grama de material, em tampão fosfato 50 mM, 50 ºC, pH 8 por 6 e 24 horas, obtendo-se 15% e 28% de rendimento de xilana, respectivamente, determinada quimicamente pelos conteúdos de xilose e arabinose. As xilanas solubilizadas do bagaço pré-tratado com a xilanase comercial por 6 horas foram precipitadas em 15% e 30% de etanol. Recuperou-se 2 frações, denominadas Xilanas 1 e 2, que apresentaram massas molares médias de 34.180 g/mol e 28.130 g/mol, respectivamente, e grau de substituição mais elevado (0,16-0,19). O restante do material foi concentrado e denominado Xilana 3. As xilanas extraídas enzimaticamente por 24 horas foram liofilizadas e denominada Xilana 4. As Xilanas 3 e 4 possuem características semelhantes, como baixas massas molares (2.890-3.660 g/mol) e graus de substituição (0,13-0,14), porém com grandes quantidades de impurezas. As xilanas obtidas foram submetidas ao processo de adsorção em polpas celulósicas \"kraft\" de eucalipto, marrom e deslignificada, em pH 10, consistência de 5% (m/v) e 10% de relação xilana/celulose (m/m). A adsorção em celulose ocorreu para as xilanas com menor grau de substituição e o aumento da concentração de xilanas com menores massas molares aumentou as taxas de adsorção. Em função desses resultados, conclui-se que a extração enzimática de bagaço de cana-de-açúcar pré-tratado quimiotermomecanicamente com sulfito alcalino produziu majoritariamente xilanas de baixa massa molar e pouco substituídas, que foram eficientes durante processo de adsorção à polpa celulósica e podem ser exploradas para redeposição em polpa celulósica visando melhorar as características da fibra e aumentar o rendimento do processo. / In a celulose pulp factory, most of the hemicellulose are dissolved in the black liquor and burn in the alkali recovery process. For this reason, the replacement of the dissolved hemicelluloses back to the fiber is one of the alternatives for the retention of hemicellulose in the pulps, which increases the yield of the process and produces high quality pulps. Brazil has the largest sugarcane crop in the world, the bagasse generated in large quantities constitutes a potential cheap and abundant source of hemicellulose for use in biotechnological processes. The utilization of this fraction of the lignocellulosic material can increase the commercial value of sugarcane bagasse. In this study, hemicellulose was extracted enzymatically from the bagasse to be used as additives in the pulp and paper industry. Initially, the bagasse was pretreated by the chemothermomechanical process, in alkaline sulfite solution (10% Na2SO3 and 5% NaOH), 120 ?, 2h. The pretreatment removed 49.1% of lignin and 16.1% of xylan from the bagasse, there was a small solubilization of glucan (9.0%) and high solids yield (73.6%). Enzymatic extraction of xylan from pretreated bagasse was made with 5 IU of commercial xylanase (Luminase) per gram of material, in 50 mM phosphate buffer, 50 °C, pH 8 by 6 and 24 hours, obtaining 15% and 28% xylan yield, respectively, determined chemically by the contents of xylose and arabinose. The solubilized xylans of pre-treated bagasse with the commercial xylanase for 6 hours were precipitated in 15% and 30% ethanol. Two fractions, named Xylans 1 and 2, were recovered, having average molar masses of 34.180 g/mol and 28.130 g/mol, respectively, and a higher degree of substitution (0,16-0,19). The remainder material was concentrated and named Xylan 3. Xylans extracted enzymatically for 24 hours were lyophilized and named Xylan 4. Xylans 3 and 4 had the same similar characteristics as low molar masses (2.890-3.660 g / mol) and degrees of substitution (0,12-0,14), but with large amounts of impurities. The xylans were submitted to the adsorption process in cellulosic pulps of eucalyptus, brown and delignified, in pH 10, consistency of 5% (m/v) and 10% ratio xylan mass/cellulose mass (m/m). The adsorption in cellulose occurred for the xylan with lower degree of substitution and the increase of the xylan concentration with smaller molar masses increased the adsorption rates. Based on the results, it was concluded that the enzymatic extraction of sugarcane bagasse pretreated chemothermically with alkali sulphite produced mainly xylans of low molar mass and degree of substitution, which were efficient during the adsorption process to the cellulosic pulp and can be used for redeposition in cellulosic pulp in order to improve the characteristics of the fiber and increase the process yield.

Em uma fábrica de celulose, a maioria da hemicelulose é dissolvida no licor negro e se queima no processo de recuperação de álcalis. Devido a isto, a reposição das hemiceluloses dissolvidas de volta à fibra é uma das alternativas para a retenção de hemicelulose nas polpas, o que aumenta o rendimento do processo e produz polpas de alta qualidade. O Brasil é o maior produção de cana-de-açúcar do mundo, o bagaço gerado em grande quantidade constitui uma potencial fonte barata e abundante de hemicelulose para uso em processos biotecnológicos. O aproveitamento desta fração do material lignocelulósico pode aumentar o valor comercial do bagaço de cana-de-açúcar. Nesse estudo, extraiu-se enzimaticamente a hemicelulose do bagaço visando utilizá-la como aditivos na indústria de papel e celulose. Inicialmente, o bagaço foi pré-tratado pelo processo quimiotermomecânico, em solução sulfito alcalino (10% Na2SO3 e 5% NaOH), 120 oC, 2 h. O pré-tratamento removeu 49,1% de lignina e 16,1% de xilana do bagaço, houve uma pequena solubilização de glucana (9,0%) e alto rendimento de sólidos (73,6%). A extração enzimática das xilanas a partir do bagaço pré-tratado foi feita com 5 UI de xilanase comercial (Luminase) por grama de material, em tampão fosfato 50 mM, 50 ºC, pH 8 por 6 e 24 horas, obtendo-se 15% e 28% de rendimento de xilana, respectivamente, determinada quimicamente pelos conteúdos de xilose e arabinose. As xilanas solubilizadas do bagaço pré-tratado com a xilanase comercial por 6 horas foram precipitadas em 15% e 30% de etanol. Recuperou-se 2 frações, denominadas Xilanas 1 e 2, que apresentaram massas molares médias de 34.180 g/mol e 28.130 g/mol, respectivamente, e grau de substituição mais elevado (0,16-0,19). O restante do material foi concentrado e denominado Xilana 3. As xilanas extraídas enzimaticamente por 24 horas foram liofilizadas e denominada Xilana 4. As Xilanas 3 e 4 possuem características semelhantes, como baixas massas molares (2.890-3.660 g/mol) e graus de substituição (0,13-0,14), porém com grandes quantidades de impurezas. As xilanas obtidas foram submetidas ao processo de adsorção em polpas celulósicas \"kraft\" de eucalipto, marrom e deslignificada, em pH 10, consistência de 5% (m/v) e 10% de relação xilana/celulose (m/m). A adsorção em celulose ocorreu para as xilanas com menor grau de substituição e o aumento da concentração de xilanas com menores massas molares aumentou as taxas de adsorção. Em função desses resultados, conclui-se que a extração enzimática de bagaço de cana-de-açúcar pré-tratado quimiotermomecanicamente com sulfito alcalino produziu majoritariamente xilanas de baixa massa molar e pouco substituídas, que foram eficientes durante processo de adsorção à polpa celulósica e podem ser exploradas para redeposição em polpa celulósica visando melhorar as características da fibra e aumentar o rendimento do processo. / In a celulose pulp factory, most of the hemicellulose are dissolved in the black liquor and burn in the alkali recovery process. For this reason, the replacement of the dissolved hemicelluloses back to the fiber is one of the alternatives for the retention of hemicellulose in the pulps, which increases the yield of the process and produces high quality pulps. Brazil has the largest sugarcane crop in the world, the bagasse generated in large quantities constitutes a potential cheap and abundant source of hemicellulose for use in biotechnological processes. The utilization of this fraction of the lignocellulosic material can increase the commercial value of sugarcane bagasse. In this study, hemicellulose was extracted enzymatically from the bagasse to be used as additives in the pulp and paper industry. Initially, the bagasse was pretreated by the chemothermomechanical process, in alkaline sulfite solution (10% Na2SO3 and 5% NaOH), 120 ?, 2h. The pretreatment removed 49.1% of lignin and 16.1% of xylan from the bagasse, there was a small solubilization of glucan (9.0%) and high solids yield (73.6%). Enzymatic extraction of xylan from pretreated bagasse was made with 5 IU of commercial xylanase (Luminase) per gram of material, in 50 mM phosphate buffer, 50 °C, pH 8 by 6 and 24 hours, obtaining 15% and 28% xylan yield, respectively, determined chemically by the contents of xylose and arabinose. The solubilized xylans of pre-treated bagasse with the commercial xylanase for 6 hours were precipitated in 15% and 30% ethanol. Two fractions, named Xylans 1 and 2, were recovered, having average molar masses of 34.180 g/mol and 28.130 g/mol, respectively, and a higher degree of substitution (0,16-0,19). The remainder material was concentrated and named Xylan 3. Xylans extracted enzymatically for 24 hours were lyophilized and named Xylan 4. Xylans 3 and 4 had the same similar characteristics as low molar masses (2.890-3.660 g / mol) and degrees of substitution (0,12-0,14), but with large amounts of impurities. The xylans were submitted to the adsorption process in cellulosic pulps of eucalyptus, brown and delignified, in pH 10, consistency of 5% (m/v) and 10% ratio xylan mass/cellulose mass (m/m). The adsorption in cellulose occurred for the xylan with lower degree of substitution and the increase of the xylan concentration with smaller molar masses increased the adsorption rates. Based on the results, it was concluded that the enzymatic extraction of sugarcane bagasse pretreated chemothermically with alkali sulphite produced mainly xylans of low molar mass and degree of substitution, which were efficient during the adsorption process to the cellulosic pulp and can be used for redeposition in cellulosic pulp in order to improve the characteristics of the fiber and increase the process yield.

Para diminuir o consumo dos combustíveis fósseis, que são os principais agentes intensificadores do efeito estufa, muitas pesquisas estão sendo realizadas para aumentar a produção de etanol, com ênfase no etanol produzido a partir de materiais lignocelulósicos. Dentre as etapas necessárias para esse processo, uma delas é a hidrólise enzimática da celulose a monômeros solúveis. No entanto, a parede celular das plantas é recalcitrante e de difícil acesso às enzimas. Diante disto, neste trabalho propôs-se tratar bagaços de cana-de-açúcar com diferentes concentrações de solução sulfito em meio alcalino, para solubilizar lignina e hemicelulose e favorecer o acesso das enzimas ao substrato. As amostras, obtidas de cultivares de cana-de-açúcar com teores reduzidos de lignina e de uma variedade comercial, foram submetidas ao processo quimio-mecânico por 2 horas, a 121oC, com soluções de hidróxido de sódio (2,5%, 3,75% e 5% m/m) e sulfito de sódio (5%, 7,5% e 10% m/m), combinadas na proporção de 1:2, respectivamente. Análises físico-químicas dos materiais pré-tratados, como quantificação dos grupos sulfônicos e capacidade de retenção de água (WRV), também foram realizadas. Conforme se empregou maior concentração de reagentes no pré-tratamento, mais eficientes foram as remoções de lignina e hemicelulose, favorecendo maiores conversões enzimáticas. A remoção de lignina, embora contribua para o acesso das enzimas ao substrato, não foi o único fator necessário para se alcançar os maiores rendimentos de açúcares. Nesse caso, o efeito da sulfonação foi essencial para melhores conversões. Os resultados de WRV não apresentaram correlação com os níveis de hidrólise, pois é provável que as fibras pré-tratadas tenham atingido seu ponto de saturação. O maior rendimento de hidrólise da celulose foi de 92% para o cultivar 58 (após 96 horas de reação), que associou o efeito da deslignificação (53,5%) com alta incorporação de sulfito (600 mmol/Kg de lignina). Todos os bagaços com menor conteúdo inicial de lignina apresentaram maiores velocidades iniciais de hidrólise, quando comparados com a variedade comercial. Dessas amostras, destacou-se o cultivar 146, que necessitou apenas de 8 horas de reação para estabelecer o patamar de conversão de celulose de 75%. Todos os cultivares foram mais eficientes que a variedade comercial, demandando menor concentração de reagentes químicos para atingir 50% de conversão de celulose, em 24 horas. Foi avaliada a diminuição de quatro vezes na carga de SO32- no pré-tratamento do cultivar 58, em que se empregou 2,5% de sulfito e 5% de NaOH, em tempos de cozimento correspondentes a 30, 60 e 120 minutos. Nesse sentido, observou-se que a maior proporção de íons OH- no meio reacional não resultou em rendimentos satisfatórios de hidrólise, devido à maior perda de hemicelulose e menor remoção de lignina, quando comparado ao mesmo processo utilizando 10% de sulfito. Para o maior tempo de pré-tratamento foi possível obter maiores rendimentos de hidrólise, pois a incorporação de sulfito e remoção de componentes aumentou com o tempo. Portanto, o efeito da sulfonação, em 2 horas de pré-tratamento, foi mais importante que a deslignificação total das amostras na conversão dos polissacarídeos do bagaço em açúcares fermentescíveis. / In order to reduce the consumption of fossil fuels, which are the main cause of the greenhouse effect, many studies are being undertaken to increase ethanol production through the use of lignocellulosic material. One of the steps in this process is enzymatic hydrolysis of the cellulose into monomers. However, the plant cell walls are recalcitrant and inaccessible to the enzymes. Thus, this study aims to treat sugar cane bagasse with different sulfite alkaline concentrations in order to dissolve lignin and hemicellulose and enable the enzymes access to the substrate. The samples, obtained from sugar cane hybrids with reduced lignin content along with a commercial variety, were submitted to a chemical-mechanical process for 2 hours at 121°C, with sodium hydroxide solutions (2.5%, 3.75% and 5% m/m) and sodium sulfite (5%, 7.5% and 10% m/m), combined in a 1:2 ratio, respectively. Furthermore, physical and chemical analyses, such as water retention value and sulfonic group measurement, were carried out. The greater reactants concentration in the pretreatment, the more efficient the lignin and hemicelullose removal was, therefore enabling greater enzymatic conversions. Although lignin removal augments enzyme access to the substrate, this was not the only factor necessary to reach better conversion rates. In this case, the effect of sulfonation was essential for better conversions. The water retention value did not present correlation with the hydrolysis levels, suggesting that the pre-treated fibers had already reached their saturation point. The greatest cellulose hydrolysis yield was 92% for hybrid 58 (after 96 hours of reaction), which is associated with the effect of delignification (53.5%) with high sulfite incorporation (600 mmol/Kg of lignin). All of the bagasse varieties with less initial lignin content presented greater initial hydrolysis velocities when compared to the commercial variety. Of these samples, the hybrid 146 stood out, since only 8 hours was needed to reach the cellulosic conversion plateau of 75%. All of the hybrids were more efficient than the commercial variety, as they required less chemical reactants to reach 50% cellulosic conversions in 24 hours. The charge of SO32- was reduced 75% for the pretreatment using 2.5% sulfite and 5% NaOH with hybrid 58 for reaction times of 30, 60 and 120 minutes. It was observed that a greater proportion of OH- ions did not lead to satisfactory hydrolysis yields due to the greater loss in hemicellulose and the great lignin removal when compared to the same treatment utilizing 10% sulfite. The greater hydrolysis yield was obtained through the longest period of pretreatment, because in this condition the sulfite incorporation and removal of components increased. Thus, the effect of sulfonation, in 2 hours of pretreatment was more important in the conversion of the bagasse polysacharides in fermentable sugars than the total delignification of the samples.

A autoxidação dos complexos de Ni(II) e Co(II) com tetra, penta e hexaglicina, em meio de tampão borato, é acelerada por espécies de enxofre (IV) (H2S0<SUB3, HS03-e SO32-). A formação dos complexos de Ni(III) e Co(III) foi acompanhada espectrofotometricamente em 325 e 265 nm, respectivamente. A velocidade da reação de autoxidação do complexo de Ni(II)/Gn aumenta com a concentração de S(IV) e é máxima em pH &#926;8,5. O processo é autocatalítico com Ni(III)ou Co(III)atuando como iniciadores, forma~os pela oxidação espontânea de Ni(II) ou Co(II) pelo oxigênio molecular. A dependência da constante de velocidade observada com a oncentração de S(IV) evidenciou possíveis reações paralelas com formação de um complexo com ligantes mistos antes da etapa da oxidação. A autoxidação dos complexos de Cu(II)com penta e hexaglicina em pH =9 é muito lenta, na presença e na ausência de S(IV).A presença de S(IV) e de traços de Ni(II)ou Co(II) aumenta significativamente a velocidade e a eficiência da reação (período de indução de 0,5 s). O mecanismo envolve uma cadeia de reações e um ciclo redox dos complexos. Acetaldeído e formaldeído inibem parcialmente a reação de autoxidação de Ni(II)/G4 na presença de S(IV) e luminol.O método quimiluminescente desenvolvido pode ser empregado para determinação de formaldeído [(5,0.10-5 - 1,0.10-2) mol L-1] e acetaldeído [(1,0.10-4 - 0,10) mol L-1], não sendo possível detectar separadamente cada um desses aldeídos. Na autoxidação de Ni(OH)2 induzida por S(IV) na presença de luminol ocorre emissão de radiação, possibilitando a detecção de S(IV) na faixa de 5,0.10-8 a 1,0.10-5 mol L-1, com limite de detecção estimado de 1,3.10-8 mol L-1. / The autoxidation of Ni(lI) and Co(lI) complexes with tetra, penta and hexaglycine, in borate medium, is accelerated by sulfur (IV) species (H2S03, HS03- and SO32-). The formation of Ni(llI) and Co(lIl) complexes was followed spectrophotometrically at 325 and 265 nm, respectively. The autoxidation rate of Ni(II)/Gn complex increases with S(IV) concentration and is maximum at pH ~ 8.5. The process is autocatalytic with Ni(lIl) or Co(llI) acting as initiators, formed by spontaneous oxidation by oxygen. The dependence of the observed rate constant with S(IV) concentration showed evidences of back or parallel reactions with formation of mixed ligand complex prior to the oxidation step. The autoxidation of Cu(II)/penta and hexaglycine complexes at pH = 9, in the presence and absence of S(IV), is very slow. The presence of S(IV) and of small amounts of Ni(lI) or Co(lI) increases significantly the effectiveness and reaction rate (induction period = 0.5 s). The mechanism involves a radical chain and redox cycling of the metal íon complexes. Acetaldehyde and formaldehyde partially inhibit the autoxidation reaction of Ni(II)/G4 in the presence of S(IV) and luminol. The developed chemiluminescent method can be used for determination of formaldehyde [(5.0.10-5 - 1.0.10-2) mol L-1] and acetaldehyde [(1.0.10-4 - 0.10) mol L-1), being not possible their isolated detection. The S(IV) induced autoxidation of Ni(OH)2 in the presence of luminol, occurs with radiation emission, allowing S(IV) detection in the range 5.0.10-8 to 1.0.10,-5 mol L-1, with detection limit of 1.3.10-8 mol L-1.

Pharmaceutical compounds represent a rapidly emerging class of environmental contaminants. Such compounds were recently classified by the U.S. Geological Survey, including several antibiotics. An LC-MS/MS screening method for the top five antibiotics in drinking water was developed and validated using a Shimadzu LC-MS-IT-TOF. The separation was performed using a Waters Acquity UPLC BEH C18 column with a gradient elution. Sulfamethazine was exposed to conditions intended to mimic drinking water chlorination, and samples were collected and quenched with excess sodium sulfite. Kinetics of sulfamethazine degradation was followed as well as the formation of the major chlorinated byproduct (m/z 313). For the screening method, all five antibiotic peaks were baseline resolved within 5 minutes. Additionally, precision and accuracy of the screening method were less than 15%. Degradation of sulfamethazine upon exposure to drinking water chlorination occurred by first order kinetics with a half-life of 5.3 × 10(4) min (approximately 37 days) with measurements starting 5 minutes after chlorination. Likewise, the formation of the major chlorinated product occurred by first order kinetics with a rate constant of 2.0 × 10(-2). The proposed identification of the chlorinated product was 4-amino-(5-chloro-4,6-dimethyl-2-pyrimidinyl)-benzenesulfonamide (C12H13N4O2SCl) using MS (n) spectra and databases searches of SciFinder and ChemSpider.

It has been shown in previous studies that when sulfite is absorbed by rabbits via either inhalation of SO2 or oral exposure to sulfite, the hydrated form, bisulfite, interacts with plasma disulfides where it is suspected to be in the form, cysteine-S-sulfonate. A rapid and specific gas chromatographic analysis procedure for cysteine-S-sulfonate has been developed to better study the distribution of sulfite in biological systems. Sulfonated proteins are enzymatically hydrolyzed to ensure stability of the acid labile S-sulfonate disulfide. The hydrolysate is then applied to a 6 cm cation-exchange column and eluted with 0.1 N HCl which elutes the acidic cysteine-S-sulfonate with the void volume of the column leaving behind any remaining cysteine. the silylated derivatives of the column effluent are prepared using Tri-Sil/BSA. These derivatives are injected into a gas chromatograph equipped with a flame-photometric detector operating in the sulfur mode, 2% 0v-101 on Chromosorb W/HP 1/4 inch glass column, oven temperture 140°C, and carrier flow rate of 86 ml/min. The presence of cysteine-S-sulfonat in the sulfite treated rabbits had been directly determined by the described method.

Today’s market offers an ever-increasing range of cellulose pulps (derivative pulps) made fromvarious wood types through different delignification processes. Each pulp segment has its uniquecharacteristics, which makes it difficult for the producer of cellulose derivatives to choose the mostsuitable pulp for optimum processability and product quality. The objective of this study was toimprove knowledge of cellulose pulps and to describe how different pulp properties affectprocessability and quality in the production of viscose dope and cellulose ethers.Ten pulp samples were investigated, originating from both sulfite and sulfate processes, with highand low viscosities and with softwood and hardwood as raw material. The pulps were analyzed fortheir properties and then processed to viscose dope and a cellulose ether in two separate pilotfacilities. The intermediates in the viscose process as well as the quality of the viscose dope andcellulose ether were analyzed and the results correlated to pulp properties.Multivariate regression methods were applied to investigate the dominating physical and chemicalproperties of each pulp and pulp segment, and to study the use of spectroscopic analyses inpredicting pulp origin, concentration and composition of hemicelluloses as well as the content ofreducing end groups in cellulose. For the production of viscose dope, the models presented showedthe most important pulp properties for good cellulose reactivity and viscose filterability. In addition,the properties affecting gel formation, flocculation, degree of substitution and clarity in theproduction of cellulose ether were highlighted. The study also emphasized the need to supplementthe use of conventional analyses on pulps and viscose intermediates with other analytical methods,such as molecular weight distribution and carbohydrate analysis, to better predict the quality ofboth viscose dope and viscose fiber.The results of the present study could be useful to predict the origin and properties of new pulps, toreplace or supplement otherwise expensive pulp analyses, and to assess the impact of pulpproperties on the production of cellulose derivatives without extensive pilot-scale trials.

2-Nitropropane dioxygenase from Hansenula mrakii is a flavin-dependent enzyme that catalyzes the oxidation of anionic nitroalkanes into the corresponding carbonyl compounds and nitrite, with oxygen as the electron acceptor. Although nitroalkanes are anticipated to be toxic and carcinogenic, they are used widely in chemical industry for a quick and effective way of synthesizing common reagents. Consequently, the biochemical and biophysical analysis of 2-nitropropane dioxyganase has a potential for bioremediation purposes. In this study, recombinant enzyme is purified to high levels, allowing for detailed characterization. The biochemical analysis of 2-nitropropane dioxygenase presented in this study has established that enzyme utilizes alkyl nitronates as substrates by forming an anionic flavosemiquinone in catalysis. The enzyme is inhibited by halide ions, does not contain iron and has a positive charge located close to the N(1)-C(2)=O locus of the isoalloxazine moiety of the FMN cofactor.

<p>Sulfite oxidase, a metabolically important enzyme, catalyzes the physiologically critical conversion of sulfite to sulfate in the terminal step of the degradation of sulfur containing compounds. The enzyme has been the focus for much research since its discovery in the 1950's. A central question to understanding the mechanism of molybdoenzymes such as sulfite oxidase and nitrate reductase concerns the roles of active site residues and the coordination chemistry of the Mo atom in the structure and function of the enzyme. The goal of this work was directed towards the characterization and determination of the structures of active site variants of sulfite oxidase using a spectroscopic, kinetic, and protein crystallographic approach.</p><p>Earlier studies have identified a single, highly conserved cysteine residue as the donor of a covalent bond from the protein to molybdenum in sulfite oxidase and nitrate reductase. The C185S and C185A variants of chicken sulfite oxidase exhibited severely attenuated activity. Crystallographic and spectroscopic analysis of both variants revealed a change in the metal coordination, from a dioxo to a trioxo form of Mo. </p><p>Assimilatory nitrate reductase is a member of the sulfite oxidase family of molybdopterin enzymes. The crystal structure of the Mo domain of the enzyme from Pichia angusta revealed high structural homology in the active sites of nitrate reductase and sulfite oxidase. Both enzymes utilize the same form of the molybdenum cofactor and have three out of five residues conserved at the active site. Substitution of two active site residues in sulfite oxidase alters the substrate affinity of chicken SO from sulfite to nitrate, resulting in an increase of nitrate reductase activity over wild-type sulfite oxidase. Additionally we identified an additional amino acid position in sulfite oxidase that corresponds to a non-conserved position in NR that further increased NR activity. Finally, these nitrate reductase variants of sulfite oxidase were crystallized and the structures solved. This represents the first example of the transmutation of a molybdenum enzyme to change activity and substrate affinity to those of a homologous enzyme.</p> / Dissertation

No description available.