No description available.

Much attention has been paid to immobilization of enzymes to improve enzyme stability and permit its reuse. Glucose oxidase entrapment in different kinds of silica sol-gel matrices was investigated. The enzyme showed stable activity for 11 uses in the sol-gel with tetramethyl orthosilicate (TMOS) as precursor, and at least 7 uses in the sol-gel induced electrochemically with tetraethyl orthosilicate (TEOS) as precursor. The sol-gel made with TEOS as precursor and HCl as catalyst showed stability in enzyme activity for 11 uses but the activity decreases on the same sol-gel when modified with silica nanoparticles. Factors such as optimal incubation time of glucose solution, the reproducibility between different sol-gels, and the storage time were investigated. Good linearity and analytical results on real samples were obtained. The detection method was based on a colorimetric method for determining the concentration of hydrogen peroxide produced from the oxidation reaction of glucose.

No description available.

The main goal of this research was to develop an easy to prepare and sensitive biosensor that would be able to detect glutamate in solution using ionic self-assembly methods. This was accomplished by preparing an ionically-self-assembled monolayer that included an electron transport mediator and an enzyme that would generate a current proportional to the concentration of analytes in solution. Biosensors were produced for the detection of glucose and glutamate. Ferrocene poly(allylamine) (FePAA) was assembled on negatively charged self-assembled monolayer and shown to be electrostatically bound by cyclic voltammetry. Model films were made of FePAA and poly(styrenesulfonate) to determine if multilayer films could be assembled using electrostatic assembly. These experiments demonstrated that 7 bilayers is the maximum number of bilayers oxidizable by the heterogeneous reaction at the electrode surface. ISAMs were then assembled on a 2 mm gold electrode and on a gold fiber microelectrode using FePAA and glucose oxidase. Using cyclic voltammetry, these ISAMs were shown to be able to oxidize glucose in solution. The LOD was determined to be lower for the microelectrode than for the 2 mm gold electrode, which was expected, while both compared well to the literature. The Km? were found to be smaller than other glucose biosensors while the Icat increased with increasing number of bilayers. This demonstrated that the GluOx is making good electrical contact with the layer below. These glucose oxidase ISAMs, however, do not exhibit structural stability in flow-injection experiments. As a solution to the ISAM modified electrodes degrading in the flowing system, a covalently modified surface was developed. Using cyclic voltammetry, these covalently modified surfaces were shown to be able to oxidize glucose in solution. The LOD of the covalently modified 2 mm gold electrode was calculated to be lower than the 2 mm ISAM modified gold electrode, due to the fast heterogeneous kinetics on the covalently modified electrode surface. The Km? and Icat for the covalently modified 2 mm gold electrode were found to be the similar to the 2 mm ISAM modified gold electrode indicating that the covalently modified electrodes will be a suitable replacement. The covalently modified surfaces exhibit excellent structural stability and detect much lower glucose amounts in flow-injection experiments. ISAMs were subsequently assembled on gold fiber microelectrodes using FePAA and glutamate oxidase. Glutamate was able to be detected in solution at biologically significantly quantities using cyclic voltammetry. The Km? was shown to be comparable to literature values and Icat was shown to increase with increasing number of bilayers. These results demonstrate that an ISAM constructed using FePAA/GlutOx is a feasible way to detect glutamate in a system. / Ph. D.

The honey bee is a widely managed crop pollinator that provides the agricultural industry with the sustainability and economic viability needed to satisfy the food and fiber needs of our society. Excessive use of agrochemicals such as the acaricides coumaphos and tau-fluvalinate, and the fungicide, chlorothalonil is implicated in the reduced number of managed bee colonies available for crop pollination services. Here, I report the effects of pesticide exposures on the nutritional and immune health of the honey bee. Total protein concentration was significantly reduced in the coumaphos- and chlorothalonil-treated individuals compared to the pesticide-untreated bees. Total carbohydrate concentration was significantly reduced in the tau-fluvalinate-, coumaphos-, and chlorothalonil-treated individuals compared to the pesticide-untreated bees. Total lipid concentration was significantly decreased in the chlorothalonil-treated individuals compared to the pesticide-untreated bees. Body weight was significantly reduced for the tau-fluvalinate-, coumaphos-, and chlorothalonil-treated individuals, respectively, compared to the pesticide-untreated bees. Head width was significantly reduced for the chlorothalonil-treated individuals whereas the wing length was significantly reduced for the coumaphos and chlorothalonil-treated individuals, respectively, compared to the pesticide-untreated bees. Phenoloxidase activity was significantly increased in the coumaphos-treated individuals compared to the pesticide-untreated bees. Glucose oxidase activity was significantly increased in the chlorothalonil-treated individuals compared to the pesticide-untreated bees. While more research is needed to verify the observed effects of the pesticides on the nutritional and immunity health of the honey bee, it is important for beekeepers to consider alternative methods for control of varroa mites and the use of fungicides near their colonies. / Master of Science in Life Sciences

Thesis (PhD)--Stellenbosch University, 2010. / ENGLISH ABSTRACT: Popular wine styles prepared from fully-ripened, more mature grapes are characterized by intense fruitiness and varietal flavors. However, lengthy maturation of grapes in the vineyard does not only translate into higher flavor intensity but also into higher sugar levels, which, in turn, leads to wines with higher concentrations of alcohol. Excessive alcohol levels can compromise wine flavor and render wine unbalanced. This, along with health issues and anti-social behavior linked to high-risk alcohol consumption patterns, stricter legislation and increased tax rates associated with high-alcohol wines, have increased demand for wines with reduced alcohol concentrations, without loss of the intense fruity aromas. Although low-alcohol wines can be made using physical post-fermentation processes, such approaches are often expensive and can impact adversely on wine flavor. As an alternative strategy, yeast strains are being developed by several research groups to convert some of the grape sugars into metabolites other than ethanol. Based on promising results from previous preliminary work, this study focused on the development of an industrial Saccharomyces cerevisiae wine strain producing glucose oxidase (GOX; b-D-glucose:oxygen oxidoreductase, EC 1.1.3.4). GOX oxidizes b-D-glucose to D-glucono-d-lactone and gluconic acid (GA) extracellularly, thus preventing its entry into glycolysis, thereby diverting a portion of the sugar carbon away from ethanol. The GOX-encoding gene from the foodgrade fungus, Aspergillus niger was used to construct three cassettes (GOX1, GOX2 and GOX2LOX). In these gene cassettes, the A. niger GOX gene was placed under the regulation of the S. cerevisiae phosphoglycerate-kinase-1 gene promoter (PGK1P) and terminator (PGK1T ). To facilitate secretion, in GOX1 the yeast mating pheromone-factor a secretion signal (MFa1S) was fused to the GOX gene, and in GOX2 the native A. niger secretion signal of GOX was used. These gene cassettes were each integrated into the genome of two laboratory yeast strains (BY4742 and S1278b) and one industrial wine yeast strain (VIN13). An additional integration cassette, designated GOX2LOX, was constructed to knock out the IME1 gene in S. cerevisiae. In GOX2LOX, GOX2 was fused to a loxP cassette. VIN13-D1 was obtained by integrating a single copy of GOX2LOX into the IME1 locus. To generate an asporogenic, GOX-producing wine yeast, VIN13-D2 was created by sporulation, micromanipulation and re-diploidisation of VIN13-D1. Comparative analysis indicated that (i) GOX2 resulted in higher levels of extracellular glucose oxidase activity than GOX1; and that (ii) the levels of secreted glucose oxidase activity in the wine yeast transformants were sufficiently high to conduct follow-up small-scale wine fermentation trials. The wine yeast transformant, VIN13-D1 was evaluated under red and white experimental winemaking conditions. Results from this work indicated that glucose oxidase was produced and secreted by VIN13-D1 that dominated the fermentation to the end, but also that the enzyme was not highly active under the evaluated winemaking conditions. Consequently, no significant decrease in ethanol concentrations was observed in the wine made from VIN13-D1 when compared to that from VIN13. Wine samples were analyzed by Fourier transform-middle infrared spectrometry (FT-MIR) to determine the chemical composition and Gas chromatography with a flame ionization detector (GC-FID) to evaluate the concentrations of aroma compounds. The levels of gluconic acid were determined by enzymatic assays. Multivariate data analysis (PCA and PLS1-discrim) was applied to highlight significant differences between the wines made by VIN13 (wild-type) and VIN13- D1. Chemometric projections of the score plots for all results allowed insight into all significant variation up to three principal components (PCA) or PLS components, which showed very clearly that GA is a key factor in evaluating the effect of GOX in VIN13-D1 fermentation with regard to VIN13 fermentations. The VIN13- D1 effect manifestations were best shown on PLS1-discrim score plots that revealed that, of the restricted variable subsets the FT-MIR-compounds and GC-compounds yielded better results, with the GC-compounds displaying greater discriminability between cultivars and VIN13 / VIN13-D1. It can be concluded from these results that the greatest influence of VIN13-D1 produced wines could be observed in the aroma components, but, because there were also discriminability effects discernable in the FT-MIR-compounds, thus the flavor components were also affected. The activity of GOX in grape juice was further investigated in controlled small scale fermentations performed in a bio-reactor. It was confirmed that GOX is active under aerobic conditions, inactive under anaerobic conditions, and can be activated instantly when an anaerobic culture is switched to aerobic conditions (simulated micro-oxygenation). These fermentations showed that glucose oxidase is active in grape juice, and that oxygen play a key-role in the enzyme’s activation. Finally, it was shown with the help of a simplified model, that under ideal conditions, GOX secreted from VIN13-D1, can be employed to reduce the ethanol by a predefined concentration for the production of low alcohol wines. This work gives more insight into how to employ a GOX-producing wine yeast during winemaking and strongly suggests the use of micro-oxygenation to activate the enzyme in order to reduce available glucose, thereby diverting a portion of the sugar carbon away from ethanol production. / AFRIKAANSE OPSOMMING: Gewilde wynstyle word dikwels gemaak van volryp, goed ontwikkelde druiwe, gekarakteriseer deur intense aromas en smaakkomponente wat direk met spesifike kultivars geassosieer word. ’n Nadelige gevolg om druiwe te lank aan die wingerdstok te laat bly hang sodat meer intense geurkomponente kan ontwikkel, is die toename in suikerinhoud. Hierdie addisionele suiker lei tot wyne met hoër alkoholvlakke. Te hoë alkoholvlakke kan wyn ongebalanseerd laat voorkom en die smaak nadelig beïnvloed. Dit, tesame met gesondheidsredes en anti-sosiale gedrag wat gekoppel kan word aan die inname van te veel alkohol, strenger wetgewing aangaande dronkbestuur en die toename in belasting op wyne met ’n hoër alkoholinhoud, het aanleiding gegee tot ’n aanvraag vir wyn met ’n verlaagte alkoholinhoud, sonder dat aroma- en geurkomponente ingeboet word. Alhoewel daar sekere fisiese/gemeganiseerde prosesse beskikbaar is om die alkohol in wyn te verwyder of te verminder, is ’n nadeel dat hierdie prosesse baie duur en arbeidsintensief is, en dat dit deur sommige wynpuriste as te ingrypend in die ‘natuurlike’ proses van wynmaak beskou word. Sommige van hierdie alkoholverwyderingsprosesse kan ook die wyn se geur- en aromakomponente nadelig beïnvloed. As alternatief tot hierdie fisies-chemiese prosesse word wyngiste reg oor die wêreld deur verskillende navorsingsgroepe ontwikkel sodat van die druifsuikers nie na alkohol omgeskakel word nie, maar eerder ander metaboliete. Belowende navorsingsresultate in ’n voorafgaande studie het aanleiding gegee tot hierdie navorsingsprojek. In hierdie studie word daar klem gelê op die ontwikkeling, deur middel van genetiese manipulering, van ’n industriële wynras van Saccharomyces cerevisiae sodat dit in staat sal wees om glukose-oksidase (GOX; b-D-glukose:suurstof oksidoreduktase, EC 1.1.3.4) te produseer. GOX kan reeds b-D-glukose in die medium oksideer na glukoonsuur (GA), wat sodoende verhoed dat dit verder gemetaboliseer word via glukolise, en dit het tot gevolg dat ’n gedeelte van die beskikbare suiker nie omgeskakel word na alkohol nie. Die strukturele glukose-oksidase-geen (GOX) van die voedsel-gegradiëerde fungus, Aspergillus niger is gebruik tydens die konstruksie van drie kassette (GOX1, GOX2 en GOX2LOX). Binne hiedie geenkassette is A. niger se GOX-geen se transkripsieinisiëring en -terminering onafhanklik deur die fosfogliseraat-kinase-1-promotor (PGK1P) en termineerder (PGK1T ) bewerkstellig. Om uitskeiding van GOX uit die gis te bewerkstellig, is daar van die a-spesifieke gisferomoon-a-faktor (MFa1S) in GOX1 gebruik gemaak, en in GOX2, van A. niger se eie natuurlike sekresiesein. Hierdie geenkassette is binne-in die genoom van twee labaratoriumgisrasse van S. cerevisiae (BY4742 en S1278b) asook een industriële wyngisras (VIN13) geintegreer. ’n Addisionele integreringskasset (die sogenaamde GOX2LOX-kasset) is gemaak om die IME1-geen van S. cerevisiae te elimineer. Binne die GOX2LOXkasset is GOX2 aan ’n loxP-kasset gekoppel. Die nuwe wyngis VIN13-D1 is verkry deur ’n genomiese integrasie van GOX2LOX binne-in die IME1-lokus. Om die niesporulerende GOX-produserende wyngis VIN13-D2 te verkry, is VIN13-D1 gesporuleer, onderwerp aan mikromanipulasie en toegelaat om te herdiploidiseer. Ontledings het aangedui dat (i) GOX2 aanleiding gegee het tot hoër vlakke van ekstrasellulêre glukose-oksidase aktiwiteit in vergelyking met GOX1; en (ii) dat die vlakke van uitgeskeide biologies-aktiewe glukose-oksidase vir die wyngisrasse aansienlik hoër was. Dit het verdere kleinskaalse wynfermentasies geregverdig. Die getransformeerde wyngis VIN13-D1 is op eksperimentele skaal in die maak van rooi- en witwyn geëvalueer. Ontledings van hierdie eksperimentele wyne het daarop gedui dat glukose-oksidase deur die VIN13-D1-gisselle geproduseer en suksesvol uitgeskei tydens die wynmaakproses is, en dat VIN13-D1 die fermentasie gedomineer het en die alkoholiese gisting voltooi het. Resultate het egter ook aangedui dat die geproduseerde glukose-oksidase nie baie aktief was onder die wynmaaktoestande wat in hierdie eksperimentele wynmaakproses gegeld het nie, en gevolglik was daar nie ’n drastiese verlaging in die alkoholvlakke sigbaar toe VIN13-D1 se wyne met VIN13 se wyne vergelyk is nie. Wynmonsters is deur middel van Fourier-transformasie-mid-infrarooispektroskopie (FT-MIR) ontleed ten einde die chemiese samestelling te bepaal, en gaschromatografie-massaspektrometrie (GCMS) is aangewend om die wynaromakomponente te bepaal. Die vlakke van glukoonsuur is deur middel van ensiematiese reaksies bepaal. Multiveranderlike data-analise [hoofkomponentanalise (PCA) en parsiële kleinte kwadrate (PLS1) diskriminantanalise] is op die data van die verskeie analitiese tegnieke toegepas om onderliggende veskille tussen die wyne van VIN13 (wilde-tipe) en VIN13-D1 uit te wys. Chemometriese projeksies het aangetoon dat daar wel beduidende variasies sigbaar was tot en met drie hoofkomponente en/of PLS-komponente wat duidelik aandui dat glukoonsuur ’n sleutelfaktor was ten opsigte van die uitwerking wat GOX op VIN13-D1- fermentasies in vergelyking met VIN13-fermentasies. VIN13-D1 effek manifestasies is die beste waargeneem op grafieke wat PLS1-diskriminantanalise-data bevat. Verder het PLS1-diskriminantanalise ook aangetoon dat van die ‘groepe’ wat gebruik was tydens die analise, die FT-MIR-komponente en die GC-komponente beter resultate gelewer het. Die GC-komponente het hulle verder daartoe geleen om tussen die verskillende kultivars en VIN13/VIN13-D1-fermentasies te diskrimineer. Daar kan dus met sekerheid gesê word dat die grootste invloed in VIN13-D1 wyne sigbaar is in die aromakomponent, maar omdat daar wel ook variasies sigbaar was in die MIR-komponente, dat die smaakkomponente ook beïnvloed was. Die aktiwiteit van GOX in druiwesap is verder ondersoek deur gebruik te maak van kleinskaalse fermentasies in bioreaktors. Daar is bevestig dat die VIN13-D1- geproduseerde GOX biologies-aktief was tydens aerobiese kondisies, onaktief was tydens anaerobiese kondisies, en onmiddelik geaktiveer kon word wanneer ’n anaerobiese fermentasie aerobies gemaak word (gesimuleerde mikro-oksigenasie). Hierdie verskillende fermentasies dui daarop dat glukose-oksidase inderdaat aktief is in druiwesap, en dat suurstof ’n sleutelfaktor is tydens die aktivering van die ensiem. Met behulp van ’n vereenvoudigde model kon aangetoon word dat tydens ideale toestande dit wel moontlik is om die alkoholvlakke te verlaag na ’n voorafbepaalde konsentrasie vir die bereiding van lae-alkohol wyne. Hierdie studie verskaf verdere insig hoe om ’n GOX-produserende wyngis gedurende die wynmaakproses vir die verlaging van die alkoholvlakke te benut. Verder is dit duidelik dat suurstof van kardinale belang is vir die aktivering van die glukoseoksidase- ensiem en dat ’n tegniek soos mikro-oksigenasie ’n belangrike rol in hierdie verband tydens die wynmaakproses sou kon speel.

Thesis (MscAgric (Viticulture and Oenology))--Stellenbosch University, 2008. / Over the years, different techniques have been used to legally reduce the ethanol content of wines. Several physical processes are available for producing wines with less alcohol. Despite their efficacy, these treatments have a capital and operational cost influence. They can also affect the concentration of other wine components. On the other hand, vast amount of research has been conducted through genetic modification of wine yeast strains in order to reduce the ethanol yield of Saccharomyces cerevisiae by diverting sugar metabolism towards various byproducts. However, genetically modified yeasts are not currently accepted in most wine industries worldwide, including South Africa. Therefore, other approaches need to be envisaged. Commercial enzymes are commonly added during winemaking. Most enzymes essential for vinification naturally occur in grapes, but are inefficient under pH and sulphur levels associated with winemaking. Enzymes of fungal origin are resistant to such conditions. The most widely used commercial enzymes include pectinases, hemicellulases, glucanases and glycosidases. With the exception of glucanases, produced by Trichoderma harzianium, all the other enzymes are produced by Aspergillus niger. In this study, the possibility of using Gluzyme Mono® 10.000 BG (Gluzyme) (Novozymes, South Africa) to reduce the glucose content of synthetic grape must and grape must before fermentation in order to produce wine with a reduced alcohol content was investigated. Gluzyme is a glucose oxidase preparation from Aspergillus oryzae, currently being used in the baking industry. Glucose oxidase catalyses the oxidation of glucose to gluconic acid and hydrogen peroxide in the presence of molecular oxygen. Gluzyme was initially used in synthetic grape must where different enzyme concentrations and factors influencing its activity were investigated for its use in winemaking. The results showed that up to 0.5% v/v less alcohol were obtained using an enzyme concentration of 20 kU compared to the control. This reduction in alcohol was increased to 1 and 1.3% v/v alcohol at pH 3.5 and pH 5.5 respectively in aerated synthetic grape must using 30 kU enzyme. Secondly, Gluzyme trials were carried out using Pinotage grape must. Gluzyme treated wines after fermentation contained 0.68% v/v less alcohol than the control samples at 30 kU enzyme. Colour and volatile flavour compounds of treated wine did not differ significantly from the untreated samples. Lower free anthocyanin and total phenol concentrations in treated than control samples were observed, possibly due to the hydrogen peroxide oxidation which could have led to polymerisation. The present study has clearly demonstrated that Gluzyme may be used in winemaking to produce reduced-alcohol wine without affecting its colour and aroma compounds. The enzyme in its current form is however, not ideal for winemaking; other forms such as liquid or powder form should be considered if the enzyme is to be used under winemaking conditions. Future work should focus on evaluating the potential new form of the enzyme and studying the effects of Gluzyme in various grape must in semi-industrial scale. A tasting panel should also evaluate its impact on the organoleptic properties and the overall quality of the resulting wines.

A sacarose é uma matéria-prima em franca expansão de produção no Brasil, seu maior produtor e exportador. Essa molécula pode ser convertida, através de um processo multienzimático, em produtos de maior valor agregado: frutose e ácido glicônico, os quais são importados pelo país, e amplamente utilizados em indústrias químicas, de produção de fármacos e setores alimentícios. Neste estudo, avaliou-se a hidrólise da sacarose pela invertase assim como a conversão da glicose em ácido glicônico, pela ação da glicose oxidase, ambas em processo descontínuo-alimentado. A solução de substrato (64g/L-sacarose; 32g/L-glicose) foi adicionada segundo as seguintes leis: constante, linear crescente, linear decrescente, exponencial crescente e exponencial decrescente. No caso da glicose, foi necessária a utilização de enzima auxiliar, a catalase, para degradar a água oxigenada formada durante a conversão da glicose. Mediante os resultados dos testes com os dois substratos, realizou-se teste de conversão direta da sacarose em frutose e ácido glicônico, utilizando-se invertase, glicose oxidase e catalase em regime descontínuo-alimentado, com alimentação linear decrescente (melhor resultado para ambos os substratos). No procedimento contínuo, alvo principal do trabalho, utilizou-se reator com membrana, da marca MILLIPORE ®, integrando em uma única etapa a conversão catalítica, a separação/concentração do produto e a recuperação do biocatalisador. A temperatura foi controlada por circulação de água, tendo acoplado uma bomba peristáltica (para controlar a vazão de alimentação do substrato) e um sistema de pressurização. O reator operou com membrana de ultrafiltração (corte molecular = 100 kDa) e foi mantido sob agitação constante. Os parâmetros de partida foram, a princípio, fixados de acordo com os valores otimizados no reator descontínuo-alimentado com o emprego simultâneo das enzimas. / Sucrose is a commodity largely produced in Brazil and one of the most used and commercialized product in food industry. It can be converted through a multienzyme process in fructose and gluconic acid, which have commercial values higher than sucrose. Both products are imported by Brazil, being largely employed in the chemical, food and pharmaceutical industry. This work dealt with the hydrolysis of sucrose by invertase into fructose and glucose, and the oxidation of glucose to gluconic acid by glucose oxidase and catalase. Catalase was added in order to decompose the hydrogen peroxide an inhibitor of glucose oxidase formed as by-product of the oxidation. Two processes were employed. Fed-batch in which the hydrolysis and oxidation reactions were carried out separately by adding invertase followed by glucose oxidase and catalase was conducted by adding the solution of substrate according to a constant, increasing linear, decreasing linear, increasing exponential or decreasing exponential mode. The best fed-batch performance was attained through the decreasing linear addition of sucrose (64g/L) and glucose (32g/L). Setting this kind of addition and using all enzymes simultaneously, the direct conversion of sucrose to fructose and gluconic acid occurred at a yield of 72%. The continuous process was carried out in a cell-type membrane reactor (membrane cut off = 100 kDa), in which the sucrose conversion was made by using all enzymes simultaneously, leading to a final yield of about 76%

A levedura Kluyveromyces marxianus, apesar de apresentar propriedades fisiológicas vantajosas para a produção heteróloga de proteínas, foi utilizada apenas poucas vezes como hospedeira na síntese dessa classe de moléculas. Em contrapartida, a sua congênere Kluyveromyces lactis possui mais de 40 sistemas de expressão desenvolvidos, inclusive comerciais. Além disso, não há literatura disponível sobre glicosilação de proteínas em K. marxianus. Levando-se isso em consideração, este trabalho visou a desenvolver sistemas para a expressão heteróloga da enzima glicose oxidase (GOX) de Aspergillus niger e de uma esterase termófila (EST) de Thermus thermophilus em K. marxianus. A linhagem K. lactis CBS 2359 foi utilizada como parâmetro de comparação em todos os sistemas de expressão construídos. Primeiramente, foi realizado um estudo fisiológico com a finalidade de selecionar, dentre três linhagens de K. marxianus pré-selecionadas a partir de informação da literatura, a que apresentasse as melhores características fisiológicas para se tornar uma hospedeira de expressão heteróloga. A linhagem selecionada foi a CBS 6556, baseando-se numa combinação das seguintes características: velocidade específica de crescimento, formação de metabólitos, rendimento de substrato em biomassa e secreção da enzima homóloga inulinase. Após, foram construídos dois sistemas de expressão epissomais. No primeiro, o gene era expresso sob controle do promotor PGK de S. cerevisiae e no segundo, sob controle de INU1 de K. marxianus. Um sistema integrativo foi utilizado, no qual a expressão era dirigida pelo promotor INU1. Estudos bioquímicos e de glicosilação foram realizados nas enzimas produzidas. Em relação aos sistemas para expressão de GOX, foram alcançados níveis de produção de 1722 U/gMS (unidades por grama de biomassa seca) em K. marxianus transformado com o sistema epissomal no qual a expressão era controlada pelo promotor INU1. As caracterizações bioquímicas da enzima mostraram que a molécula produzida apresentava propriedades semelhantes à enzima homóloga de A. niger. Além disso, os estudos de glicosilação mostraram uma menor tendência de hiperglicosilação de K. marxianus quando comparada com K. lactis. Já em relação à esterase, K. lactis apresentou maiores níveis de expressão (294 U/gMS), porém a enzima produzida em K. marxianus apresentou temperatura ótima de atividade (50 °C) ligeiramente superior à enzima produzida por sua congênere (45 °C), temperaturas abaixo da qual ocorre maior atividade da enzima homóloga (65 °C). Isso pode ser explicado pela glicosilação exercida por ambas espécies de leveduras sobre a proteína, ao contrário da homóloga, não glicosilada. Além disso, os produtos das leveduras apresentaram três padrões de glicosilação. Dessa forma, o trabalho desenvolvido alcançou seu objetivo de desenvolver esses sistemas de expressão, bem como de avaliar a síntese heteróloga de proteínas nessa levedura de destacado potencial. Os resultados obtidos devem servir à comunidade científica, no sentido de estimular e orientar futuros trabalhos que objetivem a síntese heteróloga de proteínas em microrganismos. / In spite of the advantageous physiological properties of the yeast Kluyveromyces marxianus to produce heterologous proteins, this species has not been widely explored for the synthesis of these biomolecules. On the other hand, more than 40 heterologous expression systems, including commercial ones, were developed for Kluyveromyces lactis. Moreover, there is no available literature concerning heterologous protein glycosylation in K. marxianus. Taking these facts into account, this work aimed at developing systems for the heterologous production of Aspergillus niger glucose oxidase (GOX) and of a thermophilic esterase (EST) from Thermus thermophilus in K. marxianus. The strain K. lactis CBS 2359 was utilized as a reference throughout the whole work. First, a physiological study was carried out in order to select one K. marxianus strain, out of three which had been chosen based on literature information, that exhibited the best physiological traits to be a heterologous expression host. The chosen strain was CBS 6556, based on a combination of the following properties: specific growth rate, metabolites formation, biomass yield on substrate, and secretion of the homologous enzyme inulinase. Subsequently, two episomal systems were constructed. In one of them, the heterologous gene was expressed under control of the S. cerevisiae PGK promoter, whereas in the other system, heterologous gene expression occurred under control of the K. marxianus INU1 promoter. An integrative expression system was also constructed, in which the KmINU1 promoter drove foreign gene expression. Both heterologous enzymes were characterized biochemically and also with respect to their glycosylation. The results attained with GOX led to an expression level of 1722 U/g DW (unit per gram of dry cell weight) in K. marxianus transformed with the episomal INU1-based system. The biochemical studies showed that the enzyme was very similar to the A. niger GOX. Furthermore, analysis of the glycosylation pattern showed a lower tendency of K. marxianus to hypermannosylate proteins, when compared to K. lactis. Higher levels of esterase (294 U/gDW) were obtained in K. lactis than in K. marxianus. However, the enzyme produced in the latter host presented a higher temperature for maximal activity ((50 °C), when compared to the former organism (45 °C). Both values are lower than the temperature for maximal activity of the homologous enzyme (65 °C), which can be explained by the glycans added by both yeast species to the peptide, resulting in a glycosylated protein, in contrast to the homologous esterase. Moreover, the yeast products presented three glycosylation patterns. In conclusion, the work presented in this thesis reached its aims, which were to develop these expression systems and to characterize biochemically the heterologous enzymes expressed, which included an analysis of the glycosylation pattern. The results presented here will certainly be of interest and aid the scientific community working on the expression of heterologous proteins in microorganisms.

A sacarose é uma matéria-prima em franca expansão de produção no Brasil, seu maior produtor e exportador. Essa molécula pode ser convertida, através de um processo multienzimático, em produtos de maior valor agregado: frutose e ácido glicônico, os quais são importados pelo país, e amplamente utilizados em indústrias químicas, de produção de fármacos e setores alimentícios. Neste estudo, avaliou-se a hidrólise da sacarose pela invertase assim como a conversão da glicose em ácido glicônico, pela ação da glicose oxidase, ambas em processo descontínuo-alimentado. A solução de substrato (64g/L-sacarose; 32g/L-glicose) foi adicionada segundo as seguintes leis: constante, linear crescente, linear decrescente, exponencial crescente e exponencial decrescente. No caso da glicose, foi necessária a utilização de enzima auxiliar, a catalase, para degradar a água oxigenada formada durante a conversão da glicose. Mediante os resultados dos testes com os dois substratos, realizou-se teste de conversão direta da sacarose em frutose e ácido glicônico, utilizando-se invertase, glicose oxidase e catalase em regime descontínuo-alimentado, com alimentação linear decrescente (melhor resultado para ambos os substratos). No procedimento contínuo, alvo principal do trabalho, utilizou-se reator com membrana, da marca MILLIPORE ®, integrando em uma única etapa a conversão catalítica, a separação/concentração do produto e a recuperação do biocatalisador. A temperatura foi controlada por circulação de água, tendo acoplado uma bomba peristáltica (para controlar a vazão de alimentação do substrato) e um sistema de pressurização. O reator operou com membrana de ultrafiltração (corte molecular = 100 kDa) e foi mantido sob agitação constante. Os parâmetros de partida foram, a princípio, fixados de acordo com os valores otimizados no reator descontínuo-alimentado com o emprego simultâneo das enzimas. / Sucrose is a commodity largely produced in Brazil and one of the most used and commercialized product in food industry. It can be converted through a multienzyme process in fructose and gluconic acid, which have commercial values higher than sucrose. Both products are imported by Brazil, being largely employed in the chemical, food and pharmaceutical industry. This work dealt with the hydrolysis of sucrose by invertase into fructose and glucose, and the oxidation of glucose to gluconic acid by glucose oxidase and catalase. Catalase was added in order to decompose the hydrogen peroxide an inhibitor of glucose oxidase formed as by-product of the oxidation. Two processes were employed. Fed-batch in which the hydrolysis and oxidation reactions were carried out separately by adding invertase followed by glucose oxidase and catalase was conducted by adding the solution of substrate according to a constant, increasing linear, decreasing linear, increasing exponential or decreasing exponential mode. The best fed-batch performance was attained through the decreasing linear addition of sucrose (64g/L) and glucose (32g/L). Setting this kind of addition and using all enzymes simultaneously, the direct conversion of sucrose to fructose and gluconic acid occurred at a yield of 72%. The continuous process was carried out in a cell-type membrane reactor (membrane cut off = 100 kDa), in which the sucrose conversion was made by using all enzymes simultaneously, leading to a final yield of about 76%