Made available in DSpace on 2014-12-17T15:01:53Z (GMT). No. of bitstreams: 1 MichelleRFV_TESE.pdf: 2132732 bytes, checksum: 80b95f923491eeb118d74b0376a64ba9 (MD5) Previous issue date: 2011-12-29 / Conselho Nacional de Desenvolvimento Cient?fico e Tecnol?gico / Escherichia coli has been one of the most widely used hosts in recombinant protein production, in both laboratory and industrial scale since the advent of recombinant DNA technology. Despite the substantial progress of studies on the molecular biology and immunology of infections, there is currently no medication-based prophylaxis capable of preventing leishmaniasis. As such, there is a great need to identify specific antigens for the development of vaccines and diagnostic kits against visceral leishmaniasis. Thus, the primary goal of the present study is to assess the influence of cultivation conditions on the production of Leishmania chagasi antigens, carried out in a rotating incubator and bioreactor. To that end, several assays were conducted to evaluate the kinetic behavior of antigens (648, 503) of Leishmania. i. chagasi in two different compositions of media (2xTY, TB), with and without an inducer. In order to improve expression, assays were performed in a benchtop bioreactor using the best conditions obtained in a rotating incubator, in addition to assessing the influence of stirring speed. Results show that high complexity of the cultivation medium favored kinetic growth of clones (648, 503). However, in assays submitted to induction by IPTG, this elevated complexity did not promote the expression of recombinant proteins. Expression of antigens 648 and 503 exhibited behavior associated with growth and, in terms of location, proteins 648 and 503 are intracellularly stored. Lactose may be the most adequate inducer in protein expression, when considering factors, cost, toxicity and stability. Elevated stirring may increase cell growth in clone 53, although it may not result in high concentrations for the protein of interest. On the other hand, positive results were obtained for all recombinant clones (648, 503) tested, confirmed by the electrophoretic profile / A Escherichia coli ? um dos hospedeiros mais utilizados para produ??o de prote?nas recombinantes tanto em escala de laborat?rio como em escala industrial desde o advento da tecnologia do DNA recombinante. Apesar do avan?o expressivo dos estudos da biologia molecular e da imunologia das infec??es, n?o existe, atualmente, nenhuma droga profil?tica capaz de prevenir o calazar. Desta forma, existe uma grande necessidade de identifica??o de ant?genos espec?ficos para o desenvolvimento de vacinas e kits para diagn?sticos contra a Leishmaniose visceral. Com base no exposto, o presente trabalho tem como foco principal avaliar a influ?ncia das condi??es de cultivo na produ??o dos ant?genos de Leishmania i. chagasi em cultivos realizados em incubador rotativo e biorreator. Para atingir o objetivo proposto, v?rios ensaios foram realizados a fim de se avaliar o comportamento cin?tico dos clones (648, 503) de Leishmania i. chagasi em duas diferentes composi??es de meio (2xTY, TB), com e sem adi??o de indutor em incubador rotativo. Para melhorar a express?o, ensaios foram conduzidos em biorreator de bancada com as melhores condi??es obtidas em incubador rotativo, al?m da avalia??o da influ?ncia da velocidade de agita??o. Com base nos resultados obtidos, pode-se observar que a elevada complexidade do meio de cultivo favoreceu a cin?tica de crescimento dos clones (648, 503), no entanto, ao se tratar dos ensaios submetidos ao procedimento de indu??o por IPTG, a elevada complexidade do meio de cultivo n?o favoreceu a express?o das prote?nas recombinantes. Pode-se observar que a express?o dos ant?genos 648 e 503 apresentam um comportamento associado ao crescimento e que em termos de localiza??o, as prote?nas 648 e 503, s?o armazenadas intracelularmente. A lactose pode ser o indutor mais adequado na express?o das prote?nas tendo em vista os fatores, custo, toxicidade e estabilidade. A elevada agita??o pode aumentar o crescimento celular do clone 503, entretanto, pode n?o acarretar em altas concentra??es da prote?na de interesse. Por outro lado, foram obtidos resultados positivos para todos os clones recombinantes (648, 503) testados, confirmada atrav?s do perfil eletrofor?tico

Polyhydroxyalkanoates (PHAs) are polyesters, produced by many bacteria and some archaea. The most commonly characterised is polyhydroxybutyrate (PHB). Produced when nutrients are growth limiting and carbon available in excess, PHA serves as a carbon-energy storage material and forms generally spherical insoluble inclusions between 50-500nm in diameter in the cytoplasm. The key enzyme for PHA synthesis is the PHA synthase and this enzyme catalyses the polymerisation of (R)-3-hydroxy fatty acids into PHA. PHA synthase remains covalently attached to the growing polyester chain and is displayed on the surface of the PHA granule. Other proteins associated with PHA granules include depolymerases for mobilisation or degradation of granules, regulatory proteins and phasins, proteins that aid in PHA granule stability. PHA bio-beads displaying an IgG binding protein were produced and used to purify IgG from serum demonstrating that the PHA synthase can be engineered to display functional synthase fusion proteins at the PHA granule surface. Correctly folded eukaryotic proteins were also produced and displayed at the PHA granule surface as phasin fusion proteins. Multiple-functionality was also achievable by co-expression of various hybrid genes suggesting that this biotechnological bead production strategy might represent a versatile platform technology. The production of functional eukaryotic proteins at the PHA bead surface represents a novel in vivo matrix-assisted protein folding system. Protein engineering of PHA granule surface proteins provides a novel molecular tool for the display of antigens for FACS based analysis and offers promising possibilities in the development of future biotechnological production processes. Overall, the results obtained in this study strongly enhance the applied potential of these polyester beads in biotechnology and medicine.

Made available in DSpace on 2014-12-17T15:01:21Z (GMT). No. of bitstreams: 1 RobertaVAC_DISSERT.pdf: 2111666 bytes, checksum: 5b317150d6db63bae04e852173ace9d2 (MD5) Previous issue date: 2009-12-14 / Conselho Nacional de Desenvolvimento Cient?fico e Tecnol?gico / Visceral leishmaniosis caused by Leishmania chagasi, also known as calazar, presented, in the period from 1990 to 2005, tax of incidence in Brazil varying between 1 and 3 cases for 100 000 inhabitants. The Northeast region that up to the year of 2000 contributed with almost 90% of the registered cases is reducing his participation in the current decade, reaching 56% in 2005. Conventional leishmaniasis treatment is costly and it shows high toxicity, demanding more research for alternative treatments, with special interest in development of vaccines and diagnosis kits which include production of recombinant antigens by host cells. Escherichia coli has been the microorganism most studied and used as a host for recombinant protein production. Therefore, the aim of this work was to study the influence of induction on cellular growth and to verify the type of Leishmania chagasi antigens expression (intra or extracellular) during two recombinant E. coli clones (kmp11 and P36) cultivation in rotary incubator (shaker) using three different media (2xTY, TB, FASS+EL). For that, tests were carried out using conditions established in the literature for E. coli (37?C and 200 rpm) and media supplemented with antibiotics to guarantee that only competent cells grows. First, tests were carried out without induction in order to verify the two microorganisms kinetic behavior (growth and substrate consumption) in different media. Next, the induction was carried out through the addition of IPTG (1mM as final concentration), at the first hour of cultivation. It was observed that protein expression were intracellular for all clones and media tested, however the highest level of expression was clearly observed by the electrophoresis band density (intensity) for 2xTY medium and kmp11 protein. Although it contains the lowest substrate concentration, consequently, a reduced cellular concentration when compared to other media, it appeared that this medium and clone combination is the most indicated for recombinant protein production. Therefore, the objective of this work was achieved, since the interested proteins were produced. Consequently, this result motivates new studies for production optimization using different cultivation strategies / A leishmaniose visceral, causada pela esp?cie Leishmania chagasi, tamb?m conhecida como calazar, apresentou, no per?odo de 1990 a 2005, taxa de incid?ncia no Brasil variando entre 1 e 3 casos por 100 mil habitantes. A regi?o Nordeste, que at? o ano de 2000 contribuiu com quase 90% dos casos registrados, est? reduzindo sua participa??o na d?cada atual, chegando a 56% em 2005. O alto custo e toxicidade das drogas usadas no tratamento convencional dessa leishmaniose levaram a busca de tratamentos alternativos, com interesse especial na pesquisa e produ??o de ant?genos por microrganismos recombinantes para desenvolvimento de vacinas e kits de diagn?stico. A bact?ria Escherichia coli tem sido o microrganismo mais estudado e usado como hospedeiro para produ??o de prote?nas recombinantes. Nesse contexto, este trabalho tem como objetivo estudar a influ?ncia da indu??o no crescimento celular e a verifica??o do tipo de express?o (intra ou extracelular) de ant?genos de Leishmania chagasi atrav?s de cultivo de dois clones de E. coli recombinante (kmp11 e P36) em incubador rotativo (shaker) usando tr?s meios diferentes (2xTY, TB, FASS+EL). Para isso, foram realizados ensaios em condi??es estabelecidas na literatura para E. coli (37?C ? 200 rpm) e os meios suplementados com antibi?ticos para garantir somente o crescimento de c?lulas competentes. Na primeira etapa, foram realizados ensaios sem indu??o a fim de se verificar o comportamento cin?tico dos dois clones (crescimento e consumo de substrato) nos diferentes meios. Na segunda etapa, a indu??o foi realizada atrav?s da adi??o de IPTG (concentra??o final de 1mM), na primeira hora de cultivo. Foi observada que a express?o das prote?nas foi intracelular para todos os clones e meios testados, entretanto o maior n?vel foi verificado nitidamente pela densidade (intensidade) da banda nos g?is de eletroforese para o meio 2xTY e prote?na kmp11. Apesar de o meio 2xTY conter uma menor concentra??o de substratos, conseq?entemente, uma concentra??o celular reduzida quando comparada aos outros meios, pareceu que esta combina??o de meio e clone ? mais indicada para produ??o das prote?nas recombinantes testadas neste trabalho. O objetivo desse trabalho foi alcan?ado j? que a prote?na de interesse foi produzida. Conseq?entemente, este resultado motiva novos estudos para otimiza??o da produ??o usando diferentes estrat?gias de cultivo

Made available in DSpace on 2016-06-02T19:55:31Z (GMT). No. of bitstreams: 1 4085.pdf: 6460777 bytes, checksum: 9367318799fc091b43ee6716e5057271 (MD5) Previous issue date: 2011-12-22 / Financiadora de Estudos e Projetos / High cell density cultivations of recombinant E. coli are a fast and economical way to produce recombinant proteins. Through this bioprocess, products with high added value and pharmaceuticals of great importance such as insulin, human and bovine growth hormone, protein antigens for formulation of vaccines, enzymes, among others, are obtained. However, keeping these cultivations within the desired conditions becomes a major challenge, since some variables such as dissolved oxygen concentration (DOC) and substrate concentration are difficult to control. Therefore, the development and implementation of an automatic monitoring and control tool are key requirements for the performance of high density cultivation. The present work has as main objectives to study feeding strategies for high cell density cultivation of recombinant Escherichia coli and develop a computational tool capable of ensuring the implementation of the chosen strategies, performing the monitoring, control and supervision of the cultivations. Fed batch cultivations were carried out under the supervision of the tool in a 5 L in-house bioreactor, equipped with sensors for temperature, dissolved oxygen, pH, pressure and biomass (sensor that measures the concentration of viable cells based on permittivity measurements), peristaltic pumps and connected to the gas analyzer. The tool was developed with LabView 8.0 and MatLab 6.5, being the acquisition and communication with the different bioreactor accessories via compact Field Point. Twenty two fed-batch cultivations with 5 different clones of E. coli, BL21(D3) expressing the enzyme penicillin G acylase (PGA) as well as antigenic proteins of S. pneumoniae (PspA3, PspA245 and PspA4Pro) and E. rhusiopathiae (SpaA) were performed during the development of the tool and the studies of feeding strategy. Both defined medium (HDF modified) as complex medium (ZYM-5052 modified), usually having glycerol as main carbon source and IPTG or lactose as inducers were used. In all cultivations, samples were collected to quantify the concentration of cells (dry weight method in filter of 0.22 m and optical density at 600 nm), organic acids, glucose, glycerol and lactose (HPLC) as well as protein expression (densitometry and NIPAB method for PGA) and plasmid stability (plating). The tool SUPERSYS_HCDCR (registered as a free software) developed, implemented and validated in the performed cultivations, carries out the basic functions of bioreactor supervision software, such as monitoring and data acquisition of pressure, temperature, pH, DOC, fraction of CO2 and O2 in the outlet gas as well as real-time estimate of the respiratory quotient, the rate of oxygen consumption and CO2 production. However, it also has the following special features, including: i) automatic control of air and oxygen flow according to cellular demand, ii) automatic activation of the feed pump at the end of the batch; iii) automatic control of feeding flow rate as function of the specific growth rate inferred in real time; iv) automatic control of feeding flow rate constrained by the concentration of dissolved oxygen, v) audible alarms indicating failures in the process; vi) failure messages sent via email; vii) automatic control of dissolved oxygen concentration; viii) control of the bioreactor pressure; and ix) control of bath temperature. Regarding the studies of feeding strategies aimed at biomass productivity increase in high cell density cultivations of recombinant E. coli, using the supervision tool developed together with changes in the composition of the synthetic culture medium available in the literature, a cellular concentrations greater than 150 g/L was achieved in less than 24 hours of cultivation, corresponding to a productivity of 9.2 g/Lh. This value, which is higher than the reported in the literature, was obtained without acetate accumulation and allowing high production of recombinant protein. / Cultivos de alta densidade celular de E. coli recombinante constituem uma tecnica rapida e economica para producao de proteinas recombinantes. Por meio deste bioprocesso, sao obtidos produtos de alto valor agregado e de grande importancia na industria farmaceutica, tais como insulina, hormonios de crescimento humano e bovino, antigenos proteicos para formulacao de vacinas, enzimas, dentre outros. Entretanto, manter estes cultivos dentro das condicoes desejadas se torna um grande desafio, em funcao da dificuldade de controlar variaveis como a concentracao de oxigenio dissolvido (COD) e a concentracao de substrato nos niveis desejados. Por isso, o desenvolvimento e a implementacao de sistemas automaticos de supervisao e controle sao requisitos fundamentais para o bom desempenho de um cultivo de alta densidade. O presente trabalho teve como principais objetivos estudar estrategias de alimentacao para cultivos de alta densidade celular de Escherichia coli recombinante e desenvolver uma ferramenta computacional para suporte na execucao das estrategias escolhidas, realizando o monitoramento, controle e supervisao dos cultivos. Os cultivos em batelada alimentada realizados sob supervisao da ferramenta foram conduzidos em biorreator de 5 L, equipado com sensores de temperatura, oxigenio dissolvido, pH, pressao e biomassa (sensor que mede a concentracao de celulas viaveis a partir dos dados de permissividade), bombas peristalticas e conectado a analisador de gases. A ferramenta foi desenvolvida com os programas LabView 8.0 e MatLab 6.5, sendo a aquisicao e a comunicacao com os diferentes acessorios do biorreator realizada via compact Field Point (National Instruments). Vinte e dois cultivos em batelada alimentada com 5 diferentes clones de E. coli, BL21(D3) expressando a enzima penicilina G acilase (PGA) assim como proteinas antigenicas de Streptococcus pneumoniae (PspA3, PspA245 e PspA4Pro) e de Erysipelothrix rhusiopathiae (SpaA) foram realizados durante o desenvolvimento da ferramenta e dos estudos de estrategia de alimentacao, empregando tanto meio definido (HDF modificado) como meio complexo (ZYM-5052 modificado), tendo glicerol ou glicose como principal fonte de carbono e IPTG ou lactose como indutores. Em todos os cultivos, amostras foram coletadas para quantificar a concentracao de celulas (metodo de massa seca em filtro de 0,22m e leitura da densidade otica a 600 nm), de acidos organicos, glicose, glicerol e lactose (HPLC) e a expressao da proteina (densitometria e metodo NIPAB para a PGA) e a estabilidade de plasmideo (plaqueamento). A ferramenta SUPERSYS_HCDCR (registrada como software livre) desenvolvida, implementada e validada nos cultivos realizados, desempenha as funcoes basicas de softwares de supervisao de biorreatores, tais como: monitoramento e aquisicao de dados de pressao, temperatura, pH, COD, fracao de CO2 e de O2 nos gases de saida; estimativa em tempo real do quociente respiratorio, das velocidades de consumo de oxigenio e de producao de CO2. Esta ferramenta apresenta as seguintes funcionalidades especiais: i) controle automatico das vazoes de ar e de oxigenio de acordo com a demanda celular; ii) acionamento automatico da bomba de alimentacao ao final da batelada; iii) controle automatico da vazao de alimentacao em funcao da velocidade especifica de crescimento inferida em tempo real; iv) controle automatico da alimentacao com restricoes pela concentracao de oxigenio dissolvido; v) alarmes sonoros indicando falhas no processo; vi) envio de mensagens de falhas por email; vii) controle automatico da concentracao de oxigenio dissolvido; viii) controle de seguranca da pressao do biorreator, e ix) controle da temperatura do banho. Em relacao aos estudos das estrategias de alimentacao visando ao aumento da produtividade em biomassa em cultivos de alta densidade celular de E. coli recombinante, com o auxilio da ferramenta de supervisao desenvolvida aliada a modificacoes na composicao do meio de cultivo sintetico disponivel na literatura, foram alcancadas concentracoes celulares maiores que 150 g/L em menos de 24 h de tempo total de cultivo, levando a uma produtividade de 9,2 g/Lh, a qual e superior aos valores relatados na literatura, sem acumulo de acetato e possibilitando elevada producao da proteina recombinante.