Disponibiliza??o do conte?do parcial, conforme Termo de Autoriza??o no trabalho. / Submitted by Jos? Henrique Henrique (jose.neves@ufvjm.edu.br) on 2016-12-21T19:05:57Z No. of bitstreams: 2 license_rdf: 0 bytes, checksum: d41d8cd98f00b204e9800998ecf8427e (MD5) wbiratan_cesar_macedo_oliveira_parcial.pdf: 128173 bytes, checksum: 9c9067430cf3b7ef9b7952182484b258 (MD5) / Approved for entry into archive by Rodrigo Martins Cruz (rodrigo.cruz@ufvjm.edu.br) on 2017-01-31T14:19:01Z (GMT) No. of bitstreams: 2 license_rdf: 0 bytes, checksum: d41d8cd98f00b204e9800998ecf8427e (MD5) wbiratan_cesar_macedo_oliveira_parcial.pdf: 128173 bytes, checksum: 9c9067430cf3b7ef9b7952182484b258 (MD5) / Made available in DSpace on 2017-01-31T14:19:01Z (GMT). No. of bitstreams: 2 license_rdf: 0 bytes, checksum: d41d8cd98f00b204e9800998ecf8427e (MD5) wbiratan_cesar_macedo_oliveira_parcial.pdf: 128173 bytes, checksum: 9c9067430cf3b7ef9b7952182484b258 (MD5) Previous issue date: 2016 / Coordena??o de Aperfei?oamento de Pessoal de N?vel Superior (CAPES) / Funda??o de Amparo ? Pesquisa do Estado de Minas Gerais (FAPEMIG) / Conselho Nacional de Desenvolvimento Cient?fico e Tecnol?gico (CNPq) / Neste trabalho foi estudado o comportamento de extra??o do lant?nio em sistemas aquosos bif?sicos (SAB) e foi desenvolvido um novo m?todo hidrometal?rgico ambientalmente seguro para a extra??o seletiva de La a partir de lixiviado de baterias NiMH. O comportamento de extra??o do La foi avaliado verificando a influ?ncia dos seguintes par?metros: presen?a e concentra??o de diversos agentes extratantes (Alaranjado de xilenol, 1-(2-piridilazo)-2-naftol, Ditizona, 8-hidroxiquinolina, e 1,10-fenantrolina); pH (3,00, 6,00 e 9,00); eletr?lito (Li2SO4, Na2SO4, MgSO4, Na2C4H4O6 e Na3C6H5O7 ) e pol?mero (L64 e PEO1500) formadores do sistema. A efici?ncia de recupera??o foi avaliada atrav?s da an?lise da porcentagem de extra??o (% E) e as melhores condi??es de extra??o do analito foram obtidas no SAB formado por PEO1500 + Li2SO4 + H2O, pH = 6,00; empregando o extratante 1,10-fenantrolina, atingindo um valor m?ximo de %E = 74,1 %. Na sequencia o m?todo foi aplicado a um lixiviado de bateria NiMH. Os terras raras foram precipitados mediante ajuste de pH (2,50) e posteriormente solubilizado em solu??o de H2SO4 0,1 M. Ap?s 3 etapas sucessivas de extra??o foram obtidos altos valores de fator de separa??o (S) entre o analito e os concomitantes met?licos (SLa,Co = 6.3 x 103, SLa,Ni= 2,55 x 104, SLa,Fe= 1,15 x 103 and SLa,Ce= 30,9). Al?m disso, foi realizado um ensaio de stripping no qual 88,5% de La, em uma ?nica etapa, foi redisponibilizado sob a forma i?nica na FI para uma poss?vel etapa posterior de eletrodeposi??o. / Disserta??o (Mestrado) ? Programa de P?s-Gradua??o em Qu?mica, Universidade Federal dos Vales do Jequitinhonha e Mucuri, 2016. / In this work was investigated the extraction behavior of lanthanum in the aqueous two-phase system (ATPS) and new environmentally safe hydrometallurgical method was developed for the selective extraction of La from NiMH battery leachate. The extraction behavior of La was evaluated verifying the influence of the following parameters on the metals extraction: presence and concentration of the several extractants 1-(2-piridil-azo)-2-naphtol, dithizone, 8-hydroxyquinoline, 1-10 phenanthroline and xylenol oragne; pH (3.00, 6.00 and 9.0); ATPS-forming electrolyte ((Li2SO4, Na2SO4, MgSO4, Na2C4H4O6 e Na3C6H5O7); ATPS-forming polymer (L64 or PEO1500). The recovery efficiency was evaluated through analyzing the extraction percentage (%E) and the best conditions for analyte extraction were achieved for the PEO1500 + Li2SO4 ATPS, pH = 6.00, using 1-10 phenanthroline as extractant agente (%E = 74,1 %). In the following section, the method was applied to a real NiMH battery leachate. The rare earths were precipitated by pH adjustment (2.50), which was solubilized in 0,1 M H2SO4 solution. After 3 steps of successive extractions it was possible to obtain high separation factor (S) values between the analyte and mettalic concomitant (SLa,Co = 6.3 x 103, SLa,Ni = 2,55 x 104, SLa,Fe = 1,15 x 103 and SLa,Ce = 30,9). Moreover, a stripping assay was carried out and after one single step, 88.5% of lanthanum was available to a possible electro winning step.

Data de aprova??o ausente. / Submitted by Jos? Henrique Henrique (jose.neves@ufvjm.edu.br) on 2017-03-29T18:49:58Z No. of bitstreams: 2 license_rdf: 0 bytes, checksum: d41d8cd98f00b204e9800998ecf8427e (MD5) wagner_barbosa_souza.pdf: 2617971 bytes, checksum: 3d7e6b01cafdb0a61d93af504071663c (MD5) / Approved for entry into archive by Rodrigo Martins Cruz (rodrigo.cruz@ufvjm.edu.br) on 2017-04-24T16:36:52Z (GMT) No. of bitstreams: 2 license_rdf: 0 bytes, checksum: d41d8cd98f00b204e9800998ecf8427e (MD5) wagner_barbosa_souza.pdf: 2617971 bytes, checksum: 3d7e6b01cafdb0a61d93af504071663c (MD5) / Made available in DSpace on 2017-04-24T16:36:52Z (GMT). No. of bitstreams: 2 license_rdf: 0 bytes, checksum: d41d8cd98f00b204e9800998ecf8427e (MD5) wagner_barbosa_souza.pdf: 2617971 bytes, checksum: 3d7e6b01cafdb0a61d93af504071663c (MD5) Previous issue date: 2016 / Com o avan?o exponencial da ind?stria de eletr?nicos, o consumo destes produtos tamb?m est? crescendo largamente. Com isso, os descartes destes equipamentos tamb?m crescem na mesma propor??o. Por ano, no mundo, estima-se que mais de 25 milh?es de toneladas de lixo eletr?nico sejam descartadas. Neste trabalho foi desenvolvido um novo m?todo hidrometal?rgico ambientalmente seguro para a extra??o seletiva de cobre, n?quel e prata provenientes de res?duos de placas de circuito impresso (PCI), empregando Sistemas Aquosos Bif?sicos (SAB) como t?cnica de extra??o. O comportamento de extra??o dos ?ons met?licos Cu (II), Ni(II), Fe(III) e Ag(I)em SAB formado por copol?mero tribloco L64 + MgSO4 + H2O foi avaliado para a otimiza??o do m?todo, verificando a influ?ncia dos seguintes par?metros experimentais sobre a extra??o dos analitos: valores de pH do SAB (3,0; 6,0; 9,0 e 11,0); natureza e concentra??o dos agentes extratores 1-(2-piridil-azo)-2-naftol (PAN) para os estudo de extra??o do Cu(II), 1-nitroso-2-naftol (1N2N) e dimetilglioxima (DMG) para a extra??o do ?on Ni(II), tiocianato (SCN) e ditizona (Dz) para a extra??o da Ag(I). A efici?ncia de recupera??o seletiva dos metais foi avaliada por meio da an?lise da porcentagem de extra??o (%E) e do fator de separa??o (S) entre os ?ons de interesse. As melhores condi??es para extra??o seletiva foram: PAN [3,5 mmol.Kg-1] em pH = 6,0 em 6 etapas consecutivas para separa??o do Cu(II), DMG [5,00 mmol.Kg-1] em pH = 9,0 para o Ni(II) e SCN[5,20 mmol.Kg-1] em pH = 9,0 para a Ag(I) . Em todas as situa??es foram obtidos valores de fator de separa??o(S) entre o analito e os concomitantes met?licos maiores que 103. As condi??es ?timas obtidas foram aplicadas ao lixiviado de PCI para a extra??o de cobre, n?quel e prata de forma sequencial, obtendo-se altos valores de S entre o analito e os concomitantes met?licos (SCu,Ni= 1,46 x 103, SCu,Fe= 1,55 x 104, SCu,Ag= 1,59 x 104, SNi,Fe= 3,27 x 104, SNi,Ag= 3,47 x 104 eSAg,Fe= 4,80 x 103).Ap?s a extra??o de cada metal foi realizado um estudo de stripping em uma ?nica etapa, onde 89,5%, 92,5% e 82,5% de Cu(II), Ni(II) e Ag(I), respectivamente foram disponibilizados para a etapa de eletrodeposi??o. Portanto o m?todo utilizando SAB se mostrou eficiente e dentro dos princ?pios da qu?mica verde, pois utiliza componentes at?xicos, biodegrad?veis e recicl?veis e de r?pida separa??o de fases sem a forma??o de emuls?es est?veis. Sendo um m?todo alternativo para a extra??o liquido ? liquido tradicional. / Disserta??o (Mestrado) ? Programa de P?s-Gradua??o em Qu?mica, Universidade Federal dos Vales do Jequitinhonha e Mucuri, [2016]. / With the exponential advancement of electronic industry, the consumption of these products is also growing wide. With this, the drops of this equipment also grow at the same rate. A year in the world, it is estimated that more than 25 million tons of electronic waste are disposed.This work developed a new environmentally safe hydrometallurgical method for the selective extraction of copper, nickel and silver from waste printed circuit board (PCB) using Aqueous Two-Phase Systems (SAB) as extraction technique. The extraction behavior of metal ions Cu (II), Ni (II), Fe (III) and Ag (I) SAB formed by tri-block copolymer L64 + MgSO4 + H2O was evaluated for the optimization of the method by checking the influence of the following experimental parameters on the extraction of analytes: the SAB pH (3.0, 6.0, 9.0 and 11.0); nature and concentration of agents extractors 1- (2-pyridyl-azo) -2-naphthol (PAN) Cu for the extraction method (II), the 1-nitroso-2-naphthol (1N2N) and dimethylglyoxime (DMG) for ion extraction Ni (II), thiocyanate (SCN) and dithizone (Dz) for the extraction of Ag (I).The selective metal recovery efficiency was evaluated by the percentage extraction analysis (% E) and separation factor (S) between the ions of interest. The best conditions for selective extractions were NAP [3,5 mmol.Kg-1] at pH 6.0 in 6 consecutive stages for separation of Cu (II) DMG [5.00 mmol.Kg-1] pH = 9.0 for Ni (II) and SCN [5,20 mmol.Kg-1] at pH = 9.0 for Ag (I). In all cases they were obtained separation factor values (S) between the analyte and the larger metal Concomitant 103. The obtained optimum conditions were applied to the PCI leached copper extraction, nickel and silver sequentially, yielding if high S values between the analyte and the metal concomitant (SCU, Ni = 1.46 x 103, SCU, Fe = 1.55 x 104, SCU, Ag = 1.59 x 104, SNI, Fe = 3.27 x 104, SNI, Ag = 3.47 x 104 and SAg, Fe = 4.80 x 103).After extraction of each metal it was made a study stripping in one step, where 89.5%, 92.5% and 82.5% Cu (II), Ni (II) and Ag (I), respectively, were available for the electroplating step. Therefore, the method using BSA was efficient and within the principles of green chemistry, because it uses non-toxic, biodegradable and recyclable and fast phase separation without the formation of stable emulsions components. As an alternative method for liquid - liquid extraction traditional.

O ácido clavulânico (AC) é um potente inibidor de β-lactamases, sendo utilizado em associação com antibióticos β-lactâmicos. Atualmente, a purificação industrial do AC envolve, principalmente, processos de extração líquido-líquido com solventes orgânicos e etapas cromatográficas. Assim, métodos alternativos como os sistemas micelares de duas fases aquosas (SMDFA), os quais oferecem seletividade na partição de biomoléculas de acordo com sua hidrofobicidade, são de grande interesse. O presente trabalho teve como objetivo estudar a partição do AC em sistemas micelares não iônicos de duas fases aquosas, puros e com adição do sal (NH4)2SO4 ou do polímero sulfato de dextrana (Dx-S). Os estudos de estabilidade do AC mostraram que o fármaco é mais estável em pH 6,5 e temperaturas mais baixas (5 - 20 ºC). Em relação à presença dos aditivos, foi verificado que a adição do Dx-S acarretou em menor perda da estabilidade do AC quando comparado ao (NH4)2SO4, com valor residual ≥ 90% a 35 °C. Na presença dos tensoativos Triton X-114 e Triton X-100, o AC apresentou-se estável, com valor residual de aproximadamente 100%. De acordo com os ensaios de partição, o AC foi recuperado preferencialmente na fase pobre em micelas, tanto nos sistemas TX/tampão quanto TX/sal para ambos os tensoativos, com valores de coeficiente de partição (KAC) ~ 0,7 e rendimento na fase diluída (Yclavd) ~ 75%. A adição do polímero em maiores concentrações (≥ 8% p/p) proporcionou um pequeno aumento nos valores de KAC, porém com valores ainda próximos a 1 - 1,5. Portanto, os resultados demonstraram que a presença dos aditivos não influenciou suficientemente a partição do AC para a fase micelar e, desta maneira, os sistemas TX/tampão mostraram ser mais eficientes para a recuperação do ácido clavulânico na fase pobre em micelas, podendo ser empregados como etapa prévia de extração em um processo biotecnológico. / Clavulanic acid (CA) corresponds to a potent β-lactamase inhibitor that is used in association with β-lactamic antibiotics. The industrial purification of CA usually involves liquid-liquid extraction processes employing organic solvents followed by several chromatographic steps. Therefore, new purification alternatives such as aqueous two-phase micellar systems (ATPS) are of great interest. These systems can provide selectivity in biomolecule partitioning according to hydrophobicity and other molecular properties. Within this context, the main goal of this study was to investigate CA partitioning in aqueous two-phase micellar (nonionic) systems, with and without the addition of (NH4)2SO4 or dextrane sulfate (Dx-S). Stability studies performed with CA indicated that the drug is more stable at pH 6.5 and lower temperatures (5 - 20 ºC). In addition, it was demonstrated that Dx-S addition led to a lower loss of CA stability in comparisson to (NH4)2SO4, with residual values ≥ 90% at 35 °C. The drug was found to be very stable in the presence of the surfactants Triton X-114 and Triton X-100, with residual values around 100%. Regarding CA partitioning in the ATPMS, the drug partitioned preferentially to the micelle-poor phase, irrespective of the surfactante employed and of the presence of (NH4)2SO4,with partition coefficient (KAC) ~ 0.7 and yield in the poor phase (Yclavd) ~ 75%. Nonetheless, the addition of Dx-S in concentrations (≥ 8.0% p/p) resulted in a discrete increase in KAC, with values around 1 - 1.5. Therefore, the results obtained in this work demostrated that the addition of (NH4)2SO4 or Dx-S to ATPMS did not significantly influenced CA partitioning to the micelle-rich phase and, in this context, the systems investigated could be considered more eficiente for CA recovery in the micelle-poor phase, as a previous extraction step of a biotechnological process.

Nesta tese foi estudada a influência da recirculação do percolado, ajustando as melhores taxas e freqüências, para degradação da fração orgânica dos resíduos sólidos urbanos, em sistema de batelada de uma e duas fases (híbrido). Foram utilizados reatores de 3,45 litros preenchidos com resíduo sólido urbano padrão (FORSUp), percolado como inóculo e um filtro anaeróbio como reator metanogênico. Foram testadas as taxas de recirculação do inóculo de 1%, 2,5%, 5%, 10%, 20%, 30% e 50% e seu monitoramento feito por análises físico-químicas e microbiológicas. O reator que apresentou melhores valores de produção de metano e redução de DQO foi aquele com taxa de recirculação de 20% do percolado metanogênico. Na segunda etapa foram operados três digestores de 50L, alimentados com a FORSUp com as melhores taxas de recirculação determinadas na primeira etapa desse trabalho e a obtida no trabalho de Salgado (2003). Um reator simulou o reator acidogênico de um sistema de duas fases, no qual 20% de seu inóculo foi injetado em um filtro anaeróbio (com tempo de detenção hidráulico de 24 horas). Um outro sistema com taxa de 10% de recirculação de percolado foi operado como reator de uma fase. Outro reator, inoculado com a mesma quantidade de FORSUp e percolado, porém, não se realizou qualquer recirculação do seu inóculo (controle), servindo para comparar os digestores de uma e duas fases. O sistema de duas fases, comparado aos demais reatores, confirmou que a taxa de recirculação de 20%, obteve maior eficiência na partida, com elevada produção de metano e maior percentual de degradação de sólidos. Os exames microscópicos realizados em amostras de percolado desses reatores revelaram predominância de organismos de morfologia com características de Methanococcus e Methanosarcina. Concluiu-se que a taxa de recirculação de percolado influi significativamente nos reatores degradando a matéria orgânica. O estudo cinético confirmou que o processo de digestão obedece a cinética das reações em série, com elevados valores de k´1 / This thesis studied the influence of the leachate recirculation, adjusting to the best rates and frequencies, for degradation of the organic fraction of the urban solid wastes, in one and two-phases (hybrid) system. Bioreactors of 3.45 L were used and filled out with OFMSW pattern, leachate as seed and an anaerobic filter as methanogenic reactor. The performance of the reactors was analyzed varying recirculation rates (1, 2.5, 5, 10, 20, 30 and 50 % in volume of seed). Leachate samples from these reactors were examined through microscopical examinations and physical-chemical analyses to evaluate its performance. The reactor with 20% recirculation rate, got larger efficiency in the departure, methane production and percentage of solid degradation, compared to the others reactors. In the second stage, three 50L digesters were operated and fed with standard OFMSW with the best recirculation rates of the first stage and the best rate obtained in Salgado (2003). A bioreactor simulated the acidogenic reactor of a two-phase system, in which 20% of its seed was injected in anaerobic filter (with hydraulic detention time of 24 hours). Another system, with 10% of recirculation rate of leachate was operated in a one-phase reactor. Once more bioreactor, inoculated like others, however, without any recirculation were studied to compare with one and two-phase reactor. The two-phase system confirmed that the 20% recirculation rate, compared to the others reactors, obtained better efficiency with high methane production and solid degradation. The microscopical examinations in the leachate samples from this reactor presented predominance of organisms with characteristical morphology from Methanococcus and Methanosarcina. It was concluded that the leachate recirculation has significant influence in the degradation of organic matter bioreactors. The kinetic study confirmed that the anaerobic process for OFMSW proceed the in series kinetics, with high constants values of first order

Submitted by Fabio Sobreira Campos da Costa (fabio.sobreira@ufpe.br) on 2017-07-28T13:17:05Z No. of bitstreams: 2 license_rdf: 811 bytes, checksum: e39d27027a6cc9cb039ad269a5db8e34 (MD5) DISSERTAÇÃO.pdf: 1904426 bytes, checksum: 881aba48363b69adb462f39f38edbbe8 (MD5) / Made available in DSpace on 2017-07-28T13:17:05Z (GMT). No. of bitstreams: 2 license_rdf: 811 bytes, checksum: e39d27027a6cc9cb039ad269a5db8e34 (MD5) DISSERTAÇÃO.pdf: 1904426 bytes, checksum: 881aba48363b69adb462f39f38edbbe8 (MD5) Previous issue date: 2016-02-23 / As proteases são enzimas com a capacidade de hidrolisar proteínas em peptídeos menores ou aminoácidos livres, sendo essenciais para animais, plantas e micro-organismos devido à sua atuação na regulação metabólica. As proteases são utilizadas com diversas finalidades, no processo industrial da fabricação de detergentes, na indústria farmacêutica e de alimentos, além de ser utilizada na recuperação e aproveitamento de resíduos e subprodutos. Em virtude da grande importância das proteases este trabalho teve como objetivo comparar a produção de proteases produzidas por Mucor subtilissimus UCP 1262 em fermentação em estado sólido (FES) e submersa (FS), bem como extrair em Sistema de duas fases aquosas (SDFA) PEG/Fosfato, as colagenases oriundas de ambas as fermentações. O meio de produção da FES e FS no qual o micro-organismo foi cultivado era constituído principalmente de farelo de soja e farinha de soja. As determinações enzimáticas e dosagem proteica foram realizadas após 72h de fermentação. Para montagem do SDFA foram realizados dois planejamentos fatoriais 23, o primeiro planejamento foi realizado com amostras da FES e o segundo com amostras da FS. Neste sistema foi analisada a influência de três variáveis no processo de extração: massa molar do PEG (200, 550 e 1000 g/mol), concentração do PEG (17,5; 20 e 22,5%) e concentração do sal fosfato de sódio (15; 17,5 e 20%). A maior produção de proteases (362,66 U/ml) ocorreu na FES, enquanto que na FS obteve-se apenas 26,33 U/ml. Dentre as atividades proteásicas específicas: colagenolítica, fibrinolítica e queratinolítica, os melhores resultados foram obtidos para a atividade colagenolítica, sendo esta de: 179,81 U/ml, em FES. A colagenase presente no extrato bruto obtida nos processos fermentativos foram particionadas para fase rica em PEG do SDFA. O maior valor para a variável resposta Fator de purificação (FP=3,49) foi obtido no sistema que utilizou o extrato obtido por FES. Com base nas condições estudadas, os dois sistemas mostraram-se viáveis para a extração de colagenase, pois além de ser um processo que pode ser utilizado em larga escala é constituído por componentes de baixo custo e as condições utilizadas no SDFA favoreceram a extração desta enzima. Todavia, a extração da colagenase oriunda da FES foi mais promissora em virtude da maior concentração da enzima de interesse encontrada nesse tipo de fermentação. / Proteases are enzymes with the ability to hydrolyze proteins into smaller peptides and free amino acids. They are vital for animals, plants and micro-organisms due to their role in metabolic regulation. Proteases have been used in various purposes, in the industrial process of detergents, pharmaceutical and food industry, as well as being used in the recovery and utilization of waste and by-products. Due to their economic feasibility and great medical and farmaceutical importance this study aimed to compare the production of proteases produced by Mucor subtilissimus UCP 1262 in solid state fermentation (SSF) and submerged fermentation (SF) as well as extract collagenolytic proteases using Aqueous two-phase system (ATPS) -PEG/Phosphate from both fermentations. The medium composition for the fungal fermentation in SSF and SF was based in soybean flour. Enzymatic determinations and protein levels were performed after 72 hours of fermentation. To mount the ATPS were two 23 factorial design, the first planning was carried out with samples of SSF and the second with samples of SF. In this system was analyzed the influence of three variables in the extraction process: PEG molar mass (200, 550 and 1000), the PEG concentration (17,5; 22,5 and 20%) and sodium phosphate salt concentration (15; 17,5 and 20%). The higher proteolytic activity (362,66 U/ml) was produced using SSF, while in the FS was obtained 26,33 U/ml. Among the specific proteolytic activities: collagenolytic, fibrinolytic and keratinolytic, the best results were obtained for the collagenolytic activity, this being: 179,81 U / ml in the SSF. The Collagenase present in the crude extract obtained in the fermentative processes partitioned preferencially to the PEG-rich phase. The highest value for the variable response Purification Factor (PF = 3,49) was obtained in the system that used SSF crude extract. According with the showed results, both extraction systems seemed to be feasible for collagenase extraction, as well as being a process that can be used in large scale, constituted by low cost components and conditions used in this ATPS favored the enzyme extraction. Furthermore, the collagenase extraction from the SSF was more promising because of the higher interest enzyme concentration found in this type of fermentation.

The two techniques aqueoustwo-phase partitioning and expanded bed adsorption that bothare suitable for primary protein recovery were studied. Most ofthe work was focused on partition in aqueous two-phase systemsand in particular on the possibility to effect the partitionbehaviour by fusion of short peptide tags or protein domains tothe target protein. The partitioning of fusionproteins between different variants of the domain tag Z and thenaturally occurring protein DNA Klenow polymerase were studiedin Breox/Reppal aqueous two-phase systems. Most studies wereperformed with cell homogenate. The Breox/Reppal system was infocus because if the fusion protein can be partitioned to theBreox-rich top phase the next step can be a thermoseparatingaqueous two-phase system. When the Breox phase is heated to50°C it switches from a one-phase system to a two-phasesystem resulting in an almost pure water rich top phase andhighly concentrated Breox-rich bottom phase. The Breox can thenbe reused and the protein recovered from the water phase. TheZ-domain was genetically modified in different ways to Zbasic1, Zacid2and Ztrp12and fused to the Klenow protein to try toenhance partitioning to the Breox-rich phase. From theexperiments it was not possible to observe any effects on thepartition behaviour irrespectively of tested properties of thedomain tag. Despite the absence of domain tag effects highK-values, i.e. partition to the Breox-rich top phase, wereobserved in the Breox/Reppal system. However, the proteinK-values seemed to be rather sensitive to the cell homogenateload and showed a tendency to decrease with increased cellhomogenate load. Also increased phosphate concentration reducedthe K-values. The partitioning of cell debris also seemed todependent on the cell homogenate load. At higher homogenateload (&lt;=20g DW/L) clear Breox-rich top phases were observedwith the cell debris collected in Reppal-rich bottomphases. Two different tetrapeptides,AlaTrpTrpPro and AlaIleIlePro were inserted near the C-terminusof the protein ZZT0. The Trp-rich peptide unit stronglyincreased both the partitioning of ZZT0 into the poly(ethyleneglycol) (PEG)-rich phase in a PEG/potassium phosphate aqueoustwo-phase system and its retention on PEG and propylhydrophobic interaction chromatographic columns with potassiumphosphate as eluent in isocratic systems. Both the partitioningand the retention increased with increasing number of Trp-richpeptide units inserted into ZZT0. Insertion of Ile-richtetrapeptide units affected the partitioning and retention to amuch lesser extent. Partition and modelling data also indicateda folding of inserted Trp and Ile tetrapeptide units, probablyto minimise their water contact. It was also investigated howto predict the partitioning of proteins in isoelectricPEG/phosphate aqueous two-phase systems. The capture ofß-galactosidase fromE. colicell homogentate (50g DW/L) by metal chelatexpanded bed adsorption was studied. These experiments showedthat capture, with a certain degree of selectivity, andclarification of ß-galactosidase could be achieved from acell homogenate. However, a rather low recovery of about 35 %was obtained at a capacity of 0.25mg/mL of gel. Thus, severalparameters remain to be optimised like the load buffercomposition and the cell homogenate load. <b>Keywords:</b>E. coli, aqueous two-phase systems, fusion proteins,hydrophobic interaction chromatography, expanded bedadsorption, ß-galactosidase, Klenow polymerase, Z-domain,peptide tags / NR 20140805

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”Durable water repellents (DWR) är textilimpregneringar som bidrar med vattenavvisande egenskaper som håller länge på funktionella tyg. Tyvärr är dessa hydrofobiska ytbehandlingar vanligtvis en källa till skadliga och persistenta kemikalier och de även är producerade från fossilbaserade resurser. Eftersom medvetenheten kring de här problemen har ökat, har innovativa, miljövänliga och biologiskt nedbrytbara alternativ tagits fram. Hittills finns dock inga produkter gjorda av 100% förnybara råvaror. I ett försök att utveckla en biobaserad, icke-giftig DWR som aktiveras under milda förhållanden, lades fokus på utveckling av en lagringsstabil sprayimpregneringsprodukt för hemmabruk. Vid formulering av emulsionerna/dispersionerna utvärderades en stor mängd biobaserade och kommersiellt tillgängliga hydrofobiska och amfifila molekyler med avseende den vattenavvisande effekt som de bidrog med på den behandlade textilen. Samtidigt bedömdes de producerade formuleringarna noggrant för att skapa förståelse om effekterna från ingredienserna och deras relation till produktens stabilitet. De kandidatprodukter som valdes ut och undersöktes vidare hade lovande vattenavvisande egenskaper och visade rimlig hållbarhetstid på åtminstone en månad i 40 °C. Standardiserade sprayscores på 3 (där 1 är sämst och 5 är bäst) nåddes efter 24 timmars hängtorkning i rumstemperatur. Dessutom uppnåddes sprayscore på 5 efter en kort, icke-industriell torktumling på låg temperatur och den behölls efter minst tio tvättar på syntetiska textiler. Utvalda produkter påverkade inte märkbart tygets andningsförmåga och majoriteten hade ingen influens på textilens mjukhet och färg. Förutom uppskalningsexperiment och partikelstorleksmätningar, granskades resultat med en tillämpningsstudie av formuleringarna på femton olika tygtyper. Produkternas effekter på utseende och känsla dokumenterades för de olika textilierna. Egenskaper som kontaktvinklar, sprayscores och tvättbeständighet bestämdes och jämfördes med en kommersiellt tillgänglig produkt. / Durable water repellents (DWR) are textile finishes that provide long-lasting water repelling properties to functional garments. However, these hydrophobic finishes are commonly a source of polluting and persistent chemicals and are produced from fossil resources. As a result of increasing awareness, innovation towards environmentally friendly and biodegradable alternatives has progressed, yet no 100% renewable sourced products are available. In an attempt to create a bio-based, non-toxic DWR, that is curable under mild conditions, focus was put on the development of a shelf stable spray impregnation product intended for consumer use. By formulating dispersion/emulsion systems, a wide variety of commercially available, renewable sourced amphiphilic and hydrophobic molecules were evaluated on their effect on the water repelling performance of treated textile fabrics. Simultaneously, the produced systems were assessed carefully to create understanding on the effect of substances and their corresponding ratios on the stability. Promising candidate products that were selected for further investigation showed reasonable stability for 1 month at 40 °C. Industrial standard spray ratings of 3 (where 1 is worst and 5 is best) after hang drying at room temperature could be reached within 24 hours. On top of that, spray ratings of 5 could be reached after short time, non-industrial tumble drying at low temperatures, which could even be retained for at least ten laundering cycles on synthetic textiles. The selected finishes did not have a measurable effect on the breathability of the treated fabrics, while the majority did not considerably affect the hands-feeling or colour of the textiles. Besides several scaling up experiments and particle size measurements, extrapolation of the findings was carried out by testing the developed formulations on fifteen different types of textiles. Effects on appearance and feel were documented, additionally, contact angle, spray score, and wash durability were determined and compared with a commercially available product.

A utilização de resíduos agrícolas visando à produção de insumos por via biotecnológica tem se mostrado importante uma vez que estes resíduos são fontes renováveis de carbono. A fração hemicelulósica destes resíduos apresenta como componente principal a xilose, que pode ser utilizada como substrato em processos de bioconversão para a obtenção de produtos com valor agregado. Um destes produtos é a enzima glicose-6-fosfato desidrogenase (G6PD), primeira enzima da via das pentoses fosfato que pode ser utilizada como reagente analítico em análises quantitativas, sobretudo em estudos bioquímicos e médicos. O presente trabalho visou estudar o processo de purificação dessa enzima empregando a extração em sistemas de duas fases aquosas convencional (sem integração) e integrado ao rompimento celular, em duas escalas, reduzida e ampliada. A enzima foi produzida por Candida guilliermondii FTI 20037 cultivada em meio constituído de hidrolisado hemicelulósico de palha de arroz, sob condições pré-determinadas. Inicialmente, foram realizados ensaios para avaliar o efeito das variáveis volume de suspensão celular, velocidade de agitação do moinho de esferas de vidro e tempo sobre o rompimento das células. Os valores destas variáveis foram, então, estabelecidos em: 100 mL, 400 rpm e 25 minutos, respectivamente. Posteriormente, a influência da massa molar de PEG e comprimento de linha de amarração sobre a extração da G6PD foram investigados no sistema convencional (homogeneizado obtido a partir do rompimento celular, em presença ou ausência de fragmentos) e integrado (rompimento na presença dos componentes da extração), empregando-se a metodologia do planejamento experimental. Nos ensaios realizados em escala reduzida, sob condições otimizadas, alcançou-se um fator de purificação na fase rica em sal (FPf), ou fase fundo, de 2,8 e em maior escala, ou seja, em moinho de rompimento, de 1,3. Com isso, realizou-se o estudo cinético e termodinâmico empregando a enzima presente no homogeneizado antes da purificação e após purificada no processo integrado em escala reduzida, nas seguintes condições: TLL 40% e PEG 1500 mol/L. Os valores determinados para os parâmetros cinéticos foram Km, 0,07 e 0,05 mM, Vm, 34,8 e 19,1 U/L e dos parâmetros termodinâmicos &#916;G, -13,71 e -13,64 KJ/mol; &#916;H, -2,49 e -2,50 KJ/mol; &#916;S, 37,02 e 36,77 J/mol.K; Ea, 24,18 e 15,02 KJ/mol, da enzima presente no homogeneizado celular antes e após purificação, respectivamente. / The employment of agricultural residues aiming the attainment of biotechnological products has been shown its importance since these residues are renewable and low cost sources of carbon. The hemicellulosic fraction of these residues presents xylose as main component, which can be utilized as substrate for different bioconversion processes for the acquisition of high value products. As an example, glucose-6-phosphate dehydrogenase, the first enzyme of pentose phosphate pathway which can be used as analytical reagent in several quantitative analysis, mainly in biochemical and medical studies. The present work contemplated the study of glucose-6-phosphate (G6PD) purification process by a conventional aqueous two phase systems extraction and integrated with cell disruption, in two scales, reduced and increased. The enzyme was obtained from cells of Candida guilliermondii FTI 20037 grown in hemicellulosic rice straw hydrolysate, using conditions established in previous work. Initially, assays in bead mill were performed to determine the effect of cell suspension volume, agitation speed and time on cell disruption. The determined conditions were: 100 mL, 400 rpm and 25 minutes, respectively. After this, the influence of molar mass of PEG and tie line lenght (TLL) on the G6PD recovery were investigated in the conventional system (with previous disrupted cells, with or without cell fragments) and integrated (disruption in the presence of extraction components), using the experimental design methodology. In the reduced scale assays, in optimized conditions, a purification factor in salt rich phase (FPf), or bottom phase, of 2,8 was reached while in the increased scale, this means in bead mill, a FPf of 1,3 was attained. In addition, kinetic and thermodynamic studies were performed, employing the enzyme present in the homogenate before and after purification in reduced scale, in the following conditions: TLL of 40% and PEG 1500 mol/L. The established values for the kinetics parameters were Km, 0,07 and 0,05 mM, Vm, 34,8 and 19,1 U/L and of thermodynamics &#916;G, -13,71 and -13,64 KJ/mol; &#916;H, -2,49 and -2,50 KJ/mol; &#916;S, 37,02 and 36,77 J/mol.K; Ea, 24,18 and 15,02 KJ/mol, of the enzyme present in the homogenate before and after purification respectively.

A partição e purificação de ascorbato oxidase de abóbora (Cucurbita maxima) por extração líquido-líquido em sistema de duas fases aquosas (SDFA), pelos processos descontínuos e contínuos, utilizando coluna de discos rotativos perfurados (PRDC), foram estudadas. Foram utilizados planejamentos estatísticos para selecionar as variáveis significativas no processo descontínuo de purificação, e as variáveis estudadas foram massa molar e concentração do polietileno glicol (PEG), concentração de citrato, pH, concentração de NaCl, fator de diluição e massa total do sistema. Os melhores resultados (coeficiente de partição 1,72, recuperação 90,8% e aumento de pureza 3,12) foram obtidos nas seguintes condições: massa molar do PEG 20000 (g/mol), pH 6,0, concentração de PEG 25% (m/m) e concentração de citrato 10% (m/m). No valor de pH 6,0 e temperatura 35°C a ascorbato oxidase apresentou seus maiores valores de atividade, e manteve a estabilidade na faixa de pH 5,0 a 9,0 durante 36 horas e a temperaturas de até 40°C durante 1 hora. Experimentos também foram realizados para estimar as principais propriedades cinéticas e termodinâmicas da atividade e estabilidade da ascorbato oxidase, e esse estudo revelou que a enzima foi estável nas condições testadas. A PRDC mostrou um bom desempenho para extração da ascorbato oxidase em modo contínuo utilizando SDFA. A melhor condição operacional selecionada neste estudo foi selecionada com o auxílio de planejamentos estatísticos, sendo selecionadas as seguintes condições: massa molar do PEG 20000 (g/mol), concentração de PEG 20% (m/m), concentração de citrato 10% (m/m), velocidade de rotação dos discos de 80 rpm e velocidade da fase dispersa de 2 mL/min. Os melhores resultados em valores médios foram: coeficiente de partição 3,36, recuperação 152%, aumento de pureza 2,31, coeficiente de transferência de massa 0,045, eficiência de separação 43,7% e hold up 0,33. Os dados experimentais demonstram o potencial da aplicação do sistema de duas fases aquosas PEG/citrato para purificar a ascorbato oxidase utilizando coluna de discos rotativos perfurados. / The partition and purification of ascorbate oxidase from pumpkin (Cucurbita maxima) by liquid-liquid extraction in aqueous two-phase system (ATPS) by discontinuous and continuous process, using perforated rotating disc contactor (PRDC) was studied. Experimental designs were used to choose the significant variables for discontinuous process, and polyethylene glycol (PEG) molar mass and concentration, citrate concentration, pH, NaCl concentration, dilution factor and total mass of the system, were the variables studied. The better results (partition coefficient 1.72, recovery 90.8% and purification factor 3.12) were obtained with following conditions: PEG molar mass of 20000 g/mol, pH 6.0, PEG concentration of 25% (w/w) and citrate concentration of 10% (w/w). In the pH 6.0 and temperature of 35?C the ascorbate oxidase showed their high activity values and the enzyme was stable in the pH range of 5.0 to 9.0 during 36 hours and temperatures up to 40?C for 1 hour. Experiments were also conducted to estimate the main kinetic and thermodynamic properties of ascorbate oxidase activity and stability, and this study revealed the interesting stability of this enzyme. The PRDC showed a good performance for extracting in continuous mode using aqueous two-phase systems. The best operating condition was selected in this study for the extraction of ascorbate oxidase in the PRDC, and it was obtained with PEG molar mass of 20000 g/mol, PEG concentration of 20% (w/w) and citrate concentration of 10% (w/w), the disc rotational speed of 80 rpm and dispersed phase flowrate of 2 mL/min. The results in mean values were: partition coefficient 3.36, recovery 152%, purification factor 2.31, mass transfer coefficient 0.045, separation efficiency 43.7% and Hold up 0.33. The experimental data showed the potential application of aqueous two-phase systems PEG/citrate to purification ascorbate oxidase using perforated rotating disc contactor.