Abstract L-Asparaginase (L-ASNase) is a biopharmaceutical used for acute lymphoblastic leukaemia (ALL) treatment, dramatically increasing the patients’ chance of cure. However, its production and distribution in developing countries were disrupted because of its low profitability, which caused great concern among patients. This study evaluates the feasibility of combining fractional precipitation and aqueous two-phase systems (ATPS) to purify L-ASNase from a low-grade product, commercially known as Acrylaway® L. The ATPS purification results were not particularly expressive compared to the two-step purification process composed of ethanol precipitation and gel filtration, which was able to recover the target molecule with a purification factor over 5 fold. Thus, we studied a purification process capable of manufacturing pharmaceutical grade L-ASNase from a commercially available low-grade raw material; however, improvements regarding its throughput must be achieved, and high purity is the first step to apply it as a new biopharmaceutical product. The proposed process could pose as a short-time solution to mitigate its shortage while a cost-effective production plant is being developed.

RESUMO Fibroína (FB) e nanocelulose bacteriana (BC) são produtos naturais que podem ser usados na biomedicina, nas indústrias eletrônicas e de alimentos e outras áreas. Todos eles apresentam biocompatibilidade, podendo ser utilizados para diversos fins. A mistura de fibroína e nanocelulose bacteriana foi projetada para produzir um material biocompatível para ser aplicado com um dispositivo médico. Por esse motivo, o objetivo deste trabalho foi avaliar as propriedades estruturais da mistura de BC e FB. Assim, FB foi extraída do Bombyx mori e a BC foi produzida por processo de fermentação utilizando Gluconacetobacter xylinus. As membranas compostas de BC-FB foram produzidas por contato de imersão por 24 horas, a 25 °C, em 100 rpm, sem agente reticulante. Após a produção, as amostras de membrana foram secas e caracterizadas por espectroscopia de Infravermelho com Transformada de Fourier (espectroscopia FTIR), propriedades mecânicas, eficiência de intumescimento, microscopia eletrônica de varredura (MEV) e microtomografia computadorizada (µCt). Os resultados indicam que as membranas porosas com ligações de hidrogênio obtidas apresentaram morfologia porosa anisiotrópica, fechada e interconectada. As características morfométricas, que se assemelham a um favo de mel e consistem em uma estrutura longa com alta conectividade e alta porosidade total, amplificam as áreas de aplicações da mistura BC-FB, com potencial utilização com dispositivos optoeletrônicos, em áreas que variam desde ambiental à engenharia tecidual. Além disso, a produção por contato de imersão permitirá o processo de alta qualidade e o desenvolvimento de material de rótulo verde.

ABSTRACT Fibroin (FB) and bacterial nanocellulose (BC) are natural products, being used in biomedicine, electronics, food industries and other areas. Both show biocompatibility, able to be used for many different purposes. The blending of fibroin and bacterial nanocellulose was design to produce a biocompatible material to be applied with a medical device. For this reason, the objective of this work was to evaluate the structure properties of the blending of BC and FB. Thus, FB was extracted from Bombyx mori and BC was produced by fermentation process utilizing Gluconacetobacter xylinus. The membranes composed of BC-FB were produced by immersion contact for 24 hours, at 25°C, in 100rpm; without crosslinking agent. After the production the membrane samples were dried and characterized by Fourier transform infrared spectroscopy (FTIR spectroscopy), mechanical proprieties, swelling efficiency, scanning electron microscopy (SEM) and computerized microtomography (µCt). Results indicate that the hydrogen-bonded porous membranes obtained displayed anisiotropic, closed and interconnected porous morphology. The morphometric characteristics, which resemble a honeycomb and consist of a long structure with high connectivity and high total porosity, amplify the areas of BC-FB blend applications, with potential utilization with optoelectronic devices, in areas ranging from environmental to tissue engineering. Furthermore, the production by immersion contact will allow the upscale process and the development of green label material.

Abstract Microalgae are aquatic unicellular microorganisms that can be found both in freshwater and marine systems; are capable of photosynthesis; and can grow as individual cells or associated in chains or small colonies. Microalgae cultivation has gained large momentum among researchers in the past decades due to their ability to produce value metabolites, remarkable photosynthetic efficiency, and versatile nature. The wide technological potential, and thus increasing amount of scattered knowledge, may become the very first barrier that a post graduating student, or any non-specialist reader, will face when introduced to the subject. In this review paper, we access the core aspects of microalgae technology, covering their main characteristics, and comprehensively presenting the main features of their various cultivation modes and biological activity from metabolites.

The aim of this work was to isolate and purify bromelain extracted from the pineapple peel by ammonium sulfate precipitation (40-80%), followed by desalting and freeze-drying with a 75% activity recovery and 2.2 fold increased specific activity. Ion exchange chromatography on DEAE-Sepharose was able to separate the polysaccharides from the enzyme, which was recovered in the elution step, maintaining its enzymatic activity. The batch adsorption of bromelain was evaluated in terms of total protein and enzymatic activity using Langmuir and Langmuir-Freundlich models. Results showed that the process could be suitable for the recovery and purification of the enzyme, maintaining its specific activity.

This study aimed to obtain the condition of maximum bromalein activity in different parts of pineapple plants produced in vitro, by micropropagation. The sStems and leaves of Pérola and Imperial cultivar plants were evaluated after three and eight months of in vitro cultivation in Murashige and Skoog medium without growth phytoregulator, macerated in potassium phosphate buffer at different pH values (5.7, 6.7 and 7.7). Total protein and proteolytic activity were determined in the samples after three- and eight-month cultivation periods. For both the cultivars, the best results were obtained at pH 5.7 in extraction media. Pérola cultivar, showed higher bromelain activity in the leaves cultivated in vitro for three months (0.0194U/mL) while in the Imperial cultivar, it was higher in the stem after eight months (0.0179 U/mL). Imperial cultivar showed higher bromelain activity than the Pérola's.

The aim of this work was to study the production of e bromelain from the Ananas comosus L. Merril, by determining the process conditions using flat membranes. The production system modeling generated a hyperbolical curve and the optimization by response surfaces showed an influence of the transmembrane pressure higher than the pH influence. The cost of the production of bromelain from A. comosus was estimated 9 to 13 times lower than Sigma's retail sales price and 6.5 to 8.5 times lower than when this enzyme was obtained through a liquid-liquid extraction, which showed the economical feasibility of the process.

This work aimed to study the partitioning of a lipase produced by Burkholderia cepacia in PEG/Phosphate aqueous two phase system (ATPS) and its characterization. Lipase was produced by B. cepacia strains in a fermenter. Enzyme partitioning occurred at pH 6.0 and 8.0, using PEG 1500 and 6000 on two tie lines. Metal ions, pH and temperature effects on enzyme activity were evaluated. Five milliliter of 7.5% olive oil emulsion with 2.5% gumarabic in 0.1M sodium phosphate buffer at pH 8.0 and 37ºC were used for the activity determinations. Results showed that crude stratum from B. cepacia was partitioned by PEG1500/phosphate ATPS at pH 6.0 or 8.0 for, which the partitioning coefficients were 108-and 209-folds. Lipase presented optimal activity conditions at 37ºC and pH 8.0; it showed pH-stability for 4 h of incubation at different pH values at 37ºC. Metal ions such as Mn2+ , Co2+, I-and Ca2+ sustained enzymatic activities; however, it was inhibited by the presence of Fe2+, Hg2+ and Al3+ . Km and Vmax values were 0.258 U/mg and 43.90 g/L, respectively. A molecular weight of 33 kDa and an isoelectric point at pH 5.0 were determined by SDS-PAGE and IFS electrophoresis, respectively.

O presente trabalho teve como objetivo a produção de lipase a partir de Pseudomona cepacia por fermentação líquida em biorreator do tipo Bioflo III. As fermentações foram conduzidas a 150 rpm durante 96 horas a 30 °C. Analisou-se a atividade enzimática em diferentes condições de temperatura (20 a 50 °C) e pH (3,0 a 11,0), e obtiveram-se 37 °C e 8,0, as condições ótimas, respectivamente. Para avaliar a estabilidade térmica, a enzima foi incubada em temperaturas de 40, 50 e 60 °C durante 120 minutos. Em uma segunda etapa, foram realizados experimentos preliminares para verificar as condições adequadas de partição da enzima, bem como sua estabilidade e condições ótimas de hidrólise frente às modificações de temperatura e pH. Foram preparadas soluções de PEG 1500, 4000 e 6000 a 50% p/p e soluções tampão fosfato de pHs 6, 7 e 8. Foi feita a caracterização de um sistema bifásico aquoso (SBA) a partir da preparação de soluções estoques de PEG com massas molares de 1500, 4000 e 6000 (50% w/w) e tampão fosfato pH 6,7 e 8,0 (20% w/w de KH2PO4/K2HPO4). Esta caracterização do SBA posteriormente poderá ser utilizada para partição de lipases, bem como de biomoléculas que estejam dentro dessa faixa de pH.

In this work, Pseudomonas cepacia was used for fermentation in bioreactor Bioflo III at 150 rpm, at 30 °C to 96 hours. Fermentation was conducted at 150 rpm for 96 hours in 30 °C. We analyzed the enzyme activity under different conditions of temperature (20 to 50 °C) and pH (3.0 to 11.0). The optimum activity values obtained were 37 °C and 8.0, respectively. To evaluate thermal stability, the enzyme was incubated in temperatures of 40, 50 and 60 °C for 120 minutes. Preliminary experiments were carried out to verify the appropriate conditions that should be used after the enzyme partition. Some tests were performed to determine some optimal conditions of lipase, including temperature and pH and tests of thermal stability using temperatures of 40, 50, and 60 °C. Next, the characterization of aqueous two-phase systems (ATPS) with PEG molar weight of 1500, 4000, and 6000 and phosphate varying pH 6 to 8 was made. Stock solutions of PEG 1500, 4000 and 6000 (50% w/w) and phosphate (20% w/w KH2PO4/K2HPO4) were prepared at the appropriate pH. This study on the characterization of the ATPS can be used for posterior partition of lipase, as well as of biological products within this pH range.

In this work, the thermodynamic equilibrium and applying of PEG4000/Phosphate ATPS on the purification of bromelain extracted from pineapple was studied. A rigorous study of the equilibrium curves and tie-line length from PEG4000/phosphate ATPS were done for the pH 6-11 at 25ºC. Results showed that there was augment in the PEG and salt contents with the high pH value from PEG4000/Phosphate ATPS and two-phase formation needed only increasing the PEG content. Two tie-line length at pH 11 from PEG4000/Phosphate ATPS were optimal condition for bromelain purification, one on composition of 14% PEG and 13% salt and other at 12.6% PEG and 12.2% salt, while a 25-62 folds of enzyme was found. SDS-PAGE electrophoreses had one band only, which showed that bromelain was purified. Optimum conditions of bromelain use were found at pH 7 and between 30-40ºC.

Este trabalho objetivou otimizar o processo de hidrólise do amido de mandioca com α-amilase de A. niger e obter o álcool deste xarope. Os ensaios foram realizados a pH 4,8; em que variaram-se a concentração do amido (entre 7-22 g.L-1) e a temperatura (entre 30-59,1 ºC). Durante a fermentação, usaram-se nos mostos 2,2 e 5% de amido de mandioca. Os resultados da hidrólise mostraram que o tempo ficou entre 20-200 minutos; a análise RSM mostrou que o rendimento diminuiu nas concentrações médias; e as condições ótimas foram encontradas entre 55-59,1 ºC e com a concentração entre 7,9-10 ou 20-22 g.L-1, em que se hidrolisou 80% do amido. A melhor condição de fermentação foi obtida para o mosto contendo 5% de amido. Sua composição final foi de 0,668 g.L-1 de ART, 0,572 g.L-1 e de AR, 3,71 ºGL. O rendimento alcoólico foi de 45%, demonstrando que este processo é uma alternativa eficiente à indústria sucroalcooleira.

The objective of this study was the optimization of the manioc root starch hydrolysis by α-amylase from A. niger and alcohol production from this starch syrup. Hydrolysis assays were performed at pH 4.8, the starch concentration and the temperature varied from 7 to 22 g.L-1, and 30 to 59.1 ºC, respectively. The starch contents during the syrup fermentation were 2.2 and 5%. The results of the starch hydrolysis showed that the hydrolysis time was between 20-200 minutes, the RSM analysis showed a decrease in the starch yield at the average concentration and above of 70% at high temperatures, and the optimal conditions were found at temperature between 55-59.1 ºC and concentration between 7.9-10 or 20-22 g.L-1; conditions at which 80% of the starch was hydrolyzed. The best fermentation condition was obtained for the must containing 5% of starch. The final fermentation composition obtained was of 0.68 g.L-1 ART and 0.572 g.L-1 AR. After the fermentation process, an alcohol yield of 45% was obtained showing that this process is a very good alternative for sugar-alcohol industries.

Uma micro-coluna com campânulas pulsantes foi utilizada para a extração de bromelina a partir de suco de abacaxi, usando micelas reversas. A solução catiônica micelar foi composta do surfactante BDBAC, do solvente iso-octano e do co-solvente hexanol. Seguindo um planejamento experimental, perturbações foram impostas à coluna de extração com o objetivo de capturar seu comportamento dinâmico e suas não-linearidades, usando a razão entre a vazão da fase leve e vazão total, e o intervalo de tempo entre os pulsos. Os efeitos das variáveis independentes sobre o fator de purificação e sobre o rendimento em proteínas totais foram modelados via redes neurais artificiais. A melhor topologia de rede obtida foi definida como 16-9-2, usando um esquema de janela móvel no tempo das variáveis independentes. O modelo neural obtido do histórico do processo se mostrou adequado para predizer simultaneamente o fator de purificação e o rendimento do processo em proteínas totais. No ponto ótimo de operação, foi encontrado um fator de purificação de 4.96, com produtividade de 1.29 mL/min.

A pulsed-cap microcolumn was used for bromelain extraction from pineapple juice by reversed micelles. The cationic micellar solution used BDBAC as the surfactant, isooctane as the solvent and hexanol as the co-solvent. In order to capture the dynamic behavior and the nonlinearities of the column, the operating conditions were modified in accordance with the central composite design for the experiment, using the ratio between the light phase flow rate and the total flow rate, and the time interval between pulses. The effects on the purification factor and on total protein yield were modeled via neural networks. The best topology was defined as 16-9-2, and the input layer was a moving window of the independent variables. The neural model successfully predicted both the purification factor and the total protein yield from historical data. At the optimal operating point, a purification factor of 4.96 and a productivity of 1.29 mL/min were obtained.

Neste trabalho realizou-se a purificação das enzimas α e β-amilases de malte de milho combinando os processos de adsorção em leito expandido com o fracionamento por etanol. Alimentaram-se 5 mL de uma solução a 2% de malte de milho em tampão fosfato 0,05 M a pH 5 em uma coluna contendo as resinas de troca iônica Amberlite IRA 410, em leito fixo de 4 cm fluidizado para 8 cm. A eluição foi promovida com NaCl 0,25M com 14 mL/minuto de vazão descendente e o material eluído foi fracionado com álcool etílico nas concentrações de 40-70%, 50-80% e 60-90% (v/v) a 20 e 30 ºC. A recuperação da atividade e o fator de purificação foram de 95% e 23 vezes, respectivamente, na primeira etapa. A melhor condição de fracionamento das enzimas foi apresentada a 50-80% de álcool e 20 ºC, e o fator de purificação ficou acima de 100 vezes.

In the present work the purification of α and β-amylase enzymes of maize malt was carried out by expanded bed adsorption and ethanol fractionation downstream processes. 5 mL of 2% maize malt solution in 0.05 M phosphate buffer at pH was injected into a chromatographic column containing Amberlite 410 ion-exchange resin, on a 4 cm fixed bed fluidized to 8 cm. 0.25 M NaCl solution at 14 mL/ minuto of descending flux was used for promotion of the elution, the eluted matter was fractioned by 40-70, 50-80 and 60-90% ethyl alcohol concentration at 20 and 30 ºC. Activity recovery and purification factor were of 95% and 23 times, respectively, in the first step. 50-80% alcohol concentration at 20ºC was the best condition, in which a purification factor of more than 100 times was achieved.

Este trabalho teve como objetivo principal otimizar as condições para extração da bromelina do suco do abacaxi (Ananas comosus) por micelas reversas. A purificação foi feita usando o processo de extração em batelada e contínuo, este último em uma micro-coluna de campânulas pulsantes. A solução micelar catiônica foi preparada com o surfactante BDBAC, i-octano como solvente e hexanol como co-solvente. Na extração em batelada encontrou-se um fator de purificação de 3 vezes, e seus melhores valores de concentração do agente surfactante, co-solvente e sal, de pH da re-extração e extração, foram respectivamente iguais a: 100 mM, 10% v/v, 1 M, 3,5 e 8. Para a operação contínua, as variáveis independentes ótimas foram: 0,67 para a razão entre as taxas de fluxos da fase leve e a total e 1 s para o intervalo de tempo entre pulsos das campânulas. Este ponto ótimo leva a uma produtividade de 1,29 mL/min e a um fator de purificação igual a 4,96.

The main aim of this study was to optimize the conditions for bromelain extraction by reversed micelles from pineapple juice (Ananas comosus). The purification was carried out in batch extraction and a micro-column with pulsed caps for continuous extraction. The cationic micellar solution was made of BDBAC as a surfactant, isooctane as a solvent and hexanol as a co-solvent. For the batch process, a purification factor of 3 times at the best values of surfactant agent, co-solvent and salt concentrations, pH of the back and forward extractions were, 100 mM, 10% v/v, 1 M, 3.5 and 8, respectively. For the continuous operation, independent variables optimal point was determined: ratio between light phase flow rate and total flow rate equal to 0.67 and 1 second for the time interval between the pulses. This optimal point led to a productivity of 1.29 mL/min and a purification factor of 4.96.

Neste trabalho as enzimas α e β-amilases foram obtidas de malte de milho e depois foram caracterizadas bioquimicamente. Um estudo da germinação foi feito para obtenção do malte com boa atividade amilásica. A germinação ocorreu em escala laboratorial e a atividade enzimática foi medida diariamente. Um modelo exponencial do tipo A=A0eµt foi ajustado a dependência do tempo de germinação com a atividade, mostrando que o comportamento da atividade enzimática no processo de germinação é semelhante ao crescimento de microorganismos. Este modelo pode ser aplicado para descrever o mecanismo de produção da α-amilase para cada variedade de milho e de outros cereais. A caracterização do malte de milho mostrou que as α e β-amilase têm pH ótimo entre 4,0-6,5, temperatura ótima de 50 e 90ºC, e massa molar de 67,4 e 47,5 kDa, respectivamente. Este trabalho contribuiu com os avanços da biotecnologia gerando condições de emprego de uma nova e barata fonte de amilases.

In this work the α and β-amylase enzymes were obtained from maize (Zea mays) malt and were biochemistry characterized. A germination study to obtain the maize malt with good amylase activity was made. The maize seeds were germinated in laboratory and the enzymatic activity was measured daily. Activity dependence to germination time were fitted to an exponential model (A=A0eµt), which showed that the behaviour of enzymatic activity in the germination process was similar to the growth of the microorganism. Its model could be applied to describe the mechanism of α-amylase production for each maize varieties and others cereals. Maize malt characterization showed that α and β-amylase had optimal pH between 4-6.5, optimal temperature 50 and 90ºC, and molecular weight of 67.4 and 47.5kDa, respectively. This work contributed with the advances in biotechnology generating of conditions for application of a new and of low price amylases source.

A concentração do suco de abacaxi é necessária para manter a atividade da bromelina e padronizar a composição e atividade proteolítica. Assim, este trabalho objetivou a obter um extrato de bromelina pura do suco do Ananas comosus L. Merril por processos de separação por membranas. Um planejamento experimental do tipo 2² foi feito para estudar a influência do pH a da pressão transmembranar sobre a recuperação da atividade por micro-filtração usando uma membrana plana. Em uma segunda etapa, purificou-se a enzima alvo por ultra-filtração usando um "kit millipore" de 10 kDa. A melhor condição para a concentração da bromelina foi a pH 7,5 e pressão transmembranar de 0,05 bar, onde 85% da atividade da bromelina foi recuperado. A ultra-filtração manteve 100% da atividade proteolítica e concentrou em 10 vezes o extrato de bromelina. A eletroforese via SDS-PAGE mostrou que o ultra-filtrado teve alta pureza e a bromelina da polpa do Ananas comosus tem um peso molecular de 24.5 kDa.

The concentration of pineapple juice is needed to retain the bromelain activity and to standardize the composition and proteolytic activity. Thus, this work aimed to obtain a pure bromelain extract from the Ananas comosus L. Merril juice by membrane separation process. A 2² experimental planning was used to study the influence of pH and transmembrane pressure on the activity recovery by micro-filtration using a plain membrane. In second step, this enzyme was purified by the ultra-filtration using a 10 kDa millipore kit. The best operation condition to bromelain concentration using the plain membrane was at pH 7.5 and transmembrane pressure of 0.05 bar, while 85% of bromelain activity was recovered. Ultra-filtration retained 100% of proteolytic activity and concentrated in 10 fold the bromelain extract. SDS-PAGE electrophoresis showed that the ultra-filtrated had high purity and the bromelain from A. comosus pulp had a molecular weight of 24.5 kDa.