Abstract Vinasse is the main liquid waste of the ethanol industry and its valorization by a bioprocess as a substrate for production of a value-added product contributes to the ethanol process. This work aimed to study the possibility to use vinasse for poly(3-hydroxybutyrate) (PHB) production by Cupriavidus necator. The growth of C. necator was evaluated using different vinasse concentrations and no inhibitory effect was observed. Cultivations in a bioreactor were carried out with pure vinasse, vinasse with nitrogen and vinasse with nitrogen and mineral salts. The best values of total biomass (5.1 g.L-1) and PHB (26% of total biomass) were obtained in the cultivation with nitrogen and salts added. The results indicated that vinasse could be used for PHB production. However, vinasse should be used in association with another substrate, aiming to improve the production. This is the first report on vinasse valorization for PHB production by C. necator.

Resumo A extração de poli(3-hidroxibutirato) (P(3HB)) com a utilização de solventes tóxicos e voláteis é contraditória à ideia do emprego destes biopolímeros para minimizar as agressões ambientais causadas pelos polímeros petroquímicos. O carbonato de propileno (CP) possui baixa toxicidade e alto ponto de ebulição, o que garante baixo risco de perdas por evaporação e alto rendimento de recuperação, podendo assim ser reutilizado. O objetivo deste trabalho foi verificar o efeito da reutilização do CP, recuperado do processo de extração de P(3HB) produzido por Cupriavidus necator, no rendimento e pureza do biopolímero e avaliar as perdas de solvente durante as etapas do processo de extração. Verificou-se a possibilidade de recuperar 80% do CP ao longo do processo. O solvente recuperado foi reutilizado onze vezes sem perder sua eficiência no rendimento e na pureza do produto. Desta forma, o presente estudo propõe a reutilização do CP, no processo de extração de P(3HB), contribuindo assim para a redução dos custos de produção deste biopolímero.

Abstract Poly(3-hydroxybutyrate) (P(3HB)) extraction using toxic volatile solvents is contradictory to the idea of using this biopolymer to minimize environmental aggressions caused by petrochemical polymers. Propylene carbonate (PC) has low toxicity and high boiling point, which ensure a low risk of losses due to evaporation and high recovery performance, allowing for reuse. The aim of this study was to investigate the effect of reusing PC recovered the process of extraction of P(3HB) produced by Cupriavidus necator on the performance and purity of the biopolymer and evaluate the amount of solvent loss during the stages of the extraction process. It was observed that 80% of PC could be recovered throughout the process. The recovered solvent was reused eleven times without losing its efficiency in terms of product performance and purity. Hence, the present study proposes to reuse PC in the process of P(3HB) extraction, thus contributing to reduce the costs for the production of this biopolymer.

Polyhydroxyalkanoates (PHAs) are biodegradable and biocompatible polyesters intracellularly accumulated by many bacteria as an energy reserve material and carbon source. These biopolymers may be extracted from cells after their production phase, and the extraction process involves various individual operations to ensure adequate removal of the biopolymer from the cells. During this process, the following aspects should be considered: reduction of product losses during different stages of the process to obtain a highly pure product, preservation of physical and thermal characteristics, and use of low toxicity chemicals to achieve sustainable production and avoid harming the environment. The impact of the costs of PHA extraction on the total cost of the production process may account for over 50% of the end-value of the product. Within this context, several methods of PHA extraction have been reported in the literature. These methods include the use of solvents, chemical digestion, enzymatic digestion, mechanical extraction with high-pressure homogenization and ultrasound, extraction using supercritical fluids, or a combination of these methods. The present review of the literature shows strategies for extraction processes of PHAs produced by bacteria involving cell destabilization and/or breakage, recovery, and purification of the biopolymer.

The environmental impact of plastic waste has attracted worldwide attention. Amid the current context of increasing concern for the environment, biodegradable plastics have been widely studied as a replacement for synthetic plastics. Poly(3-hydroxybutyrate) (P(3HB)) is a biopolymer stored as an intracellular energy and reserve source in many microorganisms. Because it is an intracellular product, P(3HB) must be extracted from the cells at the end of the culture. The purpose of this study was to investigate the effect of extraction time, heating temperature, first standing time (after filtration and extraction), second standing time (after P(3HB) precipitation) and solvent amount, during the process of extracting P(3HB) from Cupriavidus necator DSM 545, using propylene carbonate as solvent. The extraction kinetic of P(3HB) with propylene carbonate from thermally treated biomass was evaluated at different temperatures. The physical properties of the P(3HB) obtained were also evaluated. In this case, P(3HB) obtained at optimal conditions of recovery (98%) and purity (99%) was used. Results showed that temperature was the most important factor in these responses for the range of values studied (110-150 ºC).

A retamicina é um complexo antitumoral antraciclínico produzido por Streptomyces olindensis ICB20. Neste trabalho estudou-se a influência de diferentes concentrações de glicose no meio de alimentação sobre a produção de retamicina. Os resultados de cultivos contínuos mostraram que o uso de elevadas concentrações de glicose resultou em repressão catabólica da biossíntese do antitumoral. A maior velocidade específica de produção de retamicina, qRTM = 7,8 mg/g.h, foi obtida quando a concentração de glicose foi de 10 g/L. O menor valor de qRTM, 2,5 mg/g.h, foi observado quando a concentração de glicose foi de 20 e 25 g/L. A concentração de glicose residual aumentou de 0 a 13 g/L conforme a concentração de glicose na alimentação foi incrementada de 10 a 25 g/L.

Retamycin is an anthracyclinic antitumoral complex produced by Streptomyces olindensis ICB20. In this work the influence of different glucose concentrations in the feed medium on the production of retamycin was studied. Chemostat cultures employing glucose concentration varying between 10 g/L and 25 g/L showed that use of high glucose concentration resulted in catabolite repression of the biosynthesis of the antitumoral. The highest specific retamycin production rate, qRTM = 7.8 mg/g.h, was obtained when glucose concentration was 10 g/L. The lowest value of qRTM, 2.5 mg/g.h, was observed when glucose concentration was 20 and 25 g/L. The residual glucose concentration varied from 0 to 13 g/L, as the glucose concentration in the feed was increased from 10 to 25 g/L.