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).