Volatile fatty acid platform - a cornerstone for the circular bioeconomy.

Annually, the EU produces more than 100 million tonnes of urban biowaste, which is largely under-valorized and in some cases even still landfilled without any energy or material recovery. If Europe wants to be ready for the future, it will need to make better use of this large biomass potential within a circular economy approach. The research project funded by the European Commission under the Horizon 2020 programme entitled 'VOLATILE-Biowaste derived volatile fatty acid platform for biopolymers, bioactive compounds and chemical building blocks' aimed to produce volatile fatty acids (VFAs) from biowaste for reprocessing into products, materials or substances to close the material loop. During the project, the partners were able to obtain average volatile fatty acid yields of 627 g COD/kg organic matter (OM) for food waste, 448 g COD/kg OM for separately collected vegetable, garden and fruit waste (VGF) and 384 g COD/kg OM for the organic fraction of municipal solid waste (OF-MSW) at concentrations ranging from 12 to 48 g/L, 6 to 40 g/L and 13 to 26 g/L, respectively. A membrane filtration cascade consisting of micro-, ultra- and nano-filtration followed by reverse osmosis was identified as a feasible way to purify and concentrate the VFA effluent, making them a suitable carbon source for further fermentation processes. Besides technical optimization, socio-economic and legal aspects associated with this platform technology were also studied and show that although this technology is still in development, it is providing an answer to changing societal and market expectations both regarding organic waste treatment and bio-based production strategies. Based on the current technological, economic and market evolutions, it is expected that the VFAP will play an important role in organic waste treatment in the coming years.

Cleavage of poly(cis-1,4-isoprene) rubber as solid substrate by cultures of Gordonia polyisoprenivorans.

Potential biotechnological recycling processes for rubber products include the bacterial degradation of poly(cis-1,4-isoprene) (IR) in order to achieve its total biodegradation or its biotransformation into useful products. The actinomycete Gordonia polyisoprenivorans strain VH2 catalyzes the degradation of IR and enables its use as a sole carbon source via ß-oxidation. The initial cleavage reaction is catalyzed by the extracellular latex clearing protein (Lcp). This dioxygenase is the key enzyme for the formation of oligo(cis-1,4-isoprene) molecules with different lengths, i.e., numbers of isoprene units. For the first time, IR was used as a solid substrate in 2-l fermenters. Two different particle size fractions (63-500 and 500-1000 µm) and three stirring rates (300, 400 and 500 rpm) were evaluated in the process. An increase of the cell concentration was achieved by using smaller particles and by using lower stirring rates, reaching a final biomass concentration of 0.52 g l-1 at 300 rpm after 12 days of cultivation. In order to enhance the formation of oligo(cis-1,4-isoprene) molecules, a transposon insertion mutant (TH5) of G. polyisoprenivorans strain VH2 that has lost the ability to transport the partial degradation products into the cells was used, thereby allowing the accumulation of the degradation products in the culture supernatants. Propionate, glucose and glycerol were evaluated as additional carbon sources besides IR, and the highest yields were observed on propionate. In 2-l bioreactors with pH control, different feeding regimes were performed during cultivation by the addition of propionate every 24 or 48 h for 16 days. After liquid-liquid extraction and a derivatization with Girard's T reagent, the oligo(cis-1,4-isoprene) molecules were detected by ESI-MS. The mass distribution of the degradation products was affected by the selection of the extraction solvent, but no influence of longer cultivation periods was detected.