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Erschienen in: Biomass Conversion and Biorefinery 2/2024

30.05.2022 | Original Article

Techno-economic feasibility of P(3-hydroxybutyrate) bioprocess with concentrated sugarcane vinasse as carbon and minerals source: an experimental and in silico approach

verfasst von: Manuella Souza Silverio, Rosane Aparecida Moniz Piccoli, João Lucas Maehara Said dos Reis, José Gregório Cabrera Gomez, Antonio Sampaio Baptista

Erschienen in: Biomass Conversion and Biorefinery | Ausgabe 2/2024

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Abstract

The Brazilian ethanol industry is very relevant in the global market; however, vinasse is generated in significant amounts and its management has become costly for distilleries. In this study, the aim was to evaluate vinasse as basal culture medium for P(3-hydroxybutyrate) (PHB) biosynthesis. Two bacterial strains were evaluated, a sucrose-consuming halophilic strain, Halomonas sp. HG03; and Ralstonia eutropha L359PCJ, which used glycerol from vinasse as carbon source. Firstly, shake flask bioprocesses analyzed cellular growth and PHB biosynthesis in vinasse-based media: in natura and concentrated vinasses were both evaluated in volumetric dilutions of 50% and 75% in mineral medium. Increasing vinasse concentration improved cellular growth rather than PHB accumulation for both bacteria. In vinasse-based treatments, Halomonas sp. HG03 had PHB content between 19.6 and 75.2% and R. eutropha L359PCJ, 48.4–68.5%. Further experiments in CSTR bioreactors used concentrated vinasse-based medium and R. eutropha L359PCJ had PHB content of 66.3%, concentration of residual cell dry weight (rCDW) = 9.4 g L−1, PHB = 18.6 g L−1, YX/S = 0.16 grCDW gGLYCEROL−1, YP/S = 0.32 gPHB gGLYCEROL−1, and 0.25 gPHB Lh−1. Halomonas sp. HG03 had PHB content of 42.2%, rCDW = 10.2 g L−1, PHB = 7.4 g L−1 and YX/S = 0.22 grCDW gSUCROSE−1, YP/S = 0.16 gPHB gSUCROSE−1 and 0.14 gPHB Lh−1. Finally, cost reductions by concentrated vinasse-based medium were evaluated. As glycerol source for PHB production by R. eutropha L359PCJ, vinasse reduced overall production costs by 22.2%. Unit production costs between US$ 2.8 and 5.4 kgPHB−1 were determined for scenarios that combined vinasse-based medium with high cell density culture and improvements of productivity. The investment payback times ranged from 1.6 to 4.5 years.

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Metadaten
Titel
Techno-economic feasibility of P(3-hydroxybutyrate) bioprocess with concentrated sugarcane vinasse as carbon and minerals source: an experimental and in silico approach
verfasst von
Manuella Souza Silverio
Rosane Aparecida Moniz Piccoli
João Lucas Maehara Said dos Reis
José Gregório Cabrera Gomez
Antonio Sampaio Baptista
Publikationsdatum
30.05.2022
Verlag
Springer Berlin Heidelberg
Erschienen in
Biomass Conversion and Biorefinery / Ausgabe 2/2024
Print ISSN: 2190-6815
Elektronische ISSN: 2190-6823
DOI
https://doi.org/10.1007/s13399-022-02710-y

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