| dc.contributor.author | Guzmán Gaona, Angela | |
| dc.contributor.author | Gómez Quiroga, Xiomara | |
| dc.contributor.author | Romero Vargas, Agustín | |
| dc.contributor.author | Álvarez Gallego, Carlos José | |
| dc.contributor.author | Blandino Garrido, Ana María | |
| dc.contributor.author | Romero García, Luis Isidoro | |
| dc.contributor.other | Ingeniería Química y Tecnología de Alimentos | es_ES |
| dc.date.accessioned | 2026-05-25T11:49:35Z | |
| dc.date.available | 2026-05-25T11:49:35Z | |
| dc.date.issued | 2026-08 | |
| dc.identifier.issn | 2213-2929 | |
| dc.identifier.uri | http://hdl.handle.net/10498/39654 | |
| dc.description.abstract | The transition towards a circular bioeconomy requires the conversion of agro-industrial residues into valuable bioproducts. This study investigates an integrated approach to producing polyhydroxybutyrate (PHB) using exhausted sugar beet pulp (ESBP) as a sustainable source of material. Initially, the ESBP was processed via thermophilic dark fermentation to yield a volatile fatty acid (VFA) rich effluent (15.1 g/L) dominated by acetic and butyric acids. Subsequently, the effect of the C/N ratio (44, 35 and 20) on PHB synthesis by Cupriavidus necator was evaluated. The experimental results showed that the raw effluent (C/N 44) triggered the highest specific polymer accumulation (77.5% of cell dry weight). To gain insight into the bioconversion dynamics, an unlumped kinetic model was developed and validated (R² > 0.95), effectively decoupling residual biomass growth from PHB accumulation. The model successfully identified a critical harvest time by incorporating an intracellular degradation term, thereby preventing product loss under substrate-limiting conditions. For the C/N ratios of 44 and 35, the maximum volumetric productivity was in the range of 0.063–0.066 g·L⁻¹ ·h⁻¹ and the optimum harvesting time was in the range of 48.2–49.1 h, during which the PHB accumulation would be 65.3–65.5%. These findings suggest that non-supplemented fermentation of sugar beet pulp could be a cost-effective and efficient process for producing sustainable bioplastics. | es_ES |
| dc.description.sponsorship | Grant PID2023-146737OB-I00 funded by MICIU/AEI/ 10.13039/501100011033 and by “ERDF/EU” and by the BEET2BIO project (FEDER-UCA-2024-A2–07), funded by the Andalusia ERDF Operational Program 2021–2027. | es_ES |
| dc.format | application/pdf | es_ES |
| dc.language.iso | eng | es_ES |
| dc.rights | Attribution-NonCommercial-NoDerivatives 4.0 Internacional | * |
| dc.rights.uri | http://creativecommons.org/licenses/by-nc-nd/4.0/ | * |
| dc.source | Journal of Environmental Chemical Engineering, Volume 14, Issue 4, 2026, 123260, | es_ES |
| dc.subject | Exhausted sugar beet pulp (ESBP) | es_ES |
| dc.subject | Dark fermentation (DF) | es_ES |
| dc.subject | Polyhydroxybutyrate (PHB) | es_ES |
| dc.subject | Cupriavidus necator | es_ES |
| dc.subject | Kinetic modelling | es_ES |
| dc.subject | C/N ratio | es_ES |
| dc.subject | Volatile fatty acids (VFAs) | es_ES |
| dc.title | Strategic biorefinery approach for closing the loop in the sugar industry: Valorisation of exhausted pulp into PHB via integrated bioconversion and kinetic modelling | es_ES |
| dc.type | journal article | es_ES |
| dc.rights.accessRights | open access | es_ES |
| dc.identifier.doi | 10.1016/j.jece.2026.123260 | |
| dc.relation.projectID | info:eu-repo/grantAgreement/MICIU/AEI/10.13039/501100011033/PID2023-146737OB-I00 | es_ES |
| dc.relation.projectID | info:eu-repo/grantAgreement/FEDER-UCA/Andalusia ERDF Operational Program 2021–2027/2024-A2–07 | es_ES |
| dc.type.hasVersion | VoR | es_ES |