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Strategic biorefinery approach for closing the loop in the sugar industry: Valorisation of exhausted pulp into PHB via integrated bioconversion and kinetic modelling

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URI: http://hdl.handle.net/10498/39654

DOI: 10.1016/j.jece.2026.123260

ISSN: 2213-2929

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Author/s
Guzmán Gaona, Angela; Gómez Quiroga, XiomaraAuthority UCA; Romero Vargas, AgustínAuthority UCA; Álvarez Gallego, Carlos JoséAuthority UCA; Blandino Garrido, Ana MaríaAuthority UCA; Romero García, Luis IsidoroAuthority UCA
Date
2026-08
Department
Ingeniería Química y Tecnología de Alimentos
Source
Journal of Environmental Chemical Engineering, Volume 14, Issue 4, 2026, 123260,
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.
Subjects
Exhausted sugar beet pulp (ESBP); Dark fermentation (DF); Polyhydroxybutyrate (PHB); Cupriavidus necator; Kinetic modelling; C/N ratio; Volatile fatty acids (VFAs)
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Attribution-NonCommercial-NoDerivatives 4.0 Internacional
This work is under a Creative Commons License Attribution-NonCommercial-NoDerivatives 4.0 Internacional

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