Modelling the cathodic reduction of 2,4-dichlorophenol in a microbial fuel cell

• Published in: Bioprocess and biosystems engineering 2022-04, Vol.45 (4), p.771-782
• Main Authors: Leon-Fernandez, Luis Fernando, Fernandez-Morales, Francisco Jesús, Villaseñor Camacho, José
• Format: Article
• Language: English
• Subjects: 2,4-Dichlorophenol; Acetic acid; Anolytes; Biochemical fuel cells; Bioelectric Energy Sources; Biological models (mathematics); Biomass; Biotechnology; Carbon; Carbon sources; Cathodes; Chemical reduction; Chemistry; Chemistry and Materials Science; Chlorophenol; Chlorophenols; Dechlorination; Differential equations; Electrodes; Environmental Engineering/Biotechnology; Food Science; Fuel cells; Fuel technology; Industrial and Production Engineering; Industrial Chemistry/Chemical Engineering; Intermediates; Mathematical models; Microorganisms; Ortho-chlorophenol; Phenols; Protons; Research Paper; Sodium; Sodium acetate; Substrates
• ISSN: 1615-7591; 1615-7605
• DOI: 10.1007/s00449-022-02699-8

This work presents a simplified mathematical model able to predict the performance of a microbial fuel cell (MFC) for the cathodic dechlorination of 2,4-dichlorophenol (2,4-DCP) operating at different cathode pH values (7.0 and 5.0). Experimental data from previous work were utilized for the fitting of the model. The MFC modelled consisted of two chambers (bioanode and abiotic cathode), wherein the catholyte contained 300 mg L −1 of 2,4-DCP and the anolyte 1000 mg L −1 of sodium acetate. The model considered two mixed microbial populations in the anode compartment using sodium acetate as the carbon source for growth and maintenance: electrogenic and non-electrogenic biomass. 2,4-DCP, its intermediates of the reductive process (2-chlorophenol, 2-CP and 4-chlorophenol, 4-CP) and protons were considered in the model as electron acceptors in the electrogenic mechanism. The global process rate was assumed to be controlled by the biological mechanisms and modelled using multiplicative Monod-type equations. The formulation of a set of differential equations allowed to describe the simultaneous evolution of every component: concentration of sodium acetate in the anodic compartment; and concentration of 2,4-DCP, 2-CP, 4-CP, phenol and chloride in the cathode chamber. Current production and coulombic efficiencies were also estimated from the fitting. It was observed that most of the organic substrate was used by non-electrogenic mechanism. The influence of the Monod parameters was more important than the influence of the biomass yield coefficients. Finally, the model was employed to simulate different scenarios under distinct experimental conditions.