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Waste Water Derived Electroactive Microbial Biofilms: Growth, Maintenance, and Basic Characterization
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Computational Fluid Dynamics Reveals Mass Transfer Limitations in a Pilot-Scale Microbial Electrolysis Cell.

Oscar Guerrero-Sodric1, Rholand Jordi Navarro-Quispe1, Martí Cortada-García1

  • 1GENOCOV, Department of Chemical, Biological and Environmental Engineering, School of Engineering, Universitat Autònoma de Barcelona, Bellaterra, Spain.

Water Environment Research : a Research Publication of the Water Environment Federation
|June 19, 2026
PubMed
Summary

Computational fluid dynamics modeling of large-scale microbial electrolysis cells (MECs) revealed hydrodynamic limitations hindering wastewater resource recovery. Recirculation strategies significantly improved acetate removal efficiency by overcoming mass transfer barriers.

Keywords:
ANSYS Fluentcomputational fluid dynamics (CFD)microbial electrolysis cell (MEC)pilot plantwastewater treatment

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Electrochemically and Bioelectrochemically Induced Ammonium Recovery
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Electrochemically and Bioelectrochemically Induced Ammonium Recovery

Published on: January 22, 2015

Area of Science:

  • Environmental Engineering
  • Bioelectrochemical Systems
  • Computational Fluid Dynamics

Background:

  • Microbial electrochemical technologies (METs), especially microbial electrolysis cells (MECs), face scalability challenges due to mass transfer limitations.
  • Efficient resource recovery from wastewater in MECs is often hindered by poor substrate transport to biofilms.

Purpose of the Study:

  • To develop and validate a comprehensive computational fluid dynamics (CFD) model for a pilot-scale MEC (1 m³).
  • To identify and quantify hydrodynamic and mass transfer limitations affecting substrate consumption and resource recovery in large-scale MECs.

Main Methods:

  • A pilot-scale MEC (1 m³) was modeled using CFD, integrating fluid dynamics with bioelectrochemical substrate consumption.
  • Simulations analyzed anolyte distribution, dead zones, and preferential flow paths under various operational conditions.
  • The impact of hydraulic retention time (HRT), reaction kinetics, and diffusivity on MEC performance was evaluated.

Main Results:

  • Laminar flow and poor flow distribution led to significant inefficiencies and low acetate removal.
  • External mass transfer, not intrinsic reaction kinetics, predominantly governed reactor performance.
  • Implementing a recirculation strategy enhanced acetate removal efficiency from 16% to 48%.

Conclusions:

  • CFD modeling is a valuable tool for diagnosing transport limitations in large-scale MECs.
  • Recirculation strategies can effectively mitigate mass transfer limitations without compromising volumetric capacity.
  • This framework provides practical insights for optimizing MEC design and operation for enhanced resource recovery.