# Enhanced Anaerobic Digestion of Sewage Sludge Through the Integration of Thermal Hydrolysis and Bioelectrochemical Anaerobic Digestion

**Authors:** Chao-Wen Wang, Kai Ling Yu, Cheng-Tang Pan, Cheng-Yuan Hung, Liang-Shan Lee, Boris Tartakovsky

PMC · DOI: 10.3390/bioengineering13030311 · Bioengineering · 2026-03-08

## TL;DR

This study shows how combining thermal hydrolysis and bioelectrochemical digestion improves methane production from sewage sludge.

## Contribution

The study introduces a regime-based analysis to optimize pretreatment severity and loading for efficient methane production in BEAD reactors.

## Key findings

- At 120 °C THP, BEAD operated in a hydrolysis-limited regime with 0.8 L LR−1 methane production at sOLR of 4.5 g (LR d)−1.
- Increasing THP to 150 °C shifted the system to a kinetically enhanced regime, achieving 1.46 L LR−1 methane production at sOLR of 7.75 g (LR d)−1.
- The analysis provides quantitative guidance for optimizing pretreatment and loading strategies in BEAD reactors.

## Abstract

Thermal hydrolysis pretreatment (THP) increases the solubilization of sewage sludge, while bioelectrochemically assisted anaerobic digestion (BEAD) enhances the conversion of the solubilized organic matter into methane and improves reactor stability in the presence of inhibitory compounds. In this study, by mapping methane production in a BEAD reactor against the soluble organic loading rate (sOLR), determined from soluble chemical oxygen demand (sCOD) measurements, distinct operational regimes corresponding to different THP temperatures were identified. With the 120 °C pretreated feedstock, the BEAD reactor operated in a hydrolysis-limited regime, where increasing sOLR increased methane production but reduced conversion efficiency. Accordingly, at an sOLR of 4.5 g (LR d)−1, a volumetric methane production rate of 0.8 L LR−1 was achieved. Increasing THP severity to 150 °C improved solids solubilization and shifted the system into a kinetically enhanced regime, in which methane production was directly proportional to sOLR, indicating improved substrate accessibility and reaction kinetics. Consequently, at an sOLR of 7.75 g (LR d)−1, methane production reached 1.46 L LR−1. This regime-based analysis provides quantitative guidance for selecting pretreatment severity and loading strategies to maximize methane production, while maintaining stable BEAD reactor operation at high organic loads.

## Full-text entities

- **Chemicals:** oxygen (MESH:D010100), chemical (-), methane (MESH:D008697)

## Full text

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## Figures

6 figures with captions in the complete paper: https://tomesphere.com/paper/PMC13024326/full.md

## References

49 references — full list in the complete paper: https://tomesphere.com/paper/PMC13024326/full.md

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Source: https://tomesphere.com/paper/PMC13024326