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Modelling anaerobic co-digestion in Benchmark Simulation Model No. 2: Parameter estimation, substrate
Magnus Arnell1, Sergi Astals2, Linda Åmand3
1Department of Biomedical Engineering (BME), Division of Industrial Electrical Engineering and Automation (IEA), Lund University, P.O. Box 118, SE-221 00, Lund, Sweden; SP Technical Research Institute of Sweden, Gjuterigatan 1D, SE-582 73, Linköping, Sweden.
Anaerobic co-digestion enhances wastewater treatment plant (WWTP) energy balance. Modeling shows protein and lipid fractions are key for methane production and digester stability, with careful protein loading crucial to avoid inhibition.
Area of Science:
- Environmental Engineering
- Biotechnology
- Wastewater Treatment
Background:
- Anaerobic co-digestion is gaining traction in wastewater treatment plants (WWTPs) to boost energy recovery and waste management.
- Plant-wide modeling is essential for evaluating co-substrate impacts on digester performance and overall WWTP operation.
Purpose of the Study:
- To develop and validate a modeling procedure for anaerobic co-digestion in WWTPs.
- To assess the influence of co-substrate composition (carbohydrates, proteins, lipids) on digester performance and stability.
- To investigate plant-wide effects of co-digestion, including methane production, operational costs, and nitrogen removal.
Main Methods:
- Developed a procedure to characterize and fractionate co-substrate Chemical Oxygen Demand (COD) for the Benchmark Simulation Model No. 2 (BSM2) and Anaerobic Digestion Model No. 1 (ADM1).
- Incorporated long-chain fatty acid inhibition into the ADM1 model for lipid-rich co-substrates.
- Conducted sensitivity analysis, principal component analysis (PCA), and validated the model with bio-methane potential (BMP) tests.
Main Results:
- Protein and lipid fractions significantly impact methane production and digester stability, with identified failure modes.
- The model demonstrated good predictive capability for carbohydrate-, protein-, and lipid-rich substrates.
- Plant-wide simulations confirmed increased methane production and reduced operational costs due to co-digestion.
- High protein loads can cause ammonia inhibition and overload nitrogen removal, while lipid-rich substrates are more tolerable.
Conclusions:
- The developed modeling approach effectively simulates anaerobic co-digestion in WWTPs.
- Optimizing co-substrate selection and dosage, particularly limiting protein content, is vital for efficient and stable anaerobic digestion.
- Co-digestion offers significant benefits for energy recovery and cost reduction in wastewater treatment.
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