Insights into phosphate removal and recovery from wastewater using biosolids biochar: Pyrolysis optimisation, mechanistic and column studies

Biosolids, or sewage sludge (SS), is a byproduct from wastewater treatment plants (WWTPs) and drinking water production. SS can contain contaminants, which often generates secondary pollution post-disposal; therefore, pyrolysis is a promising approach for industrial-scale SS management (when compared to incineration, landfill, and direct agricultural use). Here, we determined optimal SS pyrolysis conditions using a Response Surface Methodology approach taking into consideration SS type, pyrolysis temperature and time. An optimised SS biochar (SSB-O) was then characterised using SEM-EDX, TGA/DSC, BET, FTIR, XRD and XPS. The biochar was then applied to phosphate adsorption from wastewater. Adsorption/desorption for phosphate (PO 4 3− -P) was evaluated through a series of batch and dynamic experiments using artificial and real WWTP effluent. Results showed that high PO 4 3− -P removal was achieved with a q max,exp of 12.7 mg/g in equilibrium studies, and the SSB-O was able to bring residual effluent PO 4 3− -P below 0.5 mg P total /L or 90 % of P total have been removed (new EU Urban Wastewater Treatment Directive 2024/3019). In column experiments, breakthrough time (for effluent P concentration < 0.1 mg/L) was 11,520 min (192 h) for an EBCT of 30 min, which corresponded to 668 Bed Volumes. Instrumental characterisation indicated that adsorption mechanisms were dominated by inner-sphere complexation onto metal ligands (mostly with aluminium). The work showed that SSB-O produced from a WWTP where an aluminium rich drinking water sludge was recirculated through the plant resulted in the best biochar, which could then serve as a water treatment material and as a medium to recover PO 4 3− -P from WWTP effluents. • Sewage sludge biochar was applied to phosphate recovery. • Pyrolysis conditions were optimised using a Central Composite Design. • Characterisation showed inner-sphere complexation as a governing mechanism for adsorption. • Modelling showed that adsorption was a complex process on a heterogeneous biochar surface. • Column studies demonstrated the biochar's applicability at larger scales.

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Publication Details

Journal
Journal of Water Process Engineering
Published
2025-05-19
DOI
https://doi.org/10.1016/j.jwpe.2025.107954
Citations
4
Primary Topic
Phosphorus and nutrient management
Type
article
Field-Weighted Citation Impact
3.99
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article

Insights into phosphate removal and recovery from wastewater using biosolids biochar: Pyrolysis optimisation, mechanistic and column studies

Christina Karmann, Thomas N. Thompson, Ruth McConnell, Tamsyn Kennedy et al.
4 citations
Journal of Water Process Engineering
Phosphorus and nutrient management
3.99
article

Insights into phosphate removal and recovery from wastewater using biosolids biochar: Pyrolysis optimisation, mechanistic and column studies

Christina Karmann, Thomas N. Thompson, Ruth McConnell, Tamsyn Kennedy, Mark A. Taggart, Sabolč Pap
article en
4 citations

Abstract

Biosolids, or sewage sludge (SS), is a byproduct from wastewater treatment plants (WWTPs) and drinking water production. SS can contain contaminants, which often generates secondary pollution post-disposal; therefore, pyrolysis is a promising approach for industrial-scale SS management (when compared to incineration, landfill, and direct agricultural use). Here, we determined optimal SS pyrolysis conditions using a Response Surface Methodology approach taking into consideration SS type, pyrolysis temperature and time. An optimised SS biochar (SSB-O) was then characterised using SEM-EDX, TGA/DSC, BET, FTIR, XRD and XPS. The biochar was then applied to phosphate adsorption from wastewater. Adsorption/desorption for phosphate (PO 4 3− -P) was evaluated through a series of batch and dynamic experiments using artificial and real WWTP effluent. Results showed that high PO 4 3− -P removal was achieved with a q max,exp of 12.7 mg/g in equilibrium studies, and the SSB-O was able to bring residual effluent PO 4 3− -P below 0.5 mg P total /L or 90 % of P total have been removed (new EU Urban Wastewater Treatment Directive 2024/3019). In column experiments, breakthrough time (for effluent P concentration < 0.1 mg/L) was 11,520 min (192 h) for an EBCT of 30 min, which corresponded to 668 Bed Volumes. Instrumental characterisation indicated that adsorption mechanisms were dominated by inner-sphere complexation onto metal ligands (mostly with aluminium). The work showed that SSB-O produced from a WWTP where an aluminium rich drinking water sludge was recirculated through the plant resulted in the best biochar, which could then serve as a water treatment material and as a medium to recover PO 4 3− -P from WWTP effluents. • Sewage sludge biochar was applied to phosphate recovery. • Pyrolysis conditions were optimised using a Central Composite Design. • Characterisation showed inner-sphere complexation as a governing mechanism for adsorption. • Modelling showed that adsorption was a complex process on a heterogeneous biochar surface. • Column studies demonstrated the biochar's applicability at larger scales.

Journal of Water Process EngineeringVol. 75
Scottish Water (United Kingdom) (GB), University of the Highlands and Islands (GB), University of Chemistry and Technology, Prague (CZ)
Clean water and sanitation
Openalex Percentile: Top 7%
Phosphorus and nutrient management
3.99
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