Long‐term VOC and siloxane removal in an anoxic biotrickling filter inoculated with Methylibium sp.

Abstract Background Volatile methyl siloxanes in biogas hinder energy recovery due to abrasive silica deposits formed during combustion. Biological removal in biotrickling filters (BTFs) is constrained by low gas–liquid mass transfer, yet few studies separate transport from biological limitations in anoxic conditions. This study evaluates the long‐term performance of a BTF inoculated with Methylibium sp. for the removal of D4, D5, hexane, toluene and limonene under anoxic and microaerobic conditions over 265 days. Results Batch assays showed that co‐substrate availability was the primary factor enhancing Methylibium growth ( P = 0.002), strongest under microaerobic conditions (interaction P = 0.005), while nitrate had no effect ( P ≥ 0.75). In the BTF, toluene (RE > 97%) and limonene (RE 86%–98%) were consistently removed throughout operation. Hexane removal responded strongly to electron acceptor supply (RE 17–100%). In contrast, D4 and D5 RE were largely invariable (13.1 ± 0.7% and 27.6 ± 1.1%; ranges 8.8%–17.9% and 18.9%–30.3%) regardless of EBRT (4.4–15.5 min) or electron acceptor regime, with elimination capacities increasing proportionally with loading, a behavior characteristic of gas–liquid mass transfer limitation. The higher RE of D5 than D4, opposite to the ranking predicted from air–water partitioning, indicates that other factors also contribute. Conclusion The BTF achieved near‐complete VOC removal and partial siloxane abatement under biogas‐compatible conditions. Siloxane removal, relatively stable and largely independent of EBRT and electron acceptor, is constrained primarily by mass transfer rather than by biological capacity. These results support using the BTF as a first purification stage coupled with a downstream adsorption polishing step. © 2026 Society of Chemical Industry (SCI).

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Publication Details

Journal
Journal of Chemical Technology & Biotechnology
Published
2026-11-09
DOI
https://doi.org/10.1002/jctb.70301
Primary Topic
Odor and Emission Control Technologies
Type
article
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article

Long‐term VOC and siloxane removal in an anoxic biotrickling filter inoculated with Methylibium sp.

Alba Cabrera‐Codony, Hèctor Monclús, Eric Santos-Clotas, Frederic B. Gich et al.
Journal of Chemical Technology & Biotechnology
Odor and Emission Control Technologies
article

Long‐term VOC and siloxane removal in an anoxic biotrickling filter inoculated with Methylibium sp.

Alba Cabrera‐Codony, Hèctor Monclús, Eric Santos-Clotas, Frederic B. Gich, Lluı́s Bañeras, Maria José Martin, Ellana Boada
article en

Abstract

Abstract Background Volatile methyl siloxanes in biogas hinder energy recovery due to abrasive silica deposits formed during combustion. Biological removal in biotrickling filters (BTFs) is constrained by low gas–liquid mass transfer, yet few studies separate transport from biological limitations in anoxic conditions. This study evaluates the long‐term performance of a BTF inoculated with Methylibium sp. for the removal of D4, D5, hexane, toluene and limonene under anoxic and microaerobic conditions over 265 days. Results Batch assays showed that co‐substrate availability was the primary factor enhancing Methylibium growth ( P = 0.002), strongest under microaerobic conditions (interaction P = 0.005), while nitrate had no effect ( P ≥ 0.75). In the BTF, toluene (RE > 97%) and limonene (RE 86%–98%) were consistently removed throughout operation. Hexane removal responded strongly to electron acceptor supply (RE 17–100%). In contrast, D4 and D5 RE were largely invariable (13.1 ± 0.7% and 27.6 ± 1.1%; ranges 8.8%–17.9% and 18.9%–30.3%) regardless of EBRT (4.4–15.5 min) or electron acceptor regime, with elimination capacities increasing proportionally with loading, a behavior characteristic of gas–liquid mass transfer limitation. The higher RE of D5 than D4, opposite to the ranking predicted from air–water partitioning, indicates that other factors also contribute. Conclusion The BTF achieved near‐complete VOC removal and partial siloxane abatement under biogas‐compatible conditions. Siloxane removal, relatively stable and largely independent of EBRT and electron acceptor, is constrained primarily by mass transfer rather than by biological capacity. These results support using the BTF as a first purification stage coupled with a downstream adsorption polishing step. © 2026 Society of Chemical Industry (SCI).

Journal of Chemical Technology & Biotechnology
Universitat de Girona (ES), Universidad Yachay Tech (EC), Centro Tecnológico del Agua (ES)
Odor and Emission Control Technologies
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