Hybrid section-based modeling of gas-phase hydrodynamics in biotrickling filters: Influence of packing material on residence time distributions

In this study, the gas-phase hydrodynamics within a 6.5 L biotrickling filter were quantified using pulse-injection residence time distributions (RTDs) recorded with a cost-effective metal oxide (MOx) sensor. This was conducted at a constant gas flow rate of 8 L min −1 across trickling liquid velocities (TLV) ranging from 0 to 10 m h − 1 , using three different packings: polyurethane foam, Tri-Packs Jaeger spheres, and wood bark. A hybrid section-based model was developed and evaluated against two closed-closed axial dispersion variants (AD c c +CSTR and AD c c +PFR). Model discrimination using AIC/BIC and R 2 indicated that the optimal model description is contingent upon the packing material and operating regime: the hybrid model most accurately represented foam and most wood cases, whereas AD c c +CSTR was sufficient for spheres under irrigation, and AD c c +PFR consistently underperformed. Employing the optimal model in each scenario, the Peclet number increased with TLV for PUF and spheres (with diminishing returns at the highest TLV), whereas wood exhibited a low Peclet number and non-monotonic behavior. By explicitly partitioning the mean residence time between the buffer zones and the bed, the hybrid model effectively separates the boundary hold-up from the core dispersion, yielding a more precise representation of the packed bed Peclet number. Overall, MOx-based RTD measurements, in conjunction with model comparison, offer a cost-effective in situ diagnostic tool for differentiating boundary mixing from bed transport, thereby informing packing selection and operating parameters in gas-phase biofiltration. • The impact of packing materials and liquid velocities on gas-phase dispersion in biotrickling filters was studied. • A novel hybrid RTD model that outperforms the traditional axial dispersion closed-closed model was proposed. • PUF exhibited superior hydraulic performance, while wood bark showed significant deviations from plug flow. • Highlighted the critical role of Peclet number in evaluating gas-phase flow dynamics. • Findings contribute to optimizing packing material design for improved biotrickling filter performance.

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Publication Details

Journal
Biochemical Engineering Journal
Published
2025-12-13
DOI
https://doi.org/10.1016/j.bej.2025.110049
Primary Topic
Odor and Emission Control Technologies
Type
article
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article

Hybrid section-based modeling of gas-phase hydrodynamics in biotrickling filters: Influence of packing material on residence time distributions

Felipe Scott, Raúl Muñoz, Patricio A. Moreno‐Casas, Alberto Vergara‐Fernández et al.
Biochemical Engineering Journal
Odor and Emission Control Technologies
article

Hybrid section-based modeling of gas-phase hydrodynamics in biotrickling filters: Influence of packing material on residence time distributions

Felipe Scott, Raúl Muñoz, Patricio A. Moreno‐Casas, Alberto Vergara‐Fernández, Felipe A. Carreño-López, José Sierra‐Pallares
article en

Abstract

In this study, the gas-phase hydrodynamics within a 6.5 L biotrickling filter were quantified using pulse-injection residence time distributions (RTDs) recorded with a cost-effective metal oxide (MOx) sensor. This was conducted at a constant gas flow rate of 8 L min −1 across trickling liquid velocities (TLV) ranging from 0 to 10 m h − 1 , using three different packings: polyurethane foam, Tri-Packs Jaeger spheres, and wood bark. A hybrid section-based model was developed and evaluated against two closed-closed axial dispersion variants (AD c c +CSTR and AD c c +PFR). Model discrimination using AIC/BIC and R 2 indicated that the optimal model description is contingent upon the packing material and operating regime: the hybrid model most accurately represented foam and most wood cases, whereas AD c c +CSTR was sufficient for spheres under irrigation, and AD c c +PFR consistently underperformed. Employing the optimal model in each scenario, the Peclet number increased with TLV for PUF and spheres (with diminishing returns at the highest TLV), whereas wood exhibited a low Peclet number and non-monotonic behavior. By explicitly partitioning the mean residence time between the buffer zones and the bed, the hybrid model effectively separates the boundary hold-up from the core dispersion, yielding a more precise representation of the packed bed Peclet number. Overall, MOx-based RTD measurements, in conjunction with model comparison, offer a cost-effective in situ diagnostic tool for differentiating boundary mixing from bed transport, thereby informing packing selection and operating parameters in gas-phase biofiltration. • The impact of packing materials and liquid velocities on gas-phase dispersion in biotrickling filters was studied. • A novel hybrid RTD model that outperforms the traditional axial dispersion closed-closed model was proposed. • PUF exhibited superior hydraulic performance, while wood bark showed significant deviations from plug flow. • Highlighted the critical role of Peclet number in evaluating gas-phase flow dynamics. • Findings contribute to optimizing packing material design for improved biotrickling filter performance.

Biochemical Engineering JournalVol. 227
Universidad de Valladolid (ES), Universidad de Los Andes, Chile (CL)
Openalex Percentile: Top 68%
Odor and Emission Control Technologies
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