Numerical Assessment of the Effects of Oxygen-Enriched Secondary Air on Fouling-Related Combustion Conditions in a Grate Furnace

Abstract Heat transfer surface fouling severely threatens the safe and efficient operation of municipal solid waste (MSW) grate incinerators and is closely linked to local oxygen-deficient combustion atmospheres. Oxygen-enriched secondary air has been investigated as an approach for modifying furnace combustion conditions; however, its influence on fouling-related combustion conditions remains insufficiently understood. This study adopts computational fluid dynamics (CFD) to investigate combustion behaviors under four secondary air oxygen mass fraction conditions: 0.21, 0.26, 0.31, and 0.36. The O2 and CO characteristics, temperature distribution, and near-wall gas phase features are compared. Simulation results demonstrate spatially nonuniform responses to secondary air oxygen enrichment. Increasing the inlet oxygen fraction reshapes the overall furnace oxygen field, yet near-wall monitoring points exhibit no monotonic increase in local oxygen content. The CO/CO2 and H2/H2O ratios stay at very low levels for all operating scenarios, and the temperature response is also spatially nonuniform. Since changing the secondary air O2/N2 composition simultaneously changes mixture density, mass flow rate, momentum flux, Reynolds number, and total oxygen supply, the obtained results reflect combined system responses rather than the independent effect of oxygen concentration. The present CFD model focuses on gas-phase combustion and excludes detailed particle transport, ash transformation, mineral phase evolution, and deposition mechanisms; hence, it only assesses relative variations of fouling-related combustion conditions and cannot directly quantify ash deposition rates or fouling suppression performance. No single optimal secondary air oxygen enrichment level is determined among the investigated cases. This work provides a numerical basis for assessing the influence of oxygen-enriched secondary air on fouling-related combustion conditions in the grate furnaces.

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Publication Details

Journal
ACS Omega
Published
2026-10-27
DOI
https://doi.org/10.1021/acsomega.6c06180
Primary Topic
Thermochemical Biomass Conversion Processes
Type
article
Field-Weighted Citation Impact
0.00

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article

Numerical Assessment of the Effects of Oxygen-Enriched Secondary Air on Fouling-Related Combustion Conditions in a Grate Furnace

Wenbo Zhao, Wenqiang Dang, Pengjian Wang, 李丰泉 et al.
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ACS Omega
Thermochemical Biomass Conversion Processes
article

Numerical Assessment of the Effects of Oxygen-Enriched Secondary Air on Fouling-Related Combustion Conditions in a Grate Furnace

Wenbo Zhao, Wenqiang Dang, Pengjian Wang, 李丰泉, Hongping Yang, Jianqiang Zhang, Limin Zhao, Чан Лю, Yongzhong Xing, Yurui Pu, Yingchun Li, Yuxiang Zhao, Xiangbing Li, Xiaojian Sun, Dan Zhang
article en

Abstract

Abstract Heat transfer surface fouling severely threatens the safe and efficient operation of municipal solid waste (MSW) grate incinerators and is closely linked to local oxygen-deficient combustion atmospheres. Oxygen-enriched secondary air has been investigated as an approach for modifying furnace combustion conditions; however, its influence on fouling-related combustion conditions remains insufficiently understood. This study adopts computational fluid dynamics (CFD) to investigate combustion behaviors under four secondary air oxygen mass fraction conditions: 0.21, 0.26, 0.31, and 0.36. The O2 and CO characteristics, temperature distribution, and near-wall gas phase features are compared. Simulation results demonstrate spatially nonuniform responses to secondary air oxygen enrichment. Increasing the inlet oxygen fraction reshapes the overall furnace oxygen field, yet near-wall monitoring points exhibit no monotonic increase in local oxygen content. The CO/CO2 and H2/H2O ratios stay at very low levels for all operating scenarios, and the temperature response is also spatially nonuniform. Since changing the secondary air O2/N2 composition simultaneously changes mixture density, mass flow rate, momentum flux, Reynolds number, and total oxygen supply, the obtained results reflect combined system responses rather than the independent effect of oxygen concentration. The present CFD model focuses on gas-phase combustion and excludes detailed particle transport, ash transformation, mineral phase evolution, and deposition mechanisms; hence, it only assesses relative variations of fouling-related combustion conditions and cannot directly quantify ash deposition rates or fouling suppression performance. No single optimal secondary air oxygen enrichment level is determined among the investigated cases. This work provides a numerical basis for assessing the influence of oxygen-enriched secondary air on fouling-related combustion conditions in the grate furnaces.

ACS Omega
Inner Mongolia Electric Power (China) (CN), Environmental Protection Engineering (Greece) (GR), Tianshui Normal University (CN), Inner Mongolia Electric Power Research Institute (CN)
Tianshui Normal University, Science and Technology Program of Gansu Province
Affordable and clean energy
Openalex Percentile: Top 24%
Thermochemical Biomass Conversion Processes
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