Modeling of hydrogen sulfide formation in pulverized coal combustion and its application to a full-scale opposed-firing boiler

In pulverized coal-fired power plants, sulfur-induced corrosion of water wall tubes remains a significant operational issue. Accurate prediction of hydrogen sulfide (H 2 S) concentration distributions within the furnace is essential for evaluating corrosion risks and planning maintenance strategies. However, detailed reaction mechanisms for H 2 S prediction are computationally expensive, and simplified models have not been sufficiently validated for large-scale boilers, leaving a practical research gap. In this study, a simplified global reaction model was developed based on detailed chemical reaction analysis. We introduce a reduced model that preserves predictive accuracy while improving computational efficiency for furnace-scale simulations. The model's validity was evaluated by comparing simulation results with experimental data at two vastly different scales, differing by three orders of magnitude, under two-stage combustion conditions: a 760 kW (thermal input) single-burner test facility and a full-scale 2500 MW (thermal input) opposed-firing boiler. The results demonstrated good agreement with experimental data, including trends in H 2 S peak concentrations due to variations in coal properties such as fuel ratio and sulfur content. Subsequently, the influence of coal properties on the wall-side distribution of H 2 S concentration in the boiler was also investigated. The analysis revealed that while the effect of fuel ratio on H 2 S distribution was limited, sulfur content had a strong positive linear correlation with wall-peak H 2 S concentrations across all cases. These findings indicate the practical applicability of the simplified model for corrosion risk assessment and support its potential use as a tool for coal selection and furnace operation optimization in utility boilers. • Elementary reaction analysis enabled development of a three-equation global model. • The global model accurately predicts H 2 S distribution for various coal types. • Model application to full-scale boilers validated H 2 S predictions on furnace walls. • Thermal-fluid analysis clarified how H 2 S forms and spreads on furnace walls.

Authors

Institutions

Publication Details

Journal
Applied Thermal Engineering
Published
2026-01-06
DOI
https://doi.org/10.1016/j.applthermaleng.2026.129721
Primary Topic
Industrial Gas Emission Control
Type
article
Field-Weighted Citation Impact
0.00
Controls
|||
ALL TIME
JAN
FEB
MAR
APR
MAY
JUN
JUL
AUG
SEP
OCT
article

Modeling of hydrogen sulfide formation in pulverized coal combustion and its application to a full-scale opposed-firing boiler

T. Fukada, Kenji TANNO, Hiroki Umetsu, Hiroaki Watanabe et al.
Applied Thermal Engineering
Industrial Gas Emission Control
article

Modeling of hydrogen sulfide formation in pulverized coal combustion and its application to a full-scale opposed-firing boiler

T. Fukada, Kenji TANNO, Hiroki Umetsu, Hiroaki Watanabe, Masahiko MORINAGA
article en

Abstract

In pulverized coal-fired power plants, sulfur-induced corrosion of water wall tubes remains a significant operational issue. Accurate prediction of hydrogen sulfide (H 2 S) concentration distributions within the furnace is essential for evaluating corrosion risks and planning maintenance strategies. However, detailed reaction mechanisms for H 2 S prediction are computationally expensive, and simplified models have not been sufficiently validated for large-scale boilers, leaving a practical research gap. In this study, a simplified global reaction model was developed based on detailed chemical reaction analysis. We introduce a reduced model that preserves predictive accuracy while improving computational efficiency for furnace-scale simulations. The model's validity was evaluated by comparing simulation results with experimental data at two vastly different scales, differing by three orders of magnitude, under two-stage combustion conditions: a 760 kW (thermal input) single-burner test facility and a full-scale 2500 MW (thermal input) opposed-firing boiler. The results demonstrated good agreement with experimental data, including trends in H 2 S peak concentrations due to variations in coal properties such as fuel ratio and sulfur content. Subsequently, the influence of coal properties on the wall-side distribution of H 2 S concentration in the boiler was also investigated. The analysis revealed that while the effect of fuel ratio on H 2 S distribution was limited, sulfur content had a strong positive linear correlation with wall-peak H 2 S concentrations across all cases. These findings indicate the practical applicability of the simplified model for corrosion risk assessment and support its potential use as a tool for coal selection and furnace operation optimization in utility boilers. • Elementary reaction analysis enabled development of a three-equation global model. • The global model accurately predicts H 2 S distribution for various coal types. • Model application to full-scale boilers validated H 2 S predictions on furnace walls. • Thermal-fluid analysis clarified how H 2 S forms and spreads on furnace walls.

Applied Thermal EngineeringVol. 289
Central Research Institute of Electric Power Industry (JP), Kyushu University (JP)
Industry, innovation and infrastructure
Openalex Percentile: Top 95%
Industrial Gas Emission Control
AI Navigator

Ask Laika to Summarize, Analyze, and Connect papers live on the map.

Summarize Papers & Methodologies

Extract key findings, datasets, and comparative methods across publications.

Benchmark Rankings & Visual Analytics

Rank top research institutions, authors, funders, topics, and journals by Field-Weighted Citation Impact (FWCI) and paper volume with instant charts.

Connect Distant Disciplines

Bridge topological clusters on the map to find hidden collaborative intersections.