Selective Non‐Catalytic Reduction of NO <i> <sub>x</sub> </i> in the Exhaust Gas of Small Wood Gasification Boilers

ABSTRACT The gas‐phase reaction of NO and NH 3 according to the selective non‐catalytic reduction (SNCR) was investigated for the removal of NO x from the exhaust gas of small‐scale wood gasification boilers. The SNCR process was studied in a specially designed laboratory‐scale flow reactor over a temperature range of 700°C–1050°C. The results demonstrated the practical potential of SNCR for application in wood gasification boilers, achieving a NO x conversion of 51% at 900°C and a residence time of 0.465 s, while maintaining an NH 3 slip below 10 ppmv and N 2 O yields below 3 ppmv. Additionally, a simplified global kinetic model of the SNCR reaction was developed to estimate achievable NO x conversions and the required reducing agent demand with limited computational effort.

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Publication Details

Journal
Chemie Ingenieur Technik
Published
2026-07-22
DOI
https://doi.org/10.1002/cite.70149
Primary Topic
Thermochemical Biomass Conversion Processes
Type
article
Field-Weighted Citation Impact
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article

Selective Non‐Catalytic Reduction of NO x in the Exhaust Gas of Small Wood Gasification Boilers

Sven Kureti, Alexander Groß
Chemie Ingenieur Technik
Thermochemical Biomass Conversion Processes
article

Selective Non‐Catalytic Reduction of NO x in the Exhaust Gas of Small Wood Gasification Boilers

Sven Kureti, Alexander Groß
article en

Abstract

ABSTRACT The gas‐phase reaction of NO and NH 3 according to the selective non‐catalytic reduction (SNCR) was investigated for the removal of NO x from the exhaust gas of small‐scale wood gasification boilers. The SNCR process was studied in a specially designed laboratory‐scale flow reactor over a temperature range of 700°C–1050°C. The results demonstrated the practical potential of SNCR for application in wood gasification boilers, achieving a NO x conversion of 51% at 900°C and a residence time of 0.465 s, while maintaining an NH 3 slip below 10 ppmv and N 2 O yields below 3 ppmv. Additionally, a simplified global kinetic model of the SNCR reaction was developed to estimate achievable NO x conversions and the required reducing agent demand with limited computational effort.

Chemie Ingenieur Technik
TU Bergakademie Freiberg (DE)
Openalex Percentile: Top 16%
Thermochemical Biomass Conversion Processes
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