Assisting denitrification and strengthening combustion by using ammonia/coal binary fuel gasification-combustion: Effects of injecting position and air distribution

The direct co-firing of ammonia (NH 3 ) with coal is an effective approach for reducing carbon emissions from coal-fired plants. However, the limitations of NH 3 combustion, such as its high ignition energy requirement and high NO x emissions, restrict its large-scale co-combustion in coal-fired units. In this study, a self-sustaining gasification–combustion experimental system was employed, and its denitrification performance and combustion strengthening capability for NH 3 /coal binary fuel under different NH 3 injection positions and air distribution methods were evaluated. The results of co-firing 20 % NH 3 in the gasifier revealed that its operating temperature can be flexibly controlled within the optimal reaction temperature window of SNCR by adjusting the primary air ratio (λ 1 ). Increasing λ 1 was beneficial for NH 3 and coal conversion and denitrification in the gasifier; at λ 1 = 0.53, the conversion rate of NH 3 and N 2 reached 86.37 % and 83.59 %, respectively, with no NO x being detected at the gasifier outlet. Furthermore, increasing λ 1 promoted the development of gasified char pore structure , thereby improving reactivity. After entering the down-fired combustor (DFC), increasing λ 1 promoted NH 3 and coal burnout and effectively controlled NO x emissions, reaching a level similar with that of pure coal under λ 1 = 0.53. Co-firing 20 % NH 3 in the DFC also demonstrated that the introduction of inner secondary air was conducive to char burnout , however, increased NH 3 slip. The outer secondary air promoted NH 3 combustion, however, exacerbated NO x emissions and inhibited gasified char combustion . The uniform air distribution method balanced the combustion of NH 3 and gasified char, and effectively controlled NO x emissions. When the same air distribution method was used, co-firing NH 3 in the gasifier was more favourable for NO x control, whereas co-firing NH 3 in the DFC benefited coal burnout. This study provides innovative ideas and serves as a reference for developing enhanced combustion and low NO x emission technologies for large-scale NH 3 co-firing in coal-fired units. • NH 3 /coal gasification-combustion studies conducted in a self-sustaining furnace. • Effects of primary air ratio were explored during NH 3 co-firing in gasifier. • Effects of secondary air distribution were studied during NH 3 co-firing in DFC. • NO x emissions and fuel burnout of different NH 3 injection position were compared.

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Publication Details

Journal
Energy
Published
2024-10-24
DOI
https://doi.org/10.1016/j.energy.2024.133609
Citations
6
Primary Topic
Thermochemical Biomass Conversion Processes
Type
article
Field-Weighted Citation Impact
1.11

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article

Assisting denitrification and strengthening combustion by using ammonia/coal binary fuel gasification-combustion: Effects of injecting position and air distribution

Houzhang Tan, Renhui Ruan, Baochong Cui, Xiaoxiao Wang et al.
6 citations
Energy
Thermochemical Biomass Conversion Processes
1.11
article

Assisting denitrification and strengthening combustion by using ammonia/coal binary fuel gasification-combustion: Effects of injecting position and air distribution

Houzhang Tan, Renhui Ruan, Baochong Cui, Xiaoxiao Wang, Yingjie Zhang, Xuebin Wang, Kejie Zhang, Shilin Yu
article en
6 citations

Abstract

The direct co-firing of ammonia (NH 3 ) with coal is an effective approach for reducing carbon emissions from coal-fired plants. However, the limitations of NH 3 combustion, such as its high ignition energy requirement and high NO x emissions, restrict its large-scale co-combustion in coal-fired units. In this study, a self-sustaining gasification–combustion experimental system was employed, and its denitrification performance and combustion strengthening capability for NH 3 /coal binary fuel under different NH 3 injection positions and air distribution methods were evaluated. The results of co-firing 20 % NH 3 in the gasifier revealed that its operating temperature can be flexibly controlled within the optimal reaction temperature window of SNCR by adjusting the primary air ratio (λ 1 ). Increasing λ 1 was beneficial for NH 3 and coal conversion and denitrification in the gasifier; at λ 1 = 0.53, the conversion rate of NH 3 and N 2 reached 86.37 % and 83.59 %, respectively, with no NO x being detected at the gasifier outlet. Furthermore, increasing λ 1 promoted the development of gasified char pore structure , thereby improving reactivity. After entering the down-fired combustor (DFC), increasing λ 1 promoted NH 3 and coal burnout and effectively controlled NO x emissions, reaching a level similar with that of pure coal under λ 1 = 0.53. Co-firing 20 % NH 3 in the DFC also demonstrated that the introduction of inner secondary air was conducive to char burnout , however, increased NH 3 slip. The outer secondary air promoted NH 3 combustion, however, exacerbated NO x emissions and inhibited gasified char combustion . The uniform air distribution method balanced the combustion of NH 3 and gasified char, and effectively controlled NO x emissions. When the same air distribution method was used, co-firing NH 3 in the gasifier was more favourable for NO x control, whereas co-firing NH 3 in the DFC benefited coal burnout. This study provides innovative ideas and serves as a reference for developing enhanced combustion and low NO x emission technologies for large-scale NH 3 co-firing in coal-fired units. • NH 3 /coal gasification-combustion studies conducted in a self-sustaining furnace. • Effects of primary air ratio were explored during NH 3 co-firing in gasifier. • Effects of secondary air distribution were studied during NH 3 co-firing in DFC. • NO x emissions and fuel burnout of different NH 3 injection position were compared.

EnergyVol. 312
Xi'an Jiaotong University (CN)
Ministry of Science and Technology of the People's Republic of China, National Key Research and Development Program of China
Openalex Percentile: Top 24%
Thermochemical Biomass Conversion Processes
1.11
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