中国电机工程学报
中國電機工程學報
중국전궤공정학보
ZHONGGUO DIANJI GONGCHENG XUEBAO
2015年
12期
3054-3060
,共7页
郝江涛%于伟%卢平%徐森荣%吴佳艺%孙桐%尹欣怡
郝江濤%于偉%盧平%徐森榮%吳佳藝%孫桐%尹訢怡
학강도%우위%로평%서삼영%오가예%손동%윤흔이
选择性非催化还原%脱硝%烟气组分%飞灰%添加剂
選擇性非催化還原%脫硝%煙氣組分%飛灰%添加劑
선택성비최화환원%탈초%연기조분%비회%첨가제
selective non-catalytic reduction (SNCR)%NO reduction%flue gas components%fly ash%additives
利用携带流脱硝试验装置,研究了反应温度(Tr)、烟气组分(O2、CO、水蒸气)、飞灰以及碱金属添加剂等对选择性非催化还原(selective non-catalytic reduction,SNCR)脱硝效果的影响,探讨了NO还原机理。结果表明:随着反应温度的升高,SNCR脱硝效率呈现先增加后降低的趋势。随着烟气中氧含量的增加,SNCR脱硝效率呈现先快速增加后逐渐降低的趋势,当氧含量为2%时,脱硝效率取得最大值84.6%。烟气中CO存在对SNCR脱硝具有一定的抑制作用。随着烟气中水蒸气含量(0~15%)的增加,脱硝效率呈现先增加后减少并逐渐趋于稳定的趋势,4%水蒸气条件下 SNCR脱硝效率达到最大值,约为73.5%。碱金属(钠、钾)添加剂对SNCR脱硝具有显著的促进作用,燃煤飞灰对SNCR脱硝效率则具有一定的抑制作用,添加125μmol/mol Na2CO3的SNCR脱硝效率可达84.9%,在水蒸气、CO、Na2CO3和飞灰的耦合作用下,仍可获得72.1%的脱硝效率。
利用攜帶流脫硝試驗裝置,研究瞭反應溫度(Tr)、煙氣組分(O2、CO、水蒸氣)、飛灰以及堿金屬添加劑等對選擇性非催化還原(selective non-catalytic reduction,SNCR)脫硝效果的影響,探討瞭NO還原機理。結果錶明:隨著反應溫度的升高,SNCR脫硝效率呈現先增加後降低的趨勢。隨著煙氣中氧含量的增加,SNCR脫硝效率呈現先快速增加後逐漸降低的趨勢,噹氧含量為2%時,脫硝效率取得最大值84.6%。煙氣中CO存在對SNCR脫硝具有一定的抑製作用。隨著煙氣中水蒸氣含量(0~15%)的增加,脫硝效率呈現先增加後減少併逐漸趨于穩定的趨勢,4%水蒸氣條件下 SNCR脫硝效率達到最大值,約為73.5%。堿金屬(鈉、鉀)添加劑對SNCR脫硝具有顯著的促進作用,燃煤飛灰對SNCR脫硝效率則具有一定的抑製作用,添加125μmol/mol Na2CO3的SNCR脫硝效率可達84.9%,在水蒸氣、CO、Na2CO3和飛灰的耦閤作用下,仍可穫得72.1%的脫硝效率。
이용휴대류탈초시험장치,연구료반응온도(Tr)、연기조분(O2、CO、수증기)、비회이급감금속첨가제등대선택성비최화환원(selective non-catalytic reduction,SNCR)탈초효과적영향,탐토료NO환원궤리。결과표명:수착반응온도적승고,SNCR탈초효솔정현선증가후강저적추세。수착연기중양함량적증가,SNCR탈초효솔정현선쾌속증가후축점강저적추세,당양함량위2%시,탈초효솔취득최대치84.6%。연기중CO존재대SNCR탈초구유일정적억제작용。수착연기중수증기함량(0~15%)적증가,탈초효솔정현선증가후감소병축점추우은정적추세,4%수증기조건하 SNCR탈초효솔체도최대치,약위73.5%。감금속(납、갑)첨가제대SNCR탈초구유현저적촉진작용,연매비회대SNCR탈초효솔칙구유일정적억제작용,첨가125μmol/mol Na2CO3적SNCR탈초효솔가체84.9%,재수증기、CO、Na2CO3화비회적우합작용하,잉가획득72.1%적탈초효솔。
The effects of reaction temperature, flue gas components (O2, CO, water vapor), fly ash and alkali metal additives on NO reduction during the selective non-catalytic reduction (SNCR) process were investigated in an entrained flow reactor, and NO reduction mechanism was also analyzed. The results indicate that: NO removal efficiency of SNCR shows a trend of increase first and decrease later with increasing reaction temperature. NO removal efficiency shows a pattern of rapid increase first and decrease later with increasing oxygen content, and the best NO removal efficiency of 84.6%is obtained when 2%oxygen was used. The additive of carbon monoxide has a certain adverse effect on NO reduction in the SNCR process. NO removal efficiency shows a tendency of increase first, decrease later and being stable gradually with increasing water vapor (0~15%) in the flue gas, and the best NO removal efficiency of 73.5%is obtained at 4%water vapor. Alkali metal (K, Na) additives have significant promoting effects on NO reduction, but the fly ash has a certain adverse effect on NO reduction in the SNCR process. NO removal efficiency through SNCR can reach 84.9% while adding 125μmol/mol Na2CO3 in the flue gas. NO removal efficiency of SNCR still reaches 72.1% through the coupling effect of water vapor, CO, Na2CO3 and fly ash.