当代化工
噹代化工
당대화공
Contemporary Chemical Industry
2015年
9期
2057-2060
,共4页
氮氧化物%选择性催化还原%催化剂%堇青石
氮氧化物%選擇性催化還原%催化劑%堇青石
담양화물%선택성최화환원%최화제%근청석
NOx%Selective catalytic reduction(SCR)%Catalysts%Cordierite
先采用溶胶凝胶法在堇青石蜂窝陶瓷载体上涂覆铝溶胶浆液,再通过浸渍法负载活性组分 Mn 和助剂,制备了 NH3选择性催化还原 NOx 低温脱硝催化剂 Mn-Fe-Ce/Al2O3/堇青石,实验结果显示:Ce 和 Fe 的添加可以明显提高催化剂的低温脱硝活性,在体积空速4000 h-1时和120℃条件下,NO 转化率由86.3%提高到93.5%,并且在120~300℃范围内,NO 的转化率均保持在93%以上。XRD、BET、NH3-TPD 和 H2-TPR 结果表明:Fe 和 Ce 改性后增加了催化剂的比表面积和孔体积、酸性位点、NH3的吸附能力和氧化能力,提高了催化剂的 SCR 活性。
先採用溶膠凝膠法在堇青石蜂窩陶瓷載體上塗覆鋁溶膠漿液,再通過浸漬法負載活性組分 Mn 和助劑,製備瞭 NH3選擇性催化還原 NOx 低溫脫硝催化劑 Mn-Fe-Ce/Al2O3/堇青石,實驗結果顯示:Ce 和 Fe 的添加可以明顯提高催化劑的低溫脫硝活性,在體積空速4000 h-1時和120℃條件下,NO 轉化率由86.3%提高到93.5%,併且在120~300℃範圍內,NO 的轉化率均保持在93%以上。XRD、BET、NH3-TPD 和 H2-TPR 結果錶明:Fe 和 Ce 改性後增加瞭催化劑的比錶麵積和孔體積、痠性位點、NH3的吸附能力和氧化能力,提高瞭催化劑的 SCR 活性。
선채용용효응효법재근청석봉와도자재체상도복려용효장액,재통과침지법부재활성조분 Mn 화조제,제비료 NH3선택성최화환원 NOx 저온탈초최화제 Mn-Fe-Ce/Al2O3/근청석,실험결과현시:Ce 화 Fe 적첨가가이명현제고최화제적저온탈초활성,재체적공속4000 h-1시화120℃조건하,NO 전화솔유86.3%제고도93.5%,병차재120~300℃범위내,NO 적전화솔균보지재93%이상。XRD、BET、NH3-TPD 화 H2-TPR 결과표명:Fe 화 Ce 개성후증가료최화제적비표면적화공체적、산성위점、NH3적흡부능력화양화능력,제고료최화제적 SCR 활성。
Mn-Fe-Ce/Al2O3/cordierite monolithic catalyst was prepared via coating Al sol on honeycomb-like cordierite carrier by sol-gel method, loading Mn and additives by impregnation method. The Mn-Fe-Ce/Al2O3/cordierite monolithic catalyst was used for low-temperature selective catalytic reduction (SCR) of NOx with ammonia. The results show that the activity of the catalyst can be significantly improved after doping Fe and Ce. The conversion of NO can be improved by doping Ce and Fe from 86.3% to 93.5% at 120 ℃ with a gas hourly space velocity(GHSV) of 4 000 h-1. The conversion of NO can be more than 93% at 120~ 300 ℃. The XRD,BET, NH3 adsorption and H2-TPR show that the catalyst after adding proper Ce has larger specific surface area and pore volume, contains more acidic site, which can promote NH3 adsorption and NO oxidation activity. These factors may lead to the increasing of the SCR activity of Mn-Fe-Ce/Al2O3/CC catalyst.