燃烧科学与技术
燃燒科學與技術
연소과학여기술
JOURNAL OF COMBUSTION SCIENCE AND TECHNOLOGY
2013年
6期
507-511
,共5页
黄思嘉%王端阳%张航%李娜%周屈兰
黃思嘉%王耑暘%張航%李娜%週屈蘭
황사가%왕단양%장항%리나%주굴란
钙钛矿%选择性催化还原%氮氧化物%甲烷
鈣鈦礦%選擇性催化還原%氮氧化物%甲烷
개태광%선택성최화환원%담양화물%갑완
perovskite%selective catalytic reduction%NOx%methane
采用溶胶-凝胶法和过量浸渍法分别制备了粉末状及负载型La(1-x)SrxMnO3(x为0、0.2和0.4)催化剂,并用XRD、SEM 对其进行表征,以及检验负载型催化剂在无氧和有氧条件下催化甲烷脱硝的活性.结果表明,掺杂 Sr不会改变钙钛矿特有的晶型结构,并且在Sr摩尔分数为0.2时,催化剂还出现了多孔结构.同时La0.8,Sr0.2,MnO3和La0.6,Sr0.4,MnO3两种催化剂在无氧条件下都具有较好的活性,脱硝效率在800~900,℃条件下能够达到90%以上.在氧体积分数为6%时,La0.8,Sr0.2,MnO3在800,℃时具有较高的催化活性,脱硝效率仍达到80%,La0.6,Sr0.4,MnO3在高温区的催化活性则受到氧气存在的抑制.在有氧条件下,两种催化剂还能相应地提高500~600,℃下的脱硝效率.
採用溶膠-凝膠法和過量浸漬法分彆製備瞭粉末狀及負載型La(1-x)SrxMnO3(x為0、0.2和0.4)催化劑,併用XRD、SEM 對其進行錶徵,以及檢驗負載型催化劑在無氧和有氧條件下催化甲烷脫硝的活性.結果錶明,摻雜 Sr不會改變鈣鈦礦特有的晶型結構,併且在Sr摩爾分數為0.2時,催化劑還齣現瞭多孔結構.同時La0.8,Sr0.2,MnO3和La0.6,Sr0.4,MnO3兩種催化劑在無氧條件下都具有較好的活性,脫硝效率在800~900,℃條件下能夠達到90%以上.在氧體積分數為6%時,La0.8,Sr0.2,MnO3在800,℃時具有較高的催化活性,脫硝效率仍達到80%,La0.6,Sr0.4,MnO3在高溫區的催化活性則受到氧氣存在的抑製.在有氧條件下,兩種催化劑還能相應地提高500~600,℃下的脫硝效率.
채용용효-응효법화과량침지법분별제비료분말상급부재형La(1-x)SrxMnO3(x위0、0.2화0.4)최화제,병용XRD、SEM 대기진행표정,이급검험부재형최화제재무양화유양조건하최화갑완탈초적활성.결과표명,참잡 Sr불회개변개태광특유적정형결구,병차재Sr마이분수위0.2시,최화제환출현료다공결구.동시La0.8,Sr0.2,MnO3화La0.6,Sr0.4,MnO3량충최화제재무양조건하도구유교호적활성,탈초효솔재800~900,℃조건하능구체도90%이상.재양체적분수위6%시,La0.8,Sr0.2,MnO3재800,℃시구유교고적최화활성,탈초효솔잉체도80%,La0.6,Sr0.4,MnO3재고온구적최화활성칙수도양기존재적억제.재유양조건하,량충최화제환능상응지제고500~600,℃하적탈초효솔.
Powder perovskite-type La(1-x)SrxMnO3(x=0,0.2,0.4)were synthesized by sol-gel method,and supported La(1-x)SrxMnO3(x=0.2,0.4)were synthesized by excessive dipping method. The powders were characterized by XRD and SEM,and supported catalysts were then submitted to activity tests in the selective catalytic reduction(SCR)of NO by meth-ane with or without O2. The experimental results showed that the crystal structure of Sr-substituted samples was the charac-teristic perovskite structure,and what’s more,La0.8,Sr0.2,MnO3possessed a porous structure. In the absence of O2,the reduction of NOx by CH4 was performed over La0.8,Sr0.2,MnO3and La0.6,Sr0.4,MnO3,leading to a maximum of 90% at 800-900,℃. The catalytic performance of La0.8,Sr0.2,MnO3 could reach a maximum of 80% at 800,℃ with 6% O2,on the other hand,the performance of La0.6,Sr0.4,MnO3was suppressed by the presence of O2. The catalytic performance was improved by both La0.8,Sr0.2,MnO3and La0.6,Sr0.4,MnO3 at 500-600,℃.