欢迎登录材料期刊网

材料期刊网

高级检索

研究了低温等离子体协助催化条件下甲烷选择性催化还原NO反应(SCR).反应气体经等离子体活化后,生成NO2,HCHO,CH3NO和CH3NO2等活性更高的中间产物.程序升温表面反应表明,这些中间产物可在等离子体后置催化装置上进一步反应,从而使NOx还原为N2.在考察的一系列催化剂(包括γ-Al2O3,Ag/γ-Al2O3,B2O3/γ-Al2O3,Ga2O3/γ-Al2O3,In2O3/γ-Al2O3等)中,B2O3/γ-Al2O3表现出最好的催化活性.当反应温度为300℃时,NOx转化率达到最高.与γ-Al2O3催化剂相比,在10wt% B2O3/γ-Al2O3催化剂上,300℃时,NOx转化为N2的转化率从33.4%提高至51.0%.催化剂的酸性对于经等离子体活化后的反应气体在催化剂上的SCR反应起到重要作用.同时,催化剂上吸附态NOx对于NOx的转化也起到一定作用.

A plasma-assisted catalytic system for the selective catalytic reduction of NO with methane was investigated.NO2,HCHO,CH3NO,and CH3NO2 were the reactive intermediates generated by the plasma.The further reactions of these intermediates on the catalyst during the thermal catalytic stage resulted in the conversion of NOx to N2,which was verified by temperature-programmed surface reaction characterization.B2O3/γ-Al2O3 was the best catalyst with the maximum conversion of NOx to N2 increasing from 33.4% on γ-Al2O3 to 51.0% on 10 wt% B2O3/γ-Al2O3 at 300 ℃.NH3-TPD characterization showed that the acidity of the catalyst is important for the reduction of NOx by the intermediates generated by the plasma.NOx-TPD showed that the adsorbed NOx species on the catalysts also played a role in the conversion of NOx.

参考文献

[1] Chen J P;Yang R T .[J].Journal of Catalysis,1990,125:411.
[2] Georgiadou I;Papadopoulou Ch;Matralis H K;Voyiatzis G A Lycourghiotis A Kordulis Ch .[J].Journal of Physical Chemistry B,1998,102:8459.
[3] Liu C J;Mallinson R;Lobban L .[J].Applied Catalysis A:General,1999,178:17.
[4] Kim H H;Lee Y H;Ogata A;Futamura S .[J].Catalysis Communications,2003,4:347.
[5] Hueso J L;Cotrino J;Caballero A;Espinos J P GonzakezElipe A R .[J].Journal of Catalysis,2007,247:288.
[6] Chen Z;Mathur V K .[J].Industrial and Engineering Chemistry Research,2003,42:6682.
[7] 牛金海,朱爱民,石川,史玲玲,宋志民,徐勇.甲烷参与下催化剂填充型介质阻挡放电等离子体脱除NOx[J].催化学报,2005(09):803-808.
[8] Niu J H;Yang X F;Zhu A M;Shi L L Sun Q Xu y Shi Ch .[J].Catalysis Communications,2006,7:297.
[9] Yoon S;Panov A G;Tonkyn R G;Ebeling A C Barlow S E Balmer M L .[J].Catalysis Today,2002,72:243.
[10] Yoon S;Panov A G;Tonkyn R G;Ebeling A C Barlow S E Balmer M L .[J].Catalysis Today,2002,72:251.
[11] 刘彤,于琴琴,王卉,蒋晓原,郑小明.等离子体与催化剂协同催化CH4选择性还原脱硝反应[J].催化学报,2011(09):1502-1507.
[12] Lukyanov DB.;Ditri JL.;Hall WK.;Sill G. .COMPARISON OF CATALYZED AND HOMOGENEOUS REACTIONS OF HYDROCARBONS FOR SELECTIVE CATALYTIC REDUCTION (SCR) OF NOX[J].Journal of Catalysis,1995(2):265-274.
[13] Spencer N D .[J].Journal of Catalysis,1988,109:187.
[14] Miro E E;Imoberdorf G;Vassallo J;Petunchi J O .[J].Applied Catalysis B:Environmental,1999,22:305.
[15] Yokoyama C;Misono M .[J].Journal of Catalysis,1994,150:9.
[16] Gorce O;Baudin F;Thomas C;Da Costa P;Djega-Mariadassou G .On the role of organic nitrogen-containing species as intermediates in the hydrocarbon-assisted SCR of NOx[J].Applied Catalysis, B. Environmental: An International Journal Devoted to Catalytic Science and Its Applications,2004(2):69-84.
[17] Sato S;Kuroki M;Sodesawa T;Nozaki F Maciel G E .[J].J Mol CatalA,1995,104:171.
[18] Bautista F M;Campelo J M;Garcia A;Luna D Marinas J M Moreno M C Romero A A .[J].Applied Catalysis A:General,1998,170:159.
[19] Yan JY.;Sachtler WMH.;Kung MC.;Kung HH. .Synergistic effect in lean NOx reduction by CH4 over Co/Al2O3 and H-zeolite catalysts[J].Journal of Catalysis,1998(2):294-301.
[20] Regalbuto J R;Zheng T;Miller J T .[J].Catalysis Today,1999,54:495.
[21] Berndt H;Schütze F W;Richter M;Sowade T Grünert W .[J].Applied Catalysis B:Environmental,2003,40:51.
[22] Burch R.;Breen JP.;Meunier FC. .A review of the selective reduction of NOx, with hydrocarbons under lean-burn conditions with non-zeolitic oxide and platinum group metal catalysts [Review][J].Applied Catalysis, B. Environmental: An International Journal Devoted to Catalytic Science and Its Applications,2002(4):283-303.
[23] Kwak J H;Szanyi J;Peden C H F .[J].Journal of Catalysis,2003,220:291.
上一张 下一张
上一张 下一张
计量
  • 下载量()
  • 访问量()
文章评分
  • 您的评分:
  • 1
    0%
  • 2
    0%
  • 3
    0%
  • 4
    0%
  • 5
    0%