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分别采用传统成型法和新的成型法制备了一系列以CeO2为主要成分的载体,将贵金属Ru浸渍在这些载体上制备了不同的催化剂.对催化剂的比表面积和机械强度进行了表征,并通过湿式氧化乙酸的静态实验和湿式氧化苯酚的动态实验分别考察了催化剂的活性和稳定性.结果表明,Ru负载在采用新方法成型的载体上制得的催化剂具有更大的比表面积.向CeO2中掺杂Zr能增大载体的比表面积.新方法制备的催化剂Ru/ZrO2-CeO2催化湿式氧化乙酸具有良好的活性,化学需氧量(COD)去除率为98%.在110 h的催化湿式氧化苯酚反应中,苯酚和COD的去除率维持在96%左右,反应过程中活性组分的溶出浓度很小,催化剂表面有少量的积炭,但积炭在300 ℃能够被完全氧化.因而催化剂具有较好的稳定性和工业应用可能性.

参考文献

[1] Maugans C B;Akgerman A .[J].Water Research,1997,31(12):3116.
[2] Imamura S;Fukuda I;Ishida S .[J].Industrial and Engineering Chemistry Research,1988,27(04):718.
[3] Duprez D;Delanoe F;Barbier J Jr;Isnard P Blanchard G .[J].Catalysis Today,1996,29(1-4):317.
[4] Barbier J Jr;Oliviero L;Renard B;Duprez D .[J].Catalysis Today,2002,75(1-4):29.
[5] Renard B;Barbier J;Duprez D;Durecu S .Catalytic wet air oxidation of stearic acid on cerium oxide supported noble metal catalysts[J].Applied Catalysis, B. Environmental: An International Journal Devoted to Catalytic Science and Its Applications,2005(1):1-10.
[6] Oliviero L;Barbier J Jr;Duprez D;Guerrero-Ruiz A Bachiller Baeza B Rodriguez-Ramos I .[J].Applied Catalysis B:Environmental,2000,25(04):267.
[7] Ismagilov Z R;Shkrabina R A;Koryabkina N A .[J].Catalysis Today,1999,47(1-4):51.
[8] Barbier J Jr;Delano(e) F;Jabouille F;Duprez D Blanchard G Isnard P .[J].Journal of Catalysis,1998,177(02):378.
[9] Béziat J-C;Besson M;Gallezot P;Duréu S .[J].Journal of Catalysis,1999,182(01):129.
[10] Pintar A.;Gallezot P.;Besson M. .Catalytic wet air oxidation of Kraft bleaching plant effluents in the presence of titania and zirconia supported ruthenium[J].Applied Catalysis, B. Environmental: An International Journal Devoted to Catalytic Science and Its Applications,2001(1/2):123-139.
[11] 魏复盛.水和废水监测分析方法[M].北京:中国环境科学出版社,1989:354.
[12] Fally F;Perrichon V;Vidal H;Kaspar J Blanco G Pintado J M Bernal S Colon G Daturi M Lavalley J C .[J].Catalysis Today,2000,59(3-4):373.
[13] Boaro M.;Dolcetti G.;Trovarelli A.;de Leitenburg C. .The dynamics of oxygen storage in ceria-zirconia model catalysts measured by CO oxidation under stationary and cycling feedstream compositions[J].Journal of Catalysis,2000(2):338-347.
[14] Hosokawa S;Kanai H;Utani K;Taniguchi Y Saito Y Imamura S .[J].Applied Catalysis B:Environmental,2003,45(03):181.
[15] Oliviero L;Barbier J Jr;Duprez D;Wahyu H,Ponton J W,Metcalfe I S,Mantzavinos D .[J].Applied Catalysis B:Environmental,2001,35(01):1.
[16] Pintar A;Levec J .[J].Journal of Catalysis,1992,135(02):345.
[17] Hamoudi S.;Sayari A.;Larachi F. .Wet oxidation of phenolic solutions over heterogeneous catalysts: Degradation profile and catalyst behavior[J].Journal of Catalysis,1998(2):247-258.
[18] Hamoudi S;Larachi F;Cerrella G;Cassanello M .[J].Industrial and Engineering Chemistry Research,1998,37(09):3561.
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