TWC-equipped exhausts are widely used in gasoline-fueled vehicles to meet stringent emission regulations.The main components in TWCs are precious metals such as palladium (Pd),platinum (Pt),and rhodium (Rh) as the active component,and inorganic oxides such as γ-alumina (Al2O3),ceria (CeO2),zirconia (ZrO2) and ceria-zirconia (CeO2-ZrO2) are used as the support.Interaction of precious metals and support plays an important role in the thermal stability and catalytic performance of TWCs.The support can improve the dispersion of precious metals and suppress the sintering of precious metals at high temperature.In the same,precious metals can also enhance the redox performance and oxygen storage capacity of support.This paper reviews the reaction phenomenon and mechanism of precious metals (Pt,Pd,Rh) and supports such as Al2O3,CeO2-based composite oxides.
参考文献
[1] | Tauster S J;Fung S C;Garten R L .Strong metal-support interaction group 8 noble metals supported on TiO2[J].Journal of the American Chemical Society,1978,100:170-175. |
[2] | 游少雄,冯长根,王丽琼,曾庆轩,安琴,王亚军.催化剂Pd/CeO2中Pd 与 CeO2之间的SMSI对汽车尾气的催化活性的影响[J].化工科技,2001(03):20-23. |
[3] | Otter G J;Dautzenberg F M .[J].Journal of Catalysis,1978,53:116. |
[4] | Yao H C;Wynblatt P;Sieg H.Platinum[M].New York,1980:561. |
[5] | A.S. Ivanova;E.M. Slavinskaya;R.V. Gulyaev .Metal-support interactions in Pt/Al2O3 and Pd/Al2O3 catalysts for CO oxidation[J].Applied Catalysis, B. Environmental: An International Journal Devoted to Catalytic Science and Its Applications,2010(1/2):57-71. |
[6] | Yao H C;Sieg M;Plummer H K .Surface interactions in the Pt/γ-Al2O3 system[J].Journal of Catalysis,1979,59:365-374. |
[7] | Siani A;Wigal KR;Alexeev OS;Amiridis MD .Synthesis and characterization of gamma-Al2O3-supported Pt catalysts from Pt-4 and Pt-6 clusters formed in aqueous solutions[J].Journal of Catalysis,2008(1):16-22. |
[8] | Deskins N A;Mei D H;Dupuis M .Adsorption and diffusion of a single Pt atom on γ-Al2O3 surfaces[J].Surface Science,2009,603:2793-2807. |
[9] | Yao H C;Japar S;ShelefM .Surface interactions in the system Rh/Al2O3[J].Journal of Catalysis,1977,50:407-418. |
[10] | Linsmeier C;Taglauer E .Strong metal-support interactions on rhodium model catalysts[J].Applied Catalysis A:General,2010,391:175-186. |
[11] | Van C Z;Dealing J C .Rhodium-support interactions in automotive exhaust catalysts[J].Studies in Surface Science and Catalysis,1987,30:369-386. |
[12] | Murrell L L;Tauster S J;Anderson D R .Laser raman characterization of surface phase precious metal oxides formed on CeO2 micro domains generated within an alumina host by sol synthesis[J].Studies in Surface Science and Catalysis,1993,75:681-690. |
[13] | Yasutaka Nagai;Takeshi Hirabayashi;Kazuhiko Dohmae .Sintering inhibition mechanism of platinum supported on ceria-based oxide and Pt-oxide-support interaction[J].Journal of Catalysis,2006(1):103-109. |
[14] | Hatanaka, M.;Takahashi, N.;Takahashi, N.;Tanabe, T.;Nagai, Y.;Suda, A.;Shinjoh, H. .Reversible changes in the Pt oxidation state and nanostructure on a ceria-based supported Pt[J].Journal of Catalysis,2009(2):182-190. |
[15] | Suhonen S;Valden M;Hietikko M et al.Effect of Ce-Zr mixed oxides on the chemical state of Rh in alumina supported automotive exhaust catalysts studied by XPS and XRD[J].Applied Catalysis A:General,2001,218:151-160. |
[16] | Murrell L L;Tauster S J;Anderson D R .Laser raman characterization of surface phase precious metal oxides formed on CeO2[J].Studies in Surface Science and Catalysis,1991,71:275-289. |
[17] | Nagai Y;Dohmae K;Shinjoh H et al.Sintering inhibition mechanism of platinum on ceria-based oxide support for automotive catalysts[J].R&D Review of Toyota CRDL,2006,41(04):32-39. |
[18] | Harrison B;Diwell A F;Hallett C .Promoting platinum metals by ceria metal-support interactions in autocatalysts[J].Platinum Metals Review,1988,32(02):73-83. |
[19] | A. Talo;J. Lahtinen;P. Hautojarvi .An XPS study of metallic three-way catalysts: The effect of additives on platinum, rhodium, and cerium[J].Applied Catalysis, B. Environmental: An International Journal Devoted to Catalytic Science and Its Applications,1995(3):221-231. |
[20] | 屠兢,伏义路,林培琰.Pd/γ-Al2O3三效催化剂中CeO2助剂的作用[J].催化学报,2001(04):390-396. |
[21] | Luo MF.;Yuan XX.;Zheng XM.;Hou ZY. .Characterization study of CeO2 supported Pd catalyst for low-temperature carbon monoxide oxidation[J].Catalysis Letters,1998(3/4):205-209. |
[22] | Luo Meng-Fei;Zheng Xiao-Ming .Redox behaviour and catalytic properties of Ce_(0.5)Zr_(0.5)O_2-supported palladium catalysts[J].Applied Catalysis, A. General: An International Journal Devoted to Catalytic Science and Its Applications,1999(1):15-21. |
[23] | Gabriela Perez Osorio;Sergio Fuentes Moyado;Vitalii Petranovskii .PdO/Al_2O_3-(Ce_(1-x)Zr_x)O_2 catalysts:effect of the sol-gel support composition[J].Catalysis Letters,2006(1/2):53-60. |
[24] | A.I. Boronin;E.M. Slavinskaya;I.G. Danilova .Investigation of palladium interaction with cerium oxide and its state in catalysts for low-temperature CO oxidation[J].Catalysis Today,2009(3/4):201-211. |
[25] | Hirofumi Shinjoh;Miho Hatanaka;Yasutaka Nagai .Suppression of Noble Metal Sintering Based on the Support Anchoring Effect and its Application in Automotive Three-Way Catalysis[J].Topics in Catalysis,2009(13/20):1967-1971. |
[26] | Satoshi Hinokuma;Hiroaki Fujii;Madoka Okamoto .Metallic Pd Nanoparticles Formed by Pd-O-Ce Interaction: A Reason for Sintering-Induced Activation for CO Oxidation[J].Chemistry of Materials: A Publication of the American Chemistry Society,2010(22):6183-6190. |
[27] | Hirataa H;Kishita K;Nagai Y et al.Characterization and dynamic behavior of precious metals in automotive exhaust gas purification catalysts[J].Catalysis Today,2010,164:467-473. |
[28] | Bemal S;Calvino J J;Cauqui M A et al.Some recent results on metal/support interaction effects in NM/CeO2 (NM:noble metal)catalysts[J].Catalysis Today,1999,50:175-206. |
[29] | Penner S.;Wang D.;Su DS.;Rupprechter G.;Podloucky R.;Schlogl R. Hayek K. .Platinum nanocrystals supported by silica, alumina and ceria: metal-support interaction due to high-temperature reduction in hydrogen[J].Surface Science: A Journal Devoted to the Physics and Chemistry of Interfaces,2003(0):276-280. |
[30] | Hardacre C.;Lambert RM.;Rayment T. .PLATINUM/CERIA CO OXIDATION CATALYSTS DERIVED FROM PT/CE CRYSTALLINE ALLOY PRECURSORS[J].Journal of Catalysis,1996(1):102-108. |
[31] | Kpifiski L;Wotcyrz M .Microstructure of Pd/CeO2 catalyst:Effect of high temperature reduction in hydrogen[J].Applied Catalysis A:General,1997,150:197-220. |
[32] | Botana B S;Calvino F J .HREM study of the behaviour of a Rh/CeO2 catalyst under high temperature reducing and oxidizing conditions[J].Catalysis Today,1995,23:219-250. |
[33] | Lin W Y;Herzing A A;Kiely C J et al.Probing metal support interactions under oxidizing and reducing conditions:in situ raman and infrared spectroscopic and scanning transmission electron microscopic x-ray energy-dispersive spectroscopic investigation of supported platinum catalysts[J].Journal of Physical Chemistry,2008,112:5942-5951. |
[34] | Knozinger H;Taglauer E;Ertl G J.In Handbook of Heterogeneous Catalysis[M].Weinheim,Germany:VCH,1997:216. |
[35] | Sun HP;Pan XP;Graham GW;Jen HW;McCabe RW;Thevuthasan S;Peden CHF .Partial encapsulation of Pd particles by reduced ceria-zirconia[J].Applied physics letters,2005(20):1915-1-1915-3-0. |
[36] | Graham G.W.;Jen H.-W.;Chun W. .High-Temperature-Aging-Induced Encapsulation of Metal Particles by Support Materials: Comparative Results for Pt, Pd, and Rh on cerium-Zirconium Mixed Oxides[J].Journal of Catalysis,1999(1):228-233. |
[37] | Gayen, A;Priolkar, KR;Sarode, R;Jayaram, V;Hegde, MS;Subbanna, GN;Emura, S .Ce1-xRhxO2-delta solid solution formation in combustion-synthesized Rh/CeO2 catalyst studied by XRD, TEM, XPS, and EXAFS[J].Chemistry of Materials,2004(11):2317-2328. |
[38] | Priolkar KR.;Bera P.;Sarode PR.;Hegde MS.;Emura S.;Kumashiro R. Lalla NP. .Formation of Ce1-xPdxO2-delta solid solution in combustion-synthesized Pd/CeO2 catalyst: XRD, XPS, and EXAFS investigation[J].Chemistry of Materials,2002(5):2120-2128. |
- 下载量()
- 访问量()
- 您的评分:
-
10%
-
20%
-
30%
-
40%
-
50%