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利用浸渍法制备了一系列具有不同W/Zr比和不同WO3-ZrO2焙烧温度的1%pd/WO3-ZrO2催化剂.通过X射线衍射、N2吸附、氨程序升温吸附、吡啶吸附红外光谱和程序升温还原方法表征了催化剂的晶体结构、表面状态以及酸性.结果表明,制备条件对W和Pd的表面状态具有很人的影响.随着W/Zr比的增加和焙烧温度的提高,催化剂表而的WOx经历了从聚钨酸物种到聚钨酸/WO3晶体共存再到WO3品体颗粒的转化.W/Zr比为0.2且焙烧湍度为1073K的催化剂具有最多的聚钨酸物种,而该催化剂具有最好的活性.因此,聚钨酸物种的最决定了催化剂的活性.Pd的分散状态只依赖于WO3-ZrO2的焙烧温度.Pd物种分散性好,则乙酸选择性高,而分散性差的人颗粒Pd会导致乙烯的燃烧反应.

A series of 1%Pd/WO3-ZrO2 catalysts with different W/Zr ratios and calcination temperatures of WO3-ZrO2were prepared by an impregnation method. Their crystal structure, surface state, and acidity were determined using X-ray diffraction, N2adsorption, NH3tem-perature-programmed desorption, pyridine infrared spectroscopy, and temperature-programmed reduction. Special attention was paid to the surface states of tungsten and palladium under different preparation conditions. The results revealed that WOxsurface species underwent a transformation from polytungstate species to coexistent polytungstate/crystalline WO3 and further to crystalline WO3particles with increase of W/Zr ratio and calcination temperature. The W/Zr=0.2 sample calcined at 1073 K showed the maximum amount of polytungstates, which were responsible for the excellent activity. Moreover, the state of palladium was only dependent on the calcination temperature. Well-dispersed Pd species were responsible for high selectivity to acetic acid, and large metallic Pd particles were favorable for ethylene combustion.

参考文献

[1] Sano K;Uchida H;Wakabayashi S .[J].Catalysis Surveys from Japan,1999,3:55.
[2] Hiroshi N;Takaharu S;Takashige M;Kyoiehi W .[P].JP 09-100254,1997.
[3] Takaharu S;Masayuki F;Takashige M;Hiroshi N .[P].JP 09-151158,1997.
[4] Capp C W;Harris B W .[P].GB 1142897,1969.
[5] 黄世煜,丁云杰,张连中,李学民,林培滋,罗洪原.乙烯直接氧化制乙酸的研究Ⅰ.Pd-Ru/HPA/SiO2双金属催化剂的催化性能[J].催化学报,2001(06):579-581.
[6] 张迮中;丁云杰;李学民;黄世煜 张家兴 朱何俊 尹红梅 吕元 .[J].催化学报,2003,24:905.
[7] 张连中,丁云杰,李学民,黄世煜,朱何俊,尹红梅,何代平.乙烯直接氧化制乙酸的研究Ⅲ.载体对Pd-Se-Ru-SiW12催化性能的影响[J].催化学报,2004(05):417-420.
[8] 张建鲁,王新平,苏显云,蔡天锡.Pd-SiW12/SiO2催化剂上乙烯直接氧化制乙酸的反应机理[J].催化学报,2002(04):309-311.
[9] Fang K G;Wang X P;Cai T X .[J].Petrochem Technol Appl,2001,19:356.
[10] 张建鲁,王新平,蔡天锡,程谟杰,包信和.载体和担载酸对乙烯直接氧化合成乙酸反应的影响[J].催化学报,2002(03):203-206.
[11] Lopez DE;Goodwin JG;Bruce DA;Lotero E .Transesterification of triacetin with methanol on solid acid and base catalysts[J].Applied Catalysis, A. General: An International Journal Devoted to Catalytic Science and Its Applications,2005(2):97-105.
[12] Furuta S;Matsuhashi H;Arata K .[J].Catalysis Communications,2004,5:721.
[13] Hino M;Arata K.[J].Journal of the Chemical Society,Chemical Communications,1987:1355.
[14] Baertsch C D;Soled S L;Iglesia E .[J].Journal of Physical Chemistry B,2001,105:1320.
[15] Chu W L;Ooka Y;Kamiya Y;Okuhara T Hattori H .[J].Chemistry Letters,2005,34:642.
[16] Chu, WL;Ooka, Y;Kamiya, Y;Okuhara, T .Reaction path for oxidation of ethylene to acetic acid over Pd/WO3-ZrO2 in the presence of water[J].Catalysis Letters,2005(3/4):225-228.
[17] Emeis CA .[J].Journal of Catalysis,1993,141:347.
[18] Pratt K C;Sanders J V;Christov V .[J].Journal of Catalysis,1990,124:416.
[19] Boyse RA.;Ko EI. .CRYSTALLIZATION BEHAVIOR OF TUNGSTATE ON ZIRCONIA AND ITS RELATIONSHIP TO ACIDIC PROPERTIES .1. EFFECT OF PREPARATION PARAMETERS[J].Journal of Catalysis,1997(1):191-207.
[20] Santiesteban JG.;Han S.;Bastian RD.;Chang CD.;Vartuli JC. .INFLUENCE OF THE PREPARATIVE METHOD ON THE ACTIVITY OF HIGHLY ACIDIC WOX/ZRO2 AND THE RELATIVE ACID ACTIVITY COMPARED WITH ZEOLITES[J].Journal of Catalysis,1997(2):431-441.
[21] Huang Y Y;Zhao B Y;Xie Y C .[J].Applied Catalysis A:General,1998,171:75.
[22] Martinez A;Prieto G;Arribas MA;Concepcion P .Hydroconversion of n-hexadecane over Pt/WOx-ZrO2 catalysts prepared by a PVA-template coprecipitation route - The effect of tungsten surface coverage on activity and selectivity[J].Applied Catalysis, A. General: An International Journal Devoted to Catalytic Science and Its Applications,2006(2):224-236.
[23] Lieske H;Volter J .[J].Journal of Physical Chemistry,1985,89:1841.
[24] Boudart M;Hwang H S .[J].Journal of Catalysis,1975,39:44.
[25] Vandagna S R;Comelli R A;Figoli N S .[J].Applied Catalysis A:General,1997,164:265.
[26] Barton D G;Soled S L;Meitzner G D;Fuentes G A Iglesia E .[J].Journal of Catalysis,1999,151:57.
[27] Barton D C;Shtein M;Wilson R D;Soled S L Iglesia E .[J].Journal of Physical Chemistry B,1999,103:630.
[28] Cortes-Jacome MA;Angeles-Chavez C;Lopez-Salinas E;Navarrete J;Toribio P;Toledo JA .Migration and oxidation of tungsten species at the origin of acidity and catalytic activity on WO3-ZrO2 catalysts[J].Applied Catalysis, A. General: An International Journal Devoted to Catalytic Science and Its Applications,2007(0):178-189.
[29] López D E;Suwannakam K;Bruce D A;Goodwin J G .[J].Journal of Catalysis,2007,247:43.
[30] Scheithauer M.;Knozinger H.;Grasselli RK. .Genesis and structure of WOx/ZrO2 solid acid catalysts[J].Langmuir: The ACS Journal of Surfaces and Colloids,1998(11):3019-3029.
[31] Villanneau R;Carabineiro H;Carrier X;Thouvenot R Herson P Lemos F Ribeiro F R Che M .[J].Journal of Physical Chemistry B,2004,108:12465.
[32] Kuba S;Che M;Grasselli R K;Knozinger H .[J].Journal of Physical Chemistry B,2003,107:3459.
[33] Kuba S.;Grasselli RK.;Gates BC.;Che M.;Knozinger H.;Heydorn PC. .Redox properties of tungstated zirconia catalysts: Relevance to the activation of n-alkanes[J].Physical chemistry chemical physics: PCCP,2001(1):146-154.
[34] Li X B;Iglesia E .[J].Angewandte Chemie International Edition,2007,46:8649.
[35] Unterberger W;Gabasch H;Hayek K;Klotzer B .[J].Catalysis Letters,2005,104:1.
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