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分别以γ-Al2O3、无定形硅铝和含少量稀土分子筛的γ-Al2O3为载体,制备了不同系列的NiW体系加氢脱硫催化剂,并在连续流动微反装置上评价了催化剂对4,6-二甲基二苯并噻吩(DMDBT)加氢脱硫反应的催化性能. 结果表明,NiW体系催化剂对该反应具有较高的芳烃加氢和脱硫活性; 先加氢后脱硫是加氢脱硫(HDS)反应的主要途径,提高加氢活性是提高HDS活性最有效的途径; 增强载体的酸性,直接脱硫和裂解活性均有所提高. 同时,酸性载体负载的催化剂还显示出一定的异构化性能,但其加氢活性低于氧化铝负载的催化剂. 酸性载体负载的NiW催化剂的异构化性能在邻二甲苯异构化反应中得到进一步证实. 根据实验结果,讨论了NiW体系催化剂上DMDBT转化反应的不同途径.

参考文献

[1] Kabe T;Ishihara A;Tajima H .[J].Industrial and Engineering Chemistry Research,1992,31(06):1577.
[2] Ma X;Sakanishi K;Isoda T;Mochida I .[J].Industrial and Engineering Chemistry Research,1995,34(03):748.
[3] Houalla M;Broderick D H;de Beer V H J;Gates B C Kwart H .[J].Preprints-American Chemical Society,Division of Petroleum Chemistry,1977,22:941.
[4] Ishihara A;Tajima H;Kabe T.[J].Chemistry Letters,1992(04):669.
[5] Sakanishi K;Ando M;Mochida I .[J].Sekiyu Gakkaishi,1992,35(05):403.
[6] Kilanowski D R;Teeuwen H;de Beer V H J;Gates B C Schuit G C A Kwart H .[J].Journal of Catalysis,1978,55(02):129.
[7] Whitehurst D D;Isoda T;Mochida I .[J].ADVANCES IN CATALYSIS,1998,42:345.
[8] Meille V.;Lemaire M.;Vrinat M.;Schulz E. .HYDRODESULFURIZATION OF ALKYLDIBENZOTHIOPHENES OVER A NIMO/AL2O3 CATALYST - KINETICS AND MECHANISM[J].Journal of Catalysis,1997(1):29-36.
[9] Singhal G H;Espino R L;Sobel J E;Huff J A Jr .[J].Journal of Catalysis,1981,67(02):457.
[10] Macaud M.;Milenkovic A.;Schulz E.;Lemaire M.;Vrinat M. .Hydrodesulfurization of Alkyldibenzothiophenes:Evidence of Highly Unreactive Aromatic Sulfur Compounds[J].Journal of Catalysis,2000(2):255-263.
[11] Ward J W;Hansford R C .[J].Journal of Catalysis,1969,13(02):154.
[12] Landau MV.;Herskowitz M.;Berger D. .HYDRODESULFURIZATION OF METHYL-SUBSTITUTED DIBENZOTHIOPHENES - FUNDAMENTAL STUDY OF ROUTES TO DEEP DESULFURIZATION[J].Journal of Catalysis,1996(1):236-245.
[13] Isoda T;Nagao S;Korai Y;Mochida I .[J].Preprints-American Chemical Society,Division of Petroleum Chemistry,1996,41(03):559.
[14] Stanislaus A;Cooper B H .[J].Catalysis Review-Science and Engineering,1994,36(01):75.
[15] Reinhoudt H R;Troost R;van Schalkwijk S;van Langeveld A D Sie S T Schulz H Chadwick D Cambra J de Beer V H J van Veen J A R Fierro J L G Moulijn J A .[J].Studies in Surface Science and Catalysis,1997,106:237.
[16] Robinson W R A M;van Veen J A R;de Beer V H J;van Santen R A .[J].Fuel Processing Technology,1999(61):103.
[17] Topse H;Clausen B S;Massoth F E.Catalysis: Science and Technology[M].New York:Springer,1996:228.
[18] Topse H;Clausen B S;Topse N-Y;Pedersen E Niemann W Müller A Bgge H Lengeler B .[J].Journal of the Chemical Society,Faraday Transactions 1,1987,83(07):2157.
[19] Mijoin J;Thévenin V;Aguirre N G;Yuze H Wang J Li W Z Pérot G Lemberton J L .[J].Applied Catalysis A:General,1999,180:95.
[20] Kabe T;Ishihara A;Zhang Q .[J].Applied Catalysis A:General,1993,97(01):L1.
[21] Breysse M;Portefaix J L;Vrinat M .[J].Catalysis Today,1991,10(04):489.
[22] Ishihara A;Shirouchi K;Kabe T.[J].Chemistry Letters,1993(04):589.
[23] Muralidhar G;Massoth F E;Shabtai J .[J].Journal of Catalysis,1984,85(01):44.
[24] Massoth F E;Muralidhar G;Shabtai J .[J].Journal of Catalysis,1984,85(01):53.
[25] Ramirez J;Fuentes S;Diaz G;Vrinat M Breysse M Lacroix M .[J].Applied Catalysis,1989,52(03):211.
[26] Isoda T;Nagao S;Korai Y;Mochida I .[J].Preprints-American Chemical Society,Division of Petroleum Chemistry,1996,41(03):563.
[27] Landau M V .[J].Catalysis Today,1997,36(04):393.
[28] Sanchez-Delgado R A .[J].Journal of Molecular Catalysis(China),1994,86(1-3):287.
[29] Michaud P;Lemberton J L;Perot G .[J].Applied Catalysis A:General,1998,169:343.
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