异丁烯选择性氧化及原位漫反射红外光谱研究
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摘要
甲基丙烯酸甲酯(MMA)是重要的丙烯酸树脂单体,市场应用前景十分广阔。MMA传统的合成方法是以丙酮、剧毒的氢氰酸和硫酸为原料,不仅是非环境友好工艺,且副产大量硫酸氢铵。因此,异丁烯选择氧化制备甲基丙烯醛(MAL)是作为异丁烯氧化法制备MMA清洁工艺的关键步骤得到人们的广泛关注,对该催化反应的催化剂及其反应规律进行研究具有重要的理论和实际意义。本文合成了V_x-UVM-7及用钼(Mo)改性后的系列催化剂,并用于异丁烯选择催化氧化研究。并以近年发展起来的研究催化剂表面反应作用机理的实验技术—原位漫反射红外光谱技术对此催化体系进行了机理探索,具体实验内容如下:
     从异丁烯氧化原理出发,在以具有高比表面及比孔容的双峰介孔材料UVM-7的基础上用钒(V)原子取代结构中的硅(Si),探讨通过V杂原子取代制备而成V_x-UVM-7系列催化剂及用Mo进行改性以后在异丁烯氧化制取甲基丙烯醛反应中的催化性能。用杂氮三环络合物法(atrane法)制备了V_x-UVM-7介孔分子筛催化剂和用Mo、V同时取代Si元素之后的Mo-V-UVM-7催化剂。催化剂的评选在固定床反应器中进行,考察了反应温度、异丁烯浓度、原料气的流速、含V量的不同及同等含钒量情况下Mo不同掺杂方式对异丁烯转化率和生成MAL选择性的影响。筛选出活性及选择性较高的催化剂,并用XRD、FT-IR、SEM、ICP、N_2吸附-脱附、UV-vis、TG等表征技术对催化剂进行了表征。实验结果表明,在最佳工艺条件下,异丁烯转化率和MAL的选择性分别可达82.6%、35.6%。
     在确定自建的原位漫反射红外实验装置的分辨率、扫描次数、催化剂粒径和气速等参数的较佳操作值的基础上动态考察了异丁烯氧化的催化剂表面反应和气相反应行为。探索了异丁烯氧化制取甲基丙烯醛的反应机理,为改进催化剂提供了理论依据。结果表明:催化剂表面的选择氧化能够有效抑制深度产物CO_2,CO的生成量,选择氧化的活性中心是催化剂表面的晶格氧。催化剂表面的异丁烯氧化反应有多种反应路径,实验中检测到的中间产物主要有:(ⅰ)p-allylic络合物;(ⅱ)异丁烯与催化剂表面的Br(o|¨)nsted酸位作用形成的甲基烯丙醇物种;(ⅲ)叔丁醇中间物种。
Methyl methacrylate (MMA) is an important precursor in the preparation of acrylic resins. Acetone, highly toxic hydrocyanic acid and sulphuric acid are used as raw materials in traditional method to produce MMA. The seriously poisonous substances and the strong acid not only results in the obvious environment pollution, but also results in the numerous ammonium bisulfate byproduct. Therefore, the selective oxidation of isobutene to methacrolein (MAL) which is a critical step for clean production of MMA from isobutene has been extensively studied for a long time worldwide. So the studies on catalysts and catalytic reaction process for selective oxidation of isobutene to methacrolein are important for both fundamental understanding and industrial application. In the paper, we synthesized series catalysts of V_x-UVM-7 and the V-UVM-7 modified with molybdenum (Mo) element and tested for the oxidation of isobutene. Then, we used in-situ DRIFTS technique to probe the mechanism of selective oxidation of isobutene. The technique is always applied to study surface reaction mechanism recently. Specific experiments as follows:
     Based on the main existing mechanism of selective oxidation of isobutene, we substituted the silicon (Si) with vanadium (V) in the bimodal mesoporous molecular sieve UVM-7 which possesse high specific surface and specific pore volume and explored the catalytical performance of the mesoporous system V_x-UVM-7 and the V-UVM-7 modified with molybdenum (Mo) element in the oxidation of isobutene to MAL. We have prepared V_x-UVM-7 series catalysts and Mo-V-UVM-7 catalysts in which the Mo element also substituted Si element or supported on the mesoporous materials with atrane route method and impregnation method. The oxidizing reactions were carried out in the fixed bed reactor. Simultaneously, we have studied some factors which can influence the conversion of isobutene and the selectivity of the methacrolein. These factors include the temperature of the reaction, the concentration of the isobutene, the flowing rate of raw material gas, the different content of V element and the different methods of incorporating Mo element into the mesoporous materials. We have synthesized many kinds of new catalysts and selected some of them with higher activity and selectivity. Furthermore, we have characterized these catalysts by means of XRD, FT-IR, TEM, ICP, N_2 adsorption/desorption, UV-vis and TG technologies. Results indicated that under the optimal reaction conditions, conversion of isobutene and selectivity of MAL reaches 82.6% and 35.6%, respectively.
     Some parameters such as the resolution, scanning time, catalyst particle size and gas velocity are fixed at best values of self-building in-situ DRIFTS experimental installation, and then it is systemically investigated for the isobutene selective oxidation over Mo-V-UVM-7 catalyst, including surface reaction and gas reaction behavior. Then the catalytic reaction mechanism, which can provide theoretical foundation for improving the catalyst, were discussed with the results of in-situ DRIFTS experiment. The selective oxidation of isobutene over catalyst surface effectively controls deep oxidation products of isobutene such as carbon dioxide and carbon monoxide. The centers of active sites of selective oxidation are surface lattice oxygens. The nature of adsorbed intermediates detected by in-situ DRIFTS are: ( i) a p-allylic intermediate; (ii) an enolic type compound formed in the presence of Bronsted acid sites; (iii) a p-bonedisobutene species interacting with Lewis acid site.
引文
[1]马占彪.甲基丙烯酸酷树脂及其应用[M].北京:化学工业出版社,2002
    [2]孙世林,李吉春,黄剑峰.异丁烯(叔丁醇)氧化生产甲基丙烯酸甲酯的技术进展[J].甘肃科技.2007,23(1):137-139
    [3]杨华.国内外甲基丙烯酸甲酯生产应用与市场分析[J].精细化工原料及中间体.2006,(11):32-36
    [4]王克智.甲基丙烯酸甲酯合成工艺进展[J].江苏化工.1993,21(3):5-8
    [5]韩占刚,李铭灿.异丁烯制甲基丙烯酸甲酯催化剂的研究[J].现代化工.2001,21(4):21-24
    [6]秋文.甲基丙烯酸甲酯的技术进展[J].精细化工原料及中间体.2006,(11):27-30
    [7]刘璐,崇明本,陈丰秋,詹晓力.甲基丙烯酸甲酯绿色工艺研究进展[J].精细石油化工进展.2006,(8):37-40
    [8]Caarrazan S R G.,Martin C.,Rives V.,et al.Selective oxidation of isobutene to methacrolein on multiphasic molybdate based catalysts[J].Appl.Catal.A..1996,135:95-123
    [9]Wang LT.,Ma S Y.,Ruiz P.,et al.Cooperation between MoO3 and other metal oxides in selective oxidation of isobutene to methacrolein[J].J.Mol.Catal..1990,61:99-112
    [10]Mamoru Ai.Partial Oxidation of isobutene to methacrylic acid on V2O5-P2O5 catalysts[J].Bull.Chem.Soc.Jpn..1988,61:2949-2953
    [11]Mamoru Ai.Comparison of catalytic properties for partial oxidation between heteropolyacids and phosphates of vanadium and iron[J].Journal of Molecular Catalysis A:Chemical.1996,114:3-13
    [12]王文波,胡长文,许林.多酸化学导论[M].北京:化学工业出版社,1998
    [13]R.S.MANN,DENIS ROULEAU.Catalytic oxidation of hydrocarbons xidation of isobutylene over copper catalyst[J].Ind.Eng.Chem.Prod.Res.Dev..1964,3(2):94-96
    [14]R.S.MANN,K.C.YAO.Oxidation of isobutene over copper oxide catalysts in the presence of sulfur dioxide[J].Ind.Eng.Chem.Prod.Res.Dev..1969,8(3):331-333
    [15]R.S.MANN,K.C.YAO.Catalytic oxidation of olefins over halogen-modified copper oxide catalysts[J],Ind.Eng.Chem.Prod.Res.Dev..1971,10(1):25-31
    [16]INOUE T,OYAMA S T,IMOTO H,et al.Characterization and selective oxidation catalysis of modified Pt particles on SbO_x[J].Applied Catalysis A:General.2000,191(1/2):131-140
    [17]INOUE T,ASAKURA K,LI W,et al.The interaction of Pt and SbOx in the selective oxidaton of isobutylene to methacrolein[J].Applied Catalysis A:General.1997,165(1/2):183-197
    [18]吴越.催化化学[M].北京:科学出版杜,2000
    [19]李铭岫,韩占刚.稀土氧化物对钼一铋催化剂性能的影响[J].稀土.2003,24(4):9-12
    [20]李镇东,金杏妹.镧系元素对异丁烯选择性氧化反应的影响[J].工业催化.2006,14:278-280
    [21]余长林,蔡铁军,邓谦等.Cs-Fe-Co-Bi-Mn-Mo复合氧化物选择性催化氧化异丁烯[J].化学研究与应用.2003,15(6):855-857
    [22]王蕾,张锁江,李增喜等.制备条件对异丁烯选择性氧化催化剂性能的影响[J].燃料化学学报.2004,32(4):481-485
    [23]王蕾,张锁江,李增喜等.异丁烯为原料制备甲基丙烯酸甲酯的催化剂[J].化工学报.2004,55(12):2082-2085
    [24]庞海舰,王正平,李强等.Mo-Bi-Fe-Co基催化剂的制备方法[J].黑龙江科技学院学报.2006,16(1):34-37
    [25]WANG Lei,LI Zengxi,ZHANG Suojiang,et al.Selective oxidation of isobutylene over Cs-promoted Mo-Bi-Co-Fe-Ce-O catalyst[J].Chinese J Chem Eng..2005,13(5):705-708
    [26]MOENS L,RUIZ P,DELMON B,et al.Evaluation of the role played by bismuth molybdates in Bi_2Sn_2O_7-MoO_3 catalysts used for partial oxidation of isobutene to methacrolein[J].Applied Catalysis A:General.1999,180(1/2):299-315.
    [27]MOENS L,RUIZ P,DELMON B,et al.Cooperation effects towards partial oxidation of isobutene in multiphasic catalysts based on bismuth pyrostannate[J].Applied Catalysis A:General.1998,171(1):131-143.
    [28]MOENS L,RUIZ P,DELMON B,et al.A simplified partial ionic charge model to evaluate the role played by bismuth pyrostannate in multiphase catalysts for the selective oxidation of isobutene to methacrolein[J].Applied Catalysis A:General.2003,249:365-374
    [29]Nianxue Song,Colin Rhodes,Jonathan K.Bartley,et al.Oxidation of isobutene to methacrolein using bismuth molybdate catalysts:Comparison of operation in periodic and continuous feed mode[J].Journal of Catalysis.2005,236:282-291
    [30]钟春龙,温德才,钟邦克.Mo-Te三元氧化物催化剂的研究[J].功能材料,2004,35(3):395-397
    [31]钟春龙,温德才,钟邦克.添加组分对Mo-Te-Ni催化剂性能的影响[J].功能材料,2004,35(3):398-400
    [32]LIU Haichao,ERIC M.Novel Re-Sb-O catalysts for the selective oxidation of isobutane and isobutylene[J].Applied Catalysis A:General.2000,202(2):251-264
    [33]SHISHID0 T,INOUE A,KONISHI T,et al.Oxidation of isobutane over Mo-V-Sb mixed oxide catalyst[J].Catalysis Letters.2000,68(3,4):215-221
    [34]Jingqi Guan,Shujie Wu,Hongsu Wang,et al.Synthesis and characterization of MoVTeCeO catalysts and their catalytic performance for selective oxidation of isobutane and isobutylene[J].Journal of Catalysis.2007251:354-362
    [35]Jingqi Guan,Cheng Xu,Zhuqian Wang,et al.Selective Oxidation of isobutane and Isobutene to Methacrolein over Te-Mo Mixed Oxide Catalysts[J].Catal.Lett..2008,124:428-433
    [36]GAIGUEAUX E M,RUIZ P,DELMON B.Further on the mechanism of the synergy between MoO_3 and a-Sb_2O_4 in the selective of isobutene to methacrolein:Reconstruction of MoO_3 via spillover oxygen[J].Catalysis Today.1996,32(1/4):37-46
    [37]GAIGUEAUX E M,DIETERLE M,RUIZ P,et al.Catalytic performances and stability of three Sb-Mo-O phases in the selective oxidation of isobutene to methacrolein[J].J Phys Chem B.1998,102(51):10542-10555
    [38]GAIGUEAUX E M,RUIZ P,WOLF E E,et al.Atomic force and scanning electron microscopic investigation of the in operandi creation of selective site on MoO_3 mixed with a-Sb_2O_4 in the isobutene to methacrolein oxidation[J].Applied surface science.1997,121/122(11):552-557
    [39]CARRAZAN S R G,CADUS L,DIEU P H,et al.Synergetic effects in multiphase catalysts:The role of FeSbO,as donor2acceptor of spillover oxygen[J].Catalysis Today.1996,32(4):311-319
    [40]WENG L T,SPITAELS N,YASSE B,et al.Phase cooperation between tin and antimony oxides in selective oxidation of isobutene to methacrolein Ⅰ.Mechanical mixtures of SnO_2 and a-Sb_2O_4[J].Journal of Catalysis.1991,132(2):319-342
    [41]WENG LT,YASSE B,LADR1ERE J,et al.Phase cooperation between tin and antimony oxides in selective oxidation of isobutene to methacrolein Ⅱ.Impregnate catalysts[J].Journal of Catalysis.1991,132(2):343-359
    [42]WENG LT,PATRONO P,SHAM E,et al.Phase cooperation between tin and antimony oxides in selective oxidation of isobutene to methacrolein Ⅲ.Coprecipitated catalysts[J].Journal of Catalysis.1991,132(2):360-374
    [43]WENGLT,MA S Y,RUIZ P,et al.Cooperation between MoO_3 and other metal oxides in selective oxidation of isobutene to methacrolein[J].Journal of Molecular Catalysis,1990,61(1):99-112
    [44]蔡铁军,余长林,邓谦等.CsCuHPVAsMoO杂多化合物对异丁烯选择性氧化反应的催化性能[J].催化学报.2003,24(12):951-956
    [45]彭少洪,黄运凤,钟邦克.H_xCU_(1.2)PAs_(0.6)Mo_(12)O_y杂多化合物膜催化剂与异丁烯选择氧化[J].化学与生物工程.2006,23(3):23-25
    [46]He Dayun,Wu Jinglin,Zhong Bangke.Oxidation of isobutene catalyzed by heteropoly compounds[J].Journal of Natural Gas Chemistry.2000,9(3):217-222
    [47]Jingqi Guan,Haiyan Xu,Shubo Jing,et al.Selective oxidation of isobutane and isobutene over vanadium phosphorus oxides[J].Catalysis Communications.2008,10:276-280
    [48]Mamoru Ai.Comparision of catalytic properties for partial Oxidation between herterpolyacids and phosphates of vanadium and iron[J].Journal of Molecular Catalysis A:Chemical.1996,114:3-13
    [49]Jose M,Lopez Nieto,Edwin Acosta Burga,et al.Oxidation of Isobutene over a Silica-Supported Multicomponent Oxide Catalyst[J].Ind.Eng.Chem.Res..1990,29:337-342
    [50]Lu-Tao Weng,Bernard Delmon.Phase cooperation and remote control effects in selective oxidation catalysts[J].Applied Catalysis A:General,1992,81:141-213
    [51]Keulks G W.Propylene oxidation:a model reaction for the selective oxidation of olefins[J].Preprints-Division of Petroleum Chemistry,American Chemical Society,1987,32(1-2):191-199
    [52]Kucherov A V,Slin'kin A.A.Mechanism of radical formation in olefin adsorption on high-Silica zeolites and the problem of the synthesis of aromatic structures[J].Stud.Surf.Sci.Catal..1984,18:77-84
    [53]Kutyrev M Yu,Firsova A A,Matyshak V A,et al.Intermediate forms of selective olefin oxidation and structures of complex molybdenum oxide catalysts.In t.Congr Catal.[Proc],8th 19-84(Pub 1985),4:Ⅳ 463-472
    [54]Matyshak V A,Kurman P V,Kutyrev M.Yu.Surface compounds formed during the catalytic selective oxidation of propylene and isobutylene.Khim.Fiz..1984,3(8):1138-1143
    [55]Samuel Y,Daniel C.Process for the manufacture of methyl methacrylate from isobutyric acid.US4978776,1990
    [56]颤开吉,王国甲,毕颖丽等.催化作用基础(第三版).北京:科学出版社,2005
    [57]Akimoto M,Tsuneki H,Echigoya E.Oxygen species incorporated into methacrylaldehyde in vapor-phase catalytic oxidation of isobutylene[J].Nippon Kagaku Kaishi,1978,(6):805-810
    [58]R.Del Rosso,C.Mazzocchia,P.Centola.OXIDATION OF ISOBUTENE OVER CUPR-OUS OXIDE BETWEEN 400 AND 550℃[J].React.Kinet.Catak Lett..1978,9(1):23-27
    [59]Gaigneaux E M,R uizP,Delmon B,et al.Catalytic synergy via spillover at low temperatuer: the dehydration and dehydrogenation of sec-butanol in the presence of oxygen[J].Catalysis Today.1997,33:151-160
    [60]Mero-oka Y.The role of acidic properties of metal oxide catalysts in the catalytic oxidation [J].Applied CatalysisA:General.1999,181:323-329
    [61]金松寿,有机催化.上海:上海科学技术出版社,1986
    [62]Keulks G W.The mechanism of oxygen atom incorporation into the products of propylene oxidation over bismuth molybdate[J].J.Catal..1970,19(2):232-235
    [63]Wragg R D,Ashmore P G,H ockey J.A.Selective oxidation of propene over bismuth molybdate catalysts:The oxidation of propene using ~(18)O labeled oxygen and catalyst[J].J.Catal.,1971,22(1):49-53
    [64]Ono T,Hironaka T,Kubokawa Y.Oxidation of olefins over bismuth-molybdenum and Cobaltmolybdenum oxides in the presence and absence of gaseous oxygen.Bull.Univ.Osaka Prefect.,Sec.A.1981,30(1):21-27
    [65]沈师孔,阂恩泽.烃类晶格氧选择氧化[J].化学进展,1998,10(2):137-145
    [66]Hoefs E V,Monnier J R,Keulks G W.The investigation of type of active oxygen for the oxidation of propylene over bismuth molybdate catalysts using infrared and Raman spectroscopy[J].J.Catal..1979,57(2):331-337
    [67]Kreuzke L D,Keulks G W.The catalytic oxidation of propylene:V1.Mechanistic studies Utilizing isotopic tracers[J].J.Catal..1980,61(2):316-325
    [68]Grasselli R K.Selectivity and activity fac吐ors in bismuth-molybdate oxidation catalysts[J].Appl Catal..1985,15(1):127-139
    [69]Belgacem J,Kress J,Osbom J A.Catalytic oxidation and ammoxidation of propylene,Modelling studies on well-defined molybdenum complexes[J].J.Mol.Catal..1994,86(1-3):267-285
    [70]Matsuura I.Adsorption equilibria of acrolein and ammonia on the bismuth molybdate koechlinite catalyst[J].J.Catal..1974,33(3):420-433
    [71]Matsuura I,Schuit G C A.Adsorption and reaction of adsorbed species on Bi_2MoO_6 catalyst Influence on sintering and of temperature of reduction[J].J.Catal..1972,25(3):314-325
    [72]Matsuura I,SchuitG C A.Adsorptione quilibria and rates of reactions of adsorbed compounds on reduced and oxidized Bi-Mo catalysts[J].J.Catal..1971,20(1):19-39
    [73]Haber J,Grzybowska B.Mechanism for the oxidation of olefins on mixed oxide catalysts[J].J.Catal..1973,28(3):489-492
    [74]Grzybowaka B,Haber J,Janas J.Interaction of allyl iodide with molybdate catalysts for the selective oxidation of hydrocarbons[J].J.Catal..1977,49(2):150-163
    [75]Aykan K,Sleight A W,RogersD S.Defect control in oxidation catalysts[J].J.Catal..1973,29(1):185-187
    [76]Sleight W.Advanced materials in catalysis.NewY ork:Academic Press,1977
    [77]Moro-oka Y,Ueda W.Multicomponent bismuth molybdate catalyst:a highly functionalized catalyst system for the selective oxidation of olefin[J].Advances in Catalysis.1994,40:233-273
    [78]Matsuura I.Successful design of catalysts-reactivity and structure of multi-system molybdate Catalysts[J].Stud.Surf.Sci.Catal..1989,44:111
    [79]Kai Krauβ,Alfons Drochner,Michael Fehfngs,et al.Oxygen exchange at Mo/V mixed oxides:A transient and ~(18)O isotope study under technical conditions.Journal of Molecular Catalysis A,Chemical.2002,177:237-245
    [80]徐丽,冯钰锜,达世禄等.有序介孔材料在分离科学中的应用[J].分析化学.2004,32(2):374-380
    [81]Everett D.H.In IUPAC manual of symbols and technology[J].PureAppl.Chem.,1972,31,578
    [82]Schmidt-Winkel,P.,Lukens,W.W.Jr.,Zhao,D.et al.Mesocellular siliceous foams with uniformly sized cells and windows[J].J.Am.Chem.Soc.,1999,121(1):254-255
    [83]Estermann M.,Mccusker L.B.,Baerlocher C.et al.A synthetic gallophosphate molecular sieve with a 20-tetrahedral-atom pore opening[J].Nature,1991,352:320-323
    [84]熊艳锋.有机硅高沸物催化裂解制单硅烷新型催化剂研究及机理探讨[M].南昌大学.2007
    [85]Kresge C T,Leonowicz M E,Roth W J,et al.Ordered mesoporous molecular sieves synthesized by a liquid-crystal template mechanism[J].Nature,1992,359:710-712
    [86]Beck J S,Vatuli J C,Roth WJ,et al.A new family of mesoporous molecular sieves prepared with liquid-crystal templates[J].J.Am.Chem.Soc.,1992,114:10834-10843
    [87]祝淑芳,倪文,张铭金等.介孔分子筛材料合成及应用研究的现状及进展[J].岩石矿物学杂志,2006,25(4):327-334
    [88]詹望成,卢冠忠,王艳芹.介孔分子筛的功能化制备及催化性能研究进展[J].化工进展,2006,25(1):1-7
    [89]Grace Davision.Matting agent[EB/OL].http://www.grace.davision.com/products/coatings/syloidma.html.2005-04-08
    [90]Degussa.Matting agent[EB/OL].http://degussa.com/en/products/product database.html.2005-04-08
    [91]Song,H.,Rioux,R.M.,Hoefelmeyer,J.D.,et al.Hydrothermal Growth of Mesoporous SBA-15 Silica in the Presence of PVP-Stabilized Pt Nanoparticles:Synthesis,Characterization,and Catalytic Properties[J].J.Am.Chem.Soc.,2006,128(9):3027-3037
    [92]YongM,Yonguo,Ka K,et al.Highly efficientVOx/SBA-15mesoporous catalysts for oxidative dehydrogenation of p ropane[J].Chem.Commun.,2002,23:2832-2833
    [93]Keisuke K,Jun-ichi T,Takuzo A.Extrusion polymerization catalyzed synthesis of crystaline linear polyethylene nanofibers with in a mesoporous silica[J].Science,1999,285:2113-2115
    [94]A.Corma,M.S.Grande,V.Gonzalez-Alfaro.Cracking Activity and Hydrothermal.Stability of MCM-41 and Its Comparison with Amorphous Silica-Alumina and a USY Zeolite[J].J.Catal,1996,159(2):375-382
    [95]Eric A.Gunnewegh,Saritha S.Gopie,Herman van Bekkum.MCM-41 type molecular sieves as catalysts for the Friedel-Crafts acylation of 2-methoxynaphthalene[J].J.Mol.Catal.A:Chem,1996,106(1-2):151-158
    [96]Elvira Armengol,Maria L.Cano,Avelino Corma,et al.Mesoporous aluminosilicate MCM-41 as a convenient acid catalyst for Friedel-Crafts alkylation of a bulky aromatic compound with cinnamyl alcohol[J].J.Chem.Soc.,Chem.Commun.,1995,(5):519-520
    [97]Reddy.K.M,Moudrakovski I.,Sayari A.Synthesis of mesoporous vanadium silicate molecular sieves[J].J.Chem.Soc.,Chem.Commun.,1994,(9):1059-1060
    [98]Kozheuniko.I.V,Sinnema.A.,Jansen.R.J.New acid catalyst comprising heteropoly acid on a mesoporous molecular sieve MCM-41[J].J.Catal.Lett 1994,30(1-4):241-252
    [99]K.Richard Kloetstra,Herman van Bekkum.Base and acid catalysis by the alkali-containing MCM-41 mesoporous molecular sieve[J].J.Chem.Soc.,Chem.Commun.,1995,(10):1005-1006
    [100]辛勤,梁长海.固体催化剂的研究方法[J].石油化工,2001,30(1):72-85;30(2):157-167;30(3):246-253
    [101]W.W.Coblentz.Investigation of infrared spectra[M].Carnegie Institute.1905,35
    [102]吴瑾光.近代傅里叶变换红外光谱技术及应用上下卷[M].上海:科学技术文献出版社,1994
    [103]W.N.Delgass,G.L.Haller,R.Kellerman,et al.Spectroscopy in Heterogeneous Catalysis[M].刘希尧等译.北京:化学工业出版社,1989:21-65
    [104]尹元根.多相催化剂的研究方法[M].北京:化学工业出版社,1988:545-604
    [105]J.Ryczkowski.IR spectroscopy in catalysis.CatalysisToday[J].2001,6 8(4):263-381
    [106]张平.多相催化中的原位漫反射红外光谱研究[M].华南理工大学,2002
    [107]季生福,季伟捷,冠元等.付里叶变换红外光谱技术用于原位催化研究的新进展[J].石油化工,1995,24:748-755
    [108]R.Mariscal,R.M.Navarro,B.Pawelec,et al.Factors affecting Ni-sulfide formation in Y-type zeolites:a combined Fourier transform infrared and X-ray photoelectron spectroscopy study[J].Microporous Mesoporous Mater.,2000,34(2):181-194
    [109]C.Chundi,B.Abdennour,R.S.John,et al.In situ IR investigation of activation and catalytic ignition of methane over Rh/Al_2O_3 catalysts[J].Appl.Catal.A:General,2008,344(1-2):78-87
    [110]Th.Weber,J.C.Muijsers,J.H.M.C.van Wolput,et al.Basic Reaction Steps in the Sulfidation of Crystalline MoO_3 to MoS_2,As Studied by X-ray Photoelectron and Infrared Emission Spectroscopy[J].J.Phys.Chem.1996,100(33):14144-14150
    [111]F.Qin,E.E.Wolf.Spatially resolved infrared spectroscopy:a novel technique for in situ study of spatial surface[J].Catal.Lett.1996,39:19.
    [112]S.C.Street,C.Xu,D.W.Goodman.The physical and chemical properties of ultrathin oxide films[J].Ann.Rev.Phys.Chem.1997,48:43-68
    [113]A.Hess,E.Kemnitz.Surface acidity and catalytic behavior of modified zirconiumand titanium dioxides[J].Applied Catalysis A:General.1997,149:373-389
    [114]许建华,陈清林,纪红兵.原位漫反射红外光谱技术用于气固催化反应机理的研究[J].化学进展,2008,20(6):811-820
    [115]J.Ryczkowski.IR spectroscopy in catalysis[J].Catal.Today,2001,68(4):263-381
    [116]张平,王乐夫,谭宇新.汽车尾气净化催化剂Ag-ZSM-5选择性催化还原NO[J].中国环境科学,2002,22(4):293-296
    [117]张平,姚焱,王乐夫.原位漫反射红外光谱考察SAPO-34分子筛骨架[J].广州大学学报,2002,1(6):24-27
    [118]阎宏涛,张平.反射光谱法直接测定沉淀物研究[J].分析化学,1998,26(5):511-514
    [119]唐波,江奇,何锡文等.多组分金属催化剂表面漫反射紫外可见光谱研究[J].光谱学与光谱分析,1999,19(1):98-92
    [120]Van Every,W.Kenneth,P.R.Griffiths.Characterization of diffuse reflectance FT-IR spectrometry for heterogeneous catalyst studies[J].Applied Spectroscopy.1991,45(3):347-359
    [121]M.P.Fuller,P.R.Griffiths.Diffuse reflectance measurements by infrared fourier transform Spectrometry[J].Analytical Chemistry.1978,50(13):1906-1910
    [122]I.M.Hamadeh,D.King,P.R.G riffths.Heatable-evacuable cell and optical system for diffuse reflectance Fr-IR spectrometry of adsorbed specises[J].Journal of Catalysis.1984,88(2):264-272
    [123]A.Goguet,S.O.Shekhtman,R.Burch,et al.Pulse-response TAP studies of the reverse water-gas shift reaction over a Pt/CeO_2 catalyst[J].J.Catal.,2006,237(1):102-110
    [124]M.de L.Sania,M.S.Adriana,O.da C.Ivna.H2 production through steam reforming of ethanol over Pt/ZrO_2,Pt/CeO_2 and Pt/CeZrO_2 catalysts[J].Catal.Today,2008,138(3-4):162-168
    [125]L.O.O.Costa,A.M.Silva,L.E.P.Borges,et,al.Partial oxidation of ethanol over Pd/CeO_2and Pd/Y_2O_3 catalysts[J].Catal.Today,2008,138:147-151
    [126]Ruiqin Yang,Yi Zhang,T.Noritatsu.Spectroscopic and kinetic analysis of a new low-temperature methanol synthesis reaction[J].Catal.Lett.,2006,106(3-4):153-159
    [127]N.Sittichai,O.Okan,S.O.Umit.Effect of lanthanide promotion on catalytic performance of sol-gel Ni/Al_2O_3 catalysts in steam reforming of propane[J].J.Mol.Catal.A:Chemical,2006,241(1/2):133-146
    [128]B.Azambre,L.Zenboury,F.Delacroix,et al.Adsorption of NO and NO_2 on ceria-zirconia of composition Ce_(0.69)Zr_(0.31)O_2:A DRIFTS study[J].Catal.Today,2008,137(1-2):278-282
    [129]Q.Elodie,P.Laurent,D.Helen.H2-induced promotion of CO oxidation over unsupported gold[J].Catal.Today,2008,138(1-2):43-49
    [130]Xiao-Mei Chen,Xue-Feng Yang,Ai-Min Zhu.In-situ DRIFTS study on the partial oxidation of ethylene over Co-ZSM-5 catalyst[J].Catal.Commu,2008,In Press
    [131]K.Takehira,T.Shishido,Z.Song,et al.Crystalline CrV0.95P0.05O4 catalyst for the vapor-phase oxidation of picolines[J].Catal.Today,2004.91/92:7-11
    [132]Jamal E1 Haskouri,David Ortiz de Zarate,Carmen Guillem,et al.Silica-based powders and monoliths with bimodal pore systems[J].CHEM.COMMUN.,2002,330-331
    [133]Liu Z.,Sakamoto Y.,Ohsuna T.et al.TEM Studies of Platinum Nanowires Fabricated in Mesoporous Silica MCM-41[J].Angew.Chem.Int.Ed.,2000,39(17):3107-3110
    [134]X.S.Zhao,C.Q.Lu,A.K.Whittaker et al.Comprehensive Study of Surface Chemistry of MCM-41 Using 29Si CP/MAS NMR,FTIR,Pyridine-TPD,and TGA[J].J.Phys.Chem.B,1997,101(33):6525-6531
    [135]F.Kleitz,W.Schmidt,F.Schuth.Calcination behavior of different surfactant-templated mesostructured silica materials.Micropor.Mesopor.Mater[J].2003,65(1):1-29
    [136]L.J.Huerta,P.Amoros,D.Beltran-Porter,et al.Selective oxidative activation of isobutane on a novel vanadium-substituted bimodal mesoporous oxide V-UVM-7[J].Catalysis Today.2006,117:180-186
    [137]P.I.Ravikovitch,D.Wei,W.T.Chueh et al.Evaluation of Pore Structure Parameters of MCM-41 Catalyst Supports and Catalysts by Means of Nitrogen and Argon Adsorption[J].J.Phys.Chem.B,1997,101(19),3671-3679
    [138]Miguel Angel Vicente-Rodriguez,Mercedes Suarez et al.Comparative FT-IR study of the removal of octahedral cations and structural modifications during acid treatment of several silicates[J].Spectrochim Acta Part A,52(1996) 1685-1694.
    [139]Michael Gr(u|¨)n,Klaus K.Unger,Akihiko Matsumoto et al.Novel pathways for the preparation of mesoporous MCM-41 materials:control of porosity and morphology[J].Micropor.Mesopor.Mater.1997,27(2-3):207-216.
    [140]C.G.Sonwane,S.K.,Bhatia,N.Calos.Experimental and theoretical investigations of adsorption hysteresis and criticality in MCM-41:studies with O_2,Ar,and CO_2[J].Ind.Eng.Chem.Res.1998,37(6):2271-2283
    [141]林洪,伊晓东,韩智三等.Te掺杂对MoPO/SiO2催化剂上丙烷选择氧化制丙烯醛反应的影响[J.催化学报,2005,26(6):497-502
    [142]Grasselli R.K.,Burrington J.D..Selective oxidation and ammoxidation of propylene by heterogeneous catalysis[J].Adv.Catal.1981,30:133
    [143]Brazdil J.E,Glaeser L.C.,Grasselli R.K..An investigation of Bismuth and defect cation vacancies in selective oxidation and ammoxidation catalysis[J].J.Catal.1983,81:142-146
    [144]E.V.ROZHKOVA,S.V.GEREI,YA.B.GOROKHOVATSKY.Investigation of chemisorption of butenes on CuO and Cu2O catalysts by infrared spectroscopy[J].J.Catal.1973,29:1-7
    [145]Grasselli R.K.Fundamental principles of selective heterogeneous oxidation catalysis[J].Topics in Catalysis.2002,21(1-3):79-88
    [146]S.R.G.Carrazan,C.Martin,R.Vidal.An FT-IR spectroscopy study of the adsorption and oxidation of propene on multiphase Bi,Mo and Co catalysts[J].Spectrochimica Acta Part A.1996,52:1107-1118
    [147]Andersson A.,Andersson S.L.T.,Centi G..Appl.Catal.A:Gen.1994,113:43
    [148]陈飞.丙烯(氨)氧化原位漫反射红外光谱研究[M]浙江大学.2006
    [149]R.Del rosso,C.Mazzocchia,P.Centola.OXIDATION OF ISOBUTENE OVER CUPROUS OXIDE BETWEEN 400 AND 550℃[J].React.Kinet.Catal.Lett..1978,9(1):23-27
    [150]J.Halasz,K.Varga,P.Fejes.SELECTIVE OXIDATION AND AMMOXIDATION OF ISOBUTENE OVER MIXED OXIDES OF TIN AND ANTIMONY[J].React.Kinet.Catal.Lett..1984,25(1-2):65-69
    [151]Adams C R,Jennings T J.Mechanism studies of the catalytic oxidation of propylene[J].J.Catal..1964,3(6):549-55

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