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BiMo基复合氧化物催化剂晶格氧性质与丙烷选择氧化性能 被引量:3

Lattice oxygen properties of BiMo based catalysts for selective oxidation of propane to acrolein
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摘要 研究了不同组成、结构的BiMo基复合氧化物催化剂的丙烷选择氧化至丙烯醛的性能。X射线衍射(XRD)、X光电子能谱(XPS)、原位傅里叶变换激光拉曼光谱(FT-LRS)、电子顺磁共振(ESR)等多种表征结果表明,BiMo基复合氧化物催化剂上丙烷经由中间物丙烯选择氧化至丙烯醛,催化剂的晶格氧为选择性活性氧物种。丙烷直接氧化下丙烷至丙烯醛的选择性和收率与催化剂的MoO物种的氧化-还原性质密切关联,而MoO物种的性质又取决于Mo离子的配位环境,MoO物种的选择性转化丙烷经由丙烯至丙烯醛活性随畸变MoO6八面体、共顶点八面体、共边八面体、MoO4四面体配位环境递增。组成、结构优化调变的催化剂上丙烷选择氧化至丙烯醛选择性和收率可达45%和13.5%,催化剂中具有选择氧化活性的晶格氧物种数可达258μmol/g。 The properties of BiMo based catalysts with varied composition and structure for the direct selective oxidation of propane to acrolein were investigated. It has been seen by XRD, XPS, in situ FT-LRS, and ESR that propane is selectively oxidized to acrolein via propylene intermediate species. The lattice oxygen of the catalysts is the active oxygen species for the selective oxidation of propane to acrolein via propylene; the selectivity and yield of acrolein associate closely with the redox properties of MoO species while the activity of MoO correlates tightly with its coordinated circumstance. The selective activity of MoO is improved in a sequence of locations as distorted octahedral MoO6, corner shared octahedral in koechlinite structure, edge shared octahedral and tetrahedral MoO4 in distorted scheelite structure. The selectivity and yield of acrolein approached 45% and 13.5%, respectively, and the amount of lattice oxygen with selective oxidative activity amounted to 258 μmol/g on the optimum catalyst.
出处 《燃料化学学报》 EI CAS CSCD 北大核心 2007年第6期684-690,共7页 Journal of Fuel Chemistry and Technology
基金 国家重点基础研究发展规划(973计划 2005CB221408)。
关键词 晶格氧 BiMo基复合氧化物 选择氧化 丙烷 丙烯醛 latttice oxygen BiMo based mixed oxides selective oxidation propane acrolein.
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  • 1[1]V(E)DRINE J C,NOVAKOVA E K,DEROUANE E G.Recent developments in the selective oxidation of propane to acrylic and acetic acids[J].Catal Today,2003,81(2):247-262.
  • 2[2]SANCIER K M,WENTRCEK P R,WISE H.Role of sorbed and lattice oxygen in propylene oxidation catalyzed by silica-supported bismuth molybdate[J].J Catal,1975,39(1):141-147.
  • 3[3]CANT N W,HALL W K.Catalytic oxidation:IV Ethylene and propylene oxidation over gold[J].J Phys Chem,1971,75(1):2914-2921.
  • 4[4]CANT N W,HALL W K.Catalytic oxidation:VI Oxidation of labeled olefins over silver[J].J Catal,1978,52(1):81-94.
  • 5[5]KUGLER B L,KOKES R J.Intermediates in the oxidation of propylene over zinc oxide[J].J Catal,1974,32(1):170-173.
  • 6[6]KUGLER B L,GRYDER J W.Investigation of the mechanism of propylene oxidation on zinc oxide[J].J Catal,1976,44(1):126-138.
  • 7[7]KEULKS G W,DANIEL C.The catalytic oxidation of propylene:I Evidence for surface initiated homogeneous reactions[J].J Catal,1971,24(3):529-535.
  • 8[8]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.
  • 9[9]WRAGG R D,ASHMORE P G,HOCKEY J A.On oxygen mobility during catalytic oxidations[J].J Catal,1973,28(2):337-341.
  • 10[10]PEACOCK J M,PARKER A J.The oxidation of propene over bismuth oxide,molybdenum oxide,and bismuth molybdate catalysts:IV The selective oxidation of propene[J].J Catal,1969,15(4):398-406.

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