欢迎登录材料期刊网

材料期刊网

高级检索

采用溶胶.凝胶法制备了MoO_3-CeO_2-SiO_2复合氧化物催化剂,通过X射线衍射、傅里叶变换红外光谱和X射线光电子能谱对催化剂进行了表征.在温和条件(40℃,常压)下,以过氧化羟基异丙苯(CHP)为氧化剂,甲苯为溶剂,二苯并噻吩(DBT)为模型硫化物,在固定床流动反应器上考察了该复合氧化物催化剂的氧化脱硫反应性能,并研究了催化剂中Mo/Si和Ce/Si摩尔比对反应活性的影响.结果表明,Mo物种主要以MoO_3的形式存在,最佳Mo/Si和Ce/si摩尔比分别为0.1和0.02.适量CeO_2的引入可以提高SiO_2上MoO_3的分散度.不含CeO_2的催化剂中钼主要以高价态的钼离子(Mo~(6+))存在,添加CeO_2后,可能有一定量的低价态的钼离子(MO~(3+))生成,MoO_3-CeO_2-SiO_2催化剂高的氧化脱硫活性可能与Mo~(5+)的存在有关.

MoO_3-CeO_2-SiO_2 mixed oxides were prepared by the sol-gel method. The catalysts were characterized by X-ray diffraction, Fourier transform infrared spectroscopy, and X-ray photoelectron spectroscopy. The catalyst activity for the oxidative desulfurization of diben-zothiophene (DBT) with cumene hydroperoxide as the oxidant in toluene was investigated at 40℃ and atmospheric pressure. The optimum Mo/Si and Ce/Si molar ratios were 0.1 and 0.02, respectively. Crystalline MoO_3 was observed in the MoO_3-CeO_2-SiO_2 catalysts. The introduction of CeO_2 promoted the high dispersion of MoO_3 over SiO_2. Mo~(6+) was the predominant species in MoO_3/SiO_2, and Mo~(5+) species appeared after the introduction of CeO_2. The presence of Mo~(5+) may be responsible for the good performance of MoO_3-CeO_2-SiO_2 in the oxidative desulfurization of DBT.

参考文献

[1] Yang RT.;Hernandez-Maldonado AJ.;Yang FH. .Desulfurization of transportation fuels with zeolites under ambient conditions[J].Science,2003(5629):79-81.
[2] Song C S .[J].Catalysis Today,2003,86:211.
[3] Shiraishi Y;Tachibana K;Hirai T;Komasawa I .[J].Industrial and Engineering Chemistry Research,2002,41:4362.
[4] Collins F M;Lucy A R;Sharp C .[J].Journal of Molecular Catalysis A:Chemical,1997,117:397.
[5] Otsuki S;Nonaka T;Takashima N;Qian W H Ishihara A Imai T Kabe T .[J].Energy and Fuels,2000,14:1232.
[6] Murata S;Murata K;Kidena K;Nomura M .[J].Energy and Fuels,2004,18:116.
[7] Villasenor F;Loera O;Campero A;Vinigre-gonzalez G .[J].Fuel Processing Technology,2004,86:49.
[8] Wang D;Qian E W;Amano H;Okata K Ishihara A Kabe T .[J].Applied Catalysis A:General,2003,253:91.
[9] Li C;Jiang Z;Gao J;Yang Y Wang S Tian F Sun F Sun X Ying P Han C .[J].Chemistry-A European Journal,2004,10:2277.
[10] 赵地顺,马四国,刘翠微,任红威.相转移催化应用于催化裂化汽油氧化脱硫的研究[J].高等学校化学学报,2006(01):144-146.
[11] 孔令艳,李钢,王祥生,王云.TS-1/过氧化氢催化体系中有机硫化物的选择氧化[J].催化学报,2004(10):775-778.
[12] 王云,李钢,王祥生,金长子.Ti-HMS催化氧化脱除模拟燃料中的硫化物[J].催化学报,2005(07):567-570.
[13] Ishihara A;Wang DH;Dumeignil F;Amano H;Qian EWH;Kabe T .Oxidative desulfurization and denitrogenation of a light gas oil using an oxidation/adsorption continuous flow process[J].Applied Catalysis, A. General: An International Journal Devoted to Catalytic Science and Its Applications,2005(1/2):279-287.
[14] Huang D;Zhai Z;Lu YC;Yang LM;Luo GS .Optimization of composition of a directly combined catalyst in dibenzothiophene oxidation for deep desulfurization[J].Industrial & Engineering Chemistry Research,2007(5):1447-1451.
[15] Miao Y X;Lu G Z;Liu X H;Guo Y L Wang Y Q Guo Y .[J].J Mot Catal A,2009,306:17.
[16] Ma Y C;Ge Q J;Li W Z;Xu H Y .[J].Applied Catalysis B:Environmental,2009,90:99.
[17] Morey M S;Bryan J D;Schwarz S;Stucky G D .[J].Chemistry of Materials,2000,12:3435.
[18] Patterson T A;Carver J C;Leyden D E;Hercules D M .[J].Journal of Physical Chemistry,1976,80:1700.
[19] Vedrine J C;Praliaud H;Meriaudeau P;Che M .[J].Surface Science,1979,80:101.
[20] 张惠良;李宗昌;赵雪英;傅献彩 .[J].催化学报,1993,14:93.
[21] Waelas I E .[J].Catalysis Today,1996,27:437.
上一张 下一张
上一张 下一张
计量
  • 下载量()
  • 访问量()
文章评分
  • 您的评分:
  • 1
    0%
  • 2
    0%
  • 3
    0%
  • 4
    0%
  • 5
    0%