Effect of TiO2 on Pd/La2O3-CeO2-Al2O3 Systems during Catalytic Oxidation of Methane in the Presence of H2O and SO2

被引:2
|
作者
Velinova, Ralitsa [1 ]
Todorova, Silviya [2 ]
Kovacheva, Daniela [1 ]
Kolev, Hristo [2 ]
Karakirova, Yordanka [2 ]
Markov, Pavel [1 ]
Tumbalova, Katerina [1 ]
Ivanov, Georgi [1 ]
Naydenov, Anton [1 ]
机构
[1] Bulgarian Acad Sci, Inst Gen & Inorgan Chem, Acad G Bonchev Str,Bl 11, Sofia 1113, Bulgaria
[2] Bulgarian Acad Sci, Inst Catalysis, Acad G Bonchev Str,Bl 11, Sofia 1113, Bulgaria
关键词
methane oxidation; Pd/La2O3-CeO2-TiO2-Al2O3; deactivation; sulfur poisoning; catalyst regeneration; TiO2; PHOTOCATALYTIC PROPERTIES; PHASE-TRANSFORMATION; PD CATALYSTS; COMBUSTION; ANATASE; OXIDE; TEMPERATURE; STABILITY; SURFACE; SULFUR;
D O I
10.3390/ma16206784
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
New results on the effect of TiO2 on Pd/La2O3-CeO2-Al2O3 systems for catalytic oxidation of methane in the presence of H2O and SO2 have been received. Low-temperature N-2-adsorption, XRD, SEM, HRTEM, XPS, EPR and FTIR techniques were used to characterize the catalyst. The presence of Ce3+ on the catalytic surface and in the volume near the lantana was revealed by EPR and XPS. After aging, the following changes are observed: (i) agglomeration of the Pd-clusters (from 8 nm to 12 nm); (ii) transformation of part of the TiO2 from anatase to larger particles of rutile; and (iii)-the increase in PdO/Pd-ratio above its optimum. The modification by Ti of the La2O3-CeO2-Al2O3 system leads to higher resistance towards the presence of SO2 most likely due to the prevailing formation of unstable surface sulfites instead of thermally stable sulfates. Based on kinetic model calculations, the reaction pathway over the Pd/La2O3-CeO2-TiO2-Al2O3 catalyst follows the Mars-van Krevelen mechanism. For evaluation of the possible practical application of the obtained material, a sample of Pd/La2O3-CeO2-TiO2-Al2O3, supported on rolled aluminum-containing stainless steel (Aluchrom VDM (R)), was prepared and tested. Methane oxidation in an industrial-scale monolithic reactor was simulated using a two-dimensional heterogeneous reactor model.
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页数:23
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