Characterization and reactivity of vanadium oxide supported on TiO2-SiO2 mixed oxide support

被引:7
|
作者
Shee, Debaprasad [1 ]
Mitra, Brishti [2 ]
Chary, Komandur V. R. [3 ]
Deo, Goutam [4 ]
机构
[1] Indian Inst Technol Hyderabad, Dept Chem Engn, Sangareddy 502285, Telangana, India
[2] CSJM Univ, Univ Inst Engn & Technol, Dept Chem Engn, Kanpur 208024, Uttar Pradesh, India
[3] Indian Inst Chem Technol, Inorgan & Phys Chem Div, Hyderabad 500007, Andhra Pradesh, India
[4] Indian Inst Technol, Dept Chem Engn, Kanpur 208016, Uttar Pradesh, India
来源
MOLECULAR CATALYSIS | 2018年 / 451卷
关键词
TiO2-SiO2; support; Vanadium oxide; DRIFT; Raman; Kinetic parameter; SELECTIVE CATALYTIC-REDUCTION; KINETIC-PARAMETER ESTIMATION; TITANIA-SILICA; SOL-GEL; OXIDATIVE DEHYDROGENATION; STRUCTURAL-PROPERTIES; ACIDIC PROPERTIES; METAL-OXIDES; FT-IR; PROPANE;
D O I
10.1016/j.mcat.2018.01.020
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
A TiO2-SiO2 support, 90Ti-Si, containing 90 wt.% TiO2 was synthesized by the sol-gel method. Several supported vanadium oxide (vanadia) catalysts, xV90Ti-Si (x = 2-12.5 wt.%) were synthesized by incipient wetness impregnation method using this support. The catalysts and support were characterized and probed with the propane oxidative dehydrogenation (ODH) reaction. The support possesses no rutile phase and retains 30-40% of its initial surface area even after calcination at 1073 K. The surface area loss is accelerated in the presence of vanadia and the rutile phase appears below 1073 K. Surface vanadia species are present for the supported vanadia catalysts calcined at 673 K and the propane ODH activity and propene yield increases with vanadia loading. The ODH activity of the 2V90Ti-Si sample at 673 K is retained even after the catalyst is pre-calcined at 1023 K. Interestingly, the activity of the 4V90Ti-Si sample at 673 K reaches a maximum at an intermediate pre-calcination temperature. The higher vanadia loading samples deactivate with an increase in calcination temperature. The ODH reactivity reveals that the propene yield at iso-conversion increases with loading. Analysis of kinetic parameters also reveals that the rate constant ratio increases with vanadia loading.
引用
收藏
页码:228 / 237
页数:10
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