V2O5/TiO2 acting as both oxygen carrier and catalyst for chemical looping oxidation of H2S at a low temperature

被引:13
作者
Cao, Jiajia [1 ]
Ma, Shiwei [1 ]
Song, Tao [1 ]
机构
[1] Nanjing Normal Univ, Sch Energy & Mech Engn, Nanjing 210023, Peoples R China
基金
中国国家自然科学基金;
关键词
Chemical looping; Oxygen carrier; Sulfur; Fixed bed; SELECTIVE OXIDATION; HYDROGEN-SULFIDE; ELEMENTAL SULFUR; MIXED OXIDES; COMBUSTION; MECHANISM; NH3; O-2; NO;
D O I
10.1016/j.fuel.2022.123999
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Chemical looping oxidization of H2S at a low reaction temperature was investigated. A V2O5/TiO2 oxygen carrier produced by sol-gel method was employed, and experiments were performed in a fixed bed. Effects of reaction temperature (150-250 degrees C), H2S inlet concentration (1000-4000 ppm) and cycles on H2S conversion behavior were investigated. X-ray diffraction (XRD) and X-ray photoelectron spectroscopy (XPS) were used to characterize the oxygen carrier property. Finally, the S conversion pattern and role of oxygen carrier during the proposed chemical looping route were identified. Thermodynamic analysis and experimental results confirmed the proposed elementary sulfur production during reduction stage and a significant SO2 production during oxidization stage. Experimental results confirmed the proposed elementary sulfur production during reduction stage and a significant SO2 production during oxidization stage. At 150 degrees C, the selectivity of SO2 during reduction stage is less than 5%, and the fraction of the converted H2S to S is higher than 95% in the present condition. XRD and XPS results supported that V5+(V2O5) was reduced to V4+(VO2) by the continuous feeding H2S. During oxidization stage, the V2O5/TiO2 material acted as both oxygen carrier and catalyst to produce SO2 for further H2SO4 production.
引用
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页数:10
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