Catalytic Activity and Molecular Behavior of Lanthanum Modified CoSx/γ-Al2O3 Catalysts for the Reduction of SO2 to Sulfur in Smelter Off-Gas Using CO-H2 Mixture as Reductant

被引:22
|
作者
Ge, Tingting [1 ]
Zuo, Cuncun [2 ]
Chen, Hongnan [2 ]
Muhammad, Yaseen [2 ]
Wei, Lubin [1 ]
Li, Chunshan [2 ,3 ]
机构
[1] China Univ Min & Technol Beijing, Sch Chem & Environm Engn, Beijing 100083, Peoples R China
[2] Chinese Acad Sci, Beijing Key Lab Ion Liquids Clean Proc, Natl Key Lab Clean & Efficient Coking Technol, Inst Proc Engn,State Key Lab Multiphase Complex S, Beijing 100190, Peoples R China
[3] Chinese Acad Sci, Inst Proc Engn, Langfang Branch, Langfang 065000, Peoples R China
基金
中国国家自然科学基金;
关键词
GAMMA-ALUMINA SURFACE; ELEMENTAL SULFUR; CARBON-MONOXIDE; STRUCTURAL MODELS; HYDROGEN-SULFIDE; AB-INITIO; COAL-GAS; DIOXIDE; ADSORPTION; RECOVERY;
D O I
10.1021/acs.iecr.8b04323
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In this study, a series of three-component CoSx/gamma-Al2O3 catalysts were developed for the reduction of high-content SO2 to sulfur in smelter off-gas. The introduction of a small amount of lanthanum additive greatly improved the catalytic activity and stability of Co-Cu/gamma-Al2O3 catalysts using coal gas as reductant. The catalysts were characterized by XRD, XPS, BET, and SEM techniques. H-2/CO-TPR was recorded to study redox properties of catalysts. With the use of a CO-H-2 mixture with different proportions, a series of parallel experiments were performed to investigate the mutual impact and relation of CO and H-2. Under optimum conditions, SO2 conversion of 99% and sulfur selectivity of 99% were obtained. The catalyst remained highly active after a long run of 200 h. Process simulation was used to investigate the molecular behavior of catalyst. Combined with in situ infrared characterization, the catalytic mechanism was put forward and verified.
引用
收藏
页码:3595 / 3605
页数:11
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