Pilot-scale testing on catalytic hydrolysis of carbonyl sulfur combined with absorption-oxidation of H2 S for blast furnace gas purification

被引:2
作者
Lin, Yuting [1 ,2 ]
Li, Yuran [1 ]
Wang, Bin [1 ]
Tian, Jinglei [3 ]
Liu, Hongqiang [3 ]
Li, Yiren [3 ]
Xu, Zhicheng
Cao, Qiang [1 ]
Zhu, Tingyu [1 ,4 ]
机构
[1] Chinese Acad Sci, Key Lab Green Proc & Engn, Inst Proc Engn, Innovat Acad Green Manufacture, Beijing 100190, Peoples R China
[2] Univ Chinese Acad Sci, Beijing 100190, Peoples R China
[3] HBIS Grp Co Ltd, Shijiazhuang 050023, Peoples R China
[4] Chinese Acad Sci, Ctr Excellence Reg Atmospher Environm, Inst Urban Environm, Xiamen 361021, Peoples R China
来源
JOURNAL OF ENVIRONMENTAL SCIENCES | 2025年 / 151卷
基金
国家重点研发计划; 中国国家自然科学基金;
关键词
Blast furnace gas; Carbonyl sulfur; Hydrogen sulfide; Hydrogen cyanide; Hydrolysis and oxidation; Activated carbon; CO2; CAPTURE; REMOVAL; DESULFURIZATION; GENERATION; REDUCTION; HYDROGEN; SULFIDE; OXYGEN;
D O I
10.1016/j.jes.2024.03.027
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
About 70 % of the flue gas in the iron -steel industry has achieved multi -pollutant ultra -low emissions in China until 2023, and then the blast furnace gas purification has become the control step and bottleneck. Our research group has designed and constructed the world's first blast furnace gas desulfurization pilot plant with the scale of 2000 Nm 3 /h in October 2021. The pilot plant is a two-step combined desulfurization device including catalytic hydrolysis of carbonyl sulfur (COS) and absorption -oxidation of H 2 S, continuously running for 120 days. In the hydrolysis system, one reason for catalyst deactivation has been verified from the sulfur deposition. HCN in blast furnace gas can be hydrolyzed on the hydrolysis catalyst to produce the nitrogen deposition, which is one of the reasons for catalyst deactivation and has never been found in previous studies. The deposition forms of S and N elements are determined, S element forms elemental sulfur and sulfate, while N element forms -NH 2 and NH 4 + . In the absorption -oxidation system, the O 2 loading and the residence time have been optimized to control the oxidation of HS - to produce elemental sulfur instead of by-product S 2 O 3 2- . The balance and distribution of S and N elements have been calculated for the whole multi -phase system, approximately 84.4 % of the sulfur is converted to solid sulfur product, about 1.3 % of the sulfur and 19.2 % of N element are deposited on the hydrolysis catalyst. The pilot plant provides technical support for multi -pollutant control of blast furnace. (c) 2024 The Research Center for Eco-Environmental Sciences, Chinese Academy of Sciences. Published by Elsevier B.V.
引用
收藏
页码:360 / 372
页数:13
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