Biological Sulfur Reduction To Generate H2S As a Reducing Agent To Achieve Simultaneous Catalytic Removal of SO2 and NO and Sulfur Recovery from Flue Gas

被引:25
作者
Sun, Jianliang [1 ]
Li, Lianghai [1 ]
Zhou, Guangying [1 ]
Wang, Xue [1 ]
Zhang, Liang [1 ]
Liu, Yueping [1 ]
Yang, Jierui [1 ]
Lu, Xianghong [1 ]
Jiang, Feng [1 ,2 ]
机构
[1] South China Normal Univ, Sch Chem & Environm, Guangzhou 510631, Guangdong, Peoples R China
[2] South China Normal Univ, Environm Res Inst, MOE Key Lab Environm Theoret Chem, Guangzhou 510006, Guangdong, Peoples R China
基金
中国国家自然科学基金;
关键词
WASTE-WATER TREATMENT; HYDROGEN-SULFIDE; SIMULTANEOUS DESULFURIZATION; ELEMENTAL SULFUR; SULFATE REDUCTION; DIOXIDE; DENITRIFICATION; REACTOR; SYSTEM; SCR;
D O I
10.1021/acs.est.7b06551
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The conventional flue gas treatment technologies require high capital investments and chemical costs, which limit their application in industrial sectors. This study developed a sulfur-cycling technology to integrate sulfide production by biological sulfur reduction and simultaneous catalytic desulfurization and denitrification with H2S (H2S-SCDD) for flue gas treatment and sulfur recovery. In a packed bed reactor, high-rate sulfide production (1.63 +/- 0.16 kg S/m(3)-d) from biological sulfur reduction was achieved using organics in wastewater as electron donors at pH around 5.8. 93% of sulfide in wastewater was stripped out as H2Sg, which can be a low-cost reducing agent in the H2S-SCDD process. Over 90% of both SO2 and NO were removed by the H2S-SCDD process under the test conditions, resulting in the formation of sulfur. 88% of the input S (H2Sg and SO2) were recovered as octasulfur with high purity. Besides partial recycling to produce biogenic sulfide, excessive sulfur can be obtained as a sellable product. The integrated sulfur-cycling technology is a chemical-saving and even profitable solution to the flue gas treatment in industrial sectors with wastewater available.
引用
收藏
页码:4754 / 4762
页数:9
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