Dynamic Experimental Study on Treatment of Acid Mine Drainage by Bacteria Supported in Natural Minerals

被引:19
作者
Dong, Yanrong [1 ]
Di, Junzhen [1 ]
Wang, Xianjun [1 ]
Xue, Lindan [1 ]
Yang, Zhenhua [2 ]
Guo, Xuying [3 ]
Li, Mingwei [1 ]
机构
[1] Liaoning Tech Univ, Coll Civil Engn, Fuxin 123000, Liaoning, Peoples R China
[2] Liaoning Tech Univ, Coll Min, Fuxin 123000, Liaoning, Peoples R China
[3] Liaoning Tech Univ, Coll Sci, Fuxin 123000, Liaoning, Peoples R China
基金
中国国家自然科学基金;
关键词
acid mine drainage; medical stone; bagasse; sulfate-reducing bacteria; immobilized particle; SULFATE-REDUCING BACTERIA; MEDICAL STONE AMENDMENT; SUGARCANE BAGASSE; HEAVY-METALS; REMOVAL; OPTIMIZATION; REDUCTION; MANGANESE; BATCH;
D O I
10.3390/en13020439
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
In order to solve the problem of pollution of acid mine drainage (AMD), such as low pH value and being rich in SO42-, Fe and Mn pollution ions, etc., immobilized particles were prepared by using sugar cane-refining waste (bagasse), a natural composite mineral (called medical stone in China) and sulfate-reducing bacteria (SRB) as substrate materials, based on microbial immobilization technology. Medical stone is a kind of composite mineral with absorbability, non-toxicity and biological activity. The adsorption capacity of medical stone is different according to its geographic origins. Two dynamic columns were constructed with Column 1 filled by Fuxin's medical stone-enhanced SRB immobilized particles, and Column 2 filled by Dengfeng's medical stone-enhanced SRB immobilized particles as fillers. The treatment effect on AMD with SRB-immobilized particles enhanced by medical stone from different areas was compared. Results showed that Column 2 had better treatment effect on AMD. The average effluent pH value of Column 2 was 6.98, the average oxidation reduction potential (ORP) value was -70.17 mV, the average removal percentages of SO42-, Fe2+ and Mn2+ were 70.13%, 83.82% and 59.43%, respectively, and the average chemical oxygen demand (COD) emission was 555.48 mg/L.
引用
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页数:14
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