固定床生物反应器模拟溶浸采铀吸附尾液中Fe2+的氧化试验

doi:10.3969/j.issn.0438-1157.2012.11.045

化工学报 ›› 2012, Vol. 63 ›› Issue (11): 3688-3693.DOI: 10.3969/j.issn.0438-1157.2012.11.045

固定床生物反应器模拟溶浸采铀吸附尾液中Fe²⁺的氧化试验

王清良^1,2, 杨懿全², 杨敬², 陈勇博², 胡鄂明², 张洪灿², 余润兰¹, 邱冠周¹

1. 中南大学资源加工与生物工程学院, 湖南长沙 410083;
2. 南华大学核资源与核燃料工程学院, 湖南衡阳 421001

收稿日期:2012-02-10 修回日期:2012-06-15 出版日期:2012-11-05 发布日期:2012-11-05
通讯作者: 王清良
作者简介:王清良(1969-),男,硕士,教授。
基金资助:
国家自然科学基金项目(51154003)。

Oxidation of Fe²⁺ in simulative adsorption tail solution of leaching uranium through packed bed bioreactor by Acidithiobacillus ferrooxidans

WANG Qingliang^1,2, YANG Yiquan², YANG Jing², CHEN Yongbo², HU Eming², ZHANG Hongcan², YU Runlan¹, QIU Guanzhou¹

1. School of Minerals Processing and Bioengineering, Central South University, Changsha 410083, Hunan, China;
2. School of Nuclear Resource and Nuclear Fuel Engineering, University of South China, Hengyang 421001, Hunan, China

Received:2012-02-10 Revised:2012-06-15 Online:2012-11-05 Published:2012-11-05
Supported by:
supported by the National Natural Science Foundation of China(51154003).

摘要/Abstract

摘要： 以活性炭作载体固定嗜酸氧化亚铁硫杆菌,构建固定床生物反应器,模拟溶浸采铀矿山吸附尾液全Fe浓度和溶液pH条件,对生物反应器氧化Fe²⁺工艺参数进行了试验研究。结果表明:活性炭作载体比无载体时生物反应器氧化Fe²⁺速率增加了1.4倍,由0.5 g·L^-1·h^-1增大至1.2 g·L^-1·h^-1;生物反应器运行过程中溶液中全Fe因生成铁钒而不断消耗,需要定期清理反应器中的铁矾和补充FeSO₄以保持溶液中全Fe浓度;生物反应器最优的操作条件是:底部通气,Fe²⁺浓度为5 g·L^-1时,溶液流量为1.2~1.4 L·h^-1;Fe²⁺浓度为1 g·L^-1时,溶液流量为5.4 L·h^-1。

关键词: 固定床生物反应器, 嗜酸氧化亚铁硫杆菌, 氧化, 溶浸采铀

Abstract: The packed bed bioreactor was designed and set up,active carbon was selected as carrier to immobilize Acidithiobacillus ferrooxidans(A. f).The process parameters of oxidizing ferrous were investigated by simulating ferrous concentration and solution pH value in uranium mine in bioreactor.The results showed that the ferrous oxidation rate could increase 1.4 times from 0.5 g·L^-1·h^-1 to 1.2 g·L^-1·h^-1 with active carbon carrier. Iron in solution was consumed due to formation of NH₄Fe₃(SO₄)₂(OH)₆ during operation.It’s necessary to add ferrous periodically in order to keep certain iron concentration in solution and clean up NH₄Fe₃(SO₄)₂(OH)₆ in bioreactor.The optimum operation condition of bioreactor was ventilation from bottom,ferrous concentration keeping 5 g·L^-1 and solution flux keeping 1.2-1.4 L·h^-1 or ferrous concentration keeping 1 g·L^-1 and solution flux keeping 5.4 L·h^-1.

Key words: packed bed bioreactor, Acidithiobacillus ferrooxidans, oxidation, solution mining of uranium

中图分类号:

王清良, 杨懿全, 杨敬, 陈勇博, 胡鄂明, 张洪灿, 余润兰, 邱冠周. 固定床生物反应器模拟溶浸采铀吸附尾液中Fe²⁺的氧化试验[J]. 化工学报, 2012, 63(11): 3688-3693.

WANG Qingliang, YANG Yiquan, YANG Jing, CHEN Yongbo, HU Eming, ZHANG Hongcan, YU Runlan, QIU Guanzhou. Oxidation of Fe²⁺ in simulative adsorption tail solution of leaching uranium through packed bed bioreactor by Acidithiobacillus ferrooxidans[J]. CIESC Journal, 2012, 63(11): 3688-3693.

参考文献 16

[1]	Wang Qingliang(王清良),Liu Xuanming(刘选明),Liu Yingjiu(刘迎九).Study on bacteria leaching of uranium[J].China Mining Magazine,2004,13(8):62-64
[2]	Li Guangyue(李广悦),Liu Yulong(刘玉龙),Wang Yongdong(王永东),Ding Dexin(丁德馨).A study of effect of Thiobacillus ferrooxidans and Thiobacillus thiooxidans on leaching of U4+[J].Chinese Journal of Nuclear Science and Engineering,2008,4:381-384
[3]	Wang Yonglian(王永莲),Tang Wenjie(唐文杰),Hu Kaiguang(胡凯光).Technology for in-situ Leaching of Uranium[M].Changsha:National University of Defense Technology Press,2007
[4]	Li Shangyuan(李尚远).The Principles and Practice of Heap Leaching of Uranium,Gold and Copper Ores[M].Beijing:Atomic Energy Press,1997
[5]	Zhang Zaihai(张在海),Qiu Guanzhou(邱冠周),Hu Yuehua(胡岳华),Wang Dianzuo(王淀佐).The investigation of the colony isolation of Thiobacillus ferrooxidans[J].Multipurpose Utilization of Mineral Resources,2001,1:119-122
[6]	Wang Weiming(王炜铭),Wang Yinggang(王英刚),Wang Linfang(王林芳).Primary studies on the growth conditions of Thiobacillus ferrooxidans[J].Non-ferrous Mining and Metallurgy,2004,20(5):54-56
[7]	Mazuelos A,Carranza F,Palencia I,Romero R.High efficiency reactor for the biooxidation of ferrous irons[J].Hydrometallurgy,2000,58(3):269-275
[8]	Grishin S I,Tuovinen O H.Fast kinetics of Fe2+ oxidation in packed-bed reactor[J].Appl. Environ. Microbiol.,1988(54):3092-3100
[9]	Zheng Huijie(郑辉杰),Chen Xun(陈洵),Di Jinshen(邸进申).Oxidation of Fe2+ by immobilized Thiobacillus ferrooxidans in packed bed bioreactor[J].Petrochemical Technology,2008,37(6):682-632
[10]	Owen F Rowe,Barrie Johnson D.Comparison of ferric iron generation by different species of acidophilic bacteria immobilized in packed-bed reactor[J].Systematic and Applied Microbiology,2008(31):68-77
[11]	Zhou Jikui,Qing Wenqing,Niu Yinjian.Ferrous ion oxidation by Thiobacillus ferrooxidans immobilized on activated carbon[J].Nonferrous Metals Society of China,2006,16:972-930
[12]	Wang Qingliang(王清良),Hu Kaiguang(胡凯光),Liu Yingjiu(刘迎九),Shi Wenge(史文革),Hu Shihe(胡士河),Hu Yincai(胡银才),Fang Qiu(方遒).Study on bacteria instead of H2O2 for in-situ leaching uranium at No.512 deposit of Yining uranium mine[J].Uranium Mining and Metallurgy,1999,18(4):262-267
[13]	Wang Yanjin(王艳锦),Zheng Zheng(郑正),Peng Xiaocheng(彭晓成),Zhou Peiguo(周培国),Li Peipei(李培培).Study on the isolation and growth characteristics of Thiobacillus ferrooxidan[J].Environmental Protection Science,2007,33(4):31-33,103
[14]	He Liangju(何良菊),Li Xiuyan(李秀艳),Zhou Jianmin(周建民),Wei Dezhou(魏德洲).Effect of Fe2+ and NO4+ on oxidizimg pyrite of Thiobacillus ferrooxidans[J].Gold Journal,1999,1(4):278-280
[15]	Zhou Shungui(周顺桂),Zhou Lixiang(周立祥),Huang Huanzhong(黄焕忠).Biosynthesis and characterization of jarosite[J].Spectroscopy and Spectral Analysis,2004,24(9):1140-1143
[16]	Zhu Changjian(朱长见),Lu Jianjun(陆建军),Lu Xiancai(陆现彩),Liu Xiandong(刘显东),Wang Rucheng(王汝成),Li Qi(李奇),Xu Zhaowen(徐兆文).SEM study on jarosite mediated by Thiobacillus ferrooxidans[J].Geological Journal of China Universities,2005,11(2):234-238

固定床生物反应器模拟溶浸采铀吸附尾液中Fe²⁺的氧化试验

Oxidation of Fe²⁺ in simulative adsorption tail solution of leaching uranium through packed bed bioreactor by Acidithiobacillus ferrooxidans

PDF (PC)

可视化

摘要/Abstract

引用本文

使用本文

参考文献 16

相关文章 15

编辑推荐

Metrics

本文评价

[1]	张义飞, 刘舫辰, 张双星, 杜文静. 超临界二氧化碳用印刷电路板式换热器性能分析[J]. 化工学报, 2023, 74(S1): 183-190.
[2]	胡超, 董玉明, 张伟, 张红玲, 周鹏, 徐红彬. 浓硫酸活化五氧化二钒制备高浓度全钒液流电池正极电解液[J]. 化工学报, 2023, 74(S1): 338-345.
[3]	宋瑞涛, 王派, 王云鹏, 李敏霞, 党超镔, 陈振国, 童欢, 周佳琦. 二氧化碳直接蒸发冰场排管内流动沸腾换热数值模拟分析[J]. 化工学报, 2023, 74(S1): 96-103.
[4]	米泽豪, 花儿. 基于DFT和COSMO-RS理论研究多元胺型离子液体吸收SO₂气体[J]. 化工学报, 2023, 74(9): 3681-3696.
[5]	范孝雄, 郝丽芳, 范垂钢, 李松庚. LaMnO₃/生物炭催化剂低温NH₃-SCR催化脱硝性能研究[J]. 化工学报, 2023, 74(9): 3821-3830.
[6]	杨百玉, 寇悦, 姜峻韬, 詹亚力, 王庆宏, 陈春茂. 炼化碱渣湿式氧化预处理过程DOM的化学转化特征[J]. 化工学报, 2023, 74(9): 3912-3920.
[7]	陈哲文, 魏俊杰, 张玉明. 超临界水煤气化耦合SOFC发电系统集成及其能量转化机制[J]. 化工学报, 2023, 74(9): 3888-3902.
[8]	杨学金, 杨金涛, 宁平, 王访, 宋晓双, 贾丽娟, 冯嘉予. 剧毒气体PH₃的干法净化技术研究进展[J]. 化工学报, 2023, 74(9): 3742-3755.
[9]	陈美思, 陈威达, 李鑫垚, 李尚予, 吴有庭, 张锋, 张志炳. 硅基离子液体微颗粒强化气体捕集与转化的研究进展[J]. 化工学报, 2023, 74(9): 3628-3639.
[10]	程业品, 胡达清, 徐奕莎, 刘华彦, 卢晗锋, 崔国凯. 离子液体基低共熔溶剂在转化CO₂中的应用[J]. 化工学报, 2023, 74(9): 3640-3653.
[11]	李锦潼, 邱顺, 孙文寿. 煤浆法烟气脱硫中草酸和紫外线强化煤砷浸出过程[J]. 化工学报, 2023, 74(8): 3522-3532.
[12]	杨菲菲, 赵世熙, 周维, 倪中海. Sn掺杂的In₂O₃催化CO₂选择性加氢制甲醇[J]. 化工学报, 2023, 74(8): 3366-3374.
[13]	洪瑞, 袁宝强, 杜文静. 垂直上升管内超临界二氧化碳传热恶化机理分析[J]. 化工学报, 2023, 74(8): 3309-3319.
[14]	李凯旋, 谭伟, 张曼玉, 徐志豪, 王旭裕, 纪红兵. 富含零价钴活性位点的钴氮碳/活性炭设计及甲醛催化氧化应用研究[J]. 化工学报, 2023, 74(8): 3342-3352.
[15]	孟令玎, 崇汝青, 孙菲雪, 孟子晖, 刘文芳. 改性聚乙烯膜和氧化硅固定化碳酸酐酶[J]. 化工学报, 2023, 74(8): 3472-3484.