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介绍了有色矿山酸性废水的来源、分布及其危害,分析总结了改造选矿流程、中和法、硫化法和置换中和法等经济、实用的矿山酸性废水处理技术现状.提出最佳的处理工艺要体现出以下优点保证处理效果,运行稳定;基建投资少;能耗和运行费用低;占地面积少;管理简单;污泥量少等.还进一步阐述了矿山酸性废水处理技术的发展前景,指出高效、廉价、安全及操作简便是矿山酸性废水处理技术的发展方向. 相似文献
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金属矿山酸性废水的形成机理比较复杂,且pH值低、酸度大、重金属离子含量高。以马鞍山向山垃圾场尾矿坝酸性废水为研究对象,通过不同中和药剂的添加试验,分析、总结了此类废水处理的一般规律,并对处理后废水pH出现返酸现象进行了研究分析,并提出了处理意见;从技术经济和环保的角度得出用电石渣处理该酸性废水最为合理的结论。 相似文献
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马钢南山铁矿酸性废水治理过程可分为三个阶段:初始阶段、攻坚阶段、突破阶段。从工艺技术角度分析其得失后,提出了技术改进措施。 相似文献
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《Hydrometallurgy》2005年77卷(1~2)期上发表了Luptarova A·文章,介绍用硫酸盐还原菌(SRB)修复被重金属污染的酸性矿山外排废水的研究成果。随采矿活动的进行,酸性矿山外排废水(AMD)已成为威胁环境的主要问题。这种利用SRB去除AMD中重金属的方法是基于SRB在该环境下产生HS-,从而使重金属生成溶解度较小的硫化物沉淀。反应式如下:4 H2 SO42- H SRBHS- 4 H2O,有机质(C·H·O) SO42-SRBHS- HCO3-,Me2 HS-MeS H 。作者以2种不同的方法,考察了SRB对样品溶液中沉淀Cu2 的动力学。第一种方法使用1个反应器,在该反应器种,… 相似文献
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酸性矿山废水(AMD)是最为严重的环境污染之一,主要由黄铁矿氧化引起。AMD的治理主要有末端处理和源头控制两条途径,末端处理技术不能从根本上解决污染问题,因此从源头控制黄铁矿的氧化是治理AMD的根本途径。源头控制技术主要有覆盖法、杀菌法和表面钝化法等,表面钝化法是目前科研工作者的研究热点。在介绍AMD成因的基础上,综述了各种表面钝化技术。重点概述了有机硅烷、载体-微胶囊化、自修复等技术的研究现状,分析了不同方法的优缺点,并针对其不足之处提出了今后的研究方向。为解决黄铁矿氧化问题、实现AMD污染的有效治理提供参考。 相似文献
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Jeff Skousen Carl E. Zipper Arthur Rose Paul F. Ziemkiewicz Robert Nairn Louis M. McDonald Robert L. Kleinmann 《Mine Water and the Environment》2017,36(1):133-153
When appropriately designed and maintained, passive systems can provide long-term, efficient, and effective treatment for many acid mine drainage (AMD) sources. Passive AMD treatment relies on natural processes to neutralize acidity and to oxidize or reduce and precipitate metal contaminants. Passive treatment is most suitable for small to moderate AMD discharges of appropriate chemistry, but periodic inspection and maintenance plus eventual renovation are generally required. Passive treatment technologies can be separated into biological and geochemical types. Biological passive treatment technologies generally rely on bacterial activity, and may use organic matter to stimulate microbial sulfate reduction and to adsorb contaminants; constructed wetlands, vertical flow wetlands, and bioreactors are all examples. Geochemical systems place alkalinity-generating materials such as limestone in contact with AMD (direct treatment) or with fresh water up-gradient of the AMD. Most passive treatment systems employ multiple methods, often in series, to promote acid neutralization and oxidation and precipitation of the resulting metal flocs. Before selecting an appropriate treatment technology, the AMD conditions and chemistry must be characterized. Flow, acidity and alkalinity, metal, and dissolved oxygen concentrations are critical parameters. This paper reviews the current state of passive system technology development, provides results for various system types, and provides guidance for sizing and effective operation. 相似文献
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Abstract.
State and federal reclamation programs, mining operators,
and citizen-based watershed organizations have constructed
hundreds of passive systems in the eastern U. S. over the past
20 years to provide reliable, low cost, low maintenance mine
water treatment in remote locations. While performance has been
reported for individual systems, there has not been a
comprehensive evaluation of the performance of each treatment
type for a wide variety of conditions. We evaluated 83 systems;
five types in eight states. Each system was monitored for
influent and effluent flow, ph, net acidity, and metal
concentrations. Performance was normalized among types by
calclating acid loading reductions and removals, and by
converting construction cost, projected service life, and metric
tonnes of acid load treated into cost per tonne of acid treated.
Of the 83 systems, 82 reduced acid load. Average acid load
reductions were 9.9 t/yr for open limestone channels (OLC), 10.1
t/yr for vertical flow wetland (VFW), 11.9 t/yr for anaerobic
wetlands (AnW), 16.6 t/yr for limestone leach beds (LSB), and
22.2 t/yr for anoxic limestone drains (ALD). Average costs for
acid removal varied from $83/t/yr for ALDs to $527 for AnWs.
Average acid removals were 25
g/m2/day for AnWs, 62
g/m2/day for VFWs, 22 g/day/t for
OLCs, 28 g/day/t for LSBs, and 56 g/day/t for ALDs. It appears
that the majority of passive systems are effective but there was
wide variation within each system type, so improved reliability
and efficiency are needed. This report is an initial step in
determining passive treatment system performance; additional
work is needed to refine system designs and monitoring. 相似文献
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The alkali–barium–calcium (ABC) desalination process is basically an integrated lime/limestone neutralisation process combined with a sulfate removal stage using barium carbonate (BaCO3), and a sludge processing stage. The BaSO4/CaCO3 sludge generated during the desalination stage is treated to recover BaS and CaO by dewatering and thermal processes, with the ultimate goal of producing sulfur and recovering BaCO3. BaCO3 is the main raw material used for sulfate removal and its recovery ensures that the ABC process is environmentally and financially sustainable. South Africa is also a large importer of sulfur. We evaluated the optimum conditions for the thermal treatment of BaSO4/CaCO3 sludge to recover by-products. A high temperature tube furnace was used to reduce BaSO4/CaCO3 sludge obtained from a pilot plant test conducted at a gold mine shaft. We used response surface methodology to investigate the combined effects of relevant process variables (time, temperature, and the carbon/barium sulfate (C/BaSO4) molar ratio to maximize the reduction of BaSO4/CaCO3 sludge. At optimal process conditions (T = 1,028 °C; molar ratio of C/BaSO4 = 2.8 mol/mol), the tube furnace yield of BaS from waste sludge was over 78.5 % after 35 min. Furthermore, the results were similar to those generated by roasting a laboratory-grade mixture of barite and calcite concentrates. 相似文献
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Acid mine drainage (AMD) and fly ash from thermal power plants both pose substantial environmental problems in India. Fly ash from the Talcher super thermal power plant was converted into zeolite and used in a column to treat AMD from the abandoned Gorbi opencast mines (Singrauli coalfields, NCL). The pH of the mine water increased, and 100 % of the total hardness, Ca hardness, Mg hardness, Mn, Zn, Pb, Cd, Ni, and acidity were removed, along with 99 % of the Fe and 90 % of the Cu. 相似文献
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A peat-humic agent (PHA), derived by mechanical, chemical, and thermobaric treatment of peat from the Krugloe deposit (Novosibirsk region, Russia), is a good sorbent for potentially toxic elements, and can be used to neutralise acid mine drainage (AMD). A new AMD remediation method has been developed using this PHA with subsequent solid/liquid separation using haydite sand or activated carbon. 相似文献
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Arsenic Geochemistry of Acid Mine Drainage 总被引:1,自引:0,他引:1
Susanta Paikaray 《Mine Water and the Environment》2015,34(2):181-196