共查询到20条相似文献,搜索用时 62 毫秒
1.
2.
3.
分析含铁氰化提金尾液的来源、特点及其危害,重点对具有离子交换法吸附、解吸含铁氰化提金尾液的原理、存在问题进行了深入分析研究,结果表明,采用化学沉淀法或电吸附处理技术对含铁氰化提金尾液进行预处理是解决离子交换法处理此类废水瓶颈的最佳途径。 相似文献
4.
5.
研究了201×7树脂吸附回收提金尾液中氰化物及金属铜的技术。通过对树脂的饱和吸附量、吸附速率及吸附等温线的研究,得到了201×7树脂对氰化物的饱和吸附量为44.39mg/ml湿树脂,铜的饱和吸附量为24.56mg/ml湿树脂;氰化物的吸附速率常数为k=9.30×10-4s-1,铜的吸附速率常数为k=1.39×10-3s-1;该树脂对氰化物及铜离子的吸附符合Freundlish方程;使用高浓度的NaCl溶液可以解吸树脂上负载的氰化物及金属铜,解吸率分别为85%和72%。 相似文献
6.
从氰化矿浆中回收氰化物的工艺 总被引:4,自引:2,他引:2
随着黄金科学技术的发展,采用氰化炭浆(浸)法、锌丝(粉)置换法及堆浸法生产黄金的矿山越来越多,由于氰化法提金排放的有害物质较多,污染危害极大,引起人们的关注。尽管处理方法较多(碱氯法,酸化法、二氧化硫法、电化学法、自然净化法等),对污水进行了处理,但多数地区仍超过规定的排放标准,而且处理费用较高,增加了生产成本,目前已成为人们十分关心的问题。寻求方法简单、成本低、效果好又实用的污水处理方法是当前急待研究的新课题。 本文着重介绍从氰化矿浆回路中回收氰化物的新工艺、新方法,具有明显的经济效果和社会效益。 相似文献
7.
8.
9.
研究了从氰化尾液中回收铜的工艺过程,主要涉及铜在吸附解吸过程发生的物理化学变化。分析了铜在溶液中的存在状态和在树脂上的吸附状态以及树脂在解吸过程中颜色的变化所伴随的相关反应,根据这些变化确定了铜的解吸剂。结果表明,铜的状态变化和解吸剂的选择密切相关,根据铜的物理化学变化能够选出有效的解吸剂。 相似文献
10.
11.
采用沉淀法新工艺,可充分地脱除氰化电积贫液中铜,铁,锌等杂质离子,还有效地回收金和部分游离氰根,经处理后的贫液可返回使用,实现闭路循环。本文对沉淀过程及电积贫液净化前后过提金过程影响的机理进行了系统分析。最后指出,该工艺可望用于净化其提金过程产生的氰化贫液。 相似文献
12.
13.
14.
15.
Feng Xie David Dreisinger Fiona Doyle 《Mineral Processing and Extractive Metallurgy Review》2013,34(6):387-411
The mainstream technology for leaching gold from gold ore is still leaching in aqueous alkaline cyanide solution. However, when copper minerals are present in the gold ore, high levels of free cyanide must be maintained during leaching because many common copper minerals react with cyanide, forming copper cyanide complexes that deplete the solution of free cyanide. This results in a significant economical penalty through excessive cyanide consumption and loss of valuable copper in tails. Environmental constraints controlling the discharge of cyanide from mining industry are being tightened by local governments worldwide. The solution chemistry of copper in cyanide solution and various technologies for the recovery of copper and cyanide from barren gold cyanide solutions were reviewed in the paper. Direct recovery methods are mainly based on the acidification–volatilization–reneutralization (AVR) process or its modifications. These processes are not very efficient for treating low cyanide solutions and high metal cyanide solutions due to their substantial operational cost. Indirect recovery technologies by activated carbon, ion-exchange resins (IX) and solvent extraction (SX) have been extensively studied. The basic principle of these technologies is to pre-concentrate copper (and part of cyanide) into a small volume of eluant or stripping solution. The copper and cyanide in the resulted solutions can be further recovered by AVR or similar processes or by the electrowinning process. Activated carbon is only suitable for use as a polishing process to remove cyanide to lower levels from those cyanide solutions where the cyanide content is already low. Compared to activated carbon, ion exchange resins are less easily poisoned by organic matter and can usually be eluted at room temperature, and selectivity for particular metals can be achieved by the choice of the functional group incorporated into the bead or by the selective elution process. Solvent extraction process developed base on guanidine and modified quaternary amines exhibit relative fast extraction kinetics and can be operated in a continuous manner. It will be necessary to thicken and wash the solids in order to produce a clarified feed solution while treating the slurry from operations using carbon-in-pulp (CIP) for the recovery of gold. Other copper and cyanide recovery technologies such as biosorption or direct electrowinning were also proposed, but they have still not found their way to practical application. 相似文献
16.
17.
针对某含铜金矿石进行了氨氰法浸金及浸出贵液脱铜试验研究。其结果表明:在一定条件下,可获得较好的技术指标,浸渣金品位0.38 g/t,浸出贵液金、铜平均质量浓度分别为2.27 mg/L、61.94 mg/L,渣计金浸出率为89.44%;采用双氧水除铜,铜沉淀率为85.85%,氧化沉淀渣铜品位超过50%,可以铜精矿出售。 相似文献
18.
19.
20.
云南某矿氰化尾矿中含有金铜铅铁等有价元素。为了充分利用矿产资源,对该氰化尾矿进行了选矿综合回收试验研究。试验结果表明:通过提高磨矿细度和延长浸出时间,氰化尾矿金品位由0.83 g/t可以降至0.35 g/t;采用异戊基黄药和环烷酸皂混合捕收剂选铅,可得到品位和回收率分别为46.83%和35.15%的铅精矿;采用CL-5消除矿浆中游离氰以及铅浮选残留药剂对铜浮选的影响,活化剂AS-2和Na2S活化铜,混合黄药T820、F-1黑药和C5-9羟肟酸作混合捕收剂选铜,可得到品位和回收率分别为17.72%和53.33%的铜精矿;磁选回收铁矿物,先弱磁后强磁,可以得到品位64%和51%两种铁精矿。 相似文献