共查询到19条相似文献，搜索用时 203 毫秒
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通过对金矿石化学及矿物组成、自然金形态、嵌布粒度、嵌布方式等深入研究,查明了该矿石性质。利用浮选法和氰化法进行可选性试验研究,浮选试验精矿品位为46.86 g/t,回收率达85.14%,氰化试验最高浸出率96.38%。综合分析认为,采用浮选法选矿较合理。 相似文献
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江山铅锌金矿选矿试验研究 总被引：1，自引：0，他引：1
针对江山铅锌金矿品位低,矿物组成复杂的特点,采用"铅-锌-硫优先浮选,硫(金)精矿氧化焙烧预处理-焙砂氰化浸金"的工艺,金在铅(金)精矿、锌精矿、硫(金)精矿中的总回收率为81.25%。可使硫(金)精矿中96.89%的硫以二氧化硫的形式得到回收,对原矿的回收率为73.25%;金的作业浸出率达84.76%,对原矿的回收率为31.91%;浸渣中的铁品位达57.99%,对原矿的回收率为26.71%。通过试验研究与分析,确定适宜的选矿工艺及药剂制度,为今后合理开发该区矿石提供技术依据。 相似文献
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对青海省五龙沟含碳,砷,硫,锑微细粒难选冶金矿石的浮选金精矿进行二段焙烧－焙砂氰化浸出提金的试验研究,获得了金浸出率８９．９０％的较好指标,为该矿山浮选金精矿的提金提供了一种可选择的工艺流程。 相似文献
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针对福建某低品位钼矿矿石性质,确定了粗磨粗选、粗精矿再磨精选的浮选方案。采用该浮选方案及合理的选别条件,对含钼为0.08%的钼原矿选别,获得钼精矿品位52.45%、钼精矿产率为0.14%、钼回收率90.19%的良好指标。 相似文献
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细粒嵌布型铜锌硫化矿采用粗磨后混合浮选工艺,具有回收率高和成本低的优势,但对所产出的混合精矿,亟需解决铜、锌、硫之间的高效彻底分离。云南玉溪地区铜锌硫混合粗精矿,其细度为-74μm 75%,含Cu 2.45%、Zn 4.93%、S 31.21%,笔者采用粗精矿再磨-铜、锌、硫选择性浮选分离工艺,研究了再磨细度、药剂种类、用量等因素对各矿物分离效果的影响。当粗精矿再磨细度为-38μm90%时,闭路试验获得品位和回收率均较高的铜、锌和硫精矿产品,铜精矿含Cu 21.00%,Cu回收率84.27%,锌精矿含Zn 48.37%,Zn回收率85.94%,硫精矿含S37.90%,S回收率82.85%,混合精矿中的铜矿物、锌矿物、硫矿物均实现了较彻底的分离。本研究为铜多金属混合精矿的有效分离提供了一种可资借鉴的方法。 相似文献
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采用生物氧化技术和化学方法,利用堆浸工艺分步提取,对含Au 140~150 g/t、Ag 900~1 000 g/t、B i 9.0%~10.0%、Cu14%~17%的多金属浮选金精矿的综合回收工艺进行了研究。经小型搅拌试验,确定了生物氧化浸铜—氰化浸金、NaC l-FeC l3-HC l体系(氯盐法)浸出铋和银的技术方法。通过柱浸试验,研究了利用该方法分步浸取Au、Ag、Cu和B i在堆浸工艺中的可行性。在10 t精矿的扩大试验验中,验证了柱浸试验所取得的工艺指标和参数。试验中掺入骨架材料,解决了精矿在堆浸中的渗透问题;生物氧化过程中,菌种在含高浓度铜离子浸出液中反复驯化,对铜的耐受力提高到30 g/L;在NaC l-FeC l3-HC l体系浸出B i和Ag时,用H2O2将浸出液中的Fe2+氧化成Fe3+,使浸出液能循环使用,且B i和Ag同时浸出。Au、Ag、Cu和B i的最终浸出率分别为92.98%、65.09%、45.33%和53.49%。 相似文献
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Gold recovery from a refractory pyrrhotite ore by biooxidation 总被引：1，自引：0，他引：1
S. Ubaldini F. Vegli F. Beolchini L. Toro C. Abbruzzese 《International Journal of Mineral Processing》2000,60(3-4)
The aim of the present investigation was to study the biooxidation of a refractory gold-bearing pyrrhotite, in order to increase the gold recovery during the subsequent conventional cyanidation.Bacterial cultures utilised in the biological test consisted predominantly of Thiobacillus genus. Tests were conducted at laboratory scale. The gold content of the ore sample, coming from Bolivia, was of 10 g t−1 Au.After 24 h leaching time by direct cyanidation, low gold recovery was obtained (<20% Au), with a high reagent consumption. On the other hand, a high gold recovery was achieved for the biooxidated samples: after 24 h cyanidation gold dissolution reached about 91% Au.Experimental results have shown the technical feasibility of the biooxidative pretreatment prior to conventional leaching and a complete circuit of treatment, on laboratory scale, has been developed considering also the subsequent gold recovery by carbon adsorption/desorption and electrowinning.A gold extraction yield of about 86% was determined in the whole process for gold extraction from pyrrhotite (biooxidation, solid–liquid separation, cyanidation, adsorption, desorption, electrowinning). 相似文献
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贵州省兴义市雄武地区金矿主要为卡林型,其次为红土型,矿床受断裂构造控制,矿石为中等含硫微细浸染状氧化矿石。目前浅部矿石已基本采完,深部矿石品位较低(0.8~1.8 g/t),因此有效提高低品位矿石浸出率和金回收率至关重要。研究表明,筑堆时矿石粒度和喷淋时氰化钠浓度是堆浸生产中的重要影响因素。矿石粒度大,金浸出率低;氰化钠浓度大,则成本增加。根据矿石物质成分和工艺特征研究,得到矿石冶炼时的最佳工艺条件:筑堆时矿石粒度为15~25 mm,氰化钠浓度为0.05%~0.08%。该研究有效提高了矿石浸出率,降低了运营成本,为金矿石堆浸实际生产提供了理论和实验依据。 相似文献
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本文介绍了堆浸提金原理和在实验室进行金矿石堆浸可行性研究的方法.以我国辽宁猫岭金矿、四川茶铺子金矿和福建紫金山金矿为研究对象,研究了矿石粒度、氰化钠溶液浓度、浸出时间等因素对金浸出率的影响,从而确定堆浸提金最佳工艺条件.通过对上述三类矿石性质及堆浸性能的比较,认为矿石的物质组成和金的嵌布特性对金的浸出率影响较大. 相似文献
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An oxide gold ore was subjected to chloride/hypochlorite leaching at room temperature. The effects of three factors, including Ca(OCl)2 vs. NaOCl, OCl− concentration, and HCl concentration on gold leaching performance were investigated. Due to formation of CaOCl+ complex in solution and hence less reactivity, calcium hypochlorite produces a sluggish gold leaching kinetics, taking twice the time (46 h) to achieve maximum gold recovery of 58% compared to sodium hypochlorite. 10 g/L of total initial hypochlorite species in solution produces reasonable gold recoveries. The amount of added HCl and hence the initial pH was found to have a major effect on gold leaching kinetics and maximum gold recovery. A high level of 9 g/L of added HCl causes HClO to be very reactive, producing very fast kinetics, reaching 67% gold extraction in 4 h. It also causes a faster consumption of hypochlorous acid, through catalytic decomposition (by NiO and CuO) and disproportionation. Hypochlorous acid reactions with sulfide and ferrous content of ore proceed very slowly in the pH range of 4–11. Gold–chloro complexes are strongly adsorbed on quartz component of ore. To minimize this undesirable adsorption of gold–chloro species, the aging time must be limited to a few hours only. 相似文献
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《International Journal of Mineral Processing》2005,76(4):260-265
The intensification of the thiosulphate leaching of silver from a silver-bearing complex sulphide concentrate (Casapalca deposit) using mechanochemical alkaline leaching as the pretreatment step was investigated. The leaching of “as-received” concentrate with the thiosulphate solution afforded only 6% recovery of Ag into leach. The mechanochemical pretreatment resulted 85% amorphization of tetrahedrite as a silver-bearing mineral in the concentrate as well as an increase in specific surface area from the original value of 0.26 m2 g−1 to a maximum value of 15.7 m2 g−1. The pretreatment was performed in a stirred ball mill using variable milling times and sample weights. The physico-chemical changes in the concentrate as a consequence of mechanochemical pretreatment had a pronounced influence on the subsequent silver extraction. The optimum results from mechanochemical pretreatment and subsequent leaching of the concentrate with ammonium thiosulphate were achieved by using a milling time of 60 min and a weight of sample of 60 g. In this case, 99% recovery of Ag was achieved after only 3 min of leaching. 相似文献
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微细粒低品位锰矿由于颗粒间的非选择性聚集、浮选药剂用量大、浮选效率低等技术难题而致使其利用困难,造成大量浪费。在品位低于13%的锰矿浮选技术研究中,捕收剂最受关注,前人已研究了多种类型的捕收剂,所得精矿品位在16.9%~18.3%之间,回收率为56%~97%,回收率比较理想,但精矿品位总体不高。本文将新型捕收剂RA-92应用于湖南凤凰-花垣地区低品位碳酸锰矿(锰品位为10.7%)的选矿工艺中,实验研究了磨矿细度、pH值、抑制剂和捕收剂用量对浮选效果的影响,在最佳工艺条件下,精矿品位由原矿的10.7%提升至17.4%,回收率达到80.2%。研究表明RA-92对碳酸锰矿具有良好的捕收性能,浮选工艺相对简单且捕收剂用量少,浮选成本较低,可为此种捕获剂在微细粒低品位碳酸盐锰矿选矿中的应用得到推广。 相似文献
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《矿物学报》2013,(Z1)
Heap leaching is a promising, less costly, alternative technology for processing low grade gold ores compared with traditional, energy intensive processes (e.g. autoclave/tank leaching). This research investigated the effectiveness of lime for enhancing gold leaching rates of gold ores from ajialongwa gold mine in china. Column and heaping experiments were performed using cyanide leaching solutions at pH=10, with and without lime (CaO). The presence of lime greatly increased gold leaching rates. Column leaching experiments showed without the addition of lime, there was 35.2% of gold leached. The addition of lime resulted in the release of 50.56% gold. Lime assisted cyanide of refractory gold was proved by heap leaching experiments. 相似文献