聚氧化乙烯絮凝微细粒高岭石强化赤铁矿反浮选脱硅机理研究

通过矿物浮选试验并结合激光粒度测试、扫描电镜(SEM)、矿物Zeta电位及XPS等检测方法对赤铁矿反浮选过程中聚氧化乙烯絮凝细粒高岭石的行为及机理进行了研究.矿物絮凝浮选试验表明：添加聚氧化乙烯可以提高高岭石的单矿物回收率和人工混合矿分离效率,促进赤铁矿和高岭石反浮选分离.激光粒度测试和扫描电镜检测结果表明：聚氧化乙烯不絮凝赤铁矿,但絮凝高岭石颗粒,使其表观粒径增大.Zeta电位测试和XPS分析表明：聚氧化乙烯在高岭石颗粒表面发生化学吸附,并使其Zeta电位正移.因此,开展聚氧化乙烯对硅酸盐矿物絮凝的研究对赤铁矿和高岭石反浮选分离具有意义.     

变性水玻璃对难选细粒氧化锑矿物浮选的影响

在pH≈7.5和有Mn~(2 )离子存在的情况下,通过浮选试验、ζ-电位测定、吸附试验,初步研究了变性水玻璃对细粒氧化锑矿物和脉石矿物硅化灰岩浮选行为的影响。研究表明,变性水玻璃对细粒氧化锑矿物与主要脉石矿物硅化灰岩的浮选分离具有明显的效果,有利于它们的浮选分离。     

铜铁灵浮选硫酸铅和菱锌矿研究

本文用铜铁灵为捕收剂浮选了硫酸铅、菱锌矿、方解石、石英单矿物和混合矿,得到了较好的结果。用测定ξ-电位、红外光谱等手段研究了铜铁灵浮选菱锌矿的作用机理。结果表明,铜铁灵与菱锌矿表面发生化学吸附。     

蛇纹石对硼镁石浮选的影响

针对蛇纹石易恶化硼镁石浮选环境的问题,通过浮选试验研究了不同粒度蛇纹石及矿物量配比对硼镁石浮选效果的影响.试验结果表明:浮选过程中蛇纹石与硼镁石颗粒间易发生相互作用,随着矿样中蛇纹石含量增加及蛇纹石粒度减小,硼镁石回收率逐渐下降,并且细粒级蛇纹石对硼镁石回收率影响更为明显,能显著降低硼镁石回收率.结合矿物zeta电位的测定及DLVO理论计算,对溶液中矿物颗粒间作用机理进行了分析,表明矿物表面电性差异是矿物颗粒间相互作用的根本原因.     

先进技术让中低品位铝土矿由“贫”变“富”

高品位铝土矿少、中低品位铝土矿多是制约我国铝工业健康持续发展的一大瓶颈。有没有一种"妙方"让中低品位铝土矿由"贫"变"富",从而被成功地利用起来呢?中国地质科学院矿产综合利用研究所在中低品位矿石利用选矿工艺技术研究项目过程中,以重庆市南川、武隆地区中低品位铝土矿为研究对象,通过进行多流程、多方案的筛选试验,采用选择性磨矿-粗细粒分级-正浮选工艺流程,实现了粗粒富集合体的预先回收。通过再磨后的分级工艺,使中、细粒目的矿物充分解离,利用正浮选工艺加强回收细粒级产     

钛铁矿的自载体浮选

本文研究了用40～80μm钛铁矿作载体,0～20μm钛铁矿的自载体浮选及其主要工艺参数。用扩展DLVO理论分析了自载体浮选的机理,主要结论如下: a.微细粒矿物粒度越细,越容易在载体上附着; b.自载体浮选的选择性取决于捕收剂吸附的选择性。钛铁矿/斜长石人工混合矿,经自载体浮选工艺一次选别,可获得TiO_247.17％的钛精矿,钛铁矿回收率为93.04％。     

颗粒表面电化学反应电荷传递模型及其浮选意义

分析了硫化矿物浮选分离体系中矿物颗粒表面反应电荷传递方式;对于不同的硫化矿物浮选体系,提出硫化矿物浮选过程中颗粒表面电化学反应电荷传递的3种模型:颗粒自身电荷传递模型;颗粒/液相介质电荷传递模型;颗粒/电极碰撞接触电荷传递模型.通过模型分析,讨论颗粒表面电化学反应电荷传递模型应用于不同硫化矿浮选工艺过程的浮选意义.研究结果表明:硫化矿物表面发生电化学反应时,反应电荷的传递与矿物性质、矿物表面特征、矿浆液相介质性质以及电位控制方式有关;所建立的模型对硫化矿物浮选电化学过程电位调控和复杂硫化矿物之间的浮选分离具有指导意义.     

酸化硅酸钠和硝酸铁对细粒石英的分散

本文以酸化硅酸钠和酸化硅酸钠加铁盐作为分散剂,对常见脉石矿物石英的微细颗粒在PH为10.5的碳酸钠溶液中的分散稳定性进行了试验研究,发现上述两种分散剂都比单独硅酸钠本身的分散作用强,浮选精矿的品位高;认为其作用机理是在实验条件下所形成的亲水性胶体对细粒石英的分散起了保护胶体的作用。细粒脉石矿物的稳定分散,有利于赤铁矿矿石阴离子捕收剂的浮选。     

旋流-静态微泡浮选柱浮选某难选钼矿的试验研究

针对某地高氧化率、微细粒不均匀嵌布、易泥化的难选钼矿石,提出粗细粒级分级分选新工艺,即原矿经破磨后将其中粒度小于0．020mm的微细粒级部分利用水力旋流器分离出来,采用高效、节能的微细粒分选设备旋流一静态微泡浮选柱进行分选,解决了该钼矿中微细粒级钼金属回收问题。以煤油为捕收剂,松醇油为起泡剂,水玻璃为分散剂和脉石矿物抑制剂,考察给料量、循环泵工作压力、药剂用量等因素对浮选指标的影响。分别采用一粗二精一扫和一粗二精2种工艺流程对平均钼含量为0．181％的原矿进行连选试验。研究结果表明：采用粗细粒级分级分选、细粒浮选柱回收的工艺流程可获得精矿品位为24．64％,回收率为54．33％的钼精矿,并简化了工艺流程。     

铝硅酸盐矿物浮选中捕收剂的设计合成及浮选机理的研究

铝土矿中脉石主要为高岭石、伊利石和叶蜡石等铝硅酸盐矿物,可以采用反浮选脱硅即通过选用合适的捕收剂将这些脉石矿物浮出.本文针对某铝土矿,结合Curis2软件中的高岭石晶体模型分析,从亲矿物基和非极性基两方面设计合成多胺类捕收剂DN12.通过浮选实验、浮选溶液化学计算、动电位测定和红外光谱测定研究该新型药剂对铝硅酸盐矿物的浮选作用及其机理.该捕收剂相对于常规捕收剂对铝硅酸盐矿物有更好的捕收效果,有效浮选pH区间为4～10.该捕收剂与铝硅酸盐矿物的作用以静电作用为主,同时也有氢键作用,从而增强了对矿物的捕收能力。     

Comprehensive recovery of gold and base-metal sulfide minerals from a low-grade refractory ore

The comprehensive recovery of small amounts of valuable minerals such as gold and base-metal sulfide minerals from a low-grade refractory ore was investigated. The following treatment strategy was applied to a sample of this ore: gold flotation–gold concentrate leaching–lead and zinc flotation from the gold concentrate leaching residue. Closed-circuit trials of gold flotation yielded a gold concentrate that assayed at 40.23 g·t-1 Au with a recovery of 86.25%. The gold concentrate leaching rate was 98.76%. Two variants of lead-zinc flotation from the residue—preferential flotation of lead and zinc and bulk flotation of lead and zinc—were tested using the middling processing method. Foam from the reflotation was returned to the lead rougher flotation or lead–zinc bulk flotation, whereas middlings from reflotation were discarded. Sulfur concentrate was a byproduct. The combined strategy of flotation, leaching, and flotation is recommended for the treatment of this kind of ore.     

硫化矿无捕收剂浮选

本文报道了不加巯基类捕收剂,在实验室和工业回路中实现了硫化铜矿石的浮选。按天然可浮性、自诱导浮选和硫诱导浮选,研究和讨论硫化矿无捕收剂浮选的不同机理,提出了无捕收剂浮选分离硫化矿混合矿的新设想。     

硫化铜矿石的无捕收剂浮选(英文)

在本研究中硫化铜矿石无捕收剂浮选取得了与加捕收剂浮选相同的选别指标,含铜1.88%的浸染铜矿无捕收剂浮选小型闭路试验,获得品位26.15%,回收率95.3%的铜精矿。研究结果表明,无捕收剂浮选中,黄铜矿的浮选速率比黄铁矿高,对铜-硫矿石的优先浮选有利;氧化还原电位较高的矿浆中容易实现硫化铜矿石的无捕收剂浮选;黄铜矿在酸性或碱性矿浆中的可浮性都比在自然pH状态下好;用石灰调浆能获得硫化铜矿浮选所需的pH值和稳定、适宜的氧化还原电位,对黄铁矿又有较好的抑制作用;加入硫化钠时,矿浆的氧化还原电位相应降低,但当充空气浮选时,随即上升为较高的氧化还原电位,适合于无捕收剂浮选,本研究不用硫化钠处理,也能实现硫化铜矿石无捕收剂浮选。     

表面活性剂溶液泡沫特性及其在磷矿浮选中的应用

本文讨论了磷矿浮选过程中表面活性剂溶液的泡沫特性。依据实际磷矿浮选结果求出表面活性剂溶液最佳泡沫特性区间。采用处最佳泡沫特性区间的表面活性剂作捕收剂时,其浮选效果显著,回收率高达92.4％。采用复合捕收剂取代传统药剂脂肪酸,可以改善磷矿浮选效果。     

Beneficiation of the gold bearing ore by gravity and flotation

Gold concentration usually consists of gravity separation, flotation, cyanidation, or the combination of these processes. The choice among these processes depends on the mineralogical characterization and gold content of the ore. Recently, the recovery of gold using gravity methods has gained attention because of low cost and environmentally friendly operations. In this study, gold pre-concentrates were produced by the stepwise gravity separation and flotation techniques. The Knelson concentrator and conventional flotation were employed for the recovery of gold. Gold bearing ore samples were taken from Gümüşhane Region, northern east part of Turkey. As a result of stepwise Knelson concentration experiments, a gold concentrate assaying around 620 g/t is produced with 41.4wt% recovery. On the other hand, a gold concentrate about 82 g/t is obtained with 89.9wt% recovery from a gold ore assaying 6 g/t Au by direct flotation.     

从尾矿中回收白钨矿的工艺试验研究

研究采用再磨——浮选工艺对南方某老尾库尾矿（含WO3 0.19%）中的钨进行回收.在高碱浮选介质中,添加浮选药剂,通过一次粗选、二次扫选和三次精选流程,获得钨粗精矿含WO3 3.26%,回收率为70.48%.红外光谱测定结果表明,733对白钨矿的捕收作用以表面化学吸附和键合为主.     

Semi-industrial experimental study on bauxite separation using a cell–column integration process

The cyclonic-static micro-bubble flotation column (FCSMC) is a highly efficient mineral processing equipment. In this study, a cell-column (FCSMC) integration process was investigated for the separation of bauxite and its feasibility was analyzed on a theoretical basis. The properties of low-grade bauxite ore from Henan Province, China were analyzed. Parameters such as reagent dosage, scraping bubble time, and pressure of the circulating pump during the sorting process were investigated and optimized to improve the flotation efficiency. On the basis of these parameters, continuous separation experiments were conducted. Bauxite concentrate with an aluminum-to-silicon (A/S) mass ratio of 6.37 and a 77.63wt% recovery rate were achieved via a flow sheet consisting of “fast flotation using a flotation cell, one roughing flotation and one cleaning flotation using flotation columns”. Compared with the full-flotation-cells process, the cell–column integration process resulted in an increase of the A/S ratio by 0.41 and the recovery rate by 17.58wt%. Cell–column integration separation technology represents a new approach for the separation of middle-to-low-grade bauxite ore.     

Aerosol flotation of low-grade refractory molybdenum ores

The characteristics of aerosol flotation, which include the effect of the concentration and particle size of kerosene aerosol on the molybdenum (Mo) flotation index and the effect of kerosene aerosol dosing method on the kerosene dosage and flotation time, were studied in the flotation of low-grade refractory molybdenum ores using kerosene aerosol. The results revealed that the particle size and concentration of kerosene aerosol had little effect on the Mo grade but had significant effect on the Mo recovery. A smaller particle size and a lower concentration of kerosene aerosol were beneficial to the Mo aerosol flotation. For the received Mo ore samples, the optimized particle size of kerosene aerosol was 0.3-2 μm and the optimized aerosol concentration was 14 mg/L. The compressed air atomizer had a more uniform distribution of aerosol particles than the ultrasonic atomizer, and the aerosol concentration was controlled easily, so the compressed air atomizer was more suitable for the research of aerosol flotation. Compared with conventional flotation in which kerosene was directly added into the ore pulp, the flotation time was reduced by ~30%, and the dosage was decreased by ~20% in aerosol flotation, while the Mo flotation index was similar.     

铜钼浮选分离中硫化钠的消耗机理

针对铜钼浮选分离生产过程中,往往存在着硫化钠抑制剂消耗量过大、生产成本过高的现象,使用硫离子选择电极动态监测不同条件下硫化钠溶液中硫离子电位,来初步研究硫化钠大量消耗的机理.结果表明:铜钼浮选分离过程中,空气的鼓入和矿浆的未加温处理会增加硫化钠的氧化消耗,是硫化钠消耗量大的原因之一.浮选矿浆中的矿物(如辉钼矿、黄铜矿和黄铁矿)有着催化硫化钠氧化分解的作用,加上矿物本身对硫化钠的吸附作用,是造成铜钼浮选分离过程中硫化钠大量消耗的又一原因.此外,矿浆中溶出的少量金属阳离子(如Cu²⁺和Fe³⁺)对硫化钠的氧化分解也有一定作用,进一步加剧了硫化钠的消耗.