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对广西盘龙铅锌矿铅锌尾矿开展600t/d规模的浮选回收重晶石工业试验研究,分析了现场铅锌尾矿性质,并在已有流程基础上配置了铅锌尾矿脱泥—脱硫浮选—重晶石浮选的工艺流程。工业试验在原矿含BaSO_4 18.47%的条件下,经优化后工艺流程获得了含BaSO_4 96.70%、BaSO_4回收率62.77%的重晶石精矿,实现了盘龙铅锌矿尾矿资源的综合利用。 相似文献
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尾矿是选矿中分选作业过程中的产物,由于其内部的有用目标组分含量较低,回收利用效果较差,经常被随意丢掉。铅锌尾矿中含有一定量的铜、锌、银、铅等有价成分,通过采用先进的湿法回收方法,能够保证铅锌尾矿中的铜、锌、银、铅等有价成分得到更好的回收利用,提升铅锌尾矿的回收利用率。铅锌尾矿的应用范围比较广泛,能够作为良好的装饰装修材料。现阶段,我国矿产资源储量逐年减少,为了保证铅锌尾矿得到更好的回收与利用,采用先进的回收利用工艺至关重要。从选矿厂角度来讲,要尽量将尾矿进行减量干堆处理,进一步提升铅锌尾矿有价成分的回收与利用。 相似文献
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针对云南某铅锌选矿厂产出的硫精矿中铅锌品位高、铅精矿中铅品位低的问题,考查了目的矿物的解离情况,通过铅硫混合粗精矿再磨提高了目的矿物的单体解离度,优化了工艺流程。试验结果表明:在磨矿细度为-325目质量分数占70%时,采用铅硫混合粗精矿再磨、脱锌扫选尾矿返至锌作业的工艺流程,可得到铅品位为61.23%、铅回收率为85.68%的铅精矿,锌品位为49.65%、锌回收率为93.38%的锌精矿;与不再磨流程相比,铅精矿中铅的品位提高了2.05个百分点,回收率提高了1.75个百分点,锌精矿中锌的回收率提高了2.28个百分点,同时铅精矿中锌品位及硫精矿中铅、锌品位均有所降低。 相似文献
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云南高泥尾矿铅锌分离实验研究 总被引:1,自引:0,他引:1
针对云南高泥尾矿铅锌嵌布粒度细、泥化严重、性质相对复杂的技术难点,进行了铅锌分离实验研究,采用泥砂分级别浮选-重选联合工艺流程,有效分离了铅锌,实现了该复杂尾矿资源的综合回收利用。结果表明,该矿中铅含量为4.29wt%,锌含量为4.99wt%,铅主要以白铅矿和铅铁矾的形式存在,铅和铁相互交代形成不同的包裹形式,分离难度极大;锌主要以氧化锌的形式存在,氧化程度较深,锌氧化率达99%,且主要为难选的异极矿。最终通过闭路选矿流程,获得铅品位33.87%,回收率62.53%的铅精矿;铅精矿中银品位142.50 g/t,银回收率30.92%;获得锌品位15.21%、回收率47.82%的锌精矿。 相似文献
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在相同的熟料设计率值、相同的烧成制度下,对不掺加和掺加铅锌尾矿的生料分别进行了生料易烧性的对比实验。研究结果表明:铅锌尾矿可以部分替代铁矿石进行配料生产硅酸盐水泥熟料并起到矿化作用,能够显著改善生料易烧性。 相似文献
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云南某煤系硫铁矿煤硫综合回收工艺研究 总被引:1,自引:0,他引:1
为了有效利用云南某地煤系硫铁矿,采取选煤与选硫铁矿的综合回收方案.在矿石化学多元素分析以及硫形态分析的基础上,进行了螺旋溜槽—摇床重选试验、浮选试验.试验最终采用浮选闭路试验流程,先浮选煤,单独浮选出中矿(该产品并入尾矿),再浮选硫铁矿,最后得到了产率5.38%,碳品位40.32%,含硫7.05%,碳回收率33.76%的煤精矿;产率24.00%,硫品位47.59%,含碳9.64%,硫回收率72.74%的硫精矿,实现了煤和硫铁矿综合回收的目的. 相似文献
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Jonathan Tenrio Vinhal Raquel Húngaro Costa Jorge Luís Coleti Denise C. R. Espinosa 《加拿大化工杂志》2021,99(1):166-177
The volume of tailings produced by the extractive industry has been increasing due to the processing of the low‐grade ore. This issue can cause environmental accidents and require significant investment to control the disposal of tailings. Therefore, this study aims to recover iron from zinc mine tailings by wet magnetic separation followed by the carbothermal reduction of self‐reducing briquettes. Two magnetic separation routes were investigated to concentrate iron. Zinc mine tailings were processed by route I, in a rougher stage followed by a scavenger stage; and route II, in a rougher stage followed by a cleaner stage. The carbothermal reductions were performed using self‐reducing briquettes composed of Fe concentrate from the route with high Fe content and charcoal. The products were analyzed by scanning electron microscopy with energy dispersive spectroscopy (SEM‐EDS), x‐ray diffraction (XRD), inductively coupled plasma optical emission spectrometry (ICP‐OES), and volumetric chemical analysis. Magnetic separation route II provided the highest‐grade Fe concentrate, 52% Fe, while route I provided 33% Fe. In the carbothermal reductions, a metallization degree of 98% in the Fe concentrate briquette, 97% in the briquette with a 10% replacement of its raw material by Fe concentrate, and 99% in the hematite briquette was reached. The replacement of raw material by Fe concentrate showed no significant change in Fe recovery. Considering the whole process, magnetic separation and carbothermal reduction, the recovery of Fe from the zinc mine tailings was 67%. Therefore, the process route suggested in this study will not only reduce tailings disposal and consequently the risk of environmental accidents, but it will also provide profitable raw material for the steel industry. 相似文献
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The kinetics of heavy mineral and bitumen recovery from oilsand tailings are presented. The results show that the recovery rates for titanium, zirconium and bitumen were affected by addition of surfactants Tretolite F46 and E3453. Recoveries were a function of time and of the minerals and bitumen present. 相似文献
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云南某富银锌精矿中银主要以类质同象形式存在于白铅矿中,本工作以该矿样为研究对象,根据其性质,采用抑铅浮锌的工艺流程进行浮选,考察了磨矿细度、抑制剂、活化剂及捕收剂等因素对浮选分离指标的影响。结果表明,–19+10 μm粒级中银含量最高。在磨矿细度–74 μm占90%,硅酸钠用量为2000 g/t,硫酸铜用量为200 g/t,丁基黄药用量为300 g/t,松醇油用量为30 g/t的条件下,1次粗选、1次精选、1次扫选,中矿顺序返回的全流程闭路实验,可获得含锌61.08%,回收率95.89%的锌精矿和含银1548.32 g/t,回收率为71.17%的银精矿,实现了锌银的浮选分离及伴生银的高效富集。 相似文献
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云南海口磷矿浮选尾矿的工艺特性研究 总被引:1,自引:0,他引:1
对云南海口磷矿浮选尾矿的物相和化学组成、反应特性及发泡性能进行了研究.结果表明:海口浮选尾矿的主要物相为CaMg(CO3)2、Ca3(PO4)3F、SiO2,镁的质量分数为11.59%.P2O3的质量分数为9.87%;浮选尾矿的反应活性很好,抗阻缓性较差,发泡比较严重,需要加入消泡剂. 相似文献