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国内某厂采用湿法炼锌,其原料中含有锗,在酸性浸出过程中锗元素随之被浸出,锗元素含量超标会造成硫酸锌电解过程烧板,严重影响锌电解过程正常运行。阐述了活性炭吸附硫酸锌浸出液、净化液中锗的部分条件试验,研究了活性炭吸附温度和酸性浸出液在不同锗浓度条件下对吸附效果的影响,目的在于利用物理方法提高焙砂浸出过程中锗的脱除率和降低净化过程中锌粉的单耗。 相似文献
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我国锌资源储量丰富,含锌矿物中很大一部分以高铁闪锌矿的形式存在,并且其中含有丰富的铟资源。为了综合回收高铁闪锌矿湿法炼锌过程富集于中浸渣中的有价金属,开展了中浸渣和锌精矿的还原酸浸试验研究,其主要目的是利用硫酸浸出中性浸出渣中以铁酸盐形式残留的锌和铟,同时利用锌精矿将溶液中的三价铁还原为二价铁,实现锌精矿中锌、铟的同步浸出。研究了锌中浸渣和锌精矿的投料质量比、浸出剂浓度、液固比、反应温度、浸出时间对锌、铟浸出行为的影响。研究表明在初始硫酸浓度220 g/L,中浸渣与锌精矿质量比1∶0.25,粒度-74μm,液固比6,温度90℃,反应时间3 h的条件下,锌、铟的浸出率在96%以上,浸出液中95%以上的铁被还原为二价铁离子,实现了浸出与还原的同步进行。 相似文献
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针对传统湿法炼锌过程铜回收工艺长、铜回收率低的难题,采用M5640直接从湿法炼锌还原浸出液中萃取分离回收铜,缩短铜回收流程,提高铜回收率。研究了混合时间、溶液pH值、萃取剂浓度、萃取级数等因素对铜萃取率的影响,以及反萃时间、相比等因素对载铜有机相中铜反萃率的影响。结果表明M5640对硫酸锌溶液中的铜离子具有很好的选择性萃取性能,在M5640浓度为15%、溶液pH值为2.0、相比(O/A)为1∶2、萃取时间为5 min的条件下,经过4级逆流萃取,铜萃取率为95.2%,锌萃取率仅为0.5%,铜锌分离系数为4 080。有机相经洗涤后,锌、铁等杂质离子被脱除,载铜有机相采用模拟铜电积废液反萃,经过2级逆流反萃,铜反萃率为97.1%。采用萃取-洗涤-反萃技术从湿法炼锌浸出液中回收铜,铜的总回收率为92.4%。 相似文献
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本文介绍了铁酸锌的软磁特性、吸波特性、催化性能等性质及其在磁性材料、隐形材料、太阳能转换材料、气敏材料等方面的用途,以及在锌冶金等过程中铁酸锌的形成及其危害;简述了工业上处理铁酸锌的典型火法工艺回转窑挥发法、常用湿法工艺热酸浸出法及其他方法如烟化法、Ausmelt法、碳酸盐焙烧法、硫化焙烧法、高压浸出法、微波碱浸法、多段浸出法、盐浸法、多酸浸出法以及碱浸法等,指出其处理锌冶金中铁酸锌的实质均是破坏铁酸锌的晶体结构,使铁酸锌分解转化为其他物质,通过冶金、化学或物理方法回收锌铁,这些方法存在着能源和材料消耗大、工艺流程复杂、残渣处理难度大、生产成本高、环境污染等问题。同时,结合铁酸锌的特殊性质,对锌冶金副产铁酸锌的高效利用进行展望,提出了在不破坏铁酸锌的晶体结构前提下,将铁酸锌从锌冶金过程中作为产品独立分离出来的新思路。 相似文献
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针对氧化锌尾矿和废弃水渣等工业固废中有价锌难以回收的问题,以当地工业含锌固废为原料,利用碳热还原氧化法,制备了高纯氧化锌微粉。通过HSC Chemistry进行热力学计算和试验研究结合的方式,分析了含锌废渣中硅酸锌与碳还原反应的热力学过程。讨论了配碳量、焙烧温度、焙烧时间以及CaF2对硅酸锌还原过程锌产率的影响。结果表明,在以CaF2为催化剂时,1 000~1 100℃催化效果最显著。得出最佳工艺条件:在温度为1 100℃、保温时间40 min、碳含量20 wt%、CaF2添加5 wt%的条件下锌产率(氧化锌回收率)为97.44%。对挥发产物进行结构和成分分析,其物相为六方纤锌矿结构的氧化锌晶体,粒度大小2~4μm,纯度达到了99.47%。 相似文献
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《Minerals Engineering》2000,13(13):1417-1421
Zinc ferrites are one of the major forms of zinc in some wastes, such as steel mill EAF dusts and the leaching residues of roasted zinc sulfide concentrates. These ferrites can be very difficult to chemically decompose so that the zinc can be recovered. This decomposition is the key to the recovery of zinc in these solid wastes. In this work, the recovery of zinc from synthetic zinc ferrite was investigated. It was found that around 75–80% of the zinc in zinc ferrite can be extracted after being fused directly with NaOH pellets and dissolved in an alkaline leaching solution. The recovery increased to over 90% when the ferrite was hydrolyzed with water or dilute NaOH solution prior to the fusion step. 相似文献
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A novel method to recover zinc and iron from zinc leaching residue (ZLR) by the combination of reduction roasting, acid leaching and magnetic separation was proposed. Zinc ferrite in the ZLR was selectively transformed to ZnO and Fe3O4 under CO, CO2 and Ar atmosphere. Subsequently, acid leaching was carried out to dissolve zinc from reduced ZLR while iron was left in the residue and recovered by magnetic separation. The mineralogical changes of ZLR during the processes were characterized by XRF, TG, XRD, SEM–EDS and VSM. The effects of roasting and leaching conditions were investigated with the optimum conditions obtained as follows: roasted at 750 °C for 90 min with 8% CO and CO/CO + CO2 ratio at 30%; leached at 35 °C for 60 min with 90 g/l sulfuric acid and liquid to solid ratio at 10:1. The iron was recovered by magnetic separation with magnetic intensity at 1160 G for 20 min. Under the optimum operation, 61.38% of zinc was recovered and 80.9% of iron recovery was achieved. This novel method not only realized the simultaneous recovery of zinc and iron but also solved the environmental problem caused by the storage of massive ZLR. 相似文献
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