Self-terminated electrodeposition of platinum on titanium nitride for methanol oxidation reaction in acidic electrolyte

The development of high-performance electrocatalysts for methanol oxidation is an urgent task to enhance the efficiency of direct methanol fuel cells. We report a simple and controllable method to fabricate Pt-decorated TiN electrocatalysts using self-terminated electrodeposition at room temperature and ambient pressure. Under optimized deposition parameters such as electrolyte pH, TiN substrate pretreatment, and pulsed deposition potential, quenching of the Pt electrodeposition facilitates obtaining an extremely low Pt mass loading (0.93 μg/cm²) on the TiN substrate. Repeated deposition potential pulses enable a gradual increase in Pt loading, with a precise control of the loaded Pt mass. Maximum intrinsic and mass activities for the methanol oxidation reaction are achieved for the catalyst with a Pt loading mass of 55.0 μg/cm², prepared by 20 deposition pulses. The maximum intrinsic activity achieved with the Pt-decorated TiN electrocatalyst is five times higher than that obtained with bulk Pt. The present results thus provide a facile method for the fabrication of cost-effective electrocatalysts.     

Flotation performance and adsorption mechanism of novel 1-(2-hydroxyphenyl)hex-2-en-1-one oxime flotation collector to malachite

A novel collector 1-(2-hydroxyphenyl)hex-2-en-1-one oxime (HPHO) was synthesized from 2-hydroxy acetophenone and butyraldehyde. Its flotation performance and adsorption mechanism to malachite were investigated by flotation test, zeta potential, Fourier transform infrared (FTIR) and X-ray photoelectron spectroscopy (XPS) analysis techniques. Compared with benzohydroxamic acid (BA), 1-(2-hydroxyphenyl)ethan-1-one oxime (HPEO) and sodium isobutyl xanthate (SIBX), HPHO exhibited excellent collecting power to malachite without additional reagents, such as Na₂S regulator and methyl isobutyl carbinol (MIBC) frother. Results of zeta potential indicated that HPHO was coated on malachite surfaces through a chemisorption process. FTIR and XPS data gave clear evidence for the formation of Cu–oxime complex on malachite surfaces after HPHO adsorption through the linkage between C=C, –OH, N–OH group and Cu species.     

甘肃某铁矿选矿工艺的研究

甘肃某铁矿为赤铁矿矿床，为了提高铁精矿品位及回收率，在细磨的条件下，采用高梯度磁选处理该矿石．当给矿铁品位50．82％，磨矿细度94．01％-0．043mm时，经一粗、一扫、一精、中矿集中再选的工艺流程选别，最终获得铁精矿品位62．03％、回收率68．78％的选别指标．     

新型捕收剂R31浮选低品位白钨矿的研究

用R31为捕收剂、Na2CO3为调整剂、Na2SiO3为抑制剂进行白钨粗选,白钨精选采用Na2SiO3加温浮选的工艺,在原矿含WO30.28%的小型试验中,获得白钨精矿品位73.10%,回收率81.67%,试验表明,R31是白钨矿较为合适的捕收剂。     

烧结时间对含铅玻璃制备微晶玻璃析晶及性能的影响

以铅玻璃与粉煤灰为原料，通过协同熔炼制备了微晶玻璃。通过XRD和SEM等手段研究了不同烧结时间下微晶玻璃的物相组成及显微结构，测定了微晶玻璃的密度、吸水率、维氏硬度和化学抗性。结果表明: 延长烧结时间对含铅玻璃加入量为40%(FG40)、50%(FG50)样品的晶相类型和晶化程度有影响，而对含铅玻璃加入量为60%(FG60)、70%(FG70)和80%(FG80)样品的影响较小。随着烧结时间延长，样品晶化程度提高，晶体长大，玻璃相减少。适宜的含铅玻璃加入量为50%~70%，对应的FG50、FG60、FG70样品最佳烧结时间分别为4 h、3 h、3 h。     

锂铍稀有金属选矿及综合利用研究现状及展望

简述了锂铍稀有金属资源分布、需求以及选矿工艺现状,并对浮选作用机理进行了概况。指出联合选矿工艺将成为复杂锂铍资源分离的发展趋势；仍需要加强锂铍浮选作用机理研究,丰富稀有金属浮选基础理论；开发绿色高效环保的浮选药剂,减少环境污染；强化钽、铌、锡、石英和长石等伴生资源的综合利用,降低固废排放。     

某金铁氧化矿中矿泥对氰化浸出影响的研究

考察了高岭土、绿泥石、白云石和褐铁矿4种常见易泥化矿物对氰化浸出过程的影响,发现褐铁矿和白云石在细磨时形成的次生矿泥比原生矿泥具有更强的吸附已溶金能力,使浸出率降低。研究了原矿经粗磨-磁选后易泥化矿物的分布,对云南某金铁氧化矿采用"粗磨-分类磁选-分组氰化浸出"的新工艺,有效减少了次生矿泥的生成,与"细磨-氰化浸出-磁选"的传统工艺相比,金浸出率由85.26%提高到93.05%,铁精矿回收率由41.20%提高到70.86%。     

某微细粒难选金矿浮选尾矿无氰提金工艺及流程诊断

某选矿厂处理低品位微细粒难选金矿,生产初期浮选指标较差、浮选尾矿品位较高,尾矿库中金资源量较高。为了提高对浮选尾矿中金资源的二次回收,同时避免高额的含氰尾矿排放的环境保护税,加强无氰提金工艺的研究与应用对环境保护及企业持续健康发展具有重要意义。本文通过对无氰提金工艺全流程考察及流程诊断,结合浸出原矿与浸渣的工艺矿物学研究结果,分析浸出工艺存在的问题,为下一步工艺优化奠定基础。     

青海五龙沟金矿中金的赋存状态研究

青海五龙沟金矿石贵金属矿物以自然金为主,金品位为2.43 g/t,伴生低品位银,属于微细粒—超微细粒浸染型含碳、砷的极难选冶金矿石。为给该矿石的开发利用提供依据,采用X荧光分析法、化学分析、矿相显微镜、X射线衍射分析及MLA矿物自动定量系统等手段对矿石的化学成分、结构构造、矿物组成及金的赋存状态进行研究。结果表明:(1)矿石有价元素为金、银,有害杂质砷、碳含量较高,含金矿物主要有自然金及方锑金矿、黑铋金矿、碲金银矿等;(2)金粒大多数呈显微、超显微分散状态包含于毒砂及斜方砷铁矿中,其次包含于绢云母、绿泥石和石英等脉石矿物中,少数与黄铁矿和磁黄铁矿连生或包裹,显微镜中可见金不多,粒度大多小于1μm;(3)金嵌布粒度以微细粒为主,98.45%金粒粒度小于0.04 mm;黄铁矿、毒砂和磁黄铁矿的嵌布粒度以中细粒为主,均处于浮选的适宜范围;(4)金的选矿回收与硫砷化物的回收密切相关,尤其是要重视毒砂的回收。研究结果可以为该金矿石的合理开发利用提供技术依据。