胶磷矿柱式双反浮选工艺研究

针对我国西南地区难选硅-钙质胶磷矿,采用旋流-静态微泡浮选柱对其进行了柱式双反浮选工艺的研究.以硫酸和磷酸作为磷矿物抑制剂,脂肪酸类药剂PA-64作为碳酸盐矿物捕收剂,胺类药剂GE-601作为硅酸盐矿物捕收剂,考察了磨矿细度、药剂用量、循环泵工作压力等因素对浮选指标的影响.研究结果表明,采用旋流-静态微泡浮选柱双反浮选工艺,可以得到精矿P_2O_5品位30.49%,MgO含量0.73%,磷回收率81.03%的浮选指标,简化了胶磷矿浮选工艺流程.     

筛板充填浮选柱的气泡行为及其影响因素

设计并建立了一套筛板充填旋流微泡浮选柱试验研究系统,利用高速动态分析仪研究了清水-空气条件下筛板充填浮选柱内气泡的运动行为及充填筛板附近流体的流态,探讨了气体表观速度、开孔率、起泡剂用量及筛板充填层数对气泡直径大小的影响.结果表明:在筛板充填个数为6个,φ(起泡剂)为6.5×1-0 3,相同开孔率和表观气速时,气泡直径最大,而且气泡直径随表观气速的增加而增加.研究结果为充填浮选柱的设计提供了依据.     

旋流-静态微泡浮选柱在胶磷矿浮选工艺中的应用

采用旋流-静态微泡浮选柱对某胶磷矿进行了半工业试验研究,在原矿品位为23.73%P2O5的情况下通过正-反浮选流程获得了精矿P2O5品位29.78%、MgO品位0.29%,回收率82.69%的良好指标,缩短了流程结构.为浮选柱技术的工业应用进行了积极探索.     

钙硅质胶磷矿浮选工艺研究

针对湖北某中低品位钙硅质胶磷矿,分别进行单一反浮选、双反浮选和常温正反浮选工艺研究及药剂费用对比,结果表明：采用单一反浮选,可得到磷精矿P2O530.37%,MgO 0.36%,回收率88.38%的较好指标,且最为经济,每吨原矿药剂费用仅为15.28元;若希望精矿质量更好些,回收率更高些,建议采用双反浮选,可得到磷精矿P2O531.60%,MgO 0.43%,回收率90.63%的好指标,每吨原矿药剂费用为23.40元;正反浮选相对来说精矿质量一般、回收率较低、药剂费用较高、磨矿细度较细,指标分别为磷精矿P2O530.54%,MgO 0.70%,回收率84.62%,每吨原矿药剂费用为26.98元.     

钙硅质胶磷矿浮选工艺研究

针对湖北某中低品位钙硅质胶磷矿,分别进行单一反浮选、双反浮选和常温正反浮选工艺研究及药剂费用对比,结果表明:采用单一反浮选,可得到磷精矿P2O5 30.37%,MgO 0.36%,回收率88.38%的较好指标,且最为经济,每吨原矿药剂费用仅为15.28元;若希望精矿质量更好些,回收率更高些,建议采用双反浮选,可得到磷精矿P2O5 31.60%,MgO 0.43%,回收率90.63%的好指标,每吨原矿药剂费用为23.40元;正反浮选相对来说精矿质量一般、回收率较低、药剂费用较高、磨矿细度较细,指标分别为磷精矿P2O5 30.54%,MgO0.70%,回收率84.62%,每吨原矿药剂费用为26.98元.     

远安低品位胶磷矿浮选试验研究

确定了远安低品位胶磷矿的正-反浮选流程,通过正-反浮选,可获得原矿P2O517.96%,MgO 2.31%,精矿P2O531.21%,MgO 0.84%的良好指标,实现了胶磷矿与石英、白云石等杂质矿物的有效分离。采用十二烷基磺酸钠（SDS）作增效剂可以较大程度提高捕收剂的捕收性能和选择性,提高P2O5品位和回收率。     

颗粒尺寸与药剂性质对胶磷矿浮选过程的影响

通过磷矿颗粒的分级浮选、药剂对比及组合浮选对湖北保康钙质磷矿和大峪口硅钙质磷矿进行了系统研究.结果表明:分级后粒径为-65μm的小颗粒磷矿更有利于反浮选,且保康磷矿反浮选效果优于大峪口磷矿;复合药剂和酸性抑制剂均能改善保康钙质磷矿浮选效果,最终磷精矿品位达到36.14%,磷回收率为96.10%;药剂表面张力降低能增强药剂对磷矿颗粒的湿润.最后,通过测量电动电位和亲水亲油平衡值,对浮选过程效率进行了分析,并对浮选机理进行了讨论.     

筛板充填浮选柱浮选流体的速度场分布

为了研究充填筛板对旋流-静态微泡浮选柱分选段流体环境的影响,分别用激光粒度测速仪（LDV）和计算流体力学软件（FLUENT）对分选段的流体速度场分布进行测试与模拟,结果表明,轴向速度在0.18-0.41 m/s之间,径向速度在-0.06-0.08 m/s之间.与柱分选段无充填情况进行对比,筛板减弱了流体切向流动速度的50%-60%,改善了流体和气泡的径向弥散不均匀状态,且使轴向速度分布更趋于均匀,降低了Pe准数,促进了浮选流体的＂塞流＂环境.最后,推导出在筛板充填浮选柱单相流体中单个气泡的运动速度.     

一种高分子絮凝剂对细粒胶磷矿浮选的影响

我国磷矿资源以钙硅质难选沉积磷块岩矿石为主,含磷矿物与杂质矿物紧密共生,胶磷矿以“胶态”非晶质集合体存在,单体难以解离,磨矿细度高,产生的细粒表面积大,表面能高,致使药剂消耗量大,选择性差,严重影响磷精矿质量. 以晋宁高硅胶磷矿为研究对象,添加一种非离子型高分子絮凝剂Ｆ－０８进行正浮选和反浮选试验. 正浮选粗选中,磨矿细度为－０．０３８　ｍｍ　８１．１１％时,碳酸钠用量为４　ｋｇ／ｔ,水玻璃３　ｋｇ／ｔ,油酸钠１．１２５　ｋｇ／ｔ时,添加３０　ｇ／ｔ Ｆ－０８,磷精矿五氧化二磷品位从２３．９９％提高到２４．５４％,回收率从８０．８０％提高到８５．３０％;反浮选粗选中,六偏磷酸钠用量为２　ｋｇ/ｔ,十二胺１　ｋｇ/ｔ时,添加４０　ｇ/ｔ Ｆ－０８,磷精矿五氧化二磷品位从２１．５０％提高到２２．９５％,回收率从６５．３２％提高到７０．４８％. 通过ｚｅｔａ电位测定、沉降实验及激光粒度分析测定,Ｆ－０８的添加可促进捕收剂吸附,沉降速度增大,同时可增大硅酸盐矿物平均粒径.     

几种阳离子捕收剂浮选胶磷矿性能比较

为了较好地实现磷矿反浮选脱硅,选取适宜的胺类捕收剂及合理的浮选条件非常关键. 通过单泡管试验,对比研究椰油二胺、工业二胺、十二胺、86D（脂肪一胺）等4种不同胺类捕收剂对胶磷矿的浮选效果. 纯矿物试验结果表明:不同的胺类捕收剂具有不同的浮选性能,在不同的pH值下同一胺类捕收剂的浮选能力不同;在低用量、弱酸性介质中,十二胺对胶磷矿的捕收能力优于椰油二胺、工业二胺,最低是长碳链的一胺86D;在相同pH值条件下,碳链组成相同的脂肪二胺捕收能力强于脂肪一胺,碳链较长的脂肪一胺比碳链短的脂肪一胺捕收能力弱;在酸性介质中胺类捕收剂对胶磷矿的捕收能力比在碱性介质中弱. 实际矿物试验结果表明:胺类捕收剂对磷酸盐和硅酸盐矿物均具有较好的捕收能力;通过改变药剂加入量,调整其选择性,可更好地分离磷矿物与脉石矿物.     

高效反浮选捕收剂的合成与应用

针对传统脂肪酸捕收剂选择性差、常温下分散性和溶解性差的问题,以工业棉籽油酸为原料,经高温高压使脂肪酸的双键水解而引入羟基活性基团,进一步与助剂按比例复配得到一种高效反浮选捕收剂HY.将其用于宜昌某高镁磷矿的浮选试验,经一反一扫简单浮选工艺流程获得了精矿五氧化二磷品位34.59%,五氧化二磷回收率96.46%,氧化镁品位0.28%的良好浮选选指标,氧化镁脱除率高达95%,各指标优于公开招标各项指标要求,且浮选在常温下进行,药剂用量仅0.84kg/t.表明反选捕收剂HY具有良好的浮选性能,其化学修饰改性改善了捕收剂的常温溶解性同时增强了其对钙离子、镁离子的选择性.     

抑制剂W—98在翁福磷矿反浮选中的选矿研究

根据公司福磷矿的性质，采用反浮选工艺处理胶磷矿，用反浮选高效抑制剂W－98作为磷矿的抑制剂，来抑制磷矿物而浮白云石等脉石，从原矿P2O5品位为27．33％，MgO为6．19％中，获得了磷精矿P2O5品位为37．34％，MgO为0．73％，回收率92．39％的选矿指标。     

磷矿反浮选捕收剂的评价方法

磷矿反浮选捕收剂大多数是由天然脂肪酸制成的,种类繁多,性能各异.从市场快速、准确地选择磷矿反浮选捕收剂,对浮选实践和浮选研究十分重要.浮选捕收剂的评价有助于掌握捕收剂的浮选性能,了解其在浮选过程中的作用.浮选法是浮选捕收剂的传统评价方法,程序复杂,耗时耗力.提出了一种新的浮选研究方法:燃烧-吸附量评价法,通过燃烧无机的矿石样品来测定其表面吸附的有机捕收剂量,评价磷矿反浮选捕收剂的性能.通过对油酸、硬脂酸和软脂酸这些结构明确且浮选工作者熟悉的脂肪酸的浮选性能和在白云石上的吸附量,建立了一个评价模型,验证燃烧-吸附量评价法的可行性.     

Process intensification of fine coal separation using two-stage flotation column

Flotation column is widely used as the separation equipment for fine mineral due to its high selectivity. However, this device may be unsuitable for the coarse particle flotation and has high handling ability. A two-stage flotation column with dimensions of 2 000 mm× 1 000 mm×4 000 mm was designed to enhance the column flotation process. The energy input was modified by adjusting the flow rate and the head of circulating pump. The flotation column was designed with low energy input in the first stage （speed flotation stage） to recover easy-to-float materials quickly, and high energy input in the second stage （recovery stage） to recover difficult-to-float minerals compulsorily. Contrast experiments on the throughput and coarse coal recovery of high ash coal from the Kailuan Mine were conducted using conventional single-stage flotation column and the two-stage flotation column. The results show that the combustible matter recovery of the two-stage flotation column is 5.25% higher than that of the conventional single-stage flotation column. However, the ash contents of clean coal for both columns are similar. Less coarse coals with low ash are obtained using the two-stage flotation column than that using the single-stage column flotation with the same handling ability. The two-stage flotation column process can enhance coal flotation compared with the conventional single-stage column flotation.     

A honeycomb-tube packing medium and its application to column flotation

We address problems in the development of large-scale flotation columns that use short cylinders. As a starting point, we investigated the packing medium to identify a highly efficient internal packing for the flotation column. The chosen packing was a honeycomb structure with an aperture diameter of 80 mm, a web thickness of 0.80 mm, a film height of 1000 mm, packed into a 400 mm diameter space, which completely filled the vessel at optimal cost. The column consisted of a modular ring of single-hole hexagonal honeycomb tube packing made from atactic polyproplene (PP-R). The packing was tested in a cyclonic, static mi-cro-bubble flotation column. Computational fluid dynamic modeling was used to analyze the flotation fluid in a honeycomb tube packed flotation column. Our results show that the fluid axial movement was maximized and that the transverse fluid velocities were zero in the vicinity of axial flow. Using the honeycomb tube packing for copper sulfide flotation we observed that the average concentration in the product was increased to 25.41%, from an average feed concentration of 0.729%, with an average recovery of 92.92%. The demands of on-site industrial production were met.     

Process mineralogy of copper-nickel sulphide flotation by cyclonic-static micro-bubble flotation column

In our study we investigated a refractory copper-nickel sulfide ore separation by using a cyclonic-static micro-bubble flotation column (FCSMC). The process mineralogy of the main products was studied. Using a scanning electron micro-scope-energy dispersive system (SEM-EDS) and an X-ray spectrometer the mineral category and content of samples were analyzed. By using a mineral liberation analyzer (MLA) the mineral liberation characteristics were revealed. It is shown that in roughing feed the monomers liberation degree of nickel pyrite and chalcopyrite take up 84.11% and 88.82%, respectively. In tailings, the lost nickel pyrite and chalcopyrite are mainly monomers. Therefore, strengthening the micro-fine particle recovery capacity is the key to increase recovery.     

Effect of hydroxamic acid polymers on reverse flotation of bauxite

The effect of hydroxamic acid starch (HAS) and hydroxamic acid polyacrylamide (HPAM) on the flotation of diaspore and kaolinite was investigated by flotation test. It is found that HAS depresses diaspore but activates kaolinite in acidic pulp,while HPAM activates both diaspore and kaolinite in the pH range of 2.0 - 10.5. The measurement of zeta potential shows that both HAS and HPAM can increase zeta potential of negatively charged diaspore, which indicates the existence of chemical bonding or hydrogen bonding between the reagents and diaspore.By covering the collector dodecyl amine(DDA) on diaspore surface, HAS increases the hydrophilicity of minerals and depresses the flotation of diaspore,however HPAM activates the flotation of diaspore by increasing the adsorption of DDA on diaspore surface.     

提高磷矿品位的单一反浮选试验

贵州某磷矿五氧化二磷品位26.43%、氧化镁含量3.82%,针对该磷矿中氧化镁含量高的特点,采用常温单一反浮选的方法进行提磷脱镁试验.试验结果表明:在矿粉-0.074 mm含量达到70.2%条件下,分别以硫酸和磷酸作为抑制剂,提磷脱镁指标均较好;以硫酸作为抑制剂时,可获得精矿五氧化二磷品位为31.69%,氧化镁含量为0.89%,回收率为96.95%的指标;以磷酸作为抑制剂时,可获得精矿五氧化二磷品位为31.63%,氧化镁含量为0.98%,回收率为97.01%的指标.