北祁连山石居里富铜矿选矿性试验与研究

石居里铜矿床矿石中主要矿石矿物由黄铜矿及黄铁矿等组成。铜含量一般为4％～20％，由于黄铜矿与黄铁矿复杂的嵌布关系，采用传统的老三样(丁黄药、石灰、2#油)浮选(一段磨矿，小于0．074mm占70％左右)精矿粉的铜品位仅达15．03％。造成了一定铜资源的浪费。通过对该类型铜矿石的矿物学组构及特征的研究，经多次试验后采用DY-1捕收剂及两段磨矿流程，即一段粗磨矿(小于200目即0．074mm占70％左右)丢尾，二段粗精矿再磨(小于325目即0．043mm占95％左右)后精选，使铜精矿Cu品位达20．73％，同时使硫回收率由51．26％上升到74．11％。     

河南省鲁山石墨矿浮选工艺研究

河南鲁山石墨矿属区域变质型矿床.根据矿石性质,进行了粗选条件试验,阶段磨矿阶段选别试验和阶段磨矿阶段选别预先分目试验,研究结果表明阶段磨矿是保护石墨大鳞片的有效方法,同时,结合预先分目能更好地提高石墨大片率.阶段磨矿阶段选别预先分目工艺闭路试验获得的指标为:当原矿品位为3.65%时,获得的技术指标为精矿品位C90.62...     

直线掏槽爆破试验

我队过去在巷道掘进中，一直采用斜眼掏槽方式，其循环进尺和炮眼利用率都比较低。为了提高掘进效率，我们进行了直线掏槽试验。通过试验对比：炮眼利用率达85—90％，比斜眼掏槽高18％左右；平均循环进尺1.5米左右，比斜眼掏槽提高约55％。加快了掘进速度，经济效益也比较好。     

拜耳法高铁赤泥回收铁的试验研究

以平果铝业公司的高铁泥为原料利用拜耳法分析高铁赤泥的基本性质,并研究采用添加煤粉还原的磁化焙烧——磁选工艺,从高铁赤泥中回收铁精矿的工艺技术,对工艺参数进行优化,寻找精矿品位和回收率参数等可能提高的途径,研究结果表明:焙烧温度800℃,焙烧时间30 min,磨矿时间5 min,煤粉用量4倍,磁选磁场强度2 000 Oe工艺条件下获得精矿品位为54.51％,回收率55.01％.回收率低的主要原因是铁矿和脉石没有实现单体分离,可以通过更高解离度的磨矿来实现.     

硫化矿浮选粗精矿再磨工艺对矿物表面性质的影响

随着矿产资源开发利用程度的逐年加剧,目前大部分有色金属选厂处理的都是品位低、嵌布粒度细的复杂多金属矿,为提高有价金属的选矿回收率、降低磨矿成本,大部分选厂都采用"阶段磨矿、阶段选别"工艺,其中以浮选粗精矿的再磨最为常见.硫化矿浮选粗精矿的再磨可显著提高磨矿效率及目的 矿物解离度,但生产实践中大部分选厂仅关注目的 矿物的解离度,而忽视了硫化矿浮选粗精矿再磨过程中磨矿介质、磨矿方式、矿浆电化学环境等多种因素对矿物表面性质及浮选行为的影响.文章系统总结了硫化矿浮选粗精矿矿物组成特点及矿浆化学性质的基础上,综述了硫化矿浮选粗精矿再磨过程中磨机类型及磨矿方式、磨矿介质材质及形状、矿浆电化学环境、药剂浓度等多种因素对再磨后矿物表面性质及浮选行为的影响规律,指出通过精矿再磨工艺参数及矿浆电化学环境的合理优化调整,增强矿物表面间的亲水/疏水性差异,提高精选分离效果应是未来硫化矿浮选粗精矿再磨研究关注的重要方向.     

矽线石浮选药剂最佳配方新探索

通过对单种药剂、混合药剂的浮选对比试验数据的直观对比 ,制定出浮选药剂最佳方案。指出采用原化皂与SA比为 2∶1和磨矿细度 - 2 0 0目占 5 1%左右为最佳 ;为制备浮选效果最佳的配方创造了条件     

人造金刚石与硬质合金分层钻进试验

我们进行生产试验的某铁矿区，地层软硬变化较大，闪长岩与蚀变闪长岩、大型岩交替出现。在较致密的闪长岩中（可钻性8级左右），人造孕镶金刚石钻进的性能发挥的较好，金刚石钻进效率比钢粒钻进提高两倍；比用针状合金钻进提高一点五倍；比用普通硬质合金钻进提高五点八倍。金刚石钻进回次进尺比钢粒钻进提高一点二倍；比用针状合金钻进提高一点六倍；比用普通硬质合金钻进提高七倍。但在6级左右的蚀变闪长岩中，人造金刚石钻进无论是钻进效率，还是回次进尺，仍然比其他钻进方法优越。相反，在较软的5级大理岩中，由于岩石较软，人造孕镶金刚石钻     

碱/聚合物驱油藏剩余油饱和度定量监测技术研究

碱／聚合物二元复合驱是一种大幅度提高老油田采收率的三次采油方法．室内研究、试验表明，可比水驱提高采收率10％～18％左右．通过开展玻璃钢套管完井技术研究、玻璃钢套管测井方法研究和厚油层细分技术研究，在碱／聚合物二元复合驱先导实验区建立玻璃钢套管井时间推移感应测井和时间推移C／O测井系统，定量监测碱／聚合物二／C复合驱注入过程中剩余油饱和度的变化，通过8年的矿场试验，成功建立了剩余油饱和度定量研究的动态监测预测系统，同时，测井资料表明，碱／聚合物二元复合驱有效提高了波及体积和驱油效率．     

江川中低品位磷矿摩擦电选试验

采用荧光光谱、X射线衍射和光学显微镜等分析手段,对江川磷矿的矿物组成、结构构造和矿物嵌布特征进行研究。结果表明,该磷矿组成中w(P_2O_5)=24.47%、w(SiO_2)=27.21%、w(MgO)=1.78%,属中低品位硅钙质磷矿,磷灰石和石英分别为主要的有用矿物和脉石矿物。在此基础上,利用摩擦电选技术处理原矿以回收矿石中的有价成分,试验结果表明,在碳粉(助磨剂)加入量占1%,磨矿细度-0.147 mm占92.90%,预热温度为110℃的条件下,原矿经"1粗1精1扫"的摩擦电选闭路试验后,获得w(P_2O_5)30.23%、回收率83.26%,以及w(MgO)/w(P_2O_5)为2.35%的优良指标,为中低品位磷矿的高效且环保的开发利用提供了一种新的技术方案。     

从四川黑水铁矿中提取超级铁精矿的研究

四川黑水铁矿原矿含铁品位为32%左右,磁性铁的占有率为89%左右。在工艺矿物学研究的基础上,采用二段磨矿—磁选—反浮选脱硅的选矿工艺流程,获得铁品位71.79%,回收率86.51%,SiO2含量小于0.3%的超级铁精矿,及含铁品位67.31%,回收率1.38%的普通铁精矿。生产超级铁精矿可以提高矿山的开发利用价值,特别是对盘活一些外部开采条件不好而资源禀赋较好的铁矿资源是有益的。     

断裂剪切带厘米级磨砾和纳米级磨粒的发现、命名及其油气地质意义

上世纪70年代初,在江苏江宁逆断层中发现了厘米（cm）级磨砾,这种磨粒通常在韧脆性断裂剪切带中都可能找到。80年代末,对美国加州深钻岩芯进行扫描电子显微镜观测时,在晚中生代花岗质糜棱岩滑移叶片中发现了纳米（nm）级超微球粒结构,球粒（2—5nm）紧密聚集、定向明显。因其形成同滚动、研磨和剪切作用过程有关,故将球形微粒称“磨粒”。嗣后,在陕北和黄海深钻岩芯石炭-二叠系泥岩滑移叶片中,也发现类同现象（微米-纳米级）。近年来又在郯庐断裂、日本中央构造线大型断裂带,以及南京幕府山寒武系至三叠系不同地层的各种剪切滑移构造中都发现了nm级磨粒构造。泥岩中含磨粒滑移层具有涂抹效应,起到油气封盖作用,这在陕北油气田已得到了验证。对其磨粒构造蕴藏的丰富地质信息,特别是在微观动力学方面（包括动热变质作用、流体渗散作用、颗粒自旋作用和地质催化作用等）应作进一步研究。     

Some breakage characteristics of ultra-fine wet grinding with a centrifugal mill

A centrifugal mill is a high-power intensity media mill that can be used for ultra-fine grinding, employing centrifugal forces generated by gyration of the axis of the mill tube in a circle. The mill charge motion is quite different depending on the ratio of the gyration diameter to the mill diameter (G / D ratio), varying from a motion similar to that of a conventional tumbling media mill to that of a vibration mill. In this study, a centrifugal mill was constructed with an arrangement where the gyration diameter could be readily adjusted. The batch grinding characteristics of three different minerals (limestone, talc and illite) in water with dispersing agent were investigated at various G / D ratios. It was found that the optimum G / D ratio in terms of the specific energy consumption to give a desired fineness of product was different for the three minerals. This was due to their different reactions to the breakage mechanisms provided by the mill charge motion at varying G / D ratios. The size distributions became progressively narrower at increased grinding times, and particles finer than about 0.1 μm were not detected even for prolonged grinding times. Measurement of specific surface areas indicated that this was not due to an artifact of the size measurements by laser diffractometry. This implies that there is a limitation in which particles finer than 0.1 μm are not produced under the conditions tested in this type of mill, but further investigation is needed for experimental verification of this limit of comminution.     

Analysis of the gold recovery profile through a cyanidation plant

Leaching in the grinding circuit is currently practiced in plants that process gold ores with low content of cyanide consuming minerals. The high gold recovery observed in the grinding–classification section of the plant is commonly explained by the inherent high initial dissolution rate of gold observed in gold ore cyanidation, or by the intense agitation prevailing in grinding mills. For understanding this leaching behavior of gold ores, the grinding, classification and leaching sections of a gold processing plant are analyzed through reconciliation of operating data. It is found that gold circulation in the grinding circuit is quite different from the flow behavior of other species due to the strong gold separation effect in the hydrocyclones, which produces quite large residence time for gold-rich particles. The results presented in this study demonstrate that the residence time of these particles in the grinding circuit can be as long as in the leaching tanks and might be the dominant factor in explaining the high dissolution of gold in this section.     

Kinetics of fine wet grinding of zeolite in a steel ball mill in comparison to dry grinding

Batch wet grinding of zeolite was studied with emphasis on a kinetic study in a laboratory size steel ball mill of 200 mm diameter. The breakage parameters were determined by using the single sized feed fractions of − 850 + 600 µm, − 600 + 425 µm and − 425 + 300 µm for the zeolite samples. The S_i (specific rate of breakage) and B_i,j (primary breakage distribution) values were obtained for those feed size fractions in order to predict the product size distributions by simulation for comparison to the experimental data. The specific rates of breakage values for wet grinding in the first-order breakage region were higher than the dry values reported previously by a factor 1.7 at the same experimental conditions, but the primary breakage distribution (B_i,j) values were approximately the same. The simulations of the product size distributions of zeolite were in good agreement with the experimental data using a standard ball mill simulation program. The wet grinding of zeolite was subjected to slowing-down effect in the mill at 2 min of grinding, corresponding to an 80% passing size of about 400 µm. On the other hand, the slowing down effect in the dry grinding of zeolite was also seen at 4 min of grinding. In addition, effects of some operational parameters on dry and wet grinding of zeolite were determined by simulation using the breakage parameters obtained experimentally.     

Study on mechanochemical effect of silica for short grinding period

Silica was ground in an oscillating mill at various grinding period to study the mechanochemical effect in fine grinding process. The ground particles exhibited massive size reduction where the volume moment diameter of 5.56 μm was reached within 600 s. Aggregation of fine particles was very pronounced when it was ground for 600 s due to high surface energy. Aggregation of fine particles caused the ground particles to exhibit poly-modal particle size distribution. Line broadening and reduction of diffractogram peak intensity were observed. Amorphization rate up to 16.9% was exhibited by the particle ground for 600 s. Preferential breakage of plane was observed where (101) and (111) was easily distorted compared to (110) and (200). Rapid reduction of crystallite size was observed at early stage of grinding until it reached a plateau at 5 nm at 600 s whilst the change in lattice strain was 0.5%.     

福建某低品位钼矿选矿试验研究

针对福建某低品位钼矿矿石性质,确定了粗磨粗选、粗精矿再磨精选的浮选方案。采用该浮选方案及合理的选别条件,对含钼为0.08%的钼原矿选别,获得钼精矿品位52.45%、钼精矿产率为0.14%、钼回收率90.19%的良好指标。     

Comparative study of microstructural characteristics and stored energy of mechanically activated hematite in different grinding environments

Hematite concentrate was mechanically treated using different milling machines and experimental conditions in air atmosphere. The changes in phase constitution, particles size, specific surface area, lattice parameters and X-ray amorphous phase fraction of activated hematite were determined. It was found that the agglomeration of the particles take place during extended milling with accessible pores for Nitrogen gas. The higher media surface brought about the largest specific surface area whatever milling devices used. After 9 h of grinding with higher media surface, the maximum and minimum specific surface area resulted from the grinding in the tumbling and vibratory mills, accounting for 6.83 m²/g and 18.42 m²/g, respectively. For the same grinding condition, tumbling mill produced the lowest X-ray amorphous phase. The maximum X-ray amorphous material estimated around 85% from the grinding in the planetary mill with higher media surface for 9 h of milling.     

The influence of pulp density on the selective grinding of ores

The size distributions of the products from laboratory-scale batch grinds, of a leadzinc ore and a tin ore, were measured as a function of pulp density. A reduction in the overall grinding rate at high pulp densities correlated well with the increase in pulp viscosity. Enhanced fines production, apparent at the higher pulp densities, was however controlled largely by the particle packing and less by viscosity effects. The individual mineral distributions themselves responded differently to changes in pulp density. In particular, the extra fines generated at the high pulp densities consisted primarily of gangue material, with the softer ore minerals actually showing a drop in production. The addition of grinding aids, essentially viscosity modifiers, increased the grinding rate under certain conditions without producing any pronounced change in the selective grinding characteristics.     

切磨过程中花岗石材料去除机理研究

深入理解切磨过程中花岗石材料的去除机理是优化加工设备，加工工具以及加工参数的基础。本文研究了花岗石的断口表面、锯切表面、粗磨表面以及精磨表面形貌特征，并结合切磨过程中临界载荷、单颗金刚石磨粒所承受的切削力以及比能特征，对加工表面形成机理进行了分析。研究表明，材料的去除机理与单颗磨粒的最大切削厚度直接相关。随着单颗金刚石磨粒最大切削厚度的减小、花岗石的去除方式也逐渐由脆性断裂为主转为塑性流变为主。由于不同的材料去除机制对应不同的能量消耗，可以通过调节单颗磨粒的最大切削厚度控制材料的去除方式，进而控制能量消耗。因此，均匀的磨粒出露高度对于控制切磨过程中材料的去除机理和优化加工过程具有重要意义。     

Grinding of mineral mixtures in high-pressure grinding rolls

Attempts at improving comminution machines generally have been directed towards increasing the performance efficiency, particularly increasing throughput rate and decreasing energy consumption. The latest and most successful new comminution technology has been the high-pressure grinding rolls (HPGR), which have proved to be highly efficient in energy consumption and to have a relatively high throughput rate at low steel consumption. Already used extensively in cement plants worldwide, the first HPGRs in the mineral industry were installed in plants processing diamond ores. They are now finding their way into the large-scale base-metal mining industry. Since feed constituents in natural ores vary in their physical properties such as hardness, plasticity and brittleness, the present paper is concerned with an investigation of the behavior of a heterogeneous feed as it passes through the HPGR. The effect of feed composition on operational parameters, the energy efficiency of comminution, and energy distribution among the feed components is addressed. Mineral particles with high hardness act as energy transfer agents in the roll gap and enhance the grinding of softer mineral particles in a mixed feed.