镁质低品位铁镍硫化矿的活化工艺及机理

细菌浸出是镁质低品位铁镍硫化矿的潜在处理方案之一。针对该矿石浸出活性较低的问题,研究了硫酸预浸出和硫酸铵焙烧预浸出2种活化方案,并与细菌直接浸出(空白试验)做了比较。结果表明,2种活化方案都有利于金属回收,但硫酸铵焙烧预浸出方案的活化效果更优:浸出时间为8 d时,Ni、Cu和Mg的浸出率分别为90.2%、89.56%和61.19%,分别高于硫酸预浸出方案2.08%、12.2%和8.95%。矿石中的Mg主要在硫酸铵焙烧预浸出阶段进入溶液,细菌对Mg浸出的影响不大。XRD和能谱分析表明:浸出渣中Ni和Cu的残留量很低,Mg主要存在于难浸出的蛇纹石之中。     

Kinetics study of leaching arsenic from Ni-Mo ore roasting in dust mixture of hydrochloric and sulfuric acids

The kinetics of leaching arsenic from Ni-Mo ore roasting dust was investigated. The effects including leaching temperature, particle size of the smelter dust, stirring speed, the coefficient β（the molar ratio of sodium chlorate to arsenic in the smelter dust） and the initial H＋ concentration on leaching arsenic were studied. The results indicate that the leaching of arsenic increases sharply with the decrease of particle size. The orders of reaction with respect to H＋ concentration and particle size are determinted to be 1.136 and 1.806, respectively. The leaching of arsenic reaches 99% under experimental conditions, the apparent activation energy is determined to be 11.157 kJ/mol, which is consistent with the values of activation energy for diffusion model The kinetics equation of leaching arsenic from the roasting dust could be expressed by a semi-empirical equation as 1-2/3η （1 -η）^2/3 = k0（c[H＋]）^1.136ro^-1.806 exp[（-11157 /RT）t].     

几种白肋烟烤机控制系统的对比分析

根据设备控制系统的差异,现有白肋烟烘焙设备可分为热风对流式、微波辐射式。主要分析了现有三层、单层、流化床隧道式烘焙机的结构特点,并针对处理过程中热风对流系统的控制方式、物料的运动状态、设备的控制方法等,指出了采用流化床隧道式白肋烟烘焙机处理过程中,其热风系统控制分布较均匀,物料始终能处于悬浮翻滚状态,物料受热面积大大提高,且过程控制精度较好,有利于物料含水率和温度的稳定,对于改善提高白肋烟处理质量有着明显的可比优势。     

化学工业固体废物毒性分析研究

介绍了对硫酸烧渣和磷石膏两种固体废物进行急性毒性和浸出毒性鉴别试验的过程与结果,并对磷石膏由危险废物转变为非危险废物的原因进行了探讨,为硫酸烧渣和磷石膏的处置和利用提供了依据.     

Novel technology on preparation of double-layered pellets for sulfur and arsenic-bearing gold concentrates

Double-layered pellet （DLP） roasting is a novel pretreatment method for sulfur and arsenic-bearing gold concentrates. In this process, preparation of DLPs is a fundamental step which is required to produce DLPs with favorable mechanical strength and thermal stability. Studies were carried out to investigate the affecting factors and conditions on the preparation and properties of DLPs. The results show that moisture content has significant influence on DLPs preparation. With the increase of moisture content in the range of no more than 9.8%, drop resistance and compressive strength of green DLPs are raised and the pelletizing dynamics is improved accordingly. The optimum conditions are determined as moisture content of 9.8%, coating time of 14-16 min, drying temperature 〈80 ℃and drying gas velocity 〈1.2 m/s. When DLPs prepared under these conditions are roasted at 600 ℃ for 1 h, favorable removal and solidifying rates can be obtained, in which the removal rates of arsenic and sulfur are 94.38% and 82.55%, and the solidifying rates of arsenic and sulfur reach 99.62% and 99.79%, respectively. These results promise industrial application of DLP roasting.     

竖罐炼锌系统使用进口锌精矿的探讨

以通常使用的国产锌精矿为参照,重点分析了几家进口锌精矿的物理、化学性质及其可能对锌冶炼造成的影响.提出了在配料过程中和沸腾焙烧过程中所应采取的措施.     

以钴钼废催化剂为原料制备仲钼酸铵试验研究

进行了以钴钼废催化剂为原料制备仲钼酸铵试验研究，采用加碱焙烧、湿式球磨、沉钼酸和氨溶工艺路线。研究结果表明，焙烧温度、时间和纯碱加入量对钼的提取率均有一定的影响，沉钼酸过程除P效果较好，产品仲钼酸铵质量稳定。     

从石油重整废催化剂中回收铂

介绍一种从石油重整废催化剂中回收铂的工艺。废催化剂采用低温焙烧、浸出、离子交换等方法进行处理,可制取纯铂,生产聚合氯化铝产品。该工艺操作简单,铂回收率高,对环境无污染。     

采用硫酸铵焙烧方法从低品位碳酸锰矿中富集回收锰

研究了采用硫酸铵焙烧法从低品位碳酸锰矿富集回收锰的工艺．将碳酸锰矿与（NH4）2SO4通过研磨混合均匀，在马弗炉中300～500％焙烧0．5～3h．将焙烧过程铵盐分解产生的氨气发二氧化碳气体通过真空通入上一次的浸出液，将硫酸锰沉淀下来．焙砂采用60—90％热水，在液固为（3～10）：1的条件下浸取10—20min，得到硫酸锰浸出溶液，作为下一次焙烧过程的吸收液，对吸收液巾过滤得到的滤饼进行干燥后得到锰精矿．吸收液过滤后得到的滤液蒸发浓缩，结晶后又得到了（NH4）2SO4固体，可以复用．采用该工艺的锰回收率达80％以上，是一种从低品位碳酸锰矿富集回收锰的新工艺。     

现代锌处理技术的最新经验

自从1969年芬兰的科科拉（kokkola）锌厂投产以来，奥托昆普已在几个扩产阶段中开发并拓展了焙烧、浸出、净液和电积等锌厂工艺，开发出了取代黄钾铁矾工艺的奥托昆普转化浸出工艺、基于砷的奥托昆普净液工艺和奥托昆普精矿直接浸出工艺等新工艺。自收购了挪威锌公司奥达厂和德国ObemrSel的鲁奇冶金公司后，奥托昆普在焙烧、烟气净化、制酸和电积方面扩展了其技术诀窍。鲁奇冶金公司于1962年在印度第一次投入锌焙烧炉开始了其锌方面的商业运作，其后共有70多台鲁奇锌焙烧炉在世界各地投产。由于这些成绩，奥托昆普现在可以将目前的锌处理技术融合在一整套技术内。