冶炼工业废气中SO_2的脱除研究

研究用软锰矿的水悬浮液脱除冶炼工业废气中SO_2的工艺可行性,提出抑制副产物MnS_2O_6生成的途径。     

生物质焦焙烧还原低品位软锰矿及其动力学

采用生物质焦和活性炭粉作还原剂,在管式炉中进行了低品位软锰矿焙烧还原对比试验.分别研究了焙烧温度、焙烧时间、生物质焦用量等条件对软锰矿还原率的影响,对焙烧产物进行了X射线衍射分析.结果表明,生物质焦在焙烧时间和还原效率上优于活性炭粉;软锰矿焙烧还原依次经历Mn O2→Mn2O3→Mn3O4→Mn O过程;在焙烧温度为800℃,焙烧时间为50 min,生物质焦用量为10%时,软锰矿还原率可达98%以上,在此基础上导出了还原动力学方程,并证实还原过程由界面化学反应控制,表观活化能为43.896 k J·mol-1.     

FeS2-MnO2-H2SO4浸出软锰矿反应

针对FeS2-MnO2-H2SO4浸出软锰矿的浸出过程进行了研究,考察了反应过程中FeS2反应方式对MnO2浸出的影响.研究过程中分别对矿浆中的Mn2+,Fe2+和Fe3+质量浓度,以及矿浆电位的变化进行了监测,并对浸出过程进行了阶段的划分与分析.通过对浸出过程中不同反应阶段的分析,发现不同反应阶段过程中Mn2+与Fe3+浸出速率的比值是不同的,说明在不同阶段存在着不同的反应方式,导致FeS2的利用率在不同阶段存在明显差异.同时,对矿浆电位的监测表明,高电位有利于FeS2浸出Fe2+,从而加快了MnO2的浸出速率.     

利用低品位软锰矿制备硫酸锰的工艺进展

介绍了目前利用低品位软锰矿制备硫酸锰的工艺现状以及目前正在开发的工艺,并且简述了它们的优缺点。对低品位软锰矿资源的开发利用具有一定的指导意义。     

用软锰矿浆在筛板塔中烟气脱硫

按一定比例将软锰矿粉与清水配成矿浆作为脱硫剂进行烟气脱硫研究,在单板筛板塔中考察了液气比、液固比、空塔气速、温度等操作条件对脱硫率的影响;并选择适宜的操作条件,在双板筛板塔中考察了脱硫率随时间变化的关系,建立了表征脱硫率与锰浸取率内在联系的回归方程     

某铜厂洗净残渣的浸出工艺条件研究

为处理某火法炼铜厂的洗净残渣，提出了湿法两矿一步法。对本工艺中浸出机理进行了叙述。对此工艺中浸出部分的工艺条件进行了摸索，结果表明：温度、浸出时间、液固比分别为80℃、3h、5时浸出结果较好。在浸出过程中，溶液中铁离子的含量对铜锰的浸出起了至关重要的作用，机理有待于进一步研究，可能由于铁离子在反应中起了催化作用，反应呈现出自催化氧化反应的特征。     

软锰矿在辉钼矿焙烧过程中的固硫作用

为克服辉钼矿传统焙烧-氨浸工艺中含硫烟气对环境的严重污染, 提出联产钼酸铵和硫酸锰的软锰矿与辉钼矿共同焙烧新工艺, 并从热力学角度和通过热重分析等手段在理论上论证该新工艺的可行性. 根据焙烧产物的性质, 设计了软锰矿和辉钼矿共同焙烧新工艺的工艺流程, 采用分段升温焙烧, 研究了辉钼矿与软锰矿的物料配比对固硫率的影响. 研究结果表明: 加入软锰矿可以显著降低辉钼矿的焙烧温度, 在450～550 ℃时, MoS2的分解率可达100%, 产物以MnMoO4为主;焙烧过程中的固硫率随着MnO2含量增加而升高, 固硫效果非常明显, 当n(MnO2):n(MoS2)=9时, 固硫率接近98%.     

Reductive leaching of manganese from low-grade pyrolusite ore in sulfuric acid using pyrolysis-pretreated sawdust as a reductant

Manganese (Mn) leaching and recovery from low-grade pyrolusite ore were studied using sulfuric acid (H₂SO₄) as a leachant and pyrolysis-pretreated sawdust as a reductant. The effects of the dosage of pyrolysis-pretreated sawdust to pyrolusite ore, the concentration of sulfuric acid, the liquid/solid ratio, the leaching temperature, and the leaching time on manganese and iron leaching efficiencies were investigated. Analysis of manganese and iron leaching efficiencies revealed that a high manganese leaching efficiency was achieved with low iron extraction. The optimal leaching efficiency was determined to be 20wt% pyrolysis-pretreated sawdust and 3.0 mol/L H₂SO₄ using a liquid/ solid ratio of 6.0 mL/g for 90 min at 90℃. Other low-grade pyrolusite ores were tested, and the results showed that they responded well with manganese leaching efficiencies greater than 98%.     

芦丁还原浸出低品位软锰矿的研究

为了研究糖蜜酒精废液中有机物还原浸出软锰矿的机理,采用芦丁为还原剂,在酸性介质中直接浸出低品位软锰矿。通过正交实验和单因素实验,研究了芦丁浓度、硫酸浓度、反应温度、浸出时间等因素对锰浸出率的影响,并对反应过程机理进行了初步探讨。实验结果表明,影响锰浸出率的主要因素依次为反应温度、硫酸浓度、浸出时间和芦丁浓度;当硫酸初始浓度2.35 mol/L,芦丁初始浓度0.041 mol/L,反应温度90℃,浸出时间90 m in时,锰浸出率达94.9%。     

Optimization of reaction conditions for the electroleaching of manganese from low-grade pyrolusite

In the present study, a response surface methodology was used to optimize the electroleaching of Mn from low-grade pyrolusite. Ferrous sulfate heptahydrate was used in this reaction as a reducing agent in sulfuric acid solutions. The effect of six process variables, including the mass ratio of ferrous sulfate heptahydrate to pyrolusite, mass ratio of sulfuric acid to pyrolusite, liquid-to-solid ratio, current density, leaching temperature, and leaching time, as well as their binary interactions, were modeled. The results revealed that the order of these factors with respect to their effects on the leaching efficiency were mass ratio of ferrous sulfate heptahydrate to pyrolusite > leaching time > mass ratio of sulfuric acid to pyrolusite > liquid-to-solid ratio > leaching temperature > current density. The optimum conditions were as follows: 1.10:1 mass ratio of ferrous sulfate heptahydrate to pyrolusite, 0.9:1 mass ratio of sulfuric acid to pyrolusite, liquid-to-solid ratio of 0.7:1, current density of 947 A/m2, leaching time of 180 min, and leaching temperature of 73℃. Under these conditions, the predicted leaching efficiency for Mn was 94.1%; the obtained experimental result was 95.7%, which confirmed the validity of the model.