Surface chemical study of the selective separation of chalcopyrite and marmatite

FCLS (Ferric Chromium Lignin Sulfonate) was used to aid the separation of chalcopyrite from marmatite. Flotation, adsorption and zeta-potential tests of treated marmatite and chalcopyrite were performed. The flotation of marmatite was strongly depressed, while that of chalcopyrite was only slightly depressed, over a wide range of pH values when FCLS was used as depressant in the presence of Butyl Xanthate (BX). The adsorption of BX onto chalcopyrite or marmatite takes place over a wide pH range. The adsorption density of BX on chalcopyrite and marmatite decreases as the pH increases. The adsorption density of FCLS onto marmatite is greater than the adsorption density onto chalcopyrite. The zeta potentials of chalcopyrite and marmatite become more negative due to the addition of xanthate and FCLS.     

硫化氢处理混合器的研制

原油中H2S的处理,是通过加入化学除硫剂及自动监测控制在管道内清除H2S,即在原油进入分离器前加入除硫剂,通过混合器将除硫剂与油气混合,在管道中与H2S产生化学反应消除H2S,除硫效果的好坏是混合器混合能力的直接反映.     

生物法应用于脱除硫化氢的实验研究

根据脱氮硫杆菌利用硫代硫酸盐、硫化物作为能源的性质,研究了脱氮硫杆菌应用于脱除硫化氢工艺中的碳酸钠溶液再生.通过单因素分析,进行了碳酸钠溶液含量、温度、pH值、进气速率、喷淋量、停留时间及洗涤液中含脱氮硫杆菌等因素对脱硫率影响的实验研究,初步确定了含H_2S(浓度≤1 300 mg/m~3)天然气脱硫的最佳工艺条件为:温度25～35 ℃,pH值8～9,初始碳酸钠质量分数5%,停留时间90 s.实验结果还表明:喷淋量和进气速率都会影响脱硫率;进入吸收塔的再生碱液携带有脱氮硫杆菌,而含脱氮硫杆菌的洗涤液(再生碱液)有利于提高脱硫率.     

捕收剂在硫化矿物表面吸附机理的研究进展

综述了药剂与硫化矿表面吸附作用机理的理论研究,总结了现代表面测试技术在硫化矿表面吸附作用机理研究中的应用前景．表面测试技术在选矿中的应用,使矿物与药剂的吸附机理研究更加深入,也促进了浮选理论和工艺技术的持续发展和不断完善．     

Bioelectrochemical sulfate reduction enhanced nitrogen removal from industrial wastewater containing ammonia and sulfate

Low organic carbon-to-nitrogen ratio and existing sulfate (SO₄²⁻) in industrial wastewater limited nitrogen removal. Coupling SO₄²⁻ reduction with sulfide autotrophic denitrification provides a novel strategy. Herein, bioelectrochemical sulfate reduction was coupled with heterotrophic sulfate reduction to drive sulfide autotrophic denitrification. In this coupled system, total nitrogen (TN) removal efficiency was increased from ~25% to ~85% by inputting −45 mA electricity. With the help of supplying electrons to denitrification through SO₄²⁻ reduction, coulomb efficiency was improved to 61.5%. Also, bioelectrochemical sulfate reduction could improve sulfur recovery and thus increase TN removal efficiency. Furthermore, through tuning turnover numbers of SO₄²⁻, high TN removal efficiency can be obtained at various concentrations of SO₄²⁻. Moreover, main functional bacteria in this system were identified. Finally, ~75% TN removal efficiency was achieved with real wastewater in this system. Overall, this work offered a new approach for efficient nitrogen removal from industrial wastewater containing SO₄²⁻.     

模拟水中硫离子对不锈钢钝化膜破坏作用的光电化学研究

采用光电化学方法研究了模拟冷却水中硫离子对不锈钢钝化膜的破坏作用.结果表明,不锈钢钝化膜显示n-型光响应,最大吸收峰出现在310 nm处.不锈钢钝化膜在电位约-0.35 V开始出现光电流,随电位升高,光电流增大.钝化膜禁带宽度Eg随电位的升高而减小,并逐渐向铁氧化物的Eg靠近.模拟冷却水中加入硫离子使不锈钢钝化膜的光电流增大,Eg减小.硫离子的浓度越大,测得的光电流越大,而Eg越小,这可归因于钝化膜膜电阻的降低及钝化膜中氧化铬含量的减少.     

Copper hydrometallurgy-current status,preliminary economics,future direction and positioning versus smelting

The heap leaching of oxide copper ores with copper cathode recovery by solvent extraction and electrowinning is now well established as a low-cost method of copper recovery. This technology has recently been applied successfully to mixed oxide and chalcocite ores, notably in Chile at Cerro Colorado, Quebrada Blanca and Zaldivar.Currently, there are significant development efforts underway to try to extend heap leaching to chalcopyrite ores.The success of heap leaching/SX/EW has also led to a revival in the development of hydrometallurgical processes to recover copper from chalcopyrite and other copper concentrates. The current status of copper hydrometallurgy is reviewed and the most commercially attractive potential applications are explored. The advantages and disadvantages of the hydrometallurgical treatment of chalcopyrite concentrates and its preliminary economics are compared with those for the current best practices in copper smelting and refining.     

Defect structure and chemical diffusion in nickel sulfide β-Ni3S2

The chemical composition, defect structure, and diffusion in nickel sulfide -Ni₃S₂ have been investigated in H₂S-H₂ mixtures containing between 1 and 65% H₂S between 560 and 700°C. Gravimetric, density, and X-ray studies were carried out. In the thermodynamically stable compound the ratio of Ni/S varied between 1.3 and 1.75. The X-ray examination showed a step change in the lattice parameter at the Ni/S ratio 1.4. A linear dependence of the density values (between 5.5 and 6.2 g/cm³) on the composition was observed. On the basis of the chemical composition and density measurements the number of nickel and sulfur atoms in 1 cm³ were determined. It has been shown that the Ni₃S₂ phase is defected in both anion and cation sublattices and that its chemical formula may be described as follows: Ni_3±yS_2x, where y 2x. It has been found that in the mixture containing 10% H₂S the process of defect formation is determined by their diffusion in the sulfide. The temperature dependence of the diffusion coefficient is described by the equation D = 13.15 exp(-30,000/RT) cm²/sec. No dependence of D on the sulfur partial pressure was observed, but this may be due to the relatively large uncertainties in the measurement of the diffusion coefficients.     

Q235B 热轧H型钢拉伸试验分层断口的显微分析

Q2 35B热轧H型钢拉伸试验后出现分层断口。用扫描电镜进行了显微观察 ,发现分层现象与试样中超长的带状组织密切相关。用能谱仪对断口分层处和超长铁素体带上的夹杂物进行了成分分析 ,证实都是硫化物。试样拉伸时在铁素体带上密集分布的硫化物处产生大量微裂纹 ,同时超长铁素体带的变形又受到阻碍 ,导致该处在试样拉断之前裂纹已经贯通 ,最终在断口上形成分层。因此 ,拉伸试验断口出现分层的原因是试样中存在密集分布的硫化物和超长的带状组织。     

含锑金精矿碱性硫化钠浸出锑研究与工业实践

为了回收含锑金精矿中的锑，减少锑对两段焙烧过程的影响，对浮选富集得到的含锑金精矿进行硫化钠碱性浸出锑研究。优化实验表明，在液固比1.5:1 (mL/g)，氢氧化钠用量20 g/L，硫化钠用量40 g/L，反应温度80℃，浸出30 min，锑浸出率可达98%以上。在此基础上，采用焙烧炉余热将电解贫液加温至80℃，对液固分离方式、锑电积阴阳极板和冷冻结晶装置进行工艺改造，使锑的浸出率>98%、阴极锑纯度>95%，日产锑量增加17.35%。