用氧化锌烟灰制备饲料级氧化锌

以锌冶炼厂氧化锌烟灰为原料,经NH3-NH4HCO3溶液浸取、Zn粉置换除杂、用自制偏钛酸吸附除A s等工序制备饲料级氧化锌。实验结果表明:氧化锌烟灰在NH3-NH4HCO3溶液中于40℃浸取2h,Zn浸出率可达96%~98%;当偏钛酸加入量为12.5g/L、吸附1h时,产品中A s的质量分数低于0.000 3%。采用该工艺制得的饲料级氧化锌符合HG/T2792—1996《饲料添加剂氧化锌》的质量标准。     

用含锌废催化剂制备纳米氧化锌

以含锌废催化剂为原料,经酸浸、除杂、锌粉置换、合成等工艺制得碱式碳酸锌,再经过滤、洗涤、干燥、煅烧制备纳米氧化锌。考察了酸浸工艺硫酸溶液含量和液固比(硫酸与含锌废催化剂的质量比)对锌浸出率的影响,以及煅烧温度对纳米氧化锌质量的影响。实验结果表明:在硫酸质量分数为30%、液固比为5的最佳酸浸工艺条件下,锌浸出率为92%;在最佳煅烧温度为400℃的条件下,氧化锌质量分数大于95%,比表面积大于50 m2/g;纳米氧化锌颗粒大小均匀,平均粒径小于50 nm。     

用含锌废催化剂制备纳米氧化锌

以含锌废催化剂为原料，经酸浸、除杂、锌粉置换、合成等工艺制得碱式碳酸锌，再经过滤、洗涤、干燥、煅烧制备纳米氧化锌。考察了酸浸工艺硫酸溶液含量和液固比（硫酸与含锌废催化剂的质量比）对锌浸出率的影响，以及煅烧温度对纳米氧化锌质量的影响。实验结果表明：在硫酸质量分数为30%、液固比为5的最佳酸浸工艺条件下，锌浸出率为92%；在最佳煅烧温度为400 ℃的条件下，氧化锌质量分数大于95%，比表面积大于50 m²/g；纳米氧化锌颗粒大小均匀，平均粒径小于50 nm。     

利用含砷氧化锌尘制备活性氧化锌

用NH3-（NH4）2SO4溶液浸取处理含砷氧化锌尘,可彻底清除砷,制备出合格的活性氧化锌。对于含砷质量分类为1%-2%的原料,产品中所含砷质量分数可降至0.0005%以下。该方法具有除砷彻底,不易产生二次污染的优点,为含砷氧化锌尘的综合利用提供了一种新方法。     

氧化锌脱硫技术研究进展

在分析了无机硫化物、有机硫化物脱硫机理的基础上,着重探讨了氧化锌脱硫技术存在的问题及国内外的研究现状。针对氧化锌脱硫剂在中温、高温脱硫时稳定性较差、低温硫容低、再生温度高导致脱硫活性下降、脱硫过程未实现无害化等问题,提出了研制纳米氧化锌脱硫剂是提高氧化锌脱硫技术水平的研究方向。     

立足技术改造,积极治理“三废”,搞好综合利用

无锡市大众化工厂生产印染还原剂保险粉及氧化锌。年产保险粉4000吨、氧化锌800吨左右。在保险粉的生产过程中有大量二氧化硫气体、氧化锌的锌渣及含碱的饱和盐水排出,同时,生产氧化锌也产生大量粉尘,环境污染极为严重。因此,我们深刻认识到,一定要积极主动地治理“三废”、把“三废”消灭在生产过程中。     

从废干电池回收锌生产纳米氧化锌粉

说明了废旧电池的危害,提出了对废旧干电池中锰粉、碳棒、铜帽、锌皮等可再利用资源的回收利用方法.着重介绍了从锌皮制取纳米级氧化锌的优惠工艺条件,对所制得的氧化锌产物进行的X射线衍射分析和TEM分析,表明所得的产品为高纯纳米氧化锌粉.进而指出了纳米氧化锌粉在橡胶工业、陶瓷材料以及高科技磁性材料产品中的用途.     

用废气中的硫化氢制硫化锌

在以重晶石（ＢａＳＯ４）为原料、用碳化法生产碳酸钡的过程中,排放含硫化氢的尾气。硫化氢是一种具有恶臭的有毒气体,在我国工业企业设计卫生标准中规定居住区大气中硫化氢最高容许浓度为００１ｍｇ／ｍ３。我们进行了以氧化锌为原料制成吸收液吸收尾气中的硫化氢,制造ＺｎＳ的试验研究。ＺｎＳ可用于生产锌钡白。１　试验１１　主要仪器、试剂与材料ＰＨＳ４型酸度计,ＷＺＧ２００型光电光谱仪。氧化锌矿粉（ＺｎＯ质量分数８６８％）,硫酸（化学纯）,氢氧化钠（化学纯）。１２　试验方法１２１　氧化锌的溶解将氧…     

用氮肥厂的废氧化锌脱硫剂生产七水硫酸锌

介绍利用氮肥厂的废氧化锌脱硫剂生产七水硫酸锌的方法，该方法具有工艺简单，操作方便，产品质量好的特点，并可减少环境污染，变废为宝，具有较好的经济效益。     

环境监测中气象仪器的防雷问题

本文根据美国经验,并结合我国有关资料介绍环境监测中杆、塔上气象仪器及其数据处理装置的防雷经验,气象杆、塔避雷针的设计、安装以及氧化锌压敏变阻器的使用方法.     

Study of the presence of fluorine in the recycled fractions during carbothermal treatment of EAF dust

Carbothermal treatment tests of electric arc furnace dusts (EAFD) using the Waelz kiln process were carried out in pilot-scale for the production of zinc oxide. The association of halides in the EAFD, and the recycled products, such as zinc oxide fumes and high-grade iron contents fractions were examined by X-ray diffraction (XRD), scanning electron microscope (SEM) and transmission electron microscope (TEM) analysis. XRD reveals the presence of chlorine and fluorine in the dusts in the form of KCl, NaCl and CaF2. An ultra-pure fraction of zinc was obtained after the Double Leaching Waelz Oxide (DLWO) process was performed on the zinc oxide fumes. The halide contents were reduced to approximately 100 ppm Cl and 700 ppm F. The rest of these elements are in the form of CaF2. About 65% F is volatilised as lead and zinc fluorides, 15% is expected in the magnetic fractions and 20% in non-magnetic fractions as CaF2 and MnF2, respectively.     

氨浸出含锌烟尘制取活性氧化锌

采用氨浸出法处理含锌烟尘,浸出液在微波-超声波联合作用下蒸氨得碱式碳酸锌沉淀,再经煅烧制得活性氧化锌.实验结果表明:在总氨浓度为9.0 mol/L、浸出温度为40 ℃、浸出液初始pH为 11.0～11.5、搅拌转速为400 r/min、浸出剂体积与含锌烟尘质量比为4、浸出时间为60 min的浸出条件下,锌的浸出率为83.3%.浸出液经过两段净化除杂后,在超声波功率50 W、微波辐射(微波功率随温度的设定而自动变化)的联合作用下,使溶液体系恒温90 ℃,进行蒸氨,沉淀得到前驱体碱式碳酸锌,经煅烧,得到平均直径为0.4 μm、晶型为六方晶系、片状的活性氧化锌.     

Zinc removal from synthetic waters using magnetite/graphene oxide composites

The removal of heavy metals from wastewater has become a global challenge, which demands the continuous study of efficient and low-cost treatment alternatives such as adsorption. In this research, the removal of zinc was evaluated using batch adsorption processes with nonconventional materials such as graphene oxide (GO), magnetite (MG), and their composites (GO:MG), formulated with three weight ratios (2:1, 1:1, and 1:2). Graphene was synthesized by the modified Marcano method, using pencil lead graphite as a precursor. MG and the composites were synthesized by chemical coprecipitation of ferrous sulfate and ferric chloride. The materials were characterized by Raman and Fourier transform infrared spectroscopies, scanning electron microscopy, X-ray diffraction, and the Brunauer–Emmett–Teller method to determine the functional groups, microstructural and morphological characteristics, and specific surface area. Batch adsorption tests were carried out to optimize the adsorbent dose and contact time with zinc solutions of 10 ppm. Zinc adsorption reached equilibrium at 2 h, with an optimal dose between 0.25 and 1.0 g/L. The maximum zinc removal efficiencies/adsorption capacities were 98.6%/165.6, 83.4%/47.6, 83.5%/21.9, 72.8%/19.9, and 82.2%/9.25 mg/g using GO, 2GO:1MG, 1GO:1MG, 1GO:2MG, and MG, respectively. Furthermore, the analysis of the isotherm and adsorption kinetics models determined that the adsorption processes using MG and the composites fit the Sips and pseudo-second-order models.     

Recovery of yttrium from fluorescent powder of cathode ray tube,CRT: Zn removal by sulphide precipitation

This work is focused on the recovery of yttrium and zinc from fluorescent powder of cathode ray tube (CRT). Metals are extracted by sulphuric acid in the presence of hydrogen peroxide. Leaching tests are carried out according to a 2² full factorial plan and the highest extraction yields for yttrium and zinc equal to 100% are observed under the following conditions: 3 M of sulphuric acid, 10% v/v of H₂O₂ concentrated solution at 30% v/v, 10% w/w pulp density, 70 °C and 3 h of reaction.Two series of precipitation tests for zinc are carried out: a 2² full factorial design and a completely randomized factorial design. In these series the factors investigated are pH of solution during the precipitation and the amount of sodium sulphide added to precipitate zinc sulphide. The data of these tests are used to describe two empirical mathematical models for zinc and yttrium precipitation yields by regression analysis. The highest precipitation yields for zinc are obtained under the following conditions: pH equal to 2–2.5% and 10–12% v/v of Na₂S concentrated solution at 10% w/v. In these conditions the coprecipitation of yttrium is of 15–20%.Finally further yttrium precipitation experiments by oxalic acid on the residual solutions, after removing of zinc, show that yttrium could be recovered and calcined to obtain the final product as yttrium oxide. The achieved results allow to propose a CRT recycling process based on leaching of fluorescent powder from cathode ray tube and recovery of yttrium oxide after removing of zinc by precipitation. The final recovery of yttrium is 75–80%.     

Recovery of metal values from zinc solder dross

Zinc solder dross containing 14.8% Sn, 16.3% Pb, 0.41% Al and 64.5% Zn was leached with 3% H₂SO₄ at 45°C for 1 h. Zinc and aluminum went into solution, whereas lead and tin remained with the residue. Aluminum was selectively precipitated as calcium aluminum carbonate by treating the sulphate leachate with limestone at pH 4.8. Zinc sulphate solution was either evaporated to obtain zinc sulphate crystals or precipitated as basic zinc carbonate at pH 6.8. The undissolved lead and tin were leached with 5 M hot hydrochloric acid. The major part of lead chloride ( 73%) was separated by cooling the leached products down to room temperature. From the soluble fraction, tin was recovered as hydrated tin oxide by alkylation with caustic soda at pH 2.4, while the remaining lead was separated at pH 8.5 as lead hydroxide. A process flowsheet had been suggested which involved two-stage hydrometallurgical treatment. Parameters affecting the recovery efficiency of the suggested method such as temperature, time, pH and acid: solid stoichiometric ratio were investigated. Results obtained revealed that the optimum leaching conditions were achieved by using 20 ml of 3% H₂SO₄ acid/g dross for 1 h at 45°C. Recovery efficiency of the metal salts was 99.1, 99.4, 99.6 and 99.5% for Zn, Al, Pb and Sn respectively. Recovery efficiency was related to the solubility of the concerned salts under the given experimental conditions.     

Nylon recovery from carpet waste through pyrolysis under the presence of zinc oxide and the roll-milling treatment

Recycling of carpet waste is not extensively carried out because of its complex combination of materials. A representative type of carpet consists of three layers: nylon fibers, adhesives, and backing materials made of poly(vinyl chloride), PVC. Thermal treatment of carpet waste, thus, leads to the emission of hazardous chlorinated compounds. In the present work, we have employed the one-directional thermal treatment of the backing materials under the presence of zinc oxide, which promotes the thermal degradation of PVC. Nylon fibers could be effectively recovered by the consequent milling treatment from the brittle backing materials. The influence of process parameters, such as pyrolysis temperature and reaction time, on the separation efficiency is discussed.     

硫酸亚铁的综合利用

以工业废弃物硫酸亚铁为原料,加入碳酸氢铵和氯化钾,通过一系列化学反应和过滤、蒸发、煅烧等步骤,可制得硫酸钾、氯化铵、氧化铁红和液态二氧化碳.原料中各主要成分的利用率均达94%以上.     

Thermal treatment for recovery of manganese and zinc from zinc-carbon and alkaline spent batteries

The aim of this paper is the recovery of manganese and zinc from a mixture of zinc-carbon and alkaline spent batteries, containing 40.9% of Mn and 30.1% of Zn, after preliminary physical treatment followed by removal of mercury. Separation of the metals has been carried out on the basis of their different boiling points, being 357°C and 906°C the boiling point of mercury and zinc and 1564°C the melting point of Mn(2)O(3). Characterization by chemical analysis, TGA/DTA and X-ray powder diffraction of the mixture has been carried out after comminution sieving and shaking table treatment to remove the anodic collectors and most of chlorides contained in the mixture. The mixture has been roasted at various temperatures and resident times in a flow of air to set the best conditions to remove mercury that were 400°C and 10min. After that, the flow of air has been turned into a nitrogen one (inert atmosphere) and the temperatures raised, thus permitting the zinc oxide to be reduced to metallic zinc by the carbon present in the original mixture and recovered after volatilization as a high grade concentrate, while manganese was left in the residue. The recovery and the grade of the two metals, at 1000°C and 30min residence time, were 84% and 100% for zinc and 85% and 63% for manganese, respectively. The recovery of zinc increased to 99% with a grade of 97% at 1200°C and 30min residence time, while the recovery and grade of manganese were 86% and 87%, respectively, at that temperature. Moreover, the chlorinated compounds that could form by the combustion of the plastics contained in the spent batteries, are destroyed at the temperature required by the process.