锡铜铅铁多元合金的氯化分离

含有锡铜铅锌的鼓风炉水淬渣经矿热电炉还原熔炼产出锡铜铅铁多元合金.用氯气浸出该合金,以硫酸铅的形式分离出铅,合金粉还原铜产出海绵铜,中和水解分离锡和铁,进而实现锡铜铅铁多元合金的有效分离.     

火焰原子吸收法测定底质中总铜,铅,锌,镉,铬的探讨

采用样品一次消解，直接火焰原子吸收法测定底质中总铜，铅，锌，镉，铬，测定方法的相对偏差≤４．５％，加标回收率为９１．８％－１０６．０％，标准参考样的测定值符合要求。     

中和—絮凝法回收硝酸型退锡废水中的锡

将传统的中和法和絮凝法相结合,采用中和—絮凝法回收硝酸型褪锡废水中的锡,考察了反应终点体系pH、碱液浓度、絮凝剂浓度等因素对锡回收效果的影响。实验结果表明,在NaOH溶液浓度为6 mol/L、反应终点体系pH为0.8、聚丙烯酰胺溶液质量浓度为3 g/L的工艺条件下,可得到干基锡含量54.6%（w）的高品位锡泥。与传统的单一中和/絮凝法相比,采用中和—絮凝法不仅可以有效提高生产效率,而且减少了碱液和絮凝剂用量,回收锡之后体系中大量的硝酸可进一步回收利用。     

废合金刀头中锡的回收利用工艺研究

探讨了废合金刀头中锡的回收利用工艺。使用三氯化铁和盐酸的混合液溶解刀头,以还原铁粉置换出铜后,添加1倍量的三氯化铁氧化Sn^(2+),使用5%的氢氧化钠以6 mL/min的速度调节溶液pH值为1.10,可较好地沉淀出锡。回收所得锡泥可供锡产业链相关厂家作为原料使用。     

氰化钠生产中聚合废料的利用

对氰化钠生产中的聚合废料进行了吸附试验和氰化钠含量分析，试验结果表明，聚合废料中含有２８％左右的氰化钠，其中黑褐色杂质可用活性炭吸附脱除。生产规模试验证明，用聚合废料为原料生产的硫氰酸钠，产品质量可达到装置设计指标，满足腈纶装置的使用要求。     

火焰原子吸收光度法测定水中铝的方法改进

研究了在盐酸介质中，壬基酚聚氧乙烯-7醚（NP-7）活化下，火焰原子吸收光度法测定环境水体中铝的方法改进。在25mL容量瓶中，加入5．0mL体积分数为50％的盐酸、2．0mL质量浓度为0．01g／mL NP-7和4．0mL质量浓度为75．0μg/mL的铝标准溶液，在原子吸收分光光度计的最佳测定条件下测定吸光度。根据吸光度与铝质量浓度绘制了工作曲线，线性范围3．0～24．0μg/mL，检出限1．32μg/mL。该法用于环境水体中铝含量的测定，加标回收率为94．4％～101．4％，最大相对标准偏差5．8％，方法对比最大相对误差4．1％。     

流动注射-氢化物发生-原子吸收法测定土壤中微量砷

用混酸消解土壤试样，用体积分数为20％的盐酸作酸介质，质量分数为1．5％的硼氢化钾作还原剂，体积分数为1％的盐酸作载液，采用流动注射-氢化物发生三-原子吸收法定量测定土壤中的微劈砷。通过实验确定，在原子化温度为920℃、土壤中共存元素含量低于5mg／kg时对测定无干扰。该方法的榆出限为0．5μg/L，线性范嘲为5～100μg/L．相对标准偏差为0．89％，平均回收率达98．99％：     

钛基锡锑电极电催化氧化处理硝基苯废水

采用钛基锡锑(Sn-Sb/Ti)电极作为氧化阳极,不锈钢为阴极,电催化氧化降解废水中硝基苯。实验结果表明,处理硝基苯废水的最佳条件为:电流密度25 mA/cm~2;Na_2SO_4作为电解质,加入量15g/L;极板间距2 cm;溶液初始pH 6。在此最佳条件下,硝基苯去除率大于95%,TOC去除率大于80%,表明Sn-Sb/Ti阳极能有效去除废水中有机污染物。     

ICP-AES测定电镀污泥中的Ag,Cu,Ni

介绍了用王水消解-氨水浸取含银电镀污泥试样的预处理方法，并对试样预处理中的若干问题进行了讨论。研究了分别在碱性和酸性介质中用高频电感耦合等离子体-原子发射光谱（ICP-AES）仪直接测定污泥中Ag，Cu，Ni等金属元素的分析方法。实验结果表明：在选定的最佳仪器工作条件下，Ag，Cu，Ni，Al，Ca，Fe加标回收率为97％～105％，相对标准偏差小于1．5％。该方法简便、快速、准确，适用的试样测定含量范围为0．01％-12．5％（干基试样）。     

用废干电池制备锰锌铁氧体的方法

该发明提供了一种用废干电池制备锰锌铁氧体的方法：用挤压法使干电池破碎，装入蒸汞炉中热蒸，去除有害杂质汞及有机物后用硫酸浸出，99％以上的汞可以从废料中挥发并被蒸汞炉中的吸收液吸收；浸出液用水解法、置换法及流化法除杂，浸除后的废渣进行安全填埋，除杂后的清液用碳酸盐中和，中和后得到的沉淀经干燥焙烧，即可制得锰锌铁氧体粉体。该法简便易行、费用省、效益高，可有效回收废干电池中各种有价元素，     

Thermal and Flame Retardancy Behavior of Oil Palm Based Epoxy Nanocomposites

The aim of present study was to investigate the thermal properties and flame retardancy behavior of flame retardant (FR) epoxy nanocomposites from chemically treated (bromine water and tin chloride) oil palm empty fruit bunch (OPEFB) nano filler at different filler loading (1, 3, 5%). Thermal properties were evaluated through thermogravimetry analyzer, derivative thermogravimetry and differential scanning calorimetry. FR properties of nanocomposites are evaluated through UL-94 vertical burning test and limiting oxygen index (LOI). The functional group analysis of all composites was made by FTIR spectroscopy. Thermal analysis shows that degradation temperature of epoxy composites shifts from 370 to 410 °C and char yield also increases for 3% loading. Furthermore LOI value of 29% and UL-94 rating of V-0 with no flame dripping and cotton ignition, revealed that 3% oil palm nano filler filled epoxy nanocomposites display satisfactory flame retardancy. The superior flame retardancy of epoxy nanocomposites are attributed to the chemical reactions occurred in the gaseous phases and the profound synergistic flame retardation effect of tin with bromine in the treated nano OPEFB filler. All the epoxy nanocomposites displayed almost similar FTIR spectra with the characteristics metal-halogen bond supporting the synergism. Homogeneous dispersion of 3% oil palm nano filler act as highly effective combustion chain terminating agent compared with 1 and 5% nano OPEFB/epoxy nanocomposites.     

卤素法电镀锡阳极泥中锡的碱浸回收及动力学分析

以NaOH溶液为浸出剂,采用碱浸法回收卤素法电镀锡阳极泥中的锡,考察了浸出效果的影响因素,并对浸出过程的动力学进行了研究。实验结果表明:在NaOH质量浓度200 g/L、反应温度90℃、液固比6、反应时间240 min的最佳工艺条件下,锡的浸出率约为98%;最佳工艺条件下,浸出液中的氟离子对后续锌粉置换回收锡没有影响;在303.15~363.15 K范围内,该浸出过程主要受内扩散控制,反应活化能为9.725 k J/mol。     

Recovery of aluminium, nickel-copper alloys and salts from spent fluorescent lamps

This study explores a combined pyro-hydrometallurgical method to recover pure aluminium, nickel-copper alloy(s), and some valuable salts from spent fluorescent lamps (SFLs). It also examines the safe recycling of clean glass tubes for the fluorescent lamp industry. Spent lamps were decapped under water containing 35% acetone to achieve safe capture of mercury vapour. Cleaned glass tubes, if broken, were cut using a rotating diamond disc to a standard shorter length. Aluminium and copper-nickel alloys in the separated metallic parts were recovered using suitable flux to decrease metal losses going to slag. Operation variables affecting the quality of the products and the extent of recovery with the suggested method were investigated. Results revealed that total loss in the glass tube recycling operation was 2% of the SFLs. Pure aluminium meeting standard specification DIN 1712 was recovered by melting at 800 degrees C under sodium chloride/carbon flux for 20 min. Standard nickel-copper alloys with less than 0.1% tin were prepared by melting at 1250 degrees C using a sodium borate/carbon flux. De-tinning of the molten nickel-copper alloy was carried out using oxygen gas. Tin in the slag as oxide was recovered by reduction using carbon or hydrogen gas at 650-700 degrees C. Different valuable chloride salts were also obtained in good quality. Further research is recommended on the thermodynamics of nickel-copper recovery, yttrium and europium recovery, and process economics.     

Leaching studies for tin recovery from waste e-scrap

Printed circuit boards (PCBs) are the most essential components of all electrical and electronic equipments, which contain noteworthy quantity of metals, some of which are toxic to life and all of which are valuable resources. Therefore, recycling of PCBs is necessary for the safe disposal/utilization of these metals. Present paper is a part of developing Indo-Korean recycling technique consists of organic swelling pre-treatment technique for the liberation of thin layer of metallic sheet and the treatment of epoxy resin to remove/recover toxic soldering material. To optimize the parameters required for recovery of tin from waste PCBs, initially the bench scale studies were carried out using fresh solder (containing 52.6% Sn and 47.3% Pb) varying the acid concentration, temperature, mixing time and pulp density. The experimental data indicate that 95.79% of tin was leached out from solder material using 5.5M HCl at fixed pulp density 50g/L and temperature 90°C in mixing time 165min. Kinetic studies followed the chemical reaction controlled dense constant size cylindrical particles with activation energy of 117.68kJ/mol. However, 97.79% of tin was found to be leached out from solder materials of liberated swelled epoxy resin using 4.5M HCl at 90°C, mixing time 60min and pulp density 50g/L. From the leach liquor of solder materials of epoxy resin, the precipitate of sodium stannate as value added product was obtained at pH 1.9. The Pb from the leach residue was removed by using 0.1M nitric acid at 90°C in mixing time 45min and pulp density 10g/L. The metal free epoxy resin could be disposed-of safely/used as filling material without affecting the environment.     

Processing of copper anodic-slimes for extraction of valuable metals

This work focuses on processing of anodic slimes obtained from an Egyptian copper electrorefining plant. The anodic slimes are characterized by high concentrations of copper, lead, tin and silver. The proposed hydrometallurgical process consists of two leaching stages for the extraction of copper (H(2)SO(4)-O(2)) and silver (thiourea-Fe3+), and pyrometallurgical treatment of the remaining slimes for production of Pb-Sn soldering alloy. Factors affecting both the leaching and smelting stages were studied.     

介孔分子筛SBA负载CuO纳米颗粒去除H2S

采用超声波辅助浸渍法制备了一种新型SBA-15负载CuO纳米颗粒的复合介孔材料(SC)，使用氮吸附、XRD、透射电子显微镜、电感耦合等离子体发射光谱、X射线光电子能谱等方法对SC进行了表征。并考察了SC对H2S的去除效果。研究结果表明:SC仍为介孔材料，超声处理会使CuO纳米颗粒更均匀地分散在主体材料孔道内;SC具有六角形长程有序性，说明辅以超声处理的浸渍方法可维持介孔材料的高度有序性;CuO纳米颗粒主要存在于载体孔道内;脱硫反应后的试样(SC-E)仍保留六角形特征，与SC相比介孔有序性降低;当Cu质量分数为3.23%时，SC的H2S穿透吸附量高达278mg/g。     

Ammoniacal leaching and recovery of copper from alloyed low-grade e-waste

The paper concerns a hydrometallurgical method for selective recovery of copper from low-grade electric and electronic wastes. The following consecutive stages were proposed: smelting of the scraps to produce Cu–Zn–Ag alloy, leaching of the alloy in ammoniacal solution, and selective copper electrowinning. Cu–Zn–Ag alloy was a polymetallic and five-phase system. It was leached in chloride, carbonate, sulfate and thiosulfate solutions. This resulted in the separation of the metals, wherein metallic tin and silver as well as lead salts remained in the slimes, while copper and zinc were transferred to the electrolyte. Copper was selectively recovered from the ammoniacal solutions by the electrolysis, leaving zinc ions in the electrolyte. The best conditions of the alloy treatment were obtained in the ammonia–carbonate system, where the final product was copper of high purity (99.9 %) at the current efficiency of 60 %. Thiosulfate solution was not applicable for the leaching of the copper alloy due to secondary reactions of the formation of copper(I) thiosulfate complexes and precipitation of copper(I) sulfide, both inhibiting dissolution of the metallic material.     

Review of environmental aspects and waste management of stone cutting and fabrication industries

Iran is the second largest stockholder of construction stones with 10 % of world production ;and there are more than 4000 stone cutting and fabrication industries (SCFIs). In the processing of raw stones, a considerable part of stone is turned into waste. Generated wastes include excess parts of different stones and sludge. The present paper reviews the state of SCFIs waste management using multiple data sources including site, analysis of effluent and sludge samples, and conducting interviews with people who are involved in 286 SCFIs in Qom and Tabriz. The results revealed that currently almost 35 to 52.5 % of raw stones were converted to solid wastes depending on stone cutting and processing methods, type of stones and their quality, which seemed a high percentage. Also, the effluents between 0.8 and 2.8 m³ were generated per ton of processed stone. Based on the analysis of heavy metals with atomic absorption spectroscopy, sludge samples contained a considerable amount of Pb, Cu, Cr, and Cd. It was also found that the lack of specific recycling, reuse and disposal programs and suitable supervision has led to uncontrolled disposal of stone wastes and sludge in different areas. However, there are good opportunities for reuse and recycling of the SCFIs wastes.     

Volatilisation and oxidation of aluminium scraps fed into incineration furnaces

Ferrous and non-ferrous metal scraps are increasingly recovered from municipal solid waste incineration bottom ash and used in the production of secondary steel and aluminium. However, during the incineration process, metal scraps contained in the waste undergo volatilisation and oxidation processes, which determine a loss of their recoverable mass. The present paper evaluates the behaviour of different types of aluminium packaging materials in a full-scale waste to energy plant during standard operation. Their partitioning and oxidation level in the residues of the incineration process are evaluated, together with the amount of potentially recoverable aluminium. About 80% of post-consumer cans, 51% of trays and 27% of foils can be recovered through an advanced treatment of bottom ash combined with a melting process in the saline furnace for the production of secondary aluminium. The residual amount of aluminium concentrates in the fly ash or in the fine fraction of the bottom ash and its recovery is virtually impossible using the current eddy current separation technology. The average oxidation levels of the aluminium in the residues of the incineration process is equal to 9.2% for cans, 17.4% for trays and 58.8% for foils. The differences between the tested packaging materials are related to their thickness, mechanical strength and to the alloy.