Na2CO3催化焙烧法回收CuS中的铜

用Ｎａ２ＣＯ３催经焙烧法将ＣｕＳ转化为Ｃｕ．最佳的转化条件；反应温度为７５０℃，ＣｕＳ：Ｎａ２ＣＯ３（摩尔比）为１：２，在空气中反应９０ｍｉｎ，ＣｕＳ的转化率可达到９９％。     

含有机硫废碱液的综合利用

采用ＣｕＯ沉淀剂与含有机硫废碱液进行固液反应,经过滤回收ＮａＯＨ,碱液中的有机硫由滤渣吸附除去,灼烧滤渣得到的ＣｕＯ可循环使用,并可得到副产品Ｎａ２Ｓ２Ｏ５。最佳的试验条件为;Ｃｕ：Ｓ＝１．５６;１,反应温度２０－３０℃,反应时间３０ｍｉｎ,滤渣灼烧温度９００－９５０℃,灼烧时间３０ｍｉｎ。     

一种将SO_2转化为元素S的新工艺

一种将ＳＯ＿２转化为元素Ｓ的新工艺ＣｈｅｍｉｃａＩＥｎｇｉｎｅｅｒｉｎｇ，１０１［３］，２５（１９９４）劳伦斯贝克莱实验室（ＬＢＬ，加利福尼亚）开发了一种经济的净化烟道气中ＳＯ＿２的工艺，可将浓缩后的ＳＯ＿２催化转化为元素Ｓ。ＳＯ＿２主要来自燃煤发电...     

用废甲醇催化剂制备活性氧化锌和五水硫酸铜

用ＮＨ４Ｃｌ和Ｈ２ＳＯ４为浸取剂，络合浸取废甲醇催化中的ＺｎＯ和ＣｕＯ，以制备活性ＺｎＯ和ＣｕＳＯ４．５Ｈ２Ｏ。浸取ＺｎＯ的适宜条件为：温度８５－１００℃，ＮＨＣｌ投加量为理论量的１．９－２．１倍，浸取时间为２０ｍｉｎ。     

含Cu,Ni泥渣的回收利用

含Ｃｕ、Ｎｉ泥渣的回收利用１前言新乡市第一化工厂在生产工业ＮｉＳＯ＿４的过程中，排出大量含Ｎｉ、Ｃｕ的泥渣，其主要成分的含量（ｗｔ）如下：Ｎｉ２５．００％，Ｆｅ１９．２５％，Ｃｕ１５．１２％，此外，还含有少量的Ｃｏ、Ｃａ、Ｃ、Ｓｉ等元素。由于其成份复...     

臭氧氧化法处理染料中间体1－氨基蒽醌和DSD酸生产废水

采用臭氧氧化法处理染料中间体１－氨基蒽醌和ＤＳＤ酸生产废水，能改善废水的可生化性，降低废水中有机物的水溶性，提高混凝处理的效率。研究结果表明，在原水ｐＨ条件下，当臭氧投加量为７．５ｇ／Ｌ时，ＤＳＤ酸氧化母液脱色率大于９０％，ＢＯＤ＿５／ＣＯＤ达到０．３。当臭氧投加量为６ｇ／Ｌ时，１－氨基蒽醌废水的ＢＯＤ＿５／ＣＯＤ达到０．３。１－氨基蒽醌废水经投加量为２．５ｇ／Ｌ的臭氧处理后，再进行两级混凝处理（ＦｅＳＯ＿４的投加量分别为５．０ｇ／Ｌ和１．０ｇ／Ｌ），ＣＯＤ和色度的去除率可分别达到９０％和９３％。     

增敏碘量法同时测定微量Mn(Ⅱ)、 Mn(Ⅶ)、 Cr(Ⅲ)、 Cr(Ⅵ)

介绍了用增敏碘量法同时测定微量的Ｍｎ（Ⅱ）、Ｍｎ（Ⅶ）、Ｃｒ（Ⅲ）和Ｃｒ（Ⅵ）。将样品中的Ｍｎ（Ⅶ）和Ｃｒ（Ⅵ）用Ｎａ２ＳＯ３预先还原,在ｐＨ为３．０的醋酸盐介质中对Ｍｎ（Ⅱ）和Ｃｒ（Ⅲ）用过量ＫＩＯ４氧化（当用Ｈ２Ｐ２Ｏ２－７掩蔽Ｃｒ（Ⅲ）时,只有Ｍｎ（Ⅱ）被氧化）,过剩的ＩＯ－４用钼酸盐掩蔽,加入ＫＩ后,以Ｎａ２Ｓ２Ｏ３滴定游离出的Ｉ２。此法对Ｍｎ的测定范围为２９～１４７０６μｇ／Ｌ,相对标准偏差为０．３１％～１．１８％;对Ｃｒ的测定范围为５９～１０２９４μｇ／Ｌ,相对标准偏差为０．３６％～１．１２％。此法与常规滴定法测定Ｍｎ和Ｃｒ相比,分别可增敏２０倍和１２倍     

用双功能催化剂由CO_2直接合成烃类物质

用双功能催化剂由ＣＯ＿２直接合成烃类物质，３８［９］，３（１９９３）日本工业技术院大阪工业技术研究所，使用新开发的双功能催化剂，由ＣＯ＿２直接合成烃类物质的实验获得成功。过去是先用催化加氢法由ＣＯ＿２合成甲醇，然后再将甲醇转变成烃。在此过程中，烃的转...     

高铁酸钾的合成及其在水处理中的应用

高铁酸钾（Ｋ２ＦｅＯ４）是一种比ＫＭｎＯ４、Ｏ３和Ｃｌ２的氧化能力更强的强氧化剂，有关其合成和应用的研究早已引起人们的关注。特别是在水处理方面，与含氯型水处理剂相比，Ｋ２ＦｅＯ４不会引起二次污染，而且其分解产物Ｆｅ（ＯＨ）３还有絮凝作用，所以Ｋ２ＦｅＯ４是比较理想的水处理剂。１　合成试验及纯度分析１．１　合成试验Ｋ２ＦｅＯ４的合成方法有次氯酸盐法、电解法、过氧化物高温氧化法等。我们选择了在实验室易于实现的次氯酸盐氧化法，即在ＮａＣｌＯ溶液中加入Ｆｅ（ＮＯ３）３·９Ｈ２Ｏ固体，在２０℃左右进行反应…     

燃煤烟气中SO_2和NO_x的处理

燃煤烟气中ＳＯ＿２和ＮＯ＿ｘ的处理省，４５［１１］，７５（１９９３）加拿大的瓦特尔卢大学等单位共同开发出一种去除燃煤烟气中ＳＯ＿２和ＮＯ＿ｘ的新工艺，ＳＯ＿２和ＮＯ＿ｘ的去除率分别达到９５％和７５％。采用该工艺处理燃煤烟气的费用较现用的催化还原脱硫工...     

用废杂铜制备碱式碳酸铜

以废杂铜为原料,用稀硝酸浸出硝酸铜溶液,与碳酸氢钠反应得到碱式碳酸铜粗品,漂洗后得到高纯度碱式碳酸铜。实验结果表明,废杂铜与质量分数为30％的硝酸反应,开始比较平缓,后期反应剧烈,有少量红棕色的NO：生成,采用碱液吸收方式处理生成的NO：可减少其对大气的污染。碳酸氢钠与硝酸铜进行合成反应,反应温度50～80℃,反应液pH6．5～7．0,产品中铜的质量分数为55％-56％,产品质量较好。     

利用含铜蚀刻废液生产碱式碳酸铜

介绍了利用含铜蚀刻废液生产碱式碳酸铜的生产工艺、技术特点、工艺流程和产品质量。以碳酸钠作蚀刻废液的除杂剂,对其进行除杂前处理,控制反应液的pH为3．5～4．0、反应液中碳酸钠的浓度为0．02～0．03mol／L。可除去其中大部分杂质。用碳酸钠与含铜溶液中的铜进行合成反应,控制反应温度为70～80℃、pH为8～9、碳酸钠和含铜溶液中铜的浓度均为1mol／L,反应生成碱式碳酸铜,此产品中铜的质量分数为56％,产品质量优于木材防腐用碱式碳酸铜国内外同类产品。     

铜基钯镍退镀液中铜的再生利用

采用硫氰酸盐沉铜法回收铜基钯镍退镀液中的铜。沉铜的优化工艺条件为初始Cu~(2+)质量浓度3.84 g/L、Cu~(2+)与Na SCN及Na_2SO_3摩尔比1∶4∶0.6、沉铜反应温度30℃,陈化时间24 h,沉铜反应后退镀液中Cu~(2+)残留量仅为0.025 mg/L。在此条件下加入聚乙二醇1.5 g/L,并提高分散液温度至50℃,可制得平均粒径为0.472μm的CuSCN超细粉体。CuSCN粉体为类球形,为含α、β两种晶型的混晶。     

Biosorption of copper from aqueous solutions utilizing agricultural wastes

The purpose of this study was to determine the copper (Cu) biosorption capacities of several agricultural wastes from aqueous solutions. Samples of agricultural wastes were tested unaltered and after hydrochloric acid (HCl) treatment. Additional parameters tested include sample dose, contact time, particle size, mixing temperature, and the concentrations and pH of the Cu solutions. Desorption studies were performed to determine if the removed Cu could be recovered. In addition, tests were conducted to determine if the agricultural waste samples (AWS) could be reused for additional Cu biosorption cycles. The results of this study demonstrate a wide range of Cu biosorption proficiencies ranging from 0% to 100% removal. The parameters that resulted in higher Cu removal include higher pH and lower Cu solution concentration. Desorption results showed a 58% to 86% Cu recovery rate. Three of the five reused AWS were effective at removing Cu during subsequent trials. Therefore, these AWS types can be reused for additional Cu biosorption cycles. Hence, it is possible that using those AWS for metal treatment could reduce hazardous waste disposal inefficiencies and costs by avoiding disposing of spent AWS following each Cu biosorption cycle.     

A Comparison Between Corrosion Rates and Runoff Rates from New and Aged Copper and Zinc as Roofing Material

Recently there has been anincreased environmental concern in severalcountries in Europe, in particular in Sweden andin the Netherlands regarding the amount of copperand zinc that is released from building materialsinto society. Due to lack of runoff data, thelegislators have so far used corrosion ratesmeasured during the last 20 years to calculatequantities of metal released from buildingsassuming that the quantity of metal corrosionequals the quantity of metal runoff. Withdecreasing levels of environmental pollutantsduring the last decade in Europe, it is importantto determine more recent and hence morerepresentative corrosion and runoff rates to beused in the calculations. For this reason a field exposure program was implemented during 48 weeks in an urbanatmosphere in Sweden determining corrosion andrunoff rates for copper and zinc of differentage. New copper exposed for 48 weeks in the urbanatmosphere shows a corrosion rate of 6.7gm^-2y^-1 and an almost constant runoff rate of1.3 gm^-2y^-1 during the period. Therunoff rate is significantly lower than thecorrosion rate and represents only a fraction(20%) of the total amount of corroded metalduring this period. Zinc shows a graduallydecreasing corrosion rate with time being 5.0gm^-2y^-1 after 48 weeks of exposure. Therunoff rate is relatively stable with an averagerate of 3.1 gm^-2y^-1 during the sameperiod. This value represents 60% of the totalamount of corroded zinc. The effect of panel age has been investigatedin parallel field and laboratory studies. Theresults show that naturally aged copper exhibitssomewhat higher average runoff rates (2 gm^-2y^-1) than new copper, probably due to acombined effect of storage and weatherconditions. No significant difference in runoffrate can be found between new and naturally agedzinc. The field and laboratory investigationsshow that precipitation rate and amount influence the magnitude of the runoff rate forboth copper and zinc.     

未知含铜物料固体废物属性鉴别研究

以某未知样品为研究对象,综合样品外观及物理、化学等特性,分析得出样品具有和铜冶炼渣一致的特征,含有特征物相——铁橄榄石,成分与铜精炼炉渣类似,而且其碳含量较高,含有少许金属铜,可以判断样品为铜;台炼渣。经过破碎、研磨、浮选得篓Ⅱ精炼渣（铜精矿）,可作为炼铜原料投入生产。     

Digital Air Photo Processing for Mapping of Copper Roof Distribution and Estimation of Related Copper Pollution

Emission of metals in the urbanenvironment is a growing concern throughout theworld. In order to identify metal emissionssources in the Stockholm metropolitan region, amethod for detailed mapping of roof coatings andother urban land covers has been developedconducted. High accuracy area calculation ofcopper roof coatings based on scanned aerialphotography was used. The geometric resolution ofthe digital photographs was 0.4 metre. Imagelayers with identified copper roof objects weremerged with a digital elevation model of 1 metregeometric resolution. The slope gradient for eachroof was calculated in order to account for slopein the calculation of roof areas. In total,622,590 m² of copper roofs were accounted,of which 176,845 m² and 447,745 m²represent new and patinated copper respectively.The number of copper roofs larger than 1,000m² was 142. Applying corrosion and runoffrates on these figures, a yearly Cu flux ofapproximately 1,200 kg in Stockholm may bederived from copper coated building.     

废杂铜回收利用工艺技术现状及展望

随着社会经济的发展,铜生产和消费的矛盾日益突出。废杂铜作为一种再生资源,其回收利用不仅能够缓解我国铜矿资源缺乏的现状,而且也符合国家当前节能减排和环保的要求。概述了废杂铜的回收分类和生产工艺技术现状,并对今后的发展趋势进行了展望。     

酸性氯化铜蚀刻废液一步沉淀法制备碱式碳酸铜

以酸性氯化铜蚀刻废液为原料,在Na₂CO₃和助剂A存在下,采用一步沉淀法制备碱式碳酸铜。考察了反应pH、n（Na₂CO₃）∶n（助剂A）、反应时间和反应温度对碱式碳酸铜制备效果的影响,并采用XRD、TG 及SEM对产品进行了表征。实验结果表明：在反应pH 7.0、沉淀剂配比n（Na₂CO₃）∶n（助剂A）=1∶2、反应时间1.0 h、反应温度70 ℃的条件下,产品的w（Cu²⁺）达55.62%,w（Cl^-）为0.013%,符合HG/T 4825—2015《工业碱式碳酸铜》的要求;蚀刻废液中Cu²⁺的回收率接近100%。表征结果表明,制得的产品为单一组分CuCO₃·Cu（OH）₂,小颗粒为直径1.8~5.4 μm的不规则球形,团聚后的大颗粒呈姜块状形貌,粒径为48~75 μm。     

Copper Emissions from Fuel Combustion Consumption and Industry in Two Urban Areas 1900–1980

The type of energy system andindustrial structure of urban areas is veryimportant for the total amounts of Cu emitted.The total per capita emission for the New Yorkarea is estimated to be approximately 4 timeslarger than Stockholm municipality between 1900–1980. The latter was mainly the result of largedifferences in energy systems and industrialstructure. Hydro-electric power and non fossilfuels were important energy sources for Stockholmwhile coal was a much more significant fuel forthe New York area. Metal processing hascharacterised the industries of Stockholm whilethe New York area was a national centre forcopper and petroleum refining as well as thechemical industry. In both cases the estimated Cuemissions from fuel combustion and industrydecreased from 1900–1980. But in the case ofconsumption related emissions the time trendsdiffer between the two urban areas. In Stockholmend use was the largest category of Cu emissionsduring the whole time period studied. In the NewYork area consumption related emissions becamethe largest source of Cu emission in the 1950s.