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首页> 外文期刊>資源と素材: 资源·素材学会志 >Separation and Recovery of Rare Earth Elements from Phosphor Sludge in Processing Plant of Waste Fluorescent Lamp by Pneumatic Classification and Sulfuric Acidic Leading
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Separation and Recovery of Rare Earth Elements from Phosphor Sludge in Processing Plant of Waste Fluorescent Lamp by Pneumatic Classification and Sulfuric Acidic Leading

机译:气动分类和硫酸致硫酸荧光灯加工厂中稀土元素的分离和回收稀土元素

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摘要

The classification and acidic leaching behaviors of phosphor sludge have been examined to establish the recycling system of rare earth components contained in fluorescent lamp waster. At first, separation characteristic of rare earth components and calcium phosphate in phosphor sludge was investigated by pneumatic classification. After pneumatic classification of phosphor sludge, rare earth components were leached in various acidic solutions and sodium hydroxide solution. For recovery of soluble component in leaching solution, rare earth component was recovered by treatment processes such as hydroxide and oxalate precipitations. The experimental results obtained are summarized as follows:(1) In classification process, rare earth components in phosphor sludge wee concentrated to 29.3 percent from 13.3 percent, and its yield was 32.9 percent.(2) In leaching process, sulfuric acidic solution was more effective one as a leaching solvent of rare earth components than other solutions. Yttrium and europium in phosphor sludge were dissolved in sulfuric acidic solution of 1.5 kmol/m~3 concentration, and other rare earth elements were rarely dissolved in leaching solution. The leaching degree of yttrium and europium were respectively 92 percent and 98 percent in following optimum leaching conditions; sulfuric acid concentration is 1.5 kmol/m~3, leaching temperature 343 K, leaching time 3.6 ks and pulp concentration 30 kg/m~3.(3) In recovery process, yttrium and europium could be recovered to above 99.1 percent by means of hydroxide treatment and oxalate precipitation method.(4) Yttrium and europium from phosphor sludge contained in fluorescent lamp waste were recovered effectively by three processes of pneumatic classification, sulfuric acid leaching and oxalate precipitation methods. Their recovery was finally about 65 percent, and its purity was 98.2 percent.
机译:已经研究了荧光粉污泥的分类和酸性浸出行为,建立了荧光灯料稀土元素的再循环系统。首先,通过气动分类研究了稀土成分和磷污泥中磷酸钙的分离特性。在磷光体污泥的气动分类后,在各种酸性溶液和氢氧化钠溶液中浸出稀土元素。为了回收浸出溶液中可溶性组分,通过处理方法如氢氧化物和草酸盐沉淀回收稀土组分。所获得的实验结果总结如下:(1)在分类过程中,磷污泥Wee的稀土元素浓缩至13.3%的29.3%,其收率为32.9%。(2)在浸出过程中,硫酸溶液更多作为稀土组分的浸出溶剂的有效溶剂,而不是其他溶液。 YTTRIUM和荧光体污泥中的铕溶解在1.5 kmol / m〜3浓度的硫酸溶液中,并且其他稀土元素很少溶解在浸出溶液中。下列最佳浸出条件下,钇和铕的浸出程度分别为92%和98%;硫酸浓度为1.5 kmol / m〜3,浸出温度343 k,浸出时间3.6 ks和纸浆浓度30kg / m〜3。(3)在回收过程中,钇和铕均可通过以下方式回收99.1%以上99.1%以上氢氧化物处理和草酸沉淀法。(4)荧光灯废物中含有荧光灯废物中含有的钇和铕的钇和铕和硫酸盐浸润和草酸沉淀方法。他们的康复终于达到了65%,其纯度为98.2%。

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