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Cadmium Recovery and Recycling from Chemical Bath Deposition of CdS Thin Layers

机译:CdS薄层化学浴沉积中的镉回收和再循环

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Cadmium sulfide thin layers for polycrystalline solar cells are produced by chemical bath deposition (CBD). This process generates wastes containing mainly ammonia and cadmium. We have implemented and described in a previous paper a process to recover 90 percent of ammonia and to confine cadmium as a cake which is a mixture of cadmium sulfide and cadmium cyanamide. The present paper concerns cadmium recycling to the CBD step. The cake is first dissolved in a moderate sulfuric acid solution 0.2-0.5 mol/l mixed with hydrogen peroxide (about 1 mol/l). This last component must be used in large excess (molar ratio H_2O_2/Cd>=5) and must be completely removed from the solution before recycling or cadmium electrowinning. Hydrogen peroxide decomposition is electrochemically catalyzed by platinized platinum immersed into the solution. The resulting solution contains cadmium sulfate 0.2 mol/l, sodium and ammonium sulfate. One can either recycle it as a chemical bath, or recover the cadmium content by electrowinning; in this case the residual concentration of hydrogen peroxide is electrochemically reduced at the beginning of cadmium electrolysis. The raffinate solution is recycled into the stripping reactor. The pure cadmium metal recovered may be dissolved in a dilute sulfuric acid solution by means of internal electrolysis with two electrodes: a platinized platinum grid as cathode and the cadmium metal as anode. According to the mass of cadmium dissolved it is possible to obtain a concentrated solution of pure cadmium sulfate. The global process recovers at least 99.999 percent of cadmium and generates only solid sulfur and a liquid effluent containing traces of cadmium (<10 mu g/l).
机译:用于多晶太阳能电池的硫化镉薄层是通过化学浴沉积(CBD)生产的。该过程产生主要包含氨和镉的废物。我们已经在先前的论文中实施并描述了一种回收90%的氨并限制作为饼状物的镉的方法,该饼是硫化镉和氰胺化镉的混合物。本文涉及将镉回收到CBD步骤。首先将滤饼溶解在0.2-0.5 mol / l的适度硫酸溶液中,与过氧化氢混合(约1 mol / l)。最后一种组分必须大量使用(摩尔比H_2O_2 / Cd> = 5),并且必须在回收或镉电解沉积之前从溶液中完全除去。过氧化氢的分解是通过浸入溶液中的铂化铂进行电化学催化的。所得溶液包含0.2mol / l的硫酸镉,硫酸钠和硫酸铵。既可以将其作为化学浴进行回收,也可以通过电解沉积法回收镉含量。在这种情况下,过氧化氢的残留浓度在镉电解开始时就被电化学降低了。提余液循环到汽提反应器中。回收的纯镉金属可通过内部电解用两个电极溶解在稀硫酸溶液中:两个电极为镀铂金栅,阴极为镉金属。根据溶解的镉的质量,可以获得纯硫酸镉的浓缩溶液。全球流程至少回收了99.999%的镉,并且仅产生固体硫和含有微量镉(<10μg / l)的液体废水。

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