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首页> 外文期刊>Hydrometallurgy >Electrowinning of antimony from model sulphide alkaline solutions
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Electrowinning of antimony from model sulphide alkaline solutions

机译:硫化物模型碱性溶液中锑的电积

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The influence of initial antimony concentration, cathode current density, concentrations of Na_2S and NaOH, gas sparging and electrolyte temperature on average cell voltage, specific energy and current efficiency of antimony deposition has been studied. The experiments were conducted in a nondiaphragm electrolytic cell. The anode and cathode were made in such a way that the anode current density was ten times higher than the cathode current density so that a vigorous production of oxygen is promoted at the anode with lesser amounts of polysulphide; and concurrently decreasing the propensity of producing hydrogen at the cathode. Increasing the initial concentration of antimony from 25 g/L to 45 g/L increased the current efficiency by 18%. The average cell voltage decreased from 2.78 V to 2.21 V when the electrolyte temperature was raised from 45 °C to 90 °C The results showed that increasing the sulphide concentration from 0.77 M to 1.92 M decreased the current efficiency by 13% due to the formation of polysulphide and thiosulphate ions which have negative effect on the current efficiency. Sparging of the electrolyte promotes a smooth and adherent antimony deposit; and the purity of deposited antimony was raised from 99.2% to 99.6%. The specific energy consumed per kilogram of deposited antimony decreased by 74% when the cathode current density was decreased from 250 to 50 A/m~2. Based on sulphate formation, anodic current efficiencies of 85% and 90% were obtained at sodium hydroxide concentrations of 8.75 M and 10 M, respectively. The preferred crystallographic orientations of the antimony deposit obtained at 2.5 M NaOH concentration are in the order (012) (202) (110) (104), but the order becomes (012) (110) (104) (202) when NaOH concentration is increased further. The order of crystal orientations for antimony electrodepo-sition at 50 A/m~2 cathodic current density is (012) (110) (104) (202), which does not change with increasing cathode current density but the peaks at (110) (104) (202) crystal planes become more broadened and suppressed as current density increased.
机译:研究了初始锑浓度,阴极电流密度,Na_2S和NaOH的浓度,气体喷射和电解液温度对平均电池电压,锑的比能和电流效率的影响。实验是在非隔膜电解池中进行的。以使阳极电流密度比阴极电流密度高十倍的方式制造阳极和阴极,从而用较少量的多硫化物促进阳极处的氧气的剧烈产生。并同时降低了在阴极产生氢的倾向。锑的初始浓度从25 g / L增加到45 g / L,电流效率提高了18%。当电解液温度从45°C升至90°C时,平均电池电压从2.78 V降低至2.21V。结果表明,硫化物的浓度从0.77 M增加至1.92 M,由于形成,电流效率降低了13%。多硫离子和硫代硫酸根离子对电流效率有负面影响。电解质的散布促进了锑沉积的顺滑和附着;沉积的锑的纯度从99.2%提高到99.6%。当阴极电流密度从250 A / m〜2降低到50 A / m〜2时,每千克沉积锑所消耗的比能降低了74%。基于硫酸盐的形成,在氢氧化钠浓度为8.75 M和10 M时,阳极电流效率分别为85%和90%。在2.5 M NaOH浓度下获得的锑沉积物的优选晶体学取向为(012)(202)(110)(104)的顺序,但当NaOH浓度为时,顺序为(012)(110)(104)(202)进一步增加。锑电沉积在50 A / m〜2阴极电流密度下的晶体取向顺序为(012)(110)(104)(202),其不随阴极电流密度的增加而变化,而是在(110)处的峰值(104)(202)的晶面随着电流密度的增加而变得更宽和受到抑制。

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