湿法冶金
濕法冶金
습법야금
HYDROMETALLURGY OF CHINA
2014年
2期
121-123
,共3页
曾斌%胡良辉%毛永星%余攀
曾斌%鬍良輝%毛永星%餘攀
증빈%호량휘%모영성%여반
二甲苯%湿法炼锌渣%硫%银%回收
二甲苯%濕法煉鋅渣%硫%銀%迴收
이갑분%습법련자사%류%은%회수
dimethylbenzene%zinc smelting residue%sulfur%silver%recovery
研究了用二甲苯浸出-焙烧-硫酸浸出杂质-氰化浸出银工艺从湿法炼锌渣中回收硫和银。试验结果表明:在反应温度95℃、反应时间15 min、液固体积质量比5∶1条件下用二甲苯浸出,硫浸出率为96.40%;分硫渣中加入1%氢氧化钠,在630℃下焙烧2 h ,然后用硫酸浸出锌、铁等杂质,控制液固体积质量比为4∶1,pH为1.0,反应温度为95℃,反应时间为3h;之后对硫酸浸出渣氰化浸出银,体系pH控制在9.5~11.5之间,液固体积质量比为3∶1,氰化钠质量浓度2.0g/L,浸出时间24h,银回收率为78.5%。
研究瞭用二甲苯浸齣-焙燒-硫痠浸齣雜質-氰化浸齣銀工藝從濕法煉鋅渣中迴收硫和銀。試驗結果錶明:在反應溫度95℃、反應時間15 min、液固體積質量比5∶1條件下用二甲苯浸齣,硫浸齣率為96.40%;分硫渣中加入1%氫氧化鈉,在630℃下焙燒2 h ,然後用硫痠浸齣鋅、鐵等雜質,控製液固體積質量比為4∶1,pH為1.0,反應溫度為95℃,反應時間為3h;之後對硫痠浸齣渣氰化浸齣銀,體繫pH控製在9.5~11.5之間,液固體積質量比為3∶1,氰化鈉質量濃度2.0g/L,浸齣時間24h,銀迴收率為78.5%。
연구료용이갑분침출-배소-류산침출잡질-청화침출은공예종습법련자사중회수류화은。시험결과표명:재반응온도95℃、반응시간15 min、액고체적질량비5∶1조건하용이갑분침출,류침출솔위96.40%;분류사중가입1%경양화납,재630℃하배소2 h ,연후용류산침출자、철등잡질,공제액고체적질량비위4∶1,pH위1.0,반응온도위95℃,반응시간위3h;지후대류산침출사청화침출은,체계pH공제재9.5~11.5지간,액고체적질량비위3∶1,청화납질량농도2.0g/L,침출시간24h,은회수솔위78.5%。
Recovery of silver and sulfur from zinc smelting residue by dimethylbenzene leaching sulfur -roasting-sulfuric acid leaching impurities-cyanide leaching silver process is investigated .T he result show that the leaching rate of sulfur is 96 .40% under the conditions of reaction temperature of 95 ℃ , reaction time of 15 min and the ratio between liquid volume and solid mass of 5 ∶ 1 .The roasting conditions of sulfur leaching residue are adding sodium hydroxide of 1% into the residue ,roasting temperature of 630 ℃ ,roasting time of 2 h .T he conditions of leaching impurities using sulfuric acid are the ratio between of liquid volume and solid mass ,system pH of 1 .0 ,reaction temperature of 95℃ ,reaction time of 3 h .The cyanide leaching silver under the conditions of system pH of 9 .5-11 .5 , the ratio between liquid volume-solid mass of 3∶1 ,sodium cyanide concentration of 2 g/L ,reaction time of 24 h ,the leaching rate of silver is 78 .50% .