有色金属科学与工程
有色金屬科學與工程
유색금속과학여공정
JIANGXI NONFERROUS METALS
2015年
1期
74-78
,共5页
张帅%曾怀远%张村%方夕辉
張帥%曾懷遠%張村%方夕輝
장수%증부원%장촌%방석휘
浮选银精矿%氰化法%硫代硫酸盐法%硫脲法%浸出率
浮選銀精礦%氰化法%硫代硫痠鹽法%硫脲法%浸齣率
부선은정광%청화법%류대류산염법%류뇨법%침출솔
silver concentrate%cyanide%thiosulfate%thiourea%leaching rate
对某浮选银精矿采用氰化法、硫代硫酸盐法、硫脲法进行银浸出实验,以评估3种不同浸出方法对该银精矿浸出效果.研究结果表明:在最优的工艺参数下[氰化法:碱预处理后加入铵盐,氰化钠浓度0.15 mol/L,pH值为11,液固比(浸出液体积与试样质量之比,单位是mL/g,下同)2∶1,搅拌强度500 r/min,浸出时间为48 h;硫代硫酸盐法:氧化焙烧预处理,氨水浓度1.0 mol/L,硫酸铜浓度0.01 mol/L,硫代硫酸钠浓度0.2 mol/L,pH值为10,液固比4∶1,搅拌强度500 r/min,浸出时间12 h;硫脲法:氧化焙烧和稀硫酸预浸处理,Fe3+浓度7.5×10-3 mol/L,硫脲浓度0.18 mol/L,pH=1.0,液固比为3∶1,搅拌速度250 r/min,浸出时间24 h],硫代硫酸盐方法获得的Ag浸出率为78.58%,硫脲相应获得的Ag浸出率为62.43%,比氰化法获得的浸出率低约3.33%.
對某浮選銀精礦採用氰化法、硫代硫痠鹽法、硫脲法進行銀浸齣實驗,以評估3種不同浸齣方法對該銀精礦浸齣效果.研究結果錶明:在最優的工藝參數下[氰化法:堿預處理後加入銨鹽,氰化鈉濃度0.15 mol/L,pH值為11,液固比(浸齣液體積與試樣質量之比,單位是mL/g,下同)2∶1,攪拌彊度500 r/min,浸齣時間為48 h;硫代硫痠鹽法:氧化焙燒預處理,氨水濃度1.0 mol/L,硫痠銅濃度0.01 mol/L,硫代硫痠鈉濃度0.2 mol/L,pH值為10,液固比4∶1,攪拌彊度500 r/min,浸齣時間12 h;硫脲法:氧化焙燒和稀硫痠預浸處理,Fe3+濃度7.5×10-3 mol/L,硫脲濃度0.18 mol/L,pH=1.0,液固比為3∶1,攪拌速度250 r/min,浸齣時間24 h],硫代硫痠鹽方法穫得的Ag浸齣率為78.58%,硫脲相應穫得的Ag浸齣率為62.43%,比氰化法穫得的浸齣率低約3.33%.
대모부선은정광채용청화법、류대류산염법、류뇨법진행은침출실험,이평고3충불동침출방법대해은정광침출효과.연구결과표명:재최우적공예삼수하[청화법:감예처리후가입안염,청화납농도0.15 mol/L,pH치위11,액고비(침출액체적여시양질량지비,단위시mL/g,하동)2∶1,교반강도500 r/min,침출시간위48 h;류대류산염법:양화배소예처리,안수농도1.0 mol/L,류산동농도0.01 mol/L,류대류산납농도0.2 mol/L,pH치위10,액고비4∶1,교반강도500 r/min,침출시간12 h;류뇨법:양화배소화희류산예침처리,Fe3+농도7.5×10-3 mol/L,류뇨농도0.18 mol/L,pH=1.0,액고비위3∶1,교반속도250 r/min,침출시간24 h],류대류산염방법획득적Ag침출솔위78.58%,류뇨상응획득적Ag침출솔위62.43%,비청화법획득적침출솔저약3.33%.
The leaching experiments are performed on samples collected from a silver concentrate with cyanide, thiosulfate and thiourea solutions respectively to compare their extraction effects. The result indicates that, under the optimal process parameters, (Cyanide: ammonium salt added on the pretreated alkali, sodium cyanide concentration being 0.15 mol/L, pH value being 11, liquid-solid rate 2∶1, mixing strength 500 r/min, leaching time 48 h; Thiosulfate: oxidizing roasting pretreatment, ammonia concentration of 1.0 mol/L, copper sulfate concentration of 0.01 mol/L, sodium thiosulfate concentration of 0.2 mol/L, pH of 10, liquid-solid rate of 4∶1, mixing strength of 500 r/min, leaching time of 12 h;Thiourea:oxidizing roasting and then dilute sulphuric pretreatment acid pre-leaching, Fe3+ concentration of 7.5 ×10-3 mol/L, thiourea concentration of 0.18 mol/L, pH of 1.0, liquid-solid rate of 3∶1, mixing strength of 250 r/min, leaching time of 24 h], the leaching rate of Ag with the method of thiosulfate is 78.58 %, while the rate in the thiourea system is about 62.43%, 3.33%lower than that in the cyanide system.