矿冶工程
礦冶工程
광야공정
2014年
5期
100-104
,共5页
褚亦功%赵洪冬%刘新刚%朱仁峰%顾帼华
褚亦功%趙洪鼕%劉新剛%硃仁峰%顧幗華
저역공%조홍동%류신강%주인봉%고귁화
低品位氧化铜矿%高碱度%氧化氨浸%三段浸出
低品位氧化銅礦%高堿度%氧化氨浸%三段浸齣
저품위양화동광%고감도%양화안침%삼단침출
low-grade oxidized copper ore%high alkalinity%oxidative leaching%three-stage leaching
以新疆滴水低品位氧化铜矿为研究对象,在( NH4)2 SO4?NH3浸出体系中分别考察了磨矿细度、浸出时间、总氨浓度、氧化剂用量、NH4+∶NH3比率等因素对铜浸出率的影响。最终确定最佳工艺条件为:磨矿细度-0.074 mm粒级占86%,反应温度25℃,搅拌转速200 r/min,一段浸出液固比2∶1,过硫酸铵0.15 mol/L,氨水浓度3 mol/L,硫酸铵浓度1.5 mol/L,搅拌浸出1.5 h,静置0.5 h;二段过硫酸铵、氨水和硫酸铵添加用量减半,继续搅拌浸出1.5 h,静置0.5 h;三段浸出药剂用量与二段浸出相同,搅拌浸出2 h,静置4 h完毕。该条件下,可获得铜浸出率大于86%的优良指标。
以新疆滴水低品位氧化銅礦為研究對象,在( NH4)2 SO4?NH3浸齣體繫中分彆攷察瞭磨礦細度、浸齣時間、總氨濃度、氧化劑用量、NH4+∶NH3比率等因素對銅浸齣率的影響。最終確定最佳工藝條件為:磨礦細度-0.074 mm粒級佔86%,反應溫度25℃,攪拌轉速200 r/min,一段浸齣液固比2∶1,過硫痠銨0.15 mol/L,氨水濃度3 mol/L,硫痠銨濃度1.5 mol/L,攪拌浸齣1.5 h,靜置0.5 h;二段過硫痠銨、氨水和硫痠銨添加用量減半,繼續攪拌浸齣1.5 h,靜置0.5 h;三段浸齣藥劑用量與二段浸齣相同,攪拌浸齣2 h,靜置4 h完畢。該條件下,可穫得銅浸齣率大于86%的優良指標。
이신강적수저품위양화동광위연구대상,재( NH4)2 SO4?NH3침출체계중분별고찰료마광세도、침출시간、총안농도、양화제용량、NH4+∶NH3비솔등인소대동침출솔적영향。최종학정최가공예조건위:마광세도-0.074 mm립급점86%,반응온도25℃,교반전속200 r/min,일단침출액고비2∶1,과류산안0.15 mol/L,안수농도3 mol/L,류산안농도1.5 mol/L,교반침출1.5 h,정치0.5 h;이단과류산안、안수화류산안첨가용량감반,계속교반침출1.5 h,정치0.5 h;삼단침출약제용량여이단침출상동,교반침출2 h,정치4 h완필。해조건하,가획득동침출솔대우86%적우량지표。
With low?grade copper oxide ore from Dishui county of Xinjiang Uygur Autonomous Region as raw material, factors affecting copper leaching in ( NH4 ) 2 SO4?NH3 system including grinding fineness, leaching time, total ammonia concentration, oxidant dosage, and ratio of NH4+∶NH3 were all investigated, resulting in the following optimal condition for leaching process, including a grinding size of -0.074 mm 86%, reaction temperature of 25℃, stirring at the speed of 200 r/min, solid/liquid ratio at 2∶1 for 1st?stage leaching with concentrations of ammonia, ammonium sulfate and ammonium persulfate at 3 mol/L, 1.5 mol/L and 0.15 mol/L, respectively, agitation leaching for 1.5 h followed by 0.5 hour′s standing, then with addition of ammonia, ammonium sulfate and ammonium persulfate for the 2nd?stage of leaching at half of previous stage, repeating agitation leaching for 1.5 h followed by 0.5 hour′s standing, and the dosage of reagent in the 3rd?stage leaching the same as the 2nd?stage, agitation leaching for 2 h followed by 4 hour′s standing. After the whole process, the leaching rate of copper can finally exceed 86%.