中国有色金属学报
中國有色金屬學報
중국유색금속학보
THE CHINESE JOURNAL OF NONFERROUS METALS
2013年
2期
549-558
,共10页
刘伟锋%杨天足%刘又年%陈霖%张杜超%唐谟堂
劉偉鋒%楊天足%劉又年%陳霖%張杜超%唐謨堂
류위봉%양천족%류우년%진림%장두초%당모당
铅阳极泥%碱性氧化浸出%盐酸浸出%NaOH
鉛暘極泥%堿性氧化浸齣%鹽痠浸齣%NaOH
연양겁니%감성양화침출%염산침출%NaOH
lead anode slime%alkaline oxidation leaching%hydrochloric acid leaching%NaOH
提出碱性NaOH体系分步氧化浸出和盐酸浸出相结合的工艺预处理铅阳极泥,在碱性分步氧化浸出过程中,实现As的氧化溶解和Bi等金属的氧化沉淀,然后用盐酸溶解碱性浸出渣中的Bi,使贵金属富集在盐酸浸出渣中.结果表明:无论碱性直接浸出或酸性直接浸出都不能有效分离铅阳极泥中的有价金属;改变烘烤温度、延长空气氧化时间和改变碱性加压氧化浸出温度都不能实现有价金属的分步分离.当双氧水用量大于0.2以后,碱性浸出过程As的浸出率达到92%以上,碱性浸出渣盐酸浸出时,Bi和Cu的浸出率分别达到99.0%和97.0%,且残余的As不溶解,实现铅阳极泥中有价金属分步分离的目的.
提齣堿性NaOH體繫分步氧化浸齣和鹽痠浸齣相結閤的工藝預處理鉛暘極泥,在堿性分步氧化浸齣過程中,實現As的氧化溶解和Bi等金屬的氧化沉澱,然後用鹽痠溶解堿性浸齣渣中的Bi,使貴金屬富集在鹽痠浸齣渣中.結果錶明:無論堿性直接浸齣或痠性直接浸齣都不能有效分離鉛暘極泥中的有價金屬;改變烘烤溫度、延長空氣氧化時間和改變堿性加壓氧化浸齣溫度都不能實現有價金屬的分步分離.噹雙氧水用量大于0.2以後,堿性浸齣過程As的浸齣率達到92%以上,堿性浸齣渣鹽痠浸齣時,Bi和Cu的浸齣率分彆達到99.0%和97.0%,且殘餘的As不溶解,實現鉛暘極泥中有價金屬分步分離的目的.
제출감성NaOH체계분보양화침출화염산침출상결합적공예예처리연양겁니,재감성분보양화침출과정중,실현As적양화용해화Bi등금속적양화침정,연후용염산용해감성침출사중적Bi,사귀금속부집재염산침출사중.결과표명:무론감성직접침출혹산성직접침출도불능유효분리연양겁니중적유개금속;개변홍고온도、연장공기양화시간화개변감성가압양화침출온도도불능실현유개금속적분보분리.당쌍양수용량대우0.2이후,감성침출과정As적침출솔체도92%이상,감성침출사염산침출시,Bi화Cu적침출솔분별체도99.0%화97.0%,차잔여적As불용해,실현연양겁니중유개금속분보분리적목적.
@@@@The united process that combining alkaline multistage oxidation leaching and hydrochloric acid leaching was used to pretreat lead anode slime. When lead anode slime was leached by alkaline multistage oxidation, arsenic is dissolved into the solution, while bismuth, copper and other metals were oxidized and remained in the alkaline leaching residue. The alkaline leaching residue was leached with hydrochloric acid solution. The result shows that valuable metals can not be separated effectively whether the direct leaching is performed in alkaline solution or hydrochloric acid solution. The valuable metals can not be separated step by step when different oxidation modes, such as roasting, prolonging the time of air oxidation leaching and decreasing the temperature of pressure oxidation leaching, are applied to strengthen the NaOH leaching procedure. When H2O2 is added to strengthen NaOH leaching, the base metals in lead anode slime can be removed efficiently. The leaching ratio of arsenic can reach 92% when the coefficient of H2O2 is 0.2, while the alkaline leaching residue is leached in hydrochloric acid solution, the leaching ratios of bismuth and copper reach 99%and 97%, respectively, and the remained arsenic can not be dissolved in the acidic leaching solution.