中国有色金属学报
中國有色金屬學報
중국유색금속학보
THE CHINESE JOURNAL OF NONFERROUS METALS
2014年
10期
2576-2581
,共6页
徐筱群%满瑞林%张建%刘琦%徐娟%孙祖眉
徐篠群%滿瑞林%張建%劉琦%徐娟%孫祖眉
서소군%만서림%장건%류기%서연%손조미
废旧锂电池%电解剥离%浸出%生物质酸浸%草酸钴
廢舊鋰電池%電解剝離%浸齣%生物質痠浸%草痠鈷
폐구리전지%전해박리%침출%생물질산침%초산고
spent Li-ion battery%electrolytic stripping%leaching%biomass acid leaching%CoC2O4
采用电解剥离?浸出正极材料、P204萃取除铝、秸秆硫酸浸出电池渣、草酸沉钴等工艺回收废旧锂电池中的钴。结果表明:经过20~30 min的电解剥离,实现了电池粉与铝箔的分离,钴的浸出率为50%,电流效率为70%;通过两次P204错流萃取除铝后,萃余液中Al3+Co 2+含量可以降到0.4 mg/L,而钴却未损失;燕麦秸秆粉?硫酸浸出电池渣中钴的最佳工艺条件如下:硫酸2 mol/L、1 g电池渣加入0.5~0.7 g麦秆粉,固液比1:10,在80~90℃反应1~2 h,钴的浸出率达到98%以上;经三级浸出,COD的含量可降至1.3 g/L左右;草酸沉钴调节溶液温度为50℃, pH为2,保持n()/n(2?24CO)=1,1 h后钴的一次沉淀率达到92%以上,滤液pH为0.2,其滤液可作为电解浸出液循环使用。
採用電解剝離?浸齣正極材料、P204萃取除鋁、秸稈硫痠浸齣電池渣、草痠沉鈷等工藝迴收廢舊鋰電池中的鈷。結果錶明:經過20~30 min的電解剝離,實現瞭電池粉與鋁箔的分離,鈷的浸齣率為50%,電流效率為70%;通過兩次P204錯流萃取除鋁後,萃餘液中Al3+Co 2+含量可以降到0.4 mg/L,而鈷卻未損失;燕麥秸稈粉?硫痠浸齣電池渣中鈷的最佳工藝條件如下:硫痠2 mol/L、1 g電池渣加入0.5~0.7 g麥稈粉,固液比1:10,在80~90℃反應1~2 h,鈷的浸齣率達到98%以上;經三級浸齣,COD的含量可降至1.3 g/L左右;草痠沉鈷調節溶液溫度為50℃, pH為2,保持n()/n(2?24CO)=1,1 h後鈷的一次沉澱率達到92%以上,濾液pH為0.2,其濾液可作為電解浸齣液循環使用。
채용전해박리?침출정겁재료、P204췌취제려、갈간류산침출전지사、초산침고등공예회수폐구리전지중적고。결과표명:경과20~30 min적전해박리,실현료전지분여려박적분리,고적침출솔위50%,전류효솔위70%;통과량차P204착류췌취제려후,췌여액중Al3+Co 2+함량가이강도0.4 mg/L,이고각미손실;연맥갈간분?류산침출전지사중고적최가공예조건여하:류산2 mol/L、1 g전지사가입0.5~0.7 g맥간분,고액비1:10,재80~90℃반응1~2 h,고적침출솔체도98%이상;경삼급침출,COD적함량가강지1.3 g/L좌우;초산침고조절용액온도위50℃, pH위2,보지n()/n(2?24CO)=1,1 h후고적일차침정솔체도92%이상,려액pH위0.2,기려액가작위전해침출액순배사용。
Cobalt was recycled from spent Li-ion battery through the electrolytic stripping-leaching cathode material, P204 extraction Al, straw sulphuric acid leaching battery slag and oxalate precipitating cobalt. The results show that the battery powder can be separated from aluminum foil after 20?30 min electrolytic stripping process, the cobalt leaching rate is 50% and current efficiency is 70%. After two?stage P204 cross-flow extraction, Al3+Co 2+ remained in the raffinate can be dropped to 0.4 mg/L, and cobalt is not lose. Under the condition of sulfuric acid concentration 2 mol/L, adding 0.5?0.7 g straw powder into 1g battery slag, and liquid-solid ratio 1:10, the cobalt leaching rate is over 98% after 1?2 h in 80?90℃. After three?stage leaching process, COD content can drop to about 1.3 g/L. In oxalate precipitating process, adjusting the pH of solution to 2, keepingn( )/n(2?24CO) of 1, cobalt precipitation rate is above 92% after 1h reaction under 50℃, and pH of the filtrate is 0.2, which can be circulated used as electrolytic leaching liquid.