中国有色金属学报(英文版)
中國有色金屬學報(英文版)
중국유색금속학보(영문판)
TRANSACTIONS OF NONFERROUS METALS SOCIETY OF CHINA
2011年
8期
1840-1846
,共7页
梁啟文%胡慧萍%付翁%叶婷%陈启元
樑啟文%鬍慧萍%付翁%葉婷%陳啟元
량계문%호혜평%부옹%협정%진계원
氨性蚀刻废液%铜回收%溶液萃取%β-二酮
氨性蝕刻廢液%銅迴收%溶液萃取%β-二酮
안성식각폐액%동회수%용액췌취%β-이동
spent ammoniaeal etchant%copper recovery%solvent extraction%beta-diketone
采用高位阻β-二酮1-(4’十二烷基)苯基-3-叔丁基-1,3-丙二酮)作为萃取剂从模拟印刷电路板(PCBs)蚀刻废液中萃取铜.利用离子强度与萃取反应平衡常数的关系校正模拟的萃取等温线,该模拟萃取等温线与实验测得萃取等温线基本相符.通过实验确定萃取剂浓度、相比、萃取级数和反萃级数等萃取工艺参数.结果表明,在室温下对于铜离子浓度为112 g/L、总氨浓度为7 mol/L的模拟氨性蚀刻废液的最佳萃取条件为:萃取剂浓度为40%,相比为5∶4,萃取时间为5min.在此条件下,经过一级萃取,蚀刻废液中铜离子浓度可降低至63.24 g/L,能返回到电路板的生产中循环使用.用含铜30g/L,硫酸浓度180 g/L的模拟废电解液对负载有机相进行反萃,相比(O/A)为1∶2,经一级反萃,铜的反萃率可达98.27%.
採用高位阻β-二酮1-(4’十二烷基)苯基-3-叔丁基-1,3-丙二酮)作為萃取劑從模擬印刷電路闆(PCBs)蝕刻廢液中萃取銅.利用離子彊度與萃取反應平衡常數的關繫校正模擬的萃取等溫線,該模擬萃取等溫線與實驗測得萃取等溫線基本相符.通過實驗確定萃取劑濃度、相比、萃取級數和反萃級數等萃取工藝參數.結果錶明,在室溫下對于銅離子濃度為112 g/L、總氨濃度為7 mol/L的模擬氨性蝕刻廢液的最佳萃取條件為:萃取劑濃度為40%,相比為5∶4,萃取時間為5min.在此條件下,經過一級萃取,蝕刻廢液中銅離子濃度可降低至63.24 g/L,能返迴到電路闆的生產中循環使用.用含銅30g/L,硫痠濃度180 g/L的模擬廢電解液對負載有機相進行反萃,相比(O/A)為1∶2,經一級反萃,銅的反萃率可達98.27%.
채용고위조β-이동1-(4’십이완기)분기-3-숙정기-1,3-병이동)작위췌취제종모의인쇄전로판(PCBs)식각폐액중췌취동.이용리자강도여췌취반응평형상수적관계교정모의적췌취등온선,해모의췌취등온선여실험측득췌취등온선기본상부.통과실험학정췌취제농도、상비、췌취급수화반췌급수등췌취공예삼수.결과표명,재실온하대우동리자농도위112 g/L、총안농도위7 mol/L적모의안성식각폐액적최가췌취조건위:췌취제농도위40%,상비위5∶4,췌취시간위5min.재차조건하,경과일급췌취,식각폐액중동리자농도가강저지63.24 g/L,능반회도전로판적생산중순배사용.용함동30g/L,류산농도180 g/L적모의폐전해액대부재유궤상진행반췌,상비(O/A)위1∶2,경일급반췌,동적반췌솔가체98.27%.
The solvent extraction of copper from simulated ammoniacal spent etchant with 1-(4'-dodecyl)-phenyl-3-tertiary butyl-1,3-octadione (HR) was studied,and a model of extraction isotherm was proposed and verified with equilibrium extraction constant.The influence of equilibration time,extractant concentration and phase ratio on the extraction of copper was studied at (298±0.5) K.For the spent etching solutions containing 112.98 g/L Cu,6 mol/L NH3 and 1 mol/L NH4+,the optimal solvent extraction condition of copper was obtained in one-stage solvent extraction at phase ratio of 5:4 with 40% HR in sulphonated kerosene for 5 min.The copper concentration in the raffinate decreased to 63.24 g/L and raffinate can be favorably recycled to the etching solution.The stripping studies were carried out with the simulated copper spent electrolyte containing 30 g/L Cu and 180 g/L H2SO4.The stripping ratio is 98.27% from the loaded organic phase after one-stage stripping at phase ratio of 1:2 at (298±0.5) K.