湿法冶金
濕法冶金
습법야금
HYDROMETALLURGY OF CHINA
2014年
3期
203-207
,共5页
冯雅丽%杜云龙%李辉%周宇照%王维大
馮雅麗%杜雲龍%李輝%週宇照%王維大
풍아려%두운룡%리휘%주우조%왕유대
离子膜电解槽%无硒%电解%锰
離子膜電解槽%無硒%電解%錳
리자막전해조%무서%전해%맹
electrolytic membrane reactor%non-selenium%electrodeposition%manganese
研究了用阴离子膜电解槽在硫酸盐体系中无硒电解金属锰,采用循环伏安法研究了阴极电化学机制。单因素条件试验确定的最佳电解条件为:锰离子质量浓度30 g/L ,硫酸铵质量浓度135 g/L ,电解温度35℃,阴极液pH=7.7,电流密度450 A/m2,SO2添加量为0.4 g/L。最佳条件下,电解效率达到82%,直流电耗为4985 kWh · t-1,电解产品为α-M n ,质量符合国家标准。阴离子交换膜可以减弱阴极浓差极化,有效区分锰沉积峰和析氢还原峰;SO2添加剂可显著抑制析氢反应,降低锰沉积电流,减小直流电耗。
研究瞭用陰離子膜電解槽在硫痠鹽體繫中無硒電解金屬錳,採用循環伏安法研究瞭陰極電化學機製。單因素條件試驗確定的最佳電解條件為:錳離子質量濃度30 g/L ,硫痠銨質量濃度135 g/L ,電解溫度35℃,陰極液pH=7.7,電流密度450 A/m2,SO2添加量為0.4 g/L。最佳條件下,電解效率達到82%,直流電耗為4985 kWh · t-1,電解產品為α-M n ,質量符閤國傢標準。陰離子交換膜可以減弱陰極濃差極化,有效區分錳沉積峰和析氫還原峰;SO2添加劑可顯著抑製析氫反應,降低錳沉積電流,減小直流電耗。
연구료용음리자막전해조재류산염체계중무서전해금속맹,채용순배복안법연구료음겁전화학궤제。단인소조건시험학정적최가전해조건위:맹리자질량농도30 g/L ,류산안질량농도135 g/L ,전해온도35℃,음겁액pH=7.7,전류밀도450 A/m2,SO2첨가량위0.4 g/L。최가조건하,전해효솔체도82%,직류전모위4985 kWh · t-1,전해산품위α-M n ,질량부합국가표준。음리자교환막가이감약음겁농차겁화,유효구분맹침적봉화석경환원봉;SO2첨가제가현저억제석경반응,강저맹침적전류,감소직류전모。
The non-selenium electrodeposition of metal manganese from sulphate-based electrolytic solution using ion membrane reactor was investigated ,and the catholic electrochemical behaviour was tested by cyclic voltammetry .The optimum electrolysis conditions through single factor experiments were found as follows :manganese ion concentration is 30 g/L ,ammonium sulfate concentration is 135 g/L ,temperature is 35 ℃ ,pH is 7 .7 ,current density is 450 A/m2 and SO2 concentration is 0 .4 g/L . Under these conditions ,the current efficiency can be up to 82% ,the DC power consumption can be reduced to 4 985 kWh/t .Manganese phase is α-Mn ,and the product quality meets national standards . Anion-exchange membrane can reduce cathode concentration polarization and distinguish effectively manganese electro-deposition peak from hydrogen evolution reduction peak .SO2 additive can suppress hydrogen reduction reaction and reduce manganese electro-deposition current ,thereby decrease DC power consumption .