湿法冶金
濕法冶金
습법야금
HYDROMETALLURGY OF CHINA
2015年
3期
229-232
,共4页
皮露%何克杰%罗炎%孙维义%丁桑岚%苏仕军
皮露%何剋傑%囉炎%孫維義%丁桑嵐%囌仕軍
피로%하극걸%라염%손유의%정상람%소사군
P204%逆流萃取%电解%锰%镁
P204%逆流萃取%電解%錳%鎂
P204%역류췌취%전해%맹%미
P204%countercurrent extraction%electrolytic manganese%manganese%magnesium
电解锰过程中,阳极液中的镁离子在闭路循环中会逐渐积累,使电流效率下降,能耗增大,同时也影响电解锰产品质量。研究了用P204‐磺化煤油溶液萃取分离阳极液中的锰离子和镁离子,分别考察了 P204体积分数、有机相皂化率、水相p H、相比等参数对锰离子和镁离子萃取率的影响。结果表明,在溶液温度35℃、P204体积分数25%、有机相皂化率50%、水相p H=4.0,V o ∶V a =2∶1的最佳条件下,经4级逆流萃取,锰离子萃取率达99.5%,镁离子萃取率为31.8%。
電解錳過程中,暘極液中的鎂離子在閉路循環中會逐漸積纍,使電流效率下降,能耗增大,同時也影響電解錳產品質量。研究瞭用P204‐磺化煤油溶液萃取分離暘極液中的錳離子和鎂離子,分彆攷察瞭 P204體積分數、有機相皂化率、水相p H、相比等參數對錳離子和鎂離子萃取率的影響。結果錶明,在溶液溫度35℃、P204體積分數25%、有機相皂化率50%、水相p H=4.0,V o ∶V a =2∶1的最佳條件下,經4級逆流萃取,錳離子萃取率達99.5%,鎂離子萃取率為31.8%。
전해맹과정중,양겁액중적미리자재폐로순배중회축점적루,사전류효솔하강,능모증대,동시야영향전해맹산품질량。연구료용P204‐광화매유용액췌취분리양겁액중적맹리자화미리자,분별고찰료 P204체적분수、유궤상조화솔、수상p H、상비등삼수대맹리자화미리자췌취솔적영향。결과표명,재용액온도35℃、P204체적분수25%、유궤상조화솔50%、수상p H=4.0,V o ∶V a =2∶1적최가조건하,경4급역류췌취,맹리자췌취솔체99.5%,미리자췌취솔위31.8%。
In the process of electrolytic manganese ,the magnesium ions in anode solution will gradually accumulated in closed cycle to reduce current efficiency and increase energy consumption ,and affect the quality of electrolytic manganese product .The separation of manganese and magnesium from the electrolytic manganese anode solution using P204 in sulfonated kerosene was investigated .The influence of several parameters on the extraction rate of manganese and magnesium were examined , such as P204 volume fraction in organic phase ,saponification rate of the organic phase ,water phase pH ,the ratio of organic phase volume to water phase volume .The results suggest that under the conditions of temperature of 35 ℃ ,P204 volume fraction of 25% ,organic phase saponification rate of 50% ,water phase pH of 4 .0 ,Vo ∶Va = 2∶1 ,and four‐stages countercurrent extraction ,satisfactory extraction efficiency (99 .5% ) of manganese ion is achieved ,while the extraction of magnesium is approximately 31 .8% ,manganese ion and magnesium ion are effectively separated at a low cost .