北京科技大学学报
北京科技大學學報
북경과기대학학보
JOURNAL OF UNIVERSITY OF SCIENCE AND TECHNOLOGY BEIJING
2015年
1期
35-41
,共7页
张魁芳%曹佐英%肖连生%曾理%张贵清%李青刚
張魁芳%曹佐英%肖連生%曾理%張貴清%李青剛
장괴방%조좌영%초련생%증리%장귀청%리청강
湿法冶金%锗%萃取%反萃%转型
濕法冶金%鍺%萃取%反萃%轉型
습법야금%타%췌취%반췌%전형
hydrometallurgy%germanium%extraction%stripping%transformation
针对现行的湿法炼锌渣中提取锗的研究现状,采用新型萃取剂HBL101从锌置换渣的高酸浸出液中直接萃取锗,考察了料液酸度、萃取剂体积分数、萃取温度、萃取时间和相比对萃取的影响以及氢氧化钠质量浓度、反萃温度、反萃时间和反萃相比对反萃的影响,并对萃取剂转型条件进行了研究.实验表明:有机相组成为30% HBL101+70%磺化煤油(体积分数)作为萃取剂,料液酸度为113.2 g·L-1 H2 SO4,其最佳萃取条件为萃取温度25℃,萃取时间20 min,相比O/A=1:4.经过五级逆流萃取,锗萃取率达到98.57%.负载有机相用150 g·L-1 NaOH溶液可选择性反萃锗得到高纯度锗酸钠溶液,其最佳反萃条件为反萃温度25℃,反萃时间25 min,相比O/A=4:1.经过五级逆流反萃,反萃率可达到98.1%.反萃锗后负载有机相再用200 g·L-1硫酸溶液反萃共萃的铜并转型,控制反萃温度25℃,反萃时间20 min,O/A=2:1.经过五级逆流反萃,铜反萃率可达到99.5%并完成转型,萃取剂返回使用.
針對現行的濕法煉鋅渣中提取鍺的研究現狀,採用新型萃取劑HBL101從鋅置換渣的高痠浸齣液中直接萃取鍺,攷察瞭料液痠度、萃取劑體積分數、萃取溫度、萃取時間和相比對萃取的影響以及氫氧化鈉質量濃度、反萃溫度、反萃時間和反萃相比對反萃的影響,併對萃取劑轉型條件進行瞭研究.實驗錶明:有機相組成為30% HBL101+70%磺化煤油(體積分數)作為萃取劑,料液痠度為113.2 g·L-1 H2 SO4,其最佳萃取條件為萃取溫度25℃,萃取時間20 min,相比O/A=1:4.經過五級逆流萃取,鍺萃取率達到98.57%.負載有機相用150 g·L-1 NaOH溶液可選擇性反萃鍺得到高純度鍺痠鈉溶液,其最佳反萃條件為反萃溫度25℃,反萃時間25 min,相比O/A=4:1.經過五級逆流反萃,反萃率可達到98.1%.反萃鍺後負載有機相再用200 g·L-1硫痠溶液反萃共萃的銅併轉型,控製反萃溫度25℃,反萃時間20 min,O/A=2:1.經過五級逆流反萃,銅反萃率可達到99.5%併完成轉型,萃取劑返迴使用.
침대현행적습법련자사중제취타적연구현상,채용신형췌취제HBL101종자치환사적고산침출액중직접췌취타,고찰료료액산도、췌취제체적분수、췌취온도、췌취시간화상비대췌취적영향이급경양화납질량농도、반췌온도、반췌시간화반췌상비대반췌적영향,병대췌취제전형조건진행료연구.실험표명:유궤상조성위30% HBL101+70%광화매유(체적분수)작위췌취제,료액산도위113.2 g·L-1 H2 SO4,기최가췌취조건위췌취온도25℃,췌취시간20 min,상비O/A=1:4.경과오급역류췌취,타췌취솔체도98.57%.부재유궤상용150 g·L-1 NaOH용액가선택성반췌타득도고순도타산납용액,기최가반췌조건위반췌온도25℃,반췌시간25 min,상비O/A=4:1.경과오급역류반췌,반췌솔가체도98.1%.반췌타후부재유궤상재용200 g·L-1류산용액반췌공췌적동병전형,공제반췌온도25℃,반췌시간20 min,O/A=2:1.경과오급역류반췌,동반췌솔가체도99.5%병완성전형,췌취제반회사용.
Germanium extraction from a high acid leach solution of zinc replacing slag by a new extractant, HBL101, was tested based on the current research status on extracting germanium from zinc smelting slag in hydrometallurgy. Investigations were performed on the effects of feed acidity, extractant concentration, extraction time, extraction phase ratio and temperature on the extraction, the effects of NaOH concentration, stripping time, stripping phase ratio and temperature on the stripping of germanium, and the conditions of extractant transformation. The results show that with 30% HBL101 in 70% sulphonated kerosene ( volume fraction) as an extract-ant, the extraction rate of germanium from the solution with 113. 2 g·L-1 H2 SO4 reaches 98. 57% in five-stage counter current extrac-tion with a volume ratio of oil phase to aqueous phase, O/A ratio, of 1:4 at 25℃ for 20 min. Germanium in the loaded organic can be selectively stripped using a 150 g·L-1 NaOH solution and the stripping rate reaches 98. 1% in five-stage counter current stripping with an O/A ratio of 4:1 at 25℃ for 25 min. After germanium stripping, copper in the loaded organic can be stripped using a 200 g·L-1 H2 SO4 solution and the stripping rate of copper reaches 99. 75% in five-stage counter current stripping with an O/A ratio of 2:1 at 25℃ for 20 min. The extractant returns to extraction circularly.