期刊文献+
共找到8篇文章
< 1 >
每页显示 20 50 100
从分银渣的盐酸浸出液中回收和制备氧化铋 被引量:11
1
作者 刘巍 蒋训雄 +4 位作者 蒋伟 冯林永 汪胜东 范艳青 张登高 《有色金属(冶炼部分)》 CAS 北大核心 2014年第11期60-62,69,共4页
铜阳极泥分银渣盐酸浸出液中含锑、锡、铅、铋等,采用水解除锡和锑、硫酸盐沉铅、一次水解沉铋等分步沉淀工艺,进行锑、锡、铅、铋的分离并得到粗氯氧铋。结果表明,在pH 1.4左右进行锑、锡水解,pH 2.1进行铋一次水解。粗氯氧铋经盐酸返... 铜阳极泥分银渣盐酸浸出液中含锑、锡、铅、铋等,采用水解除锡和锑、硫酸盐沉铅、一次水解沉铋等分步沉淀工艺,进行锑、锡、铅、铋的分离并得到粗氯氧铋。结果表明,在pH 1.4左右进行锑、锡水解,pH 2.1进行铋一次水解。粗氯氧铋经盐酸返溶后,控制pH 1.6-1.7进行铋二次水解产出精制氯氧铋,然后再碱转,即可制备出纯度大于99.9%的氧化铋。 展开更多
关键词 分银渣 盐酸浸出液 水解 氧化铋
下载PDF
采用N235从镍钼矿盐酸浸出液中萃取钼的研究 被引量:8
2
作者 肖朝龙 肖连生 龚柏凡 《中国钼业》 2011年第2期7-11,共5页
采用N235对镍钼矿盐酸浸出液进行了萃取钼的研究。试验结果表明,在最佳工艺条件下,5级逆流钼萃取率可达98%以上,镍损失率小于1%,负载有机相经稀酸洗涤除铁后采用氨水反萃,1级反萃率达97%以上,反萃液钼浓度为50 g/L左右,达到了钼镍分离... 采用N235对镍钼矿盐酸浸出液进行了萃取钼的研究。试验结果表明,在最佳工艺条件下,5级逆流钼萃取率可达98%以上,镍损失率小于1%,负载有机相经稀酸洗涤除铁后采用氨水反萃,1级反萃率达97%以上,反萃液钼浓度为50 g/L左右,达到了钼镍分离及钼富集转型的目的。 展开更多
关键词 镍钼矿盐酸浸出液 N235 萃钼
下载PDF
用N_(503)从大洋多金属结核盐酸浸出液中萃取铁的研究 被引量:2
3
作者 李先柏 杨静 +1 位作者 周勤俭 姜小平 《湿法冶金》 CAS 1997年第2期61-64,共4页
本文研究了用 N50 3作萃取剂、H2 O作反萃取剂从大洋多金属结核盐酸浸出液中萃取铁的工艺。考察了 HCl浓度、Cl-浓度、N50 3浓度、相比、时间对萃取及平衡 p H值、相比、时间对反萃取的影响 ,并进行了模拟试验。
关键词 大洋多金属结核 盐酸浸出液 萃取 萃取剂
下载PDF
用萃取剂P507从盐酸浸出液中萃取分离钒与铁 被引量:4
4
作者 李丹 陈德胜 +5 位作者 张国之 赵宏欣 齐涛 王伟菁 王丽娜 刘亚辉 《过程工程学报》 CAS CSCD 北大核心 2017年第6期1182-1187,共6页
用2-乙基己基膦酸单2-乙基己基酯(P507)作萃取剂,从铁含量高、钒含量低、杂质含量高的盐酸浸出液中萃取分离钒与铁.结果表明,在浸出液初始p H 0?0.6、萃取温度30℃、萃取时间15 min、相比(O/A)1:1及P507浓度20%(?)的优化条件下,钒和铁... 用2-乙基己基膦酸单2-乙基己基酯(P507)作萃取剂,从铁含量高、钒含量低、杂质含量高的盐酸浸出液中萃取分离钒与铁.结果表明,在浸出液初始p H 0?0.6、萃取温度30℃、萃取时间15 min、相比(O/A)1:1及P507浓度20%(?)的优化条件下,钒和铁的单级萃取率分别为70%和5%.用硫酸作反萃剂,在反萃温度30℃、反萃时间12 min、相比(O/A)4:1及硫酸浓度368 g/L的优化条件下,钒和铁的单级反萃率分别为100%和3%.一级萃取和反萃后的反萃液含V(IV)18.62 g/L和Fe(II)0.37 g/L,分离效果良好,同时,钒与铝、钙、镁、锰等杂质也有较好的分离效果. 展开更多
关键词 溶剂萃取分离 盐酸浸出液 P507
原文传递
从太平洋中部深海粘土盐酸浸出液中萃取回收钇的研究 被引量:9
5
作者 张魁芳 吴宇坤 +2 位作者 刘志强 朱克超 朱薇 《中国稀土学报》 CAS CSCD 北大核心 2016年第1期62-69,共8页
针对太平洋中部深海粘土HCl浸出液酸度高、成分复杂等特点,克服现有萃取剂不足,采用新型萃取剂P535从高浓度HCl浸出液中直接萃取回收Y^(3+),考察料液酸度、萃取剂浓度、萃取时间和相比对萃取的影响以及HCl,H2SO4反萃剂对反萃的影响,分... 针对太平洋中部深海粘土HCl浸出液酸度高、成分复杂等特点,克服现有萃取剂不足,采用新型萃取剂P535从高浓度HCl浸出液中直接萃取回收Y^(3+),考察料液酸度、萃取剂浓度、萃取时间和相比对萃取的影响以及HCl,H2SO4反萃剂对反萃的影响,分别绘制萃取平衡等温线和反萃平衡等温线,确定反萃方案并完成转型。结果表明:以有机相组成为10%P535(质量分数)+磺化煤油作为萃取剂,料液酸度为1.12 mol·L-1HCl,其最佳萃取条件为:萃取时间5 min,相比O/A=1∶2。经过3级逆流萃取,Y^(3+)萃取率达到98%,Fe^(3+)共萃进入有机相,其他金属基本不萃取。负载有机相用2 mol·L-1的H2SO4溶液可选择性反萃Y^(3+),得到Y_2(SO_4)_3溶液,反萃Y^(3+)的有机相再用8 mol·L-1HCl溶液反萃共萃的Fe^(3+),完成转型。 展开更多
关键词 太平洋中部 深海粘土 盐酸浸出液 P535 萃取
原文传递
Ag recovery from copper anode slime by acid leaching at atmospheric pressure to synthesize silver nanoparticles 被引量:7
6
作者 Atefeh Khaleghi Sattar Ghader Dariush Afzali 《International Journal of Mining Science and Technology》 SCIE EI 2014年第2期251-257,共7页
In this paper, recovery of silver from anode slime of Sarcheshmeh copper complex in lran and subsequent synthesis of silver nanoparticles from leaching solution is investigated. Sarcheshmeh anode slime is mainly consi... In this paper, recovery of silver from anode slime of Sarcheshmeh copper complex in lran and subsequent synthesis of silver nanoparticles from leaching solution is investigated. Sarcheshmeh anode slime is mainly consisted ofCu, Ag, Pb and Se. Amount of Ag in the considered anode slime was 5.4% (by weight). The goal was to recover as much as possible Ag from anode slime at atmospheric pressure to synthesize Ag nanoparticles. Therefore, acid leaching was used for this purpose. The anode slime was leached with sulfuric and nitric acid from room to 90 ~C at different acid concentrations and the run which yielded the most recovery of Ag was selected for Ag nanoparticles synthesis. At this condition, Cu, Pb and Se are lea- ched as well as Ag. To separate Ag from leach solution HCI was added and silver was precipitated as AgCl which were then dissolved by ammonia solution. The Ag nanoparticles are synthesized from this solution by chemical reduction method by aid of sodium borohydride in the presence of PVP and PEG as stabilizers. The synthesized Ag nanoparticles showed a peak of 394 nm in UV-vis spectrum and TEM images showed a rather uniform Ag nanoparticles of 12 nm. 展开更多
关键词 Copper anode slime Acid leaching Silver recovery Silver nanoparticles
下载PDF
Cyclic metallurgical process for extracting V and Cr from vanadium slag: Part Ⅱ. Separation and recovery of Cr from vanadium precipitated solution 被引量:6
7
作者 Ming-e YANG Hao-xiang YANG +2 位作者 Sheng-hui TIAN Ming-yu WANG Xue-wen WANG 《Transactions of Nonferrous Metals Society of China》 SCIE EI CAS CSCD 2021年第9期2852-2860,共9页
Cyclic metallurgical process for separation and recovery of Cr from vanadium precipitated solution by precipitation with PbCO_(3)and leaching with Na_(2)CO_(3)was investigated.The concentration of Cr residue in the so... Cyclic metallurgical process for separation and recovery of Cr from vanadium precipitated solution by precipitation with PbCO_(3)and leaching with Na_(2)CO_(3)was investigated.The concentration of Cr residue in the solution decreases from 2.360 to 0.001 g/L by adding PbCO_(3)into vanadium precipitated solution according to Pb/Cr molar ratio of 2.5,adjusting the pH to 3.0 and stirring for 180 min at 30℃.Then,the precipitates were leached with hot Na_(2)CO_(3)solution to obtain leaching solution containing Na_(2)CrO_(4)and leaching residue containing PbCO_(3).The leaching efficiency of Cr reaches 96.43%by adding the precipitates into 0.5 mol/L Na_(2)CO_(3)solution with the mass ratio of liquid to solid(L/S)of 10:1 mL/g and stirring for 60 min under pH 9.5 at 70℃.After filtration,leaching residue is reused in Cr precipitation and leaching solution is used to circularly leach the Cr precipitates until Na_(2)CrO_(4)approaches the saturation.Finally,the product of Na_(2)CrO_(4)·4H_(2)O is obtained by evaporation and crystallization of leaching solution. 展开更多
关键词 vanadium precipitated solution lead salt precipitating chromium sodium carbonate leaching chromium cyclic metallurgical process
下载PDF
Effects of Surfactant on Zinc Recovery by Solvent Extraction during Leaching in HCl-FeCl_3 Solution 被引量:1
8
作者 卢立柱 康晓红 谢慧琴 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2002年第1期109-111,共3页
The effects of surfactant on the solvent extraction in leachingsphalerite were investigated. It is found that sodium dodecylsulfonate is the effective surfactant in improving the zinc recoveryfrom sphalerite in the aq... The effects of surfactant on the solvent extraction in leachingsphalerite were investigated. It is found that sodium dodecylsulfonate is the effective surfactant in improving the zinc recoveryfrom sphalerite in the aqueous FeCl_3-HCl-tetrachloroethylene system.Through the measurements of surface tension and viscosity of thesphalerite Slurry modified with different surfactants, it isconcluded that sodium dodecyl sulfonate in the concentration rang Of0.05 to 0.2 g·L^-1 can improve the viscosity of sphalerite slurry inthe water, decrease the surface tension of Leaching solution, preventthe aggregation of ore particles, and give very high zinc extraction. 展开更多
关键词 SURFACTANT ZINC solvent extraction LEACHING
下载PDF
上一页 1 下一页 到第
使用帮助 返回顶部