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镍基高温合金废料的回收 总被引:8,自引:0,他引:8
采用电化学溶解、中和分离铬、选择性氧化沉淀分离镍钴的工艺流程,对镍基高温合金废料进行了综合回收。采用该流程可以生产出合格的镍盐、钴盐、铬盐 相似文献
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从红土镍矿镍铁渣中分离浸取镍铬工艺 总被引:1,自引:0,他引:1
将镍铁渣破碎、球磨后磁选富集Ni于精矿中,富集Cr于尾矿中. 磁选后Ni从0.26%富集至2.57%(w),Cr从4.55%富集至4.61%(w). 考察了H2SO4常压酸浸精矿时Ni的浸出规律. 结果表明,在酸浸温度110℃、酸浓度220 g/L、酸浸时间2 h、液固质量比5的优化酸浸条件下,Ni浸出率为91.5%. 在80~120℃内,Ni浸出反应活化能为19.6 kJ/mol. Ni浸出反应主要受扩散控制. 用Na2CO3碱熔焙烧尾矿,在温度1000℃、Na2CO3/渣质量比0.65、时间1 h、镍铁渣尾矿粒度<74 mm的优化条件下,Cr浸出率为94.1%. 相似文献
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电镀污泥中铜和镍的回收工艺研究——污泥的酸浸出工艺 总被引:4,自引:1,他引:4
研究了电镀污泥中铜和镍浸出的方法,对比选取硫酸作为浸出剂,考察了酸的用量对浸出效果的影响,得到最佳浸出条件为:污泥颗粒d=0.15mm,每2g污泥加10%硫酸10mL,常温下振荡0.5h。该条件下电镀污泥中铜、镍的浸出率均较高,达95%以上,为后续电解回收工艺奠定了较好的基础。 相似文献
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使用P507萃取剂萃取回收镍钴锰,考察了离心萃取机与箱式萃取槽平衡时间、相比和含油量的差异。萃取剂选用20%P507+80%磺化煤油,皂化率为60%,萃取级数为五级时,发现箱式萃取槽所需的平衡时间是离心萃取机的6倍,萃取率达到99.5%时,离心萃取机所需的相比(VO/VA)=3,萃余液含油量为25.2 mg/L;箱式萃取槽的相比(VO/VA)=5,萃余液的含油量为62.2 mg/L,离心萃取机较箱式萃取槽有更短的平衡时间、更小的油料比和耗油量,在萃取回收镍钴锰领域具有良好的工业应用前景。 相似文献
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本文采用酸解-沉淀方法对制药中间体镍-铝废催化剂进行处理,镍-铝分离效果理想,回收之硫酸镍中铝的含量达0.005%,其他指标均可满足电镀、催化剂、电池用的要求。该工艺设备简便易行。 相似文献
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《分离科学与技术》2012,47(18):2735-2740
Simultaneous recovery of nickel and cobalt from aqueous solutions by complexation-ultrafiltration process with polyethylenimine (PEI) was studied. Experiments were performed as a function of polymer/metal ratio (P/M), solution pH, and ionic strength. Effects of concentration time on metal rejection and membrane flux were also studied. At optimum experimental conditions of pH 6.0 and P/M 5.0, the nickel removal efficiency reaches at 99.9% and cobalt removal efficiency goes to 96.4%. Both nickel and cobalt removal efficiencies decreased as the adding salt concentration increases. During 12 h of the ultrafiltration process, the decline of membrane flux was less than 16% and the removal efficiencies for both nickel and cobalt were kept almost constant. Diafiltration was further performed to regenerate PEI. The removal efficiencies for both metals using recycled PEI were found to be close to those with the original PEI. Results from the two-step process of complexation-UF and decomplexation-UF separation showed that it could be a promising method for simultaneous recovery of nickel and cobalt from aqueous solutions. 相似文献
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Selective recovery of copper, cobalt, and nickel from acidic chloride media was investigated with solvent impregnated resins (SIRs) containing acidic organophosphorus extractants. The adsorption of each metal with the SIR proceeds via a cation exchange mechanism. An SIR containing 2-ethylhexylphosphonic acid mono-2-ethylhexyl ester (PC-88A) has high selectivity for Cu2+, and the order of selectivity is Cu2+ > Co2+ > Ni2+. Effective adsorption-elution can be achieved by chromatographic operation for the selective recovery of Cu2+ from a ternary metal solution. High selectivity for Co2+ was observed using a SIR comprising bis-2,4,4-trimethylpentylphosphinic acid (Cyanex 272) and can be effectively separated from a Co and Ni binary metal solution by column adsorption. A simple and effective process flow sheet is proposed for selective recovery of Cu2+, Co2+, and Ni2+ from aqueous chloride media using the two SIRs. 相似文献
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研究了某厂ZnSO4溶液砷盐净化工艺产生的含砷钴镍渣中砷在惰性和氧气气氛的碱介质中的氧化浸出机理. 结果表明,砷氧化浸出与温度、介质碱浓度、浸出气氛均密切相关. 在惰性气氛、碱介质中,渣中CuO和Cu2O均可作为砷氧化浸出的氧化剂,在80℃及以下低温下,CuO对低价砷起主要氧化作用,还原产物为Cu2O,砷最高浸出率不超过53%;在100℃及以上较高温下,CuO和Cu2O均参与低价砷的氧化浸出过程,还原产物均为单质Cu,最高浸出率约为90%;在氧气气氛、碱介质中,砷浸出率可达98%以上,除O2作为氧化剂直接氧化浸出砷外,渣中的铜可作为O2与低价砷之间电子传递的载体,强化氧化反应. 相似文献
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羰基化法生产苯乙酸工艺中生成的废催化剂,含有大量有价值的钴元素。介绍一种从废催化剂中,采用黄钠铁矾沉淀法将铁除去,用萃取法将锰、钻分离,制备得到含结晶水的氯化钴,钴的回收率达90%以上。 相似文献
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Various processes used for the recovery of valuable metals such as copper, nickel and cobalt from marine manganese nodules has been reviewed and an effective process for their extraction has been described. 相似文献