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COMPARATIVE STUDY OF PERFORMANCE OF DIFFERENT CHELATING AGENTS FOR EXTRACTION OF NI FROM SPENT CATALYST

机译:从螯合剂中萃取镍的不同螯合剂性能的比较研究

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The mobilization of heavy metals from spent catalyst is of the essence due to increasing demand of complex metallic composites in industries and to reduce the metallic waste. Present study involves the development of environmental friendly methodology for extraction of nickel from spent catalyst of fertilizer industry by adopting the chelating agents. The concept of chelation explored here to bind metal from spent catalyst and subsequently to be de-chelated by acid addition to extract metal. All chelation experiments were conducted in atmospheric reflux conditions and process parameters (reaction time, molar concentration of solvent, solid-liquid ratio of reacting mixture, pH, reaction temperature, particle size) were optimized in order to maximize the metal extraction. Three different chelating agents (EDTA, DTPA, and NTA) were employed for extraction of Ni. EDTA has been used earlier in the literature for Ni extraction with solid to liquid ratio 1:50. To reduce the S:L ratio, experiments were conducted with S/L 1:20 and very less increment were seen with increasing S/L. It was also observed that at optimized reaction conditions, DTPA showed the highest (84%) Ni extraction among all three chelating agents. Recovery of DTPA was not more than 40% at atmospheric condition, while at refrigeration condition, DTPA recovery was improved and reached upto 80-86%. Recovery of EDTA solid (93%-97%) was highest among these chelating agents. Comparative evaluation of various chelating agents on the basis of extraction efficiencies concluded that complexing ability of DTPA is slightly higher than EDTA but poor biodegradability and less recovery of DTPA makes this chelating agent less feasible to use. NTA showed its maximum 65% Ni extraction. Less extraction of Ni using NTA is due to its quadridentate structure which causes lesser stability of Ni-NTA complex. Characterization of spent catalyst and chelating agents was performed to understand the structural and phyisco-chemical properties.
机译:由于工业中对复杂金属复合材料的需求不断增加以及减少金属浪费,从废催化剂中转移重金属至关重要。目前的研究涉及采用螯合剂从肥料工业的废催化剂中提取镍的环保方法的发展。此处探讨了螯合的概念,以结合废催化剂中的金属,随后通过添加酸以萃取金属将其螯合。所有螯合实验均在大气回流条件下进行,工艺参数(反应时间,溶剂摩尔浓度,反应混合物的固液比,pH,反应温度,粒径)得到了优化,以最大限度地提取金属。三种不同的螯合剂(EDTA,DTPA和NTA)用于提取镍。 EDTA已在文献中较早地用于固液比为1:50的镍萃取中。为了降低S:L比率,以1/20的S / L进行实验,并且随着S / L的增加,观察到的增量很小。还观察到,在优化的反应条件下,DTPA在所有三种螯合剂中均显示出最高的镍提取率(84%)。在大气条件下,DTPA的回收率不超过40%,而在冷藏条件下,DTPA的回收率得到提高,达到80-86%。在这些螯合剂中,EDTA固体的回收率最高(93%-97%)。根据萃取效率对各种螯合剂进行的比较评估得出的结论是,DTPA的络合能力略高于EDTA,但生物降解性差且DTPA回收率低,使得该螯合剂的使用不太可行。 NTA表现出最大的65%Ni提取率。使用NTA提取镍的原因较少,这是由于其四方结构降低了Ni-NTA络合物的稳定性。进行废催化剂和螯合剂的表征以了解其结构和物理化学性质。

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