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Resin technology for gold recovery from alkaline cyanide solution.

机译:从碱性氰化物溶液中回收金的树脂技术。

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摘要

A review of the current literature on gold recovery from alkaline cyanide solution suggests resin ion exchange as a potential process alternative, if a suitable resin can be identified. In this regard four different adsorption systems, including commercially available and new synthetic resins, were investigated for recovery of gold from alkaline cyanide solution.; Commercially available, XAD-series, polyacrylates were found to exhibit a modest capacity (200 mg gold/kg resin, at 1 ppm gold in the aqueous phase) for gold adsorption at pH 10 under ambient conditions. Lower temperatures and higher ionic strengths promoted gold adsorption from cyanide solution.; Next, a class of recently identified gold solvent extraction systems was combined with the nonfunctional, or nonderivatized, XAD-16 resin beads to prepare solvent impregnated resins. Under ambient conditions and pH 9, at 1 ppm gold in the aqueous cyanide phase, gold adsorption by 0.5 M Adogen 283/TBP/XAD-16 and 0.5 M Adogen 283/TOP/XAD-16 resins were 1200 mg gold/l organic in the resin, and 56 mg gold/l organic in the resin, respectively.; A new class of phosphonate ester based polystyrene resins was studied. Gold loading with the most effective, monoester/monoacid type, resin was found to be ca. 1 g/kg resin at 1 ppm aqueous gold concentration. No pH dependency was observed. Gold loading was promoted by higher temperature and lower ionic strength.; Finally, amine/ester type bifunctional resins showed higher gold loadings than all other types of adsorbents examined. A typical tertiary amine/ester resin exhibited ca. 10 g gold/kg resin loading at 1 ppm aqueous gold concentration under ambient conditions and at pH 10. These resins showed slight pH dependency, being more pronounced for secondary type amine functional groups.; Generally no experimental evidence was found to show any specific bonding of the gold cyanide complex during adsorption. It is proposed that the adsorption reaction occurs by ion pairing of the gold cyanide anion with a suitable cation, M{dollar}sp+{dollar}, and the subsequent solvation at active sites in the resin structure, R, can be stated as, M{dollar}sp+{dollar} + Au(CN){dollar}sb2sp-{dollar} + R {dollar}leftrightarrow{dollar} {dollar}{lcub}rmoverline{lcub}Msp+cdots Au(CN)sb2sp-cdot R{rcub}.{rcub}{dollar}; The results of this research contributed to the understanding of gold cyanide loading and elution by organic based adsorbents. However, to identify a promising commercial resin for gold recovery from alkaline cyanide solution more work still remains to be done.
机译:对有关从碱性氰化物溶液中回收金的最新文献的评论表明,如果可以确定合适的树脂,则将树脂离子交换作为潜在的工艺选择。在这方面,研究了四种不同的吸附系统,包括市售的和新型的合成树脂,用于从碱性氰化物溶液中回收金。发现可商购的XAD系列聚丙烯酸酯在环​​境条件下在pH 10下具有适度的吸附金的能力(200 mg金/ kg树脂,在水中1 ppm的金时)。较低的温度和较高的离子强度促进了氰化物溶液中金的吸附。接下来,将一类最近确定的金溶剂萃取系统与非功能性或非衍生化的XAD-16树脂珠粒组合,以制备溶剂浸渍的树脂。在环境条件和pH值为9的情况下,氰化水溶液中的金含量为1 ppm时,0.5 M Adogen 283 / TBP / XAD-16和0.5 M Adogen 283 / TOP / XAD-16树脂对金的吸附为1200 mg / l有机物。树脂,树脂中有机金分别为56 mg / l。研究了一类新的基于膦酸酯的聚苯乙烯树脂。发现最有效的单酯/单酸型树脂的金负载量约为。 1 g / kg树脂在1 ppm含水金浓度下。没有观察到pH依赖性。较高的温度和较低的离子强度促进了金的负载。最后,胺/酯型双功能树脂比所有其他类型的吸附剂显示出更高的金载量。典型的叔胺/酯树脂表现出约。在环境条件和pH值为10时,在10 ppm的金金浓度下负载10 g金/ kg树脂。这些树脂显示出轻微的pH依赖性,对于仲型胺官能团更为明显。通常,没有实验证据表明在吸附过程中氰化金络合物有任何特定的键合。提出吸附反应是通过氰化金阴离子与合适的阳离子M {dol} sp + {dollar}的离子配对发生的,随后在树脂结构中活性位点R的溶剂化可以表示为M {dol} sp + {dollar} + Au(CN){dollar} sb2sp- {dollar} + R {dollar} leftrightarrow {dollar} {dol} {lcub} rmoverline {lcub} Msp + cdots Au(CN)sb2sp-cdot R {rcub}。{rcub} {dollar};这项研究的结果有助于理解有机基吸附剂对氰化金的负载量和洗脱的影响。但是,要确定一种从碱性氰化物溶液中回收金的有前途的商业树脂,还有更多工作要做。

著录项

  • 作者

    Akser, Mustafa.;

  • 作者单位

    The University of Utah.;

  • 授予单位 The University of Utah.;
  • 学科 Engineering Metallurgy.
  • 学位 Ph.D.
  • 年度 1987
  • 页码 214 p.
  • 总页数 214
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类 冶金工业;
  • 关键词

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