Massey Daniel, Masters Andrew, Macdonald-Taylor Jonathan, Woodhead David, Taylor Robin
Department of Chemical Engineering, The University of Manchester, Oxford Road, Manchester M13 9PL, U.K.
National Nuclear Laboratory, 5th Floor Chadwick House, Warrington Road, Birchwood Park, Warrington WA3 6AE, U.K.
J Phys Chem B. 2022 Aug 25;126(33):6290-6300. doi: 10.1021/acs.jpcb.2c02198. Epub 2022 Aug 17.
Liquid-liquid extraction is a commonly used technique to separate metals and is a process that has particular relevance to the nuclear industry. There has been a drive to use environmentally friendly ligands composed only of carbon, hydrogen, nitrogen, and oxygen. One example is the i-SANEX process that has been developed to separate minor actinides from spent nuclear fuel. The underlying science of such processes, is, however, both complex and intriguing. Recent research indicates that the liquid phases involved are frequently structured fluids with a hierarchical organization of aggregates. Effective flow-sheet modeling of such processes is likely to benefit from the knowledge of the fundamental properties of these phases. As a stepping stone toward this, we have performed molecular dynamics simulations on a metal free i-SANEX system composed of the ligand ,,','-tetraoctyl diglycolamide (TODGA), diluent hydrogenated tetrapropylene (TPH), and polar species water and nitric acid. We have also studied the effects of adding -octanol and swapping TPH for -dodecane. It would seem sensible to understand this simpler system before introducing metal complexes. Such an understanding would ideally arise from studying the system's properties over a wide range of compositions. The large number of components, however, precludes a comprehensive scan of compositions, so we have chosen to study a fixed concentration of TODGA while varying the concentrations of water and nitric acid over a substantial range. Reverse aggregates are observed, with polar species in the interior in contact with the polar portions of the TODGA molecules and the organic diluent on the exterior in contact with the TODGA alkyl chains. These aggregates are irregular in shape and grow in size as the amount of water and nitric acid increases. At a sufficiently high polar content, a single extended cluster forms corresponding to the third phase formation. No well-defined bonding motifs were observed between the polar species and TODGA. The cluster size distribution fits an isodesmic model, where the Gibbs energy change of adding a TODGA molecule to a cluster ranges between 4.5 and 7.0 kJ mol, depending on the system composition. The addition of -octanol was found to reduce the degree of aggregation, with -octanol acting as a co-surfactant. Exchanging the diluent TPH for -dodecane also decreased the aggregation. We present evidence that this is due to the greater penetration of -dodecane into the reverse aggregates. It is known, however, that the propensity for the third phase formation is greater with -dodecane as the diluent than is the case with TPH, but we argue that these two results are not contradictory. This research casts light on the driving forces for aggregation, informs process engineers as to what species are present, and indicates that flow-sheet liquid-liquid extraction modeling might benefit by incorporating an isodesmic aggregation approach.
液 - 液萃取是一种常用的金属分离技术,该过程与核工业密切相关。目前人们一直在推动使用仅由碳、氢、氮和氧组成的环境友好型配体。一个例子是已开发用于从乏核燃料中分离次锕系元素的i - SANEX工艺。然而,此类过程的基础科学既复杂又引人入胜。最近的研究表明,所涉及的液相通常是具有聚集体层次结构的结构化流体。对此类过程进行有效的流程建模可能会受益于对这些相基本性质的了解。作为迈向这一目标的垫脚石,我们对由配体N,N',N'',N'''-四辛基二甘醇酰胺(TODGA)、稀释剂氢化四丙烯(TPH)以及极性物质水和硝酸组成的无金属i - SANEX体系进行了分子动力学模拟。我们还研究了添加正辛醇以及用正十二烷替代TPH的影响。在引入金属配合物之前先了解这个更简单的体系似乎是明智的。这样的理解理想情况下应通过在广泛的组成范围内研究体系性质来实现。然而,大量的组分排除了对组成进行全面扫描的可能性,所以我们选择在固定TODGA浓度的情况下,在相当大的范围内改变水和硝酸的浓度。观察到了反向聚集体,极性物质在内部与TODGA分子的极性部分接触,有机稀释剂在外部与TODGA烷基链接触。这些聚集体形状不规则,并且随着水和硝酸量的增加而增大。在足够高的极性含量下,会形成一个对应于第三相形成的单一扩展簇。在极性物质和TODGA之间未观察到明确的键合模式。簇尺寸分布符合等键合模型,其中向簇中添加一个TODGA分子的吉布斯自由能变化在4.5至7.0 kJ/mol之间,具体取决于体系组成。发现添加正辛醇会降低聚集程度,正辛醇起到了助表面活性剂的作用。将稀释剂TPH换成正十二烷也会降低聚集程度。我们提供的证据表明,这是由于正十二烷对反向聚集体的更大渗透。然而,已知以正十二烷作为稀释剂时第三相形成的倾向比TPH时更大,但我们认为这两个结果并不矛盾。这项研究揭示了聚集的驱动力,告知过程工程师存在哪些物种,并表明流程液 - 液萃取建模可能会因纳入等键合聚集方法而受益。