Efficient separation of vanadium from chromium by a novel ionic liquid-based synergistic extraction strategy

• Published in: Chemical engineering journal (Lausanne, Switzerland : 1996) Switzerland : 1996), 2015-03, Vol.264, p.487-496
• Main Authors: Zhao, Junmei, Hu, Qiaoyu, Li, Yingbo, Liu, Huizhou
• Format: Article
• Language: English
• Subjects: [A336][NO3]; Acidified N1923; Chromium; Chromium(IV); Extraction; IL-based extraction; Mathematical analysis; Nitrates; Separation; Strategy; Vanadium; Vanadium(V)
• ISSN: 1385-8947; 1873-3212
• DOI: 10.1016/j.cej.2014.11.071

•Pure IL [A336][NO3] plus [RNH3][NO3] was used to extract and separate V from Cr.•It shows a notable synergistic effect for V with improved separation factor βV/Cr.•IL is not only extractant but also good solvent for the ion-type extracted species.•Anion exchange mechanism between NO3− and V4O124− (or V3O93−) was confirmed.•IL phase can be recycled through stripping the loaded vanadium by 0.5M NaNO3. Ionic liquid (IL)-based extraction is a promising and environmentally benign separation technology. To develop sustainable extraction technologies, quaternary ammonium-based IL extraction strategy is attractable. In this work, the separation of vanadium(V) from chromium(VI) by pure tricaprylmethylammonium nitrate ([A336][NO3]) and organic acidified primary amine N1923 ([RNH3][NO3]) was systematically investigated. The optimal proportion of [A336][NO3] and [RNH3][NO3] was studied and results showed that the mixed [A336][NO3] and [RNH3][NO3] exhibited an obvious synergistic-effect for V(V). The extraction of V(V) was strongly dependent on the acidity of the aqueous phase and reaches maximum at pH 2.5–3, while the maximum separation coefficient (βV/Cr) was located at about pH 9.0. Moreover, βV/Cr could be improved through adjusting the molar concentration ratio of V/Cr. The interference of coexisting anions (nitrates, chlorides, sulfate and phosphate) on the extraction of V(V) was examined and the results showed that PO43−, NO3− and Cl− had negative effects at various degrees except for SO42−. The V(V) extraction behaviors could be properly described by Langmuir and pseudo-second-order rate equations. The maximum extraction capacity for V(V) was estimated as 1.877mmol/g at 303K. Increased temperature had little effect on the extraction capacity, but greatly improved the extraction rate. The typical anion exchange mechanism between NO3− and V4O124− (or V3O93−) was proposed for the current extraction system. The IL phase could be renewed through stripping the loaded vanadium by a 0.5M NaNO3 solution. This work demonstrated that quaternary ammonium IL containing a commercial organic extractant is an efficient and sustainable IL-based extraction strategy for the separation of vanadium from chromium, and as a result, the development of an IL-based extraction process is straightforwardly envisaged.