Extraction and adsorption of U(VI) from aqueous solution using affinity ligand-based technologies: an overview
- 232 Downloads
In terms of energy resource recovery and environmental protection, the separation of U(VI) from aqueous solutions is vital. Adsorption and solvent extraction are the most common separation technologies, which are also widely used for uranium recovery or removal from aqueous solution. The linear structure of uranyl ion and its multiple coordination feasibilities offer great opportunities for its extractive and adsorptive separation. This review briefly summarized and analyzed the recent advances in the separation of uranyl ions from aqueous solutions, mainly focusing on the selective extraction and adsorption using affinity ligands-based technology, which is promising method due to the high selectivity, capable of recovering uranium at low concentration and complicate aqueous environment. The affinity ligands for uranyl ions, including organophosphorus, calixarenes, amidoxime, imidazole and other derivatives were introduced. These donor ligands for design of extraction solvents or adsorbents for the separation of uranyl ions were summarized. The further research on the coordination chemistry towards uranyl ions and removal mechanisms would provide vital information for the development of more effective ligands with higher affinity, stability and compatibility in various systems, which is still challenging.
KeywordsUranium Adsorption Extraction Amidoxime Calixarenes
Uranium (U) is an indispensable resource for nuclear fuel and a hazardous radionuclide of chemical toxicity or radioactivity at the same time. U(VI), in the form of uranyl ion (UO22+) and its various complexes, are soluble and widely existent in radioactive wastewater and seawater. A large quantity of U-containing wastewater is generated from the whole process of nuclear industry, from mining, processing, to reprocessing. For the recovery of uranium resource and the security of ecosystem, the selective isolation of U(VI) from aqueous solutions is of great importance.
The comparison of adsorption and extraction technologies
(1) High separation factor
(2) High selectivity
(3) Energy saving
(1) Third-phase formation
(2) Generation of secondary waste
(3) Solvent losses
Chelation; ion-association; etc.
(1) Low cost
(2) High capacity
(3) Easy operation
(1) Low selectivity
Coordination; ion exchange; etc.
There are several comprehensive reviews and reports on the uranium recovery from seawater or uranium removal from contaminated water (Chareyron et al. 2014; IAEA 1993; Katsoyiannis and Zouboulis 2013; Kim et al. 2013; Leoncini et al. 2017; Lindner and Schneider 2015; Veliscek-Carolan 2016; Husnain et al. 2018; Li et al. 2018; Madic et al. 2007). Aly and Hamza (2013) summarized different technology for U removal. Leoncini et al. (2017) and Abney et al. (2017) elaborated the knowledge regarding ligands for f-element extraction and adsorbent for the recovery of uranium from seawater, respectively. Kiegiel et al. (2013) summarized calixarenes’ application in solvent extraction and solid-phase extraction for the separation of UO22+. Radionuclide preconcentration and separation by solid-phase extraction technology was also reviewed by Mokhodoeva et al. (2011). These reviews elaborate the development of various technologies or mainly focus on specific technology. However, the specific review on the aspect of uranium separation technologies (extraction and adsorption) based on the coordinating agents is not yet sufficient. It would provide valuable insights into the design of new selective adsorbents towards uranium and the understanding of their adsorption mechanisms.
The goal of this review is to summarize affinity ligands-based methods, mainly solvent extraction and adsorption, for the selective separation of uranyl ions from aqueous solutions. Affinity ligands towards uranyl ions and their utilization in both fields are introduced. The comparison between both methods based on these ligands were also discussed.
2 Solvent extraction
Solvent extraction is based on the thermodynamic stability of different complexes in the different media. This method is known for high separation factor, low cost and energy saving. Uranium is the first element recovered by this method in large quantities (Aly and Hamza 2013). However, the solvent loss and reagent cost on the large scale applications reduce the economics of harvesting uranium from seawater, where adsorption method is more popular.
For practical use, extractant is required of a high affinity for uranyl ions, together with a good radiolytic and hydrolytic stability. According to the ‘CHON’ principle, extractants composed of only these atoms (C, H, O, and N) are preferable because no solid, radioactive residues would be produced after incineration (Kolarik 2008).
Over the years, many ligand systems have been developed for uranyl ions’ selective extraction, and several commercial processes have been proposed and widely utilized in the separation of actinide (typically U) from spent nuclear fuel (Veliscek-Carolan 2016). Many factors, including the concentration of uranyl ions, coexisting ions, and pH of the solutions, have influence on the extraction performance. Despite development of ligands, the focus of research has also been given to the development of alternative solvents, such as hydrophobic ionic liquids (Stockmann and Ding 2011; Cocalia et al. 2005).
2.1 Organophosphorus compounds
Currently, the most widely used commercial process for uranium separation from spent nuclear fuel dissolved in nitric acid is based on solvent extraction, namely Plutonium Uranium Reduction Extraction (PUREX) process (Lanham and Runion 1949). This process employs organophosphorus compound, namely tributyl phosphate (TBP), in long chain aliphatic hydrocarbon as solvent. The TBP-based PUREX includes three stages: the extraction of U(VI) and Pu(IV) by 30% TBP in kerosene from spent nuclear fuel dissolved in 3–6 M nitric acids; the separation of Pu from organic phases by reducing agents; and the stripping of U(VI) by dilute nitric acids. The extracted U(VI) are converted into oxides for reuse. This commercial process is technically and economically feasible for uranium recovery from spent nuclear fuel.
Since 1954 until today, tributyl phosphate (Fig. 2a) is the most technologically important extractant in processing and reprocessing of nuclear fuels (Paiva and Malik 2004). It demonstrates a good hydrolytic stability at extremely acidic conditions, and a good selectivity towards U(VI) with a high decontamination factor (106–108) (Sood and Patil 1996). The possible complexation stoichiometry between TBP and uranyl ions in HNO3 solutions (Stockmann and Ding 2011) using electrochemistry method is given in Fig. 2b. Complexation constants of 3.2 × 1011 (n = 3) and 3.9 × 1013 (n = 4) are identified by interfacial complexation reactions (Stockmann and Ding 2011). In high radiation environments, and will be gradually degraded during the extraction process (Mincher et al. 2009). This will affect the separation performance of TBP-based extraction process over time, because the dominant degradation product, dibutylphosphate, presents different extraction behaviors to TBP (e.g. a high affinity towards Zr) and will stimulate the formation of third phase. Washing with sodium carbonate is an effective way to remove its degradation products, but it is time-consuming. But for TPB-based adsorbents, TBP degradation would not be a problem for U recovery from seawater or mining waste, etc.
Other important organophosphorus ligands widely used in processing and reprocessing of nuclear fuels is the octyl(phenyl)-N,N-diisobutylcarbamoyl methylphosphine oxide (CMPO), whose structure is given in Fig. 1a. In TRans-URanium EXtraction (TRUEX) process (a modified form of PUREX), a combination of 1.2 M TBP and 0.2 M CMPO was utilized in paraffinic hydrocarbon diluent. The phosphine oxides of CMPO present a good coordination ability towards uranyl ions at acidic environment (Stockmann and Ding 2011) (Fig. 2a) and overcome the formation of third phase. The improved performance of CMPO derivative ligands could be obtained by construction them onto tripodal scaffolds (Sartain et al. 2015) or calixarenes.
There are also other organic phosphorus compounds derivatives being studied in different laboratories as extractants to recover uranium, including trioctylphosphine oxide (TOPO), dihexyl-N,N-diethylcarbamoyl-methylphosphonate (CMP), di-2-ethylhexyl phosphoric acid (D2EHPA), monododecyl phosphoric acid (DDPA), glycerophosphate, and di-butyl butyl phosphonate (DBBP). Singh et al. (2016) elaborated the development of these organic phosphorus compounds for uranium extraction from phosphoric acid.
2.2 Calixarene derivatives
The coordinating ability and selectivity of calixarene derivatives for uranyl ions should be attributed to their structure arrangements and functionalization. Their sophisticated architectures with affinity ligand groups in benzene units exactly could provide the required pseudoplanar penta- and hexacoordinate structures for the coordination of uranyl ions (Kiegiel et al. 2013). To permit the penetration of linear UO22+ into the calixarenes rings, exo-complex is firstly created, later changed into endo-complex after the high-energy conformation (Shinkai et al. 1987; Nagasaki et al. 1991), as shown in Fig. 3b. Advance characterization technologies (e.g. time-resolved laser fluorescence spectroscopy and extended X-ray absorption fine structure) provide powerful tools in the exploration of the coordination between calixarenes and uranyl ions. It is found that calixarene-based uranophiles usually form a 1:1 or 1:2 complex with UO22+ (Shinkai et al. 1987; Nagasaki et al. 1991). Furthermore, the presence of affinity ligands further contributes to their high efficiency. Calixarenes bearing ligands (e.g. P=O groups) proved more efficient than classical extractants (e.g. TBP, TOPO, and CMPO) (Śliwa 2002). Compared to them, only 1/100 to 1/10 of ligand concentrations of such extracting agents could reach an assumed extraction yield.
Several types of calixarene derivatives have been studied as extractants for uranyl ions’ separation at laboratories, but most are not yet in industrial application. Calixarene derivatives containing hydroxamates, hydroxypyridinone (HOPO) (Leydier et al. 2008), acid-amide (Beer et al. 2002), sulfocatecholamide (CAMS) (Leydier et al. 2008) or CMPO, were expressively designed for the selective coordination of uranyl ions. HOPO and CAMS calixarenes are more efficient to coordinate with uranyl ions at acidic/neutral pH and basic pH, respectively (Leydier et al. 2008). Additionally, the uranophile properties of calixarene and calixarene have aroused great interests (Shinkai et al. 1987). Kiegiel et al. (2013) elaborately summarized the finding of novel calixarene derivatives for uranyl extraction. More specific examples can be found in this review (Kiegiel et al. 2013). However, in most proposed process, the cost and toxic halogenated solvents is utilized, which is not acceptable in industrial utilization. Furthermore, calixarenes’ behavior at irradiation is still under investigation despite good chemical stability (Shinkai et al. 1986).
2.3 Amide type extractants
Amides extracting agent composed of only CHON atoms is a type of green extractant because of its simplified synthetic routes and benign degradation products. With a strong polarity, the –CO– group in the structure exhibits a good coordination ability towards uranyl ions. This type of extractants is regarded as an attractive alternative to organophosphorus compounds.
With only an amide group in its structure, the monoamide extracting agent could coordinate with metal ions with the help of its N or O atom separately or simultaneously. The alternation of alkyl groups on the monoamides could tune their extraction performance (Siddall 1960). For example, McCann et al. (2018) noticed that the straight chains of alkyl groups were more effective for hexavalent over tetravalent cations, whilst the performance of monoamides of branched chain of alkyl groups was the opposite. N,N-dihexyloctanamide (DHOA) is a typical monoamide compound (Drader et al. 2016). Compared to TBP, it exhibits more efficiency of U(VI) stripping using 0.01 M nitric acid (Manchanda 2004) and lower partitioning towards contaminant elements. However, it is susceptible to radiolysis, too. Compared to monoamide extracting agent, diamide one presents the same merits but a higher extracting performance towards Am. There are also other O-/N-donating ligands, such as Schiff base ligands, salon ligands, amides/diamides derivatives.
Adsorption is also a common technology for pollutants removal (Wang et al. 2018b; Wang and Zhuang 2019; Zhuang et al. 2019a, b), including uranyl ions. It is also regarded as the most promising method of uranium harvest from seawater (Abney et al. 2017). The removal of targeted pollutants into various adsorbents should be owing to various physicochemical interactions (Wang and Zhuang 2017). Among these forces, coordination is an important mechanism for the selective adsorption of various pollutants. The construction of adsorbents bearing affinity ligands is an efficient method for the efficiently adsorptive removal of targeted pollutants.
So far, various adsorbents bearing affinity organic ligands have been continuously reported for the selectively adsorptive removal of uranyl ions. The types of chelating ligands, supporting materials, and preparation methods have great effects on the adsorption performance towards uranyl ions.
Affinity ligands, including amidoxime, imidazole, and phosphoryl groups, together with the extractants developed in solvent extraction process, have been employed in adsorbents’ construction. These organic ligands physically captured or chemically grafted into adsorbents greatly promote their adsorption selectivity and capacity towards uranyl ions. Among these coordinating agents, amidoxime group is the most popular one owing to its simple structure, good stability, and, most importantly, high coordinating selectivity towards uranyl ions. That makes amidoxime-based adsorbents the dominate materials for uranium harvest from seawater. There are also other types of O-/N-containing ligands for uranyl ions, but most of them also present adsorption towards other coexisting ions.
Besides these coordinating ligands, the solid carrier is also necessary component of adsorbents. Generally speaking, solid materials regardless of adsorption capacities can be applied as the carriers of the ligands as long as they are stable and modifiable. Carboni et al. (2013) deliberately chose mesoporous carbon with a negligible background sorption capacity of U(VI) as the supporting solids of the functionalized adsorbent for the head-to-head comparison of U(VI) binding capacity of nine different organic ligands. For the utilization in harsh conditions (e.g. extreme pH and radiation), they are also required of good chemical/thermal and radiation stability. Various active groups (e.g. –OH, –COOH, and –NH2) on their structures could be covalently connected with moieties of efficient ligands. Furthermore, structures of high porosity and surface area are favor for the impregnation of extractants, the exposure of grafting sites/moieties, or the diffusion of adsorbates.
The feature and types of carriers for the grafting or impregnation
Various resins, chitosan, cellulose, polypropylene, nylon textiles, covalent organic frameworks, etc.
Silica, CNT, graphene (oxide)
Magnetic-based composites, metal–organic frameworks, etc.
The adsorption process is affected by many factors, including the pH of the solutions, coexisting ions, concentration of metal ions, temperature, and others. For example, higher remaining concentrations are observed at higher initial concentrations because of the limited adsorption sites, resulting in lower removal percentage of the U(VI). To date, adsorption has been regarded as the most promising technology for uranium recovery from seawater. The main difficulty of uranium adsorption lies in its low concentration relative to its coexisting ions. These coexisting ions may have competitive (e.g. V), coordinative (e.g. CO32−), or ionic effect on uranium adsorption. Specially, due to the economical and ecologic reasons, the physicochemical characteristics of the seawater should not be adjusted by chemical additives or heating.
3.1 Adsorbents bearing amidoxime ligands
Amidoxime functional group has been widely recognized as the most promising ligand for uranium adsorption. In 1980s, Schenk et al. (1982) systematically screened more than 200 kinds of adsorbents with different functional groups for uranyl ion uptake. Among these adsorbents, crosslinked poly(acrylamidoximes) was highly appreciated owing to its stability in seawater and high adsorption selectivity and capacity of U(VI). This work is followed by substantial research focusing on amidoxime-based adsorbents (Zhuang et al. 2018; Wu et al. 2018; Zhao et al. 2014b; Yuan et al. 2016; Wang et al. 2018b; Cheng et al. 2019), and numerous reviews on amidoxime-based adsorbents for uranium harvest (Abney et al. 2017). So far, the countable marine experiments have all involved amidoxime-based polymer adsorbents (Gill et al. 2016; Ladshaw et al. 2017).
Figure 5e demonstrated the universal method of amidoxime grafting. Firstly, acrylonitrile and other co-monomers can be grafted into the various supports with the help of free radicals generated by physical or chemical methods (Zhuang et al. 2018). Then, cyano groups (–CN) are converted into the desired amidoxime groups by the treatment of hydroxylamine and KOH conditioning. Compared with chemically initiated and thermally initiated polymerization, radiation-induced grafting polymerization (RIGP) exhibits good grafting ratio without additives. These advantages make RIGP widely adopted (Ladshaw et al. 2017).
Preparation conditions have a great influence on uranium adsorption capacity, including the radicals’ generated methods, additives, monomers choosing, and the ratio of these monomers, as well as KOH conditioning concentration, duration, and temperature (Tian et al. 2013). The alkaline conditioning of the amidoxime-based adsorbents can significantly enhance its uranium adsorption capacities due to the following two reasons: (a) the alkaline treatment can convert amidoxime group into hydrophilic carboxylate groups, and (b) the open chain amidoxime groups can be changed into cyclic imidedioxime, which can compete with carbonate for uranyl ions at seawater pH effectively (Tian et al. 2013; Ivanov and Bryantsev 2016). Das et al. (2016) conducted a parametric study on the KOH concentration, conditioning time, and temperature in terms of uranium adsorption capacity. Na et al. (2012) explored the optimal conditions of photoirradiation-induced grafting of acrylonitrile onto polypropylene. In terms of uranium adsorption capacity, the optimal conditions proved to be: concentration of acrylonitrile ≤ 1.0 M, a reaction time of 2 h and temperature of 60 °C.
The structure of adsorbent also plays a vital role in its adsorption performance. Ordered porous structure presents superiority as a decorating platform, where high density and accessible functional groups could be grafted. In comparison with amorphous polymers with same chemical compositions, covalent organic frameworks bearing amidoxime groups presented a rapider adsorption equilibrium and a higher uptake of uranyl ions owing to its uniform pore structures (Sun et al. 2018). Additionally, nanostructure is found favor for adsorption. The blow spinning strategy was adopted to produce poly(imide dioxime) nanofiber, whose thickness can be controlled and its mechanical strength can be strengthened by weaving. The nanostructure fibers with abundant imide dioxime sites showed a recorded high adsorption capacity (951 mg/g) in uranium spiked seawater (8 ppm), as well as a high capacity (8.7 mg/g) in natural seawater after 56 days’ exposure (Wang et al. 2018a).
Previously, our research group has grafted amidoxime groups into multiwalled carbon nanotubes (denoted as AO-MWCNTs) by RIGP method (Wu et al. 2018) and magnetic chitosan (denoted as MAO-chitosan) by chemical method (Zhuang et al. 2018). The introduction of amidoxime groups greatly increased their adsorption capacities towards uranyl ions. Faster adsorption equilibrium was observed in the adsorption of uranyl ions by AO-MWCNTs owing to the porous structure of multiwalled carbon nanotubes; whilst MAO-chitosan presented a higher adsorption capacity and the advantages of magnetic separation owing to higher content of amidoxime groups and the presence of magnetic Fe3O4.
3.2 Adsorbents bearing imidazole ligands
Imidazole and its derivatives have also attracted much attention for uranium adsorption. Due to the structure similarity to amidoxime groups, the nitrogen atom of imidazole groups can also be the donor to uranyl ions (Schettini et al. 2012). Furthermore, compared to amidoxime, imidazole and its derivatives presents a lower toxicity.
So far, several kinds of its derivatives, such as vinylimidazole (Pekel and Güven 2003), benzimidazole (Kitagaki et al. 2016) and dihydroimidazole (DIM) (Yuan et al. 2012), have been grafted into MOFs, SiO2, and other carriers, and they showed a good adsorption performance towards uranyl ions.
The newly emerging 2D material, COFs, was also utilized as the decorating platform of benzimidazole by post modification (Fig. 6b) (Li et al. 2015). The as-prepared adsorbent, denoted as COF-HBI, presented good a radiation resistance and thermostability, as well as fast adsorption equilibrium (~ 30 min), high uptake capacity (211 mg/g), and pH-dependent, endothermic and spontaneous adsorption process towards uranyl ions.
3.3 Adsorbents bearing phosphate ligands
The immobilization of various phosphate ligands onto solids as adsorbents for uranium adsorption have been widely reported. The referred phosphate ligands here do not contain the organophosphorus compounds developed in solvent extraction (e.g. TBP). The O-donating phosphate ligands present a good coordinating ability in the adsorption of uranyl ions. In seawater, the rate-limiting step of uranyl ions’ adsorption is the competition between ligands and carbonate. Compared to amidoxime groups, phosphate ligands can replace carbonate faster. However, besides uranyl ions, most phosphate derivative ligands also present good adsorption capacity towards other coexisting ions.
Phosphate-derivate immobilized on graphene oxides (GO) (Liu et al. 2015; Cai et al. 2017), chitosan, bacterial cellulose (Zhuang and Wang 2019), polyethylene (Shao et al. 2017), and silica (Lebed et al. 2011; Guo et al. 2017) have been reported, and they presented a good adsorption capacity for uranium, owing to the presence of phosphate-derivatives. Jayakumar et al. (2008) had a very short while useful review on the ten synthesis methods of phosphorylated chitin/chitosan, which could be used as a reference for the chemical modification of other adsorbents with phosphorylation. Specially, Shao et al. (2017) reported a uranium adsorption efficiency of ~ 39% by PO4/PE mass on the condition of 25 ± 1 °C, 24 h, 200 mg adsorbents, and 100 mL seawater. This work indicates the great potential of phosphate-based adsorbents for uranium uptake.
Nine different organic ligands functionalized mesoporous silica have been synthesized and compared for uranium adsorptive removal (Vivero-Escoto et al. 2013). Among these adsorbents, phosphonate-functionalized one showed the highest adsorption capacity in the condition of water or artificial seawater. However, large amounts of nonspecific physic-sorption resulting from the surface hydroxyl of mesoporous silica made the rigorous interpretation difficult. To solve this problem, mesoporous carbon with a negligible background sorption capacity of U(VI) was chosen as the support of the functionalized adsorbent (Carboni et al. 2013). The head-to-head comparison of U(VI) binding capacity between various amidoxime, carboxyl and phosphoryl on innocent support was consistent with previous research, indicating that the phosphoric acid-functionalized adsorbents could be the promising alternative for uranium removal. Similar results are also observed in other research (Li et al. 2016). Additionally, the adsorption of uranyl ions onto MC–O–PO(OH)2 was greatly affected by the pH values, and the inflection point of pH was close to the pKa value of the sorbent group.
3.4 Adsorbents bearing extractants
Compared with solvent extraction, solid adsorbents bearing organic compounds utilized in solvent extraction avoid organic solvents and the addition of other phase modifiers, as well as the associated problems (e.g. complicated operations, generation of third-phase, and explosive hazards).
Extractants can be physically or covalently incorporated into supporting solids for the selective separation of uranyl ions. The physical impregnation of extractants into porous materials via intermolecular forces is simpler, but covalent attachment method minimizes the loss of extractants. Additionally, subtle changes in ligand sterics may lead to great change in its reactivity (Bart and Meyer 2008), especially taking into account the sophisticated extractants (e.g. calixarenes).
The porous structure and easy modification of silica lead to various types of silica-based adsorbents for the uranyl adsorption, including porous silica impregnated by polymers, functionalized by silanes, or magnetized by incorporation of iron oxide (Veliscek-Carolan 2016). Extractants are either impregnated into porous structure or appended into its frameworks by covalent silane anchor groups. In addition, carbon nanotubes and polyacrylonitrile were also impregnated by compounds developed in solvent extraction. The as-prepared adsorbents presented efficient recovery of uranyl ions from HNO3-leaching solution (Mokhodoeva et al. 2011).
Polymer resins composing of extractants immobilized in porous insoluble matrix have been utilized for separation at the back end of the nuclear fuel cycle. Natural polymer material (e.g. chitosan and alginate) and commercial Amberlite XAD 7 are widely utilized to synthesize resins (Aly and Hamza 2013). The choice of porous supporters has a significant effect on adsorption performance (Alexandratos 2009). Two type of commercial resins, Amberlite XAD 7 and XAD 4, were compared as supporting materials for several types of monoamide compounds in terms of extraction performance towards uranyl ions. Results showed that acetyl amide extractants coated into XAD 7 was superior (Drader et al. 2016). Additionally, TBP immobilized in Amberlite XAD 7 and XAD 4, together with Levextrel OC 1023, are suggested for U and Pu separation from 3 to 5 M nitric acids. The adsorption kinetics of CMPO impregnated into different types of polymer matrices are different from each other owing to the differences in functionality and porosity of their structures. Furthermore, these resins are required of good mechanical strength, chemical stability, and porosity, which can be tailored by the types/amounts of crosslinkers and comonomers (Alexandratos 2009).
Nanofiber composed by polyacrylonitrile (PAN) and upper rim functionalized calixarene bearing N-methylglucamine (Calix-NMG) was obtained by electrospinning (Özcan et al. 2016). The presence of calix-NMG in the nanofibers converted the hydrophobic properties into hydrophilic, and increased its chelating ability of uranyl ions. Additionally, the durability advantages of this fiber made it feasible in separation.
4 Concluding remarks and perspectives
Radioactive uranium is not only a vital component of nuclear fuel, but also a chemically toxic and radioactive element. The recovery of uranium from aqueous solution have been extensively explored in order to recover the carbon-free resource or decrease its environmental risks from aqueous solutions.
Solvent extraction and adsorption are the most commonly used methods of uranium separation from aqueous solutions. The linear structure of uranyl ion and its feasibility in coordination with various ligands offer great opportunities for its adsorptive or extractive removal. For years, various kinds of affinity organic ligands of uranyl ions have been developed, including amidoxime, imidazole, amide, organophosphorus, and calixarene derivatives. The discovery of these affinity ligands and their utilization in both methods promote the development of the selective separation of uranyl ions. Searching for more efficient ligands of uranyl ions and exploring their feasibility in solvent extraction and adsorption are still the challenging work in future research.
Currently, tributyl phosphate and amidoxime group-based material has been regarded as the most promising extractant and adsorbent for the selective extraction and adsorption of uranyl ions, respectively. TBP-based extraction processes for uranium separation from spent nuclear fuel have been put into industrial application with a commercial success; whilst amidoxime-based adsorbents make uranium recovery from seawater become a technologically viable alternative to terrestrial mining. Great efforts are being made to solve the defaults in both methods and searching for more efficient alternative materials or methods. Furthermore, there are other kinds of extractants (e.g. calixarene derivatives and amide types ligands) and adsorbents (imidazole-based, phosphate-based adsorbents) under development, yet most are in the initial stage far away from industrial application.
Affinity ligands-based technologies (e.g. adsorption and solvent extraction) are promising methods for the selectivity recovery of uranium despite of its low concentration in complicate aqueous environment. The progress of both technologies in the future research lies in the development of more effective ligands of higher affinity, stability, and compatibility in various systems. Furthermore, the exploration on their coordination chemistry towards uranyl ions and removal mechanisms by both methods would provide vital information for the development of new generation of ligands for uranyl ions.
Above all, the selective recovery of uranium from aqueous solutions is of great importance in terms of energy resource recovery and environmental protection. For the selective recovery of uranium, affinity ligands-based technologies (e.g. adsorption and solvent extraction) are developed and achieved great process, but are still facing many challenging.
The research was supported by the National Key Research and Development Program (2016YFC1402507), the National Natural Science Foundation of China (51578307) and the Program for Changjiang Scholars and Innovative Research Team in College (IRT-13026).
- Beer PD, Brindley GD, Danny Fox O, Grieve A, Ogden MI, Szemes F, Drew MGB (2002) Acid-amide calixarene ligands for uranyl and lanthanide ions: synthesis, structure, coordination and extraction studies. J Chem Soc 16:3101–3111Google Scholar
- Budnyak TM, Gladysz-Plaska A, Strizhak AV, Sternik D, Komarov IV, Majdan M, Tertykh VA (2018) Imidazole-2yl-phosphonic acid derivative grafted onto mesoporous silica surface as a novel highly effective sorbent for uranium(VI) ion extraction. ACS Appl Mater Interfaces 10:6681–6693CrossRefGoogle Scholar
- Chareyron B, Živčič L, Tkalec T, Conde M (2014) Uranium mining. Unveiling the impacts of the nuclear industry. EJOLT report no. 15Google Scholar
- Gill GA, Kuo L-J, Strivens JE, Wood JR, Schlafer NJ, Janke CJ, Das S, Mayes R, Saito T, Brown SS, Tsouris C, Tsouris C, Wai CM, Pan H-B (2016) Summary of adsorption capacity and adsorption kinetics of uranium and other elements on amidoxime-based adsorbents from time series marine testing at the pacific northwest national laboratory. Report no. PNNL-25899. https://doi.org/10.2172/1330924
- IAEA (1993) Uranium extraction technology. IAEA, Vienna. ISBN 92-0-103593-4Google Scholar
- Lanham WB, Runion TC (1949) Purex process for plutonium and uranium recovery. Report no. ORNL-479(Del.). O. R. N. Laboratory, Oak Ridge, TNGoogle Scholar
- Li J, Yang XD, Bai CY, Tian Y, Li B, Zhang S, Yang XY, Ding SD, Xia CQ, Tan XY, Ma LJ, Li SJ (2015) A novel benzimidazole-functionalized 2-D COF material: synthesis and application as a selective solid-phase extractant for separation of uranium. J Colloid Interface Sci 437:211–218CrossRefGoogle Scholar
- Ling CJ, Liu XY, Yang XJ, Hu JT, Li R, Pang LJ, Ma HJ, Li JY, Wu GZ, Lu SM, Wang DL (2017) Uranium adsorption tests of amidoxime-based ultrahigh molecular weight polyethylene fibers in simulated seawater and natural coastal marine seawater from different locations. Ind Eng Chem Res 56:1103–1111CrossRefGoogle Scholar
- Nagasaki T, Shinkai S (1991) Synthesis and solvent-extraction studies of novel calixarene-based uranophiles bearing hydroxamic groups. J Chem Soc 7:1063–1066Google Scholar
- Nagasaki T, Kawano K, Araki K, Shinkai S (1991) Kinetic studies of calixarene-based cyclic and non-cyclic ‘super-uranophiles’. J Chem Soc 9:1325–1327Google Scholar
- Shinkai S, Shiramama Y, Satoh H, Manabe O, Arimura T, Fujimoto K, Matsuda T (1989) Selective extraction and transport of UO2 2+ with calixarene-based uranophiles. J Chem Soc 8:1167–1171Google Scholar
- Śliwa W (2002) Calixarene complexes with transition metal, lanthanide and actinide ions. Croat Chem Acta 75:131–153Google Scholar
Open AccessThis article is distributed under the terms of the Creative Commons Attribution 4.0 International License (http://creativecommons.org/licenses/by/4.0/), which permits unrestricted use, distribution, and reproduction in any medium, provided you give appropriate credit to the original author(s) and the source, provide a link to the Creative Commons license, and indicate if changes were made.