Separation of Minor Actinides from High-Level Liquid Waste Using Novel Silica-Based Butyl-BTP Adsorbents

To separate the long-lived minor actinides (MA = Am, Cm) from high-level liquid waste (HLLW), we have been studying an advanced separation process via selective adsorption that uses minimal amounts of organic solvent and compact equipment. The process consists of two separation columns packed with a CMPO (octyl(phenyl)-N,N-diisobutylcarbamoyl-methyl phosphine oxide) adsorbent for elemental group separation and a soft-donor named the R-BTP (2,6-bis-(5,6-dialkyl-1,2,4-triazine-3-yl) pyridine) adsorbent for the isolation of MA from lanthanides (Ln). In this work, the effects of nitrate ion (NO3−) on the adsorption behavior of Am(III) and a typical fission product Ln(III) onto the isoBu-BTP/SiO2-P adsorbent were studied experimentally. Then, the desorption properties of the adsorbed element were examined using different eluting agents. A hot test for the separation of MA from the fission product Ln in a genuine MA containing effluent from the irradiated MOX-fuel treatment process was carried out using a nBu-BTP/SiO2-P packed column. It was found that the separation factor between Am(III) and Ln(III)-FP is over 100 in the measured 0.5–4 M NO3−. The adsorbed elements could be effectively eluted off using a complexing agent such as DTPA or pure water. Complete separation between MA and Ln was achieved in the column results, indicating that the proposed MA separation process is feasible in principle.


Introduction
As a final disposal method for the high-level liquid waste (HLLW) generated by spent fuel reprocessing, as with the PUREX process, the geological disposal of vitrified HLLW has been proposed and investigated worldwide. Minor actinides (MAs; Am, Cm, etc.), which are alpha emitters with long half-lives (e.g., 241 Am t1/2 = 432.2y, 243 Am t1/2 = 7.38 × 103 y), contribute most of the long-term radiotoxicity of high-level liquid waste [1,2]. The efficient separation of MAs is of great significance for the final geological disposal of the HLLW and is also an essential component of the partition and transmutation (P&T) strategy to transmute the long-lived nuclides into short-lived or stable nuclides [3][4][5]. The fission products lanthanides (Lns) are much more abundant than MAs in HLLW and are neutron poisons, so they need to be separated before MA transmutation. Since Ln(III) possesses very similar chemical properties to MA(III) in solution, the selective separation of MA(III) from Ln(III) has become one of the most challenging technical problems in HLLW partitioning [3][4][5][6][7]. From the viewpoints of minimizing the long-term radiotoxic risk to the environment and facilitating the P&T strategy, the separation of the long-lived minor actinides (Am, Cm) from HLLW is an important task. For this purpose, we have been studying an advanced separation process involving a selective adsorption technology that uses a minimal organic solvent and compact equipment [2,3,5,[8][9][10]. The schematic Toxics 2022, 10, 741 2 of 11 flowsheet of this process is shown in Figure 1 [11]. The process is constituted by two separation columns packed with CMPO (octyl(phenyl)-N,N-diisobutylcarbamoyl-methyl phosphine oxide) and R-BTP (2,6-bis-(5,6-dialkyl-1,2,4-triazine-3-yl)pyridine, R = alkyl group) adsorbents, respectively. In the first column, the elements contained in the HLLW can be partitioned into (a) non-adsorptive fission products (FP), (b) MA-Ln, and (c) Zr-Mo, according to their different adsorption and elution properties with CMPO and the eluents. The MA-Ln effluent is then supplied to the second column packed with the R-BTP adsorbent, where the MA is expected to be selectively isolated from the Ln fission products, since the trivalent actinides have much stronger adsorbability onto R-BTP than the trivalent lanthanides [4][5][6][7]. For this process, we synthesized some new silica-based adsorbents by impregnating CMPO or R-BTP into a styrene-divinylbenzene copolymer, which was immobilized in porous silica particles with a mean diameter of 60 µm (SiO 2 -P). Compared to conventional polymeric matrix adsorbents, these highly porous silica-based adsorbents with a small particle size have faster diffusion kinetics with a relatively lower pressure drop in packed columns, making them suitable for efficient chromatographic separation [8,9]. In our previous work, it was demonstrated that Am together with the fission product Ln can be successfully separated from other FPs contained in a genuine HLLW solution, which was generated from an irradiated MOX fuel treatment process using a CMPO/SiO 2 -P packed column [12].

Reagents
241 Am(III) and 152 Eu(III) were obtained from a stock solution from the China Institute of Atomic Energy (CIAE). Commercially available Ln(NO3)3•nH2O at 99.9% purity was used to prepare the adsorption solution. The other agents used were of analytical grade. The aqueous solutions were prepared with deionized water.

Synthesis and Characterization of Materials
As the support for the nBu-BTP, the silica/polymer composite support (SiO2-P) de-  It is well known that the mutual separation of the trivalent actinides with 5f-orbital electrons and the lanthanides with 4f-orbital electrons is one of the most difficult tasks in the nuclear fuel cycle due to their very closed ionic size and similar chemical properties. At the end of last century, Kolarik et al. reported that a multidentate nitrogen donor ligand, 2,6-bistriazinylpyridine (BTP), exhibits much higher extraction selectivity for Am(III) than Ln(III) [6,7]. Since 2000, we have synthesized some new R-BTP ligands with different alkyl groups (C = 1-8) and studied their separation behavior for MA and Ln and their chemical and radiation stability in nitric acid solutions [13][14][15]. As a result, the adsorption affinity and stability strongly depend on the structure of the alkyl group in 2,6-bis-(5,6-dibutyl-1,2,4triazine-3-yl)pyridine adsorbent. It was found that Bu-BTP/SiO 2 -P showed significantly higher adsorption ability and selectivity for Am(III) than Ln(III). The separation experiment results for a simulated HLLW containing trace amounts of 243 Am(III) and typical Ln(III) using a nBu-BTP/SiO 2 -P packed column demonstrated that the Am(III) was completely separated from the Ln(III) [15].
Since Am(III) is present as a cationic ion in weak nitric acid solutions and R-BTP is a neutral compound, their coordination reaction requires anionic nitrate to form a stably neutral complex. In this work, we investigate the effects of the nitrate ion (NO 3 − ) concentration on the adsorption behavior of Am(III) and the typical fission product Ln(III) on the Bu-BTP/SiO 2 -P adsorbent. Then, the desorption(elution) properties of the adsorbed element are examined using different eluting agents. A small-scale column separation experiment using a simulated high-level waste solution and a hot test for a genuine MAcontaining effluent obtained from an irradiated MOX-fuel treatment process are carried out to verify the feasibility of the proposed separation process.

Reagents
241 Am(III) and 152 Eu(III) were obtained from a stock solution from the China Institute of Atomic Energy (CIAE). Commercially available Ln(NO 3 ) 3 •nH 2 O at 99.9% purity was used to prepare the adsorption solution. The other agents used were of analytical grade. The aqueous solutions were prepared with deionized water.

Synthesis and Characterization of Materials
As the support for the nBu-BTP, the silica/polymer composite support (SiO 2 -P) developed in our previous work was utilized. It contains a macroreticular styrene-divinylbenzene copolymer that is immobilized in porous silica particles with a pore size of 0.6 µm and mean diameter of 60 µm. The nBu-BTP was impregnated into the SiO 2 -P support at 33.3 wt% of Bu-BTP and the preparation procedure was described in our previous works [8,9]. The chemical structure of the nBu-BTP and an SEM image of nBu-BTP/SiO 2 -P adsorbent are illustrated in Figure 2. The IsoBu-BTP/SiO 2 -P adsorbent was prepared using the vacuum impregnation method [2]. Typically, 5 g isoBu-BTP dissolved in CH 2 Cl 2 was impregnated into 10 g of SiO 2 -P under vacuum conditions using a rotary evaporator with a pressure controller.

Batch Adsorption Experiment
Batch adsorption experiments were conducted to evaluate the adsorbability of Am(III) and some trivalent Ln fission products towards the isoBu-BTP adsorbent. A determined volume (typically 5 cm 3 ) of a sample solution containing 10 mM of each Ln(III) was spiked with the radioactive nuclides 243 Am and 152 Eu. A weighed amount of adsorbent (typically 0.25 g) was combined in a glass vial with a Teflon stopper with the sample solution. The resultant mixture was maintained in a water bath shaker kept at 298 K and mechanically shaken at 120 rpm until reaching an equilibrium state. After adsorption, the aqueous phase was filtrated through a membrane filter with 4.5 µ m pores and sampled for quantitative measurements. The gamma activities of 243 Am and 152 Eu were detected using a γ-ray spectrometer with a high-purity germanium detector (Seiko EG&G). The average count rate was taken from three measured values to determine the activity. The concentration of stable Ln elements in the aqueous phase was analyzed using an ICP-AES instrument. The distribution coefficient (Kd) was calculated using Equation (1). Typical experiments were performed in triplicate. The relative error rates of the adsorption experiments were all less than 5%.
where C0 and CS denote the element concentration, while A0 and AS present the nuclide activity in the aqueous phase before and after adsorption, respectively. WR indicates the weight of the dry adsorbent (kg) and vs. the volume of the aqueous phase (dm 3 ).

Batch Adsorption Experiment
Batch adsorption experiments were conducted to evaluate the adsorbability of Am(III) and some trivalent Ln fission products towards the isoBu-BTP adsorbent. A determined volume (typically 5 cm 3 ) of a sample solution containing 10 mM of each Ln(III) was spiked with the radioactive nuclides 243 Am and 152 Eu. A weighed amount of adsorbent (typically 0.25 g) was combined in a glass vial with a Teflon stopper with the sample solution. The resultant mixture was maintained in a water bath shaker kept at 298 K and mechanically shaken at 120 rpm until reaching an equilibrium state. After adsorption, the aqueous phase was filtrated through a membrane filter with 4.5 µm pores and sampled for quantitative measurements. The gamma activities of 243 Am and 152 Eu were detected using a γ-ray spectrometer with a high-purity germanium detector (Seiko EG&G). The average count rate was taken from three measured values to determine the activity. The concentration of stable Ln elements in the aqueous phase was analyzed using an ICP-AES instrument. The distribution coefficient (K d ) was calculated using Equation (1). Typical experiments were performed in triplicate. The relative error rates of the adsorption experiments were all less than 5%.
where C 0 and C S denote the element concentration, while A 0 and A S present the nuclide activity in the aqueous phase before and after adsorption, respectively. W R indicates the weight of the dry adsorbent (kg) and vs. the volume of the aqueous phase (dm 3 ).

Hot Column Separation Experiment
The HLLW sample solution containing 6 M of HNO 3 was generated from the anion exchange process that had separated the U, Pu, Pd, Ru, and Tc from a spent LWR fuel solution [12,16]. Prior to the separation of MA/Ln, the HLLW sample was fed to a CMPO/SiO 2 -P packed column for the elemental group partitioning according to the procedure shown in Figure 1. From this column, a genuine MA-Ln effluent containing Am, Cm, and almost all the FP lanthanides was obtained [12]. The solid-state NaNO 3 was . The pH value of the effluent was estimated to be around 1. Table 1 illustrates the analytic results of the representative nuclides contained in the sample solution. In this work, we conducted a separation experiment for the genuine MA-Ln effluent using a Pyrex glass column with a 10 mm inner diameter and 300 mm length. The nBu-BTP/SiO 2 -P adsorbent was filled to the column in a slurry state under 2-3 bars of nitrogen gas pressure. The temperature of the column and the throughput liquid phase were maintained constantly at 298 K. Before the chromatographic operation, the nBu-BTP/SiO 2 -P packed in the column was conditioned by pumping 100 cm 3 of 1 M NaNO 3-0.01 M HNO 3 solution through the column. Next, 30 cm 3 of the sample solution was fed into the column at a constant flow rate of 1.0 cm 3 /min (0.76 m/h) using an HPLC metering pump. Subsequently, 70 cm 3 of 0.3 M NaNO 3 and 110 cm 3 of H 2 O were supplied to the column as eluents, respectively. The outlet effluents from the column were collected using an auto-fractional collector in 10 cm 3 aliquots. The concentrations and activities of the nuclides in each aliquot were quantitatively measured using ICP-MS and alfa/gamma spectrometry. Figure 3 presents the distribution coefficients (K d ) of 241 Am(III) and 152 Eu(III) towards the isoBu-BTP/SiO 2 -P adsorbent with the change in the initial HNO 3 concentration in the solution. The adsorption affinity of Am(III) increased drastically with the increase in HNO 3 concentration and the K d reached near 5 × 10 3 cm 3 /g in the range of 1-4 M HNO 3 . The K d of Eu(III) also increased with the increasing HNO 3 concentration, but the adsorbability of Eu(III) was much lower than that of Am(III). The separation factor (SF Am/Ln = ratio of K d -Am to K d -Eu) between Am(III) and Eu(III) is about 100 in the measured 0.5-4.0 M HNO 3 range, which would be high enough for their efficient separation by means of the chromatography method.

Adsorption and Desorption Behavior of Am(III) and Ln(III)
Since Bu-BTP is a neutral ligand, the adsorption of trivalent metal cations from nitric acid or nitrate solution towards the adsorbent is supposed to result from the following complexing reaction [2]: Because the stoichiometric ratio of M:NO 3 − is 1:3, the adsorption ability of trivalent MA strongly depends on the concentration of nitrate ion (NO 3 − ) surrounding the nitrogen ligand of the adsorbent (Figure 2). Nitric acid is a very strong acid, which almost completely liberates into a nitrate ion (NO 3 − ) and proton (H + ) in aqueous solutions. Therefore, the increase in adsorbability with HNO 3 corresponds to the increase in NO 3 − concentration. Notably, since the adsorption of Am(III) and Eu(III) drastically decreased when reducing the concentration of nitrate, and as they showed almost no adsorption in very dilute HNO 3 solution, the adsorbed elements are expected to be eluted out when decreasing the NO 3 − concentration in the chromatographic separation process. On the other hand, the mechanism for the soft donor ligands containing nitrogen or sulfur to exhibit a significantly higher adsorption affinity for trivalent actinides over lanthanides has not yet been clarified.
Because the stoichiometric ratio of M:NO3 − is 1:3, the adsorption ability of trivalent MA strongly depends on the concentration of nitrate ion (NO3 − ) surrounding the nitrogen ligand of the adsorbent (Figure 2). Nitric acid is a very strong acid, which almost completely liberates into a nitrate ion (NO3 − ) and proton (H + ) in aqueous solutions. Therefore, the increase in adsorbability with HNO3 corresponds to the increase in NO3 − concentration. Notably, since the adsorption of Am(III) and Eu(III) drastically decreased when reducing the concentration of nitrate, and as they showed almost no adsorption in very dilute HNO3 solution, the adsorbed elements are expected to be eluted out when decreasing the NO3 − concentration in the chromatographic separation process. On the other hand, the mechanism for the soft donor ligands containing nitrogen or sulfur to exhibit a significantly higher adsorption affinity for trivalent actinides over lanthanides has not yet been clarified. The effects of the nitrate (NaNO3) concentration on the Kd values of Am(III) and some trivalent lanthanides are shown in Figure 4. As can be seen, the adsorption ability of isoBu-BTP/SiO2-P towards both 241 Am(III) and Ln(III) increased with the NO3 − concentration, but the adsorbability of Am(III) is much higher than that of Ln(III). The separation factors between Am(III) and the Ln(III) are over 100 at a wide range of NO3 − concentrations, except SFAm/Dy. In addition, the adsorption of Ln(III) increased regularly with the atomic number and Dy(III) showed the strongest adsorption among the tested Ln(III) elements. In our previous work, we studied the coordination chemistry for the adsorption of some Ln(III) ions towards isoBu-BTP/SiO2-P by means of an EXAFS analysis using the Ln(III)adsorbed isoBu-BTP/SiO2-P samples, e.g., Sm(III), Eu(III), Gd(III), and Dy(III) [2,5]. It was found that the [Ln(isoButyl-BTP/SiO2-P)3] 3+ complex is the dominant species and the Ln(III)-N bond length in the first coordination layer become shorter as the atomic number of Ln(III) increases, which indicates the enhanced interaction between Ln(III) and the isoBu-BTP/SiO2-P adsorbent as the atomic number increases. Therefore, the relationship between adsorption affinity of isoBu-BTP/SiO2-P and the different Ln(III) shown in Figure  4 can be reasonably explained by the EXAFS analysis results.
The lanthanide fission products resulting from the 235 U fission reaction mostly include the light lanthanides from La to Tb, while the yield of Dy is almost negligible [17]. Since Dy(III) exhibits the strongest adsorbability among the lanthanides onto the R-BTP adsorbents and its adsorption behavior is similar to Am(III), it can be used as a simulated element of Am in some cases [18][19][20].  The effects of the nitrate (NaNO 3 ) concentration on the K d values of Am(III) and some trivalent lanthanides are shown in Figure 4. As can be seen, the adsorption ability of isoBu-BTP/SiO 2 -P towards both 241 Am(III) and Ln(III) increased with the NO 3 − concentration, but the adsorbability of Am(III) is much higher than that of Ln(III). The separation factors between Am(III) and the Ln(III) are over 100 at a wide range of NO 3 − concentrations, except SF Am/Dy . In addition, the adsorption of Ln(III) increased regularly with the atomic number and Dy(III) showed the strongest adsorption among the tested Ln(III) elements. In our previous work, we studied the coordination chemistry for the adsorption of some Ln(III) ions towards isoBu-BTP/SiO 2 -P by means of an EXAFS analysis using the Ln(III)adsorbed isoBu-BTP/SiO 2 -P samples, e.g., Sm(III), Eu(III), Gd(III), and Dy(III) [2,5]. It was found that the [Ln(isoButyl-BTP/SiO 2 -P) 3 ] 3+ complex is the dominant species and the Ln(III)-N bond length in the first coordination layer become shorter as the atomic number of Ln(III) increases, which indicates the enhanced interaction between Ln(III) and the isoBu-BTP/SiO 2 -P adsorbent as the atomic number increases. Therefore, the relationship between adsorption affinity of isoBu-BTP/SiO 2 -P and the different Ln(III) shown in Figure 4 can be reasonably explained by the EXAFS analysis results.
The lanthanide fission products resulting from the 235 U fission reaction mostly include the light lanthanides from La to Tb, while the yield of Dy is almost negligible [17]. Since Dy(III) exhibits the strongest adsorbability among the lanthanides onto the R-BTP adsorbents and its adsorption behavior is similar to Am(III), it can be used as a simulated element of Am in some cases [18][19][20].  The SEM-EDS analysis result for the Dy-loaded isoBu-BTP/SiO2-P is shown in Figure  5. After the adsorption experiment, the Dy-loaded isoBu-BTP/SiO2-P adsorbent was inlaid into an epoxy resin. The particle size of the isoBTP/SiO2-P adsorbent is around 50 µ m. As can be seen, the Dy(III) was adsorbed from the surface into the inside center of the particle and then distributed across the whole cross-section of the adsorbent. The images prove that the Dy(III) was evenly adsorbed inside the isoBu-BTP/SiO2-P particles, not just on the surface. To examine the desorption behavior of the trivalent metal ions from isoBu-BTP/SiO2-P, batch desorption experiments were conducted using different eluting solutions. Figure  6 shows the effect of the eluting agent on the desorption rate of the Dy(III) from the loaded isoBu-BTP/SiO2-P adsorbent. As can be seen, DTPA(diethylenetriaminepentaacetic acid) exhibited highest desorption rate of the Dy(III) ions. DTPA is an aqueous soluble nitrogen bearing a complexing agent and can coordinate with Dy(III), resulting in its desorption from the adsorbent. On the other hand, the adsorbed Dy(III) was quite effectively eluted out by the water due to a drastic decrease in the nitrate concentration in the adsorbent. The SEM-EDS analysis result for the Dy-loaded isoBu-BTP/SiO 2 -P is shown in Figure 5. After the adsorption experiment, the Dy-loaded isoBu-BTP/SiO 2 -P adsorbent was inlaid into an epoxy resin. The particle size of the isoBTP/SiO 2 -P adsorbent is around 50 µm. As can be seen, the Dy(III) was adsorbed from the surface into the inside center of the particle and then distributed across the whole cross-section of the adsorbent. The images prove that the Dy(III) was evenly adsorbed inside the isoBu-BTP/SiO 2 -P particles, not just on the surface.  The SEM-EDS analysis result for the Dy-loaded isoBu-BTP/SiO2-P is shown in Figure  5. After the adsorption experiment, the Dy-loaded isoBu-BTP/SiO2-P adsorbent was inlaid into an epoxy resin. The particle size of the isoBTP/SiO2-P adsorbent is around 50 µ m. As can be seen, the Dy(III) was adsorbed from the surface into the inside center of the particle and then distributed across the whole cross-section of the adsorbent. The images prove that the Dy(III) was evenly adsorbed inside the isoBu-BTP/SiO2-P particles, not just on the surface. To examine the desorption behavior of the trivalent metal ions from isoBu-BTP/SiO2-P, batch desorption experiments were conducted using different eluting solutions. Figure  6 shows the effect of the eluting agent on the desorption rate of the Dy(III) from the loaded isoBu-BTP/SiO2-P adsorbent. As can be seen, DTPA(diethylenetriaminepentaacetic acid) exhibited highest desorption rate of the Dy(III) ions. DTPA is an aqueous soluble nitrogen bearing a complexing agent and can coordinate with Dy(III), resulting in its desorption from the adsorbent. On the other hand, the adsorbed Dy(III) was quite effectively eluted out by the water due to a drastic decrease in the nitrate concentration in the adsorbent. To examine the desorption behavior of the trivalent metal ions from isoBu-BTP/SiO 2 -P, batch desorption experiments were conducted using different eluting solutions. Figure 6 shows the effect of the eluting agent on the desorption rate of the Dy(III) from the loaded isoBu-BTP/SiO 2 -P adsorbent. As can be seen, DTPA(diethylenetriaminepentaacetic acid) exhibited highest desorption rate of the Dy(III) ions. DTPA is an aqueous soluble nitrogen bearing a complexing agent and can coordinate with Dy(III), resulting in its desorption from the adsorbent. On the other hand, the adsorbed Dy(III) was quite effectively eluted out by the water due to a drastic decrease in the nitrate concentration in the adsorbent.

Chromatographic Separation of Am(III) from Ln(III)
Prior to the hot test, a column dynamic adsorption-elution experiment using the isoBu-BTP/SiO2-P adsorbent was carried out for a mixed Ln(III) sample solution with Dy(III) as an analogue of Am(III). The feed sample contained 1 mM of Y(III), La(III), Ce(III), Nd(III), Sm(III), Eu(III), Gd(III), and Dy(III) in a 0.01 M HNO3-0.49 M NaNO3 solution, respectively. The elution curves of the Ln(III) ions are shown in Figure 7. As can be seen, the light Ln(III) ions, such as La(III), Ce(III), Nd(III), and Y(III), showed almost no adsorption and flowed out from the column with the feed sample and the rinsing solution. The Dy(III) was completely adsorbed and was effectively eluted off by 0.01 M DTPA as eluent. Small portions of Sm(III), Eu(III), and Gd(III) were adsorbed and were eluted together with Dy(III). It was found that the column dynamic adsorption-elution results show good agreement with the batch adsorption-desorption experiments.

Chromatographic Separation of Am(III) from Ln(III)
Prior to the hot test, a column dynamic adsorption-elution experiment using the isoBu-BTP/SiO 2 -P adsorbent was carried out for a mixed Ln

Chromatographic Separation of Am(III) from Ln(III)
Prior to the hot test, a column dynamic adsorption-elution experiment using the isoBu-BTP/SiO2-P adsorbent was carried out for a mixed Ln (III) sample   In our previous work, a hot test for an actual high-level liquid waste (HLLW) generated from an irradiated MOX fuel treatment process was carried out using a CMPO/SiO 2 -P adsorbent packed column. As a result, Am and Cm together with the fission product Ln were successfully separated from other FPs contained in the HLLW, resulting in an MA-Ln effluent with a pH of around 1 [12]. In this work, this weakly acidic MA-Ln effluent was adjusted to 0.3 M of NaNO 3 and then subjected to a nBu-BTP/SiO 2 -P packed column for Am/Ln separation. Figure 8 shows the results of the separation experiment for the genuine MA-containing effluent with the nuclide composition, as shown in Table 1. As can be seen, the Ln(III) represented by Nd(III) and Pr(III) showed almost no adsorption. They flowed out with the sample solution and the 0.3 M NaNO 3 rinsing solution. On the other hand, Am(III) and Cm(III) were strongly adsorbed by the nBu-BTP/SiO 2 -P adsorbent, and then were effectively eluted off using pure water as an eluent. A complete separation between MA (Am and Cm) and the Ln was achieved.
genuine MA-containing effluent with the nuclide composition, as shown in Table 1. As can be seen, the Ln(III) represented by Nd(III) and Pr(III) showed almost no adsorption. They flowed out with the sample solution and the 0.3 M NaNO3 rinsing solution. On the other hand, Am(III) and Cm(III) were strongly adsorbed by the nBu-BTP/SiO2-P adsorbent, and then were effectively eluted off using pure water as an eluent. A complete separation between MA (Am and Cm) and the Ln was achieved.
In the sample solution, small amounts of U, Pu, and Mo were contained. The elution profiles of these nuclides together with the MA and Ln are illustrated in Figure 8. It was found that U and Pu were also adsorbed by the adsorbent and efficiently eluted off by H2O together with the MA. Since the spent fuel solution was once reduced by electroreduction prior to the anion exchange separation process, the valence representations of U and Pu in the MA-Ln effluent were considered to be U(IV) and Pu(IV) or Pu(III), respectively [16]. From this experimental result, we can conclude that the U and Pu that remained in MA-Ln effluent could be effectively recovered together with the MA. On the other hand, the Mo showed very weak adsorption and behaved similarly to the non-adsorptive Ln(III).
These experimental results demonstrate that the proposed MA separation process shown in Figure 1 is feasible in principle. For future practical applications, further investigations including improvements of the radiation stability of the adsorbents and scale-up testing are required.  In the sample solution, small amounts of U, Pu, and Mo were contained. The elution profiles of these nuclides together with the MA and Ln are illustrated in Figure 8. It was found that U and Pu were also adsorbed by the adsorbent and efficiently eluted off by H 2 O together with the MA. Since the spent fuel solution was once reduced by electro-reduction prior to the anion exchange separation process, the valence representations of U and Pu in the MA-Ln effluent were considered to be U(IV) and Pu(IV) or Pu(III), respectively [16]. From this experimental result, we can conclude that the U and Pu that remained in MA-Ln effluent could be effectively recovered together with the MA. On the other hand, the Mo showed very weak adsorption and behaved similarly to the non-adsorptive Ln(III).
These experimental results demonstrate that the proposed MA separation process shown in Figure 1 is feasible in principle. For future practical applications, further investigations including improvements of the radiation stability of the adsorbents and scale-up testing are required.

Conclusions
The adsorption and desorption behavior of Am(III) and Ln(III) onto Bu-BTP/SiO 2 -P adsorbent were investigated. Column separation experiments using simulated and genuine MA effluent were carried out. The isoBu-BTP/SiO 2 -P exhibited much stronger adsorba-bility for 241 Am(III) than 152 Eu(III) and all of the Ln(III) ions in the acidic nitrate solution. The separation factor between Am(III) and Ln(III)-FP was over 100 in the measured 0.5-4 M NaNO 3 solution with a pH of 2. The adsorbed Am(III) and Ln(III) ions were effectively eluted out using DTPA or pure water as the eluents. The column experiment results demonstrated that the Ln(III)-FP showed almost no adsorption, while the Am(III) and Cm(III), as well as the residual U and Pu, were completely adsorbed by the adsorbent and eluted off by using water as an eluent. A complete separation between the MA and Ln was achieved, indicating that the proposed MA separation process is feasible in principle. Further investigations including improvements of the radiation stability of the adsorbents and scale-up testing are required.