Dication-accelerated anion transport inside micropores for the rapid decontamination of pertechnetate

Dication-accelerated anion transport inside micropores for the rapid decontamination of pertechnetate 1 first-author 1 1 2 corresp * hanqinw@ustc.edu.cn * hanqinw@ustc.edu.cn hanqinw@ustc.edu.cn https://orcid.org/0000-0003-1265-9681 1 https://orcid.org/0000-0001-6786-942X 1 1 3 1 https://orcid.org/0000-0001-7968-1766 School of Nuclear Science and Technology, University of Science and Technology of China, Hefei 230026, China School of Nuclear Science and Technology, University of Science and Technology of China, Hefei 230026, China Department of Beam Material Science, SANKEN (The Institute of Scientific and Industrial Research), Osaka University, 8-1 Mihogaoka, Ibaraki, Osaka 567-0047, Japan Department of Beam Material Science, SANKEN (The Institute of Scientific and Industrial Research), Osaka University, 8-1 Mihogaoka, Ibaraki, Osaka 567-0047, Japan Radiochemistry Department of China Institute of Atomic Energy, China Institute of Atomic Energy, Beijing 102413, China Radiochemistry Department of China Institute of Atomic Energy, China Institute of Atomic Energy, Beijing 102413, China Over 70% of the treated contaminated water at the Fukushima Daiichi Nuclear Power Station contains radionuclides beyond the regulatory standard for discharge that need to be re-purified. Technetium-99 ( 99 Tc), mainly in the form of pertechnetate Tc(VII)O 4 − , is one of the main sources of long-term radiotoxicity that jeopardizes the environment and human health. Herein, we used a series of dicationic pyridinium (DCP) derivative groups (–Py + C n H 2 n N + Me 3 , n = 2, 3, and 5) to modify commercial Reillex 425 resins containing tertiary pyridyl groups to improve the adsorption performance of rhenium (Re, an analog of radioactive Tc) and Tc. As the quaternary pyridinium and ammonium sites in one DCP group can adsorb ReO 4 − simultaneously, DCP-modified Reillex 425 (Reillex-Cn) exhibited high maximum adsorption capacities for Re under neutral conditions. Adsorption capacities reached 344.8, 416.7, and 588.2 mg g −1 for Reillex 425-C2, Reillex 425-C3, and Reillex 425-C5, respectively. Intraparticle diffusion of ReO 4 − /TcO 4 − in Reillex 425-Cn was verified to be the rate-limiting step of adsorption. However, adsorption can be adjusted by the length of the alkyl spacers between the two positively charged N sites in DCP. –Py + C 2 H 4 N + Me 3 significantly enhanced intraparticle diffusion compared to –Py + C 5 H 10 N + Me 3 . The two positive sites in –Py + C 2 H 4 N + Me 3 would be laterally distributed, leading to a smaller steric hindrance for ReO 4 – /TcO 4 − transport inside the microporous channels. Meanwhile, the longer alkyl spacers in –Py + C 5 H 10 N + Me 3 formed hydrophobic microphases, repulsing the hydrated ReO 4 – /TcO 4 − anions. Thus, the adsorptions of both ReO 4 − and TcO 4 − on Reillex 425-C2 were faster than those on Reillex 425-C5. Moreover, Reillex 425-Cn exhibited an exothermic nature, good selectivity, excellent reusability, and strong salinity tolerance. This study provides a simple strategy to enhance the Tc removal performance of adsorbents containing abundant micropores, which implies enormous environmental and economic benefits. Quaternary pyridinium Dicationic pyridyl derivatives Pertechnetate Intraparticle diffusion Introduction 1 Approximately 6.3–7.7 × 1017 Bq of radioisotopes was released in the Fukushima nuclear accident (Level 7 event) [ 1 1 , 2 2 ], among which technetium-99 (99Tc) is one of the main sources of long-term radiotoxicity due to its long half-life of 2.13 × 105 years [ 3 3 ]. Tc mainly exists as soluble Tc(VII)O4− anions over a wide pH range, and have the same configuration as sulfate (SO42−) [ 4 4 - 6 6 4-6 ]. Thus, plants easily take up Tc in water, leading to its accumulation in animals. To date, treated contaminated water stored at the Fukushima Daiichi Nuclear Power Station has reached 92% of the total capacity, 71% of which (over 0.9 million tons) does not meet the regulatory standard for discharge [ 7 7 ]. Re-purification to remove Tc before discharge is necessary to alleviate concerns regarding non-tritium radioactive isotopes that induce Tc [ 8 8 ]. As all Tc isotopes are radioactive, non-radioactive rhenium (Re) with chemical properties similar to those of Tc is usually used as an analog [ 9 9 , 10 10 ]. Among the diverse methods developed for TcO4− (ReO4−) removal, including adsorption [ 11 11 - 13 13 11-13 ], solvent extraction [ 14 14 ], and reduction to oxide precipitates [ 15 15 , 16 16 ], adsorption remains the most practical approach for treating a large volume of water with low contaminant concentrations [ 17 17 ]. After the Fukushima nuclear accident, the Tokyo Electric Power Company employed a comprehensive apparatus utilizing different adsorbents for seawater decontamination. Cetyltrimethylammonium-modified zeolites were used to remove TcO 4 − and other organic pollutants [ 18 18 ]. However, inorganic zeolites exhibit low adsorption of TcO 4 − even after modification [ 19 19 ] owing to electrostatic repulsion [ 20 20 ]. Organic anion exchange resins show higher TcO 4 − adsorption amounts, but they suffer from slow adsorption rates and long equilibrium times [ 21 21 ], which decreases the utilization efficiency of packed columns in fixed-bed treatment. Both radiation stability and cost should be considered for commercial resins used for radionuclide removal. Therefore, radiation-resistant pyridyl-type resins, Reillex 425 series, have become the most popular resins for the adsorption of radioactive anions such as TcO 4 − [ 22 22 , 23 23 ], compared to various recently developed functional groups [ 24 24 - 26 26 24-26 ]. As tertiary pyridyl groups must be protonated to gain electrostatic attraction with anions, quaternary pyridinium is more suitable for the removal of TcO 4 − (ReO 4 − ) under neutral conditions [ 27 27 , 28 28 ]. Furthermore, it is expected to provide more ion-exchange sites and thus increase the adsorption capacity by bonding another positive moiety onto the pyridinium via quaternization [ 29 29 ]. Commercial macroporous Reillex 425 resins, which are functionalized with pyridyl, have a large number of micropores inside the beads. In addition to the functional groups, the pore structure of resins also essential for adsorption. Although abundant micropores provide a larger specific surface area and more adsorption sites, resulting in high adsorption amounts for adsorbents [ 30 30 ], they impede the diffusion of adsorbates, resulting in slower adsorption rates and longer equilibrium times [ 31 31 ]. Our previous work showed that appropriate dications could significantly promote the intraparticle diffusion of ReO 4 − anions in hierarchically mesoporous silica [ 32 32 ]. This indicates that it is possible to accelerate the transport of TcO 4 − inside micropores. Reillex 425 resins modified with suitable dications can potentially synchronously achieve high adsorption amounts and fast adsorption rates for TcO 4 − , which are important for the removal of TcO 4 − from treated water requiring secondary treatment. In this study, we modified Reillex 425 resins with a series of dicationic pyridinium (DCP) derivatives integrating pyridinium and ammonium moieties (Py + C n H 2n N + Me 3 , where n represents the length of alkyl spacers between two positive N sites), which resulted in efficient adsorption of ReO 4 − and TcO 4 − by enhancing intraparticle diffusion. The adsorption isotherms and kinetics of different DCP-modified Reillex 425 were investigated to illustrate the adsorption mechanism and the effects of alkyl spacer lengths on adsorbate transfer. The effects of pH, salinity, and concentrations of interfering ions were studied to evaluate the potential of DCP-modified Reillex 425 for practical Tc removal. Experimental section 1 Materials and chemicals 2 Detailed information on all materials and chemicals used in this work is provided in the Supporting Information. All materials and chemicals were used without further purification, except for the commercial Reillex 425 resins, which were washed to neutral pH (6–7) with ultrapure water. Preparation of the modified Reillex 425 2 Reillex 425 resins (1.0 g) were dispersed in 50 mL of ethanol, followed by the addition of iodomethane (0.667 mL), (2-Bromoethyl)trimethylammonium bromide (2-BETAB, 2.643 g), (3-Bromopropyl)trimethylammonium bromide (3-BPTAB, 2.793 g), and (5-Bromopentyl)trimethylammonium bromide (5-BPTAB, 3.093 g) to obtain the modified resins. These were labelled Reillex 425-Me, Reillex 425-C2, Reillex 425-C3, and Reillex 425-C5, respectively. The mixtures were heated to 60°C in a water bath shaker (Changzhou Guoyu Instrument Manufacturing Co., Ltd, WHY-2) in the dark for six days. The products were purified by washing five times with ultrapure water and once with ethanol. Modified Reillex 425 resins were obtained by drying under vacuum (60°C for 6 h). Characterization of the adsorbents 2 Scanning electron microscopy (SEM, ZEISS, EVO 18, operating at 10 kV) was used to observe the morphologies of the resins. The specific surface areas and pore size distributions were calculated using the Brunauer–Emmett–Teller and Barrett–Joyner–Halenda methods, respectively. This was done using the N 2 adsorption–desorption isotherms measured using a gas adsorption analyzer (Quantachrome Autosorb iQ, operating at 77 K). The chemical structures of the resins were characterized by solid-state 13 C cross-polarization magic angle spinning (CP-MAS) nuclear magnetic resonance (NMR) spectroscopy (Bruker AVANCE AV400 spectrometer), Fourier-transform infrared (FT-IR) spectroscopy (Thermo Nicolet 6700 spectrometer), and X-ray photoelectron spectroscopy (XPS, Thermo VG Scientific ESCALAB 250, equipped with a monochromatic Al K α X-ray source at an energy of 1486.6 eV). A NanoBrook 90Plus PALS particle analyzer (Brookhaven Instruments) was used to measure the surface charges of the resins. Before measuring the zeta potential, the granular resins were ground into powders. 1.00 mg of each powder was soaked in 0.5 mL ethanol and subsequently diluted in 100 mL of water, yielding a concentration of 0.01 mg mL −1 . Adsorption experiments 2 Batch adsorption experiments using ReO 4 − as an analog to radioactive TcO 4 − were conducted to evaluate the adsorption of different Reillex 425 resins. A single adsorption experiment was performed in 4 mL of Re solution (100 mg L −1 ) containing 1.60 mg of adsorbent on a shaker. The solution pH was adjusted to the required value by adding negligible volumes (1 mol L −1 ) of concentrated NaOH or HCl. The adsorbents were separated from the solution by filtration through a mixed cellulose ester membrane filter (0.22 μm) after adsorption. The following Eq. (1) was used to calculate the equilibrium adsorption amount ( q e ): <math display="block" id="M1"><mrow><msub><mi>q</mi><mtext>e</mtext></msub><mo>=</mo><mfrac><mrow><mrow><mo>(</mo><mrow><msub><mi>c</mi><mn>0</mn></msub><mo>−</mo><msub><mi>c</mi><mtext>e</mtext></msub></mrow><mo>)</mo></mrow><mo>×</mo><mi>V</mi></mrow><mi>m</mi></mfrac><mo>,</mo></mrow></math> where c 0 (mg L −1 ) and c e (mg L −1 ) are the initial and equilibrium concentrations of adsorbate ions in the solution, respectively, both of which were obtained using an inductively coupled plasma optical emission spectrometer (ICP-OES, PerkinElmer Optima 7300DV) , m (g) is the weight of the adsorbent, and V (L) is the volume of the solution. In selective adsorption experiments, competitive anions, including I − and Sb(OH) 6 − , were mixed with ReO 4 − . Re and Sb concentrations were measured using ICP-OES, and those of I − were determined using an inductively coupled plasma mass spectrometer (ICP-MS, Thermo-VG Scientific PlasmaQuad 3). The reusability of the modified Reillex 425 was evaluated using adsorption–desorption cycles. The adsorbents were dispersed in 20 mL of HNO 3 (2 mol L −1 ) and shaken for 6 h to desorb the ReO 4 − . The desorbed adsorbents were collected by precipitation and purified by washing with ultrapure water. The adsorption–desorption cycles were repeated five times. Before the adsorption of TcO 4 − , 0.1 mL of NH 4 TcO 4 stock solution was diluted by 1.9 mL of water, and mixed with 10 mL of Ultima Gold AB cocktail to determine the active concentration using a Packard Tri-Carb 2900 Liquid Scintillation Analyzer. The active 99 Tc concentration of the stock solution was 1250 Bq mL −1 (2 mg L −1 ). The batch adsorption experiment for Tc was carried out in a TcO 4 − solution obtained by diluting the stock solution 10 times (125 Bq mL −1 ) using the same procedure as for the adsorption of Re. After adsorption, 3 mL of the supernatant was mixed with 10 mL of Ultima Gold AB cocktail to measure the active concentration, and the Tc removal ratio was calculated using Eq. (2) , <math display="block" id="M2"><mrow><mtext>Removal ratio</mtext><mo>=</mo><mrow><mo>(</mo><mrow><mn>1</mn><mo>−</mo><mfrac><mrow><msub><mi>A</mi><mtext>t</mtext></msub></mrow><mrow><msub><mi>A</mi><mn>0</mn></msub></mrow></mfrac></mrow><mo>)</mo></mrow><mo>×</mo><mn>100</mn><mtext>%,</mtext></mrow></math> where A 0 (Bq) and A t (Bq) are the radioactivity of 99 Tc in solution before and after adsorption, respectively. Results and discussion 1 Synthesis of the modified Reillex 425 2 Reillex 425 resins were modified via a simple quaternization reaction, as illustrated in Scheme 1 Scheme 1 . The operation strongly affected the morphologies of the obtained products. The resin granules became powders when the reaction was performed under stirring ( Fig. S1 ), which is undesirable for column treatment of radioactive sewage. To avoid pulverization and maintain the granular appearance of the products, modification must be carried out using a shaker. As shown in Figs. 1a–1e Figs. 1a–1e , although modification in a shaker roughened the resin surface, the modified Reillex 425 resins retained their spherical shape with an average bead size around 0.7 mm ( Table 1 Table 1 ). The resultant Reillex 425-Cn (n = 2, 3, and 5, representing the number of carbon atoms between the pyridinium and ammonium moieties) showed the same color as the pristine Reillex 425 resin, whereas Reillex 425-Me turned yellow because of adsorption of iodine during modification [ 33 33 ]. All modified resins displayed the same type II N 2 adsorption–desorption isotherms as pristine Reillex 425 ( Fig. 1f Fig. 1f ). In the high-relative-pressure region ( P / P 0 > 0.8), the N 2 adsorption quantity increased sharply, confirming the macroporous structure [ 34 34 ]. The pore size distributions demonstrated that all the resins possessed hierarchically porous structures, integrating pores at different size scales, from macropores to micropores ( Fig. 1g Fig. 1g ). The modification did not alter the specific surface areas and total pore volumes of the Reillex resins ( Table 1 Table 1 ), suggesting that the porous structure, which is beneficial for adsorption, was retained after modification. Moreover, the average pore width slightly increased after modification, which might have enhanced the mass transfer of the adsorbates. a. This value refers to the moles of (N a + N b ) per gram of Reillex 425 resin, which was estimated according to the content of 4-vinylpyridine in Reillex 425 resin (75 wt %). b. These values refer to the moles of N c per gram of the Reillex 425-Cn and Reillex 425-Me resins. 1 1   1 1 Reillex 425 1 1 Reillex 425-C2 1 1 Reillex 425-C3 1 1 Reillex 425-C5 1 1 Reillex 425-Me 1 1 Specific surface area (m 2 g −1) 1 1 35.48 1 1 34.92 1 1 24.14 1 1 23.89 1 1 28.06 1 1 Pore volume (cm 3 g −1 ) 1 1 0.21 1 1 0.22 1 1 0.27 1 1 0.26 1 1 0.24 1 1 Modification efficiency 1 1 – 1 1 13.0% 1 1 21.2% 1 1 26.6% 1 1 48.6% 1 1 ρ m (mmol g −1 ) 1 1 7.143 a 1 1 0.929 b 1 1 1.517 b 1 1 1.897 b 1 1 3.474 b The 13 C SSNMR spectra provided direct evidence for the successful modification of Reillex 425 resins. The characteristic peaks of poly(4-vinylpyridine) and polystyrene are shown in Fig. 2a Fig. 2a . After tertiary pyridyl was quaternized with alkyltrimethylammonium, Reillex 425-C2 displayed three new peaks, ascribed to the carbon atoms in the spacer (C h1 and C h2 ) and trimethylammonium moiety (C i ), at 45.2, 63.6, and 55.4 ppm, respectively. Similarly, the characteristic peaks of all other modified Reillex 425 could be identified in the corresponding 13 C SSNMR spectra. From the FT-IR spectra in Fig. 2b Fig. 2b , the quaternization of pyridyl in Reillex 425 shifted the absorption peak for the in-plane C=C stretching vibration of the pyridyl ring from 1603 to 1637 cm −1 [ 35 35 , 36 36 ]. Other peaks at 1419 (aromatic semicircle C=N stretching of the pyridyl ring), 2927, and 2972 cm −1 (stretching vibration of saturated C–H in the polymer main chain) remained the same [ 37 37 ]. Reillex 425-C2 simultaneously displayed two peaks at 1603 and 1637 cm −1 , and the other modified Reillex 425 only exhibited the latter peak, which implied that Reillex 425-C2 had a smaller quaternization efficiency than the other modified resins. XPS analysis of the valence states of the N atoms was performed to quantitatively estimate the modification efficiency. From the N 1s spectrum ( Fig. 2c Fig. 2c ), Reillex 425 only contains two types of nitrogen — N atoms at tertiary (399.0 eV) and protonated (400.4 eV) pyridyl. After quaternization, all the Reillex 425-Cn displayed a new peak at higher binding energies around 401.5 eV, which was attributed to the quaternary N atoms in both pyridinium (N c ) and ammonium (N d ) moieties ( Figs. 2d–2f Figs. 2d–2f ) [ 3 3 ]. The modification efficiency, defined as the ratio of N c to (N a + N b + N c ) ( i.e. , all N atoms in tertiary pyridyl, protonated pyridyl, and quaternary pyridinium), was estimated at 13.0%, 21.2%, and 26.6% for Reillex 425-C2, Reillex 425-C3, and Reillex 425-C5, respectively. Evidently, longer spacers reduce the electrostatic repulsion between the two positive N atoms in one DCP group, thus increasing the modification efficiency [ 38 38 ]. For comparison, Reillex 425-Me, in which the pyridyl groups were functionalized with methyl groups, was prepared. The smaller steric hindrance and weaker electrostatic repulsion of methyl-endowed Reillex 425-Me with a significantly higher modification efficiency of 48.6% ( Fig. 2g Fig. 2g ). The modification densities ( ρ m , mmol g −1 , representing the moles of N c per gram of resin) were estimated according to the modification efficiencies and the density of pyridyl in Reillex 425 ( Table 1 Table 1 ). Adsorption of Re(VII) on the modified Reillex 425 resins 2 Re(VII) primarily exists as a perrhenate anion (ReO 4 − ) over a pH range of 0 to 12 [ 39 39 ]; thus, its adsorption behavior is determined by the surface charge of the adsorbents. As shown in Fig. 3a Fig. 3a , the zeta potential of the pristine Reillex 425 resin was positive at pH < 3 and negative at pH > 5 because of deprotonation of the pyridyl groups in the polymer (p K a = 5.6) [ 40 40 ]. Consequently, the electrostatic repulsion between the resin and ReO 4 − gradually decreased when the pH decreased from 9 to 2. The q e of Re on Reillex 425 reached a maximum of 194.8 mg g −1 at pH = 2 ( Fig. 3b Fig. 3b ) . However, if the pH is further decreased, the competitive adsorption of concentrated Cl − anions would suppress ReO 4 − adsorption [ 41 41 , 42 42 ]. After the tertiary pyridyl groups on Reillex 425 were quaternized, all the modified resins exhibited positive zeta potentials at pH 1–9 owing to the intrinsic positively charged N atoms. Although all Reillex 425-Cn resins showed the same pH-dependent adsorption pattern as that of pristine Reillex 425 because of some remaining tertiary pyridyl, their q e values were significantly enlarged under neutral conditions, remaining above 135.5 mg g −1 . Particularly, Reillex 425-C3 and Reillex 425-C5 exhibited larger q e values than Reillex 425-C2 because of their higher modification efficiencies ( Table 1 Table 1 ). Reillex 425-Me showed almost the same adsorption amount as Reillex 425-C5 owing to its higher modification efficiency, even though the methyl pyridinium group had only one binding site. Notably, the morphology of the modified Reillex 425 greatly impacted the adsorption performance. The modified Reillex 425 powders obtained under stirring exhibited a dramatically decreased q e under neutral conditions compared to the Reillex 425-Cn beads ( Fig. S2 ). Maintaining the granular shape during the modification not only increases the adsorption amount but also benefits column treatment for sewage. To elucidate the adsorption mechanism for ReO 4 − on the modified Reillex 425 resins, the adsorption isotherms were investigated and analyzed using the Langmuir and Freundlich models ( Fig. 4 Fig. 4 ). The linear forms are given by Eqs. S(1) and (2) , respectively in the Supporting Information. From Table 2 Table 2 , the Langmuir model describes the adsorption of ReO 4 − on all the modified Reillex 425 resins, which suggests monolayer adsorption. The maximum adsorption capacities ( q m ) were calculated to be 344.8, 416.7, 588.2, and 625.0 mg g −1 (1.852, 2.240, 3.159, and 3.360 mmol g −1 ) for Reillex 425-C2, Reillex 425-C3, Reillex 425-C5, and Reillex 425-Me, respectively. Compared with other adsorbents listed in Table S1 , the higher q m of modified Reillex 425 favors an extended lifetime of the packed column. It is evident that q m on Reillex 425-Me equaled its ρ m , suggesting that all positively charged N atoms were occupied by ReO 4 − . Meanwhile, all q e values for Reillex 425-Cn were higher than their ρ m values, ranging from 1.5 to 2 times, indicating that ammonium and pyridinium sites should be capable of adsorbing ReO 4 − simultaneously. The q m of Reillex 425-C2 was twice its ρ m , demonstrating that all adsorption sites on the DCP groups could be utilized. However, it seemed that not all the positively charged sites on Reillex 425-C3 and Reillex 425-C5 were accessible at q m / ρ m ratios below 2, indicating that the adsorption of ReO 4 − anions inside the micropores might be hindered. a k L is the equilibrium constant for the Langmuir model. b n is a constant reflecting the favorability of the adsorption process in the Freundlich model. c k F is the equilibrium constant for the Freundlich model. 1 1   3 1 Langmuir 3 1 Freundlich 1 1   1 1 q m (mg g −1 ) 1 1 k L a (L mg −1 ) 1 1 R 2 1 1 n b 1 1 k F c (mg g −1 )(L mg −1 ) 1/ n 1 1 R 2 1 1 Reillex 425-C2 1 1 344.8 1 1 0.0368 1 1 0.9952 1 1 3.691 1 1 62.49 1 1 0.9512 1 1 Reillex 425-C3 1 1 416.7 1 1 0.1127 1 1 0.9990 1 1 4.290 1 1 108.96 1 1 0.9534 1 1 Reillex 425-C5 1 1 588.2 1 1 0.0322 1 1 0.9913 1 1 3.232 1 1 79.52 1 1 0.9466 1 1 Reillex 425-Me 1 1 625.0 1 1 0.0289 1 1 0.9975 1 1 2.701 1 1 60.09 1 1 0.9508 The adsorption thermodynamics were further investigated to gain a better understanding of the different adsorption patterns between the different DCP groups. Reillex 425-C2 and 425-C5, which contained the shortest and longest spacers, respectively, were selected as representatives. The changes in the standard Gibbs free energy (Δ G 0 ), enthalpy (Δ H 0 ), and entropy (Δ S 0 ) of adsorption were calculated using Eq. S(3) and S(4) (Supporting Information), respectively. From Fig. 5 Fig. 5 and the calculated results in Table 3 Table 3 , the negative Δ H 0 and Δ G 0 values demonstrated that the spontaneous adsorption of ReO 4 − on both Reillex 425-C2 and 425-C5 was exothermic. A lower temperature benefits the adsorption process, as q e and Δ G display negative and positive correlations with temperature, respectively. Adsorption of ReO 4 − on Reillex 425-C5 was more thermodynamically favorable as its Δ G 0 was more negative than that of Reillex 425-C2. However, the adsorption isotherms showed that Reillex 425-C5 had a lower utilization rate for binding sites. Thus, ReO 4 − adsorption on Reillex 425-C5 is controlled by kinetics rather than thermodynamics. Meanwhile, kinetics had less effect on ReO 4 − adsorption for Reillex 425-C2. 1 1   1 1 Δ H 0 1 1 Δ S 0 6 1 Δ G 0 (kJ mol −1 ) 1 1 R 2 1 1   1 1 (kJ mol −1 ) 1 1 (J mol −1 ) 1 1 298 K 1 1 313 K 1 1 323 K 1 1 328 K 1 1 338 K 1 1 343 K 1 1   1 1 Reillex 425-C2 1 1 −21.28 1 1 −55.30 1 1 −4.796 1 1 −3.967 1 1 −3.414 1 1 −3.137 1 1 −2.585 1 1 −2.308 1 1 0.9614 1 1 Reillex 425-C5 1 1 −14.43 1 1 −23.86 1 1 −7.318 1 1 −6.960 1 1 −6.721 1 1 −6.602 1 1 −6.363 1 1 −6.244 1 1 0.9535 A kinetic study demonstrated that Reillex 425-C2 showed a faster adsorption rate than Reillex 425-Me and all other Reillex 425-Cn, reducing the equilibrium time for adsorption from 5 h to 1 h ( Fig. 6a Fig. 6a ). This agrees with the deduction that the adsorption of ReO 4 − on Reillex 425-C2 was less controlled by kinetics than on other Reillex 425-Cn. Pseudo-first-order and pseudo-second-order kinetic models were used to quantitatively investigate the adsorption kinetics, the linear forms of which are given by Eqs. S(5) and (6) in Supporting Information, respectively. Figs. 6b and 6c Figs. 6b and 6c show the linear fitting curves of these two models, whose fitting results are listed in Table 4 Table 4 . The adsorption behavior of ReO 4 − can be described better by the pseudo-second-order kinetic model with a higher R 2 , revealing that the adsorption is chemisorption [ 43 43 ]. Reillex 425-C2 exhibited a high adsorption rate constant k 2 of 0.00260 g mg −1 min −1 , which was more than six times larger than that of the other modified Reillex 425. a q e, cal is the adsorption amount at equilibrium calculated using the corresponding adsorption kinetic model. b k 1 is the adsorption rate constant of the pseudo-first-order kinetic model. c k 2 is the adsorption rate constant of the pseudo-second-order kinetic model. 1 1   3 1 Pseudo-first-order 3 1 Pseudo-second-order 1 1   1 1 q e, cal a (mg g −1 ) 1 1 k 1 b (min −1 ) 1 1 R 2 1 1 q e, cal a (mg g −1 ) 1 1 k 2 c (g mg −1 min −1 ) 1 1 R 2 1 1 Reillex 425-C2 1 1 12.95 1 1 0.00227 1 1 0.1334 1 1 177.94 1 1 0.00260 1 1 0.9990 1 1 Reillex 425-C3 1 1 65.16 1 1 0.00260 1 1 0.6152 1 1 233.64 1 1 0.00024 1 1 0.9993 1 1 Reillex 425-C5 1 1 49.91 1 1 0.00181 1 1 0.3215 1 1 223.71 1 1 0.00043 1 1 0.9989 1 1 Reillex 425-Me 1 1 56.01 1 1 0.00272 1 1 0.3886 1 1 215.05 1 1 0.00028 1 1 0.9990 The adsorption process consists of four sequential stages: bulk diffusion, boundary layer diffusion, intraparticle diffusion, and surface reactions [ 44 44 ]. In batch adsorption experiments, the resistance to bulk diffusion is negligible because of the small concentration gradient of the adsorbate caused by vigorous shaking. The final stage of the adsorption reaction is nearly immediate for ion exchange, and can be neglected. Therefore, the rate of the entire adsorption process is typically limited by the boundary layer and/or intraparticle diffusion stages. The following Eq. (3) depicts the intraparticle diffusion model proposed by Weber and Morris[ 45 45 ]. <math display="block" id="M3"><mrow><msub><mi>q</mi><mtext>t</mtext></msub><mo>=</mo><msub><mi>k</mi><mtext>p</mtext></msub><msup><mi>t</mi><mrow><mn>1</mn><mo>/</mo><mn>2</mn></mrow></msup><mo>+</mo><msub><mi>c</mi><mtext>p</mtext></msub><mo>,</mo></mrow></math> where the slope k p (mg g −1 min −1/2 ) and intercept c p (mg g −1 ) are the rate constants of intraparticle diffusion and a constant related to the thickness of the boundary layer, respectively. Piecewise linear regression suggested that the q t vs . t 1/2 plots of both Reillex 425-C2 and Reillex 425-C5 showed a two-stage adsorption pattern. The first stage agrees with the intraparticle diffusion model, with an intercept of almost 0, indicating that the adsorption of ReO 4 − on modified Reillex 425 is only controlled by intraparticle diffusion ( Fig. 6d Fig. 6d ) [ 46 46 ]. The second stage displayed almost constant adsorption amounts, demonstrating that adsorption approached equilibrium. Thus, the higher adsorption rate of ReO 4 − on Reillex 425-C2 is attributed to the faster diffusion of ReO 4 − anions inside the micropores. As demonstrated above, all Reillex 425-Cn samples retained an almost unchanged pore structure. The difference between the –Py + C 2 H 4 N + Me 3 and –Py + C 5 H 10 N + Me 3 groups, or more accurately, the different spacers are presumed to drastically affect anion transport inside the microporous channels of Reillex 425-Cn. The longer alkyl spacers were more flexible, which enabled greater changes in the conformation of the DCP groups. It is possible to rearrange the pyridinium and ammonium sites vertically owing to the electrostatic repulsion between them and the hydrophobic aggregation of the long carbon spacers, as illustrated in Fig. 6e Fig. 6e . Under such circumstances, the adsorption of ReO 4 − at the first cationic site impedes the diffusion of ReO 4 − towards the second cationic moiety [ 47 47 ]. Furthermore, the aggregation of long and flexible carbon chains forms hydrophobic microphases inside microporous channels, which increases the resistance of intraparticle diffusion of hydrophilic species such as hydrated anions [ 48 48 ]. Therefore, steric hindrance and hydrophobic repulsion generated by the longer spacer of the –Py + C 5 H 10 N + Me 3 groups retard ReO 4 − transport inside the micropores of Reillex 425-C5. For Reillex 425-C2, the two positive charges connected by shorter alkyl spacers tended to be laterally arranged ( Fig. 6e Fig. 6e ), leading to smaller steric hindrance. Moreover, hydrophobic microphases are not formed due to repulsion among the positive charges. As a result, the transport of ReO 4 − anions inside the microporous channels modified with Py + C 2 H 4 N + Me 3 groups was enhanced. Reillex 425-Me functionalized with monocationic methyl pyridinium also exhibited a slower adsorption rate than Reillex 425-C2, although no spacers were present. This is because the quaternization of pyridyl with methyl increases the hydrophobicity of the surface of the microporous channels, hindering the intraparticle diffusion of ReO 4 − ( Fig. 6e Fig. 6e ) [ 49 49 ]. According to the above discussion, dicationic –Py + C 2 H 4 N + Me 3 groups with short spacers can promote the transportation of ReO 4 − inside the microporous channels. To evaluate the contribution of DCP groups to practical Tc removal, the adsorption kinetics of TcO 4 − on different modified Reillex 425 samples were further investigated. As displayed in Fig. 7a Fig. 7a , all the modified Reillex 425 resins remove approximately 99% of the Tc due to its trace concentration of 125 Bq mL −1 (0.2 mg L −1 of 99 Tc). Reillex 425-C2 still exhibited the fastest adsorption rate, with the highest 1-hour removal ratio of 93.5%. Tc removal accelerated by the –Py + C 2 H 4 N + Me 3 groups was verified by kinetic analysis. The adsorption kinetics followed a pseudo-second-order kinetic model ( Fig. 7b and 7c Fig. 7b and 7c ), similar to that of ReO 4 − . Reillex 425-C2 showed the largest k 2 of 0.211 g mg −1 min −1 among all three Reillex 425-Cn samples ( Table 5 Table 5 ). 1 1   3 1 Pseudo-first-order 3 1 Pseudo-second-order 1 1   1 1 q e, cal (mg g −1 ) 1 1 k 1 (min −1 ) 1 1 R 2 1 1 q e, cal (mg g −1 ) 1 1 k 2 (g mg −1 min −1 ) 1 1 R 2 1 1 Reillex 425-C2 1 1 7.18 1 1 0.00690 1 1 0.7340 1 1 0.45 1 1 0.21118 1 1 0.9998 1 1 Reillex 425-C3 1 1 6.28 1 1 0.00496 1 1 0.6393 1 1 0.49 1 1 0.19431 1 1 0.9999 1 1 Reillex 425-C5 1 1 5.17 1 1 0.00549 1 1 0.6725 1 1 0.49 1 1 0.13911 1 1 0.9997 1 1 Reillex 425-Me 1 1 9.24 1 1 0.00578 1 1 0.7399 1 1 0.49 1 1 0.24657 1 1 0.9999 TcO 4 − adsorption on Reillex 425-Me was faster than that on Reillex 425-C2, which was different from the adsorption of ReO 4 − . Piecewise linear regression of the kinetic data using the intraparticle diffusion model validated that the adsorption of TcO 4 − on Reillex 425-Cn showed the same pattern as that of ReO 4 − , only controlled by intraparticle diffusion ( Table 6 Table 6 ). However, TcO 4 − adsorption on Reillex 425-Me is controlled by both stages of the boundary layer and intraparticle diffusion. After obtaining the intercept c p in the intraparticle diffusion model by linear fitting of the first stage, an initial adsorption factor ( R i ), defined by the following Eq. (4) can be calculated to distinguish the contributions from different diffusion processes. R i was 0.772 for Reillex 425-Me, implying that 77.2% of the TcO 4 − adsorption was governed by intraparticle diffusion. The remaining 22.8% occurs almost instantaneously, as determined by boundary layer diffusion [ 50 50 ]. Reillex 425-C2 exhibited a 52.5% higher k p than Reillex 425-Me, demonstrating that the –Py + C 2 H 4 N + Me 3 groups also accelerated the adsorption of TcO 4 − by promoting intraparticle diffusion. Generally, higher mass transfer rates shorten the mass transfer zone when adsorbents are packed in a column. In other words, the difference between breakthrough and equilibrium times is reduced, resulting in a steeper breakthrough curve. Consequently, fixed-bed columns can be utilized more efficiently. <math display="block" id="M4"><mrow><msub><mi>R</mi><mi>i</mi></msub><mo>=</mo><mn>1</mn><mo>−</mo><mfrac><mrow><msub><mi>c</mi><mi>p</mi></msub></mrow><mrow><msub><mi>q</mi><mi>e</mi></msub></mrow></mfrac></mrow></math> a,b The fitting intercept c p became negative owing to experimental errors, and thus R i could be regarded as its maximum value of 1. 1 1   4 1 ReO 4 − 4 1 TcO 4 − 1 1   1 1 k p (mg g −1 min −1/2 ) 1 1 c p 1 1 R 2 1 1 R i 1 1 k p (mg g −1 min −1/2 ) 1 1 c p 1 1 R 2 1 1 R i 1 1 Reillex 425-C2 1 1 24 1 1 0.3963 1 1 0.9756 1 1 0.9978 1 1 0.061 1 1 −0.0279 a 1 1 0.9839 1 1 ≈ 1 b 1 1 Reillex 425-C5 1 1 22 1 1 4.9986 1 1 0.9643 1 1 0.9782 1 1 0.062 1 1 −0.0589 a 1 1 0.9996 1 1 ≈ 1 b 1 1 Reillex 425-Me 1 1 20 1 1 7.8633 1 1 0.9885 1 1 0.9633 1 1 0.040 1 1 0.1101 1 1 0.9863 1 1 0.7721 Although the contaminated seawater in Fukushima Daiichi nuclear power station has been desalinated during the treatment, the treated water still contains Cl − (1900 mg L −1 , or 5.4 × 10 −2 mol L −1 ) and SO 4 2− (610 mg L −1 , or 6.4 × 10 −3 mol L −1 ) [ 51 51 ], the two main anions in seawater [ 52 52 ], which may hamper the adsorption of TcO 4 − . In 0.05 mol L −1 of Cl − or SO 4 2− , the q e of Re on Reillex 425-C2 decreased to 64.9% and 49.7% of the original value, respectively, owing to competitive adsorption by the DCP groups ( Fig. 8a Fig. 8a ). With an increase in the anion concentration, Cl − and SO 4 2− had different effects on Re adsorption. q e declined to 25.8% in 1 mol L −1 of Cl − , while it remained almost the same (44.8%) in 1 mol L −1 of SO 4 2− . Reillex 425-C5 showed a similar trend; q e decreased from 72.1% to 28.3% in Cl − but remained constant at approximately 65.0% in SO 4 2− as the anion concentration rose from 0.05 to 1 mol L −1 ( Fig. 8b Fig. 8b ). Because of the hydrophobic nature of the Reillex 425 resin matrix, the inner walls of the porous channels should retain a certain hydrophobicity even after the dication modification. The hydration energies for the different anions follow the order SO 4 2− (−1080 kJ mol −1 ) < Cl − (−340 kJ mol −1 ) < ReO 4 − (−330 kJ mol −1 ) [ 53 53 ]. Therefore, SO 4 2− , which is more hydrophilic, has less influence on ReO 4 − adsorption. Reillex 425-C5, containing hydrophobic microphases formed by longer and more flexible carbon chains, is more resistant to these hydrophilic anions than Reillex 425-C2 for the same reason. In addition to Cl − or SO 4 2− , the treated water also contains trace amounts of other radioactive anions, such as 129 I − and 125 Sb(OH) 6 − [ 54 54 ]. Reillex 425-C2 and Reillex 425-C5 showed separation factors ( S ) between Re and I ( S Re/I = K d,Re / K d,I ) of over 4.6 and 5.0, and S Re/Sb ( S Re/Sb = K d,Re / K d,Sb ) of over 14.7 and 64.2, respectively, demonstrating their ability to remove TcO 4 − selectively from the treated water in Fukushima ( Fig. 8c Fig. 8c ). After the adsorption of ReO 4 − , the used Reillex 425-Cn could be easily regenerated by HNO 3 , with q e remaining over 95% after five adsorption–desorption cycles ( Fig. 8d Fig. 8d ). Conclusion 1 In this study, we propose a simple and efficient method for improving the adsorption performance of ReO 4 – and TcO 4 – on Reillex 425 anion exchange resins by modifying them with a series of DCP groups. After modification, the obtained Reillex 425-Cn gained higher adsorption amounts for Re ( q e > 135.0 mg g −1 ) in neutral solutions owing to the positively charged quaternary N sites in the DCP groups. The DCP integrated one quaternary pyridinium and one quaternary ammonium into a single group, both of which adsorbed ReO 4 – simultaneously. Consequently, the maximum Re adsorption capacities, q m , for Reillex 425-C2, Reillex 425-C3, and Reillex 425-C5 reached as high as 344.8, 416.7, and 588.2 mg g −1, respectively. A detailed study of the adsorption isotherms revealed that the utilization ratio of all the adsorption sites only ranged from 75% to 100% at saturated adsorption, depending on the length of the alkyl spacers between the two positive charges in the DCP group. A longer spacer was found to be more thermodynamically favorable for Re adsorption. Thus, it can be concluded that adsorption is kinetically controlled. Reillex 425-C2 exhibited an adsorption rate six times faster than those of Reillex 425-Cn and Reillex-425-Me. A deeper investigation into the mass transfer mechanism of the adsorbates illustrated that the adsorption of ReO 4 – on modified Reillex 425 was only governed by intraparticle diffusion. The enhanced transport of ReO 4 – anions inside the microporous channels of the resins is responsible for the accelerated adsorption on Reillex 425-C2. For Reillex 425-C5, longer alkyl spacers might result in the perpendicular distribution of the two positive charges and the formation of hydrophobic microphases by carbon chain aggregation. This sterically hinders the anion from approaching the second cation and repels the hydrated ReO 4 – anions. Contrarily, the two positive charges in the –Py+C2H4N+Me3 groups with shorter alkyl spacers may be arranged laterally, generating no hydrophobic microphases. The smaller steric hindrance and repulsion promoted the intraparticle diffusion of ReO 4 – inside the Reillex 425-C2 resins. For the adsorption of radioactive TcO 4 − at trace concentrations, Reillex 425-C2 showed the same adsorption pattern dictated only by intraparticle diffusion. The –Py + C 2 H 4 N + Me 3 groups enhanced the mass transfer of TcO 4 − inside the resin beads. In addition to rapid adsorption, Reillex 425-C2 also exhibited several other features that benefit the removal or remediation of TcO 4 − from treated water, which contains various non-tritium radioisotopes beyond the regulatory standard for discharge. These include exothermic adsorption, good selectivity, excellent reusability, and adequate salinity tolerance. The modification strategy with appropriate dications should increase the utilization efficiency of the fixed-bed column by accelerating the transport of TcO 4 − anions inside the micropores of the filling resins, which implies enormous environmental and economic benefits. References D. Parajuli , H. Tanaka , Y. Hakuta et al. , Dealing with the aftermath of Fukushima Daiichi nuclear accident: Decontamination of radioactive cesium enriched ash . Environ. Sci. Technol. 47 , 3800 - 3806 ( 2013 ). doi: 10.1021/es303467n http://doi.org/10.1021/es303467n Dealing with the aftermath of Fukushima Daiichi nuclear accident: Decontamination of radioactive cesium enriched ash G. Steinhauser , Fukushima’s forgotten radionuclides: A review of the understudied radioactive emissions . Environ. Sci. Technol. 48 , 4649 - 4663 ( 2014 ). doi: 10.1021/es405654c http://doi.org/10.1021/es405654c Fukushima’s forgotten radionuclides: A review of the understudied radioactive emissions P. Xiao , D. Han , M. Zhai et al. , Comparison with adsorption of Re(VII) by two different γ-radiation synthesized silica-grafting of vinylimidazole/4-vinylpyridine adsorbents . J. Hazard. Mater. 324 , 711 - 723 ( 2017 ). doi: 10.1016/j.jhazmat.2016.11.045 http://doi.org/10.1016/j.jhazmat.2016.11.045 Comparison with adsorption of Re(VII) by two different γ-radiation synthesized silica-grafting of vinylimidazole/4-vinylpyridine adsorbents I.T. Burke , C. Boothman , J.R. Lloyd et al. , Effects of progressive anoxia on the solubility of technetium in sediments . Environ. Sci. Technol. 39 , 4109 - 4116 ( 2005 ). doi: 10.1021/es048124p http://doi.org/10.1021/es048124p Effects of progressive anoxia on the solubility of technetium in sediments G. Lear , J.M. McBeth , C. Boothman et al. , Probing the biogeochemical behavior of technetium using a novel nuclear imaging approach . Environ. Sci. Technol. 44 , 156 - 162 ( 2010 ). doi: 10.1021/es802885r http://doi.org/10.1021/es802885r Probing the biogeochemical behavior of technetium using a novel nuclear imaging approach T.M. Gilliam , R.D. Spence , W.D. Bostick et al. , Solidification/stabilization of technetium in cement-based grouts . J. Hazard. Mater. 24 , 189 - 197 ( 1990 ). doi: 10.1016/0304-3894(90)87009-7 http://doi.org/10.1016/0304-3894(90)87009-7 Solidification/stabilization of technetium in cement-based grouts Update of Decommissioning and Reconstruction—Fukushima Daiichi NPS in 2021 . Ministry of Economy, Trade and Industry , https://www.meti.go.jp/english/earthquake/nuclear/decommissioning/pdf/02_meti_sideevent.pdf https://www.meti.go.jp/english/earthquake/nuclear/decommissioning/pdf/02_meti_sideevent.pdf . Accessed 6 September 2021 Update of Decommissioning and Reconstruction—Fukushima Daiichi NPS in 2021 K.O. Buesseler , Opening the floodgates at Fukushima . Science. 369 , 621 ( 2020 ). doi: 10.1126/science.abc1507 http://doi.org/10.1126/science.abc1507 Opening the floodgates at Fukushima J.S. McCloy , B.J. Riley , A. Goel et al. , Rhenium solubility in borosilicate nuclear waste glass: Implications for the processing and immobilization of technetium-99 . Environ. Sci. Technol. 46 , 12616 - 12622 ( 2012 ). doi: 10.1021/es302734y http://doi.org/10.1021/es302734y Rhenium solubility in borosilicate nuclear waste glass: Implications for the processing and immobilization of technetium-99 T. Suzuki , Y. Fujii , W. Yan et al. , Adsorption behavior of VII group elements on tertiary pyridine resin in hydrochloric acid solution . J. Radioanal. Nucl. Chem. 282 , 641 ( 2009 ). doi: 10.1007/s10967-009-0165-9 http://doi.org/10.1007/s10967-009-0165-9 Adsorption behavior of VII group elements on tertiary pyridine resin in hydrochloric acid solution J. Zu , R. Liu , J. Zhang et al. , Adsorption of Re and 99 Tc by means of radiation-grafted weak basic anion exchange resi . J. Radioanal. Nucl. Chem. 310 , 229 - 237 ( 2016 ). doi: 10.1007/s10967-016-4819-0 http://doi.org/10.1007/s10967-016-4819-0 Adsorption of Re and 99Tc by means of radiation-grafted weak basic anion exchange resi P. Y. Wang , J. H. Zu , Y. Z. Wei , Synthesis and characterization of porous 4VP-based adsorbent for Re adsorption as analogue to 99 Tc . Nucl. Sci. Tech. 28 , 30 ( 2017 ). doi: 10.1007/s41365-017-0181-3 http://doi.org/10.1007/s41365-017-0181-3 Synthesis and characterization of porous 4VP-based adsorbent for Re adsorption as analogue to 99Tc L. Zhu , D. Sheng , C. Xu et al. , Identifying the recognition site for selective trapping of 99 TcO 4 − in a hydrolytically stable and radiation resistant cationic metal–organic framework . J. Am. Chem. Soc. 139 , 14873 - 14876 ( 2017 ). doi: 10.1021/jacs.7b08632 http://doi.org/10.1021/jacs.7b08632 Identifying the recognition site for selective trapping of 99TcO4− in a hydrolytically stable and radiation resistant cationic metal–organic framework A. Thevenet , C. Marie , C. Tamain et al. , Perrhenate and pertechnetate complexation by an azacryptand in nitric acid medium . Dalton Trans. 49 , 1446 - 1455 ( 2020 ). doi: 10.1039/C9DT04314D http://doi.org/10.1039/C9DT04314D Perrhenate and pertechnetate complexation by an azacryptand in nitric acid medium Y. Wang , Z. Wu , H. Weng et al. , Separation of Re(VII) from aqueous solution by acetone-enhanced photoreduction: an insight into the role of acetone . J. Photochem. Photobiol. A Chem. 380 , 111823 ( 2019 ). doi: 10.1016/j.jphotochem.2019.04.034 http://doi.org/10.1016/j.jphotochem.2019.04.034 Separation of Re(VII) from aqueous solution by acetone-enhanced photoreduction: an insight into the role of acetone Y. Shang , J. Xiao , H. Weng et al. , Efficient separation of Re(VII) by radiation-induced reduction from aqueous solution . Chem. Eng. J. 341 , 317 - 326 ( 2018 ). doi: 10.1016/j.cej.2018.02.022 http://doi.org/10.1016/j.cej.2018.02.022 Efficient separation of Re(VII) by radiation-induced reduction from aqueous solution M.K. Uddin , A review on the adsorption of heavy metals by clay minerals, with special focus on the past decade . Chem. Eng. J. 308 , 438 - 462 ( 2017 ). doi: 10.1016/j.cej.2016.09.029 http://doi.org/10.1016/j.cej.2016.09.029 A review on the adsorption of heavy metals by clay minerals, with special focus on the past decade J. Lehto , R. Koivula , H. Leinonen et al. , Removal of Radionuclides from Fukushima Daiichi Waste Effluents . Sep. Purif. Rev. 48 , 122 - 142 ( 2019 ). doi: 10.1080/15422119.2018.1549567 http://doi.org/10.1080/15422119.2018.1549567 Removal of Radionuclides from Fukushima Daiichi Waste Effluents D. Li , D.I. Kaplan , A.S. Knox et al. , Aqueous 99 Tc, 129 I and 137 Cs removal from contaminated groundwater and sediments using highly effective low-cost sorbents . J. Environ. Radioact. 136 , 56 - 63 ( 2014 ). doi: 10.1016/j.jenvrad.2014.05.010 http://doi.org/10.1016/j.jenvrad.2014.05.010 Aqueous 99Tc, 129I and 137Cs removal from contaminated groundwater and sediments using highly effective low-cost sorbents C.D. Williams , P. Carbone , Selective removal of technetium from water using graphene oxide membranes . Environ. Sci. Technol. 50 , 3875 - 3881 ( 2016 ). doi: 10.1021/acs.est.5b06032 http://doi.org/10.1021/acs.est.5b06032 Selective removal of technetium from water using graphene oxide membranes L. Liang , B. Gu , X. Yin , Removal of technetium-99 from contaminated groundwater with sorbents and reductive materials . Sep. Technol. 6 , 111 - 122 ( 1996 ). doi: 10.1016/0956-9618(96)00148-8 http://doi.org/10.1016/0956-9618(96)00148-8 Removal of technetium-99 from contaminated groundwater with sorbents and reductive materials K. Pillay , A review of the radiation stability of ion exchange materials . J. Radioanal. Nucl. Chem. 102 , 247 - 268 ( 1986 ). doi: 10.1007/BF02037966 http://doi.org/10.1007/BF02037966 A review of the radiation stability of ion exchange materials M. Nogami , Y. Fujii , T. Sugo , Radiation resistance of pyridine type anion exchange resins for spent fuel treatment . J. Radioanal. Nucl. Chem. 203 , 109 - 117 ( 1996 ). doi: 10.1007/BF02060385 http://doi.org/10.1007/BF02060385 Radiation resistance of pyridine type anion exchange resins for spent fuel treatment Y. Wang , D. Han , S. Zhong et al. , Quaternary phosphonium modified cellulose microsphere adsorbent for 99 Tc decontamination with ultra-high selectivity . J. Hazard. Mater. 401 , 123354 ( 2021 ). doi: 10.1016/j.jhazmat.2020.123354 http://doi.org/10.1016/j.jhazmat.2020.123354 Quaternary phosphonium modified cellulose microsphere adsorbent for 99Tc decontamination with ultra-high selectivity M. Ding , L. Chen , Y. Xu et al. , Efficient capture of Tc/Re(VII, IV) by a viologen-based organic polymer containing tetraaza macrocycles . Chem. Eng. J. 380 , 122581 ( 2020 ). doi: 10.1016/j.cej.2019.122581 http://doi.org/10.1016/j.cej.2019.122581 Efficient capture of Tc/Re(VII, IV) by a viologen-based organic polymer containing tetraaza macrocycles Z. Dong , W. Yuan , Y. Li et al. , Radiation synthesis of crown ether functionalized microcrystalline cellulose as bifunctional adsorbent: A preliminary investigation on its application for removal of ReO 4 − as analogue for TcO 4 − . Radiat. Phys. Chem. 159 , 147 - 153 ( 2019 ). doi: 10.1016/j.radphyschem.2019.02.054 http://doi.org/10.1016/j.radphyschem.2019.02.054 Radiation synthesis of crown ether functionalized microcrystalline cellulose as bifunctional adsorbent: A preliminary investigation on its application for removal of ReO4− as analogue for TcO4− J. Zu , M. Ye , P. Wang et al. , Design of a strong-base anion exchanger and its adsorption and elution behavior for rhenium(VII) . RSC Adv. 6 , 18868 - 18873 ( 2016 ). doi: 10.1039/C5RA25313F http://doi.org/10.1039/C5RA25313F Design of a strong-base anion exchanger and its adsorption and elution behavior for rhenium(VII) K.M. Long , G.S. Goff , S.D. Ware et al. , Anion exchange resins for the selective separation of technetium from uranium in carbonate solutions . Ind. Eng. Chem. Res. 51 , 10445 - 10450 ( 2012 ). doi: 10.1021/ie300534e http://doi.org/10.1021/ie300534e Anion exchange resins for the selective separation of technetium from uranium in carbonate solutions A. Majavu , A.S. Ogunlaja , Z.R. Tshentu , Separation of rhodium(III) and iridium(IV) chlorido complexes using polymer microspheres functionalized with quaternary diammonium groups . Sep. Sci. Technol. 52 , 71 - 80 ( 2017 ). doi: 10.1080/01496395.2016.1235051 http://doi.org/10.1080/01496395.2016.1235051 Separation of rhodium(III) and iridium(IV) chlorido complexes using polymer microspheres functionalized with quaternary diammonium groups J. Abdi , M. Vossoughi , N.M. Mahmoodi et al. , Synthesis of metal-organic framework hybrid nanocomposites based on GO and CNT with high adsorption capacity for dye removal . Chem. Eng. J. 326 , 1145 - 1158 ( 2017 ). doi: 10.1016/j.cej.2017.06.054 http://doi.org/10.1016/j.cej.2017.06.054 Synthesis of metal-organic framework hybrid nanocomposites based on GO and CNT with high adsorption capacity for dye removal M. Hong , L. Yu , Y. Wang et al. , Heavy metal adsorption with zeolites: The role of hierarchical pore architecture . Chem. Eng. J. 359 , 363 - 372 ( 2019 ). doi: 10.1016/j.cej.2018.11.087 http://doi.org/10.1016/j.cej.2018.11.087 Heavy metal adsorption with zeolites: The role of hierarchical pore architecture H. Weng , P. Zhang , Z. Guo et al. , Efficient and Ultrafast Adsorption of Rhenium by Functionalized Hierarchically Mesoporous Silica: A Combined Strategy of Topological Construction and Chemical Modification . ACS Appl. Mater. Interfaces. 13 , 8249 - 8262 ( 2021 ). doi: 10.1021/acsami.0c19290 http://doi.org/10.1021/acsami.0c19290 Efficient and Ultrafast Adsorption of Rhenium by Functionalized Hierarchically Mesoporous Silica: A Combined Strategy of Topological Construction and Chemical Modification J.P. Stanford , N. van Rooyen , T. Vaidya et al. , Photodecomposition of methyl iodide as pretreatment for adsorption of radioiodine species in used nuclear fuel recycling operations . Chem. Eng. J. 400 , 125730 ( 2020 ). doi: 10.1016/j.cej.2020.125730 http://doi.org/10.1016/j.cej.2020.125730 Photodecomposition of methyl iodide as pretreatment for adsorption of radioiodine species in used nuclear fuel recycling operations M. Thommes , K. Kaneko , A.V. Neimark et al. , Physisorption of gases, with special reference to the evaluation of surface area and pore size distribution (IUPAC Technical Report) . Pure Appl. Chem. 87 , 1051 - 1069 ( 2015 ). doi: 10.1515/pac-2014-1117 http://doi.org/10.1515/pac-2014-1117 Physisorption of gases, with special reference to the evaluation of surface area and pore size distribution (IUPAC Technical Report) L. J. Cao , G. Wang , L. Shi et al. , Preparation and catalytic application of poly 4-vinylpyridine microspheres . J. Appl. Polym. Sci. 116 , 3178 - 3183 ( 2010 ). doi: 10.1002/app.31197 http://doi.org/10.1002/app.31197 Preparation and catalytic application of poly 4-vinylpyridine microspheres H. Berk , B. Balci , S. Ertan et al. , Functionalized polysulfide copolymers with 4-vinylpyridine via inverse vulcanization . Mater. Today Commun. 19 , 336 - 341 ( 2019 ). doi: 10.1016/j.mtcomm.2019.02.014 http://doi.org/10.1016/j.mtcomm.2019.02.014 Functionalized polysulfide copolymers with 4-vinylpyridine via inverse vulcanization J. Ortiz‐Palacios , J. Cardoso , M. de la Cruz et al. , Functionalization in copolymers based on 4VP: DVB for the removal of Cr(VI) ions from aqueous solution . J. Appl. Polym. Sci. 134 , 45548 ( 2017 ). doi: 10.1002/app.45548 http://doi.org/10.1002/app.45548 Functionalization in copolymers based on 4VP: DVB for the removal of Cr(VI) ions from aqueous solution V.A. Pashynska , M.V. Kosevich , A. Gömöry et al. , On the stability of the organic dication of the bisquaternary ammonium salt decamethoxinum under liquid secondary ion mass spectrometry . Rapid Commun. Mass Spectrom. 19 , 785 - 797 ( 2005 ). doi: 10.1002/rcm.1846 http://doi.org/10.1002/rcm.1846 On the stability of the organic dication of the bisquaternary ammonium salt decamethoxinum under liquid secondary ion mass spectrometry R.R. Srivastava , M. s. Kim , J. c. Lee et al. , Liquid–liquid extraction of rhenium(VII) from an acidic chloride solution using Cyanex 923 . Hydrometallurgy. 157 , 33 - 38 ( 2015 ). doi: 10.1016/j.hydromet.2015.07.011 http://doi.org/10.1016/j.hydromet.2015.07.011 Liquid–liquid extraction of rhenium(VII) from an acidic chloride solution using Cyanex 923 T. Kavitha , I. K. Kang , S. Y. Park , Poly(4-vinyl pyridine)-grafted graphene oxide for drug delivery and antimicrobial applications . Polym. Int. 64 , 1660 - 1666 ( 2015 ). doi: 10.1002/pi.4968 http://doi.org/10.1002/pi.4968 Poly(4-vinyl pyridine)-grafted graphene oxide for drug delivery and antimicrobial applications P. Cyganowski , A. Cierlik , A. Leśniewicz et al. , Separation of Re(VII) from Mo(VI) by anion exchange resins synthesized using microwave heat . Hydrometallurgy. 185 , 12 - 22 ( 2019 ). doi: 10.1016/j.hydromet.2019.01.013 http://doi.org/10.1016/j.hydromet.2019.01.013 Separation of Re(VII) from Mo(VI) by anion exchange resins synthesized using microwave heat C. Xiong , C. Yao , X. Wu , Adsorption of rhenium(VII) on 4-amino-1,2,4-triazole resin . Hydrometallurgy. 90 , 221 - 226 ( 2008 ). doi: 10.1016/j.hydromet.2007.10.011 http://doi.org/10.1016/j.hydromet.2007.10.011 Adsorption of rhenium(VII) on 4-amino-1,2,4-triazole resin F. Li , Z. Yang , H. Weng et al. , High efficient separation of U(VI) and Th(IV) from rare earth elements in strong acidic solution by selective sorption on phenanthroline diamide functionalized graphene oxide . Chem. Eng. J. 332 , 340 - 350 ( 2018 ). doi: 10.1016/j.cej.2017.09.038 http://doi.org/10.1016/j.cej.2017.09.038 High efficient separation of U(VI) and Th(IV) from rare earth elements in strong acidic solution by selective sorption on phenanthroline diamide functionalized graphene oxide K.K.H. Choy , D.C.K. Ko , C.W. Cheung et al. , Film and intraparticle mass transfer during the adsorption of metal ions onto bone char . J. Colloid Interface Sci. 271 , 284 - 295 ( 2004 ). doi: 10.1016/j.jcis.2003.12.015 http://doi.org/10.1016/j.jcis.2003.12.015 Film and intraparticle mass transfer during the adsorption of metal ions onto bone char Jr W.J. Weber , J.C. Morris , Kinetics of adsorption on carbon from solution . J. Sanit. Eng. Div. 89 , 31 - 59 ( 1963 ). doi: 10.1061/JSEDAI.0000430 http://doi.org/10.1061/JSEDAI.0000430 Kinetics of adsorption on carbon from solution H. Zheng , D. Liu , Y. Zheng et al. , Sorption isotherm and kinetic modeling of aniline on Cr-bentonite . J. Hazard. Mater. 167 , 141 - 147 ( 2009 ). doi: 10.1016/j.jhazmat.2008.12.093 http://doi.org/10.1016/j.jhazmat.2008.12.093 Sorption isotherm and kinetic modeling of aniline on Cr-bentonite A. Serva , V. Migliorati , A. Lapi et al. , Structural properties of geminal dicationic ionic liquid/water mixtures: a theoretical and experimental insight . PCCP. 18 , 16544 - 16554 ( 2016 ). doi: 10.1039/C6CP01557C http://doi.org/10.1039/C6CP01557C Structural properties of geminal dicationic ionic liquid/water mixtures: a theoretical and experimental insight M. Shi , Q. Dai , F. Li et al. , Membranes with well-defined selective layer regulated by controlled solvent diffusion for high power density flow battery . Adv. Energy Mater. 10 , 2001382 ( 2020 ). doi: 10.1002/aenm.202001382 http://doi.org/10.1002/aenm.202001382 Membranes with well-defined selective layer regulated by controlled solvent diffusion for high power density flow battery Z. Zhang , M.M. Rahman , C. Abetz et al. , Quaternization of a Polystyrene-block-poly(4-vinylpyridine) Isoporous Membrane: An Approach to Tune the Pore Size and the Charge Density . Macromol. Rapid Commun. 40 , 1800729 ( 2019 ). doi: 10.1002/marc.201800729 http://doi.org/10.1002/marc.201800729 Quaternization of a Polystyrene-block-poly(4-vinylpyridine) Isoporous Membrane: An Approach to Tune the Pore Size and the Charge Density F. C. Wu , R. L. Tseng , R. S. Juang , Initial behavior of intraparticle diffusion model used in the description of adsorption kinetics . Chem. Eng. J. 153 , 1 - 8 ( 2009 ). doi: 10.1016/j.cej.2009.04.042 http://doi.org/10.1016/j.cej.2009.04.042 Initial behavior of intraparticle diffusion model used in the description of adsorption kinetics Status of Contaminated Water Treatment and Tritium at Fukushima Daiichi Nuclear Power Station , Tokyo Electric Power Company, Inc. , https://www.meti.go.jp/earthquake/nuclear/pdf/140424/140424_02_008.pdf https://www.meti.go.jp/earthquake/nuclear/pdf/140424/140424_02_008.pdf . Accessed 24 April 2014 Status of Contaminated Water Treatment and Tritium at Fukushima Daiichi Nuclear Power Station F.J. Millero , R. Feistel , D.G. Wright et al. , The composition of standard seawater and the definition of the reference-composition salinity scale . Deep Sea Res. Part I. 55 , 50 - 72 ( 2008 ). doi: 10.1016/j.dsr.2007.10.001 http://doi.org/10.1016/j.dsr.2007.10.001 The composition of standard seawater and the definition of the reference-composition salinity scale Y. Marcus , Thermodynamics of solvation of ions. Part 5.—Gibbs free energy of hydration at 298.15 K . J. Chem. Soc. Faraday Trans. 87 , 2995 - 2999 ( 1991 ). doi: 10.1039/FT9918702995 http://doi.org/10.1039/FT9918702995 Thermodynamics of solvation of ions. Part 5.—Gibbs free energy of hydration at 298.15 K K.W. Kim , Y.j. Baek , K. Y. Lee et al. , Treatment of radioactive waste seawater by coagulation–flocculation method using ferric hydroxide and poly acrylamide . J. Nucl. Sci. Technol. 53 , 439 - 450 ( 2016 ). doi: 10.1080/00223131.2015.1055313 http://doi.org/10.1080/00223131.2015.1055313 Treatment of radioactive waste seawater by coagulation–flocculation method using ferric hydroxide and poly acrylamide All authors contributed to the study conception and design. Material preparation, data collection and analysis were performed by Peng Zhang, Yi-Zhi Chen, Han-Qin Weng, Zi-Fang Guo, Jia-Liang Chen, Xing Zhao, Guo-An Ye, and Ming-Zhang Lin. The first draft of the manuscript was written by Peng Zhang and Han-Qin Weng, and all authors commented on previous versions of the manuscript. All authors read and approved the final manuscript. 10.1007/s41365-022-01026-w This work was supported by the National Natural Science Foundation of China (Nos. 51803205, 11775214, and 21790371) and China Scholarship Council (No. 201906345006). 2021-11-16 2022-02-11 2022-03-12 2022-04-19 2022-11-30 © China Science Publishing & Media Ltd. (Science Press), Shanghai Institute of Applied Physics, the Chinese Academy of Sciences, ChineseNuclear Society and Springer Nature Singapore Pte Ltd. 2022 This is a post-peer-review, pre-copyedit version of an article published in Nuclear Science and Techniques. The final authenticated version is available online at: http://dx.doi.org/10.1007/s41365-022-01026-w http://dx.doi.org/10.1007/s41365-022-01026-w . 2022 Nuclear Science and Techniques 04 33