Adsorption uranium (VI) onto amidoxime-functionalized ultra-high molecular weight polyethylene fibers from aqueous solution

Adsorption uranium (VI) onto amidoxime-functionalized ultra-high molecular weight polyethylene fibers from aqueous solution 1 first-author 1 1 1 1 1 1 1 corresp Corresponding author: wangjianqiang@sinap.ac.cn Corresponding author: wangjianqiang@sinap.ac.cn wangjianqiang@sinap.ac.cn Shanghai Institute of Applied Physics, Chinese Academy of Sciences, Shanghai 201800, China Shanghai Institute of Applied Physics, Chinese Academy of Sciences, Shanghai 201800, China Amidoxime-functionalized ultra-high molecular weight polyethylene fibers (UHMWPEF-AO) were used to absorb uranium [U(VI)] from acqeous solutions. In this paper, we study effects of pH, initial U(VI) concentration, contact time, and temperature on U(VI) adsorption by UHMWPEF-AO. The adsorption process agrees well with pseudo-second-order and Langmuir model. UHMWPEF-AO exhibits excellent adsorptive performance for U(VI) with a maximum adsorption capacity of 176.12 mg/g at pH 4 and 298 K. The structures of UHMWPEF-AO and U(VI) loaded UHMWPEF-AO are characterized by FT-IR and nano-CT. U(VI) loaded UHMWPEF-AO is sintered after adsorption process to recycle absorbed U(VI). Powders collected after sintering process are examined by scanning electron microscopy and X-ray diffraction. These results indicate that UHMWPEF-AO is a promising candidate to remove U(VI) from uranium aqueous solutions. Uranium Adsorption Kinetics Isotherms Sintering 1 Introduction 1 Uranium concentration in the environment has been a public concern [ 1 1 ]. The maximum uranium concentration in drinking water is no more than 9, 20 and 20 μg/L, according to drinking water guidelines of the World Health Organization (WHO), Health Canada and Australian, respectively [ 2 2 , 3 3 ]. Importantly, the inhalation of uranium and its compounds results in deposition in the lung and may further reach to the kidney through the blood steam, leading to progressive or irreversible kidney damage and failure, even death in acute cases [ 4 4 - 6 6 4-6 ]. The maximum daily intake of uranium issued by the WHO is 0.6 μg/kg of body weight daily [ 7 7 ]. Therefore, searching for appropriately effective techniques to adsorb uranium (VI) from aqueous solutions is of significance for both utilizing U(VI) and alleviating the environment problem. Till now, numerous approaches, including ion-exchange, chemical precipitation, membrane dialysis, solvent extraction, and adsorption, have been studied extensively for U(VI) extraction [ 8 8 , 9 9 ]. Among them the adsorption method is prospective due to its reusability, cost effectiveness, ease of operation and low sludge production [ 10 10 ]. Developing high performance adsorbent is of great importance for improving adsorptive effect. Researchers developed a variety of functionalized materials as adsorbents, such as magnetic composites [ 11 11 - 14 14 11-14 ], activated carbon [ 15 15 ], nanoporous carbons [ 16 16 ], Graphene oxides[ 17 17 ] and so on. In addition, amidoxime, an exceptional amphoteric group, is often chosen to modify different matrix materials on account of sorption rate, efficient U(VI) loading capacity, and environmental friendliness [ 18 18 , 19 19 ]. In this study, amidoxime-functionalized ultra-high molecular weight polyethylene fibers (abbreviated to UHMWPEF-AO) were used to absorb U(VI) from aqueous solutions. UHMWPEF-AO exhibits high mechanical properties and resistance to chemical corrosion and weathering. Furthermore, the raw material of the as-prepared samples, PE nonwoven fabrics or long fibers, are easy-access and low-cost. Notably, the adsorbed U(VI) could be recycled through sintering samples collected after adsorption equilibrium was reached, avoiding secondary pollution in common acid elution procedures. 2 Experimental 1 2.1 Apparatus 2 Fourier-transformed infrared (FT-IR) spectra were recorded by a Nicolet 6700 infrared spectrophotometer with a Nicolet continuum FT-IR microscope at Beamline 01B1 of Shanghai Synchrotron Radiation Facility. Nano-Computed Tomography (Nano-CT) experiments were performed at Beamline BL01B of National Synchrotron Radiation Research Center (NSRRC). Samples for nano-CT were prepared by an FEI Helios NanoLab 600 DualBeam FIB-SEM (Focus Ion Beam Scanning Electron Microscopy). SEM images were acquired by Zeiss Merlin Compact LE0 1530 VP with an Inca X-Max energy dispersive spectroscopy. X-ray diffraction (XRD) analysis were carried out on a Rigaku D/max-IIIB diffractometer using Cu Ka ray (k = 1.54178), with the X-ray source being operated at 40 kV and 150 mA. 2.2 Samples and reagents 2 UHMWPEF-AO synthesized by γ-irradiation-induced graft copolymerization and amidoximation [ 20 20 ] were provided by the radiation chemistry laboratory at Shanghai Institute of Applied Physics, Chinese Academy of Sciences. Different concentrations of U(VI) solution were prepared by diluting uranium standard solution of 1000 mg/L U(VI) concentration by distilled water to desired concentrations. Uranium standard solution, sodium hydroxide and hydrochloric acid were from Sinopharm Chemical Reagent Co., Ltd. All reagents were of AR grade and used without further purification. 2.3 Adsorption experiments 2 The effects of solution pH, contact time, initial concentration and temperature on adsorption of U(VI) were investigated. Typically, a certain amount of UHMWPEF-AO (5mg) were added into 5 mL U(VI) solution in polyethylene tubes. HCl and NaOH solutions were used to adjust pH to expected values. After 24 hours, the UHMWPEF-AO samples were taken out with tweezers. The concentrations of U(VI) were measured by inductively coupled plasma atomic emission spectroscopy (Optima 8000, Perkin Elmer). The amount (mg/g) of adsorbed U(VI) was calculated by q e = ( C 0 − C e ) V / m , where, C 0 and C e are U(VI) concentrations (mg/L) in starting solution and equilibrium solution, respectively; V is the volume (L) of starting solution, and m is the mass (g) of UHMWPEF-AO. 3 Results and discussion 1 3.1 Effect of pH 2 To examine the pH effect on U(VI) adsorption, the amount of adsorbed U(VI) at pH 1–7 were measured. As shown in Fig. 1 Fig. 1 , the amount of U(VI) absorbed on UHMWPEF-AO significantly increased with pH value until pH 4, where it began to decrease, indicating that the solution pH had strong influence on adsorption of U(VI). In highly acidic aqueous solutions (pH≤2), amine groups were protonated and formed –NH 3 + . Fewer binding sites were available for U(VI) due to competition of H + [ 21 21 ]. Moreover, the great majority of U(VI) were present in the form of UO 2 2+ ( Fig. 2 Fig. 2 ), electrostatic repulsion depressed reaction between protonated UHMWPEF-AO and UO 2 2+ . Therefore, very few U(VI) were absorbed. When pH varied from 2 to 4, concentration of OH − increased and positively charged UHMWPEF-AO transformed to electrically neutral molecule. Meanwhile, some UO 2 2+ ipns were hydrolyzed to UO 2 OH + , which could form stable complexes with UHMWPEF-AO [ 22 22 ]. Consequently, adsorption of U(VI) increased and reached a maximum value (99.43 mg/g) at pH 4. When pH increased greater than 4, further hydrolysis of U(VI) formed UO 2 (OH) 2 ·H 2 O (a colloid deposit) and resulted in a decrease in adsorption capacity. Therefore, pH 4.0 was chosen for the following experiments. 3.2 Effect of contact time and kinetic studies 2 To investigate dynamic characteristics of adsorption process, experiments lasting different contacting time (5 minutes to 24 hours) were performed. As shown in Fig. 3 Fig. 3 , adsorption of U(VI) could be divided into two stages: U(VI) uptake increased sharply in the first 180 minutes and around 78% of the adsorption was achieved in this stage. In the second stage, the adsorption slowed down and reached equilibrium finally. In further experiments, 24 hours was selected to insure the equilibrium of U(VI) adsorption on UHMWPEF-AO. The pseudo-first-order and pseudo-second-order models were used to analyze the acquired data. The former is based on adsorption capacity, while the latter assumes the rate-determining step is a chemisorption process including valence forces through either sharing or the electron interchange between adsorbent and adsorbate [ 23 23 ]. The two models can be written as: <math display="block" id="M1"><mrow><mi>ln</mi><mrow><mo>(</mo><mrow><msub><mi>q</mi><mtext>e</mtext></msub><mo>−</mo><msub><mi>q</mi><mi>t</mi></msub></mrow><mo>)</mo></mrow><mo>=</mo><mtext>ln</mtext><msub><mi>q</mi><mtext>e</mtext></msub><mo>−</mo><msub><mi>k</mi><mn>1</mn></msub><mi>t</mi></mrow></math> <math display="block" id="M2"><mrow><mfrac><mi>t</mi><mrow><msub><mi>q</mi><mi>t</mi></msub></mrow></mfrac><mo>=</mo><mfrac><mn>1</mn><mrow><msub><mi>k</mi><mn>2</mn></msub><msubsup><mi>q</mi><mtext>e</mtext><mn>2</mn></msubsup></mrow></mfrac><mo>+</mo><mfrac><mi>t</mi><mrow><msub><mi>q</mi><mtext>e</mtext></msub></mrow></mfrac></mrow></math> where, q e and q t represent the amount of absorbed U(VI) at equilibrium time (min) and time t (min), resprctively; and k 1 and k 2 are coefficients. The plots of ln ( q e − q t ) versus t , and t / q t against t , are shown in Fig. 4. Fig. 4. The values of k 1 , k 2 , q e are given in Table 1 Table 1 . The higher correlation coefficient value of pseudo-second-order implied the second-order nature. This indicates that the dominant adsorption mechanism is chemisorption or strong surface complexation, instead of mass transport. * T =25℃, C 0 =100 mg/L, q e exp =92.79 mg/g 1 1 Kinetic model 1 1 q e cal (mg/g) 1 1 k 1 /k 2 (g·mg −1 ·min −2 ) 1 1 R 2 1 1 Pseudo-first order 1 1 90.72 1 1 0.0083 1 1 0.9772 1 1 Pseudo-second order 1 1 99.40 1 1 1.16×10 −4 1 1 0.9946 3.3 Effects of initial concentration and isotherm studies 2 Adsorption capacity depends in part on initial U(VI) concentration in the whole aqueous solution. At low concentrations, binding sites of UHMWPEF-AO are partially occupied by U(VI). With increasing concentration, fewer binding sites are available and the adsorption saturates finally. Experiments were carried out at different initial U(VI) concentrations (50–350 mg/L). The obtained adsorption isotherm of U(VI) on UHMWPEF-AO is shown in Fig. 5. Fig. 5. Langmuir and Freundlich isotherm models were applied to simulate the experimental data. Langmuir isotherm model assumes homogeneous monolayer adsorption. Freundlich isotherm model is widely used in heterogeneous systems [ 24 24 ]. They were expressed respectively as follows: <math display="block" id="M3"><mrow><mfrac><mrow><msub><mi>C</mi><mtext>e</mtext></msub></mrow><mrow><msub><mi>q</mi><mtext>e</mtext></msub></mrow></mfrac><mo>=</mo><mfrac><mn>1</mn><mrow><mi>b</mi><mo>·</mo><msub><mi>q</mi><mtext>m</mtext></msub></mrow></mfrac><mo>+</mo><mfrac><mrow><msub><mi>C</mi><mtext>e</mtext></msub></mrow><mrow><msub><mi>q</mi><mtext>m</mtext></msub></mrow></mfrac></mrow></math> <math display="block" id="M4"><mrow><mtext>ln</mtext><msub><mi>q</mi><mtext>e</mtext></msub><mo>=</mo><mtext>ln</mtext><mi>k</mi><mo>+</mo><mfrac><mn>1</mn><mi>n</mi></mfrac><mtext>ln</mtext><msub><mi>c</mi><mtext>e</mtext></msub></mrow></math> where, C e (mg/L) and q e (mg/g) are the U(VI) concentration in solutions and the amounts of absorbed U(VI) at equilibrium time, separately; q m (mg/g) is the maximum adsorption capacity; b (L/mg) is Langmuir constant, k (L/g) and n are Freundlich constants associated with adsorption capacity and adsorption intensity, respectively. The plots of C e / q e versus C e , and ln q e against ln C e , are shown in Fig. 6. Fig. 6. The values of b , q m , k and n calculated from the intercepts and slopes in Fig.6 Fig.6 are given in Table 2 Table 2 . The Langmuir model fits the data better, indicating a monolayer adsorption of q m =176.99. In Table 3 Table 3 , the q m of U(VI) is compared with different adsorbents in literatures. The fundamental characteristics of Langmuir model can be described as a dimensionless constant, i.e. separation factor ( R L ) [ 25 25 ], expressed as: 1 1 Isotherm model 1 1 Parameters 1 1 Value 1 1 Langmuir 1 1 q m 1 1 176.99 1 1   1 1 b 1 1 0.9142 1 1   1 1 R 2 1 1 0.9998 1 1 Freundlich 1 1 n 1 1 5.7827 1 1   1 1 k 1 1 79.8340 1 1   1 1 R 2 1 1 0.7831 1 1 Adsorbents 1 1 T (K) 1 1 pH 1 1 q m (mg/g) 1 1 Refs. 1 1 Fe 3 O 4 @PAM 1 1 293 1 1 5.0 1 1 220.94 1 1 [ 11 11 ] 1 1 CMPEI/CMK-3 1 1 293 1 1 4.0 1 1 151.5 1 1 [ 14 14 ] 1 1 CCTS 1 1 298 1 1 3.0 1 1 72.46 1 1 [ 17 17 ] 1 1 AO-g-MWCNT 1 1 298 1 1 4.5 1 1 145 1 1 [ 19 19 ] 1 1 HTC-COOH 1 1 308.15 1 1 6.0 1 1 205.8 1 1 [ 26 26 ] 1 1 UHMWPEF-AO 1 1 298 1 1 4.0 1 1 176.99 1 1 This work <math display="block" id="M5"><mrow><msub><mi>R</mi><mi>L</mi></msub><mo>=</mo><mn>1</mn><mo>/</mo><mrow><mo>(</mo><mrow><mn>1</mn><mo>+</mo><mi>b</mi><msub><mi>C</mi><mn>0</mn></msub></mrow><mo>)</mo></mrow></mrow></math> The inset of Fig. 6(a) Fig. 6(a) shows the calculated R L versus C 0 . The R L values are between 0 and 1, indicating that the adsorption process is mainly process and therefore UHMWPEF-AO are suitable adsorbent. 3.4 Effect of temperature and thermodynamic studies 2 The adsorption of U(VI) on UHMWPEF-AO as a function of temperature was investigated by experiments at 295, 308, 318 and 333 K. As shown in Fig. 7 Fig. 7 , the amounts of U(VI) absorbed increased gradually with temperature, suggesting that U(VI) adsorption was endothermic and higher temperature is more favorable for the adsorption. Relative thermodynamic parameters were calculated by Eqs.(6)–(8): <math display="block" id="M6"><mrow><mo> </mo><msub><mi>k</mi><mi>d</mi></msub><mo>=</mo><msub><mi>q</mi><mi>e</mi></msub><mo>/</mo><msub><mi>C</mi><mi>e</mi></msub></mrow></math> <math display="block" id="M7"><mrow><mtext>ln</mtext><msub><mi>k</mi><mtext>d</mtext></msub><mo>=</mo><mtext> </mtext><mi>Δ</mi><mi>S</mi><mo>/</mo><mi>R</mi><mo>−</mo><mi>Δ</mi><mi>H</mi><mo>/</mo><mrow><mo>(</mo><mrow><mi>R</mi><mi>T</mi></mrow><mo>)</mo></mrow></mrow></math> <math display="block" id="M8"><mrow><mi>Δ</mi><mi>G</mi><mo>=</mo><mtext> </mtext><mo>−</mo><mi>R</mi><mi>T</mi><mtext> ln</mtext><msub><mi>k</mi><mtext>d</mtext></msub></mrow></math> where k d (mL/g) is distribution coefficient; R = 8.314 J·mol −1 ·K −1 is the gas constant; and ∆ S (J·mol −1 ·K −1 ), ∆ H (kJ/mol) and ∆ G (kJ/mol) are changes in entropy, enthalpy and Gibbs free energy, respectively. The ∆ S and ∆ H can be calculated from the intercept and slope of ln k d versus 1/ T (see the inset of Fig. 7 Fig. 7 ). The calculated ∆ S , ∆ H and ∆ G were listed in Table 4 Table 4 . The positive value of ∆ H verified the endothermic characteristic of the U(VI) absorption, while the positive value of ∆ S exhibited the affinity of UHMWPEF-AO toward U(VI) under the experimental conditions and an increase in randomness between UHMWPEF-AO and the aqueous solution during the adsorption process. The negative values of ∆ G show this process is the spontaneous. Moreover, the decreasing ∆ G values indicate that the process is more effective at higher temperature [ 27 27 ]. Thermodynamic studies suggest the potential feasibility of UHMWPEF-AO as an adsorbent for U(VI). 1 1 C 0 (mg/L) 1 1 ∆ H (kJ/mol) 1 1 ∆ S (J·mol −1 ·K −1 ) 4 1 ∆ G (kJ/mol) 1 1   1 1   1 1   1 1 295 K 1 1 308 K 1 1 318 K 1 1 333 K 1 1 ≈100 1 1 50.35 1 1 187.59 1 1 −4.21 1 1 −8.68 1 1 −9.34 1 1 −11.58 3.5 Characterization of sample 2 FT-IR spectra of UHMWPEF-AO and U(VI)-loaded UHMWPEF-AO are shown in Fig. 8. Fig. 8. In the UHMWPEF-AO spectrum, the broad peak at 3200–3400 cm –1 is relevant to –OH groups of amidoxime groups and water absorbed by physical adsorption during preservation. The peak at 2921 and 2848 cm –1 correspond to antisymmetric and symmetric stretching vibrations of –CH 2 − , respectively [ 28 28 ]. The peaks at 1655 and 939 cm –1 are ascribed to –C=N- and –N-O- groups of amidoxime groups, separately [ 29 29 ]. In the spectrum of U(VI)-loaded UHMWPEF-AO, a new peak arises at 839 cm –1 corresponding to vibration of linear O=U=O [ 21 21 ], demonstrating that U(VI) was clearly adsorbed by complexing with amidoxime groups in UHMWPEF-AO. U(VI)-loaded UHMWPEF-AO were removed from solutions after adsorption experiments ( C 0 ≈ 100 mg/L, m = 5 mg, V = 5 mL, pH=4.0). The outer edge of the single fiber were selected through SEM and cut by FIB to form a cylinder about 12 μm in diameter and 12 μm deep. For Nano-CT experiments, X-ray energy was 8KeV and exposure time of single 2D image was 60 seconds. After 181 2D images were obtained with sample rotating from -90° to 90° at a constant velocity, the corresponding 3D tomography images were reconstructed. We used the Avizo Fire software 8.0 to analyze 3D tomography images. As shown in Fig. 9 Fig. 9 , U(VI) were absorbed along the outer edge of the single fiber. This was due to the surface complexation between amidoxime groups in UHMWPEF-AO and U(VI), consistent with results of kinetic studies and FT-IR spectra. 3.6 Sintering of the U(VI) loaded UHMWPEF-AO 2 U(VI) loaded UHMWPEF-AO collected after adsorption were sintered at 1200 o C in an air atmosphere for 12 hours. The morphology of powder obtained after sintering were showed in Fig. 10. Fig. 10. Microparticles formed along the initial U(VI) loaded UHMWPEF-AO and the angular microparticles had oval-like shape and smooth surface. The XRD pattern of the powder, diffraction peaks at 14.9°, 21.3°, 25.8°, 26.4°, 33.7°, 43.4°, 46.2°, 51.6° and 73.7°could be ascribed to U 3 O 8 (PDF#31-1424) and peaks at 27.9°, 30.4° and 33.7° were assigned to U 2 O 5 (PDF#24-1362), shown in Fig. 11. Fig. 11. This result indicated that the powder were a mixture of uranium oxides. 4 Conclusion 1 Amidoxime-functionalized ultra-high molecular weight polyethylene fibers were successfully applied for U(VI) recovery in aqueous solution as a simple and economical absorbing material. The pH value plays a critical role in the adsorption process. Kinetic and isotherm studies showed that the adsorption process met pseudo-second-order and Langmuir model. Moreover, experimental and calculated maximum adsorption capacity was 176.12 and 176.99 mg/g, respectively. Thermodynamic data proved that the adsorption of U(VI) on UHMWPEF-AO was endothermic and spontaneous. In addition, the structure of U(VI) loaded UHMWPEF-AO was well characterized by FT-IR and CT, confirming that U(VI) in aqueous solutions were combined with UHMWPEF-AO. Importantly, the absorbed U(VI) can be easily recycled by sintering U(VI) loaded UHMWPEF-AO. 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RSC Advances 3 , 18952 - 18959 ( 2013 ). doi: 10.1039/c3ra42236d http://doi.org/10.1039/c3ra42236d Efficient enrichment of uranium(VI) on amidoximated magnetite/graphene oxide composites 10.1007/s41365-017-0251-6 This work was supported by the National Natural Science Foundation of China (Grants No. U1532259). 2016-12-12 2017-01-22 2017-01-28 2017-05-26 2017-07-01 2021-04-25 © 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. 2017 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/s41365-017-0251-6 http://dx.doi.org/10.1007/s41365-017-0251-6 . 2017 Nuclear Science and Techniques 07 28