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Enhanced adsorption of p-arsanilic acid from water by amine modified UiO-67 as examined using EXAFS, XPS and DFT calculations Chen Tian, Jian Zhao, Xinwen Ou, Jieting Wan, Yuepeng Cai, Zhang Lin, Zhi Dang, and Baoshan Xing Environ. Sci. Technol., Just Accepted Manuscript • DOI: 10.1021/acs.est.7b05761 • Publication Date (Web): 31 Jan 2018 Downloaded from http://pubs.acs.org on January 31, 2018
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Enhanced adsorption of p-arsanilic acid from water by amine
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modified UiO-67 as examined using EXAFS, XPS and DFT
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calculations
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Chen Tian, †,§ Jian Zhao, ‡,§ Xinwen Ou, † Jieting Wan, † Yuepeng Cai, ‖ Zhang Lin, *,†
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Zhi Dang, † and Baoshan Xing
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†
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Restoration in Industry Clusters (Ministry of Education), Guangdong Engineering and Technology
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Research Center for Environmental Nanomaterials, South China University of Technology,
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Guangzhou 510006, China
⊥
School of Environment and Energy, The Key Laboratory of Pollution Control and Ecosystem
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‡
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Science and Ecology (Ministry of Education), Ocean University of China, Qingdao 266100, China
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‖
13 14
College of Environmental Science and Engineering, Key Laboratory of Marine Environmental
School of Chemistry and Environment, South China normal University, Guangzhou 510006, China
⊥
Stockbridge School of Agriculture, University of Massachusetts, Amherst, MA 01003, USA
§Equal
contribution
15 16 17
* Email:
[email protected] (Dr. Zhang Lin); phone: 86-20-39380503; fax: 86-20-
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39380508
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ABSTRACT
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p-Arsanilic acid (p-ASA) is an emerging organoarsenic pollutant comprising both
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inorganic and organic moieties. For the efficient removal of p-ASA, adsorbents with
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high adsorption affinity are urgently needed. Herein, amine modified UiO-67 (UiO-67-
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NH2) metal-organic frameworks (MOFs) were synthesized, and their adsorption
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affinities towards p-ASA were 2 times higher than that of the pristine UiO-67. Extended
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X-ray absorption fine structure (EXAFS), X-ray photoelectron spectroscopy (XPS) and
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density functional theory (DFT) calculation results revealed the adsorption through a
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combination of As-O-Zr coordination, hydrogen bonding, and π-π stacking, among
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which As-O-Zr coordination was the dominant force. Amine groups played a
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significant role in enhancing the adsorption affinity through strengthening the As-O-Zr
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coordination and π-π stacking, as well as forming new adsorption sites via hydrogen
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bonding. UiO-67-NH2s could remove p-ASA at low concentrations (< 5 mg L-1) in
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simulated natural and waste waters to an arsenic level lower than that in the drinking
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water standard of World Health Organization (WHO) and the surface water standard of
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China, respectively. This work provided an emerging and promising method to increase
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the adsorption affinity of MOFs towards pollutants containing both organic and
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inorganic moieties, via modifying functional groups based on the pollutant structure to
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achieve synergistic adsorption effect.
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INTRODUCTION
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As a typical phenylarsonic acid compound, p-arsanilic acid (p-ASA) is an emerging
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micropollutant, since its concentrations in water and soil were reported to be ranged
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from 0.5 to 5000 μg L-1 and 0.2 to 1000 μg kg-1, respectively.1-3 p-ASA is widely used
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as animal feed additives, due to its broad antimicrobial and nontoxic properties.4,5
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However, after excreted in manure, the water-soluble p-ASA would be degraded into
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high-toxic inorganic arsenic species (such as arsenate) in 30 days via the biotic and
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abiotic routes, thus leading to severe arsenic pollution in soil and groundwater.6,7 For
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example, in the Pearl River Delta of southern China, the concentration of p-ASA was
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detected up to 771 μg kg-1 in the surface soils surrounding swine farms, and the arsenic
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content was found to be far beyond the local background level.2 Therefore, the removal
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of p-ASA is crucial for maintaining the quality and safety of water and soil.
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To date, studies on p-ASA removal mainly focused on two types of techniques
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including degradation and adsorption.8,9 Comparing with the former technique,
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adsorption exhibited the advantages of higher efficiency, simpler operation, and lower
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risk of releasing inorganic arsenic into the environment. Several types of adsorbents
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have been studied for p-ASA adsorption, including ferric and manganese binary
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oxide,10 iron humate,11 and metal-organic frameworks (MOFs).12 Among these
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adsorbents, MOFs are attracting more attentions because of their high porosity,
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controllable structure, and high adsorption capacity to p-ASA (up to 791 mg g-1).13
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However, the adsorption affinity of MOFs to p-ASA is relatively weak, since the
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adsorption is mainly depended on the electrostatic attraction and pore filling. Therefore, 4
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to achieve efficient and quick removal of p-ASA, especially at environmentally relevant
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concentrations (e.g., below 5 mg L-1), specific adsorption sites in MOF structures
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towards p-ASA are required.
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Our previous work revealed that roxarsone (ROX) could be efficiently adsorbed by
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Fe3O4-graphene nanocomposites through coordination, hydrogen bonding, and π-π
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stacking.14 Considering the similar structure of p-ASA with ROX, new strategies are
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expected to increase the adsorption affinity through the mentioned interactions. Such
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strategies should point to utilizing MOFs which contain metal clusters for the As-O-M
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(M stands for the metal clusters in MOFs) coordination, organic linkers with benzene
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rings for π-π stacking, and functional groups for forming hydrogen bonds with p-ASA.
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UiO-67 is a Zr-based MOF which comprises Zr6O4(OH)4 clusters as 12-connected
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nodes and linear 4,4’-biphenyldicarboxylic acid (BPDC) ligands.15 UiO-67 showed
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high application potential in practical water treatments due to its simple synthesis
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method and superior chemical stability.16 It consists of substantial octahedral (16 Å)
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and tetrahedral (12 Å) cages,17,18 and consequently can expose abundant active sites for
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p-ASA adsorption. Considering the -NH2 and -OH groups in p-ASA molecules, the
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incorporation of -NH2 groups to the BPDC ligands of UiO-67 (denote as UiO-67-NH2)
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is expected to enhance the adsorption affinity through hydrogen bonding.19-21 Moreover,
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other interactions are also expected between UiO-67-NH2 and p-ASA. It was reported
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that the missing-linkers in UiO-66 could induce defects in the Zr nodes, which could
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provide more Zr-OH groups and greatly enhance the capture of ROX via the stronger
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As-O-Zr coordination.22,23 Similarly, this effect is also predicted between the Zr nodes 5
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with defects in UiO-67-NH2 and p-ASA. In addition, the BPDC ligands in UiO-67-NH2
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are also expected to bind p-ASA through π-π stacking.24,25
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Therefore, we expect the defective UiO-67-NH2 to be a powerful and advanced
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material for the efficient adsorption of p-ASA from aqueous media. Herein, we aimed
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to: (1) determine the adsorption capacity, affinity and rate of defective UiO-67-NH2
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towards p-ASA in comparison with the pristine UiO-67, to confirm the enhanced
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adsorption of UiO-67-NH2; (2) analyze the contribution of As-O-Zr coordination, π-π
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stacking and hydrogen bonding to the adsorption via extended X-ray absorption fine
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structure (EXAFS), x-ray photoelectron spectroscopy (XPS), and density functional
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theory (DFT) calculations; and (3) investigate the mechanism of amine modification on
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the enhancement of adsorption affinity. This study provides useful information on the
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design of novel and efficient materials for p-ASA removing via understanding the
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adsorption mechanism, and offers a new alternative to increase the adsorption affinity
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via the synergistic effect between the introduced functional groups.
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EXPERIMENTAL SECTION
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Synthesis and characterization of UiO-67 and UiO-67-NH2s
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The defective UiO-67 and its -NH2 modified derivatives were prepared using
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biphenyl-4,4’-dicarboxylic acid (BPDC) as ligand by following previously reported
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methods.22,26 The missing-linker-induced defects in the MOFs were produced by adding
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concentrated HCl during preparation. Two types of UiO-67-NH2s with different amine
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contents were obtained. The as-prepared UiO-67-NH2 that theoretically had one amine 6
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group per BPDC ligand was abbreviated as UiO-67-NH2(1), while the other one that
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had two -NH2 groups per BPDC ligand as UiO-67-NH2(2).
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The crystal structure, surface morphology, specific surface area and surface charge
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of UiO-67 and UiO-67-NH2s were analyzed using X-ray diffraction (XRD), scanning
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electron microscope (SEM), Brunauer-Emmett-Teller (BET) N2 adsorption/desorption
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method and zeta potential analyzer, respectively. Zeta potentials of the materials at pHs
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3-10 were determined using a NanoBrook Omni zeta potential analyzer (Brookhaven,
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USA). The concentration of the tested MOFs was 1 g L-1, and the pH was adjusted by
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HNO3 or KOH solution. Details of the characterization are provided in Section S1.
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Adsorption experiments
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For adsorption kinetic experiments, 0.045 g adsorbents were added to 300 mL p-ASA
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(Aladdin Bio-Chem Technology, China) solution at a concentration of 50 mg L-1, and
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shaken at pH 4.0 ± 0.1 and 25 C with a speed of 200 rpm for 1 min to 24 h. The
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adsorption kinetics curves were fitted with the pseudo-second-order non-linear kinetic
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model (SI Section S1). Adsorption isotherm studies were conducted with the p-ASA
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concentrations from 1 to 100 mg L-1, while the adsorbent concentration was kept at 0.15
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g L-1 in 30 mL solution (pH 4.0 ± 0.1). The mixtures were shaken under 25 C with a
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speed of 200 rpm for 24 h. After centrifugation separation, the residual p-ASA
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concentrations in the supernatants were measured by a UV-vis spectrometer (UV-2600,
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Shimadzu) at 252 nm. The adsorption isotherms were fitted with Langmuir and
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Freundlich models (SI Section S1). The effect of pH on adsorption was investigated by
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conducting adsorption experiments within the pH range of 3.0-10.0 at the p-ASA 7
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concentration of 50 mg L-1 and the adsorbent dosages of 0.15 g L-1.
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To detect the reusability of UiO-67 and UiO-67-NH2s, each adsorbent (5 mg) was
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firstly added to 30 mL p-ASA solution (pH 4.0 ± 0.1). After shaking for 24 h (25 C,
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200 rpm), the obtained adsorbents after adsorption were moved to 30 mL desorption
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solution containing 0.5 mol L-1 NaOH/ethanol, and shaking with a speed of 200 rpm at
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25 C for 1 h. The regenerated adsorbents were dried in a vacuum oven at 110 °C for
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12 h before the next adsorption cycle. The removal of p-ASA by UiO-67-NH2s in
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simulated natural and waste waters was studied in the presence of dissolved organic
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matter (DOM, 0-16 mg C L-1) and in swine manure lixivium (added p-ASA of 1-5 mg
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L-1). Experimental details were displayed in Section S1.
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EXAFS and XPS analyses
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EXAFS and XPS were used to investigate the interaction between p-ASA and UiO-
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67s.27 The samples on p-ASA (50 mg L-1) adsorbed UiO-67 and UiO-67-NH2s (0.15 g
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L-1) were prepared at pH 4.0, in a manner similar to the adsorption experiments. The K-
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edge EXAFS spectra of As in p-ASA-loaded samples were acquired at the beamline
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4W1B of the Beijing Synchrotron Radiation Facility (BSRF). All EXAFS data were
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collected in the fluorescence mode at room temperature, using a Lytle detector equipped
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with Soller slits and Ge filter for screening scattering and fluorescence background. The
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maximum absorption edge As was set to 11875 eV. The EXAFS data analysis was
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performed using the ATHENA and ARTEMIS interfaces to the IFEFFIT version 1.2.11
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program package.28 Details of the EXAFS data collection and analysis are provided in
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Section S1. 8
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XPS spectra were analyzed using an Axis Ultra DLD instrument (Kratos Analytical,
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U.K.) with an A1 Kα X-ray source. Spectra were recorded at a pass energy of 160 eV
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for survey scans and 40 eV for high-resolution scans. High-resolution scans were
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carried out in an energy range of 295-280 eV for C 1s, and 405-395 eV for N 1s XPS
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spectra.
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Computational calculation
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DFT calculations were performed using the Vienna ab initio simulation package
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(VASP). The Perdew-Burke-Ernzerhof (PBE) functional, and the potential projector
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augmented wave (PAW) pseudo-potentials were used for all the calculations. The plane-
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wave cutoff energy was set to 500 eV, which has been previously tested and shown to
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be appropriate for UIO-67.29 Scalar relativistic effects were incorporated into the
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effective core potentials via explicit mass-velocity and Darwin corrections. Detailed
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calculation methods are provided in Section S1.
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RESULTS AND DISCUSSION
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Characterization of the as-prepared MOFs
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The as-synthesized UiO-67 and UiO-67-NH2s exhibited typical characteristic peaks
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of Fm-3m symmetric space groups in the XRD patterns (Figure S1), consistent with the
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reported UiO-67 topology.30 The identical XRD peaks of UiO-67-NH2s with the
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pristine UiO-67 implied that introducing -NH2 groups did not change the framework
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structure. FTIR spectra of UiO-67-NH2s showed C-N and N-H stretching vibrations at
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1257 and 3300-3500 cm-1, respectively (Figure S2). The mole ratios of -NH2:Zr 9
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calculated from XPS data were 0.88 and 1.80 for UiO-67-NH2(1) and UiO-67-NH2(2),
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respectively (Table S1), which were similar to their theoretical values (1.0 for UiO-67-
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NH2(1) and 2.0 for UiO-67-NH2(2)). These results confirmed the successful amine
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modification of UiO-67. The structural illustrations of UiO-67, UiO-67-NH2(1) and
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UiO-67-NH2(2) are shown in Figure 1. The BET surface areas of UiO-67, UiO-67-
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NH2(1) and UiO-67-NH2(2) were 1871, 750, and 465 m2 g-1, respectively (Figure S3,
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and Table S1). The lower surface areas of UiO-67-NH2s compared with the pristine
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UiO-67 were probably due to the partial blocking of the pores by -NH2 groups on the
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surface (Figure 1a-1c).
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The as-prepared MOFs are thermally stable up to 320 °C as detected by the TG-MS
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(Figure S4) and temperature-dependent XRD (Figure S5). Therefore, based on the TGA
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data on the weight loss at 320-500 °C (Table S2, Figure S6), the numbers of the missing-
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linker induced defects for each unit of UiO-67, UiO-67-NH2(1) and UiO-67-NH2(2)
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were calculated as 4, 3.2 and 3.2, respectively. These defects would provide more
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binding centers towards p-ASA through the external Zr-OH groups,31 thus facilitating
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the p-ASA adsorption.
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Adsorption kinetics
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Adsorption kinetics of p-ASA by UiO-67 and UiO-67-NH2s was investigated and the
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results are shown in Figure 2a. All the kinetic curves were fitted using the pseudo-
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second order model, which was commonly used to describe adsorption kinetics in
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which chemisorption controlled the adsorption rate and the number of active sites
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determined the adsorption capacity.32 The obtained kinetic parameters are shown in 10
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Table S3. Good fits of the tested MOFs with the pseudo-second order model (R2 > 0.99)
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implied the adsorption of p-ASA on the tested MOFs was controlled by chemical
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interactions. The increased adsorption rates (k2) of UiO-67-NH2s relative to the pristine
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UiO-67 implied the enhancement of chemisorption between p-ASA and the amine
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modified MOFs. Moreover, in comparison with other porous MOFs (such as meso-ZIF-
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8 in ref.13), substantially enhanced adsorption rates were observed for UiO-67 and UiO-
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67-NH2s, which was possibly due to the stronger chemisorption between UiO-67s and
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p-ASA molecules.
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Adsorption isotherms
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Adsorption isotherms of UiO-67, UiO-67-NH2(1) and UiO-67-NH2(2) towards p-
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ASA are shown in Figure 2b. All isotherms were fitted well with Langmuir and
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Freundlich33,34 models (Table S4), but the R2 values of Langmuir model were higher.
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Therefore, the following discussion was mainly based on Langmuir-fitting results of all
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the MOFs. Maximum adsorption capacities (Qm) calculated from Langmuir model
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followed an order of UiO-67 > UiO-67-NH2(1) > UiO-67-NH2(2) (Figure 2b, Table S4).
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However, this order changed to an opposite sequence after normalizing by the surface
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area (Qm/Asurf in Figure 2c), indicating higher adsorption capacities of UiO-67-NH2s
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than the pristine UiO-67 deducting the effect of surface area. This observation could be
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explained by the steric hindrance of the introduced -NH2 groups situating in the aperture
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of the nanopores (Figure 1 and Table S1). The entry of p-ASA (with a molecule
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diameter of 6.625 Å13) to the internal part of UiO-67-NH2s would be obstructed because
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of their narrower apertures than the pristine UiO-67. 11
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It was reported that materials with a small Qm and large affinity coefficient (KL) could
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have a larger value of qe when compared with materials with a large Qm and small KL,
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at low pollutant concentrations.35 Therefore, considering p-ASA as a micropollutant,
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the KL value was more significant than Qm. As shown in Table S4, KL values of UiO-
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67-NH2s were much higher than that of the pristine UiO-67, and increased with
224
increasing -NH2 content. In order to further evaluate the adsorption affinity at different
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p-ASA concentrations, single point sorption coefficients (K)36 based on the Langmuir
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fitting results were calculated when Ce = 0.03 (K0.03) and 0.3 (K0.3) mg L-1. As shown
227
in Table S4, both of K0.03 and K0.3 followed the order of UiO-67-NH2(2) > UiO-67-
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NH2(1) > UiO-67, indicating that UiO-67-NH2s had higher affinities towards p-ASA.
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The higher affinities made UiO-67-NH2s having higher qe compared with the pristine
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UiO-67 at low concentrations of p-ASA, as shown in the insert of Figure 2b. This is
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very important for the practical application of UiO-67-NH2s, considering that the
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concentrations of p-ASA in environment are usually very low.
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The comparison of adsorption capacity and affinity of the present UiO-67s with other
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adsorbents in the published literature is listed in Table S5. The Qm value of UiO-67
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(454.54 mg g-1) was higher than most of the reported absorbents. Despite that
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mesoporous ZIF-8 had the highest Qm (791 mg g-1) and Qm/Asurf (0.70 mg m-2), UiO-67-
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NH2(2) was more superior for p-ASA capture in practical applications due to its much
238
higher adsorption capacity and affinity toward p-ASA (qe0.03 = 4.50 mg g-1 and K0.03 =
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150 L g-1) than ZIF-8 (qe0.03 = 0.76 mg g-1 and K0.03 = 25.3 L g-1) at low concentrations.
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Reusability 12
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The regeneration efficiency of UiO-67s is shown in Figure S7. Despite the adsorption
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capacities slightly decreased after the first recycle, UiO-67 and UiO-67-NH2(2) still
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exhibited considerable adsorption capacities after four cycles regeneration (over 85%
244
of the original capacity). FTIR analysis showed the -NH and C-N vibration bands still
245
present in UiO-67-NH2(2) after the first adsorption cycle (Figure S8), suggesting that
246
the -NH2 moieties remained stable during the repeated adsorption process. Meanwhile,
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XRD results showed that the crystal structure of UiO-67 and UiO-67-NH2(2) did not
248
change after regeneration (Figure S9). These results revealed that the UiO-67 and UiO-
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67-NH2(2) could be regenerated and reused for multiple times, thus confirming the
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practical value and application of UiO-67s as the adsorbents of p-ASA.
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Mechanism of p-ASA adsorption on UiO-67-NH2s
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To get insight into the adsorption mechanism of UiO-67-NH2s towards p-ASA,
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electrostatic interaction, As-O-Zr coordination, hydrogen bonding, and π-π interaction
254
were taken into consideration.37 The effects of pH on the adsorption of p-ASA were
255
studied to investigate the contribution of electrostatic interaction. Figure S10a showed
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that UiO-67 and UiO-67-NH2s exhibited the highest adsorption capacity at pH 4.0, and
257
then sharply decreased with the increasing pHs. The isoelectric points of the three UiO-
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67s were determined to be between pH 4 and 5, and thus their zeta potentials were quite
259
low at pH 4.0 (Figure S10b). Moreover, the aqueous dissociation constants (pKa) of p-
260
ASA molecules were 1.91, 4.13 and 9.19, respectively (Figure S11). Therefore, the
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arsenic group in p-ASA is electroneutral at pH 4.0.38 These results indicated that the
262
electrostatic attraction was not the dominant force for the p-ASA adsorption at pH 4.0. 13
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It has been well-documented that Zr-based materials could efficiently capture
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arsenate groups due to the bidentate binuclear and monodentate mononuclear
265
complexes forming between the Zr-OH groups and As.22,39 For the as-prepared UiO-67
266
and UiO-67-NH2s, these Zr-OH groups mainly originated from the defects present in
267
Zr-O clusters.23,40 To further reveal the role of As-O-Zr coordination in p-ASA
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adsorption, x-ray adsorption spectroscopy of As was determined. The As-O and As-Zr
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shells could be obviously isolated in the k3-weighted As K-edge EXAFS spectra and
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the corresponding Fourier-transforms (Figure 3), indicating the formation of As-O-Zr
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inner-sphere complexes after adsorption. In all the samples, the As-O first-neighbor
272
contributions were fit with 3.6-3.9 oxygen atoms at 1.69 Å (Table S6), which agreed
273
with the DFT calculation in the previous study.39
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The second-neighbor contributions were fitted with the As-Zr atom distances of 3.44,
275
3.41, and 3.40 Å for UiO-67, UiO-67-NH2(1) and UiO-67-NH2(2), respectively (Table
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S6). The As-Zr distances were consistent with that in the bidentate binuclear complex
277
obtained from the DFT calculation (see details in the DFT Calculation section), which
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was also observed in other Zr-based MOFs.41 Moreover, the As-Zr distances in UiO-
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67-NH2(1) and UiO-67-NH2(2) were shorter than that in UiO-67, indicating that the
280
amine modification of UiO-67 shortened the As-Zr atom distance, and thus formed
281
stronger inner-sphere complexes. The enhanced As-O-Zr coordination was one of the
282
explanations for the higher adsorption affinity of UiO-67-NH2s towards p-ASA than
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the pristine UiO-67.
284
The higher coordination number (CN) of the As-Zr contribution in UiO-67-NH2s 14
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than the pristine UiO-67 (Table S6) also indicated stronger As-O-Zr coordination. Such
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enhancement could be ascribed to the synergistic effect of other interactions, such as π-
287
π stacking and hydrogen bonding. Moreover, according to the Langmuir fitting results,
288
the maximum molecule uptake of p-ASA by UiO-67 was found to be 5.3:1 (p-ASA:Zr6
289
in Figure 4a), which exceeded the stoichiometric p-ASA:Zr6 value calculated by As-O-
290
Zr coordination (4:1 of p-ASA:Zr6 based on the bidentate binuclear complex forming
291
between p-ASA and the defective UiO-67 unit). Considering the absence of -NH2
292
groups in UiO-67 ligands, the hydrogen bonds between the pristine UiO-67 and p-ASA
293
were perceived to be relatively weak. Thus, the higher p-ASA uptake than the
294
stoichiometric value was possibly due to the π-π stacking. Further indication was
295
conducted with the high resolution C 1s XPS spectra (Figure 4b and 4c). For UiO-67s
296
before p-ASA adsorption, three peaks were observed at 284.6 eV, 285.9 eV and 288.5
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eV, which belonged to the sp2 C=C, C-N, and O-C=O groups in the BPDC linkers.42,43
298
The characteristic peak of π-π* component appeared at 291.2 eV44 after adsorption,
299
suggesting the contribution of π-π stacking for p-ASA adsorption. Meanwhile, the π-π*
300
proportions of UiO-67-NH2(1) and UiO-67-NH2(2) were 2.11% and 7.78%,
301
respectively, which were both higher than that of the pristine UiO-67, suggesting the
302
enhancement of π-π interaction after the -NH2 modification.
303
Considering the higher adsorption affinity of UiO-67-NH2s than the pristine UiO-67,
304
additional mechanism other than As-O-Zr coordination and π-π interaction should also
305
contribute to the adsorption by UiO-67-NH2s. As mentioned above, the good fitting of
306
the adsorption kinetic to the pseudo-second order model suggested that the adsorption 15
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capacities of UiO-67s were determined by the number of active sites on the
308
adsorbents.32 Since the surface area of UiO-67-NH2(2) was only 60% of UiO-67-NH2(1)
309
(Table S1), the active sites in UiO-67-NH2(2) could also conclude to be ~60% of those
310
in UiO-67-NH2(1). Therefore, the adsorption capacity of UiO-67-NH2(2) should be
311
about 60% of UiO-67-NH2(1) theoretically. However, the Langmuir-fitted adsorption
312
capacity and the molecular uptake of p-ASA:Zr6 by UiO-67-NH2(2) were calculated to
313
be 178 mg g-1 and 2.3:1, respectively, which were much higher than 60% of the p-ASA
314
amount adsorbed by UiO-67-NH2(1) (Table S4 and Figure 4a). This result suggested
315
that the additional -NH2 groups provided more active sites, thus enhancing the
316
adsorption capacity and affinity of UiO-67-NH2(2). Considering the previous
317
discussion, hydrogen bonds between UiO-67-NH2s and p-ASA were expected to be the
318
key role for the enhancement. XPS N 1s results provided strong evidence for the
319
hydrogen bond formation (Figure 4d and 4e). Before adsorption, the symmetrical peaks
320
locating at 399.4 eV were attributed to the free -NH245 in the BPDC linkers of UiO-67-
321
NH2s (Figure 4d). No signals of H-bonded -NH2 were observed in the spectra. After
322
adsorption, although no -NH2 groups existing on the pristine UiO-67 structure, the peak
323
for free -NH2 was still observed (Figure S12), which belonged to the adsorbed p-ASA.
324
Moreover, a new peak assigned to H-bonded -NH2 at 400.2 eV45 was observed in the N
325
1s spectra of UiO-67-NH2s after adsorption (Figurer 4e), and the peak ratio increased
326
with the amine content in UiO-67-NH2s. This result indicated that these hydrogen bonds
327
increased the sites for p-ASA adsorption on UiO-67-NH2s.
328 16
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DFT calculations
330
To further elucidate the roles of -NH2 groups in UiO-67-NH2s for p-ASA adsorption,
331
the possible interaction scenarios of UiO-67 and UiO-67-NH2(2) with p-ASA were
332
further investigated at the molecular level through DFT calculation. For UiO-67, it was
333
obvious that the As-O-Zr coordination had the highest interaction energy (-181.5 kJ
334
mol-1 in Figure S13a) and was considered to be the most favorable adsorption force.
335
The optimal configurations of the Zr nodes and p-ASA molecules suggested the
336
formation of bidentate binuclear As-O-Zr complexes after adsorption (Figure S13a),
337
which was consistent with the aforementioned EXAFS analysis. In addition, the
338
relatively high adsorption energy (-40.2 kJ mol-1) of the π-π interaction between p-ASA
339
and UiO-67 (face-centered distance, 3.8 Å, Figure S13b) indicated that the π-π stacking
340
also played an important role in the adsorption.
341
After amine modification, the optimal configurations between UiO-67-NH2(2) and
342
p-ASA are shown in Figure 5. The As-O-Zr bidentate binuclear complex, π-π stacking
343
and hydrogen bonds were all present in the UiO-67-NH2(2) samples after adsorption.
344
Moreover, it was obvious that the binding energies of As-O-Zr coordination and π-π
345
interaction in UiO-67-NH2(2) were both higher than those in the pristine UiO-67, while
346
the As-Zr atom distance and the benzene rings face-centered distance were shorter
347
(Figure 5, S13). These results indicated that As-O-Zr coordination and π-π stacking
348
were enhanced after -NH2 modification. Moreover, -NH2 groups in UiO-67-NH2(2) also
349
provided extra adsorption sites for p-ASA through hydrogen bonds with an optimal
350
configuration of NH…O and a bonding energy of -52.4 kJ mol-1 (Figure 5c), thus 17
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further increasing the adsorption affinity. These results were in agreement with the
352
EXAFS and XPS analyses. The interaction energies followed the order: UiO-67-NH2(2)
353
and p-ASA > water molecule and p-ASA > p-ASA and p-ASA according to DFT
354
calculation (Figure 5, S13), suggesting that p-ASA molecules were monolayerly
355
adsorbed on UiO-67-NH2(2) because free p-ASA molecules cannot be further adsorbed
356
by the bound p-ASA on UiO-67-NH2(2). Overall, p-ASA would form a monolayer
357
adsorption on the surface of UiO-67-NH2(2), under the combined interactions of As-O-
358
Zr coordination, π-π stacking and hydrogen bonding (Figure 6). It should be noted that
359
amine groups on UiO-67-NH2(2) played a significant role in enhancing the adsorption
360
affinity through forming new adsorption sites via hydrogen bonding, as well as
361
strengthening the As-O-Zr coordination and π-π stacking.
362 363
Adsorption behavior of amine modified UiO-67 in simulated natural and waste waters
364
To test if UiO-67-NH2s could efficiently remove p-ASA for practical application,
365
DOM containing water and swine manure lixivium were used to simulated natural and
366
waste water, respectively. Adsorption results indicated that at a p-ASA concentration of
367
0.5 mg L-1, the removal rate of UiO-67-NH2(2) was slightly decreased from 99.6% to
368
98.7% when the DOM concentration increased from 0 to 16 mg C L-1, which were
369
higher than those of UiO-67 (Figure 7a). When the DOM concentration was 16 mg C
370
L-1, the residual arsenic concentrations after adsorbed by UiO-67-NH2(1) and UiO-67-
371
NH2(2) were 4.15 and 2.26 μg L-1, respectively (Figure 7b), which were lower than the
372
arsenic standard in drinking water of WHO (10 μg L-1). The adsorption results of UiO18
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67-NH2s in swine manure lixivium at different p-ASA concentrations are shown in
374
Figure 7c. It can be seen that when the initial concentration of p-ASA was 5 mg L-1, a
375
dosage of 0.15 g L-1 UiO-67-NH2(2) could decrease the arsenic concentration to 28.1
376
μg L-1, which satisfied the arsenic standard in surface water of China (50 μg L-1,
377
GB3838-2002). To reduce the arsenic concentration to the same level (below 50 μg L-
378
1
379
respectively, which were 26.7 and 44.8 times higher than that of UiO-67-NH2(2) (Table
380
S7). Moreover, since UiO-67 has already been studied as a water-treatment adsorbent
381
for a period of time,16 its modification is supposed to be more simple and commercially
382
available, compared with synthesizing a new MOF. These results suggested that the
383
amine modified UiO-67 was a promising candidate for removing p-ASA from natural
384
and waste waters.
), the needed dosages of graphene and activated carbon were 4 g L-1 and 6.7 g L-1,
385 386
ENVIRONMENTAL IMPLICATIONS
387
The defective UiO-67-NH2 designed based on the structural features of p-ASA
388
showed high adsorption affinity towards p-ASA. The study of adsorption mechanism
389
indicated that the contribution of different adsorption forces followed an order of As-
390
O-Zr coordination > π-π stacking > H-bonding. The -NH2 groups in UiO-67-NH2
391
played an important role for the efficient adsorption, including enhancing the As-O-Zr
392
coordination and π-π stacking, as well as providing new adsorption sites for p-ASA
393
adsorption through H-bonding. These synergistic interactions resulted in strong affinity
394
of UiO-67-NH2 towards p-ASA, which were beneficial for the removal of p-ASA in 19
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simulated natural and waste waters. This study revealed great potential of -NH2
396
modified UiO-67s for the removal of p-ASA in practical applications. Moreover, this
397
work also provided a new route for increasing the adsorption affinity of adsorbents
398
towards targeted pollutants through engineering different functional groups to achieve
399
synergistic effects.
400 401
ASSOCIATED CONTENT
402
Supporting Information
403
Thirteen figures, seven tables and experimental details are presented in Supporting
404
Information section. The material is available free of charge via the Internet at
405
http://pubs.acs.org.
406
AUTHOR INFORMATION
407
Corresponding Authors
408
* Email:
[email protected] (Dr. Zhang Lin); phone: 86-20-39380503; fax: 86-20-
409
39380508
410
Notes
411
The authors declare no competing financial interest.
412 413
ACKNOWLEDGMENTS
414
This work was supported by the National Natural Science Foundation of China (grant
415
no. 21477129), the Guangdong Innovative and Entrepreneurial Research Team
416
Program (No. 2016ZT06N569), the China Postdoctoral Science Foundation (no. 20
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2016M600654), and the Fundamental Research Funds for the Central Universities (no.
418
2017PY009 and 2017BQ054). The authors thank the beamline 4W1B (Beijing
419
Synchrotron Radiation Facility) for providing the beam time.
420 421
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567
27
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568 569
FIGURES
570
571 572
Figure 1. Perspective views of (a) UiO-67, (b) UiO-67-NH2(1), and (c) UiO-67-NH2(2);
573
(d) Structure of the defective Zr6 node; (e) The BPDC linker for UiO-67 and its -NH2
574
modified forms for UiO-67-NH2(1) and UiO-67-NH2(2). In (a), (b), and (c), Zr6 nodes,
575
framework carbon and oxygen atoms are shown in cyan, white, and gray, respectively.
576
Modified -NH2 moieties are shown in red.
577
28
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579
580 581
Figure 2. (a) Adsorption kinetics, (b) adsorption isotherms, and (c) surface area-
582
normalized isotherms of p-ASA adsorbed by UiO-67, UiO-67-NH2(1) and UiO-67-
583
NH2(2).
29
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585
586
587 588
Figure 3. Arsenic K-edge data for p-ASA adsorbed UiO-67 and UiO-67-NH2 samples:
589
(a) filtered k3-weighted EXAFS data, (b) magnitude part of Fourier transformed R-
590
space, and (c) real part of Fourier transformed R-space. Experimental and calculated
591
curves are displayed as black solid lines and red open circles, respectively. Results of
592
the k3-weighted fitting are listed in Table S6. 30
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594
595
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597 598
Figure 4. The uptake of p-ASA by UiO-67, UiO-67-NH2(1) and UiO-67-NH2(2), and
599
related XPS analysis after p-ASA adsorption. (a) The uptake of p-ASA (adsorbed p-
600
ASA / Zr6 node) by UiO-67, UiO-67-NH2(1) and UiO-67-NH2(2); XPS C 1s and N 1s
601
spectra of UiO-67, UiO-67-NH2(1) and UiO-67-NH2(2) before (b, d) and after (c, e) p-
602
ASA adsorption.
603
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604
605
606 607
Figure 5. The optimal configurations obtained via DFT calculations of (a) As-O-Zr
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coordination, (b) π-π stacking, (c) and H-bonding between UiO-67-NH2(2) and p- ASA
609
(Magenta for As, cyan for Zr, red for O, blue for N, gray for C, and white for H). The
610
interaction energy between UiO-67-NH2(2) and p-ASA was calculated to be -297.4 kJ
611
mol-1 (As-O-Zr coordination π-π stacking, and H-bonding).
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613 614 615 616
Figure 6. The adsorption mechanism of UiO-67-NH2 towards p-ASA
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618
619 620
Figure 7. p-ASA adsorption by UiO-67, UiO-67-NH2(1) and UiO-67-NH2(2) in the
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presence of DOM or in swine manure lixiviums. (a) Effect of DOM on the removal
622
rates of p-ASA; (b) the residual arsenic concentrations (C0 = 0.5 mg L-1) in the presence
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lixiviums with different initial concentrations of p-ASA. The adsorbent concentrations
625
were kept at 0.15 g L-1 in 30 mL solution. The mixtures were shaken at pH 4.0 ± 0.1
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and 25 C with a speed of 200 rpm for 12 h.
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