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Au@Pd Bimetallic Nanocatalyst for Carbon-Halogen Bond Cleavage: Old Story with New Insight into How the Activity of Pd is Influenced by Au Rui Liu, Huimin Chen, Liping Fang, Cuihong Xu, Zuoliang He, Yujian Lai, Huachao Zhao, Deribachew Bekana Hirpa, and Jing-fu Liu Environ. Sci. Technol., Just Accepted Manuscript • DOI: 10.1021/acs.est.7b05996 • Publication Date (Web): 16 Mar 2018 Downloaded from http://pubs.acs.org on March 16, 2018
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Au@Pd Bimetallic Nanocatalyst for Carbon-
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Halogen Bond Cleavage: Old Story with New
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Insight into How the Activity of Pd is influenced by
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Au
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Rui Liu,a* Hui-min Chen,a,b Li-ping Fang,b Cuihong Xu,a,b Zuoliang He,a Yujian Laia, Huachao
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Zhaoa, Deribachew Bekanaa and Jing-fu Liua
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a
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Eco-Environmental Sciences, Chinese Academy of Sciences, Beijing 100085, China
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b
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State Key Laboratory of Environmental Chemistry and Ecotoxicology, Research Center for
Department of Chemistry, Faculty of Material Sciences and Chemistry, China University of
Geosciences, Wuhan 430074, China TOC art:
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ABSTRACT.
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AuPd bimetallic nanocatalysts exhibit superior catalytic performance in the cleavage of carbon-
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halogen bonds (C-X) in the hazardous halogenated pollutants. A better understanding of how Au
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atoms promote the reactivity of Pd sites rather than vaguely interpreting as bimetallic effect, and
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determining which type of Pd sites are necessary for these reactions are crucial factors for the
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design of atomically precise nanocatalysts that make full use of both the Pd and Au atoms.
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Herein, we systematically manipulated the coordination number of Pd-Pd, d-orbital occupation
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state and Au-Pd interface of the Pd reactive centers, and studied the structure-activity
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relationship of Au-Pd in the catalyzed cleavage of C-X bonds. It is revealed that Au enhanced
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the activity of Pd atoms primarily by increasing the occupation state of Pd d-orbits. Meanwhile,
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among the Pd sites formed on the Au surface, 5-7 contiguous Pd atoms, 3-4 adjacent Pd atoms
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and isolated Pd atoms were found to be the most active in the cleavage of C-Cl, C-Br and C-I
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bonds, respectively. Besides, neighbouring Au atoms directly contribute to the weakening of the
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C-Br/C-I bond. This work provides new insight into the rational design of bimetallic metal
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catalysts with specific catalytic properties.
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INTRODUCTION
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The catalyzed cleavage of carbon-halogen (C-X) bonds has profound and permanent importance
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for many aspects of chemical engineering,1 including the safe treatment of hazardous
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halogenated organic compounds.2-3 Traditionally, Pd nanostructures are the most favourable
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catalysts for this process in terms of cost (comparable or even lower than that of other Pt-group
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metals), activity (much more active than Cu or Ni) and reusability (better than that of ligand-
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stabilized homogeneous Pd catalysts).4 Unfortunately, the sluggish reaction kinetics,5 catalyst
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deactivation by the formation of Pd halide/Pd black on the surface, and coking deposition or
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metal sintering reduce the cost effectiveness of Pd nanocatalysts are the main barriers hindering
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implementation of Pd catalysts for environmental improvement.2-3, 6 Tremendous efforts have
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been devoted to overcoming these disadvantages. One important strategy involves engineering
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the surface atomic arrangement of Pd crystals and maximizing the exposure of the low-
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coordinate corner, edge and step atoms.7-8 For example, the {730} facet enclosed concave Pd
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nanocrystals was reported to show an activity 3.5 times higher than that of Pd nanocubes in the
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Suzuki coupling between phenylboronic acid and iodobenzene.9-10 However, later research
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revealed that this high activity like originated from the increased dissolution of active molecular
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Pd,11 which is unfavourable for the long-time stability/recyclability of Pd nanocatalysts. This
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result at least partially showed that controlling the morphology of Pd nanocrystals alone cannot
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fully overcome the drawbacks associated with Pd nanocatalysts. At the same time, parallel
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studies revealed that a bimetallic Pd nanocatalyst can exhibit markedly enhanced performance
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over its monometallic counterparts.3, 12-15 The introduction of other metal atoms typically shifts
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the Pd d-orbital occupation state, which in turn alters the sorption energies of
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substrates/intermediates/products.12,
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In addition to the electronic and geometric effect, the
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synergetic effects, which refers to other metal(c.a., Au) atom forms additional M-C or M-X bond
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to weaken the C-X bond and facilitates its cleavage on Pd sites, are also believed to contribute to
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the enhanced activity of Pd atoms.15 From this perspective, Au plays an impressive role in
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promoting the catalytic performance of Pd atoms.3,
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depositing 1 to 1.5 monolayers (ML) Pd on Au nanoparticle surface to form core (Au)-shell (Pd)
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(denoted as Au@Pd) nanostructure, Pd based mass activity in catalyzed dehalogenation of
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trichloroethylene (TCE) increased100 times over that of Pd nanoparticles (NPs).3, 5, 17, 20 Zhang
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et al. diluted Pd atoms into Au nanoparticles to form a single-atom Pd catalyst with high activity
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and durability in the Ullmann Reaction.18 Dhital et al. showed that Au-Pd alloy nanoclusters
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(NCs) could activate and break C-Cl bonds at room temperature, a process usually catalyzed by
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nucleophilic ligands stabilized Pd species at harsh conditions.19 In addition to the catalyzed
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cleavage of C-X bonds, Au@Pd bimetallic catalysts have also shown promise for application in a
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variety of other reaction processes, including nitrite reduction,21 low-temperature oxidation of
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greenhouse gases,22 and synthesis of H2O223 for Fenton or electro-Fenton mineralization of
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pollutants.24-25
13, 17-19
Wong et al. reported that upon
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Despite the broadly observed promotion of Pd activity by Au in C-X cleavage reactions, a
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consensus is still lacking on how this process occurs at the atomic level. The proposed active
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centers and the exact role of Au atoms vary greatly from case to case. For example, small Pd
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clusters of 2-3 continuous atoms on a Au surface,17 and Au-Pd interfacial sites have been
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proposed as the active centers.19 In accordance with the different atomic structure of the active
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Pd centers, the exact role of Au also varies.10, 19, 26 In addition to facilitating the formation of Pd
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clusters (geometric effect)
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effect),18 Au has also been reported to play a role in the direct cleavage of C-X bonds by
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and altering the d-orbital occupation state of Pd atoms (electronic
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weakening the Pd-X bonds and facilitating the reductive removal of X ions (synergistic effect).19
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The full answer to the above question is very crucial for the design of atom-economical
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nanocatalysts with a high performance/cost ratio.28 A precondition for this design is the
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sophisticated generation of Pd centers with defined atomic geometries (with different Pd-Pd
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coordination number, CNPd-Pd, and coordination atom), and thus the different d-orbital
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occupation state on the Au host material. Unfortunately, for the weak interaction between Pd and
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Au (the bond dissociation energy is 142.7 KJ mol-1),29-30 Pd atoms on Au surface apt to form
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additional Pd-Pd bond, this makes controlling the atomic geometry of Pd sites in Au-Pd
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nanocatalysts,31-33 especially CNPd-Pd, is almost a formidable task.
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Very recently, we introduced a strategy for modifying the binding strength to tailor the atomic
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geometry of Pd on ultrathin Au nanowires (NWs)32 by pre-depositing a Ag ML, and successfully
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synthesized AuPd core-shell (Au@Pd) NWs dominated by continuous Pd atoms and AuPd core-
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shell NWs with a Ag monolayer (AgML) between Au core and Pd shell (denoted as
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Au@AgML@Pd NWs) featured with isolated Pd atoms. Therefore, these NWs provide an ideal
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platform for identifying the active center in the C-X cleavage step, including the answer to the
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question whether a single Pd atom is active during this process or not. In this work, based on the
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developed tactic in manipulating the structure of Pd atoms,32 we synthesized Pd coated Au
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(Au@Pd) and Au@AgML (Au@AgML@Pd) NWs with different Pd coverage, as well as Pd
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NWs/NCs as catalyst for the catalyzed dehalogenation of halogenated phenols. Through
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adjusting the Pd coverage, we also manipulated the relative abundance of the Au-Pd or Au-
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Ag/Pd interface and the d-orbital occupation state of the Pd atoms. The exact structures of these
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Pd sites and their relative abundance were characterized by surface enhanced Raman scattering
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spectroscopy (SERS), extended X-ray absorption fine structure spectroscopy (EXAFS, CNPd-Pd
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and coordination number), X-ray absorption near edge structure spectroscopy (XANES, d-orbital
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occupation state) and CO-stripping experiments (Au-Pd interfacial sites). Based on the Pd
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reactive centers with well-defined structures, we systematically studied how the geometric (the
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coordination number of Pd atoms), the electronic (d-orbital occupation state) and the synergistic
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effect influence the catalytic performance of Pd bimetallic catalysts in the dehalogenation of 4-
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chlorophenol/4-bromophenol/4-iodophenol (4-CP/4-BP/4-IP). This ultimately led us to propose a
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role for Au atoms in the Pd-catalyzed cleavage of C-X bonds at the atomic level.
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EXPERIMENTAL SECTION
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Pd catalyst synthesis. Au@Pd and Au@AgML@Pd NWs with different Pd coverages (1/16, 1/8,
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1/4, 1/2 and 1.0 ML) were prepared according to our recently developed protocol,32 and details
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for calculating the amount of Pd or Ag precursor needed for the formation of Pd ML/Ag ML, as
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well as experimental evidence for the presence of Pd ML has been presented in supporting
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information (Figure S1-5). In brief, ultrathin Au NWs was synthesized by quickly injecting 3.0
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mL 100 mM KBH4 solution into a septum-sealed 50 mL flask that containing 0.05 mmol of
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HAuCl4 and 25 mg of Triton X-114 (TX-114) in 47.0 mL ice-cooled water under vigorous
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stirring.34 For the coating of Pd shell on Au core, 0.19, 0.375, 0.75, 1.50, or 3.0 mL of ice-cold
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1.0 mM Na2PdCl4 solution was dropwise added into 10.0 mL dispersion of freshly synthesized
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Au NWs under stirring. In each of these cases, the Pd coverage is 1/16, 1/8, 1/4/, 1/2 or 1.0 ML,
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respectively. The synthesis of Au@AgML NWs is similar to that of Au@Pd NWs, but replaces
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Na2PdCl4 with 3.0 mL of 1.0 mM AgNO3 solution. In the case of the Au@AgML@Pd NWs, 3.0
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mL of 1.0 mM AgNO3 solution was added into a 10.0 mL dispersion of freshly synthesized Au
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NWs while stirring, followed by the addition of 0.19, 0.375, 0.75, 1.50, or 3.0 mL of ice-cold 1.0
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mM Na2PdCl4 solution.
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Pd NWs were synthesized using a similar protocol to that of Au NWs with Pd(NO3)2 as Pd
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precursor,34 the amount of injected 100 mM ice-cooled KBH4 solution was reduced to 1.0 mL.
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PVP stabilized Pd cluster was also synthesized by reduction of Na2PdCl4 with KBH4.26
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Specifically, 27.5 mg PVP and 0.05 mmol Na2PdCl4 were dissolved in 45 mL ultrapure water
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and stirring in ice bath for 30 min, followed by injecting 5.0 mL 100 mM KBH4 solution. The
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synthesized Pd NCs were purified by ultracentrifugation at 10, 000 rpm with a molecular cutoff
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of 10.0 kD to remove unbounded PVP and inorganic ions like Cl-, K+/Na+ and BO3-, and
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redispersed in ultrapure water. Furthermore, the synthesized nanocatalysts were supported on
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aminopropyl-triethoxysilane (APTS)-modified magnetic Fe3O4 nanospheres (NSs, ~400 nm in
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diameter) to increase the colloid stability and reusability of the catalysts.35
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Catalytic test. The catalyzed dehalogenation of 4-halogen phenol was employed as a model
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reaction for studying the catalytic performance of Pd in the cleavage of C-X bonds. This
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involves the dehalogenation of 1.0 mM 4-chlorophenol (4-CP), 4-bromophenol (4-BP) or 4-
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iodophenol (4-IP) dissolved in 1.5 mM KOH aqueous solution (10.0 mL, the initial pH is about
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11.1) under a continuous H2 flow (100.0 mLmin-1) and stirring at 400 rpm. The added Au@Pd
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and Au@AgML@Pd NWs catalysts contained 5.0 µM (0.53 mg L-1, for 4-CP and 4-IP) or 0.5 µM
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(0.05 mg L-1, for 4-BP) Pd.36 The amount of unreacted 4-halogen phenol was determined by
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sampling the reacting solution at selected time intervals, neutralized with HCl and analysed by
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high-performance liquid chromatography (HPLC). For the study of the catalytic performance of
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Pd catalysts at more environmentally realistic conditions, the concentration of 4-CP/4-BP/4-IP
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studied was lowered to 0.02 mM. The initial pH was adjusted to 7.0 ± 0.5 with KOH/HNO3, and
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the catalyst was lowered to 0.4 µM (0.04 mg L-1, for 4-CP and 4-IP) or 0.1 µM (0.01 mg L-1, for
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4-BP) Pd () in Au@Pd and Au@AgML@Pd NWs accordingly. To test the colloid stability and
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reusability of the Fe3O4 NSs-supported Au@Pd NWs catalyst, the nanocatalyst was recovered at
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the end of the reaction by an external magnetic field, washed with ethanol and water, and
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resuspended in the reactant solution. The catalytic performance in three successive runs was
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studied and compared. Data shown in the figures are mean values of at least three experiments.
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The experimental uncertainties, including instrumental errors, relative standard deviations and
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sorption were evaluated in the absence of catalyst, which showed that total uncertainty was less
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less than 1% for high concentration of halogenated phenols but increased to 3-5% with the
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decrease of their initial concentration to 0.02 mM.
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XAS study. The local coordination environment (coordination number and bond lengths) of
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the Pd atoms in the Au@Pd and Au@AgML@Pd NWs was probed by EXAFS/XANES. The Pd
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and Ag k-edge EXAFS and XANES spectra were acquired at beamline 14W1 of the Shanghai
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Synchrotron Radiation Facilities (SSRF). The X-ray was monochromatized by a double-crystal
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Si{311} monochromator. The storage ring of SSRF was operated at 3.5 GeV with a current of
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300 mA. The Au LIII-edge XAS spectra (1W1B beamline at the Beijing Synchrotron Radiation
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Facilities) were also acquired to build a full model of the Pd atoms. The acquired EXAFS data
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were processed according to the standard procedures using the WinXAS 3.1 program.37 The
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theoretical amplitudes and phase shift functions were calculated with the FEFF8.2 code using the
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crystal structure parameters of Ag and Pd foils.38
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CO-stripping experiment. A 50.0-µl aliquot of a Pd NWs (0.05 µmol Pd) or Au@Pd NWs
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dispersion containing 0.05 µmol Au was dropped on a glassy carbon electrode (5 mm id) as a
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supportless electrocatalyst. This was followed by adding 10 µl of a Nafion solution (0.5% w/v in
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ethanol, DuPont). The prepared electrode was activated in a N2-saturated 0.1 M KOH solution
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with cyclic voltammetry from −1.0 to 0.45 V, and Pt wire and a Ag/AgCl electrode were used as
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the counter electrode and reference electrode, respectively. After CO was chemisorbed on the Pd
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atoms, it was then stripped at 50 mV·s-1, and the Pd surface area (SAPd) was calculated by:
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SAPd=QCO-stripping/420 (mC cm−2)
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SERS experiment. Because of the δ-donation/π-back donation behaviour between the C≡N
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bond and its bounding metal atom, the SERS spectra of chemisorbed 2,6-DMPI is very sensitive
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to the bounding metal atom and adsorption configuration,32,
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characterize the atomic geometry of the Pd atoms and estimate the relative abundance of the
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different Pd sites and track the changes in the Pd site geometry during the reaction in this work.32
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32
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RESULTS AND DISCUSSION
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and was employed to
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Characterization of the Pd catalysts. Figures 1a-d illustrate high-resolution transmission
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electron microscopy (HRTEM) images of the Pd nanostructures studied in this work. The sized
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of Pd NCs were in the range of 2 to 3 nm (Figure 1a), showing the effectiveness of polyvinyl
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pyrrolidone (PVP) in stabilizing the Pd NCs. Based on the magic cluster model,41 the surface Pd
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atoms made up ~50% of the total Pd atoms in the Pd NCs. The diameter of the Pd NWs was
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approximately 2 nm (Figure 1b), and about 50% of their Pd atoms were also located on the
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surface. On the other hand, although the epitaxially deposited Pd overlayer was difficult to
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distinguish based on the analysis of the morphology and lattice fingerprint (Figures 1c, d),
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energy-dispersive X-ray spectroscopy (EDS) mapping, SERS and EXAFS all supported the
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presence of Pd as an overlayer (Figures S6-9 and see below). Figure 1e depicts representative
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transmission electron microscopy (TEM) images of the Au@Pd NWs on Fe3O4 NSs (Figure
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S10), where the NWs are interlaced on the Fe3O4 NSs. Elemental analysis (Figure 1f) revealed
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that the loading efficiency, which referred to the ratio between nanostructures that adsorbed on
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Fe3O4 nanospheres and their total amount, was above 60% for both Au and Pd in the Au@Pd,
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Au@AgML@Pd and Pd NWs, signifying the effective immobilization of the NW catalyst on the
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Fe3O4 NSs. This is ascribed to the stabilization of the NWs by the weakly binding surfactant
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Triton X-114,34 and thus, the low steric hindrance to the formation of Metal-N bonds between
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the NWs and –NH2 groups.42 Moreover, the ratio between the capture efficiencies of Au and Pd
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in Au@Pd and Au@AgML@Pd was very close to 1.0, proving that Pd atoms were deposited on
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Au or the Au@AgML NWs and simultaneously adsorbed on the Fe3O4 NSs. Of note is for the
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ultralong nature of the NWs catalyst, only a small part of atoms (Au or Pd) take part in the
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formation of Metal-N bond, and therefore the change in the electronic structure of Pd reactive
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centers would be very small. In contrast, due to the strong binding of PVP, the associated steric
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hindrance limited the contact between the –NH2 groups and the surface Pd atoms, and thus, the
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loading efficiency for the PVP-stabilized Pd NCs was no more than 20.0%. This strong binding
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was also reflected in the inferior catalytic performance of the Pd NCs compared to that of the
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NWs (see below).
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Activities of the Pd catalysts in the dehalogenation of 4-CP. The catalytic performance of the
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Pd nanostructures in the cleavage of C-X bonds was initially evaluated through the
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dehalogenation of 4-CP. In the absence of the Pd catalyst, and also in the presence of Au or
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Au@AgML NWs, only a slight decrease (less than 5%) in the 4-CP concentrations was observed,
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even under a continuous flow of H2 for more than 2 hours, and the generated phenol was
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undetectable, suggesting that no dehalogenation of 4-CP occurred. In the reaction catalyzed by
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Au@Pd (1.0 ML) or Au@AgML@Pd (1.0 ML) NWs containing 5.0 µM Pd, the conversion
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reached 99% or above in 10 min (Figure 2a). This reveals the high activity of Au and
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Au@AgML-supported Pd atoms in the cleavage of the C-Cl bond. By comparison, the Pd NCs
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and NWs exhibited much lower conversions of 68.5 ± 9.0% and 88.2 ± 3.7%, respectively, even
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in the presence of a much higher dose of Pd atoms (20.0 µM) and elongated time of 20 min 20
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min. The higher activity of the Pd NWs over that of the Pd NCs is ascribed to the absence of the
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strongly binding PVP, which was negatively charged at the studied pH value and unfavourable
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for the adsorption of halogenated phenolate, and therefore the improved accessibility of the
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active sites. It’s deserved to point out that the influence of TX-114 molecule to the reaction
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process is neglectable (Figure S11-12). The discrepancy in the activities of the different Pd
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catalysts is more clearly illustrated in the kinetics curves (Figure 2b). The fitted rate constants for
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the Au@Pd, Au@Pd on Fe3O4 NSs and Au@AgML@Pd NWs reached at least 0.25 min-1, while
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this value was sharply reduced to 0.11 and 0.07 for the Pd NWs and Pd NCs. The Pd mass
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normalized rate constant were 53.1 ± 4.9, 53.8 ± 3.9, 46.5 ± 3.5, 5.30 ± 0.85 and 3.52 ± 0.27 min-
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1
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NWs (1.0 ML), Pd NWs and Pd NCs, respectively (Figure 2c). These values correspond to a 10-
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fold increase in mass activity of Pd after coating a monolayer of Pd on Au or Au@Ag NWs.
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Even taking into account the cost of Au, and the total mass (Au and Pd) normalized mass activity
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of Au@Pd and Au@AgML@Pd is still 2 times or higher than that of Pd NCs or NWs.
mM-1 for the Au@Pd NWs (1.0 ML), Au@Pd NWs (1.0 ML) on Fe3O4 NSs, Au@AgML@Pd
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Mass Transfer Limitation during the Catalytic Reaction. Since the catalyzed
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dehalogenation reaction is a three phase (solid−liquid−gas) process, the mass transfer process
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may influence the reaction kinetics. To ensure that the observed difference in catalytic
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performance of Pd catalysts stems from their intrinsic catalytic activity rather than the presence
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of mass transfer limitation, both external and internal mass transfer limitation was evaluated.43-47
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As shown in the Supporting Information, the external mass transfer limitation could be ignored
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in our experimental condition (bubbling the reaction solution with continuous H2 at a flow rate of
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100 mL·min-1 and stirring at 400 rpm), while the Weisz-Prater parameter down to 2.1×10-3,
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0.56×10-9 and 0.83×10-9 for Au@Pd on Fe3O4 nanospheres, Pd NCs and NWs suggests the
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internal mass transfer limitation is also negligible. Therefore, the different catalytic performance
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displayed in Figure 2, especially the superior activity of Au@Pd and Au@AgML@Pd over that of
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Pd NCs and NWs, is the direct result of their intrinsic activity.
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Enhanced stability of Pd atoms on Au or Au@AgML. In addition to the superior activity, the
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kinetics data also indicate an enhanced stability of the Pd atoms on the Au or Au@AgML surface
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(Figure 2b). Catalyzed by the Au@Pd and Au@AgML@Pd NWs, the change in the 4-CP
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concentration fits well to a pseudo-first-order kinetic model throughout the entire reaction. This
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indicates that the deactivation of Pd atoms was successfully suppressed. In contrast, gradual
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deactivation of the monometallic Pd (NWs and NCs) catalysts is indicated by the decrease in the
247
slope. In fact, for all tested Pd concentrations, i.e. 0.53 to 2.12 mg L-1, the activity diminished
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after 20-30 min (Figure S13). This enhanced stability of the Pd atoms on Au and Au@Ag is
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partially ascribed to the increased anti-oxidation capacity of the shell Pd atoms, since severe
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oxidation/dissolution was observed in Pd NWs/NCs as their deactivation (Table S1-2). Indeed,
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our XANES data (see below) confirmed that all the Pd atoms were in the metallic state after
252
being coated on the Au or Au@Ag surface, while up to 40% of the Pd atoms in the Pd NWs/NCs
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were in the form of PdII. These oxidized Pd atoms are apt to dissolve into the reaction solution
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and either redeposit on the Pd NWs/NPs surface or deactivate the catalyst in the form of Pd black
255
over time.
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To further test the superior stability of the Au@Pd and Au@AgML@Pd, we studied the activity
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of the catalysts in the absence of base as well as the ability to recycle the used catalyst. Unlike
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the low activity and fast deactivation monometallic Pd NWs, the Au@Pd NWs effectively
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catalyzed the dehalogenation of 4-CP in the absence of base (Figure S14). Moreover, no
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perceptible loss of activity was observed after 3 successive runs (Figure S15). Both of these
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results demonstrate the enhanced stability of Pd atoms on Au or Au@AgML NWs, and
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meanwhile, the Pd atoms are more likely to play role in the heterogeneous pathway with Pd
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atoms rather than ions as the active center.48 In accordance with the well-preserved activity of the
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Au@Pd NWs catalyst, the similarity of the SERS spectrum of 2,6-DMPI chemisorbed on the as-
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synthesized and spent Au@Pd and Au@AgML@Pd NWs catalyst also proved that the reaction
266
process did not influence the atomic geometry of the Pd atoms or the relative abundances of the
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Au and Pd atoms, as well as that of isolated and continuous Pd atoms (Figure S16). Notably, due
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to the high sensitivity of the SERS spectra of 2,6-DMPI to the electronic structure of the metal
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atoms underneath32, 40 as well as the high affinity of Cl- for transition metal atoms such as Pd, a
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~10 cm-1 red-shift occurred in the νNC, which is consistent with the enhanced occupation of the
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Au/Pd orbitals upon the adsorption of Cl- ions. However, leaching of Pd ions was observed for
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the monometallic Pd catalyst (See discussion and Table S1-2, Figure S17).
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Pd coverage and substrate-dependent activity. In addition to displaying enhanced
274
activity/stability, the specific structure of the Pd atoms on the Au@Pd and Au@AgML@Pd NWs
275
allowed us to ascertain the reactive centers in the reaction by studying the Pd coverage-activity
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relationship.32 Figures 3a-c shows the changes in the catalytic performance of Au@Pd and
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Au@AgML@Pd with different Pd coverages in the dehalogenation of 4-CP. Obviously, all the
278
Au@Pd NWs were active in this reaction, even for a Pd coverage as low as 1/16 ML. Moreover,
279
as the Pd coverage increased to 1/2 ML, the activity of the Au@Pd NWs increased accordingly,
280
and the first-order rate constant reached 0.26 ± 0.02 min-1, which is comparable to that of the 1.0
281
ML-covered Au@Pd NWs. In sharp contrast, the Au@AgML@Pd NWs (1/4 ML) was completely
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inactive in this reaction, and the activity of Au@AgML@Pd (1/2 ML) was also very limited.
283
However, the activity of Au@AgML@Pd (1.0 ML) quickly caught up to that of Au@Pd (1.0 ML).
284
Based on these results and our previous knowledge of the changes in the structure of the Pd
285
atoms on the Au@AgML@Pd NWs with different Pd coverages, in particular, the totally inactive
286
of Au@AgML@Pd with the Pd coverage no more than 1/4ML, we hypothesize that the atomic
287
geometry of Pd sites strongly affects their activity in the cleavage of C-Cl.
288
The Au@Pd and Au@AgML@Pd NWs displayed even higher activities in the dehalogenation
289
of 4-BP than case of 4-CP. In the reaction catalyzed by Au@Pd NWs, the conversion approached
290
100% within 10 min for most of the Au@Pd catalysts and the whole process fits the first-order
291
model. Again, this result is ascribed to the enhanced stability of the Pd atoms on the Au NWs
292
surface (Figures 3d-f). In contrast, both the Pd NWs and NPs catalysts were rapidly deactivated
293
(within 10 min). This result is consistent with the Pd-related SERS band (Figure S16), which is
294
ascribed to the rapid dissolution of Pd induced by the high affinity of Br- ions for Pd
295
atoms/ions.49 Note that unlike the monotonic increase in activity with increasing Pd coverage
296
observed for the Au@Pd NWs in the dehalogenation of 4-CP, the activity of this catalyst in the
297
dehalogenation of 4-BP was the highest for a Pd coverage of 1/2 ML, in which the rate constant
298
reached 0.687 min-1, corresponding to an initial turnover of frequency (TOF) as high as 1254.8 ±
299
82.8 min-1. A similar trend was also observed for the Au@AgML@Pd NWs, in which
300
Au@AgML@Pd (1/2 ML, 0.49 ± 0.03 min-1) displayed a much higher activity than that of
301
Au@AgML@Pd (1/4 ML, 0.07 ± 0.01 min-1) and Au@AgML@Pd (1.0 ML, 0.39 ± 0.02 min-1)
302
(Figure 3f).
303
The higher activity in the dehalogenation of 4-BP over that of 4-CP is consistent with the
304
lower bond strength of C-Br (~250 kJ mol-1) compared to that of C-Cl (~350 kJ mol-1),30 and
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therefore the lower energy barrier/activation energy. To test whether the catalytic performance of
306
the Au@Pd and Au@AgML@Pd NWs in the cleavage of the C-X bonds was solely determined
307
by the bond strength, we further studied the reaction of C-I bonds (4-IP, Figures 3g-i). To our
308
surprise, although as much as 15-40% of the 4-IP was reduced within the first 2 min, all of the
309
catalysts, including the Au@Pd and Au@AgML@Pd NWs, were completely deactivated within
310
2-4 min. However, this deactivation of Au@Pd and Au@AgML@Pd did not necessarily result
311
from the total dissolution of Pd atoms from the Au and Au@Ag NWs. In fact, the majority of the
312
Pd atoms remained on the Au@AgML@Pd and Au@Pd NWs. The plausible explanation for this
313
is the strong binding of iodine ion on Pd sites inhibits the further adsorption of 4-IP molecule. On
314
the other hand, unlike in the case of 4-CP or 4-BP where the NWs with Pd coverages of 1/2 or
315
1.0 ML were much more active than their low-coverage counterparts, in the dehalogenation of 4-
316
IP, the activities of the Au@Pd and Au@AgML@Pd NWs decreased sharply with increasing Pd
317
coverage. Moreover, the Au@AgML@Pd NWs consistently displayed higher activities than the
318
Au@Pd NWs.
319
Changes in the structure of the Pd reactive center with changing Pd coverage. Based on
320
the data shown in Figure 3, the activity of the Pd atoms in the cleavage of C-X bond was highly
321
dependent on the Pd coverage. A similar trend was reported by Wong et al.5, 20 and is attributed
322
to the increased number of Pd-Au interfacial sites at which the formation of Au-Cl bond
323
facilitates the cleavage of the C-Cl bond. Sakurai et al. also proposed this mechanism as an
324
explanation for the unexpected activity of Au0.5Pd0.5 alloy NCs in the activation of C-Cl bonds at
325
mild condition.19 To elucidate the contribution of the Au-Pd interfacial sites to the cleavage of C-
326
X bonds, the relative abundances of the Au-Pd and Pd-Pd sites in the Au@Pd NWs were
327
estimated by CO-stripping experiments (the CO-stripping behaviour of the Au@AgML@Pd NWs
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is very complicated and beyond the scope of this work).50 According to the literature, CO
329
molecules bound to Pd atoms inside the Pd cluster can be stripped at low potential,50 while due to
330
the enhanced occupation of the d-orbitals and the strong back donation of π* electrons to the
331
adsorbed CO, Pd atoms located at Pd-Au interfaces bind CO more strongly and require a higher
332
potential to be stripped. Indeed, the CO-stripping curve for the Au@Pd NWs was split into two
333
peaks centerd at -0.08 and 0.11 V, and the current of the latter peak decreased with increasing Pd
334
coverage (Figure 4a). Therefore, the observed attenuation of the 0.11 V peak with increasing Pd
335
coverage reflects the growth of the Pd cluster and a decrease in the number of Au-Pd interfacial
336
sites. Quantitatively, with the increase in the Pd coverage on Au@Pd from 1/16 to 1.0 ML, the
337
relative abundance of the interfacial sites dropped from 84.8% to 31.9%. This decrease in the
338
number of Au-Pd sites is associated with the increase in activity, especially in the reactions with
339
C-Cl and C-Br, suggesting that such sites may play a less critical role in the cleavage of C-X
340
bonds (See below).
341
In addition to the change in the relative abundance of Au-Pd interfacial sites, a direct result of
342
the increase in the Pd coverage is a change in both the CNPd-Pd on the Au@Pd and
343
Au@AgML@Pd NWs and the d-orbital occupation state of the Pd atoms. These changes are
344
reflected in the Pd k-edge EXAFS spectra (Figures 4b-d) and the whiteline (WL) intensities of
345
the XANES spectra (Figures 4e-f), respectively. In the k3-weighted Fourier-transformed (FT) Pd
346
k-edge EXAFS spectra, the Au@Pd and Au@AgML@Pd NWs displayed a unique spectrum that
347
stemmed from the distinct coordination environments, which was unlike the case of the Pd NCs
348
and NWs, whose spectral features resembled those of Pd foil (Figures S18-20). More specifically,
349
all spectra of the Au@Pd NWs shared a nearly identical shape with only slight shift in the first
350
nearest coordination peaks in the R space compared to that of Pd foil/NCs/NWs. This result is
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consistent with the fact that the epitaxially grown Pd overlayer on the Au NWs was primarily
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coordinated by Au atoms with Au-Pd bonds (~2.84 Å) that were longer than the Pd-Pd bonds in
353
Pd foil or the NCs/NWs (~2.74 Å). Meanwhile, the similarity in the spectra indicates that the
354
coordination environment did not change significantly. The detailed first-shell fitting revealed
355
that with the increase in the Pd coverage from 1/6 to 1.0 ML, the CNPd-Pd increased from 0.70 ±
356
0.27 to 1.31 ± 0.36, 1.55 ± 0.44, 2.42 ± 0.38 and 2.78 ± 0.53. The case for the Au@AgML@Pd
357
NWs is much more complicated than that of the Au@Pd NWs. The spectra of the
358
Au@AgML@Pd NWs with Pd coverages of 1/16, 1/8 and 1/4 ML possessed similar shapes, and
359
no Pd-Pd bonds were detected. With the increase in the Pd coverage to 1/2 and 1.0 ML, Pd-Pd
360
bonds were observed with CNs of 1.21 ± 0.25 and 2.34 ± 0.46, respectively, which are
361
comparatively smaller than those of the Au@Pd NWs. However, after accounting for the fact
362
that 49% and 29% of the isolated Pd atoms remained in the 1/2 and 1.0 ML-covered
363
Au@AgML@Pd NWs (Figure S6, Table S3-5), the CNPd-Pd reached 2.37 ± 0.25 and 3.30 ± 0.46,
364
respectively (see the discussion in the SI).
365
Meanwhile, as shown in the XANES spectra displayed in Figures 4e and f, the WL intensity of
366
the Pd NCs and NWs is between that of PdO and Pd foil. This results from the partial oxidation
367
of the surface Pd atoms, which is directly related to the low stability of the monometallic Pd
368
catalysts in the cleavage of C-X bonds. Upon epitaxial growth of Pd on the Au or Au@AgML
369
NWs, the Pd WL intensity decreased substantially due to the direct withdrawal of d-electrons
370
from the Au/Ag atoms.14 Naturally, a lower Pd coverage corresponded to a lower WL intensity.
371
Based on close inspection of the XANES spectra of the Au@AgML@Pd and Au@Pd NWs, the
372
WL intensity of the Au@AgML@Pd NWs was always lower than that of Au@Pd. This trend is
373
attributable to the fact that both the Au and Ag atoms donate electrons to the Pd atoms, and the
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Pd atoms on the Au@AgML@Pd NWs had a higher d-orbital occupation than the Au@Pd NWs.
375
Notably, both the Au@Pd and Au@AgML@Pd NWs exhibited a lower WL intensity than that of
376
Pd foil, signifying the more atom-like nature of Pd atoms on Au and Au@AgML, which is very
377
essential for the enhanced stability of these Pd catalysts.36, 51-52
378
Since all the above mentioned structure parameters (CNPd-Pd, WL intensity and Au-Pd
379
interfacial sites) of Au@Pd catalyst are relevant with other. Moreover, in most cases, the activity
380
of Pd centers is influenced by the above mentioned factors simultaneously. This makes the study
381
of how Au atoms work in the AuPd catalyst a very challenging work, and often vaguely
382
interpreted
383
tailoring/characterizing the structure of Pd sites on Au NWs surface, new door opened for
384
ranking the relative importance of the CNPd-Pd and d-orbital occupation state, and clarifying how
385
Au atoms influence the catalytic performance of AuPd in the cleavage of C-X bond preliminarily.
386
To this end, multivariable regression analysis was first performed for the association of the
387
activity of Au@Pd catalysts with the CNs and WL intensity of Pd center. As presented in Table
388
S6-8, the CNs (P < 0.005 for CNs in the case of 4-CP) and WL intensity (P < 0.005 for WL in
389
the case of 4-IP) are of significant influence. Besides, the high model R2 (> 0.9 in both cases)
390
reveals that it is reasonable to assume Au and Au@AgML promotes the activity of Pd atom in a
391
similar manner. On the other hand, it seems the third factor-the Au/Ag-Pd interfacial sites cannot
392
be ignored for 4-BP, as both the low model R2 and the high P-value (R2 = 0.48, P > 0.1 for CNs
393
and WL intensity) indicate that CNs and WL intensity alone are insufficient to explain the high
394
activity of Au@Pd.
as
the
bimetallic
effect.
Herein,
with
the
capacity
of
systematically
395
Critical number of Pd atoms in the reactive center for the cleavage of C-X bonds. Based
396
on the dependence of the activity on the Pd coverage shown in Figure 3, as well as the changes in
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the CNPd-Pd revealed by the EXAFS data and the coordination model (Figures 4b-d, S21), the
398
activity of the Pd atoms was strongly influenced by their atomic geometry, more specifically, the
399
CNPd-Pd, as summarized in Figures 5a-c. The observed inactivity of Au@AgML@Pd with Pd
400
coverages of 1/16 and 1/8 ML in the catalyzed dehalogenation of 4-CP and 4-BP indicates that a
401
single Pd atom is insufficient to activate/break the C-Cl and C-Br bonds. However, the opposite
402
situation was observed in the case of C-I, where the highest activity was obtained for the
403
Au@AgML@Pd and Au@Pd catalysts with the lowest Pd coverage, indicating that isolated Pd
404
atoms are highly active for the cleavage of C-I bonds (Figure 5a). Notably, the fast cleavage of
405
the C-I bond did not generate phenol, instead, 4,4-dihydroxybiphenyl was identified as the main
406
product. A plausible explanation for this is the strong adsorption of I- on Pd atoms hinders the
407
simultaneous activation of H2 and C-I bonds. Meanwhile, Au or Ag atoms facilitate the cleavage
408
of C-I bond and form Au-C/Ag-C intermediates, and finally the M-C intermediates (M=Au, Ag
409
or Pd) coupled into 4,4-dihydroxybiphenyl. On the other hand, satisfactory activity was observed
410
for Au@Pd and Au@AgML@Pd in the cleavage of C-Br catalyzed by with when the CNPd-Pd
411
reaches 2~2.5 (Figure 5b), indicates 3~4 continuous Pd atoms may form the active center in this
412
process. The case is even more apparent in the cleavage of C-Cl bonds, in which the activity was
413
linearly related to CNPd-Pd (Figure 5c) and independent of the metal atoms underneath (Au or
414
Ag), suggesting that 5-7 contiguous Pd atoms act as the active center in this reaction.
415
The cleavage of a C-X bond involves the adsorption of C-X onto a reactive center, activation
416
of C-X and H2, and finally, the breakage of C-X into C-H and X- (Figure 5f). As predicted by
417
Honkala et al.,12 only Pd atoms are favourable adsorption sites. Moreover, on the Au surface, Pd
418
sites with larger CNPd-Pd have higher adsorption energy. The observation that 5-7 contiguous Pd
419
atoms form the most active site for the cleavage of C-Cl bonds, matches well with the theoretical
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prediction that Pd4/Au is the most favourable site for the adsorption of C-Cl.12 Since the co-
421
adsorption of 4-CP and H2 (roughly needs 2 Pd atoms53) is necessary for the conversion of 4-CP
422
to phenol, it is reasonable to conclude that more Pd atoms, i.e., 5-7 atoms, are needed in this
423
process. As the affinity of Br and I for Au/Ag atoms increases, the number of Pd atoms in the
424
optimized adsorption site decreases accordingly, and only one Pd atom is sufficient for the
425
cleavage of C-I bonds.
426
The influence of d-orbital occupation state of Pd atoms. The CNPd-Pd or the size of the Pd
427
cluster is not the only factor that determines the adsorption energy, otherwise the Pd
428
monometallic catalysts would be more active than Au@Pd. In fact, the Au and Ag atoms
429
underneath the Pd layer also alter their d-orbital occupation state, and Pd atoms with higher d-
430
orbital occupation state display higher adsorption energies. Furthermore, the linear relationship
431
between the activity of the Au@Pd and Au@AgML@Pd NWs in the cleavage of C-I and the WL
432
intensities of the catalysts shown in Figure 5d demonstrates that Au or Au/Ag atoms enhanced
433
the activity of the Pd atoms through changing the d-orbital occupation state of Pd atoms. A
434
similar situation was observed in the reaction with C-Br bonds after excluding the contribution
435
from the ensemble effect. For example, Au@AgML@Pd (1/2 ML) and Au@Pd (1/2 ML)
436
possessed similar CNPd-Pd (2~2.5), but the former was much more active (Figure 5b). Note that
437
even though the highest activity in the cleavage of C-Cl bonds was observed for the Au@Pd and
438
Au@AgML@Pd NWs with the highest Pd coverage (highest WL intensity, or lowest d-orbital
439
occupation state), this does not mean that the d-orbital occupation state of Pd was less important
440
in this reaction. In fact, the 10-fold higher activity of the Au@Pd/Au@AgML@Pd NWs over that
441
of the Pd NWs/NCs demonstrated in Figure 2 stemmed from the increased d-orbital occupation
442
state.
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Mechanistically, the breakage of C-X bonds involves the oxidative addition of C-X on Pd
444
atoms to form Pd-X and Pd-C bonds through overlap between the lone pairs of electrons in the
445
X/C atoms and the unoccupied d-orbitals of the Pd atoms. This oxidative addition step is then
446
followed by the reductive removal of the halide ion and the formation of a C-C or C-H bond.19
447
The enhanced occupation of the d-orbit either strengthens the anti-bonding interaction or
448
weakens the Pd-X/Pd-C bonds, which is very essential for the subsequent removal of C/X from
449
the Pd atom and regeneration of the active site. Therefore, in addition to its contribution to the
450
determination of the adsorption energy, the d-orbital occupation state also directly influences the
451
activity of Pd atoms during the cleavage of C-X bonds.
452
The Au (Au@AgML)-Pd interfacial sites. In addition to the CNPd-Pd and d-orbital occupation
453
state, the Au/Ag-Pd interface sites also plays a vital role in the cleavage of C-X bonds. This is
454
especially important in the case of C-Br (Figures 5b, e, S25), where the Au@Pd (1/2 ML) and
455
Au@AgML@Pd (1/2 ML) were much more active than their counterparts with Pd coverages of
456
1.0 ML. Since the d-orbital occupation state of Au@Pd (1/2 ML) was similar to that of Au@Pd
457
(1.0 ML), the only explanation for this difference in reactivity is the decreased abundance of
458
Au/Ag-Pd interfaces. Cooperation between Pd and Au/Ag atoms also likely to occur in the
459
cleavage of C-I bonds, especially in the case of isolated Pd atoms in Au@AgML@Pd NWs,
460
where Pd atoms are coordinated by 4~5.5 Ag atoms (Table S3). This value is larger than the
461
theoretical one (3 for Pd ML on Au/Ag {111} facet), and indicates that parts of Pd atoms
462
diffused into the subsurface of Ag layer.54 Whether the location of Pd atoms on Ag overlayer
463
influence their catalytic performance, especially when Ag may involve in the cleavage of C-X
464
bond still needs further study. However, the role of Au/Ag-Pd interface sites is not very
465
significant in the case of C-Cl. We hypothesize that this difference in the importance of Au-Pd
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interface sites between C-Br and C-Cl arises from the difference in their binding affinities with
467
Au or Ag atoms,19 where the higher affinity between Br and Au or Ag atoms increases the
468
likelihood that these metal atoms participate in C-X cleavage, i.e., by forming a Br-Au/Ag bond
469
to weaken the C-Br bond. Remarkably, the involvement of Au or Ag atoms into the catalysis
470
process is not a necessary for the cleavage of the C-X bond. Only when the size of Pd ensemble
471
is not big enough for the adsorption/activation of the C-X molecule, the role of neighboring Au
472
or Ag atoms can be significant.
473
Removal of low concentration halogenated phenols at neutral pH. To evaluate whether the
474
mechanism proposed from the dehalogenation of high concentration pollutants in alkaline still
475
holds up for more environmentally realistic condition, i.e., with low concentration of pollutant
476
and neutral pH, where the catalyzed dehalogenation process would occur, the catalytic
477
performance of Au@Pd and Au@AgML@Pd NWs in the removal of 0.02 mM halogenated
478
phenols at pH 7.0 ± 0.5 were also studied. As presented in Table 1 and Figure S26-28, Au@Pd
479
and Au@AgML@Pd NWs showed high activity in catalyzed cleavage of the C-X bond at
480
environmental relevant condition. Moreover, a similar trend was observed in both experimental
481
conditions, i.e., high concentration at basic solution and low concentration at neutral pH.
482
Specifically, isolated Pd atoms (with Pd coverage no more than 1/4 ML in Au@AgML@Pd NWs)
483
showed extremely low activity in the case of 4-BP and 4-CP (effect of CNPd-Pd), while with the
484
highest activity in the hydrogenation of 4-IP (effect of d-orbital occupation state). On the other
485
hand, with the increase of Pd coverage, both Au@Pd and Au@AgML@Pd NWs showed
486
markedly increased activity in the removal of 4-CP. Meanwhile, the significant higher activity of
487
Au@Pd(1/2 ML) and Au@AgML@Pd(1/2 ML) over their counterparts covered with 1.0 ML Pd
488
in the removal of 4-BP, again infers the important role of Au/Ag-Pd interfacial sites.
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Environmental implications. The findings of this study highlight the potential for employing
490
rationally designed Pd nanoarchitectures with well-defined structures in the determination of
491
structure-activity relationships during environmental catalytic processes. Considering the
492
increasing importance of Pd and other Pt group metals based AuM bimetallic catalysts in various
493
environmental decontamination processes,21-25 and the demonstrated generality of coating an
494
additional metal on the surface of ultrathin Au/Au@Ag NWs to generate a highly effective
495
catalyst,32, 55 this study may create important opportunities for the atomically precise synthesis of
496
various supported bimetallic catalysts with core–shell structures for broad applications, in
497
particular for fundamental mechanistic studies. Meanwhile, previous work by Wong et al showed
498
that Au atoms also increased Pd atoms’ resistance to other deactivation factors like sulfur
499
poisoning, showing the potential of developed Au@Pd and Au@AgML@Pd NWs for water
500
treatment.56-57 Noteworthy is although C-I itself is easily cleaved in the presence of Pd atoms, the
501
high affinity of I atoms/ions for Pd atoms may hinder their further reaction. Therefore, iodinated
502
pollutants may be resistant to degradation by Pd catalysts and should be studied further.
503
ASSOCIATED CONTENT
504
Supporting Information.
505
Documentation of the experimental details; additional results of the study (HAADF-STEM-EDS
506
mapping of NWs, SERS spectra of chemisorbed 2,6-DMPI on Au@Pd and Au@AgML@Pd NWs,
507
catalytic data and fitted Pd k-edge EXAFS curve); additional discussion.
508
AUTHOR INFORMATION
509
Corresponding Author
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* E-mail:
[email protected].
511
Notes
512
The authors declare no competing financial interest.
513
ACKNOWLEDGEMENTS
Page 24 of 36
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We acknowledge the editor and the anonymous reviewers for their constructive comments,
515
criticism and suggestions. This work was financially supported by the National Key R&D
516
Program of China (2016YFA0203102), the National Natural Science Foundation of China
517
(21577157 and 21777177), and the Strategic Priority Research Program of the CAS
518
(XDB14020101). The authors acknowledge the staff at the BL 14W1/1W1B beamline of the
519
SSRF/BSRF for their assistance during the XAS measurements. Liu R. acknowledges support
520
from the Youth Innovation Promotion Association of CAS.
521
REFERENCES
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Figures
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Figure 1. (a-d) Representative TEM images of the Pd catalysts in this study: (a) Pd NCs, (b) Pd
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NWs, (c) Au@Pd NWs and (d) Au@AgML@Pd NWs. The corresponding HRTEM images and
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fast Fourier transform images are shown as inserts. (e) TEM images of Au@Pd NWs loaded on
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Fe3O4 NSs. (f) Immobilization efficiency of different Pd nanostructures on Fe3O4 NSs.
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Figure 2. Catalytic performance of the Pd nanostructures in the hydrodechlorination of 4-CP
695
(1.0 mM 4-CP+1.5 mM KOH). (a-c) 4-CP conversion, first-order kinetics data, and mass
696
normalized activity of Pd NWs (5.0, 10.0 and 20.0 µM ), Pd NCs (20.0 µM), Au@Pd NWs,
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Au@AgML@Pd NWs (5.0 µM of Pd) and Au@Pd NWs on Fe3O4 NSs.
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Figure 3. Catalytic performance of Au@Pd and Au@AgML@Pd NWs with varying Pd coverage
701
in the catalyzed dehalogenation of (a-c) 4-CP (1.0 mM 4-CP + 1.5 mM KOH, 5.0 µM Pd catalyst)
702
and (d-f) 4-BP (1.0 mM 4-BP + 1.5 mM KOH, 0.5 µM Pdcatalyst). (g-i) Activity of Au@Pd (red
703
curves) and Au@AgML@Pd NWs (blue curves) in the dehalogenation of 4-IP (1.0 mM 4-IP + 1.5
704
mM KOH, 5.0 µM Pdcatalyst).
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Figure 4. a) CO-stripping curves of Au@Pd NWs. b-d) Fourier-transformed k3-weighted Pd k-
708
edge EXAFS spectra of Pd, Au@Pd, and Au@AgML@Pd NWs. e, f) Normalized Pd K-edge
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XANES spectra of Au@Pd NWs and Au@AgML@Pd. The spectra of Pd foil, Pd NWs and Pd
710
NCs are also shown for comparison.
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Figure 5. Influence of the various primary factors on the activity of Au@Pd and Au@AgML@Pd
714
NWs in the cleavage of C-X bonds: a-c) geometric effect, d) electronic effect, and e) synergistic
715
effect. Schematic diagram of f) the size of the Pd ensemble on Au or Au@AgML increases with
716
the increase of coordination number (CN) and g) the mechanism by which Au atoms influence
717
the activity of Pd in the cleavage of C-X bonds
718 719
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Table 1. Catalytic performance of Au@Pd and Au@AgML@Pd NWs with varying Pd coverage
721
in the catalyzed dehalogenation of low concentration (0.02 mM) of 4-CP/4-BP/4-IP at neutral pH
722
(7.0± 0.5).
Catalyst
Au@Pd
Au@AgML@Pd
Pd coverage (monolayer, ML)
Initial TOF in (molphenol · molPd-1·min-1) 4-CP
4-BP
4-IP
1.0
9.10 ±2.19
55.6±9.8
0.75 ± 0.31
1/2
5.93±1.13
68.2 ± 12.3
1.06 ± 0.29
1/4
5.35±1.38
37.1 ± 5.7
2.50 ± 0.32
1/8
3.27±0.55
28.8 ± 4.5
3.02 ± 0.43
1/16
0.90±0.35
16.2 ± 3.3
4.41 ± 1.33
1.0
8.21±1.79
44.8 ± 10.3
0.95 ± 0.25
1/2
6.11±1.76
61.3 ± 17.7
2.02 ± 0.55
1/4
0.19±0.05
2.62 ± 0.53
3.11±0.90
1/8
-
3.63 ± 0.56
1/16
-
5.49 ±1.35
723
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