Accepted Manuscript Facile synthesis of N-doped carbon layer encapsulated Fe2N as an efficient catalyst for oxygen reduction reaction Zaojin Liu, Jing Yu, Xingyun Li, Lixue Zhang, Dong Luo, Xuehua Liu, Xiaowei Liu, Shuibo Liu, Hongbin Feng, Guanglei Wu, Peizhi Guo, Hongliang Li, Zonghua Wang, Xiu Song Zhao PII:
S0008-6223(17)31165-X
DOI:
10.1016/j.carbon.2017.11.051
Reference:
CARBON 12581
To appear in:
Carbon
Received Date: 8 October 2017 Revised Date:
15 November 2017
Accepted Date: 18 November 2017
Please cite this article as: Z. Liu, J. Yu, X. Li, L. Zhang, D. Luo, X. Liu, X. Liu, S. Liu, H. Feng, G. Wu, P. Guo, H. Li, Z. Wang, X.S. Zhao, Facile synthesis of N-doped carbon layer encapsulated Fe2N as an efficient catalyst for oxygen reduction reaction, Carbon (2017), doi: 10.1016/j.carbon.2017.11.051. This is a PDF file of an unedited manuscript that has been accepted for publication. As a service to our customers we are providing this early version of the manuscript. The manuscript will undergo copyediting, typesetting, and review of the resulting proof before it is published in its final form. Please note that during the production process errors may be discovered which could affect the content, and all legal disclaimers that apply to the journal pertain.
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ACCEPTED MANUSCRIPT Facile synthesis of N-doped carbon layer encapsulated Fe2N as an efficient catalyst for oxygen reduction reaction Zaojin Liu
a,b, 11
, Jing Yu
c,1
, Xingyun Li
a,b,*
, Lixue Zhang
c*
, Dong Luo
a,b
, Xuehua Liu
a,b
,
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Xiaowei Liu a,b, Shuibo Liu a,b, Hongbin Feng a,b, Guanglei Wu a,b, Peizhi Guo a,b, Hongliang Li a,b, Zonghua Wangc, Xiu Song Zhao a,b,d
Institute of Materials for Energy and Environment, Qingdao University, Qingdao, 266071, China
b
Laboratory of New Fiber Materials and Modern Textile, Breeding Basis for State Key Laboratory,
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a
c
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College of Materials Science and Engineering, Qingdao University, Qingdao, 266071, China Shandong Sino-Japanese Center for Collaborative Research of Carbon Nanomaterials, College of
Chemistry and Chemical Engineering, Qingdao University, Qingdao, 266071, China. School of Chemical Engineering, The University of Queensland, St Lucia Campus, Brisbane,
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QLD 4074, Australia
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d
*
Corresponding author. E-mail address:
[email protected] (X. Li).
1
These authors contribute equally to this work.
ACCEPTED MANUSCRIPT Abstract: Development of non-noble metal catalysts for oxygen reduction reaction (ORR) is of significant importance for the commercialization of fuel cells and metal-air batteries. Here we provide an
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efficient method to produce core-shell structured Fe-N-C catalyst via a facile in-situ chelating strategy by introducing ammonia iron citrate during the polymerization process of dopamine. The influence of calcination temperature and atmosphere on the physicochemical property and the
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activity of the catalyst are systematically evaluated. By calcination at 800 oC with NH3
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atmosphere, Fe2N encapsulated with N doped carbon layers shows excellent activity with close onset and half wave potential (E1/2) while better methanol crossover resistance than the Pt/C catalyst. The high activity could be due to the synergistic effect of Fe2N with the N-doped graphitic carbon layers and the mesoporous structure facilitating the mass transfer. Moreover, the
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simple synthesis process could provide a versatile routine to construct core-shell structured metal-N-C composite for a wild catalytic application.
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1. Introduction
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Oxygen reduction reaction (ORR) is a critical cathodic process in fuel cells and metal-air batteries which are regarded as two promising electrical devices with high energy efficiency and low environmental pollution. [1, 2] However the currently used Pt/C catalyst hinders its commercialization since the high price, limited reserve and low toxicity tolerance of Pt. [3-6] Hence the development of alternative non-noble metal catalyst has long been a hot topic in regards of both scientific research and industrial application. In the last several decades, tremendous efforts have been paid to nano-carbon based composite. [7] For instance, nitrogen doping is
ACCEPTED MANUSCRIPT adopted to endow pure carbon catalytic activity by creating positive charge on adjacent carbon atoms to facilitate the O2 activation. [8-10] Furthermore, introduction of transition metal into nitrogen doped carbon could significantly boost the ORR activity. [11] Vast of novel M-N-C
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(M=Fe, Co etc.) structures have been reported [12-17] , among which, Fe-N-C has been attracted particular research interest due to its promising catalytic performance. [18-25] However there is still no consensus on the reaction mechanism for the Fe-N-C system since various iron phases
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were identified to be catalytic active, e.g. Fe3O4 [26], Fe3C [27], Fe [28-30], FeN [31, 32], Fe2N
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[33, 34] etc. and even a dual active centers were proposed [35, 36]. Despite the above dispute, there is common view lies in that to construct iron species and nitrogen doped carbon composite is key to synergistically catalyze oxygen reduction reaction.[37] It is reported that iron could promote the graphitization and also tune the electronic states of the sp2 carbon which contribute to
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the excellent ORR activity. [38-42] In turn, the graphitic carbon layer will benefit the electron transfer and bind with the catalyst to alleviate its agglomeration. Taking advantage of the electronic interactions between iron species and carbon, core-shell structured Fe-N-C could be
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prospective with a rational design strategy.
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Dopamine is a mussel inspired biomimetic materials which can polymerize and coat on almost any substrate at high pH value. [43-45] The abundant hydroxyl and amino groups in dopamine offer itself great chelating ability with metal ions. [46-48] After calcination, PDA (polymerized dopamine) could be transformed into nitrogen doped porous carbon which will have the chances to enwrap metal species inside the final N-C materials. Taking the above features into account, here we demonstrate the feasibility of the complexing of Fe3+ with dopamine during polymerization process to construct the core-shell structured Fe-N-C composite. The precursor we
ACCEPTED MANUSCRIPT selected is ammonium ferric citrate (AFC) in that the interaction between Fe3+ with PDA could be enhanced by the possible hydrogen bonding since the existence of citrate and ammonium ions in AFC. To optimize the catalytic activity we concisely tune the final structure and iron crystalline
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phase by controlling the calcination temperature and atmosphere. By a fare comparison between different iron species of Fe3C, Fe2C, Fe3N, Fe4N, Fe2N, it is found that Fe2N encapsulated in nitrogen doped carbon showed outperformed performance with close activity and better stability
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to Pt/C catalyst. This work provides an attractive core-shell structured Fe2N-N-C as candidate to
construct other metal-N-C composite.
2. Experimental
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2.1 Preparation of Fe-PDA composite
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replace Pt and moreover the simple synthesis process could be used as common method to
Firstly, 1.5 g dopamine hydrochloride (Shanghai Macklin Biochemical Co., Ltd) was dissolved in 300 mL deionized water to form a transparent solution. 0.5 g ammonium iron (Ⅲ)
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citrate (Sinopharm Chemical Reagent Co., Ltd) in 100 mL deionized water was added slowly to
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the above solution, followed by stirring for 30 minutes. Then, the pH value of the mixture was adjusted to 8.5 using Tris-buffer (Tris(hydroxymethyl)aminomethane, Shanghai Macklin Biochemical Co., Ltd) and magnetically stirred at room temperature for 24 h. The black suspension was filtered and repeatedly washed with abundant deionized water. After drying at 60 o
C overnight, the precipitate was calcined at NH3 atmosphere with different calcination
temperature of 600 oC, 700 oC, or 800 oC for 3 h to obtain the final product which was named as NH3-Fe-N-C-600, NH3-Fe-N-C-700, NH3-Fe-N-C-800 respectively. As comparison, the sample
ACCEPTED MANUSCRIPT was calcined with Ar atmosphere at 800 oC to obtain Ar-Fe-N-C-800. The reference catalyst were also prepared by impregnating activated carbon (Shanghai Macklin Biochemical Co., Ltd) with ammonium iron citrate (Fe loading amount of 20 wt%) and calcined at 800 oC with Ar or NH3
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atmosphere respectively which was designated as Ar-Fe-AC and NH3-Fe-AC.
2.2 Physicochemial Characterization
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The morphology is characterized by JEOL JEM-2100 transmission electron microscope (TEM). Powder X-ray diffraction (XRD) was performed on a Rigaku Ultima IV X-ray
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diffractometer with Cu-Kα radiation (λ=0.15418 nm). N2 adsorption-desorption was carried out at Quantachrome Autosorb iQ3 and before the test the samples were degassed at 150 oC for 12 h. Raman spectra were collected using a Renishaw in Via Plus Micro-Raman spectroscopy system equipped with a 50 mW DPSS laser at 532 nm. X-ray photoelectron spectrometer (XPS) was
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recorded in a Thermo Fisher ESCALAB 250Xi spectrometer with Al Kα X-ray source (1486.6 eV, operated at 15 kV and 10.8 mA). The iron loading was analyzed by inductively coupled
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plasma-atomic emission spectrometry (ICP-AES, SHIMADZU ICPS-8100).
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2.3 Electrochemical measurements
The electrochemical properties of the catalysts were tested using a three-electrode system in
O2-saturated 0.1 M KOH and 0.1 M HClO4 solution by a Bio-logic VSP 300 electrochemical work station at room temperature. Catalyst-coated glassy carbon rotating disk electrode (RDE) or rotating ring-disk electrode (RRDE) were used as working electrodes, platinum mesh was used as the counter electrode and saturated calomel electrode (SCE) were used as the reference electrode. To prepare the working electrode, 10 mg catalysts or 3 mg 20 wt% Pt/C was dispersed in mixed
ACCEPTED MANUSCRIPT solution which consist of 20 µL Nafion solution (0.1 wt%) and 1 mL deionized water to form a homogeneous ink. 9 µL suspension were then casted onto the GC electrode and dried in air. The electrode was first activated by a few cycles of CV tests at 0.05 V/s and tested at 0.01
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V/s for electrochemical measurements. A rotating disk electrode (RDE) test was conducted at rotating speed from 400 rpm to 2025 rpm in O2-saturated 0.1 M KOH and 0.1 M HClO4. For the RRDE tests, the ring potential was set at 1.5 V versus RHE with a scan rate of 10 mV·s-1. The
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electron transfer numbers during the oxygen reduction reaction were determined from the
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Koutechy-Levich equation, which was analyzed at different potentials of RDE tests. Chronoamperometric measurements were performed at corresponding potential to deliver a current density of 10 mA·cm-2 for 6000 s.
The transferred electron numbers per O2 involved in the oxygen reduction can be calculated
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by the Koutechy–Levichequation as given below: ଵ ଵ
ଵ
= + =
ଵ
+
ଵ
ై ౡ னభ/మ ౡ
B= 0.2nF(DO)2/3 v-1/6 CO
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where n corresponds to the transferred number, F is the Faraday constant (F = 96485 C·mol-1), DO
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is the diffusion coefficient of O2 in 0.1 M KOH (1.9×10-5 cm2·s-1), n is the kinetic viscosity (0.01 cm2·s-1), and CO is the bulk concentration of O2 (1.2×10-6 mol·cm-3). The
electron
transfer
number
from
RRDE
experiment
was
determined
by
the following equation:
n = 4ID/[ID+ (IR/N)] where ID is the disk current, IR is the ring current, and N is the ring correction coefficient. In RRDE experiment, N was determined to be 0.45 from the reduction of Fe(CN)64-/3- redox couple.
ACCEPTED MANUSCRIPT The ring potential was held at 1.5 V vs. RHE.
3. Results and discussion
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The Fe-N-C catalyst was prepared as illustrated in Fig. 1. Ammonium ferric citrate was firstly mixed with dopamine in aqueous solution under stirring, during which iron ions could be well chelated with the catechol and amino groups of dopamine [49]. Then, as the pH value was tuned
polymer. Upon calcination, Fe-N-C catalyst was obtained.
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to 8.5, dopamine slowly polymerized to form PDA with iron species being wrapped inside the
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Figs. 2(a) show the TEM image of NH3-Fe-N-C-800 catalyst. It can be seen that iron species are evenly loaded on porous carbon materials and from HRTEM in Fig. 2(b), we can clearly detect the core-shell structure with iron species thoroughly encapsulated by few layers graphene. The lattice spacing of the iron compound is calculated to be 0.34 nm corresponding to the (101) planes
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Fe2N (JCPDS 73-2102) consistent with XRD patterns in Fig. 2(c). Meanwhile, from Fig. 2(b), we can also detect hollow vesicle, which may be created by the movement of iron species driven by
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the high temperature. The above results sufficiently prove the feasibility of in-situ iron ion
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chelating method to construct the novel carbon layer encapsulated Fe2N composite.
Fig. 1 Illustration of the preparation of Fe-N-C catalyst.
By XRD characterization in Fig. 2(c), it is interesting to find that the crystalline phase is
ACCEPTED MANUSCRIPT sensitive to the calcination atmosphere as well as the calcination temperature. When the sample was calcined at 600 oC with NH3 atmosphere, pure Fe2C phase is obtained, nevertheless the catalyst phase is changed to both Fe4N and Fe3N as the calcination temperature increased to 700 C, and Fe2N finally occurred at 800 oC. This suggests that high temperature could facilitate the
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formation of Fe2N which may be more thermodynamically stable. As comparison, 800 oC calcined samples at Ar atmosphere showed pure Fe3C phase. To get deeper insight into in-situ metal
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complexation route and the role of PDA played for iron crystalline phase, we made reference
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catalyst by post loading ammonium ferric citrate onto activated carbon with the traditional impregnation method followed by calcination at 800 oC with Ar or NH3 atmosphere. XRD patterns in Fig. S1(a) showed that besides iron carbide there exist Fe2O3 and FeO phases for Ar-Fe-AC. Comparatively, the absence of iron oxide in Ar-Fe-N-C-800 highlights the unique reducing
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capability of PDA with catechol groups to facilitate the reduction of iron oxide as documented in other literatures [48, 50, 51], which may help the formation of iron carbide. The influence of calcination temperature on the carbon graphitization was characterized by Raman spectra as
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shown in Fig. S2, there are two typical peaks of G band at 1578 cm-1 derived from the vibration of
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sp2 C and D band at around 1345 cm-1 corresponding to the amorphous carbon. The ratio of the intensity for D band to G band (ID/IG) decreased obviously with the increase of calcination temperature indicating that high temperature could facilely enhance the graphitization of N-C material. The specific surface area and the pore textures were obtained by N2 adsorption and desorption experiment. As shown in Fig. 2(d), the specific Brunauer-Emmett-Teller (BET) surface area of NH3-Fe-N-C-800 is calculated to be 124.5 m2/g with pore volume of 0.4 cc/g, and the material showed mesoporous structure with the DFT pore size distribution centered at around 3.8
ACCEPTED MANUSCRIPT nm, which will facilitate the exposure of active sites to the reactant and promote the mass
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diffusion through the solid catalyst.
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Fig. 2 (a), (b) TEM and HRTEM of NH3-Fe-N-C-800, (c) XRD patterns of Fe-PDA calcined at different temperatures, (d) N2 adsorption-desorption isotherm and DFT pore size distribution of
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NH3-Fe-N-C-800.
XPS measurements were carried out to get the surface chemical composition information. As
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shown in Fig. 3, there exist C, Fe, N and O peaks for NH3-Fe-N-C-800. The nitrogen content was calculated to be 3.5% with 43.3% pyridinic N (398.2 eV), 46.7% pyrrolic N (400.8 eV), 4.3% Fe-N (399.5 eV) and 5.7% quaternary N (402.6 eV)[52]. The excellent O2 activation activity of pyridinic and quaternary N [25, 53] make the N doped carbon surface could serve as the additional active sites to synergistically catalyze ORR. As comparison, we also investigated the surface composition of PDA calcined at 800 oC and NH3 atmosphere without adding iron. From Fig. S3 we can see that about 4% N is incorporated and the N peak is fitted into 29.6% pyridinic N, 21.0%
ACCEPTED MANUSCRIPT pyrrolic N and 49.4% quaternary N, which is quite different from that of NH3-Fe-N-C-800. This indicate that the existence of iron species during the polymerization and calcination process of dopamine could significantly influence the resulting surface N-C composition. The Fe spectrum
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could be deconvoluted into Fe3+ 2p2/3 (710.8 eV), Fe2+ 2p2/3 (713.0 eV), Fe3+ 2p1/2 (724.6 eV), satellite peak (719.0 eV) and Fe-N (707.5 eV) which are consistent with previously reported results [33, 54]. Based on the XPS peak area calculation, the amount of Fe content is estimated to
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be 2.3 % far lower than the ICP results (22%), suggesting that abundant of iron species were
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located underneath the carbon layers.
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Fig. 3 (a) XPS survey of NH3-Fe-N-C-800 and the deconvolution of (b) N and (c) Fe.
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Fig. 4 (a) Cyclic voltammetry (CV) curves of NH3-Fe-N-C-800 in O2 or N2-saturated 0.1 M KOH
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solution, (b) hao, (c) LSVs of NH3-Fe-N-C-800 with various rotation rates in O2-saturated 0.1 M KOH solution, inset of (c) is the corresponding K-L plots (j-1 vs. w-1/2) at different potentials derived from RDE measurements, (d) RRDE voltammograms of NH3-Fe-N-C-800 in O2-saturated 0.1 M KOH solution, inset of (d) is the peroxide yield and the electron transfer number n, (e) Chronoamperometric (i–t ) responses at 0.6 V vs. RHE in O2-saturated 0.1 M KOH at 1600 rpm for NH3-Fe-N-C-800, (f ) Chronoamperometric responses at 0.6 V vs. RHE in O2-saturated 0.1 M KOH followed by addition of 3 M methanol.
ACCEPTED MANUSCRIPT Cyclic voltammetry (CV) measurements for NH3-Fe-N-C-800 in N2 or O2 saturated 0.1 M KOH solution were carried out. As the results shown in Fig. 4(a), there is a well-defined oxygen reduction peak located at 848 mV vs. RHE under the O2-saturated electrolyte for NH3-Fe-N-C-800,
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which indicates the obvious ORR catalytic activity of NH3-Fe-N-C-800. The influence of the proportion of the precursor on the catalytic performance was first evaluated. From Fig. S4 we can see that the ratio of dopamine to ammonium iron (Ⅲ) citrate at 3 is the preferred condition, and
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the following catalyst were all prepared with this optimized ratio. The electrocatalytic activity of
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the Fe-N-C catalysts prepared with different conditions were compared with Pt/C catalyst by RDE techniques in O2-saturated 0.1 M KOH solution at a scan rate of 10 mV·s-1. From Fig. 4(b), we can see that there is slight catalytic activity for the PDA calcined at 800 oC which may be derived from the nitrogen doped carbon surface. Ar-Fe-N-C-800 shows a significantly improved ORR
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catalytic activity compared with that of PDA, which highlights the importance of introducing iron species for the ORR catalytic process. Interestingly, the activity is further promoted for NH3-Fe-N-C-800 with an onset potential at 939 mV, that is very close to that of Pt/C (954 mV vs
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RHE) and the half wave potential (E1/2) is 0.869 V almost equal to that of the commercial Pt/C
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catalyst (0.827 V vs. RHE). This could be due to the higher intrinsic catalytic ability for Fe2N obtained at NH3 atmosphere than that of Fe3C catalyst produced under Ar atmosphere even though Ar-Fe-N-C-800 have much higher specific surface area of 336.2 m2/g (in Fig. S5). By evaluation of the calcination temperature at NH3 atmosphere, we found that NH3-Fe-N-C-800 still achieved the highest activity. This indicates that Fe2N phase may be more preferable in ORR than Fe4N, Fe3N and Fe2C formed at lower temperature. And on the other hand the higher graphitization of the carbon layers in the core-shell structured catalyst could promote the electron conductivity
ACCEPTED MANUSCRIPT which may contribute to the activity improvement. We further investigate the ORR kinetics for NH3-Fe-N-C-800 by recording RDE curves. Fig. 4(c) displays that the limiting current density increases with the increase of rotation rate in O2 saturated electrolytes. The corresponding K-L
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(Koutecky-Levich) plots (j-1 vs. w-1/2) as inserted in Fig. 4(c) are nearly linear and parallel, suggesting an almost 4 electron transfer number for ORR. The RRDE voltammograms of the NH3-Fe-N-C-800 was shown in Fig. 4(d), and it can be found that the disk current density was
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rather small. The peroxide yield are 0.8%-6% and the average values of the electron transfer
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number (n) are calculated to be 3.94 (insert in Fig. 4d). As the durability test shown in Fig. 4(e), NH3-Fe-N-C-800 exhibits an excellent long-term stability with negligible degradation over 6000 s. Additionally we carried out toxicity resistant ability test, as the result shown in Fig. 4(f), there is typical methanol oxidation peaks appearing for the Pt/C catalyst. In contrast, NH3-Fe-N-C showed
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no obvious change in the current density, suggesting that the NH3-Fe-N-C-800 catalyst had better tolerance to the methanol crossover effect. Furthermore, the CV curves and ORR performance of NH3-Fe-C-N-800 and Pt/C in 0.1 M HClO4 electrolyte was also evaluated as shown in Fig. S6. A
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well-developed ORR peaks was observed for the NH3-Fe-C-N-800 electrode and the onset
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potential is 0.855 V and half-wave potential is 0.728 V quite close to that of Pt/C catalyst.
4. Conclusion
We have provided an efficient preparation method to construct core-shell structured Fe-N-C catalyst by complexing of ammonia iron citrate with dopamine during its polymerization process. The catalyst crystalline phase may derive into Fe3C, Fe2C, Fe3N, Fe4N, Fe2N at different preparation temperature and atmosphere, among which the obtained graphitic carbon wrapped
ACCEPTED MANUSCRIPT Fe2N under 800 oC and NH3 atmosphere showed the best performance with close activity and superior methanol crossover resistant ability than Pt/C catalyst in alkaline electrolyte. The high intrinsic activity of Fe2N, the higher graphitization of the adjacent carbon layers, the mesoporous
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structures are the contributions to the excellent catalytic behavior making itself potent candidate to replace the Pt/C catalyst. Moreover the simple preparation process could serve as an attractive
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composite for the application in catalysis and beyond.
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universal method to complex metal catalyst with polymer to produce core-shell metal-N-C
Acknowledgements
We acknowledge the financial support from Chinese Postdoctoral Science Foundation (2016M600519), Natural Science Foundation of Shandong Province (ZR2016BB03, and
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ZR2016JL007), Qingdao Municipal Science and Technology Bureau (Grant No. 16-5-1-44-jch), the Thousand Talents Plan, the World-Class University and Discipline, the Taishan Scholar's Advantageous and Distinctive Discipline Program of Shandong Province and the world-Class
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Discipline Program of Shandong Province
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