Open Access Article
Keliang Wang*a,
Ming Xub,
Xiaomin Wanga,
Zhengrong Gu
*a,
Qi Hua Fan*c,
William Gibbonsd and
Jason Croatd
aAgricultural and Biosystems Engineering Department, South Dakota State University, Brookings, SD 57007, USA. E-mail: wangsdsu@gmail.com; zhengrong.gu@sdstate.edu
bPetroChina Lanzhou Petrochemical Company, Lanzhou, Gansu 730060, China
cDepartment of Electrical and Computer Engineering, Department of Chemical Engineering and Materials Science, Michigan State University, East Lansing, MI 48824, USA. E-mail: qfan@egr.msu.edu
dBiology and Microbiology Department, South Dakota State University, Brookings, SD 57007, USA
First published on 23rd January 2017
N incorporated carbon materials are proven to be efficient EDLCs electrode materials. In this work, aniline modified fungus served as a raw material, and N-doped porous activated carbon is prepared via an efficient KOH activation method. A porous network with a high specific surface area of 2339 m2 g−1 is displayed by the prepared carbon material, resulting in a high accessible surface area and low ion diffusion resistance which is desirable for EDLC electrode materials. In assembled EDLCs, the N–AC based electrode exhibits a specific capacitance of 218 F g−1 at a current density of 0.1 A g−1. Besides, excellent stability is displayed after 5000 continuous cycles at different current densities ranging from 0.1 to 10 A g−1. The present work reveals a promising candidate for electrode materials of EDLCs.
So far, carbon materials used for EDLCs electrodes included carbon nanotubes, activated carbon, graphene and carbon fibers.9–12 Of these materials, activated carbon is considered a promising candidate for EDLCs electrode material owing to high specific surface area (SSA), large porosity, and excellent conductivity; factors that are important for EDLCs performance. Activated carbon are typically prepared via physical or chemical activation to produce porous structure with high SSA and wide pore size distribution (micropore, mesopore, and macropores). It is believed that high SSA will provide enough contact area between the electrodes and electrolyte, while pores with different sizes will serve as ion channels and reservoirs of electrolyte to shorten the ion diffusion distance. Both of these factors contribute to capacitance performance.13 However, the capacitance performance of activated carbon based electrodes is still limited and higher specific capacitance is greatly desired.
In recent years, introducing heteroatoms (P, N and B) into activated carbon was found to be efficient to improve EDLCs performance because of the induced pseudo-capacitance via reversible redox reaction and the improved wettability.14–16 In particular, N-doped carbon materials have received considerable attention and a variety of methods were explored to introduce nitrogen. Although carbonizing biomass that contains nitrogen appeared an efficient approach to achieving N-doped carbon, low-cost N-containing biomass species are very limited and the N concentration is low after pyrolysis. Alternatively, using N-rich chemicals to modify low-cost biomass becomes more attractive to preparing N-doped porous carbon via combined pyrolytic chemical activation.
In this work, N-rich aniline was used to modify fungus and the modified raw material was subsequently activated by KOH to obtain N-doped porous carbon. The activated porous carbon exhibited high SSA and desired porosity suitable for EDLC electrode materials. The performance of supercapacitors prepared with the N-doped porous carbon is reported.
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3, in a steel crucible also containing 30 mL deionized water. The crucible was placed in an oven and dried at 110 °C for 24 h. Then, the crucible was transferred into a muffle and activated at 800 °C for 1 h with a heating rate of 10 °C min−1 under N2 protection (flow rate was 96 mL min−1). Afterwards, the carbonized solids were washed with 30 mL 0.1 mol L−1 HCl (Fisher Scientific Inc.) at 110 °C for 1 h in a 60 mL polytetrafluoroethylene (PTFE) autoclave to remove the residual KOH and impurities. Finally, the carbon solids was washed several times with deionized water until the pH stabilized at 7. The material was then dried at 105 °C overnight in an oven. The carbonized samples were denoted as N–AC. Raw fungus and dried mixture of fungus and aniline were carbonized following the same procedures of N–AC preparation but in the absence of KOH, the products were donated as C and N–C, respectively.
To evaluate the surface area and pore structure of N–AC, N2 sorption–desorption isotherm was conducted (Fig. 2a). High SSA of 2339 m2 g−1 was obtained for N–AC, which offered large contact surface area between the electrodes and electrolyte. In addition, the pore size distribution suggested that the pore sizes centered at 27 nm and 34 nm with some micropores and macropores, which would serve as reservoirs and channels for the electrolyte.13 Eventually, these features were expected to improve the capacitance. Raman spectra of C, N–C and N–AC was employed to further characterize the carbon structure. As presented in Fig. 2b, two characteristic peaks located at ∼1346 and 1580 cm−1 were revealed, which was assigned to D-band and G-band, respectively. The D-band reflected degree of disordered graphite with A1g symmetry, while G-band was associated E2g mode of sp2 carbon domains.18 Meanwhile, the intensity of ratio between D-band and G-band represented the degree of graphitization, lower value indicated higher graphitization. Same ratio value of 0.96 was obtained for all the three samples, implying that they had similar degree of graphitization, which could be attributed to the same carbonization temperature (800 °C) and process time.
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| Fig. 2 (a) N2 sorption–desorption isotherms of N–AC. The insert in (a) shows pore size distribution of N–AC; (b) Raman spectra of C, N–C and N–AC. | ||
XPS was conducted to investigate the chemical state of N–AC (Fig. 3). Deconvolution of the C 1s spectra (Fig. 3a) showed the most pronounced peak being graphite-like carbon (C–C) at 285 eV and oxygen-containing groups located at different binding energy e.g., C–O/C–OH (∼286 eV), C
O (∼287 eV), COOH (∼289 eV), and CO2/CO32− (∼291 eV).19 These surface functional groups improved the hydrophilic nature of the N–AC and resulted in easy access of the electrolyte to the internal walls of the pores. In high resolution spectrum of O 1s, three types of O species located at 531 eV, 532 eV, and 535 eV, respectively, were detected (Fig. 3b), which were associated with C
O groups (carbonyl/quinone), carbonyl oxygen atoms (phenol/ether) and oxygen atoms (carboxylic groups COOH and/or chemisorbed O2/H2O), respectively.20 This result was consistent with C 1s analysis that these functional groups could improve the wettability of N–AC electrodes and provided more accessible surface for aqueous electrolyte and eventually led to enhanced capacitance. In addition, high resolution spectrum of N 1s was deconvoluted into three peaks at ∼399, 401 and 404 eV (Fig. 3c), which could be attributed to quaternary-N, pyridinic-N and N oxides of pyridinic-N, respectively. It was reported that pseudocapacitance behavior between the ions of electrolytes and the carbon electrode surface could be induced by pyridinic-N,21 which contributed to capacitance performance.
Fig. 4 illustrates the CV curves of C (a), N–C (c) and N–AC (e) electrodes at various scanning rates ranging from 5 to 300 mV s−1 to access the specific capacitance. Distorted rectangular shapes were observed for both C and N–C electrodes, which were significantly different from a typical rectangular shape with a big loop that the N–AC electrodes exhibited. These results indicated that N–AC electrodes possessed better capacitive behavior and higher specific capacitance. In addition, almost no distortion was observed for N–AC electrodes in contrast to the C and N–C electrodes even at increased scanning rates. This result implied efficient charge transfer and electrolyte diffusion in the porous N–AC.22 Moreover, to accurately evaluate the specific capacitance, the following equation23 was used:
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Nyquist plots obtained from KPF electrodes in 6 mol L−1 KOH electrolyte are shown in Fig. 5a. Typically, the resistance (3.0 Ω) consisted of bulk electrolyte resistance (0.8 Ω), interfacial impedance and intra-particle impedance (1.0 Ω), which corresponded to x-intercept at the highest frequency region (R1), semicircle at the mid-frequency region (R2), and the spike at the low-frequency region (R3).25 Among these three types of resistance, R1 and R2 were related to the electrolyte solution, and R3 was associated with intra-particle pores. This was in consistence with the porous structure, high SSA and good conductivity.25
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| Fig. 5 (a) Nyquist plots of N–AC electrodes; (b) cycle life of N–AC electrodes in 6 mol L−1 KOH electrolyte at different current density ranging from 0.1 to 10 A g−1. | ||
Rate capability is an important feature of EDLCs. Cycle life of N–AC electrode was recorded with 6 mol L−1 KOH electrolyte at different current density ranging from 0.1 to 10 A g−1. As shown in Fig. 5b, specific capacitance of 218, 196, 192, 190 and 190 F g−1 were obtained at current density of 0.1, 0.5, 1.0, 5.0 and 10.0 A g−1 for 5000 cycles, respectively. The specific capacitance of N–AC during the cycling kept almost 100% with only a little bit fluctuation in the initial 1000 cycles, indicating excellent stability and long life time of N–AC electrode materials.
Footnote |
| † Electronic supplementary information (ESI) available. See DOI: 10.1039/c6ra27600h |
| This journal is © The Royal Society of Chemistry 2017 |