Ahmed S Abou-Elyazed1,2, Sameh Hassan3, Asmaa G Ashry1, Mohammad Hegazy1. 1. Chemistry Department, Faculty of Science, Menoufia University, Shebin El-Koom 32511, Egypt. 2. MIIT Key Laboratory of Critical Materials Technology for New Energy Conversion and Storage, School of Chemistry and Chemical Engineering, Harbin Institute of Technology, Harbin 150001, China. 3. Physics Department, Faculty of Science, Menoufia University, Shebin El-Koom 32511, Egypt.
Abstract
Activated carbon granules present in our household filters used in water purification are significant waste. Activated carbon waste (ACW) was ground to a fine powder, then impregnation of SnO2 on ACW was performed under mild conditions followed by calcination of SnO2-ACW at 700 °C for 2 h, producing a SnO2-ACW hybrid composite. This hybrid composite material was used in the preparation of electrodes for supercapacitor and capacitive deionization applications. The electrochemical performance of the electrodes was investigated by using cyclic voltammetry, galvanostatic charge-discharge, and electrochemical impedance spectroscopy. Calcination and addition of SnO2 contributed to an obtained electrode with a high specific capacitance of 30.46 F g-1 in a solution of 1 M Na2SO4 compared to the original ACW (0.122 F g-1) and calcined-ACW (1.42 F g-1) at an actual current of 1 mA. This electrode was also investigated for water desalination through the capacitive deionization technique and exhibited an electrosorption capacity of 6.44 mg/g compared to the commercial AC (8.9 mg/g) so it is a highly promising and economic electrode.
Activated carbon granules present in our household filters used in water purification are significant waste. Activated carbon waste (ACW) was ground to a fine powder, then impregnation of SnO2 on ACW was performed under mild conditions followed by calcination of SnO2-ACW at 700 °C for 2 h, producing a SnO2-ACW hybrid composite. This hybrid composite material was used in the preparation of electrodes for supercapacitor and capacitive deionization applications. The electrochemical performance of the electrodes was investigated by using cyclic voltammetry, galvanostatic charge-discharge, and electrochemical impedance spectroscopy. Calcination and addition of SnO2 contributed to an obtained electrode with a high specific capacitance of 30.46 F g-1 in a solution of 1 M Na2SO4 compared to the original ACW (0.122 F g-1) and calcined-ACW (1.42 F g-1) at an actual current of 1 mA. This electrode was also investigated for water desalination through the capacitive deionization technique and exhibited an electrosorption capacity of 6.44 mg/g compared to the commercial AC (8.9 mg/g) so it is a highly promising and economic electrode.
People
use energy in everything, and this energy comes in several
forms, some of which come in the form of heat and others in the form
of radiation. Despite the different and multiple forms of energy,
all of them can be classified under two types; either renewable energy
or non-renewable energy; and the whole world is turning to the production
of renewable energy of all kinds as an alternative to non-renewable
energy, which affects one way or another on the climate and the environment.[1,2] Therefore, renewable energies have become a pivotal part to reduce
this risk, and examples of renewable energies such as sunlight, wind,
rain, tides, and waves.[3] Therefore, devices
must be provided to store this energy until it is consumed when necessary.
The most important examples of energy storage devices are supercapacitors.[4,5]Supercapacitors are charge storage devices that received a
lot
of attention due to their high power density, excellent reversibility,
and very long cycle life. Also, they deliver higher energy density
than conventional capacitors and higher power density than batteries.[6,7] In supercapacitors, active materials are the most essential factor
in leading the electrochemical performance. In General, the electrode
materials of supercapacitors are of three types, conducting polymers,[8,9] carbon materials,[10] and transition metal
oxides.[11] Each of them has its own merits
and limitations.Recently, the researchers have made more efforts
to enhance the
merits of the above-mentioned electrode materials and break the limitations
by fabricating composites of metal oxides and carbon materials or
metal oxides and conducting polymers. Among these efforts, Thangappan
and co-workers investigated Mn–MoO4/graphene nanocomposite
displays the specific capacitance (SC) (302.08 F g–1) at 0.1 A g–1 higher than that of graphene oxide
(GO) (121.39 F g–1) and Mn–MoO4 (201.81 F g–1) in an aqueous electrolyte of Na2SO4.[12] Liu and co-workers
demonstrated a flexible and light-weight supercapacitor based on bacterial
nanocellulose incorporated with tin oxide (SnO2) nanoparticles,
GO, and poly(3,4-ethylenedioxyiophene)-poly(styrene sulfonate) (PEDOT:
PSS) with a SC of 445 F g–1 at 2 A g–1.[13]Generally, for double-layer
capacitors, carbon-based materials
are widely used as electrode materials. However, they exhibit only
low SC and lower energy density than redox-based electrode materials.
Metal oxides such as RuO2, NiO, SnO2, and MnO2 have been studied by researchers with various structures
of morphologies and the desired porosity structures as electrode materials
for supercapacitors.[14,15] Among the different metal oxides,
SnO2 has exhibited a high value of SC and high cyclic stability,
due to the highest theoretical capacity (∼782 mA h g–1), high abundance, and low cost.[16]Additionally, other metal oxides like Ni, Mn, Sn, and Co materials
have a high value in supercapacitor devices. However, the semiconducting
property of these oxides is eradicating faster charge transfer at
high current density and this attributes to reducing the rate capability.[17] To solve this problem, many researchers investigated
hybrid structures with high conductive carbon-based materials. Hence,
binary or ternary composites have been widely investigated to obtain
materials with the combined nature of properties in the balanced merit
of the three kinds of materials. In this aspect, the activated carbon
(AC) waste from household filter-based tin (VI) oxide composite is
used as electrodes in both applications of supercapacitor and capacitive
deionization (CDI).In this study, a new two-step strategy has
been followed for the
synthesis of the SnO2-ACW composite. The first step involves
the impregnation of SnO2 on AC waste under mild conditions,
followed by the calcination of the composite at 700 °C for 2
h. The SC of the prepared composite is improved with excellent cyclic
stability compared with the original AC waste. Additionally, it gives
good results close to the commercial AC in the CDI process.
Experimental
Section
Materials
Commercial AC, activated carbon waste (ACW),
Tin (IV) oxide (SnO2, 99%), sulfuric acid (H2SO4, 98%), 304-stainless steel, N-dimethylpyrrolidone,
polyvinylidene fluoride (PVDF), sodium sulfate anhydrous (Na2SO4, 99%) and distilled water. All chemicals are used
directly without any further purification.
Preparation of SnO2/ACW as an Active Material
The ACW from the house
water filter was ground and prepared in three
cases: ACW only, ACW-calcined at 700 °C for 2 h, and SnO2/ACW-calcined after the impregnation; where the SnO2 was impregnated on ACW in 50 mL glass vail for 3 h at 80 °C
and then separated as black powder by centrifugation and drying in
an oven for 2 h at 100 °C and then the powder was calcined for
2 h at 700 °C as shown in Figure .
Figure 1
Active material preparation (SnO2/ACW) for
energy storage
and CDI applications.
Active material preparation (SnO2/ACW) for
energy storage
and CDI applications.
Electrode Preparation
The 304-stainless steel current
collector was first etched using concentrated sulfuric acid 98% (3
mL) for 30 min, and then rinsed thoroughly with distilled water and
then dried. The ACW electrode was prepared as follows; ACW, ACW-calcined,
and SnO2/ACW-calcined (18 mg) as an active material, graphite
(4 mg) as a conductive material, and poly-vinylidene-fluoride (PVDF,
2 mg) as a binder were mixed in a mass ratio of 75:17:8 with 0.4 mL
of N-methyl-2-pyrrolidone as a solvent, and the mixture
was sonicated in an ultrasonic bath at room temperature for half an
hour to form a homogenous slurry. Further, the etched stainless steel
was covered homogeneously from the above slurry by using a micro-pipette
(10 μm) and then dried at 80 °C for 2 h to remove any remaining
solvent. The mass loading of the prepared electrode for energy storage
was measured utilizing a four-digit microbalance to be 9.4 mg (including
graphite and PVDF mass) using an exposed area of 4 cm2.
For CDI characterization, the CDI cell was investigated using the
above-mentioned active materials as an electrode in a circular form
with a diameter of 5.3 cm and a total active mass of 191 mg.
Capacitive
Behavior Test
The electrochemical behavior
of the prepared electrodes was registered using Sp-150 potentiostat/galvanostat
electrochemical workstation through cyclic voltammetry (CV), galvanostatic
charge–discharge (GCD), and electrochemical impedance spectroscopy
(EIS) techniques with a three-electrode system comprising a working
electrode, a reference electrode, and a counter electrode. The prepared
ACW electrode, Pt. wire, and Ag/AgCl (KCl saturated) electrode were
used as a working electrode, a counter electrode, and a reference
electrode, respectively. The CV experiments were performed at varying
scan rates from 10 to 100 mV s–1 at the range of
voltage (0–1 V). The GCD tests were recorded at actual currents
from 1 to 10 mA within a voltage window from 0 to 1 V. EIS was performed
at an alternating current amplitude of 10 mV superimposed on 10 mV
DC voltage in the frequency range from 10 MHz to 100 kHz. The data
was recorded through EC-Lab software V11.33 connected with the SP-150
potentiostat/galvanostat.The SC, expressed in F/g, extracted
from chrono-potentiometry discharge curves was calculated by using
the charge–discharge current (I), voltage
change with the time (ΔV/Δt), and total mass (m) of electrode active materials using (eq ) as followsCyclic voltammetry
gravimetric capacitance (SC), expressed in F/g,
was calculated by using the capacitive charge (Q),
obtained from the integrated area of the CV curve divided by two,
the active electrode total mass, and the width of the potential window
(V) by using (eq ).
Material Characterizations
Nitrogen
sorption experiments
were performed at −196 °C on a Quantachrome TouchWin version
1.2 Gas Sorption and Porosimetry system. The samples were regularly
arranged for examination after degassing at 150 °C under a vacuum
for 2 h until the final pressure reaches 1 × 10–3 Torr. X-ray diffraction (XRD) patterns were monitored on a Rigaku
D/Max-2550 diffractometer furnished with a SolX detector-Cu K radiation
with λ = 1.542 Å. Data were enrolled by step scanning at
2θ = 0.02° per second from 5 to 50°. Scanning electron
microscopy (SEM) images were recorded on SEM quanta FEG 250 FEI and
elemental determination from energy dispersive X-ray (EDX) was examined
on (JCM-6000PLUS) fitted with an acceleration voltage of 15 kV.
Results and Discussion
Electrode Characterization
Figure displays the XRD
patterns of ACW, ACW-calcined,
simulated SnO2, and SnO2/ACW-calcined samples.
For the ACW from the household filter (Figure a), more broad diffraction peaks emerged
corresponding to 2θ = 20.8, 26.7, 31.7, 35.4, and 39.5°
in the spectrum. The XRD analyses of the ACW revealed that it appears
in the amorphous state with low crystallinity, and the additional
peaks were attributed to the contamination with different unknown
materials. The ACW-calcined sample (Figure b), exhibits the disappearance of some diffraction
peaks due to the vaporization of some contaminated materials from
ACW after calcination at 700 °C. Also, the diffraction peak at
2θ = 25° becomes a broad peak compared to ACW owing to
the effect of calcination temperature on the particle size of ACW.
For SnO2/ACW-calcined sample (Figure d), three distinguished diffraction peaks
were observed at 2θ = 26.6, 34, and 38°, respectively.
These peaks are fitted with the standard JCPDS card of SnO2 (simulated SnO2, Figure ) to confirm the successful preparation of the SnO2/ACW composite.
Figure 2
XRD patterns of (a) ACW, (b) ACW-calcined, (c)
simulated SnO2, and (d) SnO2/ACW-calcined samples.
XRD patterns of (a) ACW, (b) ACW-calcined, (c)
simulated SnO2, and (d) SnO2/ACW-calcined samples.N2 adsorption–desorption analysis
was made to
study the pore structure, pore-volume, and the specific surface area
of the samples. N2 adsorption–desorption isotherms,
pore-volume, and pore size distribution are shown in (Figure , Table ). The isotherms can be classified as type
IV, revealing the mesoporous structure of various prepared samples.[18,19] From the adsorption branch of the isotherm, a slight increase in
the specific surface area was observed by calcination at 700 °C
(the specific surface for ACW, ACW-calcined, and SnO2/ACW-calcined
samples were found to be 50.05, 56.89, and 56.45 m2 g–1, respectively). Table indicates that the pore volume of ACW-calcined and
SnO2/ACW-calcined samples exhibits wide pore volume compared
to ACW sample, and the pore size distribution confirms the existence
of mesopores and macropores[20] as shown
in Figure (inserted
Figure).
Figure 3
Adsorption–desorption isotherm and pore size distribution
(inserted Figure) of various investigated samples.
Table 1
Texture Properties of Different Samples
sample type
BET surface area (m2/g)
Langmuir
surface area (m2/g)
pore volume (cm3/g)
pore size distribution (nm)
ACW
50.05
97.54
0.16
2.25–5.69
ACW-calcined
56.89
103.2
0.2
2.27–5.67
SnO2/ACW-calcined
56.45
101.5
0.19
1.67–1.69
Adsorption–desorption isotherm and pore size distribution
(inserted Figure) of various investigated samples.The morphology of ACW, ACW-calcined,
and SnO2/ACW-calcined
samples was studied by SEM. Figure a shows the SEM image of ACW, it had irregular morphology
with a size around 100–150 nm. After calcination at 700 °C
for 2 h, the morphology changes to become a rod-like shape as shown
in Figure b. In a
close observation of the SnO2/ACW-calcined SEM image (Figure c), it was concluded
that the particles of SnO2 were decorated on the ACW. Additionally,
the EDX of the SnO2/ACW-calcined sample (Figure d) refers to the atomic content
of Sn in the prepared sample after calcination.
Figure 4
SEM images of (a) ACW,
(b) ACW-calcined, (c) SnO2/ACW-calcined
samples, and (d) EDX of SnO2/ACW-calcined sample. Electrochemical
behavior of the electrodes.
SEM images of (a) ACW,
(b) ACW-calcined, (c) SnO2/ACW-calcined
samples, and (d) EDX of SnO2/ACW-calcined sample. Electrochemical
behavior of the electrodes.The electrochemical performance of the electrodes was investigated
in a three-electrode configuration in 1 M Na2SO4 electrolyte using CV, GCD, and EIS. Practically, the presence of
SnO2 particles in the electrode of ACW resulted in a higher
SC as compared to the original ACW as discussed below.
Cyclic Voltammetry
Figure a shows
the common CV technique for the prepared
ACW electrodes in the three cases in the potential window from 0 to
1 V at a scan rate of 10 mV/s in 1 M Na2SO4 electrolyte.
The SC (as represented by the integrated area in the CV curve) of
SnO2/ACW- calcined (26.75 F g–1) is significantly
higher than that of ACW and ACW- calcined (0.48, 2.08 F g–1) respectively, due to highly reversible faradaic redox processes
associated with SnO2 which was impregnated on the ACW support
as confirmed by XRD and EDX. Also, the rectangular CV curve with an
ideal double-layer behavior suggests a fast charge transfer rate even
at high scan rates as shown in Figure b. The calculated SCs at different scan rates were
given in Figure c
in the common behavior of decreasing the SC with the scan rate. To
ensure the capacitive behavior of the SnO2/ACW-calcined
electrode, two electrodes were prepared as only SnO2 and
SnO2/ACW without calcination and compared with the SnO2/ACW-calcined electrode. As seen, the SnO2/ACW-calcined
electrode still has the larger integrated surface area giving higher
capacitance which arises the effect of calcination on the SnO2/ACW composite material.
Figure 5
(a) CV curves at a scan rate of 10 mV
s–1 for
the prepared ACW electrode in all cases, (b) CV curves of SnO2/ACW-calcined electrode at different scan rates, (c) calculated
SC for all investigated electrodes at different scan rates, and (d)
CV curves for SnO2, SnO2/ACW-non calcined, and
SnO2/ACW-calcined electrode at a scan rate of 10 mV s–1.
(a) CV curves at a scan rate of 10 mV
s–1 for
the prepared ACW electrode in all cases, (b) CV curves of SnO2/ACW-calcined electrode at different scan rates, (c) calculated
SC for all investigated electrodes at different scan rates, and (d)
CV curves for SnO2, SnO2/ACW-non calcined, and
SnO2/ACW-calcined electrode at a scan rate of 10 mV s–1.
Galvanostatic Charge–Discharge
The capacitive
performance of the prepared ACW electrodes in the three forms was
also investigated through the GCD technique using 1 M Na2SO4 electrolyte at actual currents from 1–10 mA
with a potential window between 0 and 1 V Figure a shows the GCD at 1 mA for the SnO2/ACW- calcined, ACW, and ACW- calcined. The voltage (ohmic) drop
of SnO2/ACW-calcined electrode is very small compared with
ACW and ACW- calcined indicating low DC internal resistance.[13,21] Also, the slow discharge time of the calcined SnO2/ACW
electrode expresses its high capacitance. Figure b indicates the calculated specific capacitance
(Csp) variation with the actual charge–discharge
current investigated in Na2SO4 electrolyte for
the prepared electrodes in the three forms. Upon increasing the current,
the SC decreases, which is a common behavior. The highest obtained
SCs from the GCD curve were 0.122, 1.42, and 30.46 F g–1 at an actual current of 1 mA for ACW-based electrodes investigated
in 1 M Na2SO4 electrolyte with three cases:
ACW, calcined ACW, and calcined SnO2/ACW, respectively.
The longevity and stability of the calcined SnO2/ACW electrode
were evaluated using the GCD technique for 6000 cycles at a current
of 10 mA (Figure c).
The electrode retains 108.9% of its initial capacitance over 6000
charge–discharge cycles, indicating this composite electrode
is a promising candidate for supercapacitor devices.
Figure 6
(a) CD curves at an actual
current of 1 mA for the prepared ACW
electrodes, (b) calculated SC for all investigated electrodes at different
currents, and (c) the stability measurement at 10 mA for the SnO2/ACW-calcined electrode.
(a) CD curves at an actual
current of 1 mA for the prepared ACW
electrodes, (b) calculated SC for all investigated electrodes at different
currents, and (c) the stability measurement at 10 mA for the SnO2/ACW-calcined electrode.
Electrochemical Impedance Spectroscopy
Figure shows the obtained results
of the EIS measurements, recorded in the frequency range of 10 mHz–100
kHz, applying 10 mV amplitude at room temperature using 1 M Na2SO4 electrolyte.
Figure 7
Nyquist plot of the ACW electrodes in
three forms investigated
in 1 M Na2SO4 electrolyte. The inset represents
the zoom-in view of the Nyquist plot.
Nyquist plot of the ACW electrodes in
three forms investigated
in 1 M Na2SO4 electrolyte. The inset represents
the zoom-in view of the Nyquist plot.The observed plot shows different behaviors in the applied frequency
range through the existence of a semi-circle in the high-frequency
region and a straight line in the low-frequency region, indicating
both the resistive and capacitive behaviors of the investigated electrode.
The initial intercept of the semi-circle at the beginning with the
real impedance axis at high frequency corresponds to the equivalent
series resistance (ESR), which includes the ionic resistance of the
electrolyte, interface resistance of the active material, the resistance
of the current collector, and the contact resistance at electrode/electrolyte
interface. The high-frequency intercept is followed by a semicircle
due to the presence of resistance at the electrode–electrolyte
interface and corresponds to the charge transfer resistance (Rct) that includes interfacial reaction kinetics.
The electrode possibly blocks the electron exchange of the faradic
process at the electrode/electrolyte interface. The value of Rct can be derived from the diameter of the semicircle.[22]The calculated ESR values were 2.89, 2.66,
and 3.13 Ω for
the developed electrodes in the three cases: ACW only, ACW-calcined,
and SnO2/ACW-calcined, respectively. The result reflects
a slight decrease in resistance after calcination of ACW due to larger
pore volume and surface area of calcined particles resulting in fast
ion diffusion, and then the resistance increased after the addition
of SnO2. However, the values still reflect the high power
density of the prepared electrodes. Also, the Rct values followed the same trend with values of 5.51, 4.24,
and 5.62 Ω. The pore structure variation in the smaller range
of 1.67–1.69 nm with SnO2-ACW electrode (as indicated
in Table ) leads to
a more accessible surface area which results in a higher SC.
Capacitive
Deionization Performance Evaluation
To investigate
the electrosorption capacity of the prepared ACW electrodes, a CDI
cell was manufactured and the prepared electrodes were inserted between
the cell plates without a separator between them. Figure shows the change in the total
dissolved solids (TDS) with time during adsorption and desorption
for the CDI cell using the calcined ACW and SnO2/ACW- calcined
as compared with the commercial activated carbon. As seen, except
for calcined ACW, the TDS decreases rapidly with time during the voltage
application where ions were quickly adsorbed on the electrode surface.
For the calcined SnO2/ACW, NaCl electrolyte concentration
decreased from the initial value of 870 ppm to a minimum of 828 ppm
within 619 s at a desalination rate of 0.066 ppm/s. When all the accessible
surface area was reached by the adsorbed ions, the electrosorption
capacity of the CDI cell achieved the maximum value of 6.44 mg/g,
and the salt removal efficiency reached 4.82% with the minimum concentration
of NaCl solution. While in the case of commercial AC electrode cell,
NaCl electrolyte concentration decreased from the initial value of
870 ppm to a minimum of 815 ppm within 447 s at a desalination rate
of 0.127 ppm/s. The electrosorption capacity of the CDI cell achieved
the maximum value of 8.93 mg/g, and the salt removal efficiency reached
6.52% with the minimum concentration of NaCl solution.
Figure 8
Variation of the TDS
of NaCl solution with time during adsorption
and desorption for the CDI cell electrodes.
Variation of the TDS
of NaCl solution with time during adsorption
and desorption for the CDI cell electrodes.
Conclusion
In conclusion, a facile, abundant, and low-cost
electrode was prepared
from activated carbon waste and SnO2 by impregnation method
followed by calcination at 700 °C for the supercapacitor device.
The energy storage performance of the electrodes exhibited a significant
improvement with the incorporation of SnO2 compared to
the original ACW. The electrode exhibits excellent electrochemical
performance with a specific capacitance of 30.46 F g-1 in an aqueous solution of 1 M Na2SO4 at the
actual current of 1 mA. The stability of the calcined SnO2/ACW electrode was evaluated by obtaining GCD curves, and 108.9 %
of its original capacitance was retained after 6000 cycles at the
actual current of 10 mA. Also, this electrode with good capacitive
behavior was investigated for capacitive deionization for water desalination
giving a reasonable electrosorption capacity of 6.44 mg/g as compared
with that of the commercial activated carbon (8.93 mg/g) with a promising
adsorption and desorption behavior.