Yaxin Wang1, Huimin Wang1, Shuyuan Li1, Shaorui Sun1. 1. Beijing Key Laboratory for Green Catalysis and Separation, The Faculty of Environment and Life, Beijing University of Technology, Beijing 100124, PR China.
Abstract
Recycling waste PET plastics into metal-organic frameworks is conducive to both pollution alleviation and sustainable economic development. Herein, we have utilized waste PET plastic to synthesize CoNi-MOF applied to lithium battery anode materials via a low-temperature solvothermal method for the first time. The preparation process is effortless, and the sources' conversion rate can reach almost 100%. In addition, the anode performance of MOFs with various Co/Ni mole ratios was investigated. The as-synthesized Co0.8Ni-MOF exhibits excellent crystallinity, purity, and electrochemical performance. The initial discharge and charge capacities are 2496 and 1729 mAh g-1, respectively. Even after 200 cycles, the Co0.8Ni-MOF electrode can exhibit a high Coulombic efficiency of over 99%. Consequently, given the environmental and economic benefits, the Co0.8Ni-MOF derived from waste PET plastic is thought to be an appealing anode material for lithium-ion batteries.
Recycling waste PET plastics into metal-organic frameworks is conducive to both pollution alleviation and sustainable economic development. Herein, we have utilized waste PET plastic to synthesize CoNi-MOF applied to lithium battery anode materials via a low-temperature solvothermal method for the first time. The preparation process is effortless, and the sources' conversion rate can reach almost 100%. In addition, the anode performance of MOFs with various Co/Ni mole ratios was investigated. The as-synthesized Co0.8Ni-MOF exhibits excellent crystallinity, purity, and electrochemical performance. The initial discharge and charge capacities are 2496 and 1729 mAh g-1, respectively. Even after 200 cycles, the Co0.8Ni-MOF electrode can exhibit a high Coulombic efficiency of over 99%. Consequently, given the environmental and economic benefits, the Co0.8Ni-MOF derived from waste PET plastic is thought to be an appealing anode material for lithium-ion batteries.
Environmental and energy issues are the
two most serious problems
of the 21st century.[1−3] Nowadays, demand for energy conversion and storage
is increasing as a result of severe environmental pollution caused
by the widespread use of fossil fuels and the need to power millions
of portable electronics and electric vehicles. The rational use of
clean and renewable energy and the development of sustainable energy
storage systems (EES) have emerged as global goals for addressing
energy and environmental crises.[4−9] Among various energy storage equipment, lithium-ion batteries (LIBs)
are the first to be considered owing to qualities such as high energy
density, long cycle life, low self-discharge, and environmental friendliness.[10−12] However, commercially available graphitic anodes in LIBs with limited
theoretical capacity (370 mAh g–1) cannot meet the
ever-increasing demands for high energy densities in electric vehicles
and grid-scale energy storage systems.[13−16] As a result, the key to achieving
high-energy LIBs is to look for promising anode candidates to replace
conventional graphite.Metal–organic frameworks (MOFs)
have appeared as a burgeoning
class of porous material consisting of metal nodes and organic linkers.[17,18] Since the synthesis of the first MOFs by Yaghi and Li in the 1990s,[19] they have attracted considerable attention in
recent decades due to their intriguing structural diversity and a
wide range of potential applications, such as catalysis,[20,21] gas storage and separation,[22,23] sensing,[24,25] drug delivery,[26,27] and a variety of other areas.
Recently, many researchers have concentrated their efforts on the
design and synthesis of MOFs for clean energy applications such as
fuel cells,[28] lithium-ion rechargeable
batteries,[10] supercapacitors,[29] and solar cells.[30] In 2009, Tarascon et al. first demonstrated that MOFs (MIL-53 (Fe))
were used as anode materials for lithium storage via a conversion
reaction.[31] Since then, because of their
structural diversity, customizable redox characteristics, simple synthesis
procedures, and low cost, MOFs have emerged as novel electrode materials
with significant potential in lithium-ion batteries.[10,32−34] Meanwhile, with regard to MOFs, the metal center
has a significant impact on the electrode’s lithium storage
behavior.[35] Co-based MOFs have been widely
used as electrode materials for advanced energy storage applications
due to their availability and ease of electron transfer between multiple
oxidation states ranging from +1 to +4 during conversion reactions.
However, most Co-based MOFs have low conductivity, and this problem
has been addressed by incorporating insoluble conductive additives
and combining MOFs with conductive matrices (e.g., carbon nanotubes,
reduced graphene oxide, conductive polymers, etc.). Additionally,
the synthesis of multi-metallic MOFs is also a great alternative for
intensifying electronic conductivity. Doping metal ions such as lightweight
Li, Mg, Al, Ni, and Mn into Co-based MOFs could help to conserve cobalt
resources while also effectively facilitating electronic coupling
between metal nodes to improve material conductivity.[32,36,37] Hu et al. reported a novel bimetallic
ZnCo-MOF, and using soft X-ray absorption spectra (sXAS), they demonstrated
that bimetallic MOFs could significantly improve electrode performance
due to the synergistic effect of Zn2+ and Co2+.[38] Additionally, Zhou et al. reported
a 2D BP/NiCo MOF via a simple solution reaction route at room temperature
using Ni2+, Co2+, and benzene dicarboxylic acid
(BDC) as precursors, which demonstrated high reversible capacity and
excellent cycling durability as an anode in LIBs.[39] Although tremendous progress has been made in the development
of MOF-based lithium electrode materials, there are still many challenges
that hinder the practical application of these materials. First, many
of the complex organic ligands used in the synthesis of MOFs are expensive
and may require a degree of processing complexity. Therefore, large-scale
production of MOF materials at a reasonable cost is critical for making
them economically viable for industrial applications.As an
important ligand, 1,4-benzenedicarboxylic acid (BDC) has
been used to design many MOF system structures.[21] More importantly, it is abundant as a starting material
from the recycling of polyethylene terephthalate and the metabolites
of aromatic hydrocarbon oxidation.[40] Poly(ethylene
terephthalate) (PET) is widely used in packaging and textiles due
to its good mechanical properties, low permeability to moisture and
gas, and high heat resistance.[40−43] According to statistics, global PET consumption has
surpassed 24 million tons (62.8 billion bottles) per year and is continuing
to rise. Because of its poor biodegradability, the current common
practice of PET waste land filling has caused serious environmental
problems. As a result, the innovative use of BDC derived from waste
PET for MOF synthesis will not only improve the economics of MOF fabrication
but will also reduce the environmental threat associated with waste
PET landfilling, ultimately creating a high-value end-use market for
PET waste.[44−46]Herein, we concentrate on a simple and integrated
approach to addressing
the environmental concern associated with waste PET bottles by recycling
them into promising lithium anode materials in the form of CoNi-MOF.
Moreover, we also reported the solvothermal synthesis of CoNi-MOF
with various Co/Ni ratios (the molar ratios of Co/Ni are 0.5:1, 0.8:1,
and 1:1) to select the optimal MOF as the LIB anode material. Among
them, the as-synthesized Co0.8Ni-MOF exhibits excellent
crystallinity, purity, and electrochemical performance with superior
cyclic stability. To the best of our knowledge, there is no literature
report that efficiently recycles waste PET into CoNi-MOF as an anode
for LIBs. Thus, it is firmly believed that the waste PET plastic-derived
Co0.8Ni-MOF has great potential as an electrode material
and would be beneficial to the mitigation of global warming as well
as the circular construction of the economy.
Experimental Section
Chemicals
and Regents
Cobaltous chloride hexahydrate
(CoCl2·6H2O, 99.5%), terephthalic acid
(BDC, 98%), and nickel chloride hexahydrate (NiCl2·6H2O, 95%) were bought from Sinopharm. Ethylene glycol (EG, 99.8%),
ethanol (95%), and N,N-dimethylformamide
(DMF, 99.8%) were purchased from Aladdin. No further purification
was performed on any of the reagents. The raw material was clear mineral
water bottles (PET plastics) collected from domestic waste. All of
the experiments in this work were conducted using deionized water.
Synthesis of BDC
The process schematic for the synthesis
of terephthalic acid derived from PET according to reference is illustrated
in Scheme S1.[47] Briefly, the clear mineral water bottles’ labels and caps
were removed, and the bottles were cut into small pieces. The small
flakes were washed with water and soap before being dried in an oven
at 60 °C overnight. Then, the PET hydrolysis experiment was carried
out in a stainless-steel autoclave lined with Teflon. PET flakes (2.5
g) were placed in the autoclave along with 5 mL of ethylene glycol
(EG) and 50 mL of H2O, and the reactor was heated to 210
°C and kept there for 8 h. After the reaction, the product was
centrifuged, washed twice with ethanol, and dried at 80 °C for
12 h.
Synthesis of CoNi-MOF
As shown in Scheme , the CoNi-MOF was synthesized
via solvothermal methods in a Teflon-lined high-pressure reactor.
First, 10 mL of DMF, 10 mL of ethanol, and 10 mL of deionized water
were combined in a beaker. Second, 7.2 mmol of BDC (the metal’s
molar ratio to BDC is 1.05) was added to the above mixture, and the
solution was sonicated for 15 min to achieve a uniform suspension.
Third, 3.02 mmol of NiCl2·6H2O and 3.78
mmol of CoCl2·6H2O were added to the solution
and sonicated for 15 min until completely dissolved. Then, the above
solution was transferred into a 50 mL Teflon-lined stainless steel
autoclave and heated at 150 °C for 24 h. Finally, the product
was obtained via centrifugation, washed with DMF and ethanol five
times, and then dried in a vacuum oven overnight at 60 °C. In
comparison, CoNi-MOF materials (Co0.5Ni-MOF and Co1.0Ni-MOF) were, respectively, synthesized by adding different
Co/Ni molar ratios (such as 0.5:1 and 1:1) to the solution.
Scheme 1
(a) Preparation
Process of CoNi-MOF. (b) Working Principle of the
CoNi-MOF/Li Half-Cell. (c) CoNi-MOF with Possible Interaction of Li+ Ions
Material Characterization
X-ray powder diffraction
(XRD) measurements were taken using a PAN analytical X-ray diffractometer
(Cu Kα source, λ = 1.54178 Å). X-ray Rietveld refinement
was performed with the FullProf Software package. The scanning electron
microscopy images were obtained via a Carl Zeiss Ultrafield-emission
scanning electron microscopy (FESEM) unit equipped with energy-dispersive
spectroscopy (EDS). The materials’ morphology and microstructure
were examined further using transmission electron microscopy (TEM;
JEOL-JEM-2100F). Fourier transform infrared spectroscopy (FTIR) was
performed with a PerkinElmer (Spectrum 2) spectrophotometer at a resolution
of 4 cm–1 in the scanning range of 400–4000
cm–1. The thermal stabilities of the samples were
determined using the TA Instruments SDT650 thermogravimetric analysis
(TGA) method. N2 adsorption–desorption studies were
performed using the Brunauer–Emmett–Teller (BET) method
via a Quantachrome Nova 2000e BET analyzer. The Co/Ni ratio in the
CoNi-MOF was analyzed by inductively coupled plasma-atomic emission
spectrometry (ICP-AES) using IRIS Intrepid II XSP (Thermo Fisher Scientific).
X-ray photoelectron spectroscopy (XPS) spectra were obtained using
a Thermo Fisher Scientific ESCALAB250Xi spectrometer. 1H NMR and 13C NMR spectra were provided via a Bruker spectrometer
(MSL 400).
Electrochemical Measurements
Electrochemical
tests
were performed on coin-type cells (size: 2025), which were made up
of a working electrode and a lithium foil counter electrode separated
by a Celgard 2400 microporous membrane. The active materials, carbon
black (super P) and poly vinylidene difluoride (PVDF), were dissolved
in N-methyl pyrrolidinone (NMP) in a weight ratio
of 7:2:1. The resulting slurry was cast on Cu foil and dried in a
vacuum at 100 °C for 10 h. The cell assembly was carried out
in a glove box filled with argon (H2O, O2 <
0.5 ppm). The electrolyte used was 1 M LiPF6 in a 1:1 volume
ratio of ethylene carbonate (EC) and dimethyl carbonate (DMC). The
cells were galvanostatically charged and discharged at different rates
using multichannel Neware battery testing equipment in a voltage cutoff
range of 0.01–3 V for cycle and rate performance. An electrochemical
workstation (CHI 660a) was used to do CV measurements at a scan rate
of 0.2 mV s–1. Electrochemical impedance spectra
(EIS) were also measured in the frequency range of 105 to
10–2 Hz on a CHI 660a electrochemical workstation.
Results and Discussion
Characterization of PET-Derived BDC
The XRD patterns
(Figure a) ensure
that the peaks of PET-derived BDC are positioned at 2θ = 17.4,
25.3, and 28°, which are characteristically identical to the
commercial sample and reported literature.[48] From Figure b, both
FTIR spectra show the same characteristic peaks. Aromatic ring characteristic
peaks are observed at 730 and 689 cm–1, which are
assigned to ringing-and-out-of-plane bending vibrations of aromatic
rings,[49] whereas the peaks for carboxylic
groups are located at 1288, 1420, 1689, 2542, and 2657 cm–1. The band at 1689 cm–1 denotes the C=O
stretching vibration of carbonyl groups, and the peak at 1288 cm–1 is attributed to the C–O symmetric stretching,
as per characteristic IR absorption frequencies of organic functional
groups. This indicates that the obtained product was indeed BDC, as
evidenced by the spectrum’s similarity to commercial BDC. The
FESEM analysis (Figure c,d) reveals that both PET-derived BDC and commercially available
BDC have a similar morphology. The1H NMR and 13C NMR spectra of the PET-derived BDC shown in Figure S1 confirm that the product does not require purification.
The PET-derived BDC also exhibits an identical TGA curve to the commercial
BDC (Figure S2).
Figure 1
(a) XRD patterns, (b)
FTIR infrared spectra, and SEM images (c,
d) of the PET-derived BDC and commercial BDC.
(a) XRD patterns, (b)
FTIR infrared spectra, and SEM images (c,
d) of the PET-derived BDC and commercial BDC.
Characterization of CoNi-MOF
The crystallinity, phase
analysis, and structural properties of MOF samples prepared at different
molar ratios of Co/Ni were examined by powder X-ray diffraction (XRD),
as shown in Figure a and Figure S3. All the CoNi-MOF XRD
patterns are isostructural to the previously reported Ni-based MOFs
(no. 985792).[50] Therefore, the atomic arrangement
inside CoNi-MOF can be successfully defined (Figure S4 and Table S1). Four sharp peaks appearing at 2θ =
9.219, 14.302, 15.959, and 18.161° and matching well with the
relevant crystal faces are (200), (001), (201), and (−201),
respectively, indicating the formation of pure products. Furthermore,
as the Co/Ni molar ratio increases from 0.5 to 1.0, the characteristic
peak intensity is enhanced. This can be attributed to the crystalline
enhancement and size growth of CoNi-MOF,[51] which will be discussed in the following. All the XRD patterns indicate
that these frameworks have similar structures, as shown in Figure b. Six O atoms coordinate
both the Co and Ni atoms, and these pseudo octahedra are further edge/corner-connected
with each other in the (200) crystallographic plane along the [010]/[001]
direction to form 2D bimetal layers separated by BDC molecules.[52] Furthermore, Figure c displays the FTIR spectra of all samples
of CoNi-MOF synthesized from PET. It can be seen that there is a wide
band at 3580–3400 cm–1, indicating the presence
of hydroxyl and water molecules,[53] and
for comparison, the corresponding FTIR spectrum for 1,4-H2BDC is also shown. The reaction of 1,4-H2BDC with Co2+ and Ni2+ results in complete deprotonation by
the disappearance of the nonionized carboxyl group’s characteristic
bands (vC=O, 1684 cm–1).
New bands can be observed in the regions of 1672–1508 cm–1 ascribed to carboxylate group asymmetric stretching
vibrations, whereas bands in the 1444–1375 cm–1 range can be attributed to symmetric stretching.[54] These new bands suggest that the Co2+ and Ni2+ ions have successfully interacted with the 1,4-H2BDC ligands. The TGA analysis determined the thermostability of all
CoNi-MOF samples in a temperature range of 25–800 °C (Figure d and Figure S5). All samples exhibit good thermal
stability and still maintain their structural integrity at a temperature
of 375 °C. There is a significant decrease at around 375–525
°C, which is due to the thermal degradation of MOF.[51] In the case of Co0.8Ni-MOF, at temperatures
ranging from 25 to 350 °C, an initial weight loss of 10% was
observed due to the release of DMF and ethanol molecules. The next
weight loss of approximately 54% may result from the decomposition
of the main skeleton of Co0.8Ni-MOF and the gasification
of ligands at temperatures ranging from 425 to 525 °C. The residual
mass of the product after a complete pyrolysis reduction at 525 °C
was 36%.
Figure 2
(a) PXRD patterns, (b) crystal structure of CoNi-MOF, (c) FTIR
infrared spectra of CoNi-MOF synthesized from PET-derived BDC, and
(d) TGA curves of Co0.8Ni-MOF.
(a) PXRD patterns, (b) crystal structure of CoNi-MOF, (c) FTIR
infrared spectra of CoNi-MOF synthesized from PET-derived BDC, and
(d) TGA curves of Co0.8Ni-MOF.The morphologies of MOFs synthesized at different
Co/Ni molar ratios
were analyzed by SEM at different magnifications, as presented in Figure a,b and Figure S6. The Co0.8Ni-MOF has a micrometer-sized
dandelion-like morphology composed of bulks with a length of 6–10
μm, as shown in Figure a,b. The assembled bulk-like framework of the Co0.8Ni-MOF can also be apparently observed in the TEM image in Figure c, which could lead
to improved electrolyte accessibility by forming an ion-buffering
reservoir and thus shortening the Li+ diffusion length
to the interior surfaces.[55] Furthermore,
the HRTEM image in Figure d shows very clear crystalline planes with d-spacings of 1.115
nm, which can be ascribed to the (200) planes of Co0.8Ni-MOF.
The chemical composition of Co0.8Ni-MOF was also investigated
using energy-dispersive spectroscopy (EDS), as presented in Figure f–i. The EDS
pattern of the Co0.8Ni-MOF shows that the elements C, O,
Co, and Ni are uniformly distributed throughout the sample, indicating
that the Co0.8Ni-MOF was successfully formed. Figure S6 also includes SEM images of the Co0.5Ni-MOF and Co1.0Ni-MOF samples. The morphology
of the MOF samples changes from bowknot-like (Figure S6a) to dandelion-like (Figure a) and then to flower-like (Figure S6c). When the molar ratio of Co/Ni is 0.5:1, as shown
in Figure S6b, relatively small bulk structures
are formed first, and then, with the increase in Co/Ni molar ratio,
the smaller bulks gradually develop into larger bulks. Figures S7 and S8 represent the SEM–EDX
mapping images of Co0.5Ni-MOF and Co1.0Ni-MOF,
respectively, which also clearly support that, in the sample, all
elements are distributed uniformly. Inductively coupled plasma-atomic
emission spectrometry (ICP-AES) elemental analysis demonstrated that
the atomic ratios of Co/Ni in CoxNi-MOF (x = 0.5, 0.8, and 1.0) are calculated to be 0.46, 0.75,
and 0.96, respectively (Figure S9 and Table S2). These observations are in accordance with the molar ratios of
the initial feeding materials, further revealing the successful preparation
of the CoxNi-MOF.
Figure 3
(a, b) SEM images, (c, e) TEM images,
and (d) HRTEM image of Co0.8Ni-MOF; (f–i) TEM-EDS
mapping images of Co0.8Ni-MOF: (f) C, (g) O, (h) Co, and
(i) Ni elements.
(a, b) SEM images, (c, e) TEM images,
and (d) HRTEM image of Co0.8Ni-MOF; (f–i) TEM-EDS
mapping images of Co0.8Ni-MOF: (f) C, (g) O, (h) Co, and
(i) Ni elements.As shown in Figure , the XPS technique
was used to investigate the chemical composition
and oxidation states of Co0.8Ni-MOF. Figure a indicates the existence of Ni, Co, C, and
O elements. The high-resolution Ni 2p spectra (Figure b) display two primary peaks centered at
856.3 and 874.0 eV, respectively, which are ascribed to Ni 2p3/2 and Ni 2p1/2, as well as two matching satellite
peaks positioned at 861.4 and 879.6 eV, demonstrating the presence
of Ni2+ in the Co0.8Ni-MOF.[35] Further, the high-resolution Co 2p XPS spectrum of the
as-synthesized Co0.8Ni-MOF can also be seen in Figure c. Two distinct peaks
appear at binding energies of 781.54 eV for Co 2p3/2 and
797.49 eV for Co 2p1/2, with two pronounced satellite peaks
(786.44 and 803.11 eV, respectively) beside them, illustrating that
Co ions are predominantly in the Co2+ state.[33] Notably, the coexisting Ni2+ and
Co2+ cations in the Co0.8Ni-MOF supply multiple
active sites for lithium storage. In addition, C=C, C–C,
and O=C–O are attributed to three peaks (Figure d) centered at 284.5, 285.3,
and 288.5 eV, respectively. The O 1s spectrum (Figure e) could be separated into two peaks, positioned
at 531.5 and 532.6 eV, respectively, owing to hydroxyl and chemisorbed
water. Finally, by using the XPS technique, the atomic content ratio
of Co and Ni in the Co0.8Ni-MOF could be identified to
be 0.72:1.
Figure 4
(a) Wide-range XPS spectrum of Co0.8Ni-MOF. (b) XPS
survey spectrum of Ni 2p and the corresponding XPS spectra of (c)
Co 2p, (d) C 1s, and (e) O 1s.
(a) Wide-range XPS spectrum of Co0.8Ni-MOF. (b) XPS
survey spectrum of Ni 2p and the corresponding XPS spectra of (c)
Co 2p, (d) C 1s, and (e) O 1s.Figure and Figure S10 present the N2 adsorption–desorption
isotherms and the corresponding Barrett–Joyner–Halenda
(BJH) pore size distribution profiles of the CoNi-MOF. The results
are summarized in Table S3. All of the
CoNi-MOF samples exhibit a typical type-II sorption isotherm with
an H4-type hysteresis loop, indicating that they are mesoporous.
As depicted in Figure , the as-calculated Brunauer–Emmett–Teller (BET) specific
surface area and total pore volume for Co0.8Ni-MOF are
13.688 and 0.055 cm3 g–1, respectively,
demonstrating that the Co0.8Ni-MOF has low porosity. Furthermore,
previous research has also reported MOFs with low porosity.[39,56] The ultrahigh specific surface of the electrode materials frequently
results in superfluous side reactions with the electrolyte, particularly
at low potentials (vs Li/Li+), causing the LIB’s
performance to deteriorate.[55] As a result,
the as-synthesized low CoNi-MOF’s BET specific surface area
may be advantageous.
Figure 5
N2 adsorption–desorption isotherm of
Co0.8Ni-MOF. The inset shows the BJH pore size distribution
curve.
N2 adsorption–desorption isotherm of
Co0.8Ni-MOF. The inset shows the BJH pore size distribution
curve.To assess the electrochemical
performance of the Co0.8Ni-MOF as-prepared for Li-ion storage,
the first three successive CV scans of Co0.8Ni-MOF at a
scan rate of 0.2 mV s–1 in the potential range of
0.01–3.0 V vs Li/Li+ are shown in Figure a. The initial cathodic scan
illustrates two distinct cathodic peaks at 0.625 and 0.95 V, which
belong to the Li-ion intercalation Co0.8Ni-MOF. A sloppy
peak at 1.05 V (lithiation) disappears in the subsequent scans, which
is attributed to the establishment of the SEI layer at the electrode/electrolyte
interface.[57] The anodic peaks at 0.825
and 1.25 V are caused by the delithiation reaction of Co0.8Ni-MOF. In the following successive cycles, the weak peaks at 0.615
and 1.15 V may be related to the reversible insertion and deintercalation
of Li ions into the benzene ring and carboxylic acid groups of the
Co0.8Ni-MOF framework.[49] After
the first electrochemical cycle, the CV curves of subsequent cycles
almost overlap, indicating good cycling stability and reversibility
of Co0.8Ni-MOF. The galvanostatic charge/discharge profiles
of the Co0.8Ni-MOF for various cycles within the potential
window of 3.0–0.01 V vs Li/Li+ and at a current
density of 0.5 A g–1 are shown in Figure b. The initial discharge and
charge capacities are 2496 and 1729 mAh g–1, respectively,
corresponding to a Coulombic efficiency (CE) of 69.27%, indicating
a significant initial irreversible reaction caused by the formation
of an SEI (surface electrolyte interface) film on the electrode surface
and electrolyte decomposition.[59] During
the first discharge process, three plateaus can be seen around 1.25,
0.95, and 0.55 V, which are consistent with the CV results mentioned
above, suggesting the same Li+ ion insertion mechanisms.
Although there is a decrease in reversible capacity values for the
first few cycles, a nearly invariable capacity of 1419 mAh g–1 is obtained in the following cycles. Moreover, the charge–discharge
curves of Co0.8Ni-MOF are comparable from the 100th to
the 200th cycle, which demonstrates its stable electrochemical performance
during continuous intercalation and deintercalation of Li ions. Furthermore, Figure S11 shows that the galvanostatic discharge
and charge profiles of Co0.5Ni-MOF and Co1.0Ni-MOF are similar for Co0.8Ni-MOF under 500 mA g–1 in the first cycling processes, indicating that the
same redox reactions are occurring during the electrochemical processes.
It was also found that both Co0.5Ni-MOF and Co1.0Ni-MOF presented smaller discharge (charge) capacities than Co0.8Ni-MOF. The discharge (charge) capacities of Co0.5Ni-MOF and Co1.0Ni-MOF are 1768 (1056) and 2036 (1254)
mAh g–1, resulting in Coulombic efficiency (CE)
values of 59.74 and 61.61%, respectively. Figure c and Figure S12a exhibit the cycling behavior of all CoNi-MOF samples. It is obvious
that Co0.8Ni-MOF maintains its capacity advantage over
other samples. A reversible capacity of 1200 mAh g–1 is retained after 200 cycles, which is much higher than those of
Co0.5Ni-MOF (750 mAh g–1) and Co1.0Ni-MOF (900 mAh g–1). Even after 200 cycles,
the Co0.8Ni-MOF electrode can exhibit a high CE of over
99%, as shown in Figure c. The improved Li+ diffusion kinetics during repeated
lithiation and delithiation,[51] a gradual
activation process could be attributed to the stable cycling performance.
As summarized in Figure d and Figure S12b, Co0.8Ni-MOF
also shows the most outstanding rate property among all CoNi-MOF samples.
When cycled at 0.1, 0.2, 0.5, 1, and 2 mA g–1, the
Co0.8Ni-MOF electrode delivers average charge capacities
of 914, 830, 713, 620, and 516 mAh g–1, respectively.
More importantly, the capacity is increased to 1113 mAh g–1 after lowering the current rate back to 0.1 A g–1. This may be due to the activation caused by higher-rate discharging/charging
cycles, illustrating the MOF structure’s robustness in the
face of abrupt current changes. Co0.5Ni-MOF and Co1.0Ni-MOF, on the other hand, only provide 531 and 401 mAh
g–1 at 1 A g–1, respectively,
and 276 and 198 mAh g–1 at 2 A g–1, respectively (Figure S12b). When the
current density is restored to 0.1 A g–1, the capacities
of Co0.5Ni-MOF and Co1.0Ni-MOF are restored
to 945 and 825 mAh g–1, respectively, which are
basically the same as the initial capacitance of the samples. This
shows that, after repeated charging and discharging at different current
densities, the overall structure of MOFs is not damaged and still
has excellent lithium storage performance, which may be due to the
inherent characteristics of CoNi-MOF. On the basis of the above discussion,
we speculate that Co0.8Ni-MOF as an anode material for
Li-ion batteries has great potential, even in the previously reported
MOFs (Table S4).
Figure 6
Electrochemical performance
of the as-synthesized Co0.8Ni-MOF: (a) Cyclic voltammograms
(CVs) at a scan rate of 0.2 mV s–1. (b) Galvanostatic
charge–discharge profiles
at a current density of 500 mA g–1. (c) Cycling
performance and Coulombic efficiency at a current density of 500 mA
g–1. (d) Rate performance at different current densities
from 0.1 to 2.0 A g–1.
Electrochemical performance
of the as-synthesized Co0.8Ni-MOF: (a) Cyclic voltammograms
(CVs) at a scan rate of 0.2 mV s–1. (b) Galvanostatic
charge–discharge profiles
at a current density of 500 mA g–1. (c) Cycling
performance and Coulombic efficiency at a current density of 500 mA
g–1. (d) Rate performance at different current densities
from 0.1 to 2.0 A g–1.Additionally, all CoNi-MOF samples were tested
by electrochemical
impedance spectroscopy (EIS) before and after 200 cycles at 0.5 A
g–1 to further understand their electrochemical
behaviors. An equivalent circuit model was used to fit the impedance
data (Figure ), and
the fitting parameters are summarized in Table S5. All cells exhibit a depressed semi-circle in the high-frequency
region, which corresponds to the electrode’s charge transfer
resistance (Rct), and an inclined line
at the low frequency, which corresponds to the Warburg diffusion process
(Zw). Internal resistance is correlated
with the intersection of the semi-circle at the real axis in the high-frequency
region (denoted as Rs). Both the charge-transfer
resistance (Rct) in the high-frequency
region and the Warburg impedance in the low-frequency region of Co0.8Ni-MOF are smaller than those of Co0.5Ni-MOF
and Co1.0Ni-MOF, indicating that the Co0.8Ni-MOF
hybrid has a large electrode/electrolyte contact area and accelerated
charge transfer and Li+ diffusion, as shown in Figure a. The Nyquist plots
of all samples after 200 cycles are shown in Figure b, which presents the same order as before
cycling. Taking Co0.8Ni-MOF as an example, the solution
resistance (Rs) increases slightly from
3.126 Ω in the pristine state to 10.72 Ω, signifying its
great stability, and the Rct also decreases
from 110.2 to 21.1 Ω after 200 cycles, showing the enriched
wettability and better connectivity of the electrodes. Furthermore,
the Li+ ion diffusion coefficient of the three electrodes
is also compared to demonstrate the electrochemical behaviors mentioned
above, as presented in Figure S13.
Figure 7
Nyquist plots
of all samples (a) at a pristine state and (b) after
200 continuous cycles at 0.5 A g –1. Inset: the
equivalent circuit models used to fit impedance data.
Nyquist plots
of all samples (a) at a pristine state and (b) after
200 continuous cycles at 0.5 A g –1. Inset: the
equivalent circuit models used to fit impedance data.To better understand the possible reasons for the
excellent
performance,
the reaction kinetics of Co0.8Ni-MOF (Figure a) at different scan rates
ranging from 0.2 to 1.2 mV s–1 were analyzed using
the following equation: log i = log a + b log v, where i is the peak current, v is the scan rate, a is a constant, and b is a function variable
parameter. When b approaches 1, the nanofaradaic
pseudocapacitance takes over. When b approaches 0.5,
the system is said to be Li+ ion diffusion-controlled.[33,58] As shown in Figure b, the calculated values of b at the oxidation and
reduction peaks are 0.610 and 0.699, respectively, indicating that
the electrochemical reaction of Co0.8Ni-MOF was related
to capacitive and diffusion behaviors. Furthermore, Trasatti’s
equation Q(v) = Qs + Qb = Qs + k (v1/2) distinguishes the surface charge
contribution (Qs) and the bulk diffusion contribution (Qb).[59] It can be seen from Figure c that the diffusion-controlled contribution
is 40.5% at a scan rate of 0.6 mV s–1, and the capacitive
contribution of Co0.8Ni-MOF increases with the scan rate,
as shown in Figure d. When the sweep rate is increased from 0.2 to 1.2 mV s–1, the capacitive contribution also increases from 31.82 to 73.2%.
Therefore, the excellent electrochemical performance of Co0.8Ni-MOF can be partly attributed to the pseudocapacitive behaviors,
which occupied a significant portion of the redox processes, leading
to high capacity and rate performance.
Figure 8
Kinetics of the electrochemical
behavior toward Li+ for
the Co0.8Ni-MOF electrode: (a) CV curves at various scan
rates ranging from 0.2 to 1.2 mV s–1. (b) Relationship
between peak currents and potential swing rates. (c) Separation of
capacitive and diffusion currents to the total at 0.6 mV s–1 scanning speed. (d) Charge contribution ratios of capacitive and
diffusion-controlled devices at various scan rates.
Kinetics of the electrochemical
behavior toward Li+ for
the Co0.8Ni-MOF electrode: (a) CV curves at various scan
rates ranging from 0.2 to 1.2 mV s–1. (b) Relationship
between peak currents and potential swing rates. (c) Separation of
capacitive and diffusion currents to the total at 0.6 mV s–1 scanning speed. (d) Charge contribution ratios of capacitive and
diffusion-controlled devices at various scan rates.
Conclusions
In this work, by using a one-pot solvothermal
method, we successfully
recovered PET plastic waste as a precursor to fabricate value-added
CoNi-MOF and investigated lithium anodic performance for the first
time. The as-synthesized Co0.8Ni-MOF exhibits excellent
crystallinity, purity, and electrochemical performance. The initial
discharge and charge capacities are 2496 and 1729 mAh g–1, respectively. Even after 200 cycles, the Co0.8Ni-MOF
electrode can exhibit a high CE of over 99%. Furthermore, the Co0.8Ni-MOF shows excellent rate performance at various rates.
The CV curves show excellent overlap and reproducibility, indicating
great reversibility and cycling stability of the Co0.8Ni-MOF.
Altogether, given the environmental and economic benefits, the Co0.8Ni-MOF derived from PET waste is thought to be an appealing
material for a variety of potential practical applications. Furthermore,
compared with the initial CE of most commercial anodes, the first
efficiency of Co0.8Ni-MOF is still slightly lower. However,
this problem has yet to be overcome. Surface coating and prelithiation
may provide ideas to solve this problem and improve the overall performance
of MOF anodes. Once this problem is solved, lithium anode materials
can be easily produced on a large scale in the future and can be explored
in other lithium-related fields.
Authors: Martin Drobek; Jae-Hun Kim; Mikhael Bechelany; Cyril Vallicari; Anne Julbe; Sang Sub Kim Journal: ACS Appl Mater Interfaces Date: 2016-03-25 Impact factor: 9.229