Anqi Wang1, Rui Tan1, Charlotte Breakwell2, Xiaochu Wei1, Zhiyu Fan1, Chunchun Ye3, Richard Malpass-Evans3, Tao Liu4, Martijn A Zwijnenburg5, Kim E Jelfs2, Neil B McKeown3, Jun Chen6, Qilei Song1. 1. Department of Chemical Engineering, Imperial College London, London SW7 2AZ, U.K. 2. Department of Chemistry, Molecular Sciences Research Hub, Imperial College London, London W12 0BZ, U.K. 3. EaStChem School of Chemistry, University of Edinburgh, Edinburgh EH9 3FJ, U.K. 4. Shanghai Key Laboratory of Chemical Assessment and Sustainability, Department of Chemistry, Tongji University, Shanghai 200092, China. 5. Department of Chemistry, University College London, London WC1H 0AJ, U.K. 6. Key Laboratory of Advanced Energy Materials Chemistry (Ministry of Education), Renewable Energy Conversion and Storage Center (RECAST), College of Chemistry, Nankai University, Tianjin 300071, China.
Abstract
Redox-active organic materials have emerged as promising alternatives to conventional inorganic electrode materials in electrochemical devices for energy storage. However, the deployment of redox-active organic materials in practical lithium-ion battery devices is hindered by their undesired solubility in electrolyte solvents, sluggish charge transfer and mass transport, as well as processing complexity. Here, we report a new molecular engineering approach to prepare redox-active polymers of intrinsic microporosity (PIMs) that possess an open network of subnanometer pores and abundant accessible carbonyl-based redox sites for fast lithium-ion transport and storage. Redox-active PIMs can be solution-processed into thin films and polymer-carbon composites with a homogeneously dispersed microstructure while remaining insoluble in electrolyte solvents. Solution-processed redox-active PIM electrodes demonstrate improved cycling performance in lithium-ion batteries with no apparent capacity decay. Redox-active PIMs with combined properties of intrinsic microporosity, reversible redox activity, and solution processability may have broad utility in a variety of electrochemical devices for energy storage, sensors, and electronic applications.
Redox-active organic materials have emerged as promising alternatives to conventional inorganic electrode materials in electrochemical devices for energy storage. However, the deployment of redox-active organic materials in practical lithium-ion battery devices is hindered by their undesired solubility in electrolyte solvents, sluggish charge transfer and mass transport, as well as processing complexity. Here, we report a new molecular engineering approach to prepare redox-active polymers of intrinsic microporosity (PIMs) that possess an open network of subnanometer pores and abundant accessible carbonyl-based redox sites for fast lithium-ion transport and storage. Redox-active PIMs can be solution-processed into thin films and polymer-carbon composites with a homogeneously dispersed microstructure while remaining insoluble in electrolyte solvents. Solution-processed redox-active PIM electrodes demonstrate improved cycling performance in lithium-ion batteries with no apparent capacity decay. Redox-active PIMs with combined properties of intrinsic microporosity, reversible redox activity, and solution processability may have broad utility in a variety of electrochemical devices for energy storage, sensors, and electronic applications.
With the rapid development
of renewable energy and electric vehicles,
there are increasing demands for efficient and cost-effective batteries
for grid storage and transport applications. Lithium-ion batteries
(LIBs) dominate the market of portable electronics and electric vehicles
with electrode materials mainly produced from inorganic metal oxides,
such as LiCoO2, LiMn2O4, LiFePO4, and LiNiMnCoO2. However, there
are growing concerns about these inorganic electrode materials regarding
their high cost, heavy metal toxicity, environmental pollution, and
sophisticated end-of-life recycling. In contrast, redox-active organic
materials that can reversibly store and release charges have emerged
as promising alternatives to inorganic metal oxides owing to their
various inherent merits such as chemical diversity, structural tunability,
processability, environmental sustainability, and potential low cost.[1,2] Inspired by the ubiquitous redox cofactors (e.g., quinone- and flavin-based
species) in biological systems, the discovery and development of redox-active
organic materials have attracted considerable interest for use in
batteries and supercapacitors, photo-/electrocatalysis, and sensors.
Redox-active organic molecules often have a high density of redox
sites per mass, which provides high capacity when used as electrode
materials in batteries, such as carbonyl-based small molecules, lithium
rhodizoate[3] (580 mAh g–1) and cyclohexanehexone[4] (902 mAh g–1). Nevertheless, these molecular species tend to dissolve
in electrolyte solvents, such as carbonates and ethers, leading to
rapid performance degradation and a short lifetime.[1] To avoid this dissolution problem, redox-active segments
are directly polymerized or incorporated as pendant groups into polymer
chains/networks to afford insoluble solids.[5−8] However, these redox-active polymers
often pack efficiently in a dense amorphous solid state, so that ion
transport and electron transfer are slower relative to their molecular
analogues, resulting in ineffective utilization of redox sites within
the materials and poor electrochemical performance at the device level.The recent development of porous organic materials provides extended
chemical space for designing redox-active organic materials with improved
electrochemical performance. The presence of molecular-sized channels
constitutes effective pathways for efficient ion diffusion and mass
transport, making redox sites more accessible to metal ions and analytes.[9,10] For example, covalent organic frameworks (COFs) have been extensively
studied as electrode materials in supercapacitors and metal-ion batteries,[11−13] and show rapid redox processes owing to their ordered ion-transport
channels, enabling high-power batteries.[14,15] However, complicated processing is often required to fabricate these
crystalline materials into battery electrodes to provide good dispersion
and contact between active materials and carbon additives, which are
crucial for mixed ionic-electronic conduction.[16] Several fabrication methods have been reported, such as
exfoliation of COF solids into nanosheets,[17] growth of conductive polymers within COF pores,[18] and in situ growth of COF nanosheets on carbon nanotubes[12,14,15] and graphene.[19,20] These possessing steps add additional complexity and cost to the
fabrication process and can be difficult to reproduce or scale up.
Hence, it is highly desired to develop redox-active microporous polymers
that can be dissolved in certain organic solvents for ease of processing
but remain insoluble in electrolytes.Polymers of intrinsic
microporosity (PIMs) are solution-processable
microporous materials with subnanometer channels generated from the
inefficient packing of the rigid, contorted polymer chains.[21,22] PIMs have shown great promise as next-generation membrane materials
for molecular separations,[23−25] batteries,[26−29] and fuel cells.[30] We anticipate that if incorporated with redox-active structural
units, PIMs with fast ion-transport channels could be used as high-performance
electrode materials in electrochemical devices. However, the electrochemical
properties of PIMs have been rarely investigated, with the exception
of using PIM-7 as a membrane separator in Li-S batteries.[31] We surveyed the library of reported PIMs and
noticed four examples that were initially designed for gas separation
applications but contain a redox-active structural unit, namely the
phenazine in PIM-7[32] and TPIM-1[33] as well as the conjugated diimide in PMDA-TMDAT
and NTDA-TMDAT[34] (Figure S2). However, a large portion of redox-inactive structural
units is essential in these PIMs to enforce a rigid, contorted chain
structure, resulting in a low theoretical charge capacity with values
in the range of 90–130 mAh g–1. The relatively
low density of redox sites represents an obstacle to the immediate
use of these PIMs in electrochemical devices. Although an alternative
approach toward electroactive PIMs can be achieved via vacuum thermolysis
that produces microporous carbon electrodes for supercapacitor energy
storage,[35] the intrinsic merits of PIMs
(e.g., solution processability) are sacrificed during the postsynthetic
treatment. Therefore, a molecular redesign is required to maximize
the mass ratio of redox-active units within the rigid, contorted polymer
chains to provide a new generation of solution-processable redox-active
PIMs.Here, we report the design and synthesis of redox-active
PIMs and
demonstrate their promising electrochemical performance in lithium-ion
batteries (Figure ). The material design is achieved by replacing one benzo group of
the triptycene component with a benzoquinone unit to afford a redox-active
structural unit that remains highly rigid and contorted (Figure b). To suppress rotational
freedom around the C–N single bond of the imide unit, methyl
groups are introduced to exert sufficient steric hindrance. Redox-active
PIMs give a high apparent BET surface area of up to ∼700 m2 g–1 and a high theoretical capacity of
up to 248 mAh g–1. Moreover, Li+ ion
diffusion is enhanced by the highly interconnected subnanometer pores
of redox-active PIMs (Figure c), as verified by cyclic voltammetry (CV) and electrochemical
impedance spectroscopy (EIS) measurements, while solution processability
allows the fabrication of thin films (Figure d) and polymer–carbon composites with
a well-defined microstructure (Figure f), enabling highly stable cycling performance of lithium-ion
batteries. Conventional battery electrodes are usually prepared by
a powder dispersion method, i.e., dispersing active materials (usually
micron-sized), carbon additives, and polymer binders in a solvent
to form a slurry for casting. The resulting electrodes have multiple
heterointerfaces between each component, generating high interfacial
resistance and unstable microstructures that tend to degrade during
repeated charging and discharging (Figure e). In contrast, solution-processable redox-active
PIMs afford a well-defined electrode microstructure, where active
materials are uniformly coated onto carbon additives creating seamless
interfaces, which will benefit ion transport and electron transfer
processes and promote a homogeneous current density distribution within
the electrodes (Figure f). The solution processing approach demonstrated in this work for
electrode microstructure optimization leads to a remarkable enhancement
of cycling stability of lithium-ion batteries and may be applied to
other electrochemical devices that require intimate contact between
multiple components.
Figure 1
Redox-active polymers of intrinsic microporosity (PIMs).
Redox-active
PIMs show combined features of reversible redox activity, microporosity
generated from inefficient packing of polymer chains for electrolyte
uptake and fast ion transport, as well as solution processability
for ease of fabrication. (a) Schematic diagram showing the rigid,
contorted structure of PIMs. The yellow spheres are metal ions. (b)
Redox reaction mechanism of the structural units and linking groups
of redox-active PIMs. (c) Structure of a 1 nm thick cross-section
of the 49.8 × 49.8 × 49.8 Å3 amorphous cells
of PIM-TMTrip-MQ with van der Waals surface of the polymer chains
shaded in blue and free volume shaded in yellow. Redox-active oxygen
atoms are highlighted in red. (d) Photos of a PIM-TMTrip-MHQ NMP solution
and a solution-cast self-supported film with a diameter of 2.4 cm.
(e, f) Schematic diagrams showing the different microstructures of
active material–carbon composites fabricated via the conventional
powder dispersion method (e) and the solution possessing method (f).
Redox-active polymers of intrinsic microporosity (PIMs).
Redox-active
PIMs show combined features of reversible redox activity, microporosity
generated from inefficient packing of polymer chains for electrolyte
uptake and fast ion transport, as well as solution processability
for ease of fabrication. (a) Schematic diagram showing the rigid,
contorted structure of PIMs. The yellow spheres are metal ions. (b)
Redox reaction mechanism of the structural units and linking groups
of redox-active PIMs. (c) Structure of a 1 nm thick cross-section
of the 49.8 × 49.8 × 49.8 Å3 amorphous cells
of PIM-TMTrip-MQ with van der Waals surface of the polymer chains
shaded in blue and free volume shaded in yellow. Redox-active oxygen
atoms are highlighted in red. (d) Photos of a PIM-TMTrip-MHQ NMP solution
and a solution-cast self-supported film with a diameter of 2.4 cm.
(e, f) Schematic diagrams showing the different microstructures of
active material–carbon composites fabricated via the conventional
powder dispersion method (e) and the solution possessing method (f).
Results and Discussion
Design, Synthesis, and Characterization of
Redox-Active PIMs
Cycloimidization reaction was chosen as
the polymerization route to redox-active PIMs as the imide linking
group possesses robust redox chemistry[36] and can be directly generated by careful selection of dianhydride
monomers, a conjugated structure of which is required to give reversible
redox activity. As the rigid, planar pyromellitic dianhydride (PMDA)
was selected for polymerization, a rigid diamine monomer featuring
a site of contortion is required to avoid an intractable linear polymer.
Based on a previous battery electrode work in the literature, a triptycene
quinone molecule was selected as the structural unit as it had previously
shown multielectron redox reactions as high-capacity cathode material.[37] Although its redox cycling performance was reported
to be poor due to its partial solubility in battery electrolytes,
we anticipated that utilization of this structural unit in redox-active
PIMs would simultaneously serve as sites of contortion while providing
abundant redox-active functionality.The target redox-active
PIM polymer (PIM-TMTrip-MQ) was synthesized using a diamine monomer
based on triptycene monobenzoquinone that contains tetramethyl groups
to prohibit rotation around the C–N single bond (Figures a,b and S1 and S2). Additional experimental details, materials, and
methods are provided in the Supporting Information. To compare PIM-TMTrip-MQ with structurally similar polymers, which
contain imide and quinone functionalities but with a less microporous
or nonporous structure, PI-Trip-MQ and PI-AQ were prepared (Figure a). PI-Trip-MQ is
analogous to PIM-TMTrip-MQ but without tetramethyl groups, so that
free rotation of imide bonds will lead to more efficient packing of
polymer chains, isolating the internal molecular free volume elements
generated by triptycene units from one another. Details of the synthesis
of both triptycene monomers are provided in the Supporting Information. In contrast to the triptycene-based
polyimides, the anthraquinone and diimide structural units in PI-AQ
have a planar shape and are linked via imide linkages with unrestricted
rotation freedom; hence, the formation of any free volume elements
is reduced to a minimum. During the polymerization reaction, a highly
viscous, homogeneous brown solution was obtained for PIM-TMTrip-MHQ,
while yellow precipitate was immediately formed and remained insoluble
throughout the reaction for PI-Trip-MHQ and PI-AQ. After precipitation
and purification to remove oligomers, PIM-TMTrip-MHQ can be readily
dissolved in polar aprotic solvents (such as NMP, DMF, and DMSO) owing
to its rigid and contorted chain structure that reduces interchain
cohesion and facilitates the absorption of solvent, enabling the fabrication
of mechanically robust films by solution casting (Figure d). In contrast, PI-Trip-MHQ
and PI-AQ are insoluble in common solvents, presumably due to the
strong interchain π–π stacking interactions promoted
by rearrangement and rotation of the more flexible polymer chains.
Polymer structures were confirmed by FT-IR, solid-state 13C NMR, and TGA (Figures S3–S5).
The incorporation of redox-active sites in both the structural unit
and the linking group provides high theoretical capacity values of
189 mAh g–1 for PIM-TMTrip-MQ, 209 mAh g–1 for PI-Trip-MQ, and 248 mAh g–1 for PI-AQ based
on a reversible four-electron redox reaction.
Figure 2
Polymer design and characterization.
(a) Chemical structure of
redox-active PIMs. (b) Plot showing the increase in energy associated
with the deviation in the marked dihedral angle within the imide linking
group of PIM-TMTrip-MQ (red) as compared with those in PI-Trip-MQ
(blue) and PI-AQ (gray). (c) Three-dimensional view of an amorphous
cell of the PIM-TMTrip-MQ polymer. Cell size: 49.8 × 49.8 ×
49.8 Å3. The blue surface mesh highlights the Connolly
surface with respect to a probe radius of 1.55 Å. (d) CO2 adsorption–desorption isotherms at 273 K. (e) Pore
size distributions derived from CO2 sorption based on DFT
calculations. (f) Methanol vapor sorption isotherms of polymer powders
at 25 °C. Solid symbols in (d, f): adsorption; open symbols:
desorption.
Polymer design and characterization.
(a) Chemical structure of
redox-active PIMs. (b) Plot showing the increase in energy associated
with the deviation in the marked dihedral angle within the imide linking
group of PIM-TMTrip-MQ (red) as compared with those in PI-Trip-MQ
(blue) and PI-AQ (gray). (c) Three-dimensional view of an amorphous
cell of the PIM-TMTrip-MQ polymer. Cell size: 49.8 × 49.8 ×
49.8 Å3. The blue surface mesh highlights the Connolly
surface with respect to a probe radius of 1.55 Å. (d) CO2 adsorption–desorption isotherms at 273 K. (e) Pore
size distributions derived from CO2 sorption based on DFT
calculations. (f) Methanol vapor sorption isotherms of polymer powders
at 25 °C. Solid symbols in (d, f): adsorption; open symbols:
desorption.High uptake of nitrogen at low relative pressure
at 77 K indicates
freely accessible microporosity in PIM-TMTrip-MQ with a high apparent
Brunauer–Emmett–Teller (BET) surface area value of 702
m2 g–1 (N2 adsorption isotherms
and pore size distributions in Figure S6). In contrast, PI-Trip-MQ displayed negligible nitrogen uptake and
an apparent BET surface area of only 6.4 m2 g–1. NLDFT pore size distribution derived from the nitrogen sorption
isotherm confirms the absence of any micropores in PI-Trip-MQ that
are accessible to nitrogen. Microporosity is consistent for PIM-TMTrip-MQ
and PI-Trip-MQ with their hydroquinone precursors (labeled as MHQ, Figures S2 and S6). Interestingly, substantial
carbon dioxide (CO2) adsorption at 273K (Figure d) was observed in the low-pressure
range for PI-Trip-MQ with a value comparable to that for PIM-TMTrip-MQ,
while its overall adsorption capacity is moderately lower. DFT pore
size distributions calculated from these data gave a high concentration
of both small (<0.7 nm) and large (0.7–1.0 nm) micropores
in PIM-TMTrip-MQ, but only small ultramicropores (<0.7 nm) in PI-Trip-MQ
(Figure e). The molecular
simulation further verifies the presence of micropores in both PIM-TMTrip-MQ
and PI-Trip-MQ, with the latter being predominantly ultramicroporous
and less accessible to larger molecules (Figure c and simulation data in Figures S7–S9). Importantly, pore size distributions
derived from molecular models agree well with those from the DFT analysis
of CO2 sorption (Figures e and S8). It can be concluded
that a continuous network of interconnected free volume elements (both
small and large) is formed in PIM-TMTrip-MQ owing to its chain rigidity
and contortion. In contrast, the absence of any restriction for C–N
bond rotation in PI-Trip-MQ leads to more efficient packing of the
polymer chains, generating predominantly ultramicropores that are
only accessible to smaller carbon dioxide molecules at a higher temperature
(273 K) but not to larger nitrogen molecules. In addition, the lowest
carbon dioxide adsorption in PI-AQ that is composed of planar structural
units further verifies triptycene monobenzoquinone as a porosity-generating
structural unit in PIM-TMTrip-MQ and PI-Trip-MQ (Figure d–e).Percolation
of electrolyte solvents within redox-active materials
is crucial to the formation of ion-transport channels for fast diffusion
of metal ions with a short response time during battery charging and
discharging. Methanol was used to probe the accessibility of micropores
to organic solvents and assess the corresponding solvent uptake capacity
(Figure f). Methanol
uptake correlates well with the microporosity determined from CO2 sorption and molecular simulation, with the most microporous
PIM-TMTrip-MQ showing the highest sorption of 36.5 wt % and the nonporous
PI-AQ showing the lowest of 19.0 wt % at 273 K and 116 mbar. In addition
to the siphoning effect driven by the capillary forces from micropores,
solvent percolation in these polyimides of varied microporosity is
also influenced by polymer swelling.
Electrochemical Properties
Conventional
coin cells with lithium foil anodes were prepared with cathodes fabricated
from slurries of each polymer with carbon black and PVDF binder in
anhydrous NMP. Solid-state cyclic voltammetry (CV) measurements showed
that PIM-TMTrip-MQ exhibited four pairs of well-resolved redox peaks
with E1/2 values of 2.11, 2.37, 2.64,
and 2.84 V vs Li/Li+, respectively (Figure a,b). These redox peaks correspond to the
transfer of two electrons in benzoquinone units and another two electrons
in diimide units. In principle, the four carbonyls in diimide could
accept four electrons to generate reduced tetra-anions as suggested
by the calculated molecular electrostatic potential (MESP, Figures e and S13, Table S1). However,
in previous work on other diimide polymers, the utilization of all
four carbonyls has been shown to result in structural damage to the
polymer,[38,39] which does not appear to be occurring within
the voltage range in this study. Similar CV curves as for PIM-TMTrip-MQ
were observed in PI-Trip-MQ, but with broader peak widths and larger
cathodic peak-to-anodic peak separation (ΔEp, Figure S10). Even larger
peak separation was observed in PI-AQ, which showed broad and overlapping
peaks at a scanning rate greater than 0.2 mV s–1. The difference in ΔEp suggests
larger polarization and lower utilization of carbonyl groups in the
less porous PI-Trip-MQ and PI-AQ than in PIM-TMTrip-MQ, while the
stronger intramolecular electronic interactions for the less porous
polymers may also explain the broad and poorly resolved peaks.
Figure 3
Electrochemical
properties. (a) CV of PIM-TMTrip-MQ and model compounds
TMTrip-MQ and DPPMDI. The electrolyte is a 1 M LiTFSI in DOL/DME (2:1
by vol.). (b) CV of PIM-TMTrip-MQ at varied scanning rates. (c) Log–log
plot of peak current vs scanning rate for the anodic peak of the highest
potential (∼2.9 V vs Li+/Li) in CV measurements
in Figure S10. (d) Proposed redox mechanism
of PIM-TMTrip-MQ. (e) Molecular electrostatic potential (MESP) of
the PIM-TMTrip-MQ-nLi repeat units (n = 0–4).
Electrochemical
properties. (a) CV of PIM-TMTrip-MQ and model compounds
TMTrip-MQ and DPPMDI. The electrolyte is a 1 M LiTFSI in DOL/DME (2:1
by vol.). (b) CV of PIM-TMTrip-MQ at varied scanning rates. (c) Log–log
plot of peak current vs scanning rate for the anodic peak of the highest
potential (∼2.9 V vs Li+/Li) in CV measurements
in Figure S10. (d) Proposed redox mechanism
of PIM-TMTrip-MQ. (e) Molecular electrostatic potential (MESP) of
the PIM-TMTrip-MQ-nLi repeat units (n = 0–4).Model compounds 2,6-diphenyl-pyromellitic diimide
(DPPMDI) and
tetramethyl-triptycene monobenzoquinone (TMTrip-MQ) were prepared
to confirm the assignment of CV peaks of PIM-Trip-MQ (synthetic details
in the SI). Solid-state CV measurements
of the model compounds suggest that the imide units were reduced at
less positive potentials of 2.06 and 2.25 V vs Li/Li+ in
comparison to the more positive potentials required to reduce triptycene
monobenzoquinone (2.58 and 2.83 V vs Li/Li+, Figure a). Therefore, we proposed
a redox mechanism involving the successive, reversible conversions
between the pristine PIM-TMTrip-MQ (fully oxidized state) and its
tetra-anion derivative (fully reduced state) via the formation of
quinone radical anions, quinone dianions, diimide radial anions, and
diimide dianions (Figure d). This reaction mechanism is supported by DFT calculations
on a cluster model of the hydrogen-capped PIM-TMTrip-MQ repeat unit
(Figure S13 and Table S1). The molecular
electrostatic potential (MESP) for the bare hydrogen-capped PIM-TMTrip-MQ
repeat unit was first calculated to predict the possible Li binding
sites. The surface minima revealed the carbonyl oxygens to be the
most preferable sites for lithiation, where areas of high electron
density were most likely to attract a Li+ ion. Based on
the possible Li binding sites, a conformational search was then performed
for the hydrogen-capped PIM-TMTrip-MQ repeat unit with different numbers
of Li (n = 1–4, Figure S11). The lithiation pathway was predicted based on the minimum
energy principle, and MESP plots were calculated for each preferred
intermediate (Figure e). Predicted redox potentials in the solution phase fitted well
with the values measured experimentally (Table S1), while the 5th and 6th lithiation of the PIM-TMTrip-MQ
repeat unit, theoretically forming the diimide tetra-anions, showed
considerably less positive predicted reduction potential, providing
further evidence to support the proposed four-electron redox mechanism.To understand the influence of polymer microporosity on Li+ ion diffusion and charge transfer in the composite electrodes,
the log–log plots of the scanning rate versus the peak current
density based on the CV measurements (Figure b) were analyzed. These parameters follow
the power law in eq Where b refers to the slope
of the linear fit of the log–log plot. A b value approaching unity suggests a completely surface-controlled
behavior during the electrochemical oxidation and reduction processes,
while a value of 0.5 indicates a purely diffusion-controlled Randles–Ševčik
behavior.[40] PIM-TMTrip-MQ displayed a close-to-unity
value of 0.974 (Figure c), much higher than those for PI-Trip-MQ (0.825) and PI-AQ (0.84).
The high b value suggests that the rate limitation
arising from diffusion constraints is effectively overcome in PIM-TMTrip-MQ
with highly interconnected micropores, confirming the hypothesis that
microporosity promotes ion diffusion in the redox-active polymers.
This observation is further confirmed in acetonitrile electrolyte
solutions with LiClO4, NaClO4, or TBAClO4 as the salt (Figure S11). Fast
Li+ ion diffusion in the most microporous PIM is also supported
by its high ionic conductivity as measured with a solution-cast film
using electrochemical impedance spectroscopy (EIS) with values ranging
from 1.7 to 2.7 mS cm–1 over the temperature range
of 30–80 °C (Figure S14). The
defect-free structure of the films used for the conductivity test
was confirmed by single gas permeation measurements (Table S2). However, we were not able to process PI-Trip-MQ
and PI-AQ into dense films due to their poor solubility in organic
solvents, precluding the direct comparison of their ionic conductivity.
Stable Cycling Performance Enabled by Solution-Processed
Electrode
As most redox-active organic materials are insulating,
conductive additives are required to form a composite with the active
materials. It is crucial to control the microstructure of the composites
to achieve efficient ion transport and electron transfer and to avoid
heterogeneous current density distribution that is linked to reduced
accessible capacity and local overcharge[41−43] (Figure e,f). We initially applied
the conventional powder dispersion method to fabricate insoluble PI-Trip-MQ
and PI-AQ electrode composites by manually grinding each polymer powder,
carbon black, and the PVDF binder with NMP added to form a slurry,
which was then cast onto alumina foil and dried under vacuum. SEM
images showed discrete large polymer flakes or particles as well as
carbon aggregates (Figures a,b and S15). Time-of-flight secondary
ion mass spectrometry (ToF-SIMS) further revealed the heterogeneous
spatial distribution of different components in the electrode composites,
as visualized by the signals of lithium (Li+) and fluorine
(Cs2F+) that correspond to redox-active polymers
and PVDF binder, respectively. The spatial distributions of redox-active
polymers and PVDF were complementary to each other, exhibiting scattered
large polymer particles (1–10 μm in diameter) embedded
in the PVDF matrix (Figure a,b). Although the distribution of carbon black aggregates
cannot be measured due to its lack of characteristic fragments, we
envision that PVDF binder forms a coating layer on carbon black particles,
and thus, the spatial distribution of carbon blacks would be consistent
with that of the PVDF binder.
Figure 4
Characterization of electrode microstructure.
SEM and ToF-SIMS
images for (a) PI-Trip-MQ and (b) PI-AQ electrodes that were prepared
by powder dispersion and (c) PIM-TMTrip-MHQ electrodes prepared by
solution processing. The electrodes were disassembled from batteries
at an SOC of 0 (fully discharged) and then thoroughly washed with
DOL/DME to remove absorbed lithium salts, followed by drying. First
column: SEM images. Second and third columns: secondary ion images
showing the distribution of PVDF binder (Cs2F+) and polymer (Li+), respectively. Fourth column: combined
secondary ion images showing the spatial distribution of PVDF (green)
and redox-active polymer (red).
Characterization of electrode microstructure.
SEM and ToF-SIMS
images for (a) PI-Trip-MQ and (b) PI-AQ electrodes that were prepared
by powder dispersion and (c) PIM-TMTrip-MHQ electrodes prepared by
solution processing. The electrodes were disassembled from batteries
at an SOC of 0 (fully discharged) and then thoroughly washed with
DOL/DME to remove absorbed lithium salts, followed by drying. First
column: SEM images. Second and third columns: secondary ion images
showing the distribution of PVDF binder (Cs2F+) and polymer (Li+), respectively. Fourth column: combined
secondary ion images showing the spatial distribution of PVDF (green)
and redox-active polymer (red).The solubility of PIM-TMTrip-MHQ in NMP further
motivated us to
modify the fabrication method to achieve a more homogeneous microstructure
in the composite electrode. The modified method included dissolving
the polymer and PVDF binder in NMP to form a homogeneous solution
within which carbon black was then dispersed, followed by the identical
casting and drying procedures as in the powder dispersion method.
No large particles or flakes could be identified from SEM images (Figures c and S16), while the apparent size of the carbon black
particles was noticeably larger than that in a control sample fabricated
using only carbon blacks and PVDF binder (Figure S16c). ToF-SIMS showed homogeneous spatial distribution of
the redox-active polymer and PVDF binder across the electrode composite
(Figure c), confirming
the well-defined microstructure enabled by solution processing. The
uniform coating of PIM-TMTrip-MHQ onto the carbon additives achieves
intimate contact and seamless interfaces between different components,
allowing the formation of an ionic and electronic percolation network,
which is the key to ensuring the homogeneity of current distribution
within the electrodes.After microstructure optimization of
the polymer–carbon
composites, their performance as the cathode in lithium-ion batteries
was evaluated. To study the dissolution and shuttling of redox-active
materials as the capacity decay mechanism, we performed ex
situ solubility tests of electrodes disassembled from cells
at different states of charge (Figure a,b). The small molecule, TMTrip-MQ, was found highly
soluble in electrolytes regardless of the state of charge, leading
to complete loss of capacity within 10 cycles of charging and discharging
(Figure c). In contrast,
all polymers remained insoluble in battery electrolyte solvents, as
confirmed by UV–vis (Figure d). The cell based on a solution-processed PIM-TMTrip-MHQ
cathode demonstrated highly stable cycling performance with a Coulombic
efficiency (CE) of 99.8% and no apparent capacity decay over 200 charging–discharging
cycles at 1C (Figures e and S19 and S20). The cell polarization
remained low throughout the cycling test (Figure f). In contrast, otherwise-identical cells
based on PI-Trip-MQ and PI-AQ cathodes that were prepared by the powder
dispersion method exhibited much larger cell polarization and a steady
capacity decay with a CE of 98.3 and 99.2% and capacity retention
of 75 and 67%, respectively, after 200 charging–discharging
cycles at 1C (Figure e); such performance decay is commonly observed for polymer-based
electrodes fabricated by the powder dispersion method. One potential
decay mechanism for PI-Trip-MQ and PI-AQ is the irreversible side
reactions and structural changes of active materials induced by local
overcharge,[41−43] while the well-defined microstructure of the solution-processed
PIM-TMTrip-MHQ electrode appears to ensure homogeneous current distribution
that prevents capacity loss, as evidenced by the uniform spatial distribution
of Li+ ions in the electrode after discharge. Furthermore,
the PI-Trip-MQ and PI-AQ electrodes may undergo delamination of the
discrete polymer particles with carbon additives and the current collector
due to volume changes of polymer particles during charging and discharging,
while the solution-processed electrodes possess a certain level of
resistance toward the delamination between polymer coating layer with
carbon cores.
Figure 5
Cycling performance of lithium-ion batteries. (a, b) Solubility
tests of electrodes at varied states of charge for a molecular compound
TMTrip-MQ (a) and PIM-TMTrip-MHQ polymer (b). (c) Cycling performance
for a TMTrip-MQ-based LIB, showing rapid capacity decay due to molecule
dissolution and shuttling. (d) UV–vis spectra of the washing
solution for electrodes disassembled from LIB cells after discharge.
(e) LIB cycling performance for redox-active PIMs. (f) Charging–discharging
profiles at different cycling numbers.
Cycling performance of lithium-ion batteries. (a, b) Solubility
tests of electrodes at varied states of charge for a molecular compound
TMTrip-MQ (a) and PIM-TMTrip-MHQ polymer (b). (c) Cycling performance
for a TMTrip-MQ-based LIB, showing rapid capacity decay due to molecule
dissolution and shuttling. (d) UV–vis spectra of the washing
solution for electrodes disassembled from LIB cells after discharge.
(e) LIB cycling performance for redox-active PIMs. (f) Charging–discharging
profiles at different cycling numbers.In general, redox-active organic materials have
relatively poor
electronic conductivity aside from doped conductive polymers[44] and π-conjugated redox polymers.[45] Redox-active PIMs are not an exception in this
regard, showing through-plane electronic conductivity values of 2.9
× 10–13, 2.3 × 10–12, and 2.5 × 10–14 S cm–1 for PIM-TMTrip-MQ, PI-Trip-MQ, and PI-AQ, respectively. These values
are within typical ranges for carbonyl, imine, and radical-based materials
that do not contain delocalized π-electron systems as conductive
moieties.[1] As a result, redox-active PIMs
showed limited rating performance, with the discharge capacity dropping
to negligible at 5C (Figures a and S20), while removing carbon
additives from the composite electrode led to the “shut-down”
of redox activity (Figure S12). In contrast,
some carbonyl polymers are demonstrated with high capacity at high
charge and discharge rates, such as poly(1,4-anthraquinone)[5] which delivers 69% of their low-rate capacity
(181 mAh g–1) at 20C as well as a lithium salt polymer
of dihydroxyanthraquinone[46] that displays
the capacity of 236 mAh g–1 at 10C. The high rating
performance of these polymers is based on their high electronic conductivity,
which is ensured by the π-conjugated structure. To improve electron
transfer within the composite electrode, we further utilized carbon
nanotubes (CNT) as conductive additives to construct a more conducting
network. The discharge capacity of PIM-TMTip-MHQ/CNT composite electrode
was improved to the range of 80–90 mAh g–1 at 5C from none for the electrode without CNT (Figure b), but the improvement is
highly dependent on mass loading (Figure S21). Importantly, the solution-processed electrode exhibited a stable
cycling performance over 1400 cycles of charge and discharge, further
confirming the important role of solution processing in achieving
high-capacity retention (Figure c). To track the evolution of the electrochemical properties
of PIM-TMTrip-MHQ electrode during cycling, we performed incremental
capacity analysis (Figure S22) based on
the differentiation (dQ/dV) of the
charging–discharging profiles, a method widely used as a diagnostic
tool to investigate battery state of health. The 2nd cycle of charging
showed four well-resolved peaks in the incremental capacity curve
at 2.47, 2.81, 3.07, 3.31 V, respectively, in good agreement with
CV measurements. However, the two peaks at lower potentials (i.e.,
2.47 and 2.81 V) underwent a continuing increase in peak area during
cycling, accompanied by a shift of redox potential toward higher values
(i.e., the cutoff voltage of 3.5 V) and a decrease in peak area for
the other two peaks. The mechanism for the change of potential plateaus
during cycling merits further study.
Figure 6
Rating performance improvement enabled
by carbon nanotube (CNT) additives.
(a) Rating
performance of PIM-TMTrip-MHQ electrodes with or without CNT additives.
(b) Charging–discharging profiles at different cycling numbers
and (c) LIB cycling performance for PIM-TMTrip-MHQ electrode with
CNT additives.
Rating performance improvement enabled
by carbon nanotube (CNT) additives.
(a) Rating
performance of PIM-TMTrip-MHQ electrodes with or without CNT additives.
(b) Charging–discharging profiles at different cycling numbers
and (c) LIB cycling performance for PIM-TMTrip-MHQ electrode with
CNT additives.
Discussion on Rating Performance and Charge
Capacity
Reaction kinetics in electrode materials is controlled
by ionic transport, electron transfer as well as ionic–electronic
coupling. The influence of ionic transport has been extensively studied
for porous network polymers, particularly covalent organic frameworks
(COFs). As the electron transfer in COFs is usually efficient, superior
rating performance can be achieved through the enhancement of ionic
transport. For conventional nonporous conjugated polymers, the high
degree of π-conjugation ensures efficient intrachain electron
movement through delocalized π-orbitals and interchain electron
movement where there is sufficient π–π overlap
between polymer chain segments. Ion transport in these nonporous polymers
mainly relies on electrolyte swelling and could be sluggish for some
polymer chemistries. For redox-active PIMs reported in this work,
ionic transport is effectively enhanced by their intrinsic micropores;
however, their nonconjugated structure leads to inferior electron
transfer. Consequently, the apparent redox kinetics and rate performance
of redox-PIMs are found poorer than some previously reported COFs
and conventional conjugated polymers. Nevertheless, strategies to
enhance ionic transport and improve battery lifetime, even when electron
transfer is limited, broaden the scope of the potential materials
that can be used in energy storage, and may inspire the development
of better materials that show optimal performance in all aspects of
the evaluating matrix. We envision that optimal performance would
be achieved if (1) redox-active PIMs are employed in systems where
ion uptake and transport are more critical (e.g., multivalent metal-ion
batteries[47]), (2) greater electronic conjugation
could be introduced to these microporous polymers, or (3) the concept
of PIMs is extended to other redox chemistries where electronic conjugation
is not a prerequisite for high performance, such as organic radical
polymers.[48,49]Although all structural units employed
in our material design are redox active, there are still inactive
segments present in the structural units of redox-active PIMs (e.g.,
two benzo groups of the triptycene benzoquinone component). Further
enhancement of specific capacity could be achieved based on recent
progress in making multielectron redox quinone materials including
pillarquinone macrocycles[50] and polymers
containing pyrene-4,5,9,10-tetraone[51] and
anthratetronyl sulfide.[46]
Conclusions
The design and synthesis
of redox-active PIMs with accessible microporosity
and high specific capacity involves, first, the use of a triptycene
benzoquinone structural unit to achieve a high density of redox-active
sites while maintaining the highly rigid and contorted structure,
and second, the introduction of tetramethyl groups to provide a sufficient
steric hindrance to restrict rotation about the C–N imide single
bond. Importantly, these redox-active PIMs can be readily solution-processed
into thin films and electrodes with a well-defined microstructure,
enabling enhanced Li+ diffusion and stable cycling performance
in lithium-ion batteries. The strategy of designing redox-active PIMs
with combined properties of intrinsic microporosity, reversible redox
activity, and solution processability may inspire the development
of redox-active polymers with applications in a variety of electrochemical
devices for energy storage, electrochemical sensors, supercapacitors,
and photonic devices.
Authors: Rui Tan; Anqi Wang; Richard Malpass-Evans; Rhodri Williams; Evan Wenbo Zhao; Tao Liu; Chunchun Ye; Xiaoqun Zhou; Barbara Primera Darwich; Zhiyu Fan; Lukas Turcani; Edward Jackson; Linjiang Chen; Samantha Y Chong; Tao Li; Kim E Jelfs; Andrew I Cooper; Nigel P Brandon; Clare P Grey; Neil B McKeown; Qilei Song Journal: Nat Mater Date: 2019-12-02 Impact factor: 43.841
Authors: Mariolino Carta; Richard Malpass-Evans; Matthew Croad; Yulia Rogan; Johannes C Jansen; Paola Bernardo; Fabio Bazzarelli; Neil B McKeown Journal: Science Date: 2013-01-18 Impact factor: 47.728