Lucas
Ueberricke
a,
Felix
Mildner
a,
Yuquan
Wu
b,
Elisa
Thauer
b,
Tom
Wickenhäuser
b,
Wen-Shan
Zhang
c,
Yana
Vaynzof
bd,
Sven M.
Elbert
a,
Rasmus R.
Schröder
c,
Rüdiger
Klingeler
*b and
Michael
Mastalerz
*a
aOrganisch-Chemisches Institut, Ruprecht-Karls-Universität Heidelberg, Im Neuenheimer Feld 270, Heidelberg 69120, Germany. E-mail: Michael.mastalerz@oci.uni-heidelberg.de
bKirchhoff-Institut für Physik, Ruprecht-Karls-Universität Heidelberg, Im Neuenheimer Feld 227, Heidelberg 69120, Germany. E-mail: klingeler@kip.uni-heidelberg.de
cBioQuant, Ruprecht-Karls-Universität Heidelberg, Im Neuenheimer Feld 267, Heidelberg 69120, Germany
dTechnical University of Dresden (TUD), Integrated Center for Applied Physics and Photonic Materials (IAPP) and Center for Advancing Electronics Dresden (cfaed), Dresden 01062, Germany
First published on 2nd March 2023
Redox active, insoluble pyrene tetraone based dendritic porous polymers were synthesized by using different catalyst loadings and work-up procedures. The dendritic polymers were investigated by gas sorption analysis for their porosity and characterized with respect to their properties as active material in cathodes of lithium ion secondary batteries. Electrochemical measurements by means of cyclic voltammetry and galvanostatic cycling show reversible redox activity and specific capacities of up to 137 mA h g−1 with a capacity retention of 86% after 50 cycles.
Scheme 1 Examples of PTO based materials used as cathodes and corresponding capacities and capacity retentions. |
By covalent binding PTO to an sp2-carbon surface (PYT-C), Karunadasa et al. achieved a capacity of 123 mA h g−1 and 55% retention after 100 cycles at 66 mA g−1.13 Two linear polymers PPTO and PEPTO with capacities of 234–244 mA h g−1 (57–64% of theoretical values) and 74–79% retention after 47 cycles were reported by Zhang and coworkers in 2018.18 One year later, a 2D boroxine covalent organic framework (COF) was published by the same group. PPTODB-COF showed a capacity of 198 mA h g−1 (58% of the theoretical value) and 68% retention after 150 cycles at 20 mA g−1.20 Another recently reported pyrene tetraone based COF by Zheng et al. showed reversible capacity of 225 mA h g−1 and an exceptional long-term cyclability (retention rate 98.0% after 10000 cycles) in aqueous zink–organic batteries.28 Carbonyl-based composites with carbon nanotubes reached capacities of 438 mA h g−129 and 416 mA h g−1.30 Despite this progress some challenges still remain. Except for PPYT, the experimental capacities are much smaller than theoretically possible and usually reach only little more than 50% of the theoretical capacity, indicating that only half of the redox-active sites are actually utilized. This still leaves room for improvement, as capacities higher than 200 mA h g−1 are desirable.
Another parameter, which tends to be much lower in organic as compared to inorganic materials, is the rate capability and often slow redox kinetics limits the power density. Both might be attributed to the lack of Li-ion channels in many organic materials that allow efficient ion diffusion.14 Thus, porous structures seem to be beneficial and materials with high surface areas have shown improved device performance, for example in metal organic frameworks (MOFs)5,31–34 or covalent organic frameworks (COFs).5,35–38 In the examples given in Scheme 1 pores could be seen by electron microscopy (EM) imaging for PPYT and for PYT-C a high-surface carbon source was used. PPTODB-COF most likely has channels for Li+ diffusion due to its rigid 2D framework, whereas PPTO and PEPTO are most likely non-porous. However, the porosity of none of those materials was investigated by gas sorption analysis.
Here we present the synthesis of an insoluble porous dendritic polymer network (D-PTO), where PTO monomers are connected via the meta-positions of a benzene unit. We envisioned, that the rigidity of this structure prevents close-packing, thereby opening up channels for ion and electrolyte diffusion. At the same time, we expected low solubility. The porous structure was simulated by MM2 optimization of an oligomeric cutout (Fig. 1). D-PTO is expected to form a rigid, dendrimer-like structure, where the individual branches form helical channels with an approx. diameter of 1.4 nm. The porosity was investigated by gas sorption and the material was investigated regarding its performance as cathode material in LIBs.
DFT calculations (B3LYP: 6-311++G**) showed that the HOMO orbital (EHOMO = −6.8 eV) is delocalized over the whole aromatic backbone, while the LUMO orbital (ELUMO = −3.8 eV) is located only on the pyrene tetraone unit.
By comparison of FT-IR spectra (Fig. 3), both ketal 1 and the D-PTKs showed similar absorption patterns with characteristic C–H valence vibration bands at ∼2954 cm−1 and 2864 cm−1, indicating the presence of saturated C–H groups. Similarly, an intense band at ∼1098 cm−1 can be attributed to the C–O valence vibration, thus showing the presence of ketal groups. The spectra of tetraone model compound 2 and D-PTO also had very similar peak patterns. An intense band at ∼1672 cm−1 in both spectra proves the presence of carbonyl functions. At the same time the C–H valence vibration bands vanished for D-PTOs, indicating the loss of the ketal units.
D-PTO-2a and its precursor material were investigated by 13C MAS NMR and compared with 13C NMR spectra of model compounds 1 and 2 obtained from solution (Fig. 4). The signal at ∼93 ppm is indicative for the ethylene bridges Ca and can be found in both model compound 1 and D-PTK-2a. After deprotection to D-PTO-2a this signal vanishes almost completely and a new signal at δ = 181.9 ppm, characteristic for the carbonyl carbons Cb, appears. This shows that except some trace amounts, the acid treatment effectively hydrolyzes the ketal groups.
Fig. 4 13C CP MAS NMR spectra (10000 Hz) of D-PTK 2 (a), D-PTO 2a (c) and 13C NMR spectra (CDCl3, 150 MHz) of model compounds 1 (b) and 2 (d). |
The elemental composition and purity of the D-PTO materials was determined by elemental analysis and XPS measurements. For D-PTO-1 trace residues of two different Pd species from residual catalyst traces and bromide (below 1% each) were found, indicating that some bromide groups remained unreacted (Fig. S5 and Table S3, ESI†). The elemental analysis for carbon and hydrogen is in good agreement with the theoretical values, when adsorbed water is considered. XPS measurement on D-PTO-2 and D-PTO-3 showed no traces of Pd, and also no bromide could be found (Fig. S6–S8 and Tables S4–S6, ESI†), indicating that lower catalyst loading is beneficial for material purity. Boron containing species (1.49%) found in D-PTO-2a could be completely removed by Soxhlet extraction. The extraction step is therefore also beneficial for the degree of purity.
All D-PTOs were characterized by TGA under nitrogen atmosphere. Decomposition of the materials were observed in between 285–312 °C, after an initial weight loss up to ∼100 °C due to solvent evaporation. The decomposition temperature did not show a clear correlation to reaction conditions (i.e., catalyst loading) and differ for each batch. Table 1 and Fig. 5 summarize the properties of the prepared materials.
# | Sample | T decomp [°C] | SABET [m2 g−1] | SALangmuir [m2 g−1] | d Pore,max [nm] | V Pore [cm3 g−1] | V mikro [cm3 g−1] | S mikro [%] |
---|---|---|---|---|---|---|---|---|
a Decomposition temperature determined by TGA under N2 atmosphere with 10 K min−1. b Determined by QS-DFT (Kernel: N2 on carbon at 77 K, sphere/cylindrical pores). c Determined by t-plot method. d Determined by t-plot method as (SAmicro/SABET) 100. | ||||||||
1 | D-PTO-1 | 285 | 290 | 333 | 0.67 | 0.187 | 0.070 | 59 |
2 | D-PTO-2a | n.d. | 472 | 531 | 1.27 | 0.264 | 0.136 | 71 |
3 | D-PTO-2b | 301 | 537 | 612 | 1.22 | 0.306 | 0.146 | 67 |
4 | D-PTO-3 | 312 | 676 | 767 | 1.26 | 0.325 | 0.219 | 78 |
The morphology and crystallinity of D-PTO was investigated using SEM imaging (Fig. 5a) and PXRD (Fig. S10, ESI†). Both methods reveal that the D-PTOs are mostly amorphous (see the ESI†). However, D-PTO-1 shows two peaks at 2θ = 40 and 46°, which are either absent or very weak in the other materials.
Gas sorption analysis with nitrogen at 77 K of D-PTO-1 showed a type-I-isotherm with a specific surface area (BET)41 of SABET = 290 m2 g−1, revealing the porous nature of the material (Fig. 5b and c). By QS-DFT calculation (Kernel: N2 on carbon at 77 K, sphere/cylindrical pores, adsorption branch, fitting error: 0.420%)42,43 a pore diameter of dpore,max = 0.67 nm is obtained (Fig. 5c). The microporous surface area is 59% of the overall surface area as calculated by the t-plot method44–46 with a pore volume of Vpore,micro = 0.07 cm3 g−1.
For D-PTO-2a an increased specific surface area of SABET = 472 m2 g−1 with a doubling in pore diameter (dpore,max = 1.27 nm) compared to D-PTO-1 was found (Kernel: N2 on carbon at 77 K, sphere/cylindrical pores, adsorption branch, fitting error: 0.755%). A larger fraction of microporous surface area (71%) and an increased pore volume (Vpore,micro = 0.136 cm3 g−1) was estimated. D-PTO-2b, which was prepared from D-PTO-2avia Soxhlet extraction, shows a slightly increased specific surface area (SABET = 537 m2 g−1), and pore volume (Vpore,micro = 0.146 cm3 g−1). The pore diameter (Kernel: N2 on carbon at 77 K, sphere/cylindrical pores, adsorption branch, fitting error: 1.033%) was slightly decreased (dpore,max = 1.22 nm), as well as the microporous surface fraction (67%).
Finally, for D-PTO3 again an increase in specific surface area (SABET = 677 m2 g−1) was measured and a similar pore diameter as D-PTOs 2a and 2b (dpore,max = 1.26 nm) was found (Kernel: N2 on carbon at 77 K, sphere/cylindrical pores, adsorption branch, fitting error: 1.486%). The material shows the highest microporous pore volume (Vpore,micro = 0.219 cm3 g−1) and surface fraction (78%) of all materials presented at hand. On first glance, these findings indicate that reducing catalyst loading improves the surface properties in terms of higher specific surface area, larger pore volume and microporous fractions. However, in control experiments batch-to-batch variations occur, depending on the overall experimental conditions. Table 1 summarizes the gas sorption data.
Scheme 3 Redox mechanism of pyrene tetraone.8 |
Assuming that each carbonyl unit can uptake one electron, the maximum capacity of PTO is 409 mA h g−1, whereas 360 mA h g−1 were achieved experimentally by Liang et al.8 Due to its slightly higher molecular weight, the theoretical maximum capacity of D-PTO is 345 mA h g−1. Electrodes were fabricated from D-PTO-2a, -2b and -3 (see the ESI† for details) and electrochemical studies were performed using Swagelok-type two-electrode cells.47
2-Electrode half-cell cyclic voltammograms were recorded in a potential range between 1.5 and 4 V (4.5 V in case of D-PTO-3) (Fig. 6). The cyclic voltammogram of the composite electrode of D-PTO-2a shows two clear redox pairs located at 2.42 and 2.85 V vs. Li/Li+, with overpotentials of 0.1 and 0.02 V, respectively (Fig. 6a). This indicates a two-step redox process, similar to what is found in the CVs on model compound 2 (see Fig. 2).
The redox pair at 2.8 V splits into a two-step process after the first cycle, indicating changes of electrochemical properties at the polymer–carbon interface. Similarly, for D-PTO-2b two pairs of separated redox peaks are observed as well (Fig. 6b). The intensity of the redox peaks decreases upon cycling, which indicates degradation of the redox active sites. The origin of this degradation is unclear, especially since it is occurring only for D-PTO-2b and not with D-PTO-2a. At the same time, for both materials the overpotential of the redox pair decreases to approximately 0.1 V after the first cycle. This might be rationalized by a conformational rearrangement of the dendritic structure during the first cycle, which increases π-stacking between D-PTO and carbon black and thus improves bulk conductivity.
The oxidation peak at 3.8 V and reduction peak at 1.5 V are consistent with the redox activity observed in the precursor dendrimer D-PTK. Traces of residual tetraketal units, arising from incomplete hydrolysis in the second step of the synthesis (see Scheme 1) have already been observed in the solid state 13C NMR spectroscopy (Fig. 4) and can thus be expected to be seen in the CVs as well. For D-PTO-3 only one highly reversible redox peak pair at 2.8 V with a low overpotential of 0.05 V is found (Fig. 6c). During cycling the oxidation peak splits into two signals similar to what is observed for the other two materials.
The charge and discharge curves of the D-PTO composite electrodes were obtained at a current density of 100 mA g−1 in the potential range between 1.5 V (for D-PTO-3 1.7 V) and 4 V (Fig. 6d–f). D-PTO-2a shows discharge plateaus at 2.3 V and 2.9 V vs. Li/Li+, which corresponds well with the reduction peaks in the CV curves. The specific discharge capacity amounts up to 123 mA h g−1 in the second cycle and reaches a maximum of 137 mA g−1 in cycle 11, which can be attributed to the expansion of transfer channels for Li cations and the π-stacking effect. Assuming a theoretical capacity of D-PTO of 345 mA h g−1, approximately 0.40 Li+ ions are taken up per tetraone unit in cycle 2. After 50 cycles, the capacity is reduced to approx. 106 mA h g−1, which corresponds to a retention of 86% relative to the capacity in the second cycle. The charge–discharge profiles of D-D-PTO-2b (Fig. 6e) shows two broad discharge plateaus at 2.7 V and 2.2 V, corresponding well with reduction peaks in the CV curve. There is a narrow discharge plateau at 1.8 V, consistent with the small peak at 1.9 V in the cyclic voltammogram. One broad charge plateau between 2.5 V and 3.0 V is observed, in agreement with the oxidation signals from CV. The specific discharge capacity in the second cycle amounts to 115 mA h g−1, corresponding to a utilization of the carbonyl groups in the redox process of approx. 33%. The capacity retention is 41% (47 mA h g−1) after 50 cycles.
The highest capacity is measured for the D-PTO-3 composite cathode which features 143 mA h g−1 in the second discharge cycle. This implies that approx. 41% of the carbonyl groups are utilized in the redox process. However, a continuous decay occurs upon cycling with a capacity retention of 70% (100 mA h g−1) after 50 cycles.
Table 2 summarizes the main parameters describing the electrochemical performance of the composite electrode in Li-ion half-cells. The D-PTO-2a electrode exhibits the best performance overall, especially regarding the cycling stability seen in the CV curves and was thus examined in more detail. In order to interpret the redox behaviour of the electrode in more detail, cyclic voltammetry measurements were conducted in different potential ranges on the same electrode in subsequent cycles.
The initial six cycles were performed in the range 2.5–3.5 V where only one redox pair is observed. The working window was then expanded to 1.5–4.0 V in cycles 7 and 8 and then narrowed down to 2.5–3.5 V again in cycles 9 and 10 (Fig. S13, ESI†). In both voltage ranges splitting of the peaks is observed. This finding reveals a dependence of the redox behaviour on the applied voltage range. The splitting of the redox pair at 2.8 V relates to the underlying process of the redox pair at 2.4 V since it only occurs after cycling to lower voltages.
The cycling stability of D-PTO-2a was further investigated by a long-term galvanostatic cycling measurement at 100 mA g−1 for 130 cycles (Fig. 7a). Similar to what is observed in Fig. 6d, the specific discharge capacity initially increases before starting to fade after cycle 10 (cf.Fig. 6d). In addition, the data imply moderate fading for the subsequent 90 cycles before a rather stable capacity level is reached. Even after 130 cycles, a discharge capacity of 86 mA h g−1 is measured, which corresponds to a capacity retention of 70% relative to the second cycle. The results of the corresponding rate capability test for D-PTO-2a are shown in Fig. 7b. The material delivers average capacities of 225, 140, 110, 52, 41, and 15 mA h g−1 at current densities of 10, 50, 100, 500, 1000 and 10000 mA g−1, respectively (Fig. 7b). A recovered capacity of 120 mA h g−1 is achieved when the current density is reverted back to 10 mA g−1.
To relate the electrochemical performance of the here presented D-PTO-2a to the literature, Table 3 lists the electrochemical performances of various organic cathode materials. The comparison clearly shows that the D-PTO-2a competes well with different quinones as well as other redox-active polymers as it exhibits comparable initial discharge capacity and retention after 50 cycles.
Group | Material | Potential range vs. Li/Li+ (V) | Current density (mA h g−1) | Initial discharge capacity (mA h g−1) | Retention/cycle no. | Ref. |
---|---|---|---|---|---|---|
Values marked with *are read off from the graphs. | ||||||
Quinones | D-PTO | 1.5–4.0 | 100 | 137 | 86%/50 | This work |
PPYT | 1.5–3.5 | 263 | 231 | 94%*/50 | 8 | |
PYT-C | 1.5–3.4 | 74 | 123 | 65%*/50 | 9 | |
PPTO | 1.5–3.5 | 100 | 234 | 74%/47 | 10 | |
Imides | PTCDA-HP | 1.5–3.5 | 110 | 130 | 84%/50 | 15 |
Carbonyl derivatives | N-Cyanamide | 1.8–3.2 | 207 | 137 | 89%*/50 | 20 |
Thioether | PPDT | 1.4–4.0 | 50 | 180 | 70%/20 | 31 |
Triphenylamines | PPT1N | 2.6–4.5 | 20 | 129 | 91%/50 | 39 |
TEMPO | PTMA | 3.0–4.0 | 111 | 133 | 90%*/50 | 43 |
The prepared amorphous materials show BET surfaces between 290 and 676 m2 g−1. The materials were used to fabricate composite electrodes, which were investigated regarding their electrochemical performance in lithium-ion secondary batteries. Specific capacities of up to 137 mA h g−1 and a capacity retention of 86% after 50 cycles were measured. Moreover, favorable kinetics with high reversibility of the redox processes were observed. The results show that connecting the PTO monomers via the meta-positions of a benzene unit is a successful strategy to overcome the dissolution issue of PTO. The cycling stability of the as-prepared D-PTO is significantly improved compared to PTO.8 In comparison to most other PTO-based materials (Scheme 1) the as-prepared D-PTO is also more cycle stable. Only the PPYT prepared by Yoshida and coworkers by attaching the PTO to a polymethacrylate backbone via an amide linkage, exhibits even higher cycling stability.12 However, the low carbonyl utilization of only 40% still leaves room for improvement of the specific capacity.
Footnote |
† Electronic supplementary information (ESI) available. See DOI: https://doi.org/10.1039/d2ma01039a |
This journal is © The Royal Society of Chemistry 2023 |