Daniel N.
Rainer
a,
Aamod V.
Desai
ab,
A. Robert
Armstrong
*ab and
Russell E.
Morris
*ab
aEastCHEM School of Chemistry, University of St Andrews, North Haugh, KY16 9ST, St Andrews, UK. E-mail: ara@st-andrews.ac.uk; rem1@st-andrews.ac.uk
bThe Faraday Institution, Quad One, Harwell Science and Innovation Campus, Didcot, OX11 0RA, UK
First published on 2nd November 2021
The ever-growing global energy demand necessitates, amongst other technologies, advances in materials for electrochemical energy storage such as sodium ion batteries. The recent advent of organic-based electrodes is driven by their tremendous structural versatility and the great potential in developing a green battery cycle. Current research aims to solve remaining obstacles such as a lack of robust, efficient and scalable synthesis procedures. In this vein, we present a fast and sustainable mechanochemical synthesis route towards four sodium carboxylates compounds. Target materials can be obtained in the substantially decreased reaction time of only one hour, while retaining the good electrochemical performance reported for conventionally synthesised compounds. More importantly, no solvent is required for these mechanosynthetic transformations, making this approach attractive with respect to goals in line with green chemistry as well as from an economical point of view. The variety of synthesised compounds hints at possible generalisability of the developed methodology and its potential applicability for many other known compounds, beyond the sphere of rechargeable battery systems.
Traditionally, the materials that are utilised in electrodes of AMIBs are metal oxides or carbons such as graphite.7–10 Although these electrodes perform very well, they come at a price. Oxide-based positive electrodes for LIBs typically contain cobalt, which is accompanied by severe environmental concerns. For the negative electrode, carbon-based compounds are by far the most used active component. In LIBs, graphite shows strong performance with insertion of lithium ions between the graphene layers. In the case of sodium, however, graphite is unfeasible, due to the size mismatch of the ions and the interlayer spacing.11 This obstacle is the main driving force for the quest to find a suitable anode material in NIBs.12,13 Popular alternatives are related carbon-based materials generally referred to as ‘hard carbon’.14,15 These amorphous, mechanically durable solids feature several advantageous properties both in terms of availability and electrochemical performance. Although these materials show great promise, drawbacks in their production, involving high temperatures, as well as issues regarding long term cyclability of batteries based on hard carbon warrant further development of suitable materials. Additionally, the high porosity and surface area of hard carbon necessitate larger volumes of electrolyte for sufficient coverage. This comes with disadvantages in terms of cost but more importantly a significant drop in performance due to a considerable irreversible contribution to the discharge capacity for initial cycles. Overcoming these issues, the field has seen increased interest in the possibility of using organic based electrodes.16–22 Several key advantages can be discerned: (1) immense structural flexibility through the wide range of available and synthesizable chemicals; (2) sustainable production of such reagents from biomass; (3) lower environmental impact compared to (transition) metal oxide-based materials with potentially hazardous components.
For a fully functioning anode, the organic material needs to be complemented with an electrically conductive material, in most cases simply conductive carbon. Homogeneous distribution is achieved by combining them using a binder. There are many available choices; however, water-based binders like sodium carboxymethylcellulose (CMC) or sodium alginate are favourable when considering the health and safety concerns regarding traditionally used components like the mutagenic PVDF (polyvinylidene difluoride) and the concomitantly used solvents such as NMP (N-methyl pyrrolidone).23 Fortunately, most organic-based anodes are compatible with environmentally benign water-soluble binder alternatives, once more increasing their value as candidate materials for industrial-scale production and widespread use.
The demand for environmentally friendly methods in chemistry has seen the re-discovery of mechanical methods as a driving force in chemical synthesis.24–26 Ball milling is probably the most used technique in laboratories, combining a simple setup with the potential for facile upscaling. Compared to manual grinding it has the advantage of exerting much higher forces and high reproducibility. The reagents are milled together using a milling vessel and media made from appropriate materials so as not to interfere with the reaction itself. The high impact of the balls on the reagents facilitates chemical bond breaking and making, leading to new compounds. The reactions are typically much faster compared to an analogous solution-based synthesis. Additionally, the transformation is carried out solvent-free, which means not only savings in terms of cost, but more importantly a significant reduction of produced waste. Mechanochemical synthesis has now been reported in many areas including organic synthesis,27,28 inorganic and main group chemistry,29,30 materials science,31–33 and medicinal chemistry.34 There have also been several reports of employing mechanical forces for the production of inorganic anode materials for batteries.35–37 In contrast, organic compounds for use in energy storage applications have not been investigated so far. The mechanochemical synthesis of coordination compounds based on carboxylic acids has been studied mostly in the construction of metal–organic frameworks (MOFs) where these organic molecules function as linkers between metal(-cluster) nodes.38–40 Traditionally, MOFs are produced through crystallization out of a solution containing both metal ions and the dissolved organic compound. The possibility of making these highly porous compounds with applications in gas storage, drug delivery, and catalysis through mechanochemical means renders them highly attractive from an industrial and large-scale production point of view.41
Coordination polymers of alkali metal ions and carboxylates (lithium, sodium, and potassium salts of carboxylic acids) are an attractive class of materials for anodes in AMIBs.16,42,43 The carboxylate functionality is redox active as it can undergo a reduction, enabling insertion of additional alkali-metal ions. Stabilization of this negatively charged state is facilitated by the presence of a conjugated π-system in the organic backbone such as aromatic rings or conjugated alkenes. Several materials of this type such as sodium terephthalate44–46 have been reported to be suitable active components in negative electrodes.16,18,47 The preparation of these compounds is typically conducted using corrosive sodium hydroxide as well as large amounts of solvent. Additionally, they usually require up to 24 h of reaction time as well as heating, sometimes under reflux conditions. These circumstances have been a hindrance regarding large-scale processing of such materials in an industrial setting. Furthermore, there are also several concerns with respect to environmental impact and energy consumption. Fortunately, all these issues can be addressed by employing mechanochemical methods for the synthesis of the target compounds.
Sodium dicarboxylates have been reported as promising active compounds for anodes of sodium ion batteries (NIBs).16 Taking inspiration from compounds that have been synthesised using solution-based methods, several dicarboxylic acids were selected as potential candidate reagents (Fig. 1).44–46,48–50 Besides the carboxylic acid functionality, these compounds have interesting chemical differences in their backbone that should result in different electrochemical behaviour. In contrast to conventional syntheses, mechanochemical methods feature several advantages, such as low amounts or avoidance of solvents, decreased reaction time, waste reduction and atom efficient protocols.
The reaction of the carboxylic acids towards their sodium salt derivatives hinges on the deprotonation of the carboxylate group, which can then coordinate to the sodium cation. In conventional protocols, this is facilitated by employing sodium hydroxide, as it not only functions as the source of the alkali metal but also as a pH mediating agent. The resulting solution is highly basic; ideal conditions to abstract the proton from acid groups. These highly alkaline conditions coupled with the corrosive reagent itself, however, bring with them concerns in terms of practical handling and safety. In our mechanochemical ball milling approach, we employ benign sodium acetate as the reagent, both in its hydrated as well as anhydrous form. The acetate salt used here is slightly basic, which, combined with the exerted forces from the milling balls, is shown to be sufficient for the transformation of the carboxylic acids to the respective carboxylates.
We present a fast and efficient method for the synthesis of sodium dicarboxylate compounds using mechanochemistry and their performance as electrodes in sodium ion batteries (NIB) is demonstrated (Fig. 2). Non-hazardous sodium acetate and a range of organic dicarboxylic acids such as 1,4-benzene dicarboxylic acid (BDC, terephthalic acid) were milled together using a shaker ball mill, resulting in crystalline coordination compounds. Such a mechanochemical reaction setup ensures facile preparative work and enables rapid conversion of the reagents, in some cases even within minutes. Besides the improvements in required time to prepare the target compounds, using this methodology is also beneficial with respect to amounts of liquid used, as there is no solvent necessary, leading to drastically reduced amounts of waste. Products were utilised as active materials for anodes in sodium ion batteries with performances equal to those of conventionally synthesised compounds. The variety of carboxylic acids used demonstrates the robustness of the method and can be considered precedential for production of functional organic materials for batteries.
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Fig. 2 Schematic representation of the combination of mechanochemical synthesis and organic compounds for the preparation of sustainable anode materials in sodium ion batteries. |
Calcd for Na-BPDC (disodium): C, 58.8; H, 2.8. Found: C, 54.8; H, 3.2.
Calcd for Na-SDC (disodium): C, 61.6; H, 3.2. Found: C, 62.6; H, 3.5.
Calcd for Na-PDC (disodium): C, 39.8; H, 1.4; N, 6.6. Found: C, 39.6; H, 1.6; N, 6.1.
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Fig. 3 Characterisation of mechanochemically prepared Na-BDC. (a) PXRD (simulated NaH-BDC from ref. 52), (b) TGA trace, (c) FTIR, and (d) SEM. |
PXRD analysis also indicates unreacted terephthalic acid (peak at circa 17.4°), however FTIR spectroscopy does not show any bands at high wavenumbers (>3000 cm−1), which would correspond to O–H stretch vibrations from free carboxylic acid groups (Fig. 3c). This indicates that no uncoordinated carboxylic acid remains. A band at 1700 cm−1 is assigned to carboxylic acid COO vibrations, originating either from unreacted starting material, or from the carboxylic acid on the monosodium terephthalate. Thermogravimetric analysis shows a main mass loss at ca. 300 °C, in line with a monosodium salt, compared to thermally more stable disodium compounds.46 TGA also does not indicate the presence of multiple materials, showing clear mass losses and stable plateaus (Fig. 3b) that are consistent with monosodium terephthalate. The identification of the material as NaH-BDC is further supported by elemental analysis (see Experimental section). The obtained material was also analyzed by SEM, which revealed expected agglomerates (>10 μm), consisting of primary particles with dimensions below 1 μm (Fig. 3d).
Although no liquid was added to the above-described synthesis, there is still water present in the form of crystal water of the hydrated sodium acetate used in the reaction. Demonstrating that the liquid is not required for the mechanochemical reaction itself, experiments were also conducted using anhydrous sodium acetate (M/L = 1). Assessing the reaction progression over time, PXRD patterns were collected at various time points (Fig. S2†). Interestingly, there is no discernible change throughout the studied time frame up to 4 h and product is already formed after only 15 min of milling. This reaction was also attempted using jars roughly double in size (internal volume of 25 mL instead of 14 mL) as well as larger and heavier milling balls (12 mm diameter, 7 g). Again, the product phase is formed after milling for 15 min and only small changes are observed upon increasing milling time to 90 min.
Even though the target compound can be obtained without the use of any liquid at all, there are some health and safety concerns, especially at larger scales. The product of this neat milling procedure is a very fine powder, and it is strongly advised to use appropriate masks to prevent inhalation of the fine dust. By adding a small amount of water or using the hydrated sodium salt as a reagent these issues can be avoided. Other syntheses were carried out in the presence of a small amount of liquid originating from either source.
Attempts to synthesise Na-BPDC were again conducted in varying M/L ratios and using water or ethanol as liquid additive (Fig. S3†). Comparison of PXRD patterns of obtained materials with previously published data by Choi et al. indicates the formation of both the monosodiated NaH-BPDC as well as Na2-BPDC.48 Products of experiments with M/L = 2 showed the presence of unreacted acid in FTIR spectra, thus the product of the experiment with M/L = 3 and using ethanol as liquid additive was selected for further analysis and testing. Residual amounts of sodium acetate were initially considered negligible, however, both elemental analysis and electrochemical test runs revealed a substantial amount of electrochemically inactive components, most likely consisting of residual sodium acetate starting material. Thus, a simple washing step with ethanol was conducted to improve the sample purity. For this washed Na-BPDC material, TGA shows only a small mass loss prior to 500 °C, suggesting a high degree of conversion towards the disodium salt instead of a product of incomplete deprotonation. SEM analysis once more shows agglomerates, with primary particles of ill-defined inhomogeneous shape.
Using SDC as the carboxylic acid, the obtained sodium salt with M/L = 2 exhibits a PXRD pattern roughly agreeing with previous reports, and showing some residual starting materials (Fig. S4†).49 The two observed but not fully resolved low angle peaks potentially suggest the formation of both monosodiated and disodiated carboxylate species. Despite several adaptions to synthesis conditions (M/L ratio, liquid additive), no suitable product was obtained. Brief electrochemical test runs showed lower performance than expected, indicating that the product contained a considerable amount of electrochemically inactive material as was the case for Na-BPDC. A washing step with ethanol leads to a product showing a cleaner PXRD pattern and no sign of remaining sodium acetate. FTIR analysis of this material indicates the successful formation of Na-SDC with no sign of free acid groups. The TGA trace shows mass losses in the range of 250–400 °C, suggesting the presence of a monosodium carboxylate species in addition to Na2-SDC. Elemental analysis also suggests some, albeit a small amount of impurity, however, the result overall is in line with Na2-SDC. Based on the results for Na-BDC and Na-BPDC, as well as following previously published data,49 however, this sample was still deemed appropriate for electrochemical cycling studies as shown below. As with the previously described Na-carboxylates, the morphology of the material is that of large agglomerates where in the case of Na-SDC, the primary particles are rod-like with a length of up to 1 μm.
The targeted Na-PDC was also obtained using the above mechanochemical approach and analysed similarly (Fig. S5†). From the set of conducted experiments, optimised conditions were found to be M/L = 2, ethanol as liquid additive, and 60 min of milling time as judged by PXRD pattern analysis of the products. Unreacted carboxylic acid is not observed in the obtained FTIR spectra due to the absence of O–H bands around 3000 cm−1, confirming conversion of available organic reagent. A weak band at 1724 cm−1 may originate from a small amount of unreacted acid but bound to the bulk material. TGA analysis shows the main mass loss at 500 °C, supportive of complete deprotonation of both carboxylic acids and the sole presence of a disodium salt. Similarly, the measured and calculated atom percentages agree well with a disodium pyridinedicarboxylate. In contrast to the three previously used acids, the nitrogen containing PDC appears to be more reactive, and the acidic protons more easily abstracted. This is thought to be caused by the nitrogen atom increasing the basicity of the system, thus aiding in the deprotonation reaction.53–55 SEM investigation reveals the material consists of irregularly shaped particles smaller than 1 micron, clumping together to larger agglomerates as seen for the other carboxylates.
Four different sodium carboxylate compounds are obtained using a rapid mechanochemical synthesis route. In addition to the time reduction, the important factor here is that all target materials can be obtained without bulk solvent and only reagent levels of liquid are used. This is considered to be a major improvement over conventional synthesis methods, with liquid waste reduced when using this mechanochemical approach, beneficial both in terms of cost but more importantly with respect to the principles of green chemistry.56,57 These conditions promise excellent applicability for large scale processing using, for example, extrusion techniques, in which both mechanosynthesis as well as a subsequent drying/heating step can occur concomitantly in a single processing unit.41,58–60
The electrochemical performance of the compounds was evaluated by assembling coin cells with sodium metal as the counter electrode. Cyclic voltammetry (CV) was initially recorded for 5 cycles between 0.01–2.5 V at a scan rate of 0.1 mV s−1. A single redox couple was observed for Na-BDC with a reduction peak at ∼0.14 V that shifted to the stable potential of 0.29 V in subsequent cycles (Fig. S6†). The oxidative peak at 0.55 V essentially remained unaltered during the experiment. A low voltage minor redox couple was seen which could be ascribed to contribution from conductive carbon used in the preparation of the electrode (Fig. S7b†). Galvanostatic charge/discharge cycling was initially recorded at a current density of 100 mA g−1. The first discharge for Na-BDC exhibited a large irreversible capacity, corresponding to the solid-electrolyte interphase (SEI) formation, as seen commonly for anode materials.61,62 Additionally, the transformation of the monosodium terephthalate to the disodium form may contribute to this effect.46 For the subsequent cycle, a discharge capacity of ∼270 mA h g−1 was observed with a coulombic efficiency greater than 98% (Fig. 5a). The reversible capacity retention from the 2nd cycle was seen to be 86% over 100 cycles. These values are in close agreement with the performance seen previously for Na-BDC synthesised by solution-based methods (Table S2†).44–46 The contribution to the capacity by the conductive carbon used in the preparation of electrode was estimated to be ∼37 mA h g−1 (Fig. S7†). Encouraged by these results, the rate performance was evaluated for this compound by increasing current rate from 25 mA g−1 to 1000 mA g−1 in 5 steps and back to 25 mA g−1. The compound fully recovered its capacity even after cycling at a high current density (Fig. 5b).
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Fig. 5 (a) Galvanostatic cycling performance for Na-BDC at 100 mA g−1 cycled between 0.01–2.5 V. (b) Rate performance for Na-BDC, cycled 5 times at each current density. |
Pristine solid of Na-BPDC from mechanochemical reaction exhibited slightly lower cycling capacities (Fig. S8†). Therefore, a washing step was introduced, and electrodes and other electrochemical studies were performed using the washed product. CV profiles exhibited a strong reduction peak at 0.2 V in the first discharge that shifted to a more positive potential and stabilised at 0.32 V in the subsequent cycles (Fig. S8†). The voltammogram comprised two oxidation peaks at 0.5 V and 0.65 V that remained unaltered. These peaks suggested the presence of both the monosodiated and disodiated forms as seen in the earlier example.48 Galvanostatic cycling studies showed a first discharge capacity of 304 mA h g−1, that stabilised from the 2nd cycle onwards with a capacity retention thereafter of 84% over 100 cycles (Fig. S8†). The coulombic efficiency required a few cycles before stabilising, which could be ascribed to the sodiation of the monosodium component. The material exhibited stable rate performance with complete recovery of capacities at 25 mA g−1 after step wise cycling up to a high current rate of 1 A g−1 (Fig. S9†).
Similar to Na-BPDC, for pristine Na-SDC we observed marginally lower specific capacity and its retention (Fig. S10†), indicating presence of an inactive component hindering cycling stability. Electrodes were consequently prepared after a washing step for the pristine material. The voltammogram, shown in Fig. S10,† exhibited a single step redox couple corresponding to the active material. A reduction peak at 0.33 V had a slight shift and stabilised at 0.39 V in the subsequent cycles. The oxidative peak seen at 0.67 V in the first cycle, remained relatively unchanged. It is, however, noteworthy that no noticeable humps or secondary peaks were observed from the second cycle onwards that were seen in the previous report.49 This implies absence of any by-product or amorphous solids and reiterates the advantage of mechanochemical synthesis in terms of cleaner conversion. During galvanostatic cycling a discharge capacity of ∼233 mA h g−1 for the 2nd cycle was observed, with a moderately stable capacity retention over 100 cycles (Fig. S10†).49 The rate performance for the compound exhibited complete retention of the capacity at low rate (25 mA g−1), after cycling over multiple current densities (Fig. S11†). Notably, the cycling stability and capacities for Na-SDC are comparable to the corresponding previous study, despite reduction in the amount of carbon additive (Table S2†).
Unlike other examples in this work, the CV profile for Na-PDC had two discernible peaks in both the reduction and oxidation cycles (Fig. S12†). As reported earlier by Padhy et al., this corresponds to insertion of Na+ ions in two steps involving the interaction with the pyridyl N-atom at higher voltage and subsequent insertion to the carboxylate group at lower potential.50 During galvanostatic cycling a relatively low irreversible capacity and much higher coulombic efficiency (75%) was seen for the first cycle (Fig. S12†). In the following cycle, a discharge capacity of ∼258 mA h g−1 was observed which was highly reversible and reasonably stable over 100 cycles. This compound also demonstrated very stable rate performance with almost complete recovery of capacity at 25 mA g−1 after cycling in multiple steps up to 1 A g−1 (Fig. S13†). It is also worth noting that in the current work the capacity retention is achieved with the use of CMC as the binder and lower content of conductive carbon (Table S2†). Avoiding the previously discussed issues accompanying the use of PVDF which has been used as binder in published reports while displaying a comparable electrochemical performance is to be considered a promising aspect in attempting to make the production of these anode materials less hazardous.
The mechanochemical methodology applied in this project should serve as a blueprint for further studies. The variety of used carboxylic acids, including nitrogen containing PDC, demonstrates the versatility of the method and it promises to be applicable for other reagents.
Electrochemistry and performance of organic electrode materials is still at an early stage of practical applications and somewhat less competitive to the benchmark hard carbon, but apart from inherent advantages of being environmentally friendly, such widely applicable and facile preparation methods of active materials can only spur interest and facilitate its development.
Footnote |
† Electronic supplementary information (ESI) available. See DOI: 10.1039/d1ta07897f |
This journal is © The Royal Society of Chemistry 2021 |