Author: Eshaal Alavi
Two of the biggest environmental advantages that SIBs have is that they are able to avoid the use of critical materials and aid in waste management. With over 220 billion tonnes of agricultural residues (waste from agriculture) and 300 million tonnes of plastic produced every year (and only 10% recycled), the production of HC anodes can be a significant contributor to upcycling waste that is otherwise unexploited (Liu, 2021). For example, a company called Kuraray uses coconut shells in order to create its HC anodes, called ‘Kuranodes’. These would otherwise be incinerated (increasing greenhouse gas emissions) or left in landfills (Liu, 2022).
In order to assess and compare the environmental impacts of HC production with graphite’s, life cycle assessments (LCAs) are used. They quantify different types of impacts such as:
- Global Warming Potential (GWP) – how much greenhouse gas is emitted (measured in kg of CO2)
- Acidification Potential (AP) – how much a process acidifies the environment, like through acid rain
- Abiotic Resource Depletion (ADP) – measures depletion of non-renewable resources
- Human Toxicity Potential (HTP) – measures how harmful substances are to human health.
- Photochemical Ozone Creation Potential (POCP) – measures the potential of chemicals to form ground-level ozone, which is harmful to humans, plants, and is also a potent greenhouse gas.
According to an LCA published by the Royal Society, HC anodes produced from a biomass precursor have a smaller environmental impact than graphite, in all the impact categories they studied, when comparing anode production per kilogram (Liu, 2021). Excluding GWP, there is a reduction in impact of over 90% in all categories (fig. 1). The LCA also compared two methods of synthesis: method A composed of HTC followed by pyrolysis (the method outlined earlier) and method B consisted of only pyrolysis. In addition to this, the pyrolysis was carried out at two different temperatures (fig. 2) of 1000°C (A2 and B2) and 1300°C (A1 and B1). It was found that the anodes, A1 and B1, produced at 1300°C, had a higher yield (33-40%) and a much better electrochemical performance, with a charge capacity that was 74-80% of the capacity of LIBs (372mAh/g). Overall, direct pyrolysis, performed better in all categories, apart from GWP.
A major reason for the GWP using method A (fig. 1), is electricity use – for both step 1 (HTC) and step 2 (pyrolysis). In order to reduce this, the study examined heat recycling, which is commonly used to save energy in chemical plants, for reactions which have a two-step synthesis (fig. 3). It considered how the overall GWP would be reduced if 30% of the heat was recycled from HTC or if 50% was recycled (fig. 3). It was found that the overall GWP decreases from –30% (without recycling) to –41% (when 50% was recycled).
Figure 1: environmental impacts of HC anode from direct pyrolysis (B1) compared with HTC, followed by pyrolysis (A1). Both methods show a decrease in impacts when being compared to graphite.
Figure 2: The two methods used in the study (A and B). A1 and B1 refer to pyrolysis at 1300°C and A2 and B2 at 1000°C.
Figure 3: Heat recycling scenario analysis for hard carbons in System A and System B for SIBs. A1-R1 scenario (assume 30% HTC energy recycling) and A1-R2 scenario (assume 50% HTC energy recycling) are compared.
However, a key issue with this type of LCA is that it does not account for the full-cell SIB with all its components, nor does it consider its energy density, efficiency, or lifetime. In other words, comparing anodes solely based on mass (per kilogram) overlooks the fact that SIBs typically have a lower energy density than LIBs, so a larger mass of material is needed for the same energy capacity (energy storage). Consequently, even if the per-kilogram impact of HC is less than that of graphite, this does not necessarily hold true when comparing impacts based on per unit energy storage (per kilojoule). For instance, let’s assume the GWP for HC is 4 kg CO2 eq/kg, and for graphite it is 5 kg CO2 eq/kg (fig. 4). But in order to achieve the same energy storage (for example, of 1kWh), 1.5 kg of HC is required for every 1 kg of graphite (if we assume the SIB has a lower energy density compared to the LIB). The GWP for HC and graphite based on energy storage would be 6 kg CO2 eq/kg and 5 kg CO2 eq/kg, respectively. Therefore, not accounting for energy density and energy capacity can result in misleading conclusions about the relative environmental impacts of different anode materials.
Figure 4: an example table showing how energy density affects environmental impacts.
Example | Hard Carbon | Graphite |
GWP per kg (CO2 eq/kg) | 4 | 5 |
Mass for 1kWh energy capacity (kg) | 1 | 1.5 |
GWP per kWh (CO2 eq/kg) | 6 | 5 |
Another problem with this LCA is that it does not account for the full-cell battery’s lifetime. Frequent cell replacements can significantly increase the overall environmental impact, even if the per-cell impact is lower for the SIB compared to the LIB (assuming each cell has the same energy capacity). For example, suppose an SIB has a GWP of 40 kg CO2 eq/kWh, while an LIB has a GWP of 50 kg CO2 eq/kWh. Although the SIB has a lower GWP per cell, it also has a shorter lifespan of 2000 cycles compared to the LIB’s 3000 cycles. Assuming both batteries undergo 2 charge-discharge cycles per day, over a period of 12,000 days (or 6,000 cycles), the LIB would need to be replaced once, while the SIB would need to be replaced twice. When we consider the GWP for this time period, the total GWP over 12,000 days is 100 kg CO2 eq for the LIB and 120 kg CO2 eq for the SIB. Therefore, the higher frequency of SIB replacement results in a greater overall GWP. This trend is also evident in other impact categories.
A third concern with this LCA is that it does not examine the impacts associated with the complete chemistry of the SIB, including all its components. For instance, factors such as the choice of cathode material, electrolyte, binder, and separator can dramatically influence both the overall environmental impact per cell and its impact over its entire lifetime. Some cathodes and electrolyte salts use critical raw materials that can significantly increase the ADP of the overall cell. Moreover, the processing of these components can substantially alter the GWP.
An LCA published by the Royal Society of Chemistry incorporates all these variables, by taking into account the full-cell chemistry, use-phase and recycling (Peters, 2021). They compare five different SIB chemistries (which use HC anodes), as well as two common LIB chemistries (which use graphite anodes), in their study. All the cells used the same binders (which is what glues the electrode material together) and similar electrolytes, so that the only things affecting the LCA was the cathode, anode and choice of ions. First, they compared the environmental impacts caused by the production of these batteries, for a 1kWh energy capacity (fig. 5). Secondly, the study incorporated the use-phase, cell-replacement and recycling into the LCA (fig. 6).
While examining the impacts of producing a cell of 1kWh of capacity (fig. 5), it was observed that the reason for a high GWP for NaPBA and NaNMC was due to a low energy density. This meant they required larger battery cells (therefore more material, which needs to be processed) for the same energy capacity of 1kWh. Furthermore, across all the SIBs, process heat (fossil fuels burnt for heat – this is often natural gas) is the main reason for greenhouse gas emissions (GWP). It is estimated that 82-94% of the manufacturing energy is process heat. Therefore, decarbonising HTC and pyrolysis, by making it more efficient, is important, in order to decrease GWP. In terms of ADP and HTP, most of the SIBs performed well in comparison to the LIBs. In figure 5, you can see how ADP varies depending on the cathode material, as well as the electrolyte.
Figure 5: Environmental impacts of production of five SIB chemistries and two LIB chemistries (per 1kWh of energy storage)
Figure 6: Overall environmental impacts, when considering production, use-phase, cell-replacement and recycling (for 1kWh of energy storage)
To assess the overall impact of each cell throughout its lifetime, the study evaluated the impacts of each cell in a stationary storage application (fig. 6) – this is where energy is stored in a fixed location for later use, like with renewable energy systems. In the use-phase (orange-pink section), the source of energy used (PV vs European grid mix) to charge the batteries and its impacts were also taken into account. Unsurprisingly, the GWP and AP are much higher for batteries which were powered by the grid, which is primarily driven by fossil fuels. However for PV, the ADP is much higher, as many critical metals are used in order to construct the solar cells. Interestingly, it was found that efficiency seems to quite significantly affect the use-phase impacts. If we look at LiFP and LiNMC, you can see that for all the categories, LiFP seems to have a lower use-phase impact. However, the difference in efficiency between the two is minute with only a 1% discrepancy (92% and 93%). Although the efficiencies of SIBs and LIBs are assumed to be quite similar, improvements in this aspect for SIBs can greatly reduce environmental impacts in the use-phase.
Impacts from cell replacement (grey section) depend on cycle life, which was mentioned earlier. In general, the higher the cycle life, the lower the impacts from replacement. LiFP and NaPBA were assumed to have a life of 7000 cycles whereas the others were assumed to have 4000 cycles. For this reason, they generally have the lowest impacts when considering replacement.
The yellow dots indicate what the LCA would look like without recycling the components of the battery. However, in reality, most batteries are not recycled in the way they should be and electrolyte recovery is rarely carried out, as most recycling facilities do not possess an advanced enough treatment process. If we take this into consideration, the SIBs (apart from NaNMC) significantly outperform the LIBs, in terms of ADP.
Overall, LiFP cells, despite having relatively high impacts in the production phase (fig. 5) seem to have the lowest impacts (apart from in ADP) over its full life cycle due to its high efficiency and lifetime. In contrast to this, NaNMC performs the worst in all categories due to its low energy density and the use of critical materials in its cathode. Therefore, either the energy density or the cycle life must be substantially increased for SIBs to compete with current LIB chemistries (efficiency is already similar to LIBs).
However, despite the more detailed assessment of different battery chemistries, there are still a lot of assumptions made in this LCA as well. Firstly, there is a lack of reliable data for efficiencies, GWP values and cycle lives. In addition, the values for efficiency and energy density rely heavily on the shape of the cells and thickness of the electrodes, which was not considered in detail when obtaining the values used in this LCA. Secondly, the use-phase impacts depend largely on the specific application (e.g. EVs vs grid storage). Thirdly, the recycling model used for the battery components is specifically for LiNMC cells therefore ideally a more optimised process for recycling should be used for the other cell chemistries. These are a few of the reasons why you can see such large uncertainties (large error bars in fig. 6) in this LCA.
As Sodium ion batteries evolve, they are set to become competitive with Lithium ion batteries in terms of environmental impact, energy density, and lifetime. While SIBs are not yet as advanced as LIBs, companies are increasingly investing in SIB technologies, leading to improvements in energy density and battery life. With continued development, SIBs are expected to offer a more sustainable and cost-effective alternative to LIBs, potentially meeting future energy needs with greater environmental benefits.
References:
- Peters, J. F. et al. (2021) ‘On the environmental competitiveness of sodium-ion batteries under a full life cycle perspective – a cell-chemistry specific modelling approach’, Sustainable Energy & Fuels, 5(24), 6414–6429. doi: 10.1039/D1SE01292D
- Liu, H. et al. (2021) ‘A life cycle assessment of hard carbon anodes for sodium-ion batteries’, Philosophical Transactions of the Royal Society A: Mathematical, Physical and Engineering Sciences, 379(2209). doi: 10.1098/rsta.2020.0340.
- Liu, H. et al. (2022) ‘Tracing the technology development and trends of hard carbon anode materials: A market and patent analysis’, Journal of Energy Storage, 56(Part B), 105964. doi: 10.1016/j.est.2022.105964.