Lukas Ihlbrocka,
Anne Sehnala,
Moritz Gutsch
a and
Simon Lux
*ab
aInstitute of Business Administration at the Department of Chemistry and Pharmacy, University of Münster, Leonardo Campus 1, 48149 Münster, Germany. E-mail: simon.lux@uni-muenster.de
bFraunhofer Research Institution for Battery Cell Production FFB, Bergiusstraße 8, 48165 Münster, Germany
First published on 4th September 2025
Europe is currently heavily dependent on imports for the critical raw materials needed for lithium-ion battery (LIB) production, as most of these resources are distributed outside the region. Despite this dependency, Europe accounts for around 25% of global electric vehicle (EV) sales. This creates an indirect form of energy dependency, as much of the energy used in battery cell production is embedded in imported materials and cells. Persistent supply chain bottlenecks have made battery access a strategic priority for automakers, prompting efforts to build more resilient domestic supply chains. However, this shift also means that a significant amount of energy will need to be sourced within Europe itself, raising concerns about energy consumption amid surging European battery capacity demand – an important factor that will shape strategic decisions in both industry and policy. This work addresses the future energy demand of LIBs and their potential near-term competitors, sodium-ion batteries, by quantifiying the cradle-to-gate and cradle-to-cradle cumulative energy demand for large-format prismatic cells, using primary machinery data on gigafactory scale. The European energy demand forecast until 2070 is conducted using a novel circular economy simulation model, considering recycling, second use and the use phase of EVs and stationary energy storage (SES) applications. We show that the local European energy demand to establish a domestic battery cell production and to be self-sufficient by 2050 will rise to 250 TWh annually. Including the use phase of EVs and SES, a total of 450–500 TWh will be needed within Europe starting in 2040, offset by savings of approx. 90 TWh from reduced fossil fuel upstream energy. The comprehensive analysis provides a quantitative framework for understanding the energy flows associated with large-scale battery cell production in Europe. We highlight processes with significant reduction potential, while also identifying factors that could increase energy demand in the future.
Broader contextThe transition to electric vehicles (EVs) and stationary energy storage (SES) is accelerating battery demand in Europe. However, battery cell production depends on critical raw materials, which are predominantly sourced from outside the region. This leaves Europe heavily reliant on imports and creates an indirect form of energy dependency, due to the substantial embedded energy in imported materials and cells. Recent European Union policies, including the Critical Raw Materials Act and the Net-Zero Industry Act, aim to strengthen local battery cell production. However, this shift also raises concerns about rising energy demand in Europe, necessitating access to affordable, abundant and reliable energy to enable a successful transition. This study quantifies the cradle-to-cradle cumulative energy demand of selected lithium-ion and sodium-ion battery cells utilising primary machine data on gigafactory scale. Going beyond previous studies, we analyse the imported and locally required energy demand along Europe's path toward battery self-sufficiency. This includes a detailed assessment of cell production, while also considering the EV and SES use phase, considering different fuel consumptions and round-trip efficiency losses at the cell level. Our findings provide critical insights for policymakers and industry leaders working at the intersection of clean energy targets, battery technology and industrial resilience. |
To meet this growing demand, companies are ramping up their battery production capacity, which requires critical raw materials such as lithium, nickel, cobalt and graphite. For European companies, this primarily results in reliance on other countries, primarily on China, due to concentrated distribution of resources.10,11 Moreover, the ownership distribution along the LIB value chain further reinforces China's influence.12 Amid rising geopolitical tensions, the risk of supply disruptions is increasing. Consequently, Europe is strengthening local battery production and promoting circular economies.13–15 However, expanding its own LIB supply chain will also result in a significant increase in energy demand, as most of the energy currently used for mining, refining and cell manufacturing is required outside of Europe. As part of the European Green Deal, the EU submitted the Critical Raw Materials Act (CRMA) in 2023, which aims to achieve an extraction capacity of 10% of the EU's annual demand for strategic raw materials, a domestic processing and refining capacity of 40% for battery materials and a recycling capacity of 25% by 2030 to ensure access to a secure and sustainable supply.13 Furthermore, the Net Zero Industry Act (NZIA) was proposed, aiming for 40% local battery cell and cathode and anode active material (CAM/AAM) production by 2030.15 Understanding the European local energy requirements, which inevitably involve CO2-emissions and costs, is therefore central to achieving this goal and to guide strategic decisions in industry and policy. Existing life-cycle assessment (LCA) research focusing on cumulative energy demand (CED) typically concentrates on the energy requirements associated with gate-to-gate battery manufacturing16–18 or provides cradle-to-gate energy assessments at the cell level.19–21 Forecast-oriented studies, often focus on material demands22–25 or battery cost projections.26–29 This study aims to bridge the gap between cell-level energy demand analyses and forecasting approaches by predicting the cradle-to-cradle energy demand across the entire battery value chain accumulated for the European market. The analysis is categorized into several key stages, ranging from mining and refining of lithium hydroxide (LiOH), lithium carbonate (Li2CO3), nickel sulfate (NiSO4), cobalt sulfate (CoSO4) and manganese sulfate (MnSO4) to CAM and AAM synthesis, metals and non-active materials production, gate-to-gate battery cell manufacturing and scrap generation, while also considering the use phase of EVs and SES applications.
Therefore, the energy consumption per kWhcell of selected state-of-the-art LIBs, sodium-ion battery (SIB) cells and next-generation materials are determined by applying a (1) battery cell model, a (2) battery cell production model and an (3) LCA model. The production model, based on primary gigafactory-scale machine data,16 calculates energy usage and material needs. These outputs, alongside results from the battery cell model, feed into a cradle-to-gate LCA focused on CED. The energy requirements for cells based on secondary materials are modeled, considering the recycling of lithium, nickel, cobalt, manganese, aluminum and copper. In addition, we go beyond previous studies by applying a (4) circular economy simulation model (see Fig. 1) to develop a forecast of the European energy demand, with a detailed breakdown into cell production and the use phase of EVs and SES. The EV and SES battery capacity demand is determined based on European EV sales, sales-weighted battery size data and SES capacity projections.
For the first time, this analysis approach quantifies the local European energy demand required to develop domestic battery cell production, aiming to strengthen national capabilities and to be self-sufficient by 2050. Additionally, the energy demand associated with imported materials required to meet Europe's overall battery capacity demand is determined, considering three dominant technology scenarios: lithium nickel manganese cobalt oxide (NMC), lithium iron phosphate (LFP) and SIB. Moreover, the study examines the use phase of EV and SES applications and models the annual electricity demand for EV charging in Europe by taking into account the varying fuel efficiencies of different battery technologies and factoring in round-trip efficiency losses at the cell level.
Innovation | Motivation |
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The entire EV fleet and SES “battery stock”, which refers to all existing batteries in the economy, is modelled, including both primary and secondary battery materials. | This allows analyzing the quantity and properties of the various battery stocks at any given point in time, such as their technological constitution, material flows or energy throughputs. |
The market segmentation for EVs and SES batteries in small and large EVs and low- and high-demanding SES applications and the technology roadmap is taken into consideration. | The application of the battery is expected to influence technological choices and the battery size. The influence of such market-driven effects can thus be analysed. |
A market-driven perspective on the demand for second use batteries is employed, compared to a fixed share of EV batteries deployed in second use applications in other studies.22,23 | Due to the supply of used EV batteries significantly exceeding projected SES demands, saturation effects can be expected to occur rapidly. This setup ensures that such effects are considered. |
Combination of market-driven perspective with technology dependent prefiltering of potential second use batteries. | The technology constitution of second use batteries can be expected to differ from that of all retired EV batteries. This influences system properties such as the recycled material streams or round-trip efficiencies of the SES sector. |
This study focuses on the CED of LIB and SIB cell chemistries that are either commercially relevant or considered promising next-generation batteries. For LIBs, the battery cells examined include LFP|Graphite (Gr), NMC|Gr, LiNi0.8Co0.15Al0.05O2 (NCA)|Gr and 0.33 Li2MnO3·0.67 LiNi0.27Mn0.6Co0.13O2 (LMR-NMC)|Gr. NMC622, NMC811 and NMC955 are also analysed with 5 wt% and 20 wt% silicon containing anodes. For SIBs, O3-NaNi1/3Fe1/3Mn1/3O2|hard carbon (NFM111|HC), Na3V2(PO4)2F3 (NVPF)|HC and Na2Mn[Fe(CN)6] (Mn-PBA)|HC are considered. The lithium and sodium layered oxide CAMs are modeled by the precursor synthesis via co-precipitation and calcination.34 The polyanionic type CAMs (LFP35 and NVPF36) are modeled via a solid-state synthesis and for Mn-PBA, a solvent based precipitation synthesis is modeled based on primary industrial data.37 For the synthetic graphite synthesis process, the energy intensive calcination and graphitization steps are considered. The calcination step is based on a new modeling approach to produce needle coke, considering condensable volatiles for energy generation.33 In contrast to existing LCA studies, the graphitization is modeled using an Acheson powder process based on recent industrial primary data, which is published by Carrére et al. to produce battery grade graphite.38 Previous studies, which mainly refer to the carbon footprint, have significantly underestimated the CO2-emissions of graphite.21,39,40 Additionally, the graphite modeling includes milling, micronizing, coating and packaging steps, whereby the packaging steps are excluded in this study.
For SIBs, HC synthesis from petroleum pitch is considered, as this supply chain offers the highest potential for large-scale production.41 Alternative HC precursors are lignin, phenolic resin and coconut shells.41,42
For silicon containing anodes, the production of metallurgical grade silicon is modeled based on the life cycle inventory data by Frischknecht et al. (SI Table S10).43 In the manufacturing process, it is assumed that the co-utilization of graphite and silicon is carried out by blending silicon with graphite in the electrode fabrication process,44 resulting in the same energy consumption as for the graphite AAM production process. To enable a more accurate modeling of silicon containing anodes, comprehensive industrial synthesis data is essential. The raw material mining and refining are modeled globally. The output is the produced energy consumption (kWhprod) per specific cell energy (kWhcell) and is shown in Fig. 4. For all battery cells the same prismatic cell housing is modeled. The resulting life cycle inventory data is provided in the SI. The functional unit for this analysis is defined as 1 kWh of battery cell energy produced. Ecoinvent 3.9.1 is used as the underlying life cycle inventory database.
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Fig. 2 European EV stock development projected until 2070 subdivided in small and large BEVs and PHEVs (a) and the produced SES capacity forecast (b). |
The yearly EV sales result in the battery demand dn,EV(y). The EV battery production is based on dn,EV(y) and the battery size (Ebat(y)), that are defined by the input scenario. Multiplying dn,EV(y) and Ebat(y) yields the demand of EV batteries in units of capacity (dE,EV(y)), as described by eqn (1).
dE,EV(y) = Ebat(y)·dn,EV(y) | (1) |
dE,SES (y) = dSES,total(y) − ESES(y) | (2) |
![]() | (3) |
![]() | (4) |
The round-trip efficiency is defined as the ratio of energy that can be used relative to the energy that went into charging the battery. Ideally, discharging energy should be the same as charging energy, but in practice a part of the energy is lost, which is affected by the voltage hysteresis between the charge and discharge curves.76 The round-trip efficiency is also highly sensitive to operating parameters such as C-rate, depth-of-discharge, temperature and voltage range, which makes the comparability of round-trip efficiencies difficult in existing studies.76–79 In this model, round-trip efficiency values are based on a C-rate of 0.2C (see Table 2). In addition, an annual degradation factor of 0.2% was considered in this study. It is crucial to note that the round-trip efficiency is evaluated at the cell level. For silicon containing graphite anodes, however, it is assessed at the material level due to the limited available data.76,79–85
Type | Fuel efficiency [km kWh−1] | Round-trip efficiency [%] | |||
---|---|---|---|---|---|
Cathode | Anode | Small BEVs | Large BEVs | 0.2Ca | Ref. |
a Extrapolated to 0.2C. The round-trip efficiency of NMC811|Gr is also assumed for NMC955|Gr, NMC622|Gr and NMC532|Gr. Gr: graphite, HC: hard carbon, Si: silicon. | |||||
NMC532 | Gr | 7.81 | 7.04 | 96 | 79 |
NMC622 | Gr | 7.82 | 7.05 | 96 | 79 |
NMC622 | Gr+ 5 wt% Si | 7.90 | 7.13 | 95 | 76 and 79 |
NMC622 | Gr+ 20 wt% Si | 7.99 | 7.21 | 91 | 76 and 79 |
NMC811 | Gr | 7.86 | 7.09 | 96 | 79 |
NMC811 | Gr+ 5 wt% Si | 7.94 | 7.17 | 95 | 76 and 79 |
NMC811 | Gr+ 20 wt% Si | 8.03 | 7.25 | 91 | 76 and 79 |
NCA | Gr | 7.86 | 7.09 | 96 | 85 |
LFP | Gr | 7.67 | 6.91 | 98 | 79 |
LMR-NMC | Gr | 7.90 | 7.13 | 87 | 85 |
NMC955 | Gr+ 5 wt% Si | 7.96 | 7.18 | 95 | 76 and 79 |
NMC955 | Gr+ 20 wt% Si | 8.04 | 7.27 | 91 | 76 and 79 |
NFM111 | HC | 7.58 | 6.82 | 92 | 82 |
NVPF | HC | 7.59 | 6.83 | 95 | 80 |
PBA | HC | — | — | 98 | 83 |
In 2023, Europe installed 17.2 GWh of new SES capacity, reaching about 36 GWh installed capacity in total.54 By 2050, about 1600 GWh of SES battery capacity are forecasted.55–60
The LFP scenario (Fig. 3a) projects that LFP-based LIBs will dominate the EV and SES market over the next decades. Starting in 2040, approx. 1000 GWh year−1 of battery capacity will be required, with the LFP scenario projecting that the share of LFP|Gr will continuously increase, reaching 570 GWh year−1 for EVs and 75 GWh year−1 for less-demanding SES applications by 2070. As in the NMC scenario, SIBs are considered for small BEVs and less demanding SES applications reaching a share of 20% and 30%, respectively, by 2070. For small BEVs, NVPF|HC and NFM111|HC are considered due to their high volumetric energy density compared to other SIB chemistries,71,95 while Mn-PBA|HC96 accounts for the majority of SIBs in SES applications. NMC|Gr is expected to capture a market share of 10% for small BEVs and 30% for large BEVs by 2070.
NMC remains the dominant cathode chemistry in the NMC scenario (Fig. 3b), capturing a market share of 75–95% for EVs (750 GWh year−1) and 60–85% for SES (98 GWh year−1) in the forecast period from 2024 until 2070. Within this scenario, NMC811|Gr has the largest share for small BEVs and SES, while high-nickel and silicon-rich batteries are dominant for large BEVs. The share of LFP|Gr is projected to steadily decline starting from 2024.
SIBs are considered in this analysis as a compelling near-term challenger to LIBs with 240 GWh of battery capacity globally announced.27 The high SIB scenario (Fig. 3c) is largely driven by elevated lithium carbonate prices and lithium supply chain risks, leading to an increased market share for SIBs,27 particularly as an alternative to LFP|Gr cells. By 2070, the battery capacity demand of SIBs is projected to reach up to 205 GWh year−1 for small EVs and up to 220 GWh year−1 for large EVs. In the SES market, SIBs are expected to be even more dominant, accounting for 72 GWh year−1 of SES installations.
It is noteworthy that, compared to existing literature, our battery capacity demand analysis represents a relatively conservative scenario. Many studies project between 0.7–1.4 TWh year−1 by 2030.7 Nevertheless, our forecast of 0.55 TWh year−1 by 2030 aligns closely with BloombergNEF's base case8 and the accelerated ambition scenario by Yang et al.97
The results of the CED of primary and secondary materials for prismatic cells are depicted in Fig. 4, with a cathode thickness of 90 μm, showing the sustainability in terms of energy consumption. On the anode side, LIBs were modeled with pure synthetic graphite as well as with 5 wt% and 20 wt% silicon. Natural graphite production is less energy intensive than synthetic graphite synthesis but was not considered in this study due to the increasing share of synthetic graphite as an anode material.104,105 For SIBs, pitch-based HC was considered. A major difference in graphite and HC production is the graphitization step, where needle coke powder is heated above 3000 °C for several weeks,38 while HC carbonization process typically occurs at temperatures between 1100–1700 °C.106 This results in significantly higher energy consumptions for the graphite synthesis process, as shown in Fig. 4a, where the anode CED for LFP|Gr exceeds that of SIB cells by more than a factor of two. The anode impact decreases with increasing silicon content, as silicon production requires 28.7 kWh kgAAM−1, compared to 147.1 kWh kgAAM−1 for graphite (HC: 57.3 kWh kgAAM−1) and further amplified by an increased energy density. Accordingly, the energy consumption for anode production accounts for 22.8–31.7% of the total energy consumption for NMC|Gr cells, 53.4% for LFP|Gr cells and between 19.2–21.2% for SIBs. For NMC|Gr + 20 wt% silicon, the anode impact drops to just 12–15%.
The largest driver of energy consumption for all cells, except LFP|Gr, is the cathode. This is primarily due to the mining and refining processes of CoSO4 (321.4 kWh kg−1) and NiSO4 (71.8 kWh kg−1). Further, the co-precipitation and calcination steps to produce NMC, NCA and NFM111 cathode materials are highly energy intensive (see SI).34,39 LFP shows the lowest cathode contribution to the total energy impact among all selected cells, with a share of 16.5%, since less-energy intensive materials (Fe, PO4) are required. Cell mechanics impact both LFP|Gr and SIB cells more than NMC|Gr battery cells, particularly due to their lower energy densities. The impact is notable because this model considers a large commercial prismatic cell, where the majority of the 330 g housing weight comes from high impact material aluminum (42.95 kWh kg−1). For pouch and cylindrical cells, the impact is significantly lower. Pouch cells require less cell housing (per kWhcell), while for cyclindrical cells the cell housing is based on nickel-plated steel, which has a reduced impact (6.97 kWh kg−1).
The gate-to-gate cell production has a relatively small impact on the overall energy consumption, ranging between 25–28 kWhprod. kWhcell−1 for NMC|Gr and NCA|Gr based on today's production technology and know-how for LIB production. Owing to significantly lower energy densities, the cell production accounts for 36 kWhprod. kWhcell−1 for LFP|Gr and 32–50 kWhprod. kWhcell−1 for SIBs, underlying the importance of increasing energy density.
Combined, LFP|Gr emerges as the most energy-efficient to produce at cell level with approx. 300 kWhprod. kWhcell−1, which is nearly half of the CED of NMC622|Gr. Following LFP|Gr, NVPF|HC has the second-lowest CED, closely followed by PBA|HC. NFM|HC has a slightly higher energy consumption due to the NiSO4 precursor. Overall, SIBs are therefore competitive with NMC|Gr and NCA|Gr in terms of energy consumption, but the production per kWhcell requires 20–90 kWh more than LFP|Gr cells, which are considered the competing technology. For pure graphite cells, LMR-NMC stands out regarding the CED, achieving a high energy density due to its high practical capacity of 250 mAh g−1 and the utilization of the low impact material MnSO4 (3.7 kWh kg−1). The use of silicon-rich anodes would further reduce energy consumption.
Since a large part of the mining and refining of important battery materials takes place outside of Europe,101 recycling of battery cells is important for Europe to reduce dependence on other countries and in transition to a circular economy, to reduce pressure on natural resources. In Fig. 4b, the CED of cells based on secondary materials is shown. The recycling energy was modeled utilizing a hydrometallurgical process according to Jiang et al.,72 based on industrial data for NMC|Gr and LFP|Gr recycling. For the recycling process 15–38.4 kWh kWhcell−1 are needed, in line with the advanced process by Düsenfeld, which is published by Mohr et al.107 In contrast to the CED of battery cells based on primary materials, SIB and LFP|Gr cells exhibit the highest CED for secondary cells, as only less energy intensive materials are recovered (LFP: Li2CO3 and NFM: NiSO4). For NVPF|HC and PBA|HC, only aluminum is recovered. In case of NVPF|HC cells, significant potential for energy reduction originates from vanadium recycling, as energy intensive vanadium pentoxide (105 kWh kg−1)108 is used in CAM synthesis. In general, processes need to be developed for SIBs that are tailored for SIB recycling to be competitive in terms of CED of battery cells based on secondary materials. Nevertheless, recycling can further mitigate battery life cycle impacts for cells with low elemental value. In the assumptions made in this work, the reduction potential of secondary NVPF|HC and PBA|HC cells are still 10.5% (−34 kWh) and 13.6% (−46 kWh), respectively. The savings potential for LFP|Gr is in the same order of magnitude (11.9%). Significant energy savings can be achieved for NMC and NCA-based LIBs and NFM111|HC cells. The savings range from approx. 119 kWh (LMR-NMC|Gr) to 367 kWh (NMC111|Gr), with most being over 50% (NFM111|HC: 151 kWh, 38%). Overall, the CEDs of secondary cells containing pure graphite are in the same range (252–272 kWh kWhcell−1). As the silicon content increases, the CED decreases significantly. For NMC955|Gr + 20 wt% silicon, the CED drops to just 139 kWh kWhcell−1, representing a 52.2% reduction compared to LFP|Gr. Compared to cells produced from primary materials, the percentage contribution of cell production based on secondary materials gains increasing relevance in the transition to a circular economy. Most of the energy consumption of secondary cells is attributed to the anode, indicating that at least in terms of energy consumption, graphite recycling is of great interest.
In 2024, the energy demand for producing LIB cells for 2.5 million EVs and approx. 22.4 GWh of SES capacity across all three scenarios is around 50 TWh. Almost 45% of this energy is required for the mining and refining of LiOH, Li2CO3, NiSO4, CoSO4 and MnSO4 and a significant share also arises from CAM and AAM synthesis. The peak energy demand is projected to be reached in 2035 and will increase by a factor of 7.7 in the NMC scenario, 7.2-fold in the LFP scenario and 7.3-fold in the SIB scenario. In the NMC scenario, energy demand is projected to reach 378 TWh by 2035, primarly due to the energy intensive production of NMC|Gr cells based on primary materials (see Fig. 4a). In total, the production of CAM and AAM (including mining, refining and synthesis) represents 80% of the energy requirements in 2035, while gate-to-gate battery cell production contributes only about 6.4%. Although the EV battery capacity demand remains steady in the following years and SES demand rises, the energy consumption in the NMC scenario decreases significantly starting from 2035 and reaches a steady state by 2050. This decline is primarily attributed to recycling, as valuable and energy intensive precursors for NMC production are recovered. By 2070, it is forecasted that the energy demand drops to 206 TWh, a reduction of 45%, with recycling accounting for 10.4% of the total energy demand.
The LFP scenario (Fig. 5b and e) has the lowest peak energy demand compared to the NMC (Fig. 5a and d) and SIB (Fig. 5c and f) scenarios. The model predicts approx. 340 TWh in 2035, which is 11% lower than in the NMC scenario (see Fig. 6). This difference is due to significantly less energy intensive production of LFP|Gr, highlighting substantial short-term reduction potentials from CAM materials that do not use critical raw materials such as nickel and cobalt. However, the total energy demand from 2024–2070 is only 3.7% lower and will require more energy beyond the forecast period (see Fig. 6). The lower energy savings that come with recycling are the main reasons for this. Furthermore, the production of AAM, metals, non-active materials and battery cells has a higher impact, resulting from their lower energy density. The proportion of AAM synthesis increases from 30% to 50%, the share of gate-to-gate cell production is predicted to increase from 6% to 14%, while the share of metals and non-active materials will remain relatively constant in the range of 12–15% throughout the forecast period. The SIB scenario (Fig. 5c and f) represents a combination of the LFP and NMC scenarios in the initial years, as SIBs are predicted to enter the European market in 2030–2035. As in all scenarios, CAM and AAM synthesis are the main energy drivers, but the more energy intensive CAM synthesis compared to LFP-based LIBs is offset by the less energy intensive HC synthesis, resulting in an overall lower energy demand. The impact of cell production and metals and non-active materials is in the same order of magnitude compared to the LFP scenario. Total energy consumption from 2024–2070 is 4.5% and 0.7% lower than in the NMC and LFP scenarios, respectively. However, it should be noted that a substantial SIB share is projected towards the end of the forecast period and that SIBs have the highest energy consumption (kWh kWhcell−1) for secondary cells. As a result, the influence of SIBs based on secondary materials only become apparent from 2070 onwards.
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Fig. 6 European energy demand comparison for the NMC, LFP and SIB scenarios (based on Fig. 5a–c). The peak energy demand in 2035, the last year of the forecast (2070) and the overall energy demand from 2024–2070 are depicted. |
While the base case provides a reference point, future energy demand will depend on a range of variables whose evolution remains uncertain. One major factor is the emergence of post-lithium-ion technologies. Solid-state batteries have the potential to reduce the gate-to-gate cell production energy demand to 10.6–17.5 kWhprod., lithium–sulfur batteries to 13.4 kWhprod. and lithium air batteries to 20.9 kWhprod..16 This contrasts substantially with present large-scale LIB technologies such as LFP|Gr (36 kWhprod.) and NMC811|Gr (25 kWhprod.), highlighting potential energy reductions. However, to assess the impact of these post-lithium-ion technologies, the materials are of crucial importance, requiring cradle-to-gate CED analyses with large-scale synthesis data. A recent study models a high CED of 493–655 kWh kWhcell−1 for oxide-based solid-state batteries,109 significantly higher than for silicon-containing NMC cells. Furthermore, it remains uncertain if and when these technologies will achieve market penetration and their adoption would necessitate modifications to existing manufacturing lines.16 By contrast, SIBs are considered in this analysis as they represent a drop-in technology and are on the verge of large-scale commercialization.27 Further improvements may arise from advances in the gate-to-gate production processes, as demonstrated by Degen et al.,16 including dry coating, integration of heat pumps and efficiency improvements from learning effects and economies of scale, with potential savings of up to 66%. Nevertheless, as the gate-to-gate cell production is only projected to account for around 5–6% of total energy consumption in the base case by 2040, substantial overall reductions can only be achieved by significantly improving the energy efficiency of raw material mining and refining. A key focus is the optimization of comminution processes, where crushing and grinding represent the largest opportunities for energy savings.110–112 Emerging technologies such as high-pressure grinding rolls and stirred mills have the potential to substantially contribute to these reductions. Additionally, adopting advanced combustion technologies110 and optimizing the energy supply can further enhance overall efficiency, with one study reporting that the U.S. metal mining sector could reduce its energy consumption by about 61% by shifting from current practices to the best-estimated practical minimum energy use.113 In the refining stage, considerable energy savings can be achieved by implementing new metallurgical processes. For nickel production, for instance, these include ore pre-concentration, transitioning to bath smelting technology and utilizing bioleaching in hydrometallurgical processing.111
However, this technological progress is offset by several factors that are expected to drive higher energy inputs in the mining industry in the future. Declining ore grades for metals such as copper, nickel, cobalt and lithium mean that larger volumes of rock must be mined, crushed and processed, leading to an increased energy consumption.102,113 Furthermore, the development of more challenging deposits, characterized by deeper orebodies, remote locations, and more complex mineralogy, is anticipated to raise energy intensity.102,113 Hence, energy inputs in mining have already risen substantially in the 21st century and are expected to continue increasing in the coming decades as these trends persist.113
The largest potential for reducing energy demand of LIBs is derived from AAM synthesis, as illustrated in Fig. 5. This is driven by improved material recovery for synthetic graphite,38 increased utilization of silicon and natural graphite105,114 and especially by graphite recycling. The concept of recycling anode materials back into the battery supply chain is still a relatively new process and remains largely in the research and development phase.115 This is primarily because graphite116,117 has received less attention in LIB recycling compared with high-value cathode metals such as cobalt,118 nickel119 and lithium.120 Furthermore, concerns over the purity and electrochemical performance of recycled materials have hindered commercial utilization. Hence, graphite anodes have been downcycled or used in lower-value applications.121 Significant innovations are required to establish a profitable and sustainable industrial-scale recycling process that meets the high-performance requirements for LIB anode materials122 (see SI for details). In Europe, political incentives are still lacking: the EU's Battery Regulations set mandates for recycled content in new batteries, yet graphite was notably excluded despite being designated a critical mineral under the CRMA.123 This exclusion is particularly striking given that recycling graphite also presents a strategic opportunity to reduce dependence on China.
Furthermore, there is a growing need for more tailored recycling processes for SIB recycling, such as recovering vanadium pentoxide from NVPF cathodes. Reduction potential also exists through increasing the energy density of battery cells. For example, the specific energy density of LIBs has doubled over the past decades, rising from around 150 Wh kg−1 to approx. 300 Wh kg−1.18 In the case of SIBs, further improvements are expected primarily through increases in the specific capacity of HC anodes, which could exceed 400 mAh g−1.27
Future energy demand could increase significantly if circular economy strategies, such as recycling and second use, are implemented less extensively than modeled in this study. The analysis assumes sufficient recycling capacities and a collection rate of 97% (additional 1% EV loss rate). Failure to meet these recycling rates and recovery efficiencies would lead to a substantial rise in energy demand. Under the study's assumptions, recycling in the NMC scenario saves approx. 5100 TWh of energy, averaging 118 TWh annually throughout the forecast period. Fig. 4 demonstrates that recycling is environmentally attractive even for cathode materials with lower elemental value, contributing to annual energy savings of 67 TWh and 84 TWh in the LFP and SIB scenarios, respectively. Moreover, if recycled raw materials fail to meet battery-grade quality and necessitate additional energy-intensive refining, overall energy demand will further increase.
The presented base case is also based on strong EV fleet growth until 2035, which is uncertain, especially if the ban on ICEV sales in the EU is lifted.
In 2024, only about 3 TWh of energy used for cradle-to-cradle battery cell production is sourced domestically in Europe, despite the region representing nearly 25% of the global EV market.11 This indicates that almost all the energy needed for electrification is imported currently, leading to significant energy dependency. By ramping up the local LIB and SIB supply chains, dependency on other countries is reduced, but the energy demand is consequently shifted to Europe. This model projects that local energy demand will rise to 83–87 TWh annually by 2030 in the base case to meet the stated CRMA and NZIA targets, representing approx. 35% of the total energy required for battery cell production. In order to achieve self-sufficiency by 2050, the annual domestic energy demand would still need to triple to around 250 TWh, assuming that circular economy approaches are prevalent by then (see Fig. 5d–f and 7). The use of SLB in the less-demanding application SES sector leads to energy savings of 9–11 TWh annually on average across the three scenarios. Furthermore, the recycling supply of end-of-life batteries is postponed, resulting in more time to build up recycling capacities. Overall, it is crucial for Europe to minimize the electric vehicle loss rate, maximize the recycling collection rate and build up the recycling infrastructure.
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Fig. 7 Local European energy demand comparison for the NMC, LFP and SIB scenarios (based on Fig. 5d–f). The comparison includes the year 2030, for which targets have been set through the CRMA and NZIA regulations, the year 2050, in which we assume self-sufficiency for Europe and the entire forecast period from 2024 to 2070. |
Fig. 8 illustrates the projected local European energy demand for domestic cradle-to-cradle cell production, EV charging and the efficiency losses (for both EV and SES) in the NMC (a), LFP (b) and SIB (c) scenarios. The European energy demand for battery cell production is derived from Fig. 5 (marked areas). The model projects that by 2045 the charging energy demand for approx. 140 million EVs in Europe will reach around 210–215 TWh in all scenarios. This represents a tenfold increase from 2024 levels and a threefold rise in EV energy consumption between 2030 and 2045. These trends are consistent across all three scenarios, despite variations in fuel efficiency among the different battery technologies. While NMC|Gr cells demonstrate the highest fuel efficiency, resulting in the lowest energy consumption in the NMC scenario, the differences are relatively minor. Over the entire forecast period, the EV charging energy demands for the LFP and SIB scenarios are only 109 TWh and 83 TWh higher, respectively. Variations in round-trip efficiency led to overall losses that are approx. 165 TWh and 148 TWh higher for the NMC and SIB scenarios, respectively, in contrast to the LFP scenario. Overall, efficiency losses have a significant impact resulting in efficiency losses during the EV use phase ranging from 4% to 7%. This impact is even more dominant for SES batteries, which undergo 250 discharge cycles per year (SI Fig. S12). Additionally, because SES batteries have a longer service life and are reused from the automotive sector, the influence of the annual degradation factor of 0.2% on the energy efficiency becomes more substantial. Combined, efficiency losses are projected to increase from around 7 TWh in 2030 to over 35 TWh in 2070, underscoring an essential area of battery research. Minimizing future efficiency losses could be achieved through thermal management and optimization of charging and discharging rates by using advanced charging algorithms and implementing smart charge/discharge control systems.125 Further, potential reduction arises from improvements in material properties, electrode characteristics and operating conditions.76 Large voltage hysteresis occurs for silicon-containing anodes, which can be attributed to the significant kinetic resistance experienced during the lithiation/delithiation process,126 as well as the compressive stress that arises during lithiation.127 The issues of low coulombic efficiencies are related to the substantial volume changes of silicon and ongoing solid electrolyte interphase formation and electrolyte decomposition.128,129 Future developments addressing these issues could improve energy efficiency. Similarly, LMR-NMC cathodes exhibit large voltage hysteresis and potential decay, which could be addressed by surface treatments.85 For SIBs, potential efficiency improvements exist through cycling at high states of charge, as demonstrated by Rehm et al. for NFM|HC cells.130 For next-generation battery technologies, targeted research to minimize such inefficiency losses will be critical for future system performance and sustainability. Developing new electrode materials with huge overpotentials are therefore not of great practical interest.78 It is important to note that we consider round-trip efficiencies at the cell level. In practice, the remaining components of a battery system (e.g., pack and module casing, inverter and battery management systems) contribute additionally to lower overall efficiencies.
The local energy demand in Europe for battery cell production, EV charging and inefficiency losses (EV and SES) is projected to increase sixfold from 2024 to 2030 and twentyfold until 2050. To achieve self-sufficiency starting in 2050, Europe must supply 450–500 TWh annually in all three scenarios, sourced primarily from electricity. McKinsey predicts an average growth in electricity demand of 1.1% per year from 2020 to 2050 in Europe, which is 0.4% lower than the average annual growth observed between 1990 and 2007.124 This corresponds to an energy increase of approx. 1400 TWh, reaching around 4900 TWh by 2050. This is equivalent to an average rise of 45 TWh per year or about 66 TWh annually between 2023 and 2030 (460 TWh in total).131 Based on our calculations, the average annual growth rate of battery-related electricity demand is projected at +35% from 2024 to 2030, averaging around 22 TWh per year. An average annual growth rate of +12.9% is projected until 2050, thus expanding disproportionately compared with overall electricity demand. Consequently, based on assumptions made in this study, batteries account for roughly one-third of McKinsey's projected additional electricity demand in both 2030 and 2050. Meeting the additional energy demand would be feasible for Europe but entails considerable uncertainties and challenges. To meet the increasing demand with natural gas power plants, Europe would need to double electricity generation from natural gas (450 TWh in 2023132). To produce the energy entirely from solar panels, an area of ∼2300 km2 would be required, based on the assumption that one m2 of solar panels generates 220 kWh year−1.133 That correspond approx. to the size of US state Rhode Island or 2.5 times the area of Berlin. Furthermore, approx. 250–300 TWh of electricity will be required for EV charging alone by 2040, with demand occurring largely in a decentralized manner. This necessitates the large-scale deployment of charging infrastructure. Additionally, capacity issues in the power grid, including long lead times for grid connections, highlight the urgency of expanding distribution networks.134 Substantial investments will be needed in generation assets, transformers, local grids and charging points. At the same time, the continued expansion of renewable energy capacity is essential to meeting climate targets. However, permitting procedures and slow build-out speeds remain critical bottlenecks and the increasing share of renewables tends to drive higher overall system costs.135 These developments underscore the dual challenge of decarbonizing the power system while maintaining affordability and system stability.136 Nevertheless, large-scale electrification combined with clean domestic power generation offers significant benefits for Europe's security of energy supply. Reducing dependence on imported fossil fuels not only strengthens resilience but also represents a key step toward achieving long-term climate goals. Although Europe may not have a classical comparative advantage in large-scale battery cell production due to higher costs compared to Asia, strategic factors are crucial. Advanced recycling technologies could give Europe a comparative advantage by enabling the more efficient use of critical raw materials and reducing reliance on imports. Integration with the local automotive industry and the growing renewable energy sector can further enhance system-level efficiency and innovation. Together, these factors enable Europe to optimize resource allocation, strengthen energy security and reduce economic dependency. This avoids a shift from reliance on fossil fuels to another form of energy and economic vulnerability.
The substantial growth in electricity demand driven by electrification also results in a considerable decline in fossil fuel consumption, as illustrated in Fig. 9, which quantifies the potential savings in both locally produced and imported energy. The modeling accounts for the upstream energy demand associated with the production of petroleum-based products for use in ICEVs, as well as for electricity generation from natural gas, coal and oil, including both upstream energy and energy losses during the electricity generation process. It is important to note that this refers solely to the energy required for these processes and not to the embedded energy of fossil fuels. Gasoline and diesel are produced from crude oil, only about 23% of which is sourced locally in Europe.137 By 2045, the transition to EVs is projected to reduce local upstream energy for petroleum fuels by 35 TWh per year, while avoiding around 120 TWh of energy imports. For electricity generation, SES systems with a capacity of 1600 GWh are expected to store and release approx. 500 TWh of electricity per year by 2050 (see SI Fig. S12). Between 2050 and 2070, this saves 90–110 TWh of upstream fossil fuel energy, about half of which is locally produced. Overall, local energy savings would amount to 21 TWh by 2030, rising to around 90 TWh in 2050, considering current shares of locally produced and imported fossil fuels.
This study quantifies the energy demand associated with large-scale battery cell production to electrify Europe, divided into locally required and imported energy. The model projections indicate that, for the NMC scenario, the cradle-to-cradle battery cell production to electrify Europe will demand approx. 380 TWh of energy by 2035. Similar estimates for the LFP (340 TWh) and SIB scenarios (355 TWh) underscore the substantial rise in overall energy demand. However, only a limited share of approx. 35% would be produced locally within Europe based on the forecast. To achieve self-sufficiency by 2050, Europe's local energy demand for battery cell production is projected to rise to approx. 250 TWh. An additional 200–250 TWh will be needed to power EVs and to compensate for efficiency losses during the discharge of EVs and SES applications, reflecting the unique approach of this model, which incorporates both EV fuel efficiency and round-trip efficiency losses. Combined, a projected 450–500 TWh annually will be needed from 2038 until 2070, highlighting significant amounts of energy thus need to be supplied for the transition to EVs and renewable energy storage (see Fig. 8). This is offset by 90 TWh of upstream fossil fuel energy. The European battery industry will require access to affordable, abundant and reliable energy in order to successfully achieve the transition toward self-sufficiency.
Mining and refining processes for lithium, nickel, cobalt and manganese are projected to account for nearly half of the total energy demand of battery cell production in the initial years, while recycling is significantly less energy intensive. It should be noted that sufficient recycling capacities are assumed in the base case (800 GWh year−1 by 2050), although the recycling infrastructure is still in very early stages (SI Fig. S11). The assumption of a 50% collection rate of end-of-life batteries would increase the energy demand in the NMC scenario by 2500 TWh, adding an average of additional 54 TWh annually for the entire forecast period. For Europe, maximizing collection rates and recycling efficiencies will be essential, while graphite recycling and tailored recycling processes for SIBs offer further potential to reduce energy demand.
Building on this extended portfolio, future work could analyse the potential factors influencing the overall energy intensity of battery manufacturing, as outlined in this study. These factors include the impact of next-generation batteries and improvements in energy efficiency, particularly in the mining and refining industries. Additionally, the associated abatement costs could be examined further. It can be concluded that European policymakers need to implement effective and supportive regulations that enable companies to develop viable, sustainable recycling capabilities. Such measures will be instrumental in mitigating future energy demand, reducing dependence on imports and ensuring a stable, long-term supply of critical battery materials. Meeting these goals will also require substantial investment in renewable electricity and supporting infrastructure. Ultimately, large-scale electrification combined with clean domestic power generation will strengthen Europe's energy security and mark a decisive step towards achieving long-term climate goals.
AAM | Anode active material |
AM | Active material |
BEV | Battery electric vehicle |
BOM | Bill of material |
CAM | Cathode active material |
CED | Cumulative energy demand |
C&I | Commercial & industrial |
CRMA | Critical raw material act |
EU | European Union |
EV | Electric vehicle |
Gr | Graphite |
HC | Hard carbon |
ICEV | Internal combustion engine vehicle |
LCA | Life-cycle assessment |
LIB | Lithium-ion battery |
LFP | Lithium iron phosphate |
LMR | Lithium- and manganese-rich |
Mn-PBA | Manganese-Prussian blue analogue |
NCA | Lithium nickel cobalt aluminum oxide |
NFM | Sodium nickel iron manganese oxide |
NMC | Lithium nickel manganese cobalt oxide |
NVPF | Sodium vanadium fluorophosphate |
NZIA | Net Zero Industry Act |
pCAM | Precursor cathode active material |
PHEV | Plug-in electric vehicle |
RoW | Rest of World |
SES | Stationary energy storage |
SIB | Sodium-ion batteries |
SLB | Second life batteries |
The production model used in this study is primarily based on the framework developed by Degen et al., available under “Source Data Fig. 3” at https://doi.org/10.1038/s41560-023-01355-z.
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