4.1. Introduction to Energy Storage Technology
Energy storage has become one of the key pillars of the RES-based energy transition. The variability of photovoltaic and wind production necessitates energy buffering and flexibility on both the demand and supply sides to ensure the stability of frequency, voltage, and power quality. Current literature reviews indicate that storage technologies have undergone rapid progression in the last decade: from small-scale designs to commercial solutions at the grid (BESS), industrial, building and microgrid levels [
2]. In parallel, market and status reports (IEA, REN21) show accelerating investment in RES and increasing demand for flexibility, which directly translates into demand for energy storage in the 2030 horizon [
1,
2].
In the literature, energy storage technologies are most often classified according to the function performed and the dominant energy accumulation mechanism. In this view, there are five main classes of solutions (
Figure 2). The first group is electrochemical technologies, encompassing different battery types such as lithium-ion batteries, lithium-iron-phosphate batteries, systems based on NMC/NCA chemistries, sodium-ion batteries, flow batteries and solid-state solutions, which are being developed intensively. The second category is made up of mechanical and physical technologies, which include pumped hydro energy storage, compressed air energy storage (CAES), flywheels and gravity systems. The subsequent group comprises thermal energy storage technologies (TES), which encompass the accumulation of sensible, latent, and chemical heat. A separate class is formed by chemical technologies, most often incorporated within the Power-to-X concept, in which electricity is converted to carriers such as hydrogen, ammonia, synthetic methane or liquid fuels. Complementing this classification are electrical technologies, including super capacitors and superconducting magnetic energy storage systems (SMES), characterised by very fast response times but limited energy capacity. Each class has a specific system function: from fast power regulation and smoothing services (super capacitors, Li-ion), to multi-hour RES profile balancing (Li-ion/LFP, Na-ion, flow, TES, PHS/CAES), to seasonal storage and sector coupling (Power-to-X). In system practice, it is crucial to match the technology to the scale and time horizon of the service: seconds, minutes (stabilisation), hours (peak-shaving), days (time-shift), weeks/months (long-term storage) [
2,
10,
16].
From the perspective of
Figure 2, the five technology classes also differ in the type of system problem they are designed to solve. Electrochemical systems are primarily used for fast and medium-duration balancing, high-quality ancillary services and modular deployment at distribution and behind-the-metre level. Mechanical and physical systems, especially PHS and CAES, are more suitable for bulk storage and longer discharge durations, while flywheels occupy a niche in ultra-fast dynamic services. Thermal energy storage is particularly important where electricity and heat sectors interact, including district heating, industrial heat recovery and CSP systems. By contrast, Power-to-X technologies form a distinct category because they do not merely store energy, but convert electricity into alternative carriers such as hydrogen, synthetic methane, liquid e-fuels or ammonia, thereby enabling sector coupling and long-duration or seasonal balancing. Electrical storage technologies such as supercapacitors and SMES remain important mainly for very short response times and power-quality support rather than for energy shifting.
Energy Strategy Reviews highlights a strong increase in publications and implementations after 2017, which coincides with a reduction in the cost intensity of battery components and the maturity of power control on the inverter/PCS and EMS side [
2]. The IEA’s projections for RES by 2030 (tripling capacity post-COP28) remain ambitious, but still insufficient without a leap in flexibility and grid modernisation, which, in terms of energy storage, is a necessary component (both in the power industry and in the heating sector/process heating) [
1]. REN21 reports historically record increases in RES capacity but also points to gaps in integration and system infrastructure that inhibit the full use of volatile sources, so it can be inferred that the role of storage will therefore grow not only for technical, but also for regulatory and market reasons [
12].
At the same time, the effective integration of storage into modern distribution networks depends not only on storage chemistry or rated capacity, but also on the quality of inverter-side coordination and control. In storage-rich and distributed-resource-rich grids, voltage fluctuations, power imbalances and mode-switching complexity increasingly become limiting factors for practical deployment. Recent work on voltage–power self-coordinated control for load-side storage and distributed generation inverters shows that advanced control strategies can improve local power balance and voltage regulation while reducing the operational complexity of multi-mode inverter systems. This indicates that future storage deployment should be analysed not only in terms of storage medium characteristics, but also in conjunction with the development of intelligent inverter control, EMS logic and distribution-grid coordination architectures [
17].
The central criterion for assessing energy storage technologies in this review is their contribution to the principles of sustainable development, understood in a multidimensional perspective. The core element of this assessment is the environmental footprint analysed over the entire life cycle of the technology (life cycle assessment, LCA), which includes the raw material extraction phase, the production processes, the exploitation phase and recycling or end-of-life disposal. Of equal importance is operational safety, including thermal and fire risks, the toxicity of the components used and potential emissions and environmental pollution in the event of an accident. The systemic impact of the technology, understood as the ability of energy storage to reduce greenhouse gas emissions by better matching generation from renewable energy sources with actual demand, is also an important criterion. Complementing this perspective is system resilience, which also includes cyber resilience of control and energy management systems (BMS, EMS, SCADA), as digital incidents can lead to material failures, losses of resources, and indirect but significant environmental impacts (
Table 3).
4.2. Electrochemical Technologies (Batteries)
Contemporary research on electrochemical energy storage technologies focuses on simultaneously improving battery performance, reducing raw material pressures and increasing operational safety, which is crucial in the context of the rapid growth of stationary applications. Recent studies emphasise that the next generation of lithium-ion and lithium-metal batteries aims to combine high energy density with long cycle life and improved safety through advanced electrode architectures and electrolyte design. Dominant material developments include, in particular, modification of electrode chemistry, including cathodes with reduced or completely eliminated cobalt content, such as lithium-iron-phosphate (LFP) and high-nickel cathode materials with significant reduction in Co. In parallel, new anode concepts are being intensively developed, including silicon and composite anodes in lithium-ion systems and hard carbon anodes in sodium-ion batteries, which enable increased capacity and operational stability using more available raw materials. Solid and gel electrolytes in solid-state technologies, seen as a potential breakthrough in safety and energy density, also remain an important area of research. Material development is enhanced by advanced battery management system (BMS) algorithms aimed at reducing cell degradation through precise management of temperature, charge and discharge profiles [
2,
6].
In parallel with material development, recycling processes for electrochemical battery systems and end-of-life management strategies are being intensively researched. In the case of lithium-ion batteries, hydrometallurgical processes enabling the recovery of lithium, nickel, cobalt and manganese are growing in importance, as well as the concept of direct recycling, which involves preserving the structure of the cathode materials and reusing them. These approaches have the potential to significantly improve the environmental balance throughout the battery life cycle and reduce the need for critical raw materials. Sodium-ion technologies, on the other hand, are seen as solutions with lower raw material pressure and potentially less material toxicity, although effective methods for their recycling are still under development [
2,
18,
22,
23,
24].
The operational safety of electrochemical energy storage is the third key area of research and implementation. The LFP chemistry has significantly better thermal stability compared to NMC/NCA cathodes, which translates into a reduced risk of thermal runaway in BESS. Solid-state technologies, on the other hand, seek to eliminate liquid, flammable electrolytes, which, in the long term, can provide significant benefits in terms of both operational safety and life cycle analysis results, assuming that adequate technological maturity and production scalability are achieved [
2,
9,
21].
Such focused development of electrochemical battery technologies indicates that their future role in energy systems will be determined not only by technical performance, but also by their ability to reduce environmental pressures, improve safety and integrate the principles of a circular economy, making them one of the key pillars of a sustainable energy transition. For better illustration, a comparison of the above technologies is summarised in a table below (
Table 4).
4.3. Mechanical and Physical Energy Storage Technologies: Operating Principle and System Role
Mechanical–physical energy storage technologies encompass pumped hydro energy storage (PHS), compressed air energy storage (CAES) systems, flywheel-based energy storage systems (FESSs), and gravity-based solutions that utilise the lifting and lowering of masses. The common feature of these technologies is the conversion of electrical energy into mechanical or potential energy and its subsequent recovery, which is done without chemical reactions. As a result, these systems have a very long operating life, high cyclic load resistance and short response times, making them a natural complement to variable generation renewable energy sources (
Table 5) [
2,
9,
25,
26].
Pumped hydro energy storage (PHS) remains the most mature and widespread system-scale energy storage technology. Their operating principle is based on a two-tank water system, in which electricity is stored by pumping water into the upper tank and then recovered in generation mode using water turbines. PHSs are characterised by high specific power outputs of up to hundreds of megawatts, high cycle efficiencies of 70–85% and a very long plant life. These systems play a key role in shifting energy over time, dampening fluctuations in generation energy from RES and providing regulatory services, including primary and secondary regulation and black-start capabilities. Their main constraints remain topographical and hydrological requirements and potential environmental impacts, necessitating detailed environmental impact assessments and compensation activities [
9,
10,
26]. In contrast, research on micro-PHS confirms the usefulness of this technology on a local scale and in stabilising frequency and power balance in islanded microgrids [
27].
Compressed air energy storage (CAES) provides an alternative for locations where PHS construction is difficult. The technology involves compressing air and storing it in salt caverns, pore structures or aboveground tanks, and then using the energy of the compressed air to drive turbines or expanders. There are diabatic, adiabatic and isothermal variants, which differ in the way the heat of compression is managed. CAES technology enables energy storage on the megawatt-hour to gigawatt-hour scale, with very low self-discharge and long operating times, but its use is limited by the availability of suitable geological structures and, in diabatic variants, by the additional emissions associated with reheating the air. Reliability analyses of power systems indicate that the integration of CAES with wind farms significantly improves power adequacy and system stability, especially at high RES shares [
2,
16,
28].
Flywheels (FESS) represent mechanical energy storage systems with very short reaction times, in which energy is accumulated in the form of kinetic energy of a rotating mass. Modern FESSs use magnetic bearings, a vacuum environment and advanced power electronics to achieve cycle efficiencies of 85–95% and cycle counts in excess of 10
5. Their main advantage is their ability to respond instantly to load changes, making them particularly useful for frequency control, improving power quality and smoothing short-term fluctuations in renewable generation output. However, a limitation remains in the short storage time, usually counted in seconds or minutes, which narrows the scope of their applications to system services of a dynamic nature [
9,
10].
Classic mechanical solutions are supplemented by gravity storage systems other than pumped hydro energy storage (PHS), wherein energy is stored by elevating and lowering masses such as concrete blocks, rock spoil, or transport platforms. These systems can be implemented in the form of towers, shafts, pits or rail solutions and are characterised by simple operating physics, long lifetimes and potentially low life-cycle costs. However, their efficiency is highly dependent on the mechanical and drive systems used, and implementation requires suitable spatial and location conditions. Literature reviews indicate that these technologies can play a complementary role to PHS, especially in regions lacking adequate water resources [
2,
16].
Taken together, mechanical–physical energy storage technologies play a key role in stabilising electricity systems with a high proportion of renewable energy sources. They provide both short-term synthetic inertia and power quality improvement, as well as long-term energy shifting and power reserve building. Development projections to 2030 indicate that PHS technology will remain the “anchor” of large-scale storage, CAES will gain importance in locations with suitable geology, flywheels will maintain their role in dynamic services, and gravity storage will be developed as a niche but promising solution in specific local conditions [
2,
16,
29].
4.4. Thermal Energy Storage (TES)
TES (Thermal Energy Storage) technologies are an important part of the energy transition, particularly in the district heating, industrial and solar energy sectors. Their importance stems from the possibility of temporarily decoupling the production and consumption of thermal energy, allowing for greater flexibility in energy systems and better integration of renewable energy sources. In the literature, TES technologies are usually classified into three main groups: sensible heat storage (SHS), latent heat storage (LHS) using phase change materials (PCM) and thermochemical storage (TCS), in which energy is stored in the form of chemical reaction potentials or sorption processes [
9,
16,
30,
31,
32].
Phase change materials (PCM) are increasingly investigated as effective thermal energy storage media due to their high latent heat capacity and ability to stabilise operating temperatures in energy systems. Recent studies also highlight their potential for improving thermal management of lithium-ion batteries, where PCM-based structures can significantly enhance heat dissipation and reduce temperature gradients within battery packs [
33,
34].
SHS facilities are based on heating a medium with a known heat capacity, such as water, glycols, concrete, stone deposits or molten salts. These are technologically mature solutions, characterised by a low unit cost per thermal output unit (e.g., kWh) and a wide range of applications, from the construction industry and district heating networks to concentrated solar power (CSP) plants. Systems based on molten nitrate salts (NaNO
3/KNO
3) play a particularly important role here, enabling operation in the temperature range up to 500–600 °C and achieving cycle efficiencies of 70–90% [
16,
31,
32,
35].
LHS technologies use the phenomenon of phase transformation, which allows for a much higher energy storage density with a nearly constant operating temperature. The most commonly used PCMs include paraffins, salt hydrates and nitrates. These solutions have found applications in buildings, HVAC systems, the refrigeration industry and selected industrial processes. Their main limitations are the low thermal conductivity of paraffins and the cyclic stability problems of salt hydrates, such as overcooling and phase separation. In response to these challenges, intensive research is being conducted on PCM composites, micro-encapsulation and additives that increase thermal conductivity, such as graphite or aluminium [
9,
31,
36,
37,
38,
39,
40].
The most advanced but least mature groups are the TCSs, where energy is stored in the form of chemical bond energy or sorption processes. These systems, based inter alia on CaO/Ca(OH)
2 or MgO/Mg(OH)
2 reaction pairs and porous materials such as zeolites or silica gel, enable long-term thermal energy storage with virtually no standstill losses, achieving energy densities in excess of 250 kWh/m
3. Despite their high potential, TCS technologies remain mainly at the research and demonstration stage and their further development depends on improved cyclic stability and integration with efficient heat exchangers [
9,
16,
31,
32].
A summary of the key technical and environmental characteristics of the three classes of TES is presented in a table that illustrates the differences in operating temperatures, energy density, level of technological maturity and potential environmental impacts (
Table 6).
Applications of TES technology cover a broad spectrum of sectors. In the industry, these systems facilitate the stabilisation of thermal profiles in technological processes and promote the efficient utilisation of waste heat. This advancement, particularly within the food and chemical sectors, leads to a reduction in CO
2 emissions by 10–25%. In buildings, the integration of PCM into structural elements and HVAC systems leads to a reduction in peak energy demand and improved thermal comfort. In CSP technology, molten salt-based SHS systems enable power generation for 6–10 h after sunset, increasing the turbine capacity factor to more than 60%. Consequently, in heating networks, large water tanks with a capacity of GWh
th facilitate the integration of energy from renewable sources and industrial surpluses, leading to a reduction in fossil fuel consumption by up to 20–30% on a system-wide scale [
9,
16,
31,
32,
35].
Examples of TES configurations and their application areas are summarised in
Table 7, maintaining the distinction between SHS, LHS and TCS systems.
Current research trends in the TES area focus on improving the thermal conductivity of PCMs through the use of nanostructured additives and metallic foams, the development of stable salt eutectics for CSP systems with temperatures above 600 °C, as well as on enhancing cycling durability and reaction kinetics in TCS systems. Pilot test results indicate that TCS parameters can remain stable even after 1000 cycles of operation, confirming the potential of these technologies for long-term thermal energy storage [
9,
16,
31,
32,
41].
From a systemic perspective, TES technologies play a key role in decarbonising the district heating, industrial and power engineering sectors. They make it possible to increase auto-consumption of energy from RES, reduce the use of fossil fuels and reduce the need for gas reserves in power engineering systems. With the right choice of materials (non-toxic PCMs), closed-loop salts or regenerated sorbents, TES technologies have a favourable environmental balance and improved life cycle analysis results compared to conventional heat sources [
9,
16,
32,
35,
36,
37,
40,
41].
Thermal energy storage technologies, particularly those based on phase change materials (PCM), have attracted growing attention due to their ability to store and release heat at nearly constant temperature, which makes them suitable for thermal management applications in energy systems and electronic devices (e.g., hybrid PCM heat sinks) [
44].
4.5. Power-to-X (PtX) Technologies: Idea, Conversion Chains, Sectoral Integration and Determinants of Emission Reductions
Power-to-X (PtX) refers to the conversion of electricity (optimally from renewable energy sources) into chemical carriers and energy products, such as hydrogen (Power-to-Hydrogen, PtH
2), synthetic methane (Power-to-Gas, PtG), liquid fuels (Power-to-Liquid, PtL) and ammonia (NH
3), which acts as both an industrial product and an energy carrier (
Table 8) [
2,
10,
20]. The core of the PtX chains is the electrolysis of water realised in alkaline medium (AEL, alkaline electrolysis), proton exchange membrane (PEM) and high temperature (SOEC, solid oxide electrolysis cell) variants. The hydrogen (H
2) produced is a key intermediate, which can then be utilised in several complementary pathways: stored compressed, liquid, in salt caverns, converted into synthetic methane with CO
2, used for the synthesis of ammonia using the Haber-Bosch method or, together with CO
2, converted to liquid fuels (e.g., methanol, e-diesel) [
9,
25,
45,
46,
47,
48,
49,
50,
51,
52,
53,
54].
However, the efficiency and environmental sense of the entire PtX chain are strongly determined by three systemic factors: (I) the availability and nature of the CO
2 source (process, biogenic or DAC—Direct Air Capture), (II) the profile and variability of RES generation, and (III) the degree of process integration, including the use of waste heat, process steam and cooling [
2,
9,
25,
30,
46,
50,
51,
53,
54].
In technological practice, the selection of the type of electrolyser and its operation within the energy system is of paramount importance. Alkaline electrolysis (AEL) remains a mature and stable solution in continuous operation but is less flexible in the situation of rapid load changes. PEM electrolysers have higher dynamics and better interaction with RES but involve greater material and cost pressures. In turn, SOECs utilise high-temperature steam and present the potential for the highest efficiency at the cell stage, particularly when integrated with industrial applications or concentrating solar energy. However, they remain a technology that is currently in the process of development and gradual implementation [
2,
9,
30,
47,
48,
50,
52,
53,
54]. The integration of electrolysers with RES requires power buffering, management of operating profiles and (in practice) partial hybridisation with the electricity grid to reduce downtime and increase the utilisation of installed capacity [
2,
9,
30,
50,
54].
The hydrogen produced can be stored and transported as gas (200–700 bar) or liquid (LH
2, Liquid Hydrogen), and the choice of technology depends on the scale of the system, the storage horizon and logistics. This is complemented by liquid organic hydrogen carriers (LOHCs), allowing the use of liquid fuel-like infrastructure at the expense of hydrogenation and dehydrogenation steps, and seasonal storage in salt caverns; these solutions are considered crucial in a systems perspective [
47,
50,
55,
56,
57,
58]. At the same time, the integration of hydrogen into the gas network is limited by acceptable doping levels and material compatibility of the transmission and distribution infrastructure [
50,
56].
Hydrogen produced in Power-to-X systems can also be converted back into electricity through fuel cells, especially proton exchange membrane fuel cells (PEMFCs). PEMFCs are characterised by high efficiency, low operating temperature, fast dynamic response and zero direct carbon emissions at the point of use. For this reason, they are considered one of the most promising technologies for transport applications and flexible hydrogen-based power systems. Their integration with electrolysis-based hydrogen production closes the conversion loop within the broader PtX framework [
59].
In the Power-to-Gas pathway, hydrogen reacts with carbon dioxide, leading to the production of SNG (synthetic natural gas) methane via Sabatier catalytic methanation or biomethanation. The advantage of this approach is the compatibility of the product with existing gas infrastructure and the possibility of long-term energy storage, while the provision of CO
2 sources, thermal integration of the reactors and control of residual methane emissions (“methane slip”) remain critical [
9,
46,
50,
53,
54,
56,
60]. Alternatively, the Power-to-Liquid pathway involves the synthesis of methanol and synthetic fuels using the Fischer-Tropsch process, including e-diesel and sustainable aviation fuels (SAF). It requires stable process conditions, high purity of reactants and access to CO
2 (including from DAC). Furthermore, the integration and utilisation of waste heat significantly enhances the outcomes of the life cycle assessment for the entire chain [
48,
49,
50,
51,
52,
53,
54]. A particular role is played by ammonia (NH
3) produced from “green” H
2, which can act as a fuel, energy carrier and intermediate hydrogen storage; however, limitations to the development of this pathway relate to nitrogen oxide (NO
x) emissions, toxicity, safety requirements and the energy intensity of cracking at the point of use [
49,
50,
53,
55].
The added value of PtX is the ability to couple sectors and decouple generation and energy consumption over time, which is crucial with a high proportion of PV and wind [
2,
9,
30,
50,
54]. The most promising integration directions include refineries and chemistry (H
2, methanol, NH
3), metallurgy (replacing fossil reducers with green hydrogen), fertiliser industry (green ammonia), power generation (SNG as seasonal storage, gas turbines and hybrid systems) and transport (SAF, e-diesel, e-methanol, NH
3 in shipping) [
9,
25,
46,
48,
49,
50,
51,
52,
53,
54,
56,
57]. Process integration can additionally include the use of waste heat (e.g., in SOEC and methanation), the provision of system services by controlling the operation of electrolysers and the linking of CO
2 streams between sources and receivers [
2,
9,
30,
46,
50,
56,
57].
An important complementary dimension of sector coupling is the role of electric vehicles as distributed and mobile storage resources in vehicle-to-grid (V2G) and vehicle-to-home (V2H) schemes. However, the practical system value of EV fleets cannot be assessed only from nominal battery capacity, because it depends strongly on behavioural factors such as arrival and departure times, charging preferences, state-of-charge trajectories, daily mobility patterns and users’ willingness to participate in grid services. Recent review evidence indicates that behavioural modelling remains one of the key methodological challenges in V2G analysis, because simplified assumptions about vehicle availability may substantially overestimate realistic flexibility potential. Therefore, EV-based storage should be treated as a promising but behaviour-constrained flexibility resource whose system contribution depends on both technical integration and robust user-centred modelling frameworks [
61].
The potential to reduce greenhouse gases (GHG) in PtX chains is conditional. The primary factors include the emission intensity of the electricity used for electrolysis (gCO
2/kWh), the source of CO
2 utilised in the synthesis (biogenic, process or DAC versus fossil CO
2), the efficiency of the conversion stages, and the extent of thermal integration and waste heat utilisation [
2,
9,
30,
48,
50,
51,
52,
53,
54]. In PtG, SNG production can replace fossil gas and support seasonal storage as long as the “methane slip” is controlled; with the use of biogenic CO
2, the balance of the chain can approach climate neutrality [
46,
50,
51,
53,
56,
57,
60]. PtL is particularly relevant for transport segments that are difficult to electrify (aviation and shipping), and the use of green H
2 and biogenic CO
2 or CO
2 from DAC allows for a significant reduction in life-cycle emissions (LCA, Life Cycle Assessment) [
48,
51,
53,
54,
56]. In the case of NH
3, real emission benefits require green H
2 and control of NO
x emissions, including selective catalytic reduction (SCR) systems, while meeting high safety standards [
50,
51,
53,
55].
The economic determinants of PtX are dominated by the cost of electricity from RES, often described by the levelised cost of electricity (LCOE), as well as the capital and operating expenditures (CAPEX/OPEX) of electrolysers and synthesis plants, economies of scale and technology learning, as well as the possibility to monetise and utilise waste heat [
2,
9,
30,
48,
50,
52,
53,
54]. By 2030, the primary challenges will include AEL and PEM scaling, enhancing their dynamic operational capabilities in alignment with RES, and implementing SOEC in locations where high-temperature steam or process heat streams are accessible [
2,
9,
30,
50,
52,
53,
54]. Simultaneously, integrated PtG and PtL systems with heat recovery and adaptation to local CO
2 streams, along with H
2/NH
3/LOHC logistics and seasonal storage in salt caverns, will be developed [
9,
25,
47,
50,
55,
57,
58]. Ultimately, however, the pace of implementation and financial credibility of PtX projects will be determined by the regulatory and market framework, including certification of “greenness”, definitions and support for RFNBO (Renewable Fuels of Non-Biological Origin) and recognition in the ETS (Emissions Trading System) and CBAM (Carbon Border Adjustment Mechanism) mechanisms [
50,
62,
63,
64,
65].
4.6. Technology Comparison and Development Prospects
In the review literature and reports from international institutions, a functional division of energy storage technologies into five main classes has become established: electrochemical, mechanical/physical, thermal (TES), chemical (Power-to-X) and electrical (super capacitors and SMES) (
Table 9) [
1,
2,
5]. This classification reflects not only the technological differences, but above all the different system roles of the different solutions, resulting from the trade-offs between round-trip efficiency, storage time, investment and operating costs, durability and life-cycle environmental impact [
1,
2,
12].
For short to medium time horizons (minutes to a few hours), battery-based electrochemical systems, particularly lithium-ion technologies, currently play a dominant role. Their high efficiency, fast response and market maturity make them an essential tool for services such as peak-shaving, energy arbitrage and frequency regulation. At the same time, numerous reviews have highlighted that the environmental profile of Li-ion batteries remains heavily dependent on cathode chemistry and the raw material supply chain. The transition from NMC/NCA technology towards LFP and the development of sodium-ion batteries and recycling significantly reduce material pressures and carbon footprints. Within the same time segment, with a focus on durability and energy scalability, flow batteries (VRFB, Fe-Cr) are gaining significant importance. They allow for the independent scaling of power and capacity and are distinguished by their exceptionally long lifespans, albeit with the trade-off of lower energy density and greater spatial requirements [
2,
66,
67,
68]. An additional feature of many aqueous redox flow batteries is the relatively slow electrochemical kinetics of redox reactions in aqueous electrolytes. Therefore, electrode modification and catalytic activation are often applied to improve reaction rates, reduce overpotentials and enhance the overall performance of RFB systems [
69].
In daily and multi-day horizons, mechanical–physical technologies play a crucial role, particularly pumped hydro energy storage (PHS) and compressed air energy storage (CAES) systems. PHS remains the most mature large-scale technology, offering high efficiency and multi-decade durability, but its development is strongly constrained by topographical considerations and hydrological impacts. CAES is an alternative to sites without hydrological conditions, with the important environmental distinction between diabatic and adiabatic options. The latter, through the integration of compression heat storage, makes it possible to significantly reduce emissions [
2,
16,
28,
30]. Flywheels (FESS) occupy a niche but critical position in this landscape in terms of system stability, providing millisecond-scale response and a very high number of cycles, albeit with short hold times [
10,
21].
In parallel, thermal energy storage (TES) technologies, whose importance goes beyond the electricity sector, play an important role in the energy transition. SHS based on water and molten salts offers low cost and high maturity, especially in district heating and CSP systems. Meanwhile, phase change materials (PCM) and thermochemical systems (TCS) enhance energy density and facilitate extended storage periods, accompanied by progressively improving material stability [
1,
16,
31,
35,
41]. TES technology acts as a key element in the decarbonisation of the heat sector; its importance in the emissions balance remains comparable to that of the electricity sector [
41,
70].
The longest storage horizons (weeks to seasons) are achieved by Power-to-X technologies, in which RES electricity is converted to chemical carriers such as hydrogen, synthetic methane, liquid fuels or ammonia. These solutions enable the coupling of the electricity, gas, fuel and industrial sectors, but their environmental and economic efficiency remains strongly dependent on the emission level of the energy feeding the electrolysis, the CO
2 source and the specific emissions in the conversion chain (e.g., “methane slip” or NO
x) [
2,
12,
51,
53]. For this reason, PtX is regarded not as a substitute for short-term energy storage but as a complementary system for seasonal balancing and the decarbonization of sectors that are challenging to electrify [
56,
57,
60,
71].
Forecasts until 2030 suggest that the growing share of RES will necessitate the concurrent advancement of a comprehensive range of storage technologies, with the likelihood of any single solution prevailing being low. BESS, especially in LFP chemistry, will remain the primary tool for short-term flexibility, while longer-term technologies such as flow, PHS, CAES and TES will become increasingly important as the demand for energy shifting increases on a daily and multi-day scale [
1,
2,
12]. PtX, on the other hand, will be developed selectively, in close connection with climate policies, the availability of low-cost renewable energy and the regulatory framework for RFNBO (Renewable Fuels of Non-Biological Origin) as well as with mechanisms such as ETS (Emissions Trading System) or CBAM (Carbon Border Adjustment Mechanism) [
2,
62,
63,
64,
65].
From a systems perspective, it is becoming increasingly clear that the highest technical, economic and environmental value is offered by hybrid architectures, combining different storage technologies depending on the time horizon required and the type of system service (
Table 10).
Combining BESS with TES, PHS, CAES, FESS or PtX separates the functions of fast control, energy shifting and seasonal storage, while reducing component degradation and improving the results of LCA analyses. Consequently, the future of energy storage lies not in the competition of single technologies, but in their complementary coexistence, supported by policies and market models that price not only energy, but also flexibility, sustainability and environmental benefits over the entire life cycle (
Table 11) [
1,
2,
12,
15,
72].
The comparison presented in
Table 10 and
Table 11 indicates that no single storage technology can simultaneously optimise response speed, discharge duration, material sustainability, cycling stability and system-level flexibility. This reinforces the rationale for hybrid storage configurations based on complementary functional roles of different technologies. Such a perspective provides an important bridge between the technology-specific review and the broader system-level recommendations presented in the concluding section.
Due to the wide diversity of energy storage technologies, their technical and operational characteristics vary significantly depending on the underlying storage principle and intended application. Key parameters commonly used to compare storage technologies include energy density, round-trip efficiency, lifetime, technological maturity, and typical application domains.
Table 12 summarises the main characteristics of major energy storage technologies discussed in this study.
Battery storage primarily supports short-duration grid flexibility, while thermal energy storage contributes to the decarbonization of heating systems and Power-to-X technologies enable long-duration storage and sector coupling. Therefore, the environmental performance of energy storage technologies should be evaluated in relation to the system services they provide [
71].