An In-Depth Life Cycle Assessment (LCA) of Lithium-Ion Battery for Climate Impact Mitigation Strategies

: Battery energy storage systems (BESS) are an essential component of renewable electricity infrastructure to resolve the intermittency in the availability of renewable resources. To keep the global temperature rise below 1.5 ◦ C, renewable electricity and electriﬁcation of the majority of the sectors are a key proposition of the national and international policies and strategies. Thus, the role of BESS in achieving the climate impact mitigation target is signiﬁcant. There is an unmet need for a detailed life cycle assessment (LCA) of BESS with lithium-ion batteries being the most promising one. This study conducts a rigorous and comprehensive LCA of lithium-ion batteries to demonstrate the life cycle environmental impact hotspots and ways to improve the hotspots for the sustainable development of BESS and thus, renewable electricity infrastructure. The whole system LCA of lithium-ion batteries shows a global warming potential (GWP) of 1.7, 6.7 and 8.1 kg CO 2 eq kg − 1 in change-oriented (consequential) and present with and without recycling credit consideration, scenarios. The GWP hotspot is the lithium-ion cathode, which is due to lithium hexaﬂuorophosphate that is ultimately due to the resource-intensive production system of phosphorous, white, liquid. To compete against the fossil economy, the GWP of BESS must be curbed by 13 folds. To be comparable with renewable energy systems, hydroelectric, wind, biomass, geothermal and solar (4–76 g CO 2 eq kWh − 1 ), 300 folds reduction in the GWP of BESS will be necessary. The areas of improvement to lower the GWP of BESS are as follows: reducing scopes 2–3 emissions from fossil resource use in the material production processes by phosphorous recycling, increasing energy density, increasing lifespan by effective services, increasing recyclability and number of lives, waste resource acquisition for the battery components and deploying multi-faceted integrated roles of BESS. Achieving the above can be translated into an overall avoided GWP of up to 82% by 2040.


Introduction
Battery energy storage systems (BESS) are used to shave off-peak electricity demands, stabilise grid electricity systems and increase the proportion of renewable energy that is intermittent in the energy mix. Their applications are manifold including enhanced stability, reliability, security and efficiency of whole energy system. BESS can be optimised for their multi-faceted integrated contributions to maximise savings in carbon footprint in the electricity sector. At present, there are a limited number of studies on environmental impact savings, global warming potential or climate change impact potential (GWP) being a critical one, by BESS. Carbon footprint saving by BESS needs to be accurately evaluated to justify investment particularly to mitigate climate change impact in the electricity sector.
Over the past two decades, considerable innovations have been made in cathode and anode materials including recyclability, power and energy densities and life of BESS. With

Literature Review for the Technical and Environmental Performances of BESS
Over the past two decades, considerable innovations are seen in cathode and anode materials including 2D planar carbon haeckelite structures with lithium intercalation, recyclability, power and energy densities and lifespan of BESS [8]. The types of BESS reported are Li-ion, Li metal polymer, Ni metal hybrid, Na metal chloride, sodium-sulphur, nickel-cadmium, lead acid and V redox flow battery with energy (kWh kg −1 ) and power (kW kg −1 ) densities of 0.12-0.18 and 0.2-0.3; 0.11-0.14 and 0.12-0.2; 0.06-0.1 and 0.07-0.21; 0.05-0.1 and 0.02-0.18; 0.06-0.13 and 0.01-0.1; 0.04-0.06 and 0.03-0.11; 0.025-0.045 and 0.05-0.12; and <0.025 and <0.02, respectively [9]. Compared to electrochemical technologies for storage, compressed air energy storage and pumped hydro storage are mature large scale low-cost options, more suited for fossil-based conventional grid energy systems [10]. However, fossil energy systems (coal, oil and natural gas) have higher global warming potential 0.475-1.3 kg CO 2 eq kWh −1 compared to renewable energy systems (hydro, wind, solar, bioenergy and nuclear) 0.01-0.1 kg CO 2 eq kWh −1 [10]. A net zero carbon future neutralising greenhouse gas emissions by balancing between carbon sources and sinks is only achievable if electricity generation is entirely from renewable resources and the majority energy demand is met by electricity. Thus, there is increasing pressure on the sustainable development of BESS that allows renewables integration into infrastructure. The GWP of BESS varies widely and exceeds that of fossil-based energy systems, which may not need storage. There is no consensus on the GWP of BESS for future targets. Amongst the lithium-ion batteries, lithium iron phosphate, lithium nickel cobalt manganese, lithium manganese oxide, lithium cobalt oxide, lithium nickel cobalt aluminium, lithium cobalt phosphate, lithium iron manganese phosphate, lithium metal polymer and lithium cobalt nickel have been studied for chemistries and LCA performances [11]. An LCA study of lithium cobalt phosphate cathode based battery shows a GWP of 70.7 kg CO 2 eq kWh −1 and the cathode as the hotspot incurring 75% of the total GWP [12]. Another study reports a GWP of 185-440 kg CO 2 eq MWh −1 [13]. Thus, there could be a difference in GWP of several hundred manifolds between the published studies. This calls for a benchmarking LCA study based on a globally standard database. The functional unit of an LCA study of lithium-ion batteries also varies between per unit mass and unit energy stored of BESS. Some studies chose to report the LCA results per kg batteries. For example, an LCA study gives 12.5 and 4.4 kg CO 2 eq kg −1 battery production for n-methyl-2-pyrrolidone solvent and water solvent-based lithium-ion batteries [14]. The LCA results vary widely depending on the choice of the functional unit for the LCA, energy or mass unit due to varying energy density [15]. Their study has shown a GWP of 22.97 kg CO 2 eq kg −1 lithium-ion battery with 55% resulting from the cathode [15]. In addition to energy density, the lifespan of BESS is another key variable. It is desired to achieve both the increased lifespan in each life and the number of times BESS can be recycled. A cascaded life cycle analysis of Li-ion battery, first applied in electric vehicle (8 years lifetime), followed by repurposing to store energy for the grid (10 years lifetime), gives a global warming potential of 0.25 kg CO 2 eq kWh −1 [16]. It is expected that after the first life in the electric vehicle (about 10-20 years), which causes 20-30% decay in capacity, BESS can be reused for connection to a grid system (5-10 years) [17]. Another study identifies that the main difference in LCA of BESS is due to the way they are disposed of and recycled [18]. Although treatment and recycling incur only 10-20% of overall life cycle impacts, these vary from one type to another type of BESS [18]. High energy density and long life expectancy would drive the technology development in BES [19]. Research has been conducted on the analysis of life cycle climate impact mitigation by BESS in the UK and made available as an industrial report in 2019 [20]. Another similar study has been published that analyses the avoided GWP and natural gas consumption by BESS integrated renewable electricity systems in the UK [21]. The overall results obtained are very similar in these two studies [20,21]. Both have shown 87-90% avoided GWP by BESS integration to the UK grid electricity system. However, the study in [21] does not show all plausible ways to improve the GWP of BESS necessary to compete against natural gas. In addition, the core cause of the GWP impact hotspot has remained unrevealed in these studies demanding an in-depth rigorous and comprehensive LCA of BESS that this study offers using lithium manganese oxide cathode in lithium-ion batteries as an example. Without the improved GWP of BESS, renewables can't triumph fossil-based electricity systems. This study systematically shows a global BESS life cycle inventory model, all plausible ways to improve the life cycle GWP of BESS, the maximum life cycle GWP limit for BESS to transcend fossil counterparts and thereby the avoided GWP by BESS-connected renewable electricity systems. The paper is structured as follows. The following sections discuss the LCA methodology adopted in this study and the results of the LCA of BESS and BESS-connected renewable electricity systems. The final section concludes the main results of this research.

Materials and Methods
LCA is a standardised methodology for holistic whole system environmental impact assessment [22][23][24][25][26]. The approach this study takes is a holistic, systematic and rigorous LCA to establish overall environmental impact savings by BESS in the context of the UK renewable energy system. Amongst numerous life cycle impact categories, the most important one that should be included for energy-saving services is GWP impact or climate change impact potential. The other important atmospheric impacts include urban smog (local), acidification potential (regional) and ozone depletion potential (global). Important aquatic impact potentials include freshwater depletion, aquatic ecotoxicity potential and eutrophication potential. Terrestrial ecotoxicity potential is a land emission impact indicator. In addition, life cycle impact assessment methods provide several human health-related impact potentials. Many life cycle impact assessment methods have been developed with differing characterisation factors of pollutants and impact categories with distinctive units depending upon demography, e.g., ILCD and Impact 2002+ for Europe, TRACI for the USA and CML from Leiden University Netherlands. The ReCiPe is a popular choice giving a comprehensive representative range of environmental impact characterisations. The life cycle impact assessment methodologies and the selection rationale are discussed in earlier work [27]. For this study, the primary environmental impact category selected is the GWP over 100 years according to the Intergovernmental Panel on Climate Change (IPCC). For consistency check in the in-depth hotspot analysis of BESS by LCA, the ReCiPe, CML and ILCD methods have been applied. Also, the other important life cycle environmental impact potentials, acidification potential (AP), eutrophication potential (EP) and fossil depletion potential (FDP) using the CML characterisation factors and photochemical oxidant creation potential or urban smog (POCP) using the ILCD characterisation factors are shown for the various UK electricity generation systems [28].
LCA is a standardised holistic and rigorous methodology for the assessment of environmental impacts of cradle-to-grave or cradle-to-cradle supply chain systems in temporal and spatial scales. The methodology has been discussed in the ISO14040-44 (International Organization for Standardization) [22][23][24][25][26]. According to the methodology, all stages of the life cycle of a product or service should be considered for a comprehensive assessment of environmental impacts. The life cycle stages of a product or service include raw material acquisition, manufacturing, logistics, use and resource circulation [28]. According to the waste disposal hierarchy, future systems should be developed to avoid the bottom of pyramid options, i.e., landfill, disposal. This emphasises the importance of embedding a circular economy for the sustainable development of systems. The circular economy should be an embedded ethos in the development of BESS that considers resource circulation for the indefinite life of BESS.
According to the ISO14040-44, LCA comprises four interactive stages: goal and scope definition, inventory analysis, impact assessment and interpretation. In the goal and scope definition, objectives and system boundary and definition should be included. Demography of the supply chains of the products or services under consideration should be defined, alongside functional unit and configuration of the system. Impact characterisations that are relevant and important for the system under consideration should also be discussed at this stage of LCA. To establish the role of BESS by LCA, not only the LCA of BESS should be considered, but also the LCA of resources and technologies for electricity supply should also be conducted, discussed in the following sections.
Inventory analysis is about the acquisition of input and output material and energy flows (quality and quantity) of various unit blocks within the system boundary under consideration and between the various unit blocks and the environment. This is followed by assigning detailed resource and emission inventories to each flow and involves the acquisition of a fundamental inventory database for each material or energy flow from a robust inventory database provision, i.e., Ecoinvent. The Ecoinvent 3.0 life cycle inventory databases are extracted and SimaPro 9.2.0.1 is used for analysing the life cycle impacts of lithium-ion batteries. Impact assessment is about assigning and applying impact characterisation factors as applicable to each resource or emission inventory and then aggregating for total impact value in each category. Thus far, the LCA of the system may be focused on a stand-alone basis. Interpretation allows investigation of the present, attributional and consequential or change-oriented scenarios. In this study, plausible scenario bases and results are included for transparency and transferability to other studies. Only a limited number of studies exist on LCA of energy storage systems but focused on the systems only, without in-depth hotspot analysis and linking the results to all the problems that energy storage systems can tackle, leaving a gap in research that needs closing by rigorous LCA of BESS. The multi-faceted role of BESS has been identified in ancillary, transmission, distribution and customer services as shown in Figure 1. Thus, this study offers the following objectives. results are included for transparency and transferability to other studies. Only a limited number of studies exist on LCA of energy storage systems but focused on the systems only, without in-depth hotspot analysis and linking the results to all the problems that energy storage systems can tackle, leaving a gap in research that needs closing by rigorous LCA of BESS. The multi-faceted role of BESS has been identified in ancillary, transmission, distribution and customer services as shown in Figure 1. Thus, this study offers the following objectives. Estimation of life cycle GWP impact of BESS. Life cycle GWP hotspot analysis of BESS. ReCiPe, CML and ILCD impact characterisations of BESS for consistency in outcomes. Target improvement areas to lower the life cycle GWP impacts of BESS. Assigning GWP to the UK electricity mix from 2016 through to 2040. Estimation of avoided GWP by BESS including in the consequential scenario, where fossil energy systems could be eliminated from the UK electricity sector.

System Boundary and Life Cycle Inventory Analysis of BESS
Following the principles of ISO 14040-44, the LCA of BESS has been conducted as follows. The system boundary included for BESS and fossil and renewable energy resource options are cradle-to-cradle, from raw material acquisition through manufacturing, logistics and use to reuse and recycle.
A Li-ion battery is chosen to represent BESS to target life cycle GWP impact reductions. This is because Li-ion batteries have the lowest GWP amongst BESS [7]. They have a major share amongst the battery technologies and are suitable for storing large scale renewable electricity makes them appropriate for the UK renewable energy systems. The

Energy resource
Stops or reduces resources from peaking Arbitrage: differential between selling during peak periods and buying during off-peak periods  Assigning GWP to the UK electricity mix from 2016 through to 2040. Estimation of avoided GWP by BESS including in the consequential scenario, where fossil energy systems could be eliminated from the UK electricity sector.

System Boundary and Life Cycle Inventory Analysis of BESS
Following the principles of ISO 14040-44, the LCA of BESS has been conducted as follows. The system boundary included for BESS and fossil and renewable energy resource options are cradle-to-cradle, from raw material acquisition through manufacturing, logistics and use to reuse and recycle.
A Li-ion battery is chosen to represent BESS to target life cycle GWP impact reductions. This is because Li-ion batteries have the lowest GWP amongst BESS [7]. They have a major share amongst the battery technologies and are suitable for storing large scale renewable electricity makes them appropriate for the UK renewable energy systems. The life cycle of a Li-ion battery consists of the battery manufacturing, operation, reuse and waste treatment for recycling the battery constituents. In simple terms, further, the manufacturing stage that contributes to more than 45% of the total GWP (11 kg CO 2 eq per kg of battery), consists of materials, cathode/anode/parts, cell manufacturing and pack manufacturing. BESS have thus other components, such as steel, cable and printed wiring board. For the construction phase of BESS, metal working factories also need to be considered. Within a cell, the major components are cathode, anode and electrolytes. Also, the cell contains aluminium and polymers as other constituents. The manufacturing and operation phases of the cell consume heat and electricity. Furthermore, separation and reuse of used batteries should be considered in a new battery for recyclability and sustainability. Now that more sophisticated techniques for recycling Li-ion batteries exist, the disposal option must be omitted. Two main Li-ion battery treatment technologies exist for the parts not being reused, hydrometallurgy and pyrometallurgy. In system boundary terms for LCA, these activities described could be represented by a block flow diagram, as shown in Figure 2. Table 1 shows their in-depth inventory flows making up the Li-ion battery (Ecoinvent 3.0: Battery, Li-ion, rechargeable, prismatic {GLO} production). life cycle of a Li-ion battery consists of the battery manufacturing, operation, reuse and waste treatment for recycling the battery constituents. In simple terms, further, the manufacturing stage that contributes to more than 45% of the total GWP (11 kg CO2 eq per kg of battery), consists of materials, cathode/anode/parts, cell manufacturing and pack manufacturing. BESS have thus other components, such as steel, cable and printed wiring board. For the construction phase of BESS, metal working factories also need to be considered. Within a cell, the major components are cathode, anode and electrolytes. Also, the cell contains aluminium and polymers as other constituents. The manufacturing and operation phases of the cell consume heat and electricity. Furthermore, separation and reuse of used batteries should be considered in a new battery for recyclability and sustainability. Now that more sophisticated techniques for recycling Li-ion batteries exist, the disposal option must be omitted. Two main Li-ion battery treatment technologies exist for the parts not being reused, hydrometallurgy and pyrometallurgy. In system boundary terms for LCA, these activities described could be represented by a block flow diagram, as shown in Figure 2. Table 1 shows their in-depth inventory flows making up the Li-ion battery (Ecoinvent 3.0: Battery, Li-ion, rechargeable, prismatic {GLO}| production).     Each system could be further scrutinised for hotspot analysis for the chosen impact categories, in this case primarily, GWP 100 years in the quantity of carbon dioxide equivalent (CO 2 eq). For life cycle inventory analysis, Ecoinvent 3.0 databases relevant to the UK electricity system have been assimilated. The databases exist in the form of activities or services, i.e., materials and energy. Relevant ones are plugged in to construct a system. As discussed, each hotspot activity is expanded for assimilation of life cycle inventory databases from Ecoinvent 3.0 specific to the activity. This way, a top-down approach is followed to conduct the LCA of BESS.

Results of LCA of BESS and BESS-Connected Renewable Energy Systems
This section first discusses the overall GWP analysis results of BESS (benchmarking exercise), then the hotspot or contribution analysis of activities making up the BESS (benchmarking exercise), and finally, climate impact mitigation analysis of BESS-connected renewable energy systems (consequential analysis).

Overall GWP Analysis of BESS
An overall BESS GWP analysis (IPCC 100 years) is conducted using the Ecoinvent 3.0 database (Table 1) and the LCA software SimaPro 9.2.0.1. The results in the three conditions of Ecoinvent 3.0 are as follows.

1.
Allocation at the point of substitution: 6.7 kg CO 2 eq per kg of lithium-ion battery 2.
Cut-off: 8.1 kg CO 2 eq per kg of lithium-ion battery 3.
Consequential: 1.7 kg CO 2 eq per kg of lithium-ion battery The 'allocation at the point of substitution' method of Ecoinvent 3.0 considers burdens or credits being carried through recycled materials across the supply chains. The 'cut-off' method of Ecoinvent 3.0 takes burden or credit free recycled materials across the supply chains. The 'consequential' method of Ecoinvent 3.0 considers the consequences of a change in supply chains connected or not connected by mass or energy flows considering rebound effects.
The provision of service from all the systems under consideration, BESS and fossil and renewable energy resources, is electricity. Thus, the functional unit should be 1 kWh energy storage by the battery. However, for the battery systems, Ecoinvent 3.0 inventory databases are available for 1 kg of the battery system. A conversion factor in kWh kg −1 is needed for presenting the inventory values based on per kWh electricity storage. This value is 11.6 kWh per kg Li (wiki: lithium-ion battery). Cathode only constitutes 17.5% by mass of a battery pack according to the database source in Ecoinvent 3.0. Thus, when other components would be added to construct a whole battery system, energy density (kWh kg −1 ) would be lower,~0.26 kWh kg −1 reported widely. The other kWh kg −1 value for BESS reported in Ecoinvent 3 is 2.1 kWh kg −1 (Ecoinvent 3.0 database name: Battery, Li-ion, rechargeable, prismatic {GLO}| production). The battery pack consists of 14 single cells providing 2.1 kWh kg −1 energy density and a voltage of 48 V.
By dividing the total GWP impact by the energy density range (0.26 kWh kg −1 ) discussed earlier, a GWP impact factor of 6.5, 25.8 and 31 kg CO 2 eq per kWh electricity provision of BESS is obtained for the three conditions, consequential, allocation at the point of substitution and cut-off, respectively. Further improvement in the GWP impact factor is essential. For example, increasing the life of the battery from 8 years to 20 years would lower the GWP to 2.6 kg CO 2 eq per kWh in the change-oriented scenario. Another demonstratable strategy to lower the GWP from life cycle energy storage of BESS is to acquire organic material deploying green chemistry from the family of oxocarbons or carboxylates, alongside lowering of Li-ion in electrodes [9].
Given intermittent supplies of renewable systems, BESS will be essential to store electricity or charge during the time of renewable generations or resource availability and supply electricity or discharge during the time of high electricity demand. If the BESS integration is explored in the wider context of the whole energy service system as shown in Figure 1, its GWP impact factor can be shared across the whole system lowering this factor further. For example, by allocating the total GWP impact of BESS to their five different services, the GWP impact of BESS for the renewable electricity provision would be 0.5 kg CO 2 eq per kWh, comparable to the GWP of gas [28]. Based on the literature survey [6], percentage contributions of BESS in life cycle energy storage and saving in various services, energy resources, transmission, distribution, customer and ancillary, are shown in Figure 3. The data analyses are split based on mean, maximum and 25th and 75th percentile values of life cycle energy capacities and saving by BESS. The total GWP impact of BESS can be distributed to their various service offerings in the decreasing order, customer (19-34%) > ancillary (24-29%) > energy resources (14-26%) > transmission (14-25%) > distribution. This approach would allocate a certain fraction of the total GWP impact of BESS for the service under consideration. kg −1 ) would be lower, ~0.26 kWh kg −1 reported widely. The other kWh kg −1 value for BESS reported in Ecoinvent 3 is 2.1 kWh kg −1 (Ecoinvent 3.0 database name: Battery, Li-ion, rechargeable, prismatic {GLO}| production). The battery pack consists of 14 single cells providing 2.1 kWh kg −1 energy density and a voltage of 48 V.
By dividing the total GWP impact by the energy density range (0.26 kWh kg −1 ) discussed earlier, a GWP impact factor of 6.5, 25.8 and 31 kg CO2 eq per kWh electricity provision of BESS is obtained for the three conditions, consequential, allocation at the point of substitution and cut-off, respectively. Further improvement in the GWP impact factor is essential. For example, increasing the life of the battery from 8 years to 20 years would lower the GWP to 2.6 kg CO2 eq per kWh in the change-oriented scenario. Another demonstratable strategy to lower the GWP from life cycle energy storage of BESS is to acquire organic material deploying green chemistry from the family of oxocarbons or carboxylates, alongside lowering of Li-ion in electrodes [9].
Given intermittent supplies of renewable systems, BESS will be essential to store electricity or charge during the time of renewable generations or resource availability and supply electricity or discharge during the time of high electricity demand. If the BESS integration is explored in the wider context of the whole energy service system as shown in Figure 1, its GWP impact factor can be shared across the whole system lowering this factor further. For example, by allocating the total GWP impact of BESS to their five different services, the GWP impact of BESS for the renewable electricity provision would be 0.5 kg CO2 eq per kWh, comparable to the GWP of gas [28]. Based on the literature survey [6], percentage contributions of BESS in life cycle energy storage and saving in various services, energy resources, transmission, distribution, customer and ancillary, are shown in Figure 3. The data analyses are split based on mean, maximum and 25th and 75 th percentile values of life cycle energy capacities and saving by BESS. The total GWP impact of BESS can be distributed to their various service offerings in the decreasing order, customer (19-34%) > ancillary (24-29%) > energy resources (14-26%) > transmission (14-25%) > distribution. This approach would allocate a certain fraction of the total GWP impact of BESS for the service under consideration.

Hotspot Analysis of BESS Components
An overall BESS hotspot analysis of GWP shows cathode (LiMn 2 O 4 ) and anode (graphite) carry the major impacts, half the total GWP impact of BESS that is resulted from the LCA conducted using Ecoinvent 3.0 database and the LCA software SimaPro 9.2.0.1. Figure 4 shows the contribution analysis of the various activities illustrated in Figure 2 constitutes the life cycle of a Li-ion battery system. In terms of hotspot analysis, the contributions by the various activities shown in Figure 4 does not change between the three methods or conditions applied in Ecoinvent 3.0, allocation at the point of substitution, cut-off and consequential. Furthermore, following the life cycle inventory analysis of BESS in Table 1, the hotspots deep-down at the fundamental resource level are analysed. The results surprisingly show that the apparent high impact is actually due to the phosphorous white liquid production and is not due to the sourcing of lithium (lithium brine, 6.7% Li). The production of phosphorous white liquid is resource-intensive causing 13 kWh kg −1 electricity consumption and 1.25 kg kg −1 hard coal consumption (Wöhler process). The latter consumption also raises the question of sustainability given the dwindling supply of coal, increasing concerns over climate emergency due to fossil consumption and rising demand for lithium-ion batteries. This stresses the importance of nutrient circulation for a sustainable earth system for mankind-this not only supports the food system, influences biodiversity but also the sustainability of renewable electricity infrastructure, a key determinant to the 1.5 • C future.

Hotspot Analysis of BESS Components
An overall BESS hotspot analysis of GWP shows cathode (LiMn2O4) and anode (graphite) carry the major impacts, half the total GWP impact of BESS that is resulted from the LCA conducted using Ecoinvent 3.0 database and the LCA software SimaPro 9.2.0.1. Figure 4 shows the contribution analysis of the various activities illustrated in Figure 2 constitutes the life cycle of a Li-ion battery system. In terms of hotspot analysis, the contributions by the various activities shown in Figure 4 does not change between the three methods or conditions applied in Ecoinvent 3.0, allocation at the point of substitution, cutoff and consequential. Furthermore, following the life cycle inventory analysis of BESS in Table 1, the hotspots deep-down at the fundamental resource level are analysed. The results surprisingly show that the apparent high impact is actually due to the phosphorous white liquid production and is not due to the sourcing of lithium (lithium brine, 6.7% Li). The production of phosphorous white liquid is resource-intensive causing 13 kWh kg −1 electricity consumption and 1.25 kg kg −1 hard coal consumption (Wöhler process). The latter consumption also raises the question of sustainability given the dwindling supply of coal, increasing concerns over climate emergency due to fossil consumption and rising demand for lithium-ion batteries. This stresses the importance of nutrient circulation for a sustainable earth system for mankind-this not only supports the food system, influences biodiversity but also the sustainability of renewable electricity infrastructure, a key determinant to the 1.5 °C future.         Furthermore, the GWP (w/w) over 100 years following the IPCC characterisation method is shown in Figure 8 for the key material productions in Table 1 to identify the hotspots in the entire system. Within the Li-ion battery, the battery cell, Li-ion carries most of the GWP burdens. Lithium hexafluorophosphate rather than lithium-ion cathode is the GWP hotspot. The GWP impacts of lithium hexafluorophosphate are primarily due to the impacts of phosphorus, white, liquid via phosphorous chloride. The next level of GWP impacts is due to the lithium-ion cathode, which is due to lithium manganese oxide, which is further due to lithium carbonate and manganese (III) oxide. Lithium carbonate's GWP is due to lithium brine, 6.7% Li. The anode, graphite has then the next level of GWP, which is due to the copper cathode and graphite anode, respectively, to make the anode, graphite product.    Table 1.
The ReCiPe (M) (H) life cycle impact assessment method gives eighteen mid-point characterisations. The negative impacts imply environmental credits due to recycling and displacement of fossil resources where applicable. Thus, there are savings in fossil, mineral and water resources. The GWP impact is high due to phosphorous, white, liquid production.
There are eleven life cycle impact categories assessed in the CML method. Credits in fossil resources and toxicity impacts can be observed from the CML-based life cycle impact characterisations of the system. The climate impact hotspots are phosphorous white liquid > copper cathode > anode graphite. Amongst the various materials making up the cathode LiMn 2 O 4 , carbon black > manganese (III) oxide > lithium brine, 6.7%, lithium, incur GWP in decreasing order, respectively. Fossil resource saving by the battery is due to the recycling of the battery. To mitigate the climate impact potential of the battery, phosphorous recycling is needed. Microbial electrosynthesis [29][30][31] is a potential process for the recovery of phosphorous from wastewater sludge. Alternative organic solvents can be investigated that can be sourced from waste resources applying the circular economy principle [32,33].
There are sixteen impact categories analysed in the ILCD method. Similar to the ReCiPe (M) (H) method, the credit-bearing impact characterisations are related to fossil and water resource use. Consistent with the other two impact characterisation methods, the impact hotspots in the whole system are due to the productions of phosphorous, white, liquid > copper cathode > anode graphite. Carbon black and manganese (III) oxide productions are the next levels of GWP impact bearing processes. The in-depth life cycle hotspot analysis from life cycle inventory data collection (Table 1)  Furthermore, the GWP (w/w) over 100 years following the IPCC characterisation method is shown in Figure 8 for the key material productions in Table 1 to identify the hotspots in the entire system. Within the Li-ion battery, the battery cell, Li-ion carries most of the GWP burdens. Lithium hexafluorophosphate rather than lithium-ion cathode is the GWP hotspot. The     The ReCiPe (M) (H) life cycle impact assessment method gives eighteen mid-point characterisations. The negative impacts imply environmental credits due to recycling and displacement of fossil resources where applicable. Thus, there are savings in fossil, mineral and water resources. The GWP impact is high due to phosphorous, white, liquid production.
There are eleven life cycle impact categories assessed in the CML method. Credits in fossil resources and toxicity impacts can be observed from the CML-based life cycle impact characterisations of the system. The climate impact hotspots are phosphorous white liquid > copper cathode > anode graphite. Amongst the various materials making up the cathode LiMn2O4, carbon black > manganese (III) oxide > lithium brine, 6.7%, lithium, incur GWP in decreasing order, respectively. Fossil resource saving by the battery is due to the recycling of the battery. To mitigate the climate impact potential of the battery, phosphorous recycling is needed. Microbial electrosynthesis [29][30][31] is a potential process for the recovery of phosphorous from wastewater sludge. Alternative organic solvents can be investigated that can be sourced from waste resources applying the circular economy principle [32,33].
There are sixteen impact categories analysed in the ILCD method. Similar to the ReC-iPe (M) (H) method, the credit-bearing impact characterisations are related to fossil and water resource use. Consistent with the other two impact characterisation methods, the impact hotspots in the whole system are due to the productions of phosphorous, white, liquid > copper cathode > anode graphite. Carbon black and manganese (III) oxide productions are the next levels of GWP impact bearing processes. The in-depth life cycle hotspot analysis from life cycle inventory data collection (Table 1) through to life cycle impact assessment (Figures 5-7) stresses the importance of consideration of life cycle stages, i.e., fundamental resource acquisition, beyond the manufacturing, use and recycling stages of LCA.

GWP Analysis of BESS-Connected Renewable Energy Systems
LCA of the UK renewable electricity system before and after BESS integration must be conducted to comprehend the role of BESS. BESS allow more than 20% (by energy) Figure 8. GWP of material productions in the entire system to show the contributing materials.

GWP Analysis of BESS-Connected Renewable Energy Systems
LCA of the UK renewable electricity system before and after BESS integration must be conducted to comprehend the role of BESS. BESS allow more than 20% (by energy) renewable electricity mix in a grid mix [3]. Up until 2020, energy storage has been driven by pumped storage in the UK. However, with an increasing proportion of renewable energies in the UK electricity sector, integration of BESS is imperative. Wind, solar and hydro electricity is expected to play a key role, eventually taking over from gas in the UK electricity sector. To calculate the avoided GWP by BESS integration into the UK renewable electricity system, the following data are presented and analysed.
(1) The UK electricity generation by alternative resource (both TWh and percentage per annum) from 2016 through to 2020 ( Figure 9) [2]. (2) The proportion of the UK electricity generation, present and forecasted, by resource (Table 2). In this case, the proportion of renewables (wind, solar and hydro) would increase to 56% and the proportion of gas would decrease to 18% by 2040 [34]. The contributions shown in Figure 9, are the actual values of the main resources. Thus, the total annual electricity generation in the UK can be obtained from the ratio between TWh and fractional contribution from a resource. Oil, other fossil resources and pumped storage with their aggregated contributions of less than 3% are not presented. The totals in Table 2 do not include their contributions. (3) The proportion of gas by the energy of the UK electricity generation is forecasted for the years 2025, 2030, 2035 and 2040 for a non-fossil electricity generation scenario by 2040 (Table 3). In this case, all other resource energy contributions are kept the same [34] thus reducing the totals to as shown in Table 3. The demand reduction is necessary in this case. (4) The GWP using the IPCC characterisation factors of coal, gas, solar, bioenergy, wind, nuclear and hydro electricity in the UK (Table 4) [28]. (POCP) using the ILCD characterisation factors of the above technologies in the UK (Table 4) [28]. Table 3). In this case, all other resource energy contributions are kept the s [34] thus reducing the totals to as shown in Table 3. The demand reduction is ne sary in this case. (4) The GWP using the IPCC characterisation factors of coal, gas, solar, bioenergy, w nuclear and hydro electricity in the UK (Table 4) [28]. (5) The other life cycle environmental impact potentials, acidification potential (AP), trophication potential (EP) and fossil depletion potential (FDP) using the CML c acterisation factors and photochemical oxidant creation potential or urban sm (POCP) using the ILCD characterisation factors of the above technologies in the (Table 4) [28].   Coal  31  23  17  7  6  0  0  0  0  Gas  143  137  131  132  111  80  73  68  6  Nuclear  72  70  65  56  50  56  65  70  8  Hydro  5  6  5  6  7  7  7  7  7  Wind  37  50  57  64  75  116  156  175  20  Solar  10  11  13  13  13  16  20  23  2  Bioenergy  30  32  35  37  39  39  39  39  3  Total  329  328  323  315  301  315  360  382  41   Table 3. The proportion of gas by the energy of the UK electricity generation forecasted for the y 2025, 2030, 2035 and 2040 for defossilised electricity by 2040.  Table 4. The GWP (IPCC characterisation factors), acidification potential (AP), eutrophication potential (EP) and fossil depletion potential (FDP) (CML characterisation factors) and photochemical oxidant creation potential or urban smog (POCP) (ILCD characterisation factors) of coal, gas, solar, bioenergy, wind, nuclear and hydro electricity in the UK extracted from [28].  Table 5 shows the overall avoided GWP by year compared to the year 2000. The GWP is calculated for the various resource energy contributions from the year 2016 through to the year 2020 and for the forecasted years, 2025, 2030, 2035 and 2040. The calculations apply the GWP factors of the various electricity generation systems in Table 4. These GWP factors are multiplied with the proportion of the UK electricity generation, present and forecasted, by resource (Table 2) for their resulting GWP as shown in Table 5. The GWP intensity of the UK electricity system decreases from 336 kt CO 2 eq TWh −1 in 2016 to 110 kt CO 2 eq TWh −1 in 2040. The percentage of GWP reduction compared to the year 2000 (204,228 kt CO 2 eq) varies 46-78% between the years 2016 and 2040. Compared to the GWP in the year 2020, the percentage GWP reduction is 29-34% through to the year 2040. The percentage GWP reduction in the final two rows in Table 5 is calculated for the zero-fossil resource electricity generation scenario in Table 3. The percentage GWP reduction in this scenario (Table 3) is 76-94% and 29-82% compared to the years 2000 and 2020.

(
The total GWP for the years 2025, 2030, 2035 and 2040 in Table 5 account for a GWP of 20 kt CO 2 eq TWh −1 from BESS in addition to the GWP from the electricity generation systems. From Table 4, the GWP of BESS must be less than 0.5 kg CO 2 eq kWh −1 (for gas) to achieve an acceptable avoided GWP from defossilization. Also, in the analysis, it must be noted that in zero or non-fossil or defossilization scenarios, only the scope 1 emission from direct fossil burning to generate electricity in the fossil power plant is avoided. The remaining GWP results from other indirect emissions across the systems' life cycle supply chains (scopes 2-3), which can be from fossil resources. These must be eliminated to hit the net zero target. For example, phosphorous, white, liquid carries the main GWP burden, which if eliminated by recycling phosphorous, can result in an acceptable GWP (4-76 g CO 2 eq kWh −1 for renewable energy generation systems) applied in the analysis shown in Table 5.

Discussion
This research conducts a rigorous comprehensive life cycle assessment (LCA) of BESS following the ISO14040-44 by taking lithium-ion batteries as an example. The study is to benchmark the global warming potential (GWP) of BESS using a globally standardised life cycle inventory database for lithium-ion batteries using lithium manganese oxide cathode. A literature review of GWP of BESS identifies a lack of consensus approach and standard GWP to target. The literature shows widely varying GWP per kg or kWh energy storage of BESS, by several hundred times. There are some breakthrough results obtained from this benchmarking study. An overall BESS GWP analysis (IPCC 100 years) using the Ecoinvent 3.0 life cycle inventory database and the LCA software SimaPro 9.2.0.1 shows the following transferable results.