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Article

Comprehensive Aging Analysis of Volumetric Constrained Lithium-Ion Pouch Cells with High Concentration Silicon-Alloy Anodes

1
ETEC Department & MOBI Research Group, Vrije Universiteit Brussel (VUB), Pleinlaan 2, 1050 Brussel, Belgium—VUB-MOBI is a Core Lab Member of Flanders Make
2
ZSW, Zentrum für Sonnenenergie- und Wasserstoff-Forschung BW, Helmholtzstraße 8, 89081 Ulm, Germany
*
Author to whom correspondence should be addressed.
Submission received: 28 September 2018 / Revised: 24 October 2018 / Accepted: 25 October 2018 / Published: 29 October 2018
(This article belongs to the Section D: Energy Storage and Application)

Abstract

:
In this research, twenty-four high capacity (1360 mAh) NMC622/Si-alloy Li-ion full pouch cells with high silicon-alloy content (55%) are cycle aged under seven different cycling conditions to study the effect of different stressors on the cycle life of Si-anode full cells, among which are the effect of ambient temperature, Depth of Discharge (DoD) and the discharge current. The cells are volumetrically constrained at an optimal initial pressure to improve their cycle life, energy and power capabilities. Furthermore, the innovative test setup allows measuring the developed pressure as a result of repeated (de-)lithiation during battery cycling. This uniquely vast testing campaign on Si-anode full cells allows us to study and quantify independently the influence of different stress factors on their cycle life for the first time, as well as to develop a new capacity fade model based on an observed linear relationship between capacity retention and total discharge capacity throughput.

1. Introduction

The continuous rise of long-lived greenhouse gases in our Earth’s atmosphere, among which are CO2, CH4 and N2O, presents the largest driving force behind climate change and has driven humankind to explore new technologies. Naturally, decarbonization of transportation has become a huge element of these new technologies due to the overwhelming contribution that combustion of fossil fuels presents to these harmful gases [1]. Electric Vehicles (EV), powered by rechargeable batteries rather than traditional combustion engines, show great potential in advancing this decarbonization. However, the commercial Li-ion batteries currently powering EV’s are reaching their theoretical capacity limits, leaving limited opportunity to increase energy density using traditional materials [2]. Silicon (Si) presents an attractive alternative to the graphite anode material currently used in conventional Li-ion batteries owing to its natural abundance, significantly higher volumetric capacity and specific capacity (2194 Ah/l vs. 719 Ah/l for L i 15 S i 4 and L i C 6 ; 3579 mAh/g vs. 372 mAh/g for Si and graphite) [3,4]. However, Si anodes have shown poor cyclability as a result of substantial volumetric expansion/contraction (280–400%) [3,5,6,7,8,9,10,11,12,13,14] due to repeated (de-)lithiation, giving rise to high internal stresses within the anode. Plenty of research [5,6,7,8,9,10,11,12,13,15,16,17] is available in the literature, identifying the aging mechanisms induced by electrochemical cycling of Si anode half-cells as: (1) deterioration of the electrode’s structural integrity due to pulverization; (2) disconnection between the current collector and electrode due to (de-)lithiation-induced stress; (3) consumption of cyclable lithium in the reformation process of the damaged Solid Electrolyte Interface (SEI). However, as Dupré et al. [18] and Delpuech et al. [19] recently indicated, the aging mechanisms for full Li-ion cells with Si anodes appears to be different from those known for half-cells. Both research works conclude that the main aging mechanism in Si anode full cells is due to the consumption of limited available cyclable lithium by parasitic, electrolyte-additive-consuming reactions occurring well before the deterioration of electrode integrity or disconnection between active materials, as is the case for half cells. This makes a strong case for additional research focused on the aging of full Li-ion cells with Si anodes. Nevertheless, very few research works have been reported in the literature handling full Li-ion cells with Si anodes, of which an overview is presented in Table 1. Clearly, the most studied cell types are low capacity coin cells with NMC532 cathodes and anodes with low Si content (<30%). While only Louli et al. [3] reported a study on low capacity (<260 mAh) Si-anode pouch cells, only Chevrier et al. [20] reported on a high capacity (2 Ah) cylindrical cell with an excellent cycle life (80% capacity retention at 500 cycles) thanks to prelithiation. Furthermore, they stand alone in employing NMC622 as the cathode material in high capacity (2 Ah) coin/cylindrical cells.
In this research, twenty-four high capacity (1360 mAh) NMC622/Si-alloy Li-ion full pouch cells with high silicon-alloy content (55%) are cycle aged under seven different cycling conditions, including the Worldwide harmonized Light Vehicles Test Procedure (WLTP) driving cycle, to study the effect of different stressors on the cycle life of Si-anode full cells, among which are the effect of ambient temperature, Depth of Discharge (DoD) and the discharge current. Furthermore, the cells are volumetrically constrained at an optimal initial pressure to improve their energy and power capabilities, as reported in our previous work [21]. This uniquely vast testing campaign on Si-anode full cells allows for the first time to study and quantify independently the influence of different stress factors on their cycle life, as well as to develop a new capacity fade model based on an observed linear relationship between capacity retention and total discharge capacity throughput.
The paper is structured as follows: Section 2 presents the characteristics of the investigated Si-alloy cells and their imposed volumetric constraints. Section 3 presents the lifetime testing methodology followed throughout this research, including testing procedures and the selection of cycling conditions. Section 4 introduces the results of the lifetime study and discusses them in depth. Section 5 presents the observed relationship between capacity retention and total capacity throughput, followed by a methodology to implement the relation for capacity fade modeling. Finally, Section 6 presents the conclusions and future work.

2. Silicon Li-Ion Batteries

2.1. Investigated Cells

The investigated next-generation cells in this research are full pouch cells built from prototype materials, assembled by the Zentrum für Sonnenenergie und Wasserstoff-Forschung (ZSW) with an NMC622 cathode developed by Umicore and adjusted binders developed by Arkema. The anode consists of 55% Si-alloy, developed by 3M, combined with graphite. The electrolyte is composed of 1 M LiPF6 and 0.1 M Lifetime Electrolyte Arkema (LEA) in EC:EMC3:7 (V/V) combined with 10% Fluoroethylene Carbonate (FEC). This cell is the third generation of cells developed during the European FiveVB project (www.fivevb.eu), funded by the Horizon 2020 research and innovation program of the European Commission. These next generation electrode materials result in a voltage window of 2.7 V–4.4 V, a nominal capacity of 1360 mAh (average measurement during first C/25 discharge for 33 tested cells) and a specific energy of 205 Wh/kg. A summary of the tested Si-alloy cell specifications is presented in Table 2.

2.2. Electrical Characterization

To establish the baseline electrical performance of the Si-alloy cells, as well as to evaluate their electrical performance over their lifetime, three well-defined characterization tests are performed: a capacity test, a Quasi-Open Circuit Voltage test (QOCV) and a Hybrid Pulse Power Characterization test (HPPC). The standardized capacity test [28,29,30,31] is utilized to evaluate the cell’s discharge capacity at various c-rates by using constant current constant voltage charging cycles followed by a constant current discharge at 0.1C, 0.2C, 0.33C, 1C and 1.5C. The Beginning of Life (BoL) capacity test results for all tested cells in this research are summarized in Figure 1a. The median capacity values are 1347.7 mAh, 1329.5 mAh, 1310.6 mAh, 1255.9 mAh and 1215.6 mAh for 0.1C, 0.2C, 0.33C, 1C and 1.5C, respectively. Furthermore, the maximum deviation from the median capacity never exceeds 2.5% over all c-rates, which testifies to a high quality manufacturing process performed by ZSW.
The QOCV test is used as a time efficient non-standardized test to approximate the open circuit voltage of a cell over the State of Charge (SoC), by charging and discharging the cell at a very low constant current of C/25, as can be seen in Figure 1b. Furthermore, this test is utilized as a check-up test to assess capacity degradation during cycle aging, which is further explained in Section 3.2.
Finally, the HPPC test is employed to evaluate the electrical and dynamic behavior of the cell over the entire SoC window. This is achieved by imposing a train of alternating charge and discharge current pulses at 0.2C, 0.33C, 1C, 1.5C and 2C at every 5% SoC interval. Analyzing the measured voltage response from this test offers a range of possibilities to evaluate the cell’s behavior, e.g., electrical modeling, assessing battery internal resistance and assessing power capabilities.

2.3. The Influence of Pressure

It is widely reported in the literature that silicon anodes endure substantial volumetric expansion/contraction (280–400%) due to repeated (de-)lithiation, giving rise to high internal stresses within the anode, which lead to continuous repair of the damaged SEI and ultimately result in the consumption of cyclable lithium and capacity fade [3,5,6,7,8,9,10,11,12,13,14]. In an initial effort to monitor this characteristic behavior, it was observed that applying external pressure perpendicular to the cell’s electrodes by constraining it volumetrically improved both its energy and power capabilities, as reported in our previous work [21]. In order to study the influence of the applied external pressure on the Si-alloy pouch cell’s cycle life and identify the optimal initial pressure, a dedicated setup was developed as shown in Figure 2. The Si-alloy cells are volumetrically constrained on a 3D-printed battery holder, with built-in electrical connectors, by an aluminum pressure plate. A Tekscan™Flexiforce resistive pressure sensor is mounted between the lower pressure plate and a second, upper pressure plate. Thanks to this innovative setup, tightening of four screws allows to regulate the applied initial pressure on the Si-alloy cell during the calibration procedure, while the pressure sensor allows measuring the perpendicular counterforce as a result of repeated (de-)lithiation during battery cycling. In the performed pressure study, four Si-alloy cells were cycle aged with different starting pressures to study the effect on their respective capacity retention and identify the optimal initial pressure for maximal cycle life. The pressure study results are presented in Section 4.1.

3. Lifetime Testing Methodology

3.1. Capacity Fade Model Concept

The aging of Li-ion batteries can be divided into two separate mechanisms: cycle aging and calendar aging, where cycle aging is the degradation that occurs due to repeated (dis-)charging of the cell and calendar aging is the degradation attributed to storing the cell at curtain storage conditions. Due to limited cell availability, it was preferred to consider the effects of cycle aging exclusively for the capacity fade model. Nevertheless, calendar aging was also performed on a small amount of cells. To develop a comprehensive understanding of the Si-alloy full cell’s cycle aging and degradation mechanisms under different operational conditions, the essential stress factors, which greatly influence the cycle aging, are identified to be: current rate, temperature and DoD [32,33,34,35,36]. Figure 3 presents a flowchart overview of the methodology followed during this research. After the identification of the optimal initial pressure during the pressure study (Section 2.3), the influence of current rate, depth of discharge and ambient temperature on the cycle life of the Si-alloy cells is studied independently (Section 3.2). This allows creating a semi-empirical capacity fade model and reveals the influence that the identified stress factors have on the aging mechanisms of the full cell Li-ion batteries with Si-alloy anodes for the first time.

3.2. Testing Procedure

In order to obtain the necessary empirical data to study the aging phenomena of the Si-alloy full cells under various conditions and create the capacity fade model, a meticulous testing procedure was conceived of and strictly followed throughout every cycling condition, which is shown in Figure 4. A fresh cell first undergoes BoL characterization, which consists of three conventional electrical characterization tests for Li-ion batteries: a capacity test, a QOCV test and an HPPC test (Section 2.2). After the BoL characterization is completed, 50 cycles are performed at the given cycling condition. Hereafter, a short check-up is performed, which consists solely of a QOCV test to minimize additional aging due to characterization tests. After 50 more cycles at the given cycling condition, a detailed check-up is performed, which consists of the same electrical characterization tests as the BoL characterization. This procedure is repeated until the cell reaches End of Life (EoL), which is defined in this research as 80% capacity retention.

3.3. Cycle Aging Test Campaign

To investigate the influence of the identified stress factors on battery lifetime independently, the test campaign shown in Table 3 was developed. Eighteen prototype, next generation, NMC622/Si-alloy cells are cycled under seven different cycling conditions. To demonstrate the repeatability of the results, every cycling condition is tested twice. All cells are cycled at the identified optimal initial pressure of 7.5 kg (Section 2.3 and Section 4.1). To the author’s best knowledge, no previous research exists that investigates the cycle aging of such a vast amount of Si-alloy anode full cells under different cycling conditions, nor volumetrically constraining the cell during cycling.
The cycling conditions shown in Table 3 are considered to be constant current cycles. All these tests share the same foundation as they commence with a constant current charge at C/3 followed by a constant voltage charge at 4.4 V to ensure the cell is fully charged before cycling. Hereafter, 50 full charge and discharge cycles are performed, after which the cell is charged back to 3.7 V for safe storage. The specificity of each cycling condition lies with the current rate at which the charge and discharge cycles are performed, how deep the cell is discharged and the ambient temperature of the climate chamber. The current rate was varied between C/3 and 1C; the temperature was varied between 10 °C, 25 °C and 45 °C; while the DoD was 60%, 80% or 100%. It should be noted that DoD is defined in this research with reference to 50% middle SoC, meaning that 60% DoD cycles between 80% and 20% SoC, 80% DoD cycles between 90% and 10% SoC and 100% DoD operates between 100% and 0% (4.4 V–2.7 V) SoC.
In an effort to extend the understanding of the Si-alloy battery lifetime to more practical automotive applications, a real-life driving cycle test condition was developed, based on the WLTP. The standardized speed profile was converted to a load current expressed in C-rate. Two validation cells are cycle aged at 25 °C by performing ten consecutive WLTP cycles after a constant current charge at C/3. This process is repeated fifty times before the cell’s remaining performance is evaluated during a detailed check-up. Besides offering compelling insights towards the real-life applicability of Si-alloy Li-ion cells, this test condition also serves as the dynamic validation profile for the developed capacity fade model.

4. Results and Discussion

4.1. Pressure Study

To investigate the influence of the initial applied pressure on the cycle life of Si-alloy cells, an extensive pressure study was performed prior to the actual cycle aging campaign. Eight cells were cycle aged under identical conditions (c-rate, DoD and temperature), but the initial perpendicular pressure applied on the cell’s surface was randomly varied between 3.25 kg, 7.5 kg, 11.25 kg and 15 kg. Hereafter, the cells were cycled at the benchmark cycling condition of C/3 charge and discharge current, 100% DoD and at an ambient temperature of 25 °C, according to the aforementioned testing procedure (Section 3.2). For repeatability, each initial pressure was tested on two cells. The average measured capacity retention over the battery lifetime during the QOCV check-up tests is presented for all cells in Figure 5, along with their respective error bars. From the obtained results, it was concluded that applying external pressure on the Si-alloy pouch cells significantly increased battery performance, as reported in our previous work [21]. However, no clear relation was observed between the amount of pressure and the cell’s capacity retention, as long as a curtain threshold pressure was met. Consequently, the optimal initial pressure for further cycle age testing was identified to be 7.5 kg, as it showed slightly better average capacity retention (1.9%) than the 3.5-kg case, while increasing the pressure beyond the 7.5-kg threshold to 11.25 kg and 15 kg led to a 3.3% and 1.0% decrease in capacity retention, respectively.

4.2. Capacity Degradation

4.2.1. The Influence of Current Rate

The influence of current rate on Si-alloy battery lifetime was examined by cycle aging four cells, two of which at a current rate of C/3 and two at a current rate of 1C, while the other main identified stress factors for battery degradation, DoD and temperature were kept constant at 100% and 25 °C, respectively. The State of Health (SoH) of each cell was determined based on the discharged capacity of every performed cycle relative to the discharged capacity during the second cycle, as defined by Equation (1). The discharge capacity obtained from the second cycle ( C c y c l e , 2 ) was designated as the reference capacity rather than the first cycle due to the test design. As discussed in Section 3.3, every cycling block started with a constant current charge at C/3 followed by a constant voltage charge at 4.4 V to ensure the cell was fully charged. However, during the cycling block, only constant current charging was performed, leaving out the constant voltage charge, which naturally resulted in a lower discharged capacity for the consecutive cycles. Correspondingly, using the discharged capacity from the first cycle would result in an unrealistic drop of the SoH of up to 4.7% after the first cycle. It should be mentioned that the observed peaks in SoH every fifty cycles were also attributed to the CCCV charge of every new cycling block.
S o H = C c y c l e , k C c y c l e , 2 · 100 %
From the presented results in Figure 6, it is clear that an increased current rate has an adverse effect on battery lifetime. The average cycles to end of life diminished from 160 to 143 for a current rate of C/3 and 1C, respectively, which corresponds to a significant decrease in battery lifetime of 10.6%. Furthermore, the obtained results show excellent repeatability under both cycling conditions. The cells cycled at the higher c-rate of 1C showed a dissimilarity in the number of cycles to EoL of only one (144 cycles and 142 cycles), while both cells cycled at the lower c-rate of C/3 reached EoL after 159 and 160 cycles, respectively. The number of cycles reached to end of life for each cell at every cycling condition during this research is summarized in Table 4.

4.2.2. The Influence of Depth of Discharge

The influence of the depth of discharge on Si-alloy battery lifetime was evaluated by cycle aging six cells, of which two cells at respectively 100%, 80% and 60% DoD, while the other main identified stress factors for battery degradation, current rate and temperature were kept constant at C/3 and 25 °C. Figure 7 shows the SoH over battery lifetime, calculated from the obtained discharge capacity during a QOCV check-up test, which was performed every fifty cycles. For the clarity of the presented results, only one cell at each DoD cycling condition is shown. However, the mean difference on the measured SoH was only 0.4% for all six cells with a maximum deviation of 0.6%, which demonstrates the repeatability of the obtained results. Furthermore, it should be noted that cycle life is presented using full equivalent cycles, where one full equivalent cycle is defined as consuming 100% of the nominal battery capacity followed by recharging 100% of the nominal capacity, in order to allow one on one comparison between the different cycling conditions’ lifetime. The results reveal a drastic improvement in cycle life for the Si-alloy cells with reduced DoD cycling conditions of up to 100 full equivalent cycles.
A reasonable explanation for this phenomenon is the continuous growth of the SEI layer on the silicon-alloy anode, owing to the induced stress of repeated (de-)lithiation of silicon particles during which gradual consumption of cyclable lithium occurs and the electrolyte additive FEC is depleted by parasitic reactions on the anode [8,18,19,37]. While volumetric expansion perpendicular to the electrode’s surface is inhibited by the external pressure applied on the cells through the test setup, lateral volumetric expansion is only limited by intrinsic cell dimensions. However, it is proposed that the detrimental effect of the large pressure variations outweigh the small lateral volumetric changes and present the major driving force behind the cell’s degradation. This posit is substantiated by pressure measurements taken on the cells during the first fifty cycles, which are presented in Figure 8a. A clear relationship between pressure variation Δ P and cycling DoD can be observed where cycling conditions at 100%, 80% and 60% DoD show a pressure variation of 3.6 kg, 3.4 kg and 2.2 kg, respectively. Furthermore, Klett et al. [37] have previously reported a significant improvement (up to 10%) in capacity retention of NMC532/Si-Gr coin cells with low silicon content (15 wt% Si) after 100 cycles, when cycling at a more narrow voltage window. They postulated that by discharging to a lower cut-off voltage, the Si-Gr anode potential rises, which enhances the fracture of the Si particles caused by the deeper discharge and enhances SEI decomposition at high anode potentials. Comparing the total discharge throughput during cycling against the capacity retention allows assessing the likelihood that pressure variations induced by repeated (de-)lithiation influence the cell’s cycle life. After all, a cell with a lower total discharge throughput is expected to have an increased capacity retention caused by a smaller pressure change due to less (de-)lithiation. Indeed, Figure 8b shows that over battery lifetime (after 50, 100 and 150 cycles), cells with a lower total discharge throughput show improved capacity retention. Combined with the presented pressure measurements and improved lifetime of the 60% DoD cycling condition, this allows us to conclude that the internal pressure variations developed by volumetric constrained silicon-alloy cells had a substantial influence on their cycle life.

4.2.3. The Influence of Temperature

The influence of the ambient temperature on Si-alloy battery lifetime was evaluated by cycle aging six cells, of which two cells were at respectively 10 °C, 25 °C and 45 °C, while the other main identified stress factors for battery degradation, current rate and depth of discharge were kept constant at C/3 and 100%. From the results shown in Figure 9, a clear trend of rising aging rates was observed for both 10 °C and 45 °C cycling conditions. These findings are in agreement with the available literature on the aging of conventional Li-ion batteries [32,33,34,38,39,40], where it is shown that in low temperature cycling (T < 25 °C), lithium plating on the anode and successive reactions with the electrolyte caused a loss of lithium and resulting capacity fade; while at higher temperatures (T > 25 °C), other aging mechanisms were predominantly reported, such as degradation of the cathode and the growth of the SEI layer. However, to the author’s best knowledge, no literature of the ambient temperature’s impact on the cycle life of Si anode full cells is currently available. Even the effect of ambient temperature on Si half cells is barely reported. Haruta et al. studied the effect of different SEI-forming additives on the cycle performance of Si nanoflake powder anodes [15]. They reported an 11% decrease in capacity retention after 50 cycles between 30 °C and 60 °C when utilizing 10 wt% FEC as electrolyte additive and a substantially larger capacity loss at −5 °C. Interestingly, the half cells containing additives showed worse capacity retention at low temperatures than those that did not. In [18], the influence of an elevated temperature (55 °C) compared to room temperature (25 °C) on the calendar aging of full cell NMC111/Si coin cells was presented. It was reported that the parasitic, electrolyte-additive-consuming reactions at the anode surface occurred spontaneously and were thermally activated. To confirm this thermal activation in our Si-alloy pouch cells, as it might explain the drastic reduction in the 45 °C cycle life observed in Figure 9, two cells were calendar aged at 4.4 V (100% SoC) using the same volumetric constrained pressure setup as used for the cycle aging (Section 2.3), which exerted 7.5 kg of initial pressure on the cells. From the obtained results, shown in Figure 10, it is confirmed that the parasitic degradation of the electrolyte at the anode took place without (de-)lithiation and was significantly thermally intensified. Furthermore, the cell calendared at 45 °C showed considerable bulging after reaching EoL, which indicates the formation of gases. It has been reported [16,17,21] that the main decomposition products of fluoroethylene carbonate are CO2 and LiF, where the formation of CO2 gas explains the cell bulging and thus confirms that the electrolyte degradation was thermally enhanced. It is thus proposed that the drastically reduced cycle life of the Si-alloy cells at 45 °C was caused by an increased reaction rate of the parasitic electrolyte degradation, which resulted in CO2 gas formation, increasing the internal pressure of the cell, which damaged the SEI layer further and thus resulted in an increased consumption rate of cyclable lithium and capacity loss.

4.2.4. The Influence of Real-Life Driving

In an effort to extend the understanding of the Si-alloy battery aging to more practical automotive applications, a real-life driving cycle test condition was developed, based on the WLTP. This test condition also served as the dynamic validation profile for the developed capacity fade model presented in Section 5. As previously described in Section 3, the cells underwent ten consecutive standardized WLTP driving cycles before being recharged to 4.4 V (100% SoC). This cycling block was repeated fifty times, concurring with 500 total WLTP cycles in between cell check-ups. Since one WLTP cycle corresponds to 23.3 driven kilometers, a driving distance of 233 km was simulated between charging events, and a total driven distance of 11,650 km was simulated between every check-up. Figure 11 presents the measured capacity retention during check-ups of the WLTP cycling conditions. It is observed that the Si-alloy cells showed excellent capacity retention throughout the drive cycle aging, where Cell 1 maintained 88.5% of it’s initial capacity after 46,600 km (= 200 cycles × 10 WLTP’s/cycle × 23.3 km/WLTP). Assuming that the aging rate remains constant from the second measurement point on, linear extrapolation of the capacity retention obtained an estimate of 98 536 km to battery EoL. This assumption was justified by the observed strong linear relationship (R2 = 0.997) between the capacity retention and number of cycles when excluding the first measurement; while leaving out the first measurement point for the extrapolation was justified by the high initial irreversible capacity loss that occurred during the first few cycles in Si cells [2,41]. Either way, it was concluded that the studied Si-alloy cells showed promising prospects for automotive applications.

4.3. Pressure Evolution over Battery Lifetime

Over the past few years, only a handful of publications have dealt with the measurement and effect of stress induced by (de-)lithiation in various electrodes [3,42,43,44,45,46,47,48]. A few researchers have successfully used stress measurements on pouch cells of various conventional chemistries for SoC [46,47] and SoH [45,46,48] estimations. However, to the author’s best knowledge, only one publication briefly mentions the evolution of pressure over the lifetime of pouch cells with silicon-based anodes (SiO-graphite, Si-alloy and nano-Si:carbon) [3]. As previously mentioned, pressure measurements were performed during all tests in the presented aging campaign of this research, which offer a compelling insight towards the evolution of pressure over Si-alloy battery lifetime. Figure 12 presents the general evolution in pressure observed during all cycling conditions: as the discharge capacity decreases, an irreversible pressure increase transpires. A clear relationship can be identified between capacity retention and the pressure behavior of our Si-alloy cells, which implies a correlation between the main aging mechanism within Si-alloy cells and their irreversible pressure growth. However, the in-depth analysis of the pressure measurements will be presented extensively in our future work.

5. Capacity Fade Modeling

5.1. The State of Health-Capacity Throughput Relationship

In Section 4.2.2, we already compared the total discharged capacity throughput during cycling, for the first 150 cycles, against the capacity retention of cells cycled at different DoDs. A seemingly linear relationship could be observed in Figure 8b between the capacity retention and the total discharge capacity throughput, depending on the cycling condition. To further investigate this phenomenon, the total discharged capacity throughput during cycling was calculated for all cells under the six studied cycling conditions and plotted against the SoH in Figure 13. All SoH measurements are based on the discharged capacity obtained during the QOCV check-ups at C/25 (Section 3.2), except for the 45 °C cycling condition. Since the aging rate at this high temperature is so severe, cells reached EoL before the first check-up test. Hence, the discharged capacity for the calculation of the SoH for this condition was taken from the cycling test (Table 3) every 10 cycles.
From the results in Figure 13, a linear relationship between the cell’s total discharge capacity throughput and its capacity retention was observed, where the slope of degradation depends on the cycling condition. To quantify this behavior, linear curve fitting was performed for every cycling condition, which relates the SoH to the capacity throughput ( C t h r o u g h ) by S o H = p 1 × C t h r o u g h + p 2 . The value of coefficient p 2 (intercept) was fixed to 100 for curve fitting, as it was assumed that every cell starts cycling at 100% SoH even though it slightly reduced the goodness of fit. The linear fitting results summarized in Table 5 clearly substantiate the linearity between SoH and total discharge capacity throughput, where the degradation rate (slope) p 1 depends on the cycling condition. However, the limitation of this linearity needs to be noted: it only holds until approximately 80% SoH is reached, whereafter capacity retention drops at an increased rate most likely due to depletion of cyclable lithium [8,18,19,37].

5.2. Degradation Rate Equation

The slope of capacity degradation clearly depends on the cycling condition, based on the presented results in Section 5.1. Therefore, mathematically describing the relation between the cycling stress factors Temperature (T), DoD and c-rate (C) using a polynomial function p 1 ( T , D o D , C ) would allow one to estimate the capacity fade in our Si-alloy cells by simply using Equation (2), where C t h r o u g h is the measured total discharge capacity throughput. Furthermore, measuring total discharge capacity throughput is easily implementable by numerical integration of the measured current, similar to the Coulomb counting method for SoC estimation [49].
S o H ( C t h r o u g h ) = p 1 ( T , D o D , C ) × C t h r o u g h + p 2
As such, the experimentally-obtained degradation rates ( p 1 ) shown in Table 5, together with their respective cycling condition values for T, DoD and C-rate are used as input for a multivariate polynomial regression analysis. The matrix representation B = C × A of the system of second order polynomial equations is presented in Equation (3), where the elements b i of Matrix B represent the experimentally-obtained degradation rates, elements T i , D o D i and C i of Matrix C represent the stress factors of the cycling condition and Matrix A contains the coefficients a i that describes their relation.
b 1 b 2 b 3 b 4 b 5 b 6 = T 1 D o D 1 C 1 T 1 · D o D 1 D o D 1 · C 1 T 1 · C 1 T 1 2 D o D 1 2 C 1 2 1 T 2 D o D 2 C 2 T 2 · D o D 2 D o D 2 · C 2 T 2 · C 2 T 2 2 D o D 2 2 C 2 2 1 T 6 D o D 6 C 6 T 6 · D o D 6 D o D 6 · C 6 T 6 · C 6 T 6 2 D o D 6 2 C 6 2 1 * a 1 a 2 a 3 a 4 a 5 a 6 a 7 a 8 a 9 a 10
This analysis results in the second order polynomial equation with three variables p 1 ( T , D o D , C ) , presented in Equation (4). This degradation rate equation allows one to estimate the degradation rate (%SoH/mAh) given curtain cycling conditions within the boundaries of 10 °C–45 °C, 60–100% DoD and C/3–1C.
p 1 ( T , D o D , C ) = - 7.56 e - 4 D o D + 2.72 e - 5 T - 1.82 e - 6 T · C + 2.07 e - 7 T · D o D - 6.82 e - 7 T 2 + 4.08 e - 4 D o D 2
The surface of the degradation rate equation is plotted in Figure 14a against depth of discharge and temperature at a C/3 current rate. The influence of current rate is not shown since only two measurement points are available (C/3 and 1C), which results in a linear relation in any case. This means that the surface plot for 1C cycling is identical to C/3 cycling, only shifted downwards on the Z-axis due to increased capacity degradation at higher c-rates (Section 4.2.1). Furthermore, Figure 14b,c present 2D plots of respectively the DoD’s and temperature’s influence on the degradation rate. It is observed that the degradation rate decreases with falling DoD, as per the results and discussion presented in Section 4.2.2. The temperature-degradation rate relationship shows a peak (lowest degradation rate) at 20 °C, suggesting that this would be the optimal temperature to cycle the Si-alloy cells.

5.3. Dynamic Model Validation

Next to providing an extended understanding of the Si-alloy battery aging process during more practical automotive applications (Section 4.2.4), the real-life driving cycle test condition, based on the WLTP, was also used as dynamic model validation for the developed capacity fade model. The influence of the WLTP driving cycles on the Si-alloy cell’s capacity retention was previously presented in Figure 11. The model was validated by using Equation (2) with the appropriate cycling condition parameters of the WLTP for the degradation rate equation (Equation (4)), which are: 25 °C, 60% DoD and 0.1430 C. It should be noted, however, that the used C-rate was the median value of the current during one WLTP discharge cycle (Section 3.3) rather than the actual current rate at every time step during cycling. This is a necessary approximation because the individual (dis-)charge events during one WLTP cycle are impossible to correlate to their respective, very limited DoD around varying middle SoCs, which goes beyond the scope of the performed cycle aging test campaign presented in Section 3.3. Nevertheless, the obtained SoH predictions using the presented capacity fade model shown in Table 6 are very promising with a median error of only 0.5% over 250 cycles, i.e., 2500 WLTP cycles. This allows us to conclude that the presented capacity fade modeling methodology is both legitimate and sufficiently accurate.

6. Conclusions

In this research, twenty-four high capacity (1360 mAh) NMC622/Si-alloy Li-ion full pouch cells with high silicon content (55%) are cycle aged under seven different cycling conditions, including the Worldwide harmonized Light Vehicles Test Procedure (WLTP) driving cycle, to study the effect of different stressors on the cycle life of Si-anode full cells, among which are the effect of ambient temperature, Depth of Discharge (DoD) and the discharge current. Since Si anodes endure substantial volumetric expansion/contraction (280–400%) due to repeated (de-)lithiation, giving rise to high internal stresses within the anode, which lead to the consumption of cyclable lithium and capacity fade [3,5,6,7,8,9,10,11,12,13,14], the cells are volumetrically constrained to improve their cycle life. Using an innovative test setup allows us to regulate the applied initial pressure on the volumetrically-constrained Si-alloy cell during the calibration procedure, while a resistive pressure sensor allows us to measure the perpendicular counterforce as a result of repeated (de-)lithiation during cycling. After the identification of the optimal initial pressure (7.5 kg) during the pressure study, the uniquely vast testing campaign on Si-anode full cells allows us to study and quantify independently for the first time the influence of current rate, depth of discharge and ambient temperature on their cycle life.
Firstly, it is concluded that an increased current rate has an adverse effect on battery lifetime. The average cycles to EoL diminished from 160 to 143 for a current rate of C/3 and 1C, respectively, which corresponds to a significant decrease in battery lifetime of 10.6%.
Furthermore, the results reveal a drastic improvement in cycle life for the Si-alloy cells with reduced DoD cycling conditions of up to 100 full equivalent cycles. It is concluded that the magnitude of pressure variations within the cell present the major driving force behind the cell’s degradation, which are measured to be significantly less at lower DoD. Combined with the comparison of total discharge throughput during cycling against capacity retention, this supports the assumption that the induced stress of repeated (de-)lithiation of silicon particles results in continuous growth of the SEI layer on the silicon-alloy anode, during which gradual consumption of cyclable lithium occurs and the electrolyte additive FEC is depleted by parasitic reactions on the anode [8,18,19,37].
Greater aging rates are observed both at 45 °C and 10 °C cycling conditions. Comparing capacity degradation results from calendar aging two cells at 45 °C and 25 °C allows us to conclude that the parasitic, electrolyte-additive-consuming reactions at the anode surface occur spontaneously and are thermally activated, which results in CO2 gas formation, increasing the internal pressure of the cell, which damages the SEI layer further and thus results in an increased consumption rate of cyclable lithium and capacity loss when cycling at higher temperatures.
It is observed that the Si-alloy cells show excellent capacity retention throughout the drive cycle aging, based on the WLTP, where one cell maintained 88.5% of its initial capacity after 46,600 km (= 200 cycles × 10 WLTP’s/cycle × 23.3km/WLTP). Assuming that the aging rate remains constant, linear extrapolation of the capacity retention obtains an estimate of 98,536 km to battery EoL, which allows us to conclude that Si-alloy cells show promising prospects for automotive applications.
The pressure evolution is monitored over battery lifetime and exhibits the same behavior during all cycling conditions: as the capacity retention decreases, an irreversible pressure increase transpires. A clear relationship can be identified between capacity retention and the pressure behavior of the Si-alloy cells, which implies a correlation between the main aging mechanism within Si-alloy cells and their irreversible pressure growth. Further investigation of this phenomenon, as well as the exploration of using pressure measurements for state estimations will be the topic of a following paper.
Finally, a linear relationship between the cell’s total discharge capacity throughput and its capacity retention is demonstrated, where the slope of degradation depends on the cycling condition. Therefore, the relation between the cycling condition’s temperature, DoD and c-rate is described by a polynomial function that allows us to estimate the capacity fade in the Si-alloy cells by only measuring the total capacity throughput. This capacity fade model is validated using the dynamic WLTP drive cycle, showing a mean error of only −0.5% on the predicted SoH after 250 cycles.

Author Contributions

Conceptualization, L.D.S. and G.B.; Methodology, L.D.S., G.B., J.S. and M.M.; Software, L.D.S.; Validation, L.D.S.; Formal analysis, L.D.S.; Investigation, L.D.S.; Resources, M.M. and M.W.-M.; Data curation, L.D.S, G.B. and J.S.; Writing, original draft preparation, L.D.S.; Writing, review and editing, Y.F., N.O. and M.M.; Visualization, L.D.S.; Supervision, J.S., J.v.M. and N.O.; Project administration, J.S., M.M. and G.B.; Funding acquisition, N.O. and M.W.-M.

Funding

This research was funded by the European Union’s Horizon 2020 research and innovation program under Grant Agreement No. 653531.

Acknowledgments

We acknowledge Flanders Make for the support to our research group MOBI.

Conflicts of Interest

The authors declare no conflict of interest.

Abbreviations

The following abbreviations are used in this manuscript:
SiSilicon
SEISolid Electrolyte Interface
WLTPWorldwide harmonized Light vehicle Test Procedure
QOCVQuasi-Open Circuit Voltage
CCCVConstant Current Constant Voltage
HPPCHybrid Pulse Power Characterization
BoLBeginning of Life
EoLEnd of Life
SoCState of Charge
DoDDepth of Discharge
SoHState of Health
FECFluoroethylene Carbonate

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Figure 1. (a) Statistical analysis on the discharge capacity of Silicon cells at Beginning of Life (BoL) and (b) quasi-open circuit voltage test performed at BoL on a silicon cell.
Figure 1. (a) Statistical analysis on the discharge capacity of Silicon cells at Beginning of Life (BoL) and (b) quasi-open circuit voltage test performed at BoL on a silicon cell.
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Figure 2. Pressure setup to monitor developed perpendicular counterforce due to repeated (de-)lithiation of the Si-alloy full cells [21].
Figure 2. Pressure setup to monitor developed perpendicular counterforce due to repeated (de-)lithiation of the Si-alloy full cells [21].
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Figure 3. Overview of the performed lifetime study and developed capacity fade model of silicon cells.
Figure 3. Overview of the performed lifetime study and developed capacity fade model of silicon cells.
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Figure 4. Flowchart representation of the testing procedure for lifetime testing of Si-alloy full cells.
Figure 4. Flowchart representation of the testing procedure for lifetime testing of Si-alloy full cells.
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Figure 5. Influence of the initial applied perpendicular pressure on Si-alloy cell’s capacity retention, where the black horizontal line indicates the optimum capacity retention after 150 cycles.
Figure 5. Influence of the initial applied perpendicular pressure on Si-alloy cell’s capacity retention, where the black horizontal line indicates the optimum capacity retention after 150 cycles.
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Figure 6. The influence of current rate on capacity retention over battery lifetime during cycling, where the black line indicates End of Life (EoL). Increases in SoH at Cycles 51 and 101 due to CCCV charge at the start of the cycling block, instead of consecutive C/3 charges.
Figure 6. The influence of current rate on capacity retention over battery lifetime during cycling, where the black line indicates End of Life (EoL). Increases in SoH at Cycles 51 and 101 due to CCCV charge at the start of the cycling block, instead of consecutive C/3 charges.
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Figure 7. The influence of DoD on capacity retention over battery lifetime, where the black line indicates EoL.
Figure 7. The influence of DoD on capacity retention over battery lifetime, where the black line indicates EoL.
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Figure 8. The effect of cycling DoD on (a) the cell’s generated perpendicular counterforce pressure due to volumetric constraints and (b) total discharge capacity throughput after 50, 100 and 150 cycles; the color legend in (b) is identical to (a).
Figure 8. The effect of cycling DoD on (a) the cell’s generated perpendicular counterforce pressure due to volumetric constraints and (b) total discharge capacity throughput after 50, 100 and 150 cycles; the color legend in (b) is identical to (a).
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Figure 9. The influence of ambient temperature on capacity retention over Si-alloy battery lifetime, where the black line indicates EoL.
Figure 9. The influence of ambient temperature on capacity retention over Si-alloy battery lifetime, where the black line indicates EoL.
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Figure 10. Discharge capacity of two calendar aged Si-alloy cells at 25 °C and 45 °C, stored at 4.4 V (100% SoC) and both stored at an optimized initial pressure of 7.5 kg.
Figure 10. Discharge capacity of two calendar aged Si-alloy cells at 25 °C and 45 °C, stored at 4.4 V (100% SoC) and both stored at an optimized initial pressure of 7.5 kg.
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Figure 11. The influence of the standardized Worldwide harmonized Light vehicle Test Procedure (WLTP) driving cycles on the capacity retention of Si-alloy cells.
Figure 11. The influence of the standardized Worldwide harmonized Light vehicle Test Procedure (WLTP) driving cycles on the capacity retention of Si-alloy cells.
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Figure 12. Measured perpendicular pressure evolution due to volumetric constraints of a Si-alloy pouch cell and the discharged capacity during cycles 1–10, 5–60 and 100–110.
Figure 12. Measured perpendicular pressure evolution due to volumetric constraints of a Si-alloy pouch cell and the discharged capacity during cycles 1–10, 5–60 and 100–110.
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Figure 13. Linear relationship between total discharge capacity throughput (mAh) and the state of health until the EoL criterion (80% SoH), for all tested Si-alloy cells under different cycling conditions.
Figure 13. Linear relationship between total discharge capacity throughput (mAh) and the state of health until the EoL criterion (80% SoH), for all tested Si-alloy cells under different cycling conditions.
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Figure 14. (a) The capacity degradation rate expressed in % SoH / mAh of discharged capacity throughput, mapped by the developed degradation rate Equation (4) at C/3 between 10 °C and 45 °C and 60% and 100% DoD. 2D plots of the degradation rate’s dependencies on (b) depth of discharge and (c) temperature, where red dots mark experimentally-observed degradation rates (Table 5).
Figure 14. (a) The capacity degradation rate expressed in % SoH / mAh of discharged capacity throughput, mapped by the developed degradation rate Equation (4) at C/3 between 10 °C and 45 °C and 60% and 100% DoD. 2D plots of the degradation rate’s dependencies on (b) depth of discharge and (c) temperature, where red dots mark experimentally-observed degradation rates (Table 5).
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Table 1. Overview of available literature reporting on full Li-ion cells with Si anodes and their specifications.
Table 1. Overview of available literature reporting on full Li-ion cells with Si anodes and their specifications.
PaperCell typeCathodeAnodeSi ContentCapacity RetentionCapacityPrelithiated
Kierzek [22]CoinNMC532Si-C18%72% at 100 cycles50 mAhno
Lu [23]CoinNMC532-LFO
Kalaga [24]CoinNMC532Si-Gr15%66% at 100 cyclesano
Chevrier [20]CoinNMC622Si-alloy55%80% at 500 cycles2 Ahyes
CoinNMC622Si-alloy55%80% at 150 cycles2 Ahno
CylindricalNMC622Si-alloy30%80% at 500 cycles2 Ahyes
Klett [25]CoinNMC532Si-Gr15%80% at 20 cycles bano
Delpuech [19]CoinLCOSia80% at 20 cycles bano
Dupré [18]CoinNMC111Si-C80%80% at 20 cycles bano
Louli [3]PouchNCASiO-Graa260 mAhno
PouchLCOSi-Alloya86% at 90 cycles230 mAhno
PouchNCASi-Ca93% at 90 cycles165 mAhno
Marinaro [26]PouchNMC532Si-alloy55%80% at 290 cycles1.22 Ahno
Gabrielli [27]CoinLMNO-O/RSi-C75%75% at 100 cyclesano
a Information unavailable in publication; b Not explicitly mentioned, deduced from publication information.
Table 2. Cell specifications of tested 1360-mAh NMC622/Si-alloy pouch cells.
Table 2. Cell specifications of tested 1360-mAh NMC622/Si-alloy pouch cells.
PropertiesValue
Cathode Composition
L i N i 0 . 6 M n 0 . 2 C o 0 . 2 O 2 93%
Carbon4%
HSV1800 (Arkema)3%
Loading (mg/cm2)17.5
Electrode density (g/cc)3.0
Anode Composition
Si-alloy (3M)55%
SMG-A333%
LiPAA10%
Super-PLi2%
Loading (mg/cm2)6.5
Electrode density (g/cc)1.7
Electrical
Nominal capacity (mAh)1360
Upper cut-off voltage (V)4.4
Lower cut-off voltage (V)2.7
Specific energy (Wh/kg)205
Table 3. Cycle aging test campaign.
Table 3. Cycle aging test campaign.
DoD100%80%60%
TC-rate
10 °CC/32
25 °CC/3222
1C2
45 °CC/32
Table 4. Number of full equivalent cycles to end of life for both tested cells at every cycling condition.
Table 4. Number of full equivalent cycles to end of life for both tested cells at every cycling condition.
DoD100%80%60%
TC-rate
10C/3107/104
25C/3160/159161/159244/a
1C144/142
45C/339/37
a Cell did not reach end of life conditions.
Table 5. Linear fitting results per cycling condition relating total discharge capacity to state of health.
Table 5. Linear fitting results per cycling condition relating total discharge capacity to state of health.
Cycling ConditionLinear Fit
T (C)DoD (%)C-Rate (C)p1p2R2RMSE
251001/3−1.048 × 10 4 1000.9950.494
251001−1.351 × 10 4 1000.9532.055
101001/3−1.481 × 10 4 1000.9870.904
451001/3−5.248 × 10 4 1000.9581.767
25801/3−1.016 × 10 4 1000.9930.584
25601/3−6.576 × 10 5 1000.9631.145
Table 6. Dynamic validation results of the presented capacity fade model based on the WLTP driving profile.
Table 6. Dynamic validation results of the presented capacity fade model based on the WLTP driving profile.
Cycles (#)Capacity throughput (Ah)State of Health (%)
MeasurementPredictionError
00.00100.00100.000.00
5049.9297.0597.420.36
10099.8494.5894.830.26
150149.7792.7492.25−0.49
200199.6990.4689.67−0.79
250249.6188.8287.09−1.73
Median−0.49
Mean−0.48

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De Sutter, L.; Berckmans, G.; Marinaro, M.; Smekens, J.; Firouz, Y.; Wohlfahrt-Mehrens, M.; Van Mierlo, J.; Omar, N. Comprehensive Aging Analysis of Volumetric Constrained Lithium-Ion Pouch Cells with High Concentration Silicon-Alloy Anodes. Energies 2018, 11, 2948. https://0-doi-org.brum.beds.ac.uk/10.3390/en11112948

AMA Style

De Sutter L, Berckmans G, Marinaro M, Smekens J, Firouz Y, Wohlfahrt-Mehrens M, Van Mierlo J, Omar N. Comprehensive Aging Analysis of Volumetric Constrained Lithium-Ion Pouch Cells with High Concentration Silicon-Alloy Anodes. Energies. 2018; 11(11):2948. https://0-doi-org.brum.beds.ac.uk/10.3390/en11112948

Chicago/Turabian Style

De Sutter, Lysander, Gert Berckmans, Mario Marinaro, Jelle Smekens, Yousef Firouz, Margret Wohlfahrt-Mehrens, Joeri Van Mierlo, and Noshin Omar. 2018. "Comprehensive Aging Analysis of Volumetric Constrained Lithium-Ion Pouch Cells with High Concentration Silicon-Alloy Anodes" Energies 11, no. 11: 2948. https://0-doi-org.brum.beds.ac.uk/10.3390/en11112948

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