조규상
(Kyusang Cho)
1
찬드라 발라무루간
(Chandran Balamurugan)
2
임하나
(Hana Im)
3
김형진
(Hyeong-Jin Kim)
4*
-
차세대에너지연구소, 광주과학기술원
(Research Institute for Solar and Sustainable Energies, Gwangju Institute of Science
and Technology, Gwangju 61005, Republic of Korea)
-
히거신소재연구센터, 광주과학기술원
(Heeger Center for Advanced Materials (HCAM), Gwangju Institute of Science and Technology,
Gwangju 61005, Republic of Korea)
-
세종대학교
(Department of Integrative Bioscience and Biotechnology, Sejong University, Seoul 05006,
Republic of Korea)
-
융합기술원, 광주과학기술원
(Graduate School of Energy Convergence, Institute of Integrated Technology, Gwangju
Institute of Science and Technology, Gwangju 61005, Republic of Korea)
Copyright © 2021 The Korean Institute of Metals and Materials
Key words
lithium-ion battery, separator, solid electrolyte interface
1. Introduction
Lithium-ion batteries (LIBs) are essential power sources in a wide range of products
in our modern society. Portable devices ranging from mobile phones to laptops, from
electric vehicles (EV) to large-scale energy storage systems (ESS) are powered by
LIBs [1-3]. Considerable research has been devoted to efforts to enhance their energy density,
power density, life span, and total capacity. Among them, various attempts to improve
the performance of the separator, which is an essential component of a robust LIB,
have been made by numerous researchers. These separators provide chemical stability
and mechanical strength, but they are typically too soft and will melt at high temperatures
[4,5]. The difference in the polarities of the separator and electrolyte surface also
has a negative impact on LIBs [6,7].
Recently, several efforts have attempted to address the weaknesses of the standard
separator. Micro-nano particles prepared as inert ceramic oxides (Al2O3, SiO2, and TiO2) have been coated on the separator to increase ionic conductivity, and reduce the
safety problems caused by internal electrical short circuits [8-11]. The ceramic-coated separator provides micropore channels for lithium-ion migration,
acts as a wall between the anode and the cathode, and prevents electrical shorts from
the anode [4,5]. For these reasons, ceramic-coated separators are currently used in all EV batteries.
Polyimide (PI) has also been used as a separator because of its thermal stability,
high tensile strength, and excellent electrolyte wettability [12-14]. However, it is rarely used in applications, because of the high cost and complex
manufacturing process of PI membranes.
In this study, we examined the differences of commercial polypropylene (PP), ceramic
(Boehmite) coated PP (C-PP), and polyimide (PI) separators from an electrochemical
perspective. For the battery model, the half-cell using lithium nickel manganese cobalt
oxides (NMC), which is the most used in the current industry, and the full-cell using
graphite as the opposite electrode were adopted [15]. We conducted rate capability tests at rates from 0.1 to 5 C, focusing on the differences
in each C rate section. Also, a high C rate cycle stability test was conducted to
determine which separator membrane could maintain good performance, even at fast charge
and discharge rates, which is essential to meet the demand for fast charging in mobile
devices and electric vehicles.
In addition, electrochemical impedance spectroscopy (EIS) tests were carried out for
each separator. EIS is a powerful tool for determining charge-transfer resistance
and solid electrolyte interphase (SEI) layer resistance which has high resistance
similar with nonconductor [16]. After the cycle tests, we also disassembled the cell and checked both sides of
each separator, and the surface of the NMC electrode. Finally, we tested the three
separators in an NMC//graphite full-cell system to study each separator’s performance
from a commercial perspective.
2. Experimental Procedure
2.1 Material Information
The polypropylene (PP) separator was purchased from Celgard 2400. The ceramic-coated
polypropylene (C-PP) was purchased from Everener Battery Solution (Korea). Boehmite
was coated to a 4 um thickness on the 12 um thick PP separator. The porous polyimide
(PI) separator was purchased from TOK (Japan). The porosity of the PI separator was
70 % and thickness was 20 um. As the electrolyte, 1 M LiPF6 in ethylene carbonate (EC):dimethyl carbonate (DMC) (1:1 wt%) products from the company
ENCHEM (Korea) were used. The lithium metal chip was a 16 Φ product of NEBA (Korea).
NMC is a product of LGCHEM with a nickel, manganese, cobalt ratio of (8:1:1). The
2032 coin-cell parts were purchased from Welcos corp. (Korea).
2.2 Cell assembly
The NMC electrode was prepared by the slurry doctor blade coating method. The NMC
power was mixed with a carbon additive (Carbon Black, Super-C) and polyacrylic acid
(PAA) binder at an 8:1:1 ratio (wt%) in series with the proper amount of DI water
as a solvent. The slurry was coated on 20 um thickness aluminum foil by doctor blade.
The material loading mass was set as 2.5 mg cm-2. The graphite anode was made by Alfa Aesar using the above doctor blade procedure
and 20 um thick copper foil. The sample 2032 coin type cells were assembled using
PP, C-PP, and PI as the separators, the NMC electrode as a working electrode, lithium
metal as a counter, and a reference electrode in a glove box filled with Argon gas.
The ceramic coated side was aligned to face the lithium metal. In the NMC//graphite
full cell assembly, lithium metal was replaced by the graphite electrode. 1 M LiPF6 in EC:DEC (1:1) and EC:DMC (1:1) were used as electrolytes.
2.3 Characterization and analysis
The surface morphologies of the PP, C-PP, and PI separators were visualized by field
emission scanning electron microscope (SEM, Jeol, JSM-7500F). The cell performance
was evaluated using a Wonatech Cycler System (Wonatech, WBCS3000). The potential window
was set at 2.8~4.2 V. The cycle testing was performed using a galvanostatic charge-discharge
analysis with a 5 C rate. The rate capability test was performed at 0.1, 0.2, 0.5,
1.0, 2.0, 5.0, 0.1 C rate in sequence (1 C = 150 mAh gNMC-1). In the full cell cycle test, the first 5 cycles were tested at the 0.1 C rate for
electrode activation, and after that, 200 cycles were set with the 1 C rate. EIS analysis
was conducted using a Biologic potentiostat (Biologic, VMP-3). We used a 105~10-1 Hz scale and EIS fitting was performed using the EC-Lab software Z-fit program.
After the cycle tests, the coin cells were carefully disassembled in a glove box to
extract the shaped separator. The obtained separators were rinsed in DMC based on
their used electrolyte composition, in a glove box. After complete drying, SEM analysis
was carried out to determine the differences in the morphology of each side. When
measured at a high voltage, the separator structure burns. So the acceleration voltage
of the SEM electron beam was set to 3 kV.
3. Results and Discussion
First, we attempted to determine the surface structure of each separator by SEM analysis.
Fig 1 shows the surface SEM image of the PP separator, which has a fiber structure with
very small porosity. Fig 1(b) shows the surface of the C-PP separator exhibiting the porous ceramic coating layer
composed of 1~10 um boehmite particles. This layer prevents the shrinkage problem
that occurs at high temperatures of 100 to 200 °C [17]. The PI separator has a porous structure like a sponge, with 1~10 um sized pores,
as shown in Fig 1(c). The high porosity of the PI separator allows the electrolyte to transfer easily,
and this is the main way its reduces internal resistance (RS).
Electrochemical tests were carried out to examine the difference in battery performance
with the three separators. As shown in Fig 2, the discharge capacities of the three separators were 192 mAh g-1, 190 mAh g-1, 181 mAh g-1. There was no significant difference between the PP cell and the C-PP cell in the
first few cycles. As the cycles increased, the capacity retention characteristics
and stability in the C-PP cell were excellent. Even at a high current density at the
5 C rate, the capacity of the C-PP cell was the highest, 112 mAh g-1. Notably, the PP cell had a sharp drop in capacity when compared to the 2 C rate,
which was the previous current density.
For the next 10 cycles at the 0.1 C rate, the C-PP cell showed the best cycle stability
performance. The capacity of the C-PP cell decreased from 188 mAh g-1 to 183 mAh g-1, only a 2.3% drop. This fading was only half that of the PP cell (200 mAh g-1 to 190 mAh g-1, almost a 5% decrease) and the PI cell (180 mAh g-1 to 174 mAh g-1, almost 3.6%). These results suggest that the ceramic layer in the C-PP separator
influences the stabilization of the lithium ions and intermediate ions [18]. By adding the ceramic coated layer to the separator, interfacial impedance was
reduced and lithiumion migration was promoted across the coating layer [17]. Also, ceramic layers can prevent electrolyte leakage during repeated cycles [19]. The PI separator has many micro-pores, and not only lithium-ion but other intermediates
can also migrate through these pores. This phenomenon is the main reason for the capacity
fading observed with PI cells.
Based on these results, we established the cycle stability performance of each of
the three cells at the 5 C rate, as shown in Fig 3. Since the difference in capacity and stability was large at the 5 C rate, cycle
measurements were performed at the corresponding current density. As shown in Fig 3(a), the irreversible capacity and initial capacity in the PP cell and the C-PP cell
were similar at 174 mAh g-1 and 181 mAh g-1, respectively, and only the PI cell showed a relatively low capacity of 138 mAh g-1. However, after 200 cycles, the C-PP cell maintained a capacity of 115 mAh g-1. The PP cell continued to decrease to a capacity of 80 mAh g-1 and the PI cell declined to 64 mAh g-1.
Fig 3(b) shows the charge-discharge voltages of the three cells vs. Li/Li+. The capacitive slope of the C-PP cell was higher than the other two cells between
3.4 V and 4.0 V. And the PI cell hardly showed any capacitive slope in the section
of the 350th charge-discharge graph.
To examine this result more precisely, we analyzed the differential capacity vs. cell
voltage graph for each cell after the 350th cycle, as shown in Fig 3(c). The y value of this graph represents the plateau of each graph, and the higher the
value, the longer the plateau region. In the C-PP cell, a redox peak exists near 4.0
V and 4.15 V. Each peak represents the phase transition of NMC from monoclinic (M)
to hexagonal (H2) and then from hexagonal (H2) to hexagonal (H3). In the oxidation
peak, a large sharp peak was observed near 3.6 V. This peak can be explained as the
phase transition of the NMC from a hexagonal to a monoclinic (H1 → M) lattice [20]. The main reason for capacity fading near the discharge region is rapid volume contraction
during the structural transformation from H2 to H3 phase [21]. Using the C-PP separator, the peaks were less polarized, less shifted, and maintained
the capacity reaction.
To better understand the results of the cycle test, we used EIS analysis. As shown
in Fig 3(d), the resistance of the high-frequency region is related to the SEI layer of the electrode
(RSEI) [22]. In low-frequency region, the resistance represents the charge-transfer resistance
of the two electrode-electrolyte interfaces (RCT) [22]. By using the Z-fit program with the EIS model of the NMC half-cell, we calculated
the resistances of the solution, SEI layer, and charge-transfer for each cell, as
listed in Table 1.
In Fig 3(d), the resistance of the C-PP cell’s SEI layer was determined to be the lowest of the
three samples. The result indicates the intermediates of several phase of NMC were
less than other separators [23]. The ceramic inert oxides coated on the surface of the polymer separator led to
an increase in ionic conductivity [5], and that’s why the C-PP separator had the lowest impedance value. Overall, despite
the extremely fast 5C rate condition, our experiments demonstrated remarkable results
in capacity stability, compared to previous papers using ceramic-coated separators
[8,24-26].
3.1 Cell disassembly after cycle tests
After the cycle testing at the 5 C rate, we disassembled the cells and analyzed the
separators and electrode surfaces. Part of the PP separator structure was broken,
and the opaque white tissue was changed to a thin translucent tissue. More than 90%
of the PP separator that was directly facing the electrode became a thin translucent
structure. However, in the C-PP cell, the separator retained its original structure.
In the PI cell, there was a dark green region directly facing the electrolyte. The
edge part was pressed by the gasket when the coin cell was assembled and did not contact
the electrolyte. But after perfectly drying the solvent, that separator returned to
its original yellow color. Because the PI separator had 70% porosity, the structure
was easily torn. After sufficient drying, we peeled off the separator and carried
out the SEM analysis.
In Fig 4, the SEM images of each separator are shown. All of the left column images are the
Li facing side, and the right column is the NMC electrode facing side. The separator
tissue on the lithium-facing side was almost fully covered with some type of material.
However, it maintained half of the original structure of separators facing NMC electrodes.
Most of the pores in the PI separator were blocked by the layer, which means that
the internal structure was also affected. That is, the pore volume of the fiber-like
PP structure was decreased by the stacking of some intermediate layer on the fiber
structure.
Lithium-ion diffusion through a separator is a significant issue in battery performance.
If transport paths are blocked by the SSEI layer, then ionic conductivity will decrease,
and that can cause some serious problems for long-term cycling. Moreover, if this
phenomenon becomes severe, the separator pores will be blocked by the SSEI layer,
as we see in Fig 4(a), (e).
As shown in Fig 4(c), the rough ceramic layer was covered with the SSEI layer, and the porous sponge-like
structure was blocked by the SSEI layer in Fig 4(e). However, as shown in Fig 5(b), only a thin layer was formed on the surface of the C-PP separator, and as observed
through cracks on this surface, the original structure of the internal PP fiber was
retained. In addition, the surface of the PP (Fig 5(a)) and PI (Fig 5(c)) separators had a thick SSEI layer. Therefore, the use of a C-PP separator seems
to be a good strategy to prevent the pores of the separator from being blocked by
the SSEI layer, as indicated by our electrochemical analysis.
We also examined the NMC electrode surface using SEM and EDS analyses. Observing the
surfaces of each electrode, we found the overall morphology to be similar, and there
were no issues such as coating problems. However, it was noted that nickel and manganese
elution of the NMC occurred, causing a decrease in capacity when the battery continued
to be charged and discharged. We measured the EDS of the electrode surface to confirm
the ratio of surface elements [27]. As summarized in Table 2, the atomic ratio of each element was compared based on the relatively stable cobalt.
The manganese ratio of the electrode using the PP separator was found to be lower
than that of the other two separators, and the electrode using the PI separator had
the lowest ratio of nickel. On the other hand, the electrode using C-PP had a high
ratio of both nickel and manganese, which can be explained since the elution of nickel
and manganese was suppressed by the C-PP separator.
3.2 Full-cell application
We also conducted a NMC//Graphite full-cell cycle test to compare the three separators’
performance. As shown in Fig 6(a), in the first 5 cycles, the C rate was set to 0.1C to stabilize the NMC electrode
and the graphite electrode. After the 0.1 C rate cycle, we set a 1.0 C rate for 200
cycles, for a charge-discharge analysis. The C-PP and PP cells exhibited the best
capacity of 115 mAh g-1 among the three, and maintained 70% capacity after 200 cycles.
However, the PI cell was stable but showed low capacity. To determine the reason for
the differences among the separators, we conducted an EIS analysis after the cycle
stability test. In Fig 6(b), the Nyquist plots of each of the three separator cells are illustrated. In the high
frequency region, the semi-circle of C-PP was smaller than the other graphs. At this
point, we used the Z-fit program with the full-cell model. This model is composed
of solution resistance, SEI layer resistance, anode resistance, and cathode resistance.
The results are organized in Table 3. We observed that the SEI resistance of the C-PP cell was lowest for the three sets.
The structure of the C-PP separator was maintained by the ceramic layer, and that
affected the cycle performance.
4. Conclusion
In this study, we report the differences of PP, C-PP and PI separator surfaces after
cycle testing. The electrochemical properties of these separators were also observed
in half-cell and full-cell tests. In the rate capability test, the C-PP separator
showed stable and high capacity characteristics at a high 5 C rate. Because of the
ceramic layer on the PP membrane, lithium-ion migration was stabilized and the phase
transition of NMC was well controlled. Also, a less resistive solid electrolyte interphase
was the critical factor in the C-PP separator performance.
To examine the surface of each separator, we disassembled the cycled cells and observed
the surfaces of both sides of the separator and electrode surface. Normal PP and PI
separators were blocked by electrolyte intermediates, known as the SSEI layer, and
this phenomenon made it difficult for lithium-ions to effectively migrate by reducing
the pore size of each separator. However, with the C-PP, the coated ceramic layer
worked as a barrier, so the internal fiber structure was maintained, and this played
a significant role in ionic conductivity. These ceramic layers can effectively limit
SSEI layer formation on the PP separator from, reducing the effect of the stacked
intermediates on the separator structure and pores. In addition, based on the EDS
results of the NMC electrode, the C-PP separator helped prevent manganese and nickel
element elution to the anode through the electrolyte and separator. Finally, the results
of the NMC//Graphite full-cell confirmed that cycle stability was excellent when the
C-PP separator was used. Our work can provide guidelines for the life management of
EV batteries and separator development issues.
As shown in Fig 3(d), the resistance of the C-PP cell’s SEI layer was the lowest among the three samples.
The result suggests the intermediates of several phase of NMC were less than the other
separators [23]. Coating the surface of polymer separators with the inert ceramic oxides leads to
an increase in ionic conductivity [5], and that’s why the C-PP separator’s had the lowest impedance value. Overall, despite
the extremely fast 5C rate condition, our experiments achieved remarkable capacity
stability compared to previous papers using ceramic-coated separators [8,24-26].
Acknowledgements
This research was supported by the Korea Institute of Energy Technology Evaluation
and Planning (KETEP) and the Ministry of Trade, Industry & Energy (MOTIE) of the Republic
of Korea [Grant No. 20204010600340] and a GIST Research Institute (GRI) grant funded
by the GIST in 2021.
REFERENCES
Armand M., Tarascon J. M., Nature,451, 652 (2008)

Dunn B., Kamath H., Tarascon J. M., Science,334, 928 (2011)

Goodenough J. B., Park K. S., J Am Chem Soc,135, 1167 (2013)

Lee H., Yanilmaz M., Toprakci O., Fu K., Zhang X. W., Energ Environ Sci,7, 3857 (2014)

Nunes-Pereira J., Costa C. M., Lanceros-Mendez S., J Power Sources,281, 378 (2015)

Saunier J., Alloin F., Sanchez J. Y., Caillon G., J Power Sources,119, 454 (2003)

Lee Y. M., Kim J. W., Choi N. S., Lee J. A., Seol W. H., Park J. K., J Power Sources,139,
235 (2005)

Shin W. K., Kim D. W., J Power Sources,226, 54 (2013)

Shi C., Dai J. H., Shen X., Peng L. Q., Li C., Wang X., Zhang P., Zhao J. B., J Membrane
Sci,517, 91 (2016)

Gong W. Z., Zhang Z., Wei S. Y., Ruan S. L., Shen C. Y., Turng L. S., J Electrochem,Soc,
167 (2020)

Wang Z., Pang P. P., Ma Z., Chen H. Y., Nan J. M., J Electrochem,Soc, 167 (2020)

Huang X. S., J Solid State Electr,15, 649 (2011)

Jiang W., Liu Z. H., Kong Q. S., Yao J. H., Zhang C. J., Han P. X., Cui G. L., Solid
State Ionics,232, 44 (2013)

Lin D. C., Zhuo D., Liu Y. Y., Cui Y., J Am Chem Soc,138, 11044 (2016)

Han D., Park I., Kim M., Kim D., Jung H., Korean J. Met. Mater,57, 360 (2019)

Park J.-H., Choi Y.-S., Shim H. C., Ahn J.-P., Lee J.-C., Korean J. Met. Mater,57,
67 (2019)

Li D., Qin D. J., Nie F., Wen L. L., Xue L. X., J Mater Sci,53, 11038 (2018)

Yu L. H., Jin Y., Lin Y. S., Rsc Adv,6, 40002 (2016)

Choi J. A., Kim S. H., Kim D. W., J Power Sources,195, 6192 (2010)

Noh H. J., Youn S., Yoon C. S., Sun Y. K., J Power Sources,233, 121 (2013)

Jung R., Metzger M., Maglia F., Stinner C., Gasteiger H. A., J Electrochem Soc,164,
A1361 (2017)

Naoi K., Ogihara N., Igarashi Y., Kamakura A., Kusachi Y., Utsugi K., J Electrochem
So,152, A1047 (2005)

Lu P., Li C., Schneider E. W., Harris S. J., J Phys Chem C,118, 896 (2014)

Liu H. Y., Xu J., Guo B. H., He X. M., Ceram Int,40, 14105 (2014)

Sharma G., Jin Y., Lin Y. S., J Electrochem Soc,164, A1184 (2017)

Peng L. Q., Shen X., Dai J. H., Wang X., Zeng J., Huang B. Y., Li H., Zhang P., Zhao
J. B., J Electrochem Soc,166, A2111 (2019)

Li X. M., Colclasure A. M., Finegan D. P., Ren D. S., Shi Y., Feng X. N., Cao L.,
Yang Y., Smith K., Electrochim Acta,297, 1109 (2019)

Figures and Tables
Fig. 1.
SEM images of the (a) PP separator, (b) C-PP separator, (c) PI separator.
Fig. 2.
Rate capability test of NMC/Li half cells at 25 °C.
Fig. 3.
NMC/Li half-cell performance (a) cycle stability at the 5 C rate, (b) charge-discharge
normal graph, (c) differential capacity-voltage, (d) EIS Nyquist plot.
Fig. 4.
SEM images of the separators. (a, c, e) Li side, and (b, d, f) NMC side of PP, C-PP,
PI separator after 5 C rate cycle stability analysis.
Fig. 5.
SEM images of separators: (a) PP, (b) C-PP, (c) PI.
Fig. 6.
(a) Cycle performance of NMC/Graphite full cells at 25 °C and (b) EIS Nyquist plot
after cycle testing.
Table 1.
EIS results showing the resistance of each separator
|
Resistance
|
RS (Ω)
|
RSEI (Ω)
|
RCT (Ω)
|
|
PP
|
1.59
|
73.59
|
74.59
|
|
C-PP
|
1.568
|
40.13
|
113.5
|
|
PI
|
0.830
|
140
|
38.55
|
Table 2.
Atomic ratio based on cobalt in the NMC electrode elements for each separator
|
Separator
|
Nickel
|
Manganese
|
Cobalt (standard)
|
|
PP
|
7.091
|
0.636
|
1
|
|
C-PP
|
7.133
|
0.650
|
1
|
|
PI
|
7.037
|
0.667
|
1
|
Table 3.
EIS result showing the resistance of each separator after full-cell cycle testing
|
Resistance
|
RS (Ω)
|
RSEI (Ω)
|
RAn (Ω)
|
RCa (Ω)
|
|
PP
|
6.256
|
34.2
|
1.049
|
3.197
|
|
C-PP
|
2.312
|
17.02
|
8.665
|
1.14
|
|
PI
|
0.455
|
29.2
|
2.313
|
2.752
|