Ionic liquids (ILs) have been considered as an alternative class of electrolytes compared to conventional carbonate
solvents in rechargeable lithium/sodium batteries. However, the drawbacks of ILs are their reducing ionic conductivity
and their large viscosity. Therefore, mixtures of alkyl carbonate solvents with an IL and a sodium bis(trifluoromethane
sulfonyl)imide (NaTFSI) have been investigated to develop new electrolytes for sodium-ion batteries. In this work, NButyl-N-methylpyrrolidinium bis(trifluoro-methanesulfonyl) imide (Py14TFSI) was used as co-solvent mixing with
commercial electrolytes based on the carbonate, i.e. EC-PC (1:1), EC-DMC (1:1), and EC-PC-DMC (3:1:1). The
addition of ionic liquid in the carbonate-based electrolyte solution results in (i) enhancing ionic conductivity to be
comparable with a solvent-free IL-based electrolyte, (ii) maintaining the electrochemical stability window, and (iii) IL
acted as a retardant rather than a flame-inhibitor based on the self-extinguish time (SET) of the mixed electrolyte
mixture when exposed to a free flame. All mixed electrolyte systems have been tested in sodium-coin cells versus
Na0.44MnO2 (NMO) and hard carbon (HC) electrodes. The cells show good performances in charge/discharge cycling
with a retention > 96 % after 30 cycles (∼90 mAh.g-1 for NMO and 180 mAh.g-1 for HC, respectively) demonstrating
good interfacial stability and highly stable discharge capacities.
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Cite this paper: Vietnam J. Chem., 2021, 59(1), 17-26 Article
DOI: 10.1002/vjch.202000078
17 Wiley Online Library © 2021 Vietnam Academy of Science and Technology, Hanoi & Wiley-VCH GmbH
Safe sodium-ion battery using hybrid electrolytes of organic
solvent/pyrrolidinium ionic liquid
Phung Quan
1
, Le Thi My Linh
2
, Huynh Thi Kim Tuyen
3
, Nguyen Van Hoang
1,3
, Vo Duy Thanh
3
,
Tran Van Man
1,3
, Le My Loan Phung
1,3*
1
Department of Physical Chemistry, Faculty of Chemistry, University of Science, Vietnam National
University - Ho Chi Minh City, 227 Ly Thuong Kiet, District 5, Ho Chi Minh City 70000, Viet Nam
2
Materials Science and Engineering, Pennsylvania State University, Pennsylvania 16802
3
Applied Physical Chemistry Laboratory (APCLAB), University of Science, Vietnam National University -
Ho Chi Minh City, 227 Ly Thuong Kiet, District 5, Ho Chi Minh City 70000, Viet Nam
Submitted July 2, 2020; Accepted August 11, 2020
Abstract
Ionic liquids (ILs) have been considered as an alternative class of electrolytes compared to conventional carbonate
solvents in rechargeable lithium/sodium batteries. However, the drawbacks of ILs are their reducing ionic conductivity
and their large viscosity. Therefore, mixtures of alkyl carbonate solvents with an IL and a sodium bis(trifluoromethane
sulfonyl)imide (NaTFSI) have been investigated to develop new electrolytes for sodium-ion batteries. In this work, N-
Butyl-N-methylpyrrolidinium bis(trifluoro-methanesulfonyl) imide (Py14TFSI) was used as co-solvent mixing with
commercial electrolytes based on the carbonate, i.e. EC-PC (1:1), EC-DMC (1:1), and EC-PC-DMC (3:1:1). The
addition of ionic liquid in the carbonate-based electrolyte solution results in (i) enhancing ionic conductivity to be
comparable with a solvent-free IL-based electrolyte, (ii) maintaining the electrochemical stability window, and (iii) IL
acted as a retardant rather than a flame-inhibitor based on the self-extinguish time (SET) of the mixed electrolyte
mixture when exposed to a free flame. All mixed electrolyte systems have been tested in sodium-coin cells versus
Na0.44MnO2 (NMO) and hard carbon (HC) electrodes. The cells show good performances in charge/discharge cycling
with a retention > 96 % after 30 cycles (∼90 mAh.g-1 for NMO and 180 mAh.g-1 for HC, respectively) demonstrating
good interfacial stability and highly stable discharge capacities.
Keywords. Ionic liquid, Pyr14TFSI, co-solvent, electrolytes, sodium-ion batteries.
1. INTRODUCTION
Currently, lithium-ion technology is dominant in the
market from abundant small to medium (e.g.
portable electronic devices, power tools etc.) as well
as large-scale applications (e.g. electric/hybrid
vehicles, smart grids, electric energy storage from
renewable power sources).
[1,2]
However, the fast
growth of the lithium-ion batteries market leads to
big concerns about the availability and price rising
of lithium resources.
[3-5]
Lithium metal and lithium-
based compounds are not worldwide available and
are mainly distributed in some politically unstable
countries.
Although large-scale lithium recycling programs
have been planned, the future exhaustion of lithium
could occur.
[3,6,7]
These concerns have inspired the
battery scientist community to launch a novel
alternative technology with similar characteristics.
Low cost, large abundant availability of sodium
minerals as well as the feasible use of aluminum as
anode current collector
[8]
have promoted the research
in sodium-based technology as an alternative energy
storage system.
[9]
In addition, sodium- and lithium-
chemistry exhibit some similar fundamental
features,
[4,5]
and their redox potential differs by only
300 mV.
[8-10]
Nevertheless, like lithium-ion batteries,
Na-based systems often use alkyl carbonate-based
electrolytes, which represent safety issues.
[11-14]
For
instance, uncontrolled internal temperature increase
might cause flammability of the volatile organic
electrolyte with oxygen originated from the
decomposition of the positive electrode,
[15,16]
leading
to catastrophic events (burning, explosion, rapid cell
disassembly). Therefore, many efforts have been
devoted to designing highly stable and compatible
electrolytes aiming to resolve the drawbacks.
Interestingly, mixing ionic liquids (ILs) with
Vietnam Journal of Chemistry Le My Loan Phung et al.
© 2021 Vietnam Academy of Science and Technology, Hanoi & Wiley-VCH GmbH www.vjc.wiley-vch.de 18
aprotic organic solvents to form hybrid electrolytes
have been proposed in the literature.
[17-20]
For
example, a hybrid electrolyte comprising 1M LiPF6
in ethylene carbonate and diethyl carbonate mixed
with 1-ethyl-3-methylimidazolium
bis(trifluoromethanesulfonyl) imide ionic liquid is
possible to improve the safety without
compromising performances.
[17]
Moreover, N-alkyl
pyrrolidinium (Py) and piperidinium (Pp) cations
combined with imide anion have exhibited some
interesting properties. Indeed, viscosities are close to
those involved by imidazolium ILs and good
conductivity values are reached.
[21]
Comparing to the
quaternary ammonium ILs (N111xILs) and
piperidinium ILs, PyILs is as stable in oxidation as
PpILs with the HOMO values showing in table 1.
Furthermore, Py14TFSI + LiTFSI electrolyte showed
remarkable performance in terms of efficiency and
rate-capability for using in lithium cell using the
alloying Sn–C nanocomposite negative and
LiFePO4 positive electrodes.
[22]
Full-cell using ILs
electrolyte delivered a maximum reversible capacity
of about 160 mA h.g
-1
(versus cathode weight) at a
working voltage of about 3 V corresponding to an
estimated practical energy density of about 160
Wh.kg
-1
prolonged over 2000 cycles without
declined signs and satisfactory rate capability. This
high performance and the high safety provided by
the IL-electrolyte make this cell chemistry feasible
for application in new-generation electric and
electronic devices.
[22]
Wongittharom et al.
[23]
demonstrated the Na/NaFePO4 cell with a sodium
bis(trifluoromethanesulfonyl)imide (NaTFSI)-
incorporated Py14TFSI ionic liquid (IL) electrolyte
operating in the voltage of ∼3 V. The relationship
between cell performance and NaTFSI concentration
(0.1-1.0 M) at 25 and 50 °C is investigated. At 50
°C, the highest capacity of 125 mAh.g
−1
(at 0.05 C)
was found for NaFePO4 in a 0.5 M NaTFSI-
incorporated IL electrolyte; moreover, the cell could
retain 65% of this capacity when the charge-
discharge rate increased to 1C. Py14TFSI could be
used as a co-solvent with conventional carbonate
solvents in mixed electrolytes to enhance the thermal
and oxidation potential stability. The previous
studies indicated that electrolytes contain 20-30
%wt. of IL give the best balance between viscosity
and ionic conductivity.
[24-26]
Herein, we report the characterization of hybrid
electrolytes prepared by a large addition of an ionic
liquid, Py14TFSI, to binary solvents containing a
sodium salt dissolved in carbonate-based
(combination of ethylene carbonate (EC), dimethyl
carbonate (DMC), and propylene carbonate (PC))
solutions, i.e. 1M NaTFSI in EC-DMC (1:1 %wt)
and EC-PC (1:1 %wt). The performance of sodium
half-cells using Hard carbon (HC) and
NaMn0.44MnO2 (NMO) was tested with these new
electrolytes. Our results demonstrate good stability
and highly stable discharge capacity of the battery
based on these electrolytes.
Table 1: Physical properties of different ionic liquids
using a variety of cations combined with
TFSI
-
anion
Ionic
liquid
HOMO
value (eV)
1
Eanodic
(V)
2
Viscosity,
20
o
C (mPa.s)
N1114TFSI -0.453 5.6 168
Py14TFSI -0.467 5.2 92
Pp14TFSI -0.462 5.3 210
1
Value from DFT calculation
2
Oxidation potential determined from cyclic voltammetry
in a three-electrode cell.
2. MATERIALS AND METHODS
2.1. Preparation of ionic liquid-based electrolytes
and electrodes
Py14TFSI and NaTFSI were bought from Sigma-
Aldrich (≥ 99 %), stored in a controlled argon-filled
glovebox having a humidity content below 5 ppm to
avoid any contamination. Other chemical reagents
including EC, PC, and DMC were also purchased
from Sigma-Aldrich (≥ 98 %). Ionic liquid-based
electrolytes were obtained by mixing different
amounts (10-40 %wt.) of Py14TFSI to both the
carbonate-based solutions EC-PC (1:1), EC-DMC
(1:1), and 1M NaTFSI. These mixtures were
vigorously stirred with a magnetic paddle for at least
24 hours to form a homogeneous solution.
The anode/cathode electrodes were prepared by
doctor-blade coating on the aluminum substrate of a
slurry formed of 80%wt. active material (home-
made NMO or HC KUREHA, Japan), 5%wt. PVDF
6020 (Solvay Solef) binder and 10%wt. acetylene
black (Timcal, Swiss). The electrode films were all
dried at 80
o
C in a vacuum oven overnight then were
punched in 15 mm diameter round discs. The
electrode discs were dried under vacuum overnight
at 100
o
C and directly transferred into an Ar-filled
glove box for cell assembly.
2.2. Characterization techniques
Density functional theory (DFT) calculations of the
HOMO value (based on geometry optimization and
frequency computation) were carried out with the
Vietnam Journal of Chemistry Safe sodium-ion battery using hybrid electrolytes
© 2021 Vietnam Academy of Science and Technology, Hanoi & Wiley-VCH GmbH www.vjc.wiley-vch.de 19
GAUSSIAN 03 software package with a basic set of
B3LYP/6-311++G(2d,p)
Thermal stability of mixed electrolytes was
characterized by thermogravimetric analysis (TGA)
measurements using TGA Q500 V20.10 Build. A
few milligrams of the sample were heated from the
room temperature up to 600 °C at 10 °C.min
-1
with
nitrogen flow.
Flammability tests were performed to measure
the thermal stability of hybrid electrolytes. A fixed
weight of electrolytes was impregned into a glass
fiber filter that was exposed for 5 seconds by a
burner staying 15 cm far away. The time required to
extinguish the flame was recorded and normalized
against liquid mass to evaluate the self-extinguish
time (SET) in s.g
-1
.
[18]
The ionic conductivity of mixed electrolytes was
calculated from AC impedance spectroscopy method
using an HP 4192A impedance analyzer in the
frequency range from 5 to 13 MHz. The
conductivity test cell with platinized platinum
blocking electrodes was dipped in the electrolyte
solution and calibrated by 0.01 M KCl at 25
o
C to
determine the cell constant. The ionic conductivity
measurements were performed in the temperature
range from 10 to 60
o
C. The cell should be kept at a
constant temperature for at least 1 hour to reach
thermal equilibration.
The electrical conductivity data taken at different
temperatures were fitted using Vogel–Tamman–
Fulcher (VTF) equation to obtain activation energy
(Eq. 1). It is common for researchers to utilize the
(VTF) equation to separate the effects of charge
carrier concentration, often related to the pre-factor,
A, and segmental motion, related to the activation
energy, Ea, on overall conductivity, σ, at a given
temperature T.
[27]
(
( )
) (1)
T0 in this equation is referred to as the Vogel
temperature, equal to the glass transition in ideal
glasses,
[28]
but typically taken as 50 °C below the
glass transition temperature in several electrolytes.
Cyclic voltammetry (CV) measurements were
performed at the scan rate of 1 mV.s
-1
recorded on
MGP2 Biologic Instrument to assess the stability of
the electrolytes over oxidation and reduction.
Measurements were carried out by using a standard
three-electrode cell. The counter electrode was a Pt
wire and the working electrode was a Pt micro-
electrode with a diameter of 25 μm. The reference
electrode was a silver wire embed in a solution of
AgNO3 10 mM in acetonitrile + 0.1 M
tetrabutylammonium perchlorate (TBAP).
The coin cells for galvanostatic tests were
assembled by coupling a sodium metal foil with
NMO or HC that separated by a Celgard separator
soaked by the prepared electrolytes.
The sodium half-cells were cycled at the current
constant C/10 in the potential range 0.04-2.4 V and
2-4 V for HC and NMO, respectively, using an
MGP2 Biologic Battery Test System. The
performance of the cells was evaluated in terms of
specific capacity, charge/discharge efficiency, and
cycle life.
3. RESULTS AND DISCUSSION
3.1. Thermal and conduction properties of
electrolytes containing various amount of ionic
liquid Py14TFSI
Figure 1 shows the TGA curves of all considered
electrolytes. As indicated in Fig. 1, there was almost
no weight loss for pure Py14TFSI-based electrolyte
up to 360
o
C; confirming the excellent thermal
stability of the ionic liquid. In contrast, the
significant weight loss of the carbonate solvent-
based electrolytes, due to vigorous evaporation, was
approximately 85 % per initial content at 180
o
C for
all cases.
[29,30]
The addition of Py14TFSI into the
electrolyte shifted the solvent evaporation
temperatures to higher values. The increase in EC,
PC, DMC evaporation temperature deduced from the
variable temperature TGA experiments support the
interaction between solvents and Py14TFSI.
[24,25]
At 100
o
C, the mixtures containing 10 %, 20 %,
30 %, and 40 % of Py14TFSI displayed weight losses
of 2.6, 1.8, 1.4 and 0.9 %, respectively. A weight-
loss corresponding to 5 % was reached at
significantly higher temperatures for the mixtures
(130.2, 136.1, 138.0, 143.5
o
C for the 10, 20, 30 and
40 % IL mixture, respectively) with respect to the
EC-PC-based electrolytes, for which this weight loss
was already reached at 80
o
C.
For the EC-DMC-based samples, the first weight
loss commensurate with insoluble DMC evaporation
in the complexes, the second thermal process begins
near 150
o
C and finishes near 250
o
C proportionated
with solvents evaporation in the ternary systems and
the third degradation starts near 400
o
C and finishes
approximately 500
o
C. Thermal decomposition of
the Py14TFSI component of the mixtures appears to
shift to a higher temperature (at least for these
variable-temperature measurements).
According to Fig. 1(c), a similar result was
found for EC-PC-DMC-based electrolytes with two
steps of weight loss observed. The first process
Vietnam Journal of Chemistry Le My Loan Phung et al.
© 2021 Vietnam Academy of Science and Technology, Hanoi & Wiley-VCH GmbH www.vjc.wiley-vch.de 20
related to solvents evaporation starts at near 100
o
C
and finishes at near 200
o
C. The second process
proportionated with a decomposition of IL was in
the range of 400 – 500 oC. The separated addition of
EC or PC in pure IL does not affect much in the
complexes. The range of temperature for solvents
evaporation and IL degradation in the mixtures was
the same with the electrolyte only IL contained.
Figure 1: TGA diagrams of ionic quid Py14TFSI mixed with (a) EC-DMC 1:1, (b) EC-PC 1:1, (c) 30 %wt.
EC or PC along with 1M NaTFSI, (d) evolutions of weight loss versus temperature
Fig. 2 (a-d) shows the glass fiber mat after the flame
switched off. Table 2 reports the occurrence of
ignition (each sample was tested 6 times) and the
average value (ca. 10% error) of the self-
extinguishing time of the mixed electrolytes
containing organic solvents and Py14TFSI.
Like EMITFSI, under exposure to the burner,
Py14TFSI produced only small flare-ups that
promptly extinguished once the burner switched off,
thus it was not considered as ignition. Ignition
occurrence in table 1 indicates the flame inhibition
effect induced by the addition of IL: all 6 samples
containing 10 %wt. of IL ignited, but only 1 sample
out of 6 containing 40 %wt. did. The lower amount
of Py14TFSI needed to observe the flame-inhibition
effect was 20 wt%., whereas at 40 wt%. the
tendency to ignite was significantly reduced. In
contrast, the SET values showed an opposite trend:
the larger IL content in the sample, the higher the
Figure 2: Glass fiber mats after flammability tests of
the electrolytes: (a) IL pure, (b-d) 20 %wt. PY14TFSI
+ 1M NaTFSI amalgamated in solvent solutions
EC-PC, EC-DMC, EC-PC-DMC, respectively. (e)
IL during exposure to flame EC-DMC (1:1) + 10
%wt. IL +1M NaTFSI
Vietnam Journal of Chemistry Safe sodium-ion battery using hybrid electrolytes
© 2021 Vietnam Academy of Science and Technology, Hanoi & Wiley-VCH GmbH www.vjc.wiley-vch.de 21
time needs for the flame to extinguish (normalized
against liquid mass). The samples with 10 %
Py14TFSI ignited with a SET value of 74.7 s.g
-1
and
67.3 s.g
-1
) for the electrolytes mixed with EC-PC
and EC-DMC, respectively, which were higher than
that (50.7 s.g
-1
of pure EC-PC and 63.6 s.g
-1
of pure
EC-DMC).
The results can be assumed that ignited solvent
vapors triggered the combustion of IL. The
oxidizing flame completely burned the solvent
vapors without leaving a layer of carbon as the
reducing yellow flame of a lighter does. By contrast,
the samples soaked with the solutions containing
Py14TFSI in different percentages displayed
carbonaceous deposit due to slow, oxygen-poor
combustion of the IL triggered by the organic
electrolyte: the more IL in the mixture, the more
carbon was formed.
Table 2: The mean values of the Self-Extinguishing Time (SET) of several mixtures of IL and binary-solvent
systems with 1M NaTFSI in all samples
Electrolytes
Ignition
occurrence
SET
(s.g
-1
)
Electrolytes
Ignition
occurrence
SET
(s.g
-1
)
EC-PC 6/6 50.7 EC-DMC 6/6 63.6
EC-PC + 10 %wt. IL 6/6 74.7 EC-DMC + 10 %wt. IL 6/6 67.3
EC-PC + 20 %wt. IL 6/6 87.7 EC-DMC + 20 %wt. IL 5/6 80.9
EC-PC + 30 %wt. IL 4/6 104.9 EC-DMC + 30 %wt. IL 4/6 103.3
EC-PC + 40 %wt. IL 3/6 113.7 EC-DMC + 40 %wt. IL 3/6 116.0
IL + 30 %wt. EC 2/6 61.2 EC-PC-DMC + 20 %wt.IL 6/6 71.9
IL + 30 %wt. PC 2/6 94.0 Py14TFSI pure 0/6 -
The hybrid electrolytes based on binary systems
EC-DMC or EC-PC with Py14TFSI are less volatile
than the pure conventional electrolyte, an effect that
was more evident the more IL was added.
Nevertheless, the mixtures containing Py14TFSI
easily ignite because the presence of the organic
solvent continued to burn with SET values
proportional to the amount of IL, which acted as a
retardant rather than a flame-inhibitor. The fact that
the mixtures with high amounts of ionic liquids are
more difficult to ignite and burn for a longer time
once they are ignited is worth noting especially for
the overall estimation of the safety behavior of IL-
based mixed electrolytes.
Ionic conductivity and density of ILs based
electrolyte was also evaluated at room temperature
(table 3). Py14TFSI has the lowest conductivity
compared to the carbonated-based electrolyte due to
its high viscosity. The increase of Py14TFSI addition
in conventional electrolytes lowered their ionic
conductivity because of the viscosity increase. Thus,
the two aspects (viscosity and conductivity) should
be comprised to obtain the favorable performance of
the ILs-based electrolytes.
Table 3: Density and ionic conductivity of complex electrolytes based on Py14TFSI at 30 °C
Electrolytes Conductivity (mS.cm
-1
) Density (g.cm
-3
)
Py14TFSI + 1M NaTFSI 5.6 1.412
EC-PC (1:1 in vol%) + 1M NaTFSI 13.2 -
EC-PC + 10 %wt. IL + 1M NaTFSI 10.8 1.249
EC-PC + 20 %wt. IL + 1M NaTFSI 10.3 1.270
EC-PC + 30 %wt. IL + 1M NaTFSI